# Patent

## Title
Polyurethanes, articles and coatings prepared therefrom and methods of making the same

## Abstract

The present invention provides polyurethanes including a reaction product of components including: (a) at least one isocyanate functional prepolymer including a reaction product of: (1) about 1 equivalent of at least one polyisocyanate; and (2) about 0.01 to about 0.5 equivalent of at least one polycarbonate polyol; and (b) about 0.01 to about 1 equivalent of at least one branched polyol having at least 3 hydroxyl groups; compositions, coatings and articles made therefrom and methods of making the same.

## Background
CROSS-REFERENCE TO RELATED APPLICATIONS
This application claims the benefit of priority from U.S. Provisional Patent Application No. 61/783,197, filed on Mar. 14, 2013. Also, this application is a continuation-in-part application of U.S. patent application Ser. No. 13/712,110, filed on Dec. 12, 2012, which is a continuation of U.S. patent application Ser. No. 12/410,102, filed on Mar. 24, 2009, which is a continuation-in-part application of U.S. patent application Ser. No. 11/639,058, filed on Dec. 14, 2006, which is a continuation-in-part application of U.S. patent application Ser. No. 10/932,641, filed on Sep. 1, 2004, and application Ser. Nos. 11/303,670, 11/303,422, 11/303,892, and 11/303,671, each of which was filed on Dec. 16, 2005. Each of the above applications is incorporated by reference herein.


BACKGROUND OF THE INVENTION
I. Field of the Invention
The present invention relates to polyurethanes and poly(ureaurethanes) prepared from polyols and polyisocyanates, articles, castings, laminates and coatings prepared therefrom, and methods of making the same.
II. Technical Considerations
A number of organic polymeric materials, for example plastics such as polycarbonates and acrylics, have been developed as alternatives and replacements for glass in applications such as optical lenses, fiber optics, windows and automotive, nautical and aviation transparencies. For example, in aircraft glazings both polycarbonates, such as LEXAN®, and acrylics have enjoyed widespread acceptance. These polymeric materials can provide advantages relative to glass, including shatter or penetration resistance, lighter weight for a given application, flexibility, ease of molding and dyeability. Unfortunately, there are some serious disadvantages associated with both polycarbonates and acrylics. Polycarbonates scratch easily, and, if directly exposed to sunlight and harsh environments, soon become difficult to view through. Acrylics, although not as scratchable as polycarbonates, do not have the physical properties of the polycarbonates such as heat distortion temperature and impact resistance. Some “high impact” strength polycarbonates, can have inconsistent impact strength that can degrade over time, poor crack propagation resistance (K-factor), poor optical quality, poor solvent resistance and poor weatherability. Even though polycarbonates can exhibit good impact strength when impacted at low speeds, at high impact speeds of greater than about 1100 ft/sec (335.3 m/sec), such as those exhibited in ballistics applications, a 9 mm bullet (125 grain) fired from about 20 feet (6.1 m) at a speed of about 1350 ft/sec (411 msec) can pass easily through a 1 inch (2.5 cm) thick polycarbonate plastic.
Also, polycarbonates are typically extruded, which can produce optical distortions in the extrudate in the direction of extrusion. For optical applications such as fighter plane canopies, polycarbonates typically must undergo an additional processing step to remove the distortions, which can increase cost. Also, some polycarbonates are birefringent which can also cause optical distortions. The Abbe number of LEXAN is 34. Higher Abbe values indicate better visual acuity and less chromatic aberrations.
Thus, there is a need in the art to develop polymers useful for producing articles having good optical quality, high impact resistance, high impact strength, high K factor, good ballistics resistance, good solvent resistance and good weatherability. The ability to fabricate articles by casting or reaction injection molding rather than extrusion also is desirable.
SUMMARY OF THE INVENTION
In some non-limiting embodiments, the present invention provides a polyurethane comprising a reaction product of components comprising: (a) at least one isocyanate functional prepolymer comprising a reaction product of: (1) about 1 equivalent of at least one polyisocyanate; and (2) about 0.01 to about 0.5 equivalent of at least one polycarbonate polyol based upon the about 1 equivalent of the at least one polyisocyanate; and (b) about 0.01 to about 1 equivalent of at least one polyol having at least 3 hydroxyl groups based upon the about 1 equivalent of the at least one polyisocyanate.
In other non-limiting embodiments, the present invention provides a polyurethane comprising a reaction product of components comprising: (a) about 1 equivalent of at least one polyisocyanate; and (b) about 0.01 to about 0.5 equivalent of at least one polycarbonate polyol based upon the about 1 equivalent of the at least one polyisocyanate; and (c) about 0.01 to about 1 equivalent of at least one polyol having at least 3 hydroxyl groups based upon the about 1 equivalent of the at least one polyisocyanate.
In other non-limiting embodiments, the present invention provides a process for preparing a polyurethane article comprising: (a) heating a mixture of about 1 equivalent of at least one polyisocyanate and about 0.01 to about 0.5 equivalent of at least one polycarbonate polyol based upon the about 1 equivalent of the at least one polyisocyanate, to a temperature of about 110° C. to about 130° C. for at least about an hour to form a reaction product; (b) mixing the reaction product (a) with about 0.01 to about 1 equivalent of at least one polyol having at least 3 hydroxyl groups based upon the about 1 equivalent of the at least one polyisocyanate until the mixture reaches a temperature of at least about 110° C. to about 130° C., optionally by heating if necessary; (c) casting the reaction product into a mold preheated to a temperature of at least about 100° C. to about 130° C.; and (d) curing the reaction product at a first predetermined temperature of about 100° C. to about 120° C. for at least about 0.5 hours; and then at a second predetermined temperature of about 140° C. to about 180° C. for about 15 to about 30 hours.
Cured compositions, articles, laminates and methods of making and using the same comprising the above polyurethanes and poly(ureaurethane)s are also provided by the present invention.



BRIEF DESCRIPTION OF THE DRAWINGS
The foregoing summary, as well as the following detailed description, will be better understood when read in conjunction with the appended drawings. In the drawings:
FIG. 1 is a photograph of a front elevational view of a test sample of Formulation 93, Example A is a photograph of a front elevational view of a test sample of 9 mm bullets shot from 20 feet (6.1 m) at a velocity of 1350 ft/sec (411.5 m/sec);
FIG. 2 is a photograph of a perspective view of a test sample of Formulation 94, Example A after shooting of the sample with a 9 mm bullet shot from 20 feet (6.1 m) at an initial velocity of 1350 ft/sec (411.5 m/sec);
FIG. 3 is a side elevational view of the sample shown in FIG. 2;
FIG. 4 is front elevational view of a portion of a composite according to the present invention after shooting of the sample with four 7.62×39 mm bullets having a steel core shot from an AK-47 rifle from a distance of 30 yards (27.4 m) at an initial velocity of 2700 ft/sec (823 m/sec); and
FIG. 5 is a rear perspective view of the sample of FIG. 4.



DETAILED DESCRIPTION
As used herein, spatial or directional terms, such as “inner”, “left”, “right”, “up”, “down”, “horizontal”, “vertical” and the like, relate to the invention as it is described herein. However, it is to be understood that the invention can assume various alternative orientations and, accordingly, such terms are not to be considered as limiting. For the purposes of this specification, unless otherwise indicated, all numbers expressing quantities of ingredients, reaction conditions, dimensions, physical characteristics, and so forth used in the specification and claims are to be understood as being modified in all instances by the term “about.” Accordingly, unless indicated to the contrary, the numerical parameters set forth in the following specification and attached claims are approximations that may vary depending upon the desired properties sought to be obtained by the present invention. At the very least, and not as an attempt to limit the application of the doctrine of equivalents to the scope of the claims, each numerical parameter should at least be construed in light of the number of reported significant digits and by applying ordinary rounding techniques.
Notwithstanding that the numerical ranges and parameters setting forth the broad scope of the invention are approximations, the numerical values set forth in the specific examples are reported as precisely as possible. Any numerical value, however, inherently contain certain errors necessarily resulting from the standard deviation found in their respective testing measurements.
Also, it should be understood that any numerical range recited herein is intended to include all sub-ranges subsumed therein. For example, a range of “1 to 10” is intended to include any and all sub-ranges between and including the recited minimum value of 1 and the recited maximum value of 10, that is, all subranges beginning with a minimum value equal to or greater than 1 and ending with a maximum value equal to or less than 10, and all subranges in between, e.g., 1 to 6.3, or 5.5 to 10, or 2.7 to 6.1.
“Alkyl” means an aliphatic hydrocarbon group which may be straight or branched and comprising about 1 to about 20 carbon atoms in the chain. Non-limiting examples of suitable alkyl groups contain about 1 to about 18 carbon atoms in the chain, or about 1 to about 6 carbon atoms in the chain. Branched means that one or more lower alkyl groups such as methyl, ethyl or propyl, are attached to a linear alkyl chain. “Lower alkyl” or “short chain alkyl” means a group having about 1 to about 6 carbon atoms in the chain which may be straight or branched. “Alkyl” may be unsubstituted or optionally substituted by one or more substituents which may be the same or different, each substituent being independently selected from the group consisting of halo, alkyl, aryl, cycloalkyl, cyano, hydroxy, alkoxy, alkylthio, amino, —NH(alkyl), —NH(cycloalkyl), —N(alkyl)2, carboxy and —C(O)O-alkyl. Non-limiting examples of suitable alkyl groups include methyl, ethyl, n-propyl, isopropyl and t-butyl.
“Alkylene” means a difunctional group obtained by removal of a hydrogen atom from an alkyl group that is defined above. Non-limiting examples of alkylene include methylene, ethylene and propylene.
“Aryl” means an aromatic monocyclic or multicyclic ring system comprising about 6 to about 14 carbon atoms, or about 6 to about 10 carbon atoms. The aryl group can be optionally substituted with one or more “ring system substituents” which may be the same or different, and are as defined herein. Non-limiting examples of suitable aryl groups include phenyl and naphthyl.
“Heteroaryl” means an aromatic monocyclic or multicyclic ring system comprising about 5 to about 14 ring atoms, or about 5 to about 10 ring atoms, in which one or more of the ring atoms is an element other than carbon, for example nitrogen, oxygen or sulfur, alone or in combination. In some non-limiting embodiments, the heteroaryls contain about 5 to about 6 ring atoms. The “heteroaryl” can be optionally substituted by one or more “ring system substituents” which may be the same or different, and are as defined herein. The prefix aza, oxa or thia before the heteroaryl root name means that at least one of a nitrogen, oxygen or sulfur atom respectively, is present as a ring atom. A nitrogen atom of a heteroaryl can be optionally oxidized to the corresponding N-oxide. Non-limiting examples of suitable heteroaryls include pyridyl, pyrazinyl, furanyl, thienyl, pyrimidinyl, pyridone (including N-substituted pyridones), isoxazolyl, isothiazolyl, oxazolyl, thiazolyl, pyrazolyl, furazanyl, pyrrolyl, pyrazolyl, triazolyl, 1,2,4-thiadiazolyl, pyrazinyl, pyridazinyl, quinoxalinyl, phthalazinyl, oxindolyl, imidazo[1,2-a]pyridinyl, imidazo[2,1-b]thiazolyl, benzofurazanyl, indolyl, azaindolyl, benzimidazolyl, benzothienyl, quinolinyl, imidazolyl, thienopyridyl, quinazolinyl, thienopyrimidyl, pyrrolopyridyl, imidazopyridyl, isoquinolinyl, benzoazaindolyl, 1,2,4-triazinyl, benzothiazolyl and the like. The term “heteroaryl” also refers to partially saturated heteroaryl moieties such as, for example, tetrahydroisoquinolyl, tetrahydroquinolyl and the like.
“Aralkyl” or “arylalkyl” means an aryl-alkyl-group in which the aryl and alkyl are as previously described. In some non-limiting embodiments, the aralkyls comprise a lower alkyl group. Non-limiting examples of suitable aralkyl groups include benzyl, 2-phenethyl and naphthalenylmethyl. The bond to the parent moiety is through the alkyl.
“Alkylaryl” means an alkyl-aryl-group in which the alkyl and aryl are as previously described. In some non-limiting embodiments, the alkylaryls comprise a lower alkyl group. A non-limiting example of a suitable alkylaryl group is tolyl. The bond to the parent moiety is through the aryl.
“Cycloalkyl” means a non-aromatic mono- or multicyclic ring system comprising about 3 to about 10 carbon atoms, or about 5 to about 10 carbon atoms. In some non-limiting embodiments, the cycloalkyl ring contains about 5 to about 7 ring atoms. The cycloalkyl can be optionally substituted with one or more “ring system substituents” which may be the same or different, and are as defined above. Non-limiting examples of suitable monocyclic cycloalkyls include cyclopropyl, cyclopentyl, cyclohexyl, cycloheptyl and the like. Non-limiting examples of suitable multicyclic cycloalkyls include 1-decalinyl, norbornyl, adamantyl and the like.
“Halogen” or “halo” means fluorine, chlorine, bromine, or iodine. In some non-limiting embodiments, the halogen groups are fluorine, chlorine or bromine.
“Ring system substituent” means a substituent attached to an aromatic or non-aromatic ring system which, for example, replaces an available hydrogen on the ring system. Ring system substituents may be the same or different, each being independently selected from the group consisting of alkyl, alkenyl, alkynyl, aryl, heteroaryl, aralkyl, alkylaryl, heteroaralkyl, heteroarylalkenyl, heteroarylalkynyl, alkylheteroaryl, hydroxy, hydroxyalkyl, alkoxy, aryloxy, aralkoxy, acyl, aroyl, halo, nitro, cyano, carboxy, alkoxycarbonyl, aryloxycarbonyl, aralkoxycarbonyl, alkylsulfonyl, arylsulfonyl, heteroarylsulfonyl, alkylthio, arylthio, heteroarylthio, aralkylthio, heteroaralkylthio, cycloalkyl, heterocyclyl, —C(═N—CN)—NH2, —C(═NH)—NH2, —C(═NH)—NH(alkyl), Y1Y2N—, Y1Y2N-alkyl-, Y1Y2NC(O)—, Y1Y2NSO2— and —SO2NY1Y2, wherein Y1 and Y2 can be the same or different and are independently selected from the group consisting of hydrogen, alkyl, aryl, cycloalkyl, and aralkyl. “Ring system substituent” may also mean a single moiety which simultaneously replaces two available hydrogens on two adjacent carbon atoms (one H on each carbon) on a ring system. Examples of such moieties are methylene dioxy, ethylenedioxy, —C(CH3)2— and the like which form moieties such as, for example:




“Heterocyclyl” means a non-aromatic saturated monocyclic or multicyclic ring system comprising about 3 to about 10 ring atoms, or about 5 to about 10 ring atoms, in which one or more of the atoms in the ring system is an element other than carbon, for example nitrogen, oxygen or sulfur, alone or in combination. There are no adjacent oxygen and/or sulfur atoms present in the ring system. In some non-limiting embodiments, the heterocyclyl contains about 5 to about 6 ring atoms. The prefix aza, oxa or thia before the heterocyclyl root name means that at least a nitrogen, oxygen or sulfur atom respectively is present as a ring atom. Any —NH in a heterocyclyl ring may exist protected such as, for example, as an —N(Boc), —N(CBz), —N(Tos) group and the like; such protections are also considered part of this invention. The heterocyclyl can be optionally substituted by one or more “ring system substituents” which may be the same or different, and are as defined herein. The nitrogen or sulfur atom of the heterocyclyl can be optionally oxidized to the corresponding N-oxide, S-oxide or S,S-dioxide. Non-limiting examples of suitable monocyclic heterocyclyl rings include piperidyl, pyrrolidinyl, piperazinyl, morpholinyl, thiomorpholinyl, thiazolidinyl, 1,4-dioxanyl, tetrahydrofuranyl, tetrahydrothiophenyl, lactam, lactone, and the like.
It should be noted that in hetero-atom containing ring systems of this invention, there are no hydroxyl groups on carbon atoms adjacent to a N, O or S, as well as there are no N or S groups on carbon adjacent to another heteroatom. Thus, for example, in the ring:




there is no —OH attached directly to carbons marked 2 and 5.

It should also be noted that tautomeric forms such as, for example, the moieties:




are considered equivalent in certain embodiments of this invention.

“Heteroaralkyl” means a heteroaryl-alkyl-group in which the heteroaryl and alkyl are as previously described. In some non-limiting embodiments, the heteroaralkyl contains a lower alkyl group. Non-limiting examples of suitable heteroaralkyl groups include pyridylmethyl, and quinolin-3-ylmethyl. The bond to the parent moiety is through the alkyl.
“Hydroxyalkyl” means a HO-alkyl-group in which alkyl is as previously defined. In some non-limiting embodiments, the hydroxyalkyl contains a lower alkyl group. Non-limiting examples of suitable hydroxyalkyl groups include hydroxymethyl and 2-hydroxyethyl.
“Alkoxy” means an alkyl-O— group in which the alkyl group is as previously described. Non-limiting examples of suitable alkoxy groups include methoxy, ethoxy, n-propoxy, isopropoxy and n-butoxy. The bond to the parent moiety is through the ether oxygen.
“Aryloxy” means an aryl-O— group in which the aryl group is as previously described. Non-limiting examples of suitable aryloxy groups include phenoxy and naphthoxy. The bond to the parent moiety is through the ether oxygen.
“Alkylthio” means an alkyl-S— group in which the alkyl group is as previously described. Non-limiting examples of suitable alkylthio groups include methylthio and ethylthio. The bond to the parent moiety is through the sulfur.
“Arylthio” means an aryl-S— group in which the aryl group is as previously described. Non-limiting examples of suitable arylthio groups include phenylthio and naphthylthio. The bond to the parent moiety is through the sulfur.
“Aralkylthio” means an aralkyl-S— group in which the aralkyl group is as previously described. A non-limiting example of a suitable aralkylthio group is benzylthio. The bond to the parent moiety is through the sulfur.
“Alkoxycarbonyl” means an alkyl-O—CO— group. Non-limiting examples of suitable alkoxycarbonyl groups include methoxycarbonyl and ethoxycarbonyl. The bond to the parent moiety is through the carbonyl.
“Aryloxycarbonyl” means an aryl-O—C(O)— group. Non-limiting examples of suitable aryloxycarbonyl groups include phenoxycarbonyl and naphthoxycarbonyl. The bond to the parent moiety is through the carbonyl.
“Aralkoxycarbonyl” means an aralkyl-O—C(O)— group. A non-limiting example of a suitable aralkoxycarbonyl group is benzyloxycarbonyl. The bond to the parent moiety is through the carbonyl.
“Alkylsulfonyl” means an alkyl-S(O2)— group. In some non-limiting embodiments, the alkylsulfonyl group includes a lower alkyl group. The bond to the parent moiety is through the sulfonyl.
“Arylsulfonyl” means an aryl-S(O2)— group. The bond to the parent moiety is through the sulfonyl.
The term “substituted” means that one or more hydrogens on the designated atom is replaced with a selection from the indicated group, provided that the designated atom's normal valency under the existing circumstances is not exceeded, and that the substitution results in a stable compound. Combinations of substituents and/or variables are permissible only if such combinations result in stable compounds.
The term “optionally substituted” means optional substitution with the specified groups, radicals or moieties.
It should also be noted that any carbon as well as heteroatom with unsatisfied valences in the text, schemes, examples and Tables herein is assumed to have the sufficient number of hydrogen atom(s) to satisfy the valences.
When a functional group in a compound is termed “protected”, this means that the group is in modified form to preclude undesired side reactions at the protected site when the compound is subjected to a reaction. Suitable protecting groups will be recognized by those with ordinary skill in the art as well as by reference to standard textbooks such as, for example, T. W. Greene et al., Protective Groups in Organic Synthesis (1991), Wiley, New York.
When any variable (e.g., aryl, heterocycle, R2, etc.) occurs more than one time in any constituent, its definition on each occurrence is independent of its definition at every other occurrence.
As used herein, the term “composition” is intended to encompass a product comprising the specified ingredients in the specified amounts, as well as any product which results, directly or indirectly, from combination of the specified ingredients in the specified amounts.
As used herein, “formed from” or “prepared from” denotes open, e.g., “comprising,” claim language. As such, it is intended that a composition “formed from” or “prepared from” a list of recited components be a composition comprising at least these recited components or the reaction product of at least these recited components, and can further comprise other, non-recited components, during the composition's formation or preparation. As used herein, the phrase “reaction product of” means chemical reaction product(s) of the recited components, and can include partial reaction products as well as fully reacted products.
As used herein, the term “polymer” means a substance, typically of large molecular mass, comprising structural units or monomers. Examples of polymers include oligomers, homopolymers and copolymers. The term “oligomer” means a polymer consisting of only a few monomer units up to about ten monomer units, for example a dimer, trimer or tetramer.
The term “prepolymer” means a compound, monomer or oligomer used to prepare a polymer, and includes without limitation both homopolymer and copolymer oligomers.
The phrase “thermoplastic polymer” means a polymer that undergoes liquid flow upon heating and can be soluble in solvents.
The phrase “thermoset polymer” means a polymer that solidifies or “sets” irreversibly upon curing or crosslinking. Once cured, a crosslinked thermoset polymer will not melt upon the application of heat and is generally insoluble in solvents.
As used herein, the term “cure” or “cured” as used in connection with a composition, e.g., “composition when cured” or a “cured composition”, shall mean that any curable or crosslinkable components of the composition are at least partially cured or crosslinked. In some non-limiting embodiments of the present invention, the crosslink density of the crosslinkable components, i.e., the degree of crosslinking, ranges from about 1% to about 100% of complete crosslinking. In other non-limiting embodiments, the crosslink density ranges from about 35% to about 85% of full crosslinking. In other non-limiting embodiments, the crosslink density ranges from about 50% to about 85% of full crosslinking. One skilled in the art will understand that the presence and degree of crosslinking, i.e., the crosslink density, can be determined by a variety of methods, such as dynamic mechanical thermal analysis (DMA) using a TA Instruments DMA 2980 DMA analyzer over a temperature range of −148° F. (−100° C.) to 350° F. (177° C.) conducted under nitrogen according to ASTM D 4065-01. This method determines the glass transition temperature and crosslink density of free films of coatings or polymers. These physical properties of a cured material are related to the structure of the crosslinked network. In an embodiment of the present invention, the sufficiency of cure is evaluated relative to the solvent resistance of a cured film of the polymer. For example, solvent resistance can be measured by determining the number of double acetone rubs. For purposes of the present invention, a coating is deemed to be “cured” when the film can withstand a minimum of 100 double acetone rubs without substantial softening of the film and no removal of the film.
Curing of a polymerizable composition can be obtained by subjecting the composition to curing conditions, such as but not limited to thermal curing, irradiation, etc., leading to the reaction of reactive groups of the composition and resulting in polymerization and formation of a solid polymerizate. When a polymerizable composition is subjected to curing conditions, following polymerization and after reaction of most of the reactive groups occurs, the rate of reaction of the remaining unreacted reactive groups becomes progressively slower. In some non-limiting embodiments, the polymerizable composition can be subjected to curing conditions until it is at least partially cured. The term “at least partially cured” means subjecting the polymerizable composition to curing conditions, wherein reaction of at least a portion of the reactive groups of the composition occurs, to form a solid polymerizate. The at least partially cured polymerizate can be demolded and, for example, used to prepare articles such as windows, cut into test pieces or subjected to machining operations, such as optical lens processing. In some non-limiting embodiments, the polymerizable composition can be subjected to curing conditions such that a substantially complete cure is attained and wherein further exposure to curing conditions results in no significant further improvement in polymer properties, such as strength or hardness.
The term “polyurethane” is intended to include not only polyurethanes that are formed from the reaction of polyisocyanates and polyols but also poly(ureaurethane)(s) that are prepared from the reaction of polyisocyanates with polyols and water and/or amines.
Generally, the polyurethanes and poly(ureaurethane)s of the present invention comprise a reaction product of components comprising at least one polyisocyanate and at least one polyol.
In some non-limiting embodiments, the polyurethane comprises a reaction product of components comprising, consisting essentially of, or consisting of: (a) at least one isocyanate functional prepolymer comprising a reaction product of (1) about 1 equivalent of at least one polyisocyanate; and (2) about 0.01 to about 0.5 equivalent of at least one polycarbonate polyol based upon the about 1 equivalent of the at least one polyisocyanate; and (b) about 0.01 to about 1 equivalent of at least one polyol having at least 3 hydroxyl groups based upon the about 1 equivalent of the at least one polyisocyanate.
In some non-limiting embodiments, the polyurethane comprises a reaction product of components comprising, consisting essentially of, or consisting of: (a) about 1 equivalent of at least one polyisocyanate; and (b) about 0.01 to about 0.5 equivalent of at least one polycarbonate polyol based upon the about 1 equivalent of the at least one polyisocyanate; and (c) about 0.01 to about 1 equivalent of at least one polyol having at least 3 hydroxyl groups based upon the about 1 equivalent of the at least one polyisocyanate.
In some non-limiting embodiments, the present invention provides a polyurethane comprising a reaction product of components comprising, consisting essentially of, or consisting of: (a) an isocyanate functional urethane prepolymer comprising a reaction product of components comprising: (i) about 1 equivalent of at least one polyisocyanate; and (ii) about 0.1 to about 0.4 equivalents of polycarbonate diol based upon the about 1 equivalent of at least one polyisocyanate; (b) about 0.5 to about 0.8 equivalents of trimethylolpropane based upon the about 1 equivalent of at least one polyisocyanate; and (c) about 0.1 to about 0.5 equivalents of butanediol or cyclohexane dimethanol based upon the about 1 equivalent of at least one polyisocyanate.
In some non-limiting embodiments, the present invention provides a polyurethane comprising a reaction product of components comprising, consisting essentially of, or consisting of: (a) an isocyanate functional urethane prepolymer comprising a reaction product of components comprising: (i) about 1 equivalent of at least one polyisocyanate; and (ii) about 0.2 equivalent of polycarbonate diol based upon the about 1 equivalent of at least one polyisocyanate; (b) about 0.7 equivalent of trimethylolpropane based upon the about 1 equivalent of at least one polyisocyanate; and (c) about 0.1 equivalent of butanediol or cyclohexane dimethanol based upon the about 1 equivalent of at least one polyisocyanate.
In some non-limiting embodiments of the present invention, at least one of the polyisocyanates and/or at least one of the polyols is branched. As used herein, “branched” means a chain of atoms with one or more side chains attached to it. Branching occurs by the replacement of a substituent, e.g, a hydrogen atom, with a covalently bonded substituent or moiety, e.g, an alkyl group. While not intending to be bound by any theory, it is believed that branching of the polyisocyanate and/or polyol can increase the free volume within the polymer matrix, thereby providing room for the molecules to move. The molecules can orient and rotate into configurations and alignments having favorable energy states which can provide good impact properties and/or high modulus of elasticity for the cured polymer matrix. As shown in FIGS. 1, 2 and 3, Dynamic Mechanical Analysis (DMA) of polyurethane castings prepared according to Examples 1, 2 and 40, respectively, for loss modulus as a function of temperature show a low temperature transition at about −70° C. DMA analysis was conducted over a temperature range of −148° F. (−100° C.) to 350° F. (177° C.) under nitrogen according to ASTM D 4065-01. While not intending to be bound by any theory, it is believed that this low temperature transition is due to molecular torsional mobility at that temperature and is believed to contribute to the high impact strength of these polymers.
When a viscoelastic material is subjected to an oscillatory vibration, some energy is stored in the polymer, which is proportional to the elastic component of the modulus G′, or storage modulus, and some of the energy is converted to heat through internal friction, or viscous dissipation of the energy, which is termed the loss modulus G′′. The maximum in the loss modulus is termed tan Delta, which is the maximum in internal friction, damping, or viscous energy dissipation.
High light transmittance, glassy polymers rarely exhibit high impact strength. Polycarbonate plastics such as LEXAN can exhibit a similar low temperature transition, but can have lower impact strength and lower Young's Modulus.
The physical properties of the polyurethanes and poly(ureaurethane)s of the present invention are derived from their molecular structure and are determined by the selection of building blocks, e.g., the selection of the reactants, the ratio of the hard crystalline and soft amorphous segments, and the supra-molecular structures caused by atomic interactions between chains.
Hard segments, i.e., the crystalline or semi-crystalline region of the urethane polymer, result from the reaction of the isocyanate and a chain extender, such as an aliphatic polyol having 4 to 18 carbon atoms or a low molecular weight polyol having a molecular weight of less than about 200 discussed herein. Generally, the soft segment, i.e., the amorphous, rubbery region of the urethane polymer, results from the reaction of the isocyanate and a polymer backbone component, for example a polyester polyol (such as a polycarbonate polyol) or a polyether polyol or short chain diols that have not formed crystalline regions.
The qualitative contribution of a particular organic polyol to either the hard or soft segment when mixed and reacted with other polyurethane-forming components can be readily determined by measuring the Fischer microhardness of the resulting cured polyurethane according to ISO 14577-1:2002.
In some non-limiting embodiments, the hard segment content of the polyurethane ranges from about 10 to about 100 weight percent, or about 50 to about 100 weight percent, or about 70 to about 100 weight percent. The hard segment content is the percentage by weight of the hard segment linkages present in the polymer and can be calculated by determining the total number of equivalents, and from this the total weight of all reactants, and dividing the total weight of the hard segment linkages obtainable from these reactants by the total weight of the reactants themselves. The following example will further explain the calculation. For a polyurethane prepared by reacting 0.7 equivalents of 1,4-butanediol, 0.3 equivalents of trimethylolpropane and one equivalent of 4,4′-methylene-bis-(cyclohexyl isocyanate) (DESMODUR W), the equivalent weight of the 1,4-butanediol is 45 g/eq., the equivalent weight of the trimethylolpropane is 44.7 g/eq. (corrected for impurities) and the equivalent weight of the DESMODUR W is 131.2 g/eq. Therefore, the actual weight of ingredients used is 31.54 parts by weight of 1,4-butanediol, 13.2 parts by weight of trimethylolpropane and 131.2 parts by weight of DESMODUR W or a total reactant weight of 175 parts by weight. One equivalent of 1,4-butanediol will yield one equivalent of hard segment linkage, where the hard segment linkage is 1,4-butanediol/DESMODUR W dimer. The equivalent weight of a 1,4-butanediol/DESMODUR W dimer linkage is 176 g/eq. so that the total weight of the hard segment linkages determined by multiplying the equivalent weight of the hard segment dimer by the number of equivalents of 1,4-butanediol would be 123.2 g/eq. Thus, the total weight of the 1,4-butanediol/DESMODUR W dimer linkage, 123.2, divided by the total weight of the reactants, 175.7, multiplied by 100 to convert to percentages would give a percentage by weight of hard segment linkage of 70 percent by weight.
Both Plexiglas and stretched acrylic absorb quite a bit of water from the atmosphere. In accelerated tests such as QUV-B or soaking in water at room temperature, surprisingly, polyurethanes according to the present invention including short chain diols such as butanediol and pentanediol, absorbed essentially no water in water vapor transmission rate studies and after soaking in water for about 24 hours. While not intending to be bound by any theory, it is believed that even though these plastics are very polar, the hydrogen bonding in the hard segment domains is strong enough to block water vapor transmission and uptake of water. In comparison, stretched acrylic will absorb enough water to cause severe swelling of the plastic, to the point that it cracks in-plane, like layers of onion skin separating until it falls apart. The low water absorption can also mitigate any hydrolysis degradation of the urethane groups in the polymer.
As used herein, the term “equivalent” means the mass in grams of a substance which will react with one mole (6.022×1023) of another substance. As used herein, “equivalent weight” is effectively equal to the amount of a substance in moles, divided by the valence or number of functional reactive groups of the substance.
As used herein, the term “isocyanate” includes compounds, monomers, oligomers and polymers comprising at least one or at least two —N═C═O functional groups and/or at least one or at least two —N═C═S (isothiocyanate) groups. Monofunctional isocyanates can be used as chain terminators or to provide terminal groups during polymerization. As used herein, “polyisocyanate” means an isocyanate comprising at least two —N═C═O functional groups and/or at least two —N═C═S (isothiocyanate) groups, such as diisocyanates or triisocyanates, as well as dimers and trimers or biurets of the isocyanates discussed herein. Suitable isocyanates are capable of forming a covalent bond with a reactive group such as hydroxyl, thiol or amine functional group. Isocyanates useful in the present invention can be branched or unbranched. As discussed above, use of branched isocyanates may be desirable to increase the free volume within the polymer matrix to provide space for the molecules to move.
Isocyanates useful in the present invention include “modified”, “unmodified” and mixtures of “modified” and “unmodified” isocyanates. The isocyanates can have “free”, “blocked” or partially blocked isocyanate groups. The term “modified” means that the aforementioned isocyanates are changed in a known manner to introduce biuret, urea, carbodiimide, urethane or isocyanurate groups or blocking groups. In some non-limiting embodiments, the “modified” isocyanate is obtained by cycloaddition processes to yield dimers and trimers of the isocyanate, i.e., polyisocyanates. Free isocyanate groups are extremely reactive. In order to control the reactivity of isocyanate group-containing components, the NCO groups may be blocked with certain selected organic compounds that render the isocyanate group inert to reactive hydrogen compounds at room temperature. When heated to elevated temperatures, e.g., ranging from about 90° C. to about 200° C., the blocked isocyanates release the blocking agent and react in the same way as the original unblocked or free isocyanate.
Generally, compounds used to block isocyanates are organic compounds that have active hydrogen atoms, e.g., volatile alcohols, epsilon-caprolactam or ketoxime compounds. Non-limiting examples of suitable blocking compounds include phenol, cresol, nonylphenol, epsilon-caprolactam and methyl ethyl ketoxime.
As used herein, the NCO in the NCO:OH ratio represents the free isocyanate of free isocyanate-containing materials, and of blocked or partially blocked isocyanate-containing materials after the release of the blocking agent. In some cases, it is not possible to remove all of the blocking agent. In those situations, more of the blocked isocyanate-containing material would be used to attain the desired level of free NCO.
The molecular weight of the isocyanate and isothiocyanate can vary widely. In alternate non-limiting embodiments, the number average molecular weight (Mn) of each can be at least about 100 grams/mole, or at least about 150 grams/mole, or less than about 15,000 grams/mole, or less than about 5,000 grams/mole. The number average molecular weight can be determined using known methods, such as by gel permeation chromatography (GPC) using polystyrene standards.
Non-limiting examples of suitable isocyanates include aliphatic, cycloaliphatic, aromatic and heterocyclic isocyanates, dimers and trimers thereof and mixtures thereof. Useful cycloaliphatic isocyanates include those in which one or more of the isocyanato groups are attached directly to the cycloaliphatic ring and cycloaliphatic isocyanates in which one or more of the isocyanato groups are not attached directly to the cycloaliphatic ring. Useful aromatic isocyanates include those in which one or more of the isocyanato groups are attached directly to the aromatic ring, and aromatic isocyanates in which one or more of the isocyanato groups are not attached directly to the aromatic ring. Useful heterocyclic isocyanates include those in which one or more of the isocyanato groups are attached directly to the heterocyclic ring and heterocyclic isocyanates in which one or more of the isocyanato groups are not attached directly to the heterocyclic ring.
Cycloaliphatic diisocyanates are desirable for use in the present invention because they are not adversely affected by ultraviolet light and can yield polyurethanes having high impact energy absorption levels, which make them desirable for glass replacements and bilayer safety glass applications. Also, polyurethanes prepared with cycloaliphatic diisocyanates are not adversely affected by conventional processing temperatures. When an aromatic polyisocyanate is used, generally, care should be taken to select a material that does not cause the polyurethane to color (e.g., yellow).
In some non-limiting embodiments, the aliphatic and cycloaliphatic diisocyanates can comprise about 6 to about 100 carbon atoms linked in a straight chain or cyclized and having two isocyanate reactive end groups.
Non-limiting examples of suitable aliphatic isocyanates include ethylene diisocyanate, trimethylene diisocyanate, 1,6-hexamethylene diisocyanate (HDI), tetramethylene diisocyanate, hexamethylene diisocyanate, octamethylene diisocyanate, nonamethylene diisocyanate, decamethylene diisocyanate, 1,6,11-undecanetriisocyanate, 1,3,6-hexamethylene triisocyanate, bis(isocyanatoethyl)-carbonate, bis(isocyanatoethyl)ether.
Other non-limiting examples of suitable aliphatic isocyanates include branched isocyanates such as trimethylhexane diisocyanate, trimethylhexamethylene diisocyanate (TMDI), 2,2′-dimethylpentane diisocyanate, 2,2,4-trimethylhexane diisocyanate, 2,4,4-trimethylhexamethylene diisocyanate, 1,8-diisocyanato-4-(isocyanatomethyl)octane, 2,5,7-trimethyl-1,8-diisocyanato-5-(isocyanatomethyl)octane, 2-isocyanatopropyl 2,6-diisocyanatohexanoate, lysinediisocyanate methyl ester and lysinetriisocyanate methyl ester.
Non-limiting examples of suitable cycloaliphatic isocyanates include dinuclear compounds bridged by an isopropylidene group or an alkylene group of 1 to 3 carbon atoms. Non-limiting examples of suitable cycloaliphatic isocyanates include 1,1′-methylene-bis-(4-isocyanatocyclohexane), 4,4′-methylene-bis-(cyclohexyl isocyanate) or 4,4′-dicyclohexylmethane diisocyanate (such as DESMODUR W commercially available from Bayer Corp. of Pittsburgh, Pa.), 4,4′-isopropylidene-bis-(cyclohexyl isocyanate), 1,4-cyclohexyl diisocyanate (CHDI), 3-isocyanato methyl-3,5,5-trimethylcyclohexyl isocyanate (a branched isocyanate also known as isophorone diisocyanate or IPDI) which is commercially available from Arco Chemical Co. of Newtown Square, Pa., and mixtures thereof.
Other useful dinuclear cycloaliphatic diisocyanates include those formed through an alkylene group of from 1 to 3 carbon atoms inclusive, and which can be substituted with nitro, chlorine, alkyl, alkoxy and other groups that are not reactive with hydroxyl groups (or active hydrogens) providing they are not positioned so as to render the isocyanate group unreactive. Also, aromatic diisocyanates such as meta-tetramethylxylylene diisocyanate (a branched isocyanate also known as 1,3-bis(1-isocyanato-1-methylethyl)-benzene which is commercially available from Cytec Industries Inc. of West Patterson, N.J. under the tradename TMXDI® (Meta) Aliphatic Isocyanate), and hydrogenated aromatic diisocyanates such as hydrogenated toluene diisocyanate may be used. Dinuclear diisocyanates in which one of the rings is saturated and the other unsaturated, which are prepared by partially hydrogenating aromatic diisocyanates such as diphenyl methane diisocyanates, diphenyl isopropylidene diisocyanate and diphenylene diisocyanate, may also be used.
Mixtures of cycloaliphatic diisocyanates with aliphatic diisocyanates and/or aromatic diisocyanates may also be used. An example is 4,4′-methylene-bis-(cyclohexyl isocyanate) with commercial isomer mixtures of toluene diisocyanate or meta-phenylene diisocyanate. Another useful mixture is 4,4′-methylene-bis-(cyclohexyl isocyanate) and isophorone diisocyanate.
Isothiocyanates corresponding to the above diisocyanates can be used, as well as mixed compounds containing both an isocyanate and a thioisocyanate group.
Non-limiting examples of suitable isocyanates can include but are not limited to DESMODUR W, DESMODUR N 3300 (hexamethylene diisocyanate trimer), DESMODUR N 3400 (60% hexamethylene diisocyanate dimer and 40% hexamethylene diisocyanate trimer), which are commercially available from Bayer Corp.
In some non-limiting embodiments, the isocyanate can include 1,1′-methylene-bis-(4-isocyanatocyclohexane) (also known as 4,4′-methylene-bis-(cyclohexyl isocyanate)) and isomeric mixtures thereof. As used herein, the term “isomeric mixtures” refers to a mixture of the cis-cis, trans-trans, and cis-trans isomers of the isocyanate. Non-limiting examples of isomeric mixtures suitable for use in the present invention can include the trans-trans isomer of 4,4′-methylenebis(cyclohexyl isocyanate), hereinafter referred to as “PICM” (paraisocyanato cyclohexylmethane), the cis-trans isomer of PICM, the cis-cis isomer of PICM, and mixtures thereof. Three suitable isomers of 4,4′-methylenebis(cyclohexyl isocyanate) (also known as 1,1′-methylenebis(4-isocyanatocyclohexane) for use in the present invention are shown below.




In some non-limiting embodiments, the PICM used in this invention can be prepared by phosgenating the 4,4′-methylenebis(cyclohexyl amine) (PACM) by procedures well-known in the art such as the procedures disclosed in U.S. Pat. Nos. 2,644,007 and 2,680,127, which are incorporated herein by reference. The PACM isomer mixtures, upon phosgenation, can produce PICM in a liquid phase, a partially liquid phase, or a solid phase at room temperature. The PACM isomer mixtures can be obtained by the hydrogenation of methylenedianiline and/or by fractional crystallization of PACM isomer mixtures in the presence of water and alcohols such as methanol and ethanol.
In some non-limiting embodiments, the isomeric mixture can comprise from about 10 to about 100 weight percent of the trans, trans isomer of 4,4′-methylenebis(cyclohexyl isocyanate) (PICM), or about 30 to about 100 weight percent, or about 50 to about 100 weight percent, or about 75 to about 100 weight percent. In other non-limiting embodiments, the cycloaliphatic isocyanate can consist essentially of the trans, trans isomer of 1,1′-methylene-bis-(4-isocyanatocyclohexane) (also known as 4,4′-methylene-bis-(cyclohexyl isocyanate)), e.g., at least about 80 weight percent of the trans, trans isomer of 1,1′-methylene-bis-(4-isocyanatocyclohexane), or at least about 90 weight percent of the trans, trans isomer of 1,1′-methylene-bis-(4-isocyanatocyclohexane), or at least about 95 weight percent of the trans, trans isomer of 1,1′-methylene-bis-(4-isocyanatocyclohexane) and in other non-limiting embodiments consists of about 100 weight percent of the trans, trans isomer of 1,1′-methylene-bis-(4-isocyanatocyclohexane).
Non-limiting examples of suitable polyisocyanates for use in the present invention include polyisocyanates and polyisothiocyanates having backbone linkages such as urethane linkages (—NH—C(O)—O—), thiourethane linkages (—NH—C(O)—S—), thiocarbamate linkages (—NH—C(S)—O—), dithiourethane linkages (—NH—C(S)—S—), polyamide linkages, and combinations thereof.
Other non-limiting examples of suitable polyisocyanates include ethylenically unsaturated polyisocyanates and polyisothiocyanates; alicyclic polyisocyanates and polyisothiocyanates; aromatic polyisocyanates and polyisothiocyanates wherein the isocyanate groups are not bonded directly to the aromatic ring, e.g., α,α′-xylylene diisocyanate; aromatic polyisocyanates and polyisothiocyanates wherein the isocyanate groups are bonded directly to the aromatic ring, e.g., benzene diisocyanate; aliphatic polyisocyanates and polyisothiocyanates containing sulfide linkages; aromatic polyisocyanates and polyisothiocyanates containing sulfide or disulfide linkages; aromatic polyisocyanates and polyisothiocyanates containing sulfone linkages; sulfonic ester-type polyisocyanates and polyisothiocyanates, e.g., 4-methyl-3-isocyanatobenzenesulfonyl-4′-isocyanato-phenol ester; aromatic sulfonic amide-type polyisocyanates and polyisothiocyanates; sulfur-containing heterocyclic polyisocyanates and polyisothiocyanates, e.g., thiophene-2,5-diisocyanate; halogenated, alkylated, alkoxylated, nitrated, carbodiimide modified, urea modified and biuret modified derivatives of isocyanates; and dimerized and trimerized products of isocyanates.
Non-limiting examples of suitable ethylenically unsaturated polyisocyanates include butene diisocyanate and 1,3-butadiene-1,4-diisocyanate. Non-limiting examples of suitable alicyclic polyisocyanates include isophorone diisocyanate, cyclohexane diisocyanate, methylcyclohexane diisocyanate, bis(isocyanatomethyl)cyclohexane, bis(isocyanatocyclohexyl)methane, bis(isocyanatocyclohexyl)-2,2-propane, bis(isocyanatocyclohexyl)-1,2-ethane, 2-isocyanatomethyl-3-(3-isocyanatopropyl)-5-isocyanatomethyl-bicyclo[2.2.1]-heptane, 2-isocyanatomethyl-3-(3-isocyanatopropyl)-6-isocyanatomethyl-bicyclo[2.2.1]-heptane, 2-isocyanatomethyl-2-(3-isocyanatopropyl)-5-isocyanatomethyl-bicyclo[2.2.1]-heptane, 2-isocyanatomethyl-2-(3-isocyanatopropyl)-6-isocyanatomethyl-bicyclo[2.2.1]-heptane, 2-isocyanatomethyl-3-(3-isocyanatopropyl)-5-(2-isocyanatoethyl)-bicyclo[2.2.1]-heptane and 2-isocyanatomethyl-2-(3-isocyanatopropyl)-6-(2-isocyanatoethyl)-bicyclo[2.2.1]-heptane.
Non-limiting examples of suitable aromatic polyisocyanates wherein the isocyanate groups are not bonded directly to the aromatic ring include α,α′-xylene diisocyanate, bis(isocyanatoethyl)benzene, α,α,α′,α′-tetramethylxylene diisocyanate, 1,3-bis(1-isocyanato-1-methylethyl)benzene, bis(isocyanatobutyl)benzene, bis(isocyanatomethyl)naphthalene, bis(isocyanatomethyl)diphenyl ether, bis(isocyanatoethyl)phthalate, mesitylene triisocyanate and 2,5-di(isocyanatomethyl)furan.
Non-limiting examples of suitable aromatic polyisocyanates having isocyanate groups bonded directly to the aromatic ring include phenylene diisocyanate, ethylphenylene diisocyanate, isopropylphenylene diisocyanate, dimethylphenylene diisocyanate, diethylphenylene diisocyanate, diisopropylphenylene diisocyanate, trimethylbenzene triisocyanate, benzene diisocyanate, benzene triisocyanate, naphthalene diisocyanate, methylnaphthalene diisocyanate, biphenyl diisocyanate, ortho-toluidine diisocyanate, ortho-tolylidine diisocyanate, ortho-tolylene diisocyanate, 4,4′-diphenylmethane diisocyanate, bis(3-methyl-4-isocyanatophenyl)methane, bis(isocyanatophenyl)ethylene, 3,3′-dimethoxy-biphenyl-4,4′-diisocyanate, triphenylmethane triisocyanate, polymeric 4,4′-diphenylmethane diisocyanate, naphthalene triisocyanate, diphenylmethane-2,4,4′-triisocyanate, 4-methyldiphenylmethane-3,5,2′,4′,6′-pentaisocyanate, diphenylether diisocyanate, bis(isocyanatophenylether)ethyleneglycol, bis(isocyanatophenylether)-1,3-propyleneglycol, benzophenone diisocyanate, carbazole diisocyanate, ethylcarbazole diisocyanate and dichlorocarbazole diisocyanate.
In some non-limiting embodiments, sulfur-containing isocyanates of the following general formula (I) can be used:




wherein R10 and R11 are each independently C1 to C3 alkyl.

Non-limiting examples of suitable aliphatic polyisocyanates containing sulfide linkages include thiodiethyl diisocyanate, thiodipropyl diisocyanate, dithiodihexyl diisocyanate, dimethylsulfone diisocyanate, dithiodimethyl diisocyanate, dithiodiethyl diisocyanate, dithiodipropyl diisocyanate and dicyclohexylsulfide-4,4′-diisocyanate. Non-limiting examples of aromatic polyisocyanates containing sulfide or disulfide linkages include but are not limited to diphenylsulfide-2,4′-diisocyanate, diphenylsulfide-4,4′-diisocyanate, 3,3′-dimethoxy-4,4′-diisocyanatodibenzyl thioether, bis(4-isocyanatomethylbenzene)-sulfide, diphenyldisulfide-4,4′-diisocyanate, 2,2′-dimethyldiphenyldisulfide-5,5′-diisocyanate, 3,3′-dimethyldiphenyldisulfide-5,5′-diisocyanate, 3,3′-dimethyldiphenyldisulfide-6,6′-diisocyanate, 4,4′-dimethyldiphenyldisulfide-5,5′-diisocyanate, 3,3′-dimethoxydiphenyldisulfide-4,4′-diisocyanate and 4,4′-dimethoxydiphenyldisulfide-3,3′-diisocyanate.
Non-limiting examples of suitable aromatic polyisocyanates containing sulfone linkages include diphenylsulfone-4,4′-diisocyanate, diphenylsulfone-3,3′-diisocyanate, benzidinesulfone-4,4′-diisocyanate, diphenylmethanesulfone-4,4′-diisocyanate, 4-methyldiphenylmethanesulfone-2,4′-diisocyanate, 4,4′-dimethoxydiphenylsulfone-3,3′-diisocyanate, 3,3′-dimethoxy-4,4′-diisocyanatodibenzylsulfone, 4,4′-dimethyldiphenyl sulfone-3,3′-diisocyanate, 4,4′-di-tert-butyl-diphenylsulfone-3,3′-diisocyanate and 4,4′-dichlorodiphenylsulfone-3,3′-diisocyanate.
Non-limiting examples of aromatic sulfonic amide-type polyisocyanates and suitable isothiocyanates are disclosed in U.S. Patent Application Publication 2009/0280709, incorporated by reference herein in its entirety.
In some non-limiting embodiments, the isocyanate comprises at least one triisocyanate or at least one polyisocyanate trimer. Non-limiting examples of such isocyanates include aromatic triisocyanates such as tris(4-iso-cyanatophenyl)methane (DESMODUR R), 1,3,5-tris(3-isocyanato-4-methylphenyl)-2,3,6-trioxohexahydro-1,3,5 triazine (DESMODUR IL); adducts of aromatic diisocyanates such as the adduct of 2,4-tolylene diisocyanate (TDI, 2,4-diisocyanatotoluene) and trimethylolpropane (DESMODUR L); and from aliphatic triisocyanates such as N-isocyanatohexylaminocarbonyl-N,N′-bis(isocyanatohexyl)urea (DESMODUR N), 2,4,6-trioxo-1,3,5-tris(6-isocyanatohexyl)hexahydro-1,3,5-triazine (DESMODUR N3390), 2,4,6-trioxo-1,3,5-tris(5-isocyanato-1,3,3-trimethylcyclo-hexylmethyl)hexahydro-1,3,5-triazine (DESMODUR Z4370), and 4-(isocyanatomethyl)-1,8-octane diisocyanate. The above DESMODUR products are commercially available from Bayer Corp. Also useful are the biuret of hexanediisocyanate, polymeric methane diisocyanate, and polymeric isophorone diisocyanate, and trimers of hexamethylene diisocyanate, isophorone diisocyanate and tetramethylxylylene diisocyanate.
In some non-limiting embodiments, the polyisocyanate used to make a polyurethane polyol prepolymer as a precursor is a cycloaliphatic compound, such as a dinuclear compound bridged by an isopropylidene group or an alkylene group of 1 to 3 carbon atoms.
The components for forming the isocyanate functional prepolymer comprise about 0.01 to about 0.5 equivalent of at least one polycarbonate polyol based upon the about 1 equivalent of the at least one polyisocyanate. As used herein, the term “polyol” includes compounds, monomers, oligomers and polymers comprising at least two hydroxyl groups (such as diols) or at least three hydroxyl groups (such as triols), higher functional polyols and mixtures thereof. Suitable polyols are capable of forming a covalent bond with a reactive group such as an isocyanate functional group.
In some non-limiting embodiments, the amount of the at least one polycarbonate polyol used to form the polyurethane is about 0.02 to about 0.5 equivalent, or about 0.025 to about 0.5 equivalent, or about 0.05 to about 0.5 equivalent; or about 0.1 to about 0.5 equivalent, or about 0.01 to about 0.3 equivalent based upon the about 1 equivalent of the at least one polyisocyanate.
Non-limiting examples of polycarbonate polyols include aliphatic polycarbonate diols, for example those based upon alkylene glycols, ether glycols, alicyclic glycols or mixtures thereof. In some embodiments, the alkylene groups for preparing the polycarbonate polyol can comprise from 5 to 10 carbon atoms and can be straight chain, cycloalkylene or combinations thereof. Non-limiting examples of such alkylene groups include hexylene, octylene, decylene, cyclohexylene and cyclohexyldimethylene. Suitable polycarbonate polyols can be prepared, in non-limiting examples, by reacting a hydroxy terminated alkylene glycol with a dialkyl carbonate, such as methyl, ethyl, n-propyl or n-butyl carbonate, or diaryl carbonate, such as diphenyl or dinaphthyl carbonate, or by reacting of a hydroxy-terminated alkylene diol with phosgene or bischoloroformate, in a manner well-known to those skilled in the art. Non-limiting examples of such polycarbonate polyols include those commercially available as RavecarbTM 107 from Enichem S.p.A. (Polimeri Europa) of Italy, and polyhexylene carbonate diols, about 1000 number average molecular weight, such as KM10-1733 polycarbonate diol prepared from hexanediol, available from Stahl. Examples of other suitable polycarbonate polyols that are commercially available include KM10-1122, KM10-1667 (prepared from a 50/50 weight percent mixture of cyclohexane dimethanol and hexanediol) (commercially available from Stahl U.S.A. Inc. of Peabody, Mass.), DESMOPHEN 2020E (commercially available from Bayer Corp), and ETERNACOLL® polycarbonate diols such as ETERNACOLL® UH-100W 1,6-hexanediol based polycarbonate diol (molecular weight of 1000, OH value of from 100-120 KOH mg/PCD g, melting point 45° C., viscosity 360-460 cP @ 75° C.) from UBE Industries.
The polycarbonate polyol can be produced by reacting a diol, such as described herein, and a dialkyl carbonate, such as described in U.S. Pat. No. 4,160,853. The polycarbonate polyol can include polyhexamethylene carbonate such as HO—(CH2)6—[O—C(O)—O—(CH2)6]n—OH, wherein n is an integer from 4 to 24, or from 4 to 10, or from 5 to 7.
Methods for making the prepolymer are discussed in detail below.
In some non-limiting embodiments, the components for preparing the isocyanate functional prepolymer can further comprise at least one polyol having at least 3 hydroxyl groups. The amount of the at least one polyol having at least 3 hydroxyl groups used to form the polyurethane is about 0.01 to about 1 equivalent, or about 0.02 to about 1 equivalent, or about 0.05 to about 1 equivalent, or about 0.1 to about 1 equivalent, or about 0.01 to about 0.7 equivalent, or about 0.1 to about 0.7 equivalent, or about 0.01 to about 0.3 equivalent based upon the about 1 equivalent of the at least one polyisocyanate.
In some non-limiting embodiments, the polyurethane comprises a reaction product of components comprising, consisting essentially or, or consisting of: the at least one isocyanate functional prepolymer discussed above and about 0.01 to about 1 equivalent of at least one polyol (b) having at least 3 hydroxyl groups based upon the about 1 equivalent of the at least one polyisocyanate. In some non-limiting embodiments, the components comprise about 0.01 to about 1 equivalent of the at least one polyol (b) having at least 3 hydroxyl groups, or about 0.02 to about 1 equivalent of the at least one polyol (b) having at least 3 hydroxyl groups, or about 0.1 to about 1 equivalent of the at least one polyol (b) having at least 3 hydroxyl groups, or about 0.4 to about 1 equivalent of the at least one polyol (b) having at least 3 hydroxyl groups or about 0.6 to about 0.7 equivalent of the at least one polyol (b).
The polyol having at least 3 hydroxyl groups can have at least 3 carbon atoms, or at least 4 carbon atoms, or 4 to 18 carbon atoms, or range from 4 to 18, or from 4 to 12, or from 4 to 10, or from 4 to 8, or from 4 to 6 carbon atoms. In some non-limiting embodiments, one or more carbon atoms in the polyol can be replaced with one or more heteroatoms, such as N, S, or O.
As discussed above, the polyol having at least 3 hydroxyl groups may increase the free volume within the polymer matrix to provide space for the molecules to move or rotate when impacted.
Non-limiting examples of suitable polyols having at least 3 hydroxyl groups include aliphatic, cycloaliphatic, aromatic, heterocyclic, oligomeric, and polymeric polyols and mixtures thereof. In some embodiments, such as for transparencies or windows exposed to sunlight, aliphatic or cycloaliphatic polyols can be used.
Non-limiting examples of trifunctional, tetrafunctional or higher polyols suitable for use as the polyol having at least 3 hydroxyl groups include alkane polyols such as glycerol (glycerin), tetramethylolmethane (pentaerythritol), trimethylolethane (for example 1,1,1-trimethylolethane), trimethylolpropane (TMP) (for example 1,1,1-trimethylolpropane), erythritol, pentaerythritol, dipentaerythritol, tripentaerythritol, sorbitan, alkoxylated derivatives thereof (discussed below) and mixtures thereof.
In some non-limiting embodiments, the polyol having at least 3 hydroxyl groups can be a cycloalkane polyol, such as trimethylene bis(1,3,5-cyclohexanetriol). In some non-limiting embodiments, the polyol having at least 3 hydroxyl groups can be an aromatic polyol, such as trimethylene bis(1,3,5-benzenetriol).
Further non-limiting examples of suitable polyols having at least 3 hydroxyl groups include the aforementioned polyols which can be alkoxylated derivatives, such as ethoxylated, propoxylated and butoxylated. In alternate non-limiting embodiments, the following polyols can be alkoxylated with from 1 to 10 alkoxy groups: glycerol, trimethylolethane, trimethylolpropane, benzenetriol, cyclohexanetriol, erythritol, pentaerythritol, sorbitol, mannitol, sorbitan, dipentaerythritol and tripentaerythritol. In alternate non-limiting embodiments, alkoxylated, ethoxylated and propoxylated polyols and mixtures thereof can be used alone or in combination with unalkoxylated, unethoxylated and unpropoxylated polyols having at least three hydroxyl groups and mixtures thereof. The number of alkoxy groups can be from 1 to 10, or from 2 to 8 or any rational number between 1 and 10. In a non-limiting embodiment, the alkoxy group can be ethoxy and the number of ethoxy groups can be 1 to 5 units. In another non-limiting embodiment, the polyol can be trimethylolpropane having up to 2 ethoxy groups. Non-limiting examples of suitable alkoxylated polyols include ethoxylated trimethylolpropane, propoxylated trimethylolpropane, ethoxylated trimethylolethane, and mixtures thereof.
Mixtures of any of the above polyols having at least 3 hydroxyl groups can be used.
In some non-limiting embodiments, the polyol having at least 3 hydroxyl groups can have a number average molecular weight of about 100 to about 500 grams/mole. In some non-limiting embodiments, the polyol having at least 3 hydroxyl groups can have a number average molecular weight of less than about 450 grams/mole or less than about 200 grams/mole.
In some embodiments, the polyurethanes of the present invention can be thermoplastics, for example those polyurethanes having a molecular weight per crosslink of at least about 6000 g/mole.
In some non-limiting embodiments, the components further comprise about 0.001 to about 0.5 equivalent or more, or about 0.01 to about 0.3 equivalent, or about 0.1 equivalent of at least one polyol (c) different from the polyol (b), based upon the about 1 equivalent of the at least one polyisocyanate. In some non-limiting embodiments, the polyol (c) is a diol.
In some non-limiting embodiments, the reaction components for preparing the polyurethane can further comprise about 0.01 to about 0.98 equivalents of at least one diol having 2 to 18 carbon atoms, or from about 2 to about 14 carbon atoms, or from 2 to 10 carbon atoms, or from 2 to 6 carbon atoms. In some non-limiting embodiments, one or more carbon atoms in the diol can be replaced with one or more heteroatoms, such as N, S, or O. The at least one diol having 2 to 18 carbon atoms can be a component used to prepare the prepolymer, and/or the overall polyurethane.
In some non-limiting embodiments, the amount of the diol used to form the polyurethane is about 0.01 to about 0.955 equivalent, or about 0.01 to about 0.875 equivalent, or about 0.01 to about 0.85 equivalent, or about 0.01 to about 0.4475 equivalent, or about 0.1 to about 0.98 equivalent, 0.1 to about 0.955 equivalent, or about 0.1 to about 0.875 equivalent, or about 0.1 to about 0.85 equivalent, or about 0.1 to about 0.4475 equivalent based upon the about 1 equivalent of the at least one polyisocyanate.
Non-limiting examples of suitable diols include straight chain alkane diols such as ethylene glycol, diethylene glycol, triethylene glycol, tetraethylene glycol, 1,2-ethanediol, propane diols such as 1,2-propanediol and 1,3-propanediol, butane diols such as 1,2-butanediol, 1,3-butanediol, and 1,4-butanediol, pentane diols such as 1,5-pentanediol, 1,3-pentanediol and 2,4-pentanediol, hexane diols such as 1,6-hexanediol and 2,5-hexanediol, heptane diols such as 2,4-heptanediol, octane diols such as 1,8-octanediol, nonane diols such as 1,9-nonanediol, decane diols such as 1,10-decanediol, dodecane diols such as 1,12-dodecanediol, octadecanediols such as 1,18-octadecanediol, sorbitol, mannitol, and mixtures thereof. In some non-limiting embodiments, the diol is a propane diol such as 1,2-propanediol and 1,3-propanediol, or butane diol such as 1,2-butanediol, 1,3-butanediol, and 1,4-butanediol. In some non-limiting embodiments, one or more carbon atoms in the polyol can be replaced with one or more heteroatoms, such as N, S, or O, for example sulfonated polyols, such as dithio-octane bis diol, thiodiethanol such as 2,2-thiodiethanol, or 3,6-dithia-1,2-octanediol.
Other non-limiting examples of suitable diols include those represented by the following formula:




wherein R represents C0 to C18 divalent linear or branched aliphatic, cycloaliphatic, aromatic, heterocyclic, or oligomeric saturated alkylene radical or mixtures thereof; C2 to C18 divalent organic radical containing at least one element selected from the group consisting of sulfur, oxygen and silicon in addition to carbon and hydrogen atoms; C5 to C18 divalent saturated cycloalkylene radical; or C5 to C18 divalent saturated heterocycloalkylene radical; and R′ and R′′ can be present or absent and, if present, each independently represent C1 to C18 divalent linear or branched aliphatic, cycloaliphatic, aromatic, heterocyclic, polymeric, or oligomeric saturated alkylene radical or mixtures thereof.

Other non-limiting examples of suitable diols include branched chain alkane diols, such as propylene glycol, dipropylene glycol, tripropylene glycol, neopentyl glycol, 2-methyl-butanediol. 2,2,4-trimethyl-1,3-pentanediol, 2-methyl-1,3-pentanediol, 2-ethyl-1,3-hexanediol, 2-methyl-1,3-propanediol, 2,2-dimethyl-1,3-propanediol, dibutyl 1,3-propanediol, polyalkylene glycols such as polyethylene glycols, and mixtures thereof.
In some non-limiting embodiments, the diol can be a cycloalkane diol, such as cyclopentanediol, 1,4-cyclohexanediol, cyclohexanedimethanols (CHDM), such as 1,4-cyclohexanedimethanol, cyclododecanediol, 4,4′-isopropylidene-biscyclohexanol, hydroxypropylcyclohexanol, cyclohexanediethanol, 1,2-bis(hydroxymethyl)-cyclohexane, 1,2-bis(hydroxyethyl)-cyclohexane, 4,4′-isopropylidene-biscyclohexanol, bis(4-hydroxycyclohexanol)methane and mixtures thereof.
In some non-limiting embodiments, the diol can be an aromatic diol, such as dihydroxybenzene, 1,4-benzenedimethanol, xylene glycol, hydroxybenzyl alcohol and dihydroxytoluene; bisphenols, such as, 4,4′-isopropylidenediphenol, 4,4′-oxybisphenol, 4,4′-dihydroxybenzophenone, 4,4′-thiobisphenol, phenolphthalein, bis(4-hydroxyphenyl)methane, 4,4′-(1,2-ethenediyl)bisphenol and 4,4′-sulfonylbisphenol; halogenated bisphenols, such as 4,4′-isopropylidenebis(2,6-dibromophenol), 4,4′-isopropylidenebis(2,6-dichlorophenol) and 4,4′-isopropylidenebis(2,3,5,6-tetrachlorophenol); alkoxylated bisphenols, which can have, for example, ethoxy, propoxy, α-butoxy and β-butoxy groups; and biscyclohexanols, which can be prepared by hydrogenating the corresponding bisphenols, such as 4,4′-isopropylidene-biscyclohexanol, 4,4′-oxybiscyclohexanol, 4,4′-thiobiscyclohexanol and bis(4-hydroxycyclohexanol)methane, the alkoxylation product of 1 mole of 2,2-bis(4-hydroxyphenyl)propane (i.e., bisphenol-A) and 2 moles of propylene oxide, hydroxyalkyl terephthalates such as meta or para bis(2-hydroxyethyl) terephthalate, bis(hydroxyethyl)hydroquinone and mixtures thereof.
In some non-limiting embodiments, the diol can be an heterocyclic diol, for example a dihydroxy piperidine such as 1,4-bis(hydroxyethyl)piperazine, a diol of an amide or alkane amide (such as ethanediamide (oxamide)), for example N,N′,bis(2-hydroxyethyl)oxamide, a diol of a propionate, such as 2,2-dimethyl-3-hydroxypropyl-2,2-dimethyl-3-hydroxypropionate, a diol of a hydantoin, such as bishydroxypropyl hydantoin, a diol of a phthalate, such as meta or para bis(2-hydroxyethyl)terephthalate, a diol of a hydroquinone, such as a dihydroxyethylhydroquinone, and/or a diol of an isocyanurate, such as dihydroxyethyl isocyanurate.
In some non-limiting embodiments, the diol for use in the present invention can be an SH-containing material, such as polythiols having at least three thiol groups and 4 to 18 carbon atoms. Non-limiting examples of suitable polythiols can include but are not limited to aliphatic polythiols, cycloaliphatic polythiols, aromatic polythiols, heterocyclic polythiols, polymeric polythiols, oligomeric polythiols and mixtures thereof. The sulfur-containing active hydrogen-containing material can have linkages including but not limited to ether linkages (—O—), sulfide linkages (—S—), polysulfide linkages (—Sx—, wherein x is at least 2, or from 2 to 4) and combinations of such linkages. As used herein, the terms “thiol,” “thiol group,” “mercapto” or “mercapto group” refer to an —SH group which is capable of forming a thiourethane linkage, (i.e., —NH—C(O)—S—) with an isocyanate group or a dithioruethane linkage (i.e., —NH—C(S)—S—) with an isothiocyanate group.
In some non-limiting embodiments, the components of the polyurethane are essentially free of SH-containing materials, i.e., comprise less than about 5 weight percent of SH-containing materials, in other non-limiting embodiments the components comprise less than about 2 weight percent of SH-containing materials, and in other non-limiting embodiments are free of SH-containing materials.
In some non-limiting embodiments, the diol can have a number average molecular weight of about 200 to about 10,000 grams/mole, or less than about 500 grams/mole, or less than about 200 grams/mole.
Mixtures of any of the above diols can be used.
In other non-limiting embodiments, the components of the polyurethane are essentially free of or free of diols, such as are discussed above. As used herein, “essentially free of diols” means that the reaction components comprise less than about 5 weight percent, or less than about 2 weight percent, or less than about 1 weight percent, or less than about 0.1 weight percent of diol, based upon the total components used to prepare the polyurethane.
In some non-limiting embodiments, the reaction components for preparing the polyurethane of can further comprise one or more non-branched triols and/or one or more higher functional polyols different from the polyol having at least 3 hydroxyl groups discussed above, and/or one or more branched or unbranched polyols (diols, triols, and/or higher functional polyols) having more than 18 carbon atoms. In some non-limiting embodiments, the amount of the one or more non-branched triols and/or one or more higher functional polyols different from the polyol having at least 3 hydroxyl groups, and/or one or more branched or unbranched polyols (diols, triols, and/or higher functional polyols) having more than 18 carbon atoms, used to form the polyurethane is about 0.01 to about 0.98 equivalent, or about 0.01 to about 0.9 equivalent, or about 0.01 to about 0.8 equivalent, or about 0.01 to about 0.5 equivalent, or about 0.01 to about 0.2 equivalent, or about 0.1 to about 0.98 equivalent, 0.1 to about 0.95 equivalent, or about 0.1 to about 0.8 equivalent, or about 0.1 to about 0.5 equivalent, or about 0.1 to about 0.2 equivalent based upon the about 1 equivalent of the at least one polyisocyanate.
Non-limiting examples of suitable non-branched triols and higher functional polyols include aliphatic, cycloaliphatic, aromatic, heterocyclic, oligomeric, and polymeric polyols and mixtures thereof, such as a cycloalkane polyol, such as cyclohexanetriol (for example 1,3,5-cyclohexanetriol), an aromatic polyol, such as benzenetriol (for example 1,2,3-benzenetriol, 1,2,4-benzenetriol, and 1,3,5-benzenetriol) and phenolphthalein, a polyol of an isocyanurate, such as tris hydroxyethyl isocyanurate.
In some non-limiting embodiments, the reaction components for preparing the polyurethane can further comprise one or more branched or unbranched polyols (diols, triols, and/or higher functional polyols) having more than 18 carbon atoms.
Non-limiting examples of suitable polyols having more than 18 carbon atoms include straight or branched chain aliphatic polyols, cycloaliphatic polyols, cycloaliphatic polyols, aromatic polyols, heterocyclic polyols, oligomeric polyols, polymeric polyols and mixtures thereof, such as 1,18-icosanediol and 1,24-tetracosanediol.
Other non-limiting examples of suitable polyols having more than 18 carbon atoms include those represented by the following formula:




wherein R represents C0 to C30 divalent linear or branched aliphatic, cycloaliphatic, aromatic, heterocyclic, or oligomeric saturated alkylene radical or mixtures thereof; C2 to C30 divalent organic radical containing at least one element selected from the group consisting of sulfur, oxygen and silicon in addition to carbon and hydrogen atoms; C5 to C30 divalent saturated cycloalkylene radical; or C5 to C30 divalent saturated heterocycloalkylene radical; and R′ and R′′ can be present or absent and, if present, each independently represent C1 to C30 divalent linear or branched aliphatic, cycloaliphatic, aromatic, heterocyclic, polymeric, or oligomeric saturated alkylene radical or mixtures thereof.
Non-limiting examples of other suitable cycloaliphatic polyols having more than 18 carbon atoms include biscyclohexanols having more than 18 carbon atoms, which can be prepared by hydrogenating the corresponding bisphenols, and aromatic polyols having more than 18 carbon atoms include bisphenols, and alkoxylated bisphenols, such as alkoxylated 4,4′-isopropylidenediphenol which can have from 3 to 70 alkoxy groups, oligomeric or polymeric polyols having more than 18 carbon atoms including higher polyalkylene glycols such as polyethylene glycols having number average molecular weights ranging from about 200 grams/mole to about 2,000 grams/mole, and mixtures thereof, or SH-containing materials, such as polythiols having at least two thiol groups or at least three thiol groups and at least 18 carbon atoms such as are disclosed in U.S. Patent Application Publication 2009/0280709, incorporated by reference herein.
In some non-limiting embodiments, the components of the polyurethane are essentially free of SH-containing materials, e.g., contain less than about 5 weight percent of SH-containing materials, in other non-limiting embodiments the components contain less than about 2 weight percent of SH-containing materials, and in other non-limiting embodiments are free of SH-containing materials.
In some non-limiting embodiments, the polyol having at least 18 carbon atoms can have a number average molecular weight of about 200 to about 5,000 grams/mole, or about 200 to about 4,000 grams/mole, or at least about 200 grams/mole, or at least about 400 grams/mole, or at least about 1000 grams/mole, or at least about 2000 grams/mole. In some non-limiting embodiments, the polyol can have a number average molecular weight of less than about 5,000 grams/mole, or less than about 4,000 grams/mole, or less than about 3,000 grams/mole, or less than about 2,000 grams/mole, or less than about 1,000 grams/mole, or less than about 500 grams/mole.
Mixtures of any of the above polyols can be used. For example, the polyol can comprise trimethylolpropane and the diol can comprise butanediol and/or pentanediol.
In some non-limiting embodiments, the polyurethanes can be prepared from reaction components comprising at least one polyester polyol and/or at least one polyether polyol. The amount of polyester polyol or polyether polyol can range from about 0.01 to about 0.5 equivalent, or about 0.1 to about 0.5 equivalent, or about 0.1 to about 0.3 equivalent, or about 0.1 to about 0.2 equivalent based upon the about 1 equivalent of polyisocyanate.
Non-limiting examples of such polyester polyols include polyester glycols, polycaprolactone polyols, and mixtures thereof, but not polycarbonate polyols. Polyester glycols can include the esterification products of one or more dicarboxylic acids having from four to ten carbon atoms, such as but not limited to adipic, succinic or sebacic acids, with one or more low molecular weight glycols having from two to ten carbon atoms, such as but not limited to ethylene glycol, propylene glycol, diethylene glycol, 1,4-butanediol, neopentyl glycol, 1,6-hexanediol and 1,10-decanediol. Esterification procedures for producing polyester polyols are described, for example, in the article by D. M. Young, F. Hostettler et al., “Polyesters from Lactone,” Union Carbide F-40, p. 147.
Non-limiting examples of polycaprolactone polyols include those prepared by condensing caprolactone in the presence of difunctional active hydrogen material such as water or low molecular weight glycols, for example ethylene glycol, propylene glycol, 1,2-propanediol, 1,4-butanediol, trimethylolpropane or 1,6-hexanediol, also known as polycaprolactone polyester polyols. Non-limiting examples of suitable polycaprolactone polyols can include commercially available materials designated as the CAPA series from Solvay Chemical of Houston, Tex., such as CAPA 2047A and CAPA 2077A polycaprolactone polyols, and the TONE series from Dow Chemical of Midland, Mich., such as TONE 0201, 0210, 0230 & 0241 polycaprolactone polyols. In some non-limiting embodiments, the polycaprolactone polyol has a molecular weight ranging from about 500 to about 2000 grams per mole, or about 500 to about 1000 grams per mole.
Non-limiting examples of polyether polyols include poly(oxyalkylene) polyols or polyalkoxylated polyols. Poly(oxyalkylene) polyols can be prepared in accordance with known methods. In a non-limiting embodiment, a poly(oxyalkylene) polyol can be prepared by condensing an alkylene oxide, or a mixture of alkylene oxides, using acid- or base-catalyzed addition with a polyhydric initiator or a mixture of polyhydric initiators, such as ethylene glycol, propylene glycol, glycerol, and sorbitol. Compatible mixtures of polyether polyols can also be used. As used herein, “compatible” means that two or more materials are mutually soluble in each other so as to essentially form a single phase. Non-limiting examples of alkylene oxides can include ethylene oxide, propylene oxide, butylene oxide, amylene oxide, aralkylene oxides, such as styrene oxide, mixtures of ethylene oxide and propylene oxide. In some non-limiting embodiments, polyoxyalkylene polyols can be prepared with mixtures of alkylene oxide using random or step-wise oxyalkylation. Non-limiting examples of such poly(oxyalkylene) polyols include polyoxyethylene polyols, such as polyethylene glycol, and polyoxypropylene polyols, such as polypropylene glycol.
Other polyether polyols include block polymers such as those having blocks of ethylene oxide-propylene oxide and/or ethylene oxide-butylene oxide. In some non-limiting embodiments, the polyether polyol comprises a block copolymer of the following formula:

HO—(CHR1CHR2—O)a—(CHR3CHR4—O)b—(CHR5CHR6—O)c—H

wherein R1 through R6 can each independently represent hydrogen or methyl; and a, b, and c can each be independently selected from an integer from 0 to 300, wherein a, b and c are selected such that the number average molecular weight of the polyol is less than about 32,000 grams/mole, or less than about 10,000 grams/mole, as determined by GPC. In other non-limiting embodiments a, b, and c each can be independently an integer from 1 to 300. In other non-limiting embodiments, R1, R2, R5, and R6 can be hydrogen, and R3 and R4 each can be independently selected from hydrogen and methyl, with the proviso that R3 and R4 are different from one another. In other non-limiting embodiments, R3 and R4 can be hydrogen, and R1 and R2 each can be independently selected from hydrogen and methyl, with the proviso that R1 and R2 are different from one another, and R5 and R6 each can be independently selected from hydrogen and methyl, with the proviso that R5 and R6 are different from one another.

In some non-limiting embodiments, polyalkoxylated polyols can be represented by the following general formula:




wherein m and n can each be a positive integer, the sum of m and n being from 5 to 70; R1 and R2 are each hydrogen, methyl or ethyl; and A is a divalent linking group such as a straight or branched chain alkylene which can contain from 1 to 8 carbon atoms, phenylene, and C1 to C9 alkyl-substituted phenylene. The values of m and n can, in combination with the selected divalent linking group, determine the molecular weight of the polyol. Polyalkoxylated polyols can be prepared by methods that are known in the art. In a non-limiting embodiment, a polyol such as 4,4′-isopropylidenediphenol can be reacted with an oxirane-containing material such as ethylene oxide, propylene oxide or butylene oxide, to form what is commonly referred to as an ethoxylated, propoxylated or butoxylated polyol having hydroxyl functionality. Non-limiting examples of polyols suitable for use in preparing polyalkoxylated polyols can include those polyols described in U.S. Pat. No. 6,187,444 B1 at column 10, lines 1-20, incorporated herein by reference.

In some non-limiting embodiments, the polyether polyol can be PLURONIC ethylene oxide/propylene oxide block copolymers, such as PLURONIC R and PLURONIC L62D, and/or TETRONIC tetra-functional block copolymers based on ethylene oxide and propylene oxide, such as TETRONIC R, which are commercially available from BASF Corp. of Parsippany, N.J.
As used herein, the phrase “polyether polyols” also can include poly(oxytetramethylene) diols prepared by the polymerization of tetrahydrofuran in the presence of Lewis acid catalysts such as, but not limited to, boron trifluoride, tin (IV) chloride and sulfonyl chloride.
In other non-limiting embodiments, the polyurethanes can be essentially free of polyester polyol and/or polyether polyol. As used herein, “essentially free of” polyester polyol and/or polyether polyol means that the reaction product components comprise less than about 10 weight percent of polyester polyol and/or polyether polyol, or less than about 5 weight percent of polyester polyol and/or polyether polyol, or less than about 2 weight percent of polyester polyol and/or polyether polyol, or is free of polyester polyol and/or polyether polyol, or less than about 0.1 equivalents of polyester polyol and/or polyether polyol.
In some non-limiting embodiments, the polyurethane has a hard segment content of about 10 to about 100 weight percent, or about 30 to about 70 weight percent. In some non-limiting embodiments, the polyurethane has a urethane content of about 20 to about 40 weight percent, or about 30 to about 43 weight percent. In some non-limiting embodiments, the polyurethane has a cyclic content of about 10 to about 80 weight percent, or about 30 to about 46 weight percent. In some non-limiting embodiments, the polyurethane has a molecular weight per crosslink of at least about 500 grams per mole or more.
In some non-limiting embodiments, the components for preparing the polyurethane and/or prepolymer can further comprise at least one polyol having one or more bromine atoms, one or more phosphorus atoms or combinations thereof. Brominated or phosphonated polyols can provide the polyurethane with enhanced flame retardancy. The flame retardancy of polyurethanes of the present invention can be determined simply by exposure to flame to determine if the polymer is self-extinguishing or burns more slowly than a polymer without the brominated or phosphonated polyol, or according to Underwriter's Laboratory Test UL-94, incorporated by reference herein. Alternatively, horizontal and vertical burning rate can be determined according to EC Directive 95/28/EC, Annexes IV and VI respectively, incorporated by reference herein. Federal Aviation Regulation (FAR) 25.853 (a)(1)(ii), incorporated by reference herein, permits a burn length of 8 inches and flame time of 15 seconds.
Non-limiting examples of suitable polyols having one or more bromine atoms, one or more phosphorus atoms or combinations thereof include 4,4′-isopropylidene bis(2,6-dibromophenol), isopropylidene bis[2-(2,6-dibromo-phenoxy)ethanol], bis(4-(2-hydroxyethoxy)-3,5-dibromophenyl)sulfone heptakis(dipropylene glycol)triphosphite, tris(dipropylene glycol) phosphate, diethyl-N,N-bis(2-hydroxyethyl)aminoethanol phosphonate and mixtures thereof. Non-limiting examples of suitable phosphonated polyols include those of the formula HO—Y—O[POOR—O—Y—O][POOR—O—Y—OH, wherein each R is independently selected from an alkylene group having 1 to 10 repeat units, such as CH2 to (CH2)10 and each Y is independently selected from an alkylene group having 1 to 6 repeat units, such as CH2 to (CH2)6.
The amount of brominated polyols and/or phosphonated polyols used to form the polyurethane of can be about 0.01 to about 0.9 equivalent, or about 0.1 to about 0.9 equivalent, or about 0.1 to about 0.3 equivalent, based upon the about 1 equivalent of polyisocyanate.
In some non-limiting embodiments, the components for preparing the polyurethane and/or prepolymer can further comprise one or more of the following: polyurethane polyols, (meth)acrylamides, hydroxy(meth)acrylamides, polyvinyl alcohols, polymers containing hydroxy functional (meth)acrylates, polymers containing allyl alcohols, dihydroxy oxamides, dihydroxyamides, dihydroxypiperidines, dihydroxy phthalates, dihydroxyethyl hydroquinones, polyesteramides and mixtures thereof. These additional components may or may not react with the other reaction components. In some embodiments, polymerization with acrylamides can form an interpenetrating network having high transparency, good impact strength, and high Young's Modulus.
Non-limiting examples of suitable polyurethane polyols include the reaction product of an excess of polyisocyanate and a branched or straight chain polyol. The equivalent ratio of polyisocyanate to polyol can range from about 1.0:0.05 to about 1.0:3, or about 1.0:0.7. The amount of polyurethane polyols used can range from about 1 to about 90 weight percent, about 5 to about 70 weight percent, or about 20 to about 50 weight percent on a basis of total weight of the components.
Non-limiting examples of suitable acrylamides include acrylamide, methacrylamide and dimethylacrylamide. The acrylamide can be added with all of the other reaction components, or it can be dissolved in the diol and then mixed with the other reaction components. The amount of acrylamide used can range from about 5 to about 70 weight percent, about 10 to about 50 weight percent, or about 10 to about 30 weight percent on a basis of total weight of the components.
Non-limiting examples of suitable polyvinyl alcohols include polyvinyl alcohol. The amount of polyvinyl alcohol used can range from about 5 to about 90 weight percent, about 10 to about 70 weight percent, or about 10 to about 40 weight percent on a basis of total weight of the components.
Non-limiting examples of suitable polymers containing hydroxy functional (meth)acrylates include hydroxypropylacrylate; hydroxyethylacrylate; hydroxypropylmethacrylate; hydroxyethylmethacrylate; and copolymers of hydroxy functional (meth)acrylates with acrylamides, cyanoethyl(meth)acrylates, methylmethacrylates, methacrylates, ethacrylates, propylacrylates and vinylpyrrolidinone. The amount of hydroxy functional (meth)acrylates used can range from about 10 to about 90 weight percent, about 10 to about 70 weight percent, or about 10 to about 30 weight percent on a basis of total weight of the components.
Non-limiting examples of suitable polymers containing allyl alcohols include diethylene glycol bis(allylcarbonate), allyloxytrimethylsilane, and diallylcarbonate. The amount of allyl alcohols used can range from about 5 to about 70 weight percent, about 10 to about 50 weight percent, or about 10 to about 30 weight percent.
Non-limiting examples of suitable polyesteramides include esteramide polymers obtained by the reaction of bis-oxamidodiols such as N,N′-bis(omega-hydroxyalkylene)oxamide with a dicarboxylic acid or diester such as diethyl oxalate, diethyl succinates, diethyl suberate, or dimethyl terephthalate. The amount of polyesteramides used can range from about 10 to about 80 weight percent, about 20 to about 60 weight percent, or about 30 to about 50 weight percent on a basis of total weight of the components.
In some non-limiting embodiments, the components for preparing the polyurethane and/or prepolymer can further comprise one or more amine curing agents. The amine curing agent, if present, can act as a catalyst in the polymerization reaction, be incorporated into the resulting polymerizate and can form poly(ureaurethane)s. The amount of amine curing agent used can range from about 0.05 to about 0.9 equivalents, about 0.1 to about 0.7 equivalents, or about 0.3 to about 0.5 equivalents.
Non-limiting examples of such amine curing agents include aliphatic polyamines, cycloaliphatic polyamines, aromatic polyamines and mixtures thereof. In some non-limiting embodiments, the amine curing agent can have at least two functional groups selected from primary amine (—NH2), secondary amine (—NH—) and combinations thereof. In some non-limiting embodiments, the amine curing agent can have at least two primary amine groups. In some non-limiting embodiments, the amino groups are all primary groups.
Examples of such amine curing agents include compounds having the following formula:




wherein R1 and R2 are each independently selected from methyl, ethyl, propyl, and isopropyl groups, and R3 is selected from hydrogen and chlorine, such as the following compounds manufactured by Lonza Ltd. (Basel, Switzerland): LONZACURE® M-DIPA, in which R1═C3H7; R2═C3H7; R3═H; LONZACURE® M-DMA, in which R1═CH3; R2═CH3; R3═H; LONZACURE® M-MEA, in which R1═CH3; R2═C2H5; R3═H; LONZACURE® M-DEA, in which R1═C2H5; R2═C2H5; R3═H; LONZACURE® M-MIPA: in which R1═CH3; R2═C3H7; R3═H; and LONZACURE® M-CDEA, in which R1═C2H5; R2═C2H5; R3═Cl, each of which is commercially available from Air Products and Chemicals, Inc. of Allentown, Pa.

Such amine curing agents can include a diamine curing agent such as 4,4′-methylenebis(3-chloro-2,6-diethylaniline), (LONZACURE® M-CDEA); 2,4-diamino-3,5-diethyl-toluene, 2,6-diamino-3,5-diethyl-toluene and mixtures thereof (collectively “diethyltoluenediamine” or “DETDA”), which is commercially available from Albemarle Corporation under the trade name ETHACURE 100; dimethylthiotoluenediamine (DMTDA) (commercially available as ETHACURE 300); the color stabilized version of ETHACURE 100 (i.e., formulation which contains an additive to reduce yellow color), which is available under the name ETHACURE 100S; 4,4′-methylene-bis-(2-chloroaniline) (commercially available from Kingyorker Chemicals under the trade name MOCA). DETDA can be a liquid at room temperature with a viscosity of 156 centipoise (cp) at 25° C. DETDA can be isomeric, with the 2,4-isomer amount being from 75 to 81 percent while the 2,6-isomer amount can be from 18 to 24 percent.
Other non-limiting examples of amine curing agents include ethyleneamines, such as ethylenediamine (EDA), diethylenetriamine (DETA), triethylenetetramine (TETA), tetraethylenepentamine (TEPA), pentaethylenehexamine (PEHA), piperazine, morpholine, substituted morpholine, piperidine, substituted piperidine, diethylenediamine (DEDA), and 2-amino-1-ethylpiperazine. In some non-limiting embodiments, the amine curing agent can be selected from one or more isomers of C1-C3 dialkyl toluenediamine, such as 3,5-dimethyl-2,4-toluenediamine, 3,5-dimethyl-2,6-toluenediamine, 3,5-diethyl-2,4-toluenediamine, 3,5-diethyl-2,6-toluenediamine, 3,5-diisopropyl-2,4-toluenediamine, 3,5-diisopropyl-2,6-toluenediamine, and mixtures thereof. In some non-limiting embodiments, the amine curing agent can be methylene dianiline or trimethyleneglycol di(para-aminobenzoate).
Other non-limiting examples of amine curing agents include compounds of the following general structures (XIII-XV):




Other non-limiting examples of amine curing agents include one or more methylene bis anilines, one or more aniline sulfides, and/or one or more bianilines, and other amine curing agents such as are disclosed in U.S. Patent Application Publication No. 2009/0280709, incorporated by reference herein.
In an embodiment wherein it is desirable to produce a poly(ureaurethane) having low color, the amine curing agent can be selected such that it has relatively low color and/or it can be manufactured and/or stored in a manner as to prevent the amine from developing a color (e.g., yellow).
In some non-limiting embodiments, the polyurethanes can be essentially free of amine curing agent, as discussed in detail below. As used herein, “essentially free of amine curing agent” means that the reaction product components comprise less than about 10 weight percent of amine curing agent, or less than about 5 weight percent of amine curing agent, or less than about 2 weight percent of amine curing agent, or in other non-limiting embodiments are free of amine curing agent.
The polyurethanes of the present invention can be polymerized using a variety of techniques. In some non-limiting embodiments described in further detail below, polyisocyanate(s) and polyol(s) and/or polythiol(s) can be reacted together in a one-pot process with other optional reaction components and/or catalyst to form the polyurethane.
In other non-limiting embodiments, the polyurethane can be prepared by reacting polyisocyanate(s) and polyol(s) to form a polyurethane prepolymer and then introducing other polyol(s), polythiol(s), polyisocyanates, and optionally catalyst and other optional reaction components.
In other non-limiting embodiments, the polyurethane can be prepared by reacting polyisocyanate(s) and polyol(s) to form an isocyanate functional urethane prepolymer and then introducing diol(s), polyols and optionally catalyst and other optional reaction components. In some non-limiting embodiments, the isocyanate functional urethane prepolymer, polyol and other reaction components, upon mixing, are maintained at a temperature of at least about 100° C. for at least about 10 minutes, or at least about 110° C., or at least about 120° C., or at least about 130° C., or at least about 140° C., for at least about 3 seconds to two hours or more, at least about 10 minutes, at least about 20 minutes, or at least about 30 minutes, or at least about an hour. In some non-limiting embodiments, upon mixing, the components are maintained at a temperature of at least about 100° C., or at least about 105° C., or at least about 110° C. for at least about 10 minutes, at least about 20 minutes, or at least about an hour, as described below.
In some non-limiting embodiments, the prepolymer and polyurethane can be prepared using a Max Urethane Processing System having a dynamic pin mixer, such as a Max Urethane Processing System Model No. 601-000-282 or Model No. 601-000-333 available from Max Machinery, Inc. of Healdsburg, Calif. The mixing head or chamber volume can be varied as desired, for example 8 cc, 62 cc, 70 cc, 140 cc, 205 cc or 250 cc. The Max Urethane Processing System is used to heat the raw materials to the specified temperatures desired, maintain the temperature of the raw materials delivered to the mix head, degass each component, and deliver the specified quantities of each raw material to a dynamic pin mixer for blending and dispensing. See “Max Urethane Processing System”, a publication of Max Machinery, Inc. (2005), incorporated by reference herein. The dynamic pin mixers can run at 3,000 to 12,000 RPM. The system can be continuous or synchronized to the dispensing pour. In some embodiments, increased residence time of the reactants in the mix head can provide improved physical properties, such as Young's Modulus and Gardner Impact strength. For some embodiments, a residence time of about 0.5 seconds to about 30 minutes, 4 seconds to about 30 minutes, or about 4 seconds to about 15 minutes, or about 4 seconds to about 1 minute, or about 4 to about 30 seconds, or about 4 to about 15 seconds, or about 4 to about 8 seconds can be desirable.
Whether prepared in a one-shot process or in a multi-stage process using a prepolymer, in some non-limiting embodiments, the aforementioned ingredients each can be degassed prior to reaction. In some non-limiting embodiments, the prepolymer can be degassed, the difunctional material can be degassed, and then these two materials can be combined. One or more of the reactants can be preheated to a temperature of at least about 100° C., at least about 110° C., or at least about 120° C., prior to reaction. The components can be cured after degassing.
In the “one shot”, “one pot” or bulk polymerization method, all of the ingredients, that is, isocyanate, polyol and diol are mixed simultaneously. This method is generally satisfactory when all active hydrogens react at about the same rate such as when all contain hydroxyl groups as the only reactive sites. The urethane reaction can be conducted under anhydrous conditions with dry reactants such as in a nitrogen atmosphere of atmospheric pressure and at a temperature ranging from about 75° C. to about 140° C. If polycarbonate polyols or any hydroxy functional compounds are used, they are typically dried before reaction, usually to a moisture content ranging from about 0.01 to about 0.05 percent.
To obtain the randomness desired and a generally clear polymer, the diol, for example, anhydrous 1,4-butanediol (containing a maximum of 0.04 percent water) can be added to the polyol under a nitrogen atmosphere to exclude moisture and the temperature maintained sufficiently high so that there is no phase separation and a homogeneous mixture is obtained. The polyisocyanate, for example, 4,4′-methylene-bis-(cyclohexyl isocyanate), can be added rapidly and the mixture can be maintained at a temperature of at least about 75° C., or at least about 85° C., or at least about 90° C., or at least about 95° C. for at least about 10 minutes or at least about 20 minutes. In some embodiments, upon mixing, the mixture is maintained at a temperature of at least about 100° C., or at least about 105° C., or at least about 110° C. for at least about 10 minutes or at least about 20 minutes, so that there is no phase separation and the mixture remains homogeneous, prior to degassing and cure. upon mixing, the mixture can be maintained at a pressure of ranging from about 2 to about 6 mm Hg (about 266.6 to about 800 Pascal (Pa)), or about 266.6 Pa for a time period of about 10 minutes to about 24 hours, or about 10 minutes to about 4 hours prior to degassing and cure.
In some non-limiting embodiments, upon mixing the mixture can be vigorously agitated at a temperature of at least about 75° C., or at least about 85° C., or at least about 90° C., or at least about 95° C., or at least about 100° C., or at least about 105° C., or at least about 110° C., and degassed for a period of at least about 3 minutes during which time the pressure is reduced from atmospheric to about 3 millimeters of mercury. The reduction in pressure facilitates the removal of the dissolved gases such as nitrogen and carbon dioxide and then the ingredients can be reacted at a temperature ranging from about 100° C. to about 140° C., or about 110° C. to about 140° C., in the presence of a catalyst and the reaction continued until there are substantially no isocyanate groups present, in some embodiments for at least about 6 hours. In the absence of a catalyst, the reaction can be conducted for at least about 24 hours, such as under a nitrogen atmosphere. After degassing, the mixture can be reacted or cured at a temperature of at least about 90° C., or at least about 95° C., or at least about 100° C., or at least about 105° C., or at least about 110° C., or at least about 120° C., or at least about 125° C., or at least about 130° C., or at least about 140° C., or generally about 90° C. to about 200° C., or at least about 90° C. to about 160° C. or 180° C., or any subrange within these ranges.
In some non-limiting embodiments, wherein a window can be formed, the polymerizable mixture which can be optionally degassed can be introduced into a mold and the mold can be heated (i.e., thermal cure cycle) using a variety of conventional techniques known in the art. The thermal cure cycle can vary depending on the reactivity and molar ratio of the reactants. In a non-limiting embodiment, the thermal cure cycle can include heating the mixture of prepolymer and diol and optionally diol and dithiol; or heating the mixture of polyisocyanate, polyol and/or polythiol and diol or diol/dithiol, from room temperature to a temperature of about 200° C. over a period of from about 0.5 hour to about 72 hours; or from about 80° C. to about 150° C. for a period of from about 5 hours to about 48 hours.
In other non-limiting embodiments described in further detail below, isocyanate and polyol can be reacted together to form a polyurethane prepolymer and the prepolymer can be reacted with more of the same or a different polyol(s) and/or diol(s) to form a polyurethane or sulfur-containing polyurethane. When the prepolymer method is employed, the prepolymer and diol(s) can be heated so as to reduce the prepolymer viscosity to about 200 cp or at most a few thousand centipoise so as to aid in mixing. As in the bulk polymerization, reaction should be conducted under anhydrous conditions with dry reactants. The reactants can be preheated to a temperature of at least about 100° C., at least about 110° C., or at least about 120° C. prior to reaction. Upon mixing, the reactants can be maintained at a temperature of at least about 100° C., at least about 110° C. or at least about 120° C. for at least about 10 minutes to at least about 2 hours, to facilitate reaction, prior to degassing and curing. Upon mixing, the mixture can be maintained at a pressure of ranging from about 2 to about 6 mm Hg (about 266.6 to about 800 Pascal (Pa)), or about 266.6 Pa for a time period of about 10 minutes to about 24 hours, or about 10 minutes to about 4 hours.
In some non-limiting embodiments, the present invention provides a process for preparing a polyurethane article comprising: (a) heating a mixture of about 1 equivalent of at least one polyisocyanate and about 0.01 to about 0.5 equivalent of at least one polycarbonate polyol based upon the about 1 equivalent of the at least one polyisocyanate, to a temperature of about 110° C. to about 130° C. for at least about an hour to form a reaction product; (b) mixing the reaction product (a) with about 0.3 to about 1 equivalent of at least one polyol having at least 3 hydroxyl groups based upon the about 1 equivalent of the at least one polyisocyanate until the mixture reaches a temperature of at least about 110° C. to about 130° C., optionally by heating if necessary; (c) casting the reaction product into a mold preheated to a temperature of at least about 100° C. to about 130° C.; and (d) curing the reaction product at a first predetermined temperature of about 100° C. to about 120° C. for at least about 0.5 hours; and then at a second predetermined temperature of about 140° C. to about 180° C. for about 15 to about 30 hours.
In some non-limiting embodiments, upon mixing, the components are maintained at a temperature of at least about 100° C., or at least about 105° C., or at least about 110° C. for at least about 10 minutes or at least about 20 minutes prior to degassing and/or curing in a manner such as is discussed above.
The polyurethane prepolymer can have a number average molecular weight (Mn) of less than about 50,000 grams/mole, or less than about 20,000 grams/mole, or less than about 10,000 grams/mole, or less than about 5,000 grams/mole, or at least about 1,000 grams/mole or at least about 2,000 grams/mole, inclusive of any range in between.
When polyurethane-forming components, such as polyols and isocyanates, are combined to produce polyurethanes, the relative amounts of the ingredients are typically expressed as a ratio of the available number of reactive isocyanate groups to the available number of reactive hydroxyl groups, i.e., an equivalent ratio of NCO:OH. For example, a ratio of NCO:OH of 1.0:1.0 is obtained when the weight of one NCO equivalent of the supplied form of the isocyanate component is reacted with the weight of one OH equivalent of the supplied form of the organic polyol component. The polyurethanes of the present invention can have an equivalent ratio of NCO:OH ranging from about 0.9:1.0 to about 1.1:1.0, or about 1.0:1.0.
In some non-limiting embodiments, when the isocyanate and polyol are reacted to form a prepolymer, the isocyanate is present in excess, for example the amount of isocyanate and the amount of polyol in the isocyanate prepolymer can be selected such that the equivalent ratio of (NCO):(OH) can range from about 1.0:0.05 to about 1.0:0.7.
In some non-limiting embodiments, the amount of isocyanate and the amount of polyol used to prepare isocyanate-terminated polyurethane prepolymer or isocyanate-terminated sulfur-containing polyurethane prepolymer can be selected such that the equivalent ratio of (NCO):(SH+OH) can be at least about 1.0:1.0, or at least about 2.0:1.0, or at least about 2.5:1.0, or less than about 4.5:1.0, or less than about 5.5:1.0; or the amount of isothiocyanate and the amount of polyol used to prepare isothiocyanate-terminated sulfur-containing polyurethane prepolymer can be selected such that the equivalent ratio of (NCS):(SH+OH) can be at least about 1.0:1.0, or at least about 2.0:1.0, or at least about 2.5:1.0, or less than about 4.5:1.0, or less than about 5.5:1.0; or the amount of a combination of isothiocyanate and isocyanate and the amount of polyol used to prepare isothiocyanate/isocyanate terminated sulfur-containing polyurethane prepolymer can be selected such that the equivalent ratio of (NCS+NCO):(SH+OH) can be at least about 1.0:1.0, or at least about 2.0:1.0, or at least about 2.5:1.0, or less than about 4.5:1.0, or less than about 5.5:1.0
The ratio and proportions of the diol and the polyol can affect the viscosity of the prepolymer. The viscosity of such prepolymers can be important, for example when they are intended for use with coating compositions, such as those for flow coating processes. The solids content of such prepolymers, however, also can be important, in that higher solids content can achieve desired properties from the coating, such as weatherability, scratch resistance, etc. In conventional coatings, coating compositions with higher solids content typically require greater amounts of solvent material to dilute the coating in order to reduce the viscosity for appropriate flow coating processes. The use of such solvents, however, can adversely affect the substrate surface, particularly when the substrate surface is a polymeric material. In the present invention, the viscosity of the prepolymer can be appropriately tailored to provide a material with lower viscosity levels at higher solids content, thereby providing an effective coating without the need for excessive amounts of solvents which can deleteriously affect the substrate surface.
In some non-limiting embodiments in which optional amine curing agent is used, the amount of isocyanate-terminated polyurethane prepolymer or sulfur-containing isocyanate-terminated polyurethane prepolymer and the amount of amine curing agent used to prepare sulfur-containing polyurethane can be selected such that the equivalent ratio of (NH+SH+OH):(NCO) can range from about 0.80:1.0 to about 1.1:1.0, or from about 0.85:1.0 to about 1.0:1.0, or from about 0.90:1.0 to about 1.0:1.0, or from about 0.90:1.0 to about 0.95:1.0, or from about 0.95:1.0 to about 1.0:1.0.
In some non-limiting embodiments, the amount of isothiocyanate or isothiocyanate/isocyanate terminated sulfur-containing polyurethane prepolymer and the amount of amine curing agent used to prepare sulfur-containing polyureaurethane can be selected such that the equivalent ratio of (NH+SH+OH):(NCO+NCS) can range from about 0.80:1.0 to about 1.1:1.0, or from about 0.85:1.0 to about 1.0:1.0, or from about 0.90:1.0 to about 1.0:1.0, or from about 0.90:1.0 to about 0.95:1.0, or from about 0.95:1.0 to about 1.0:1.0.
It is believed that the unusual energy absorption properties and transparency of the polyurethanes of the present invention may not only be dependent upon the urethane ingredients and proportions, but also may be dependent on the method of preparation. More particularly, it is believed that the presence of polyurethane regular block segments may adversely affect the polyurethane transparency and energy absorption properties and, consequently, it is believed that random segments within the polymer can provide optimal results. Consequently, whether the urethane contains random or regular block segments depends upon the particular reagents and their relative reactivity as well as the conditions of reaction. Generally speaking, the polyisocyanate will be more reactive with a low molecular weight diol or polyol, for example, 1,4-butanediol, than with a polymeric polyol and, hence, in some non-limiting embodiments, it is desirable to inhibit the preferential reaction between the low molecular weight diol or polyol and the polyisocyanate such as by rapidly adding the polyisocyanate to an intimate mixture of the low molecular weight diol or polyol and polymeric polyol with vigorous agitation, such as at a temperature of at least about 75° C. when no catalyst is employed, and then, upon mixing, maintained at temperature of reaction of at least about 100° C. or about 110° C. after the exotherm has subsided. When a catalyst is employed, the initial mixing temperature can be lower, such as about 60° C., so that the exotherm does not carry the temperature of the mixture substantially above the reaction temperature desired. Inasmuch as the polyurethanes are thermally stable, however, reaction temperatures can reach as high as about 200° C. and as low as about 60° C., and in some non-limiting embodiments, ranging from about 75° C. to about 130° C. when a catalyst is employed, or ranging from about 80° C. to about 100° C. When no catalyst is employed, in some non-limiting embodiments the reaction temperature can range from about 130° C. to about 150° C.
It is also desirable, upon mixing, to rapidly attain reaction temperatures after a homogeneous mixture is obtained when a catalyst is not employed, so that the polymer does not become hazy due to phase separation. For example, some mixtures can become hazy in less than one-half hour at less than 80° C. without catalyst. Thus, it can be desirable either to use a catalyst or introduce the reactants to rapidly reach a reaction temperature above about 100° C., or about 110° C. or about 130° C., for example by the use of a high-speed shear mixing head, so that the polymer does not become hazy. Suitable catalysts can be selected from those known in the art. In some non-limiting embodiments, degassing can take place prior to or following addition of catalyst.
In some non-limiting embodiments, a urethane-forming catalyst can be used in the present invention to enhance the reaction of the polyurethane-forming materials. Suitable urethane-forming catalysts include those catalysts that are useful for the formation of urethane by reaction of the NCO and OH-containing materials, and which have little tendency to accelerate side reactions leading to allophonate and isocyanate formation. Non-limiting examples of suitable catalysts are selected from the group of Lewis bases, Lewis acids and insertion catalysts as described in Ullmann's Encyclopedia of Industrial Chemistry, 5th Edition, 1992, Volume A21, pp. 673 to 674.
In some non-limiting embodiments, the catalyst can be a stannous salt of an organic acid, such as stannous octoate or butyl stannoic acid. Other non-limiting examples of suitable catalysts include tertiary amine catalysts, tertiary ammonium salts, tin catalysts, phosphines or mixtures thereof. In some non-limiting embodiments, the catalysts can be dimethyl cyclohexylamine, dibutyl tin dilaurate, dibutyltin diacetate, dibutyltin mercaptide, dibutyltin diacetate, dibutyl tin dimaleate, dimethyl tin diacetate, dimethyl tin dilaurate, 1,4-diazabicyclo[2.2.2]octane, bismuth carboxylates, zirconium carboxylates, zinc octoate, ferric acetylacetonate and mixtures thereof. The amount of catalyst used can vary depending on the amount of components, for example about 10 ppm to about 600 ppm.
In alternate non-limiting embodiments, various additives can be included in compositions comprising the polyurethane(s) of the present invention. Such additives include light stabilizers, heat stabilizers, antioxidants, colorants, fire retardants, ultraviolet light absorbers, light stabilizers such as hindered amine light stabilizers, mold release agents, static (non-photochromic) dyes, fluorescent agents, pigments, surfactants, flexibilizing additives, such as but not limited to alkoxylated phenol benzoates and poly(alkylene glycol) dibenzoates, and mixtures thereof. Non-limiting examples of anti-yellowing additives include 3-methyl-2-butenol, organo pyrocarbonates and triphenyl phosphite (CAS Registry No. 101-02-0). Examples of useful antioxidants include IRGANOX 1010, IRGANOX 1076, and IRGANOX MD 1024, each commercially available from Ciba Specialty Chemicals of Tarrytown, N.Y. Examples of useful UV absorbers include CYASORB UV 5411, TINUVIN 130 and TINUVIN 328 commercially available Ciba Specialty Chemicals, and SANDOVAR 3206 commercially available from Clariant Corp. of Charlotte, N.C. Examples of useful hindered amine light stabilizers include SANDOVAR 3056 commercially available from Clariant Corp. of Charlotte, N.C. Examples of useful surfactants include BYK 306 commercially available from BYK Chemie of Wesel, Germany.
Such additives can be present in an amount such that the additive constitutes less than about 30 percent by weight, or less than about 15 percent by weight, or less than about 5 percent by weight, or less than about 3 percent by weight, based on the total weight of the polymer. In some non-limiting embodiments, the aforementioned optional additives can be pre-mixed with the polyisocyanate(s) or isocyanate functional prepolymer. In other non-limiting embodiments, the optional additives can be pre-mixed with the polyol(s) or urethane prepolymer.
Poly(ureaurethanes)
Poly(ureaurethane)s can be prepared from any of the above polyurethanes by including one or more amine curing agents in the reaction components. The amine functionality of the amine curing agent can react with isocyanate groups to form urea linkages or units within the polyurethane matrix. Suitable amounts of amine curing agents and reaction conditions are discussed in detail above.
Optionally, the components further comprise about 0.01 to about 0.5 equivalent, or about 0.01 to about 0.1 equivalent, of water based upon the about 1 equivalent of the at least one polyisocyanate. The water can be reacted with the isocyanate functional prepolymer, and/or included in the reaction of the isocyanate functional prepolymer and polyol (b), as desired, to form a poly(ureaurethane). The reaction synthesis can be as described above with respect to Poly(ureaurethane) Synthesis A or B.
Poly(ureaurethane) Synthesis A
Alternatively or additionally, urea linkages or units can be formed within the polyurethane matrix to the extent desired by reacting isocyanate functional groups of the polyisocyanate with water. As shown in Step 1 of the reaction scheme of Poly(ureaurethane) Synthesis A below, isocyanate functional groups are converted to carbamate functional groups by the reaction with water. In some non-limiting embodiments, the equivalent ratio of NCO:water ranges from about 10:1 to about 2:1, or about 5:1 to about 2:1, or about 3:1 to about 2:1.
The isocyanate shown in Step 1 is a diisocyanate in which R is any linking group, such as aliphatic, cycloaliphatic, aromatic, heterocycle, etc. as described in detail above. However, one skilled in the art would understand that the isocyanate can have one or more, two or more, three or more or a higher number of isocyanate functional groups, as desired. Examples of suitable isocyanates can be any of the isocyanates discussed above. In some non-limiting embodiments, the polyisocyanate is one or more aliphatic polyisocyanates. In some non-limiting embodiments, the polyisocyanate is 4,4′-methylene-bis-(cyclohexyl isocyanate) (such as DESMODUR W).
Removal of carbon dioxide facilitates conversion of the carbamate groups into amine groups. Excess isocyanate is desirable to ensure essentially complete consumption of the water. Also, it is desirable to remove essentially all of the carbon dioxide generated to facilitate conversion to amine groups. The water can be reacted with the polyisocyanate or polyurethane polyisocyanate prepolymer at a temperature of up to about 60° C. under vacuum. The vacuum pressure should be low enough so as not to remove water from the system, and can range for example from about 10 to about 20 mm Hg (about 1333 to about 2666 Pa) for a time period of about 10 to about 30 minutes. After the reaction is essentially complete, i.e., no further carbon dioxide is formed, the temperature can be increased to at least about 100° C. or about 110° C. and heated for about 2 to about 24 hours, or about 2 hours, using 10 ppm or more of catalyst such as dibutyltin diacetate. After substantially all of the water reacts with the excess isocyanate, the amine that is formed reacts essentially instantaneously with the isocyanate.




As is well known to those skilled in the art, certain amine curing agents (such as aliphatic amine curing agents having 2 to 18 carbon atoms, e.g., ethylene diamine, diethylenediamine, diaminobutane, PACM, diamine hexane, 1,10-decanediamine) are highly reactive and impractical to use under normal production conditions because the amine functionality begins to react with oxygen present in the ambient air very quickly to discolor the polymerizate. Aliphatic amine curing agents are typically very hygroscopic and difficult to keep dry. Generally, aliphatic amines are so reactive as to be impractical for making 100% solids, transparent, low color and low haze plastics.
By forming the amine in situ as discussed above and shown in Step 2, amines can be generated in situ that normally are not practical to use under normal production conditions without formation of undesirable side products, color or haze. Also, the rate of reaction can be more easily regulated. This reaction can be used for any type of polyisocyanate described above, but is especially useful for converting aliphatic polyisocyanates to amines as described above.
As shown in Step 2 above, the amine formed in situ reacts with another isocyanate to form a urea group. Use of excess polyisocyanate permits formation of an isocyanate functional urea prepolymer. In some non-limiting embodiments, the equivalent ratio of NCO:amine functional groups ranges from about 1:0.05 to about 1:0.7, or about 1:0.05 to about 1:0.5, or about 1:0.05 to about 1:0.3. Suitable reaction temperatures can range from about 25° C. to about 60° C. with a catalyst such as a tin catalyst. After the water is reacted and the carbon dioxide removed, the reaction temperature can be increased up to about 90° C. for about 2 to about 4 hours. Alternatively, the reaction can proceed at about 25° C. for up to about 8 hours until complete. Optionally, one or more polyols or diols as described above can be included in this reaction to form isocyanate functional urethane prepolymers, as shown in Poly(ureaurethane) Synthesis B, described in further detail below.
As shown in Step 3 of the reaction scheme of Poly(ureaurethane) Synthesis A above, the polyol and/or diol can be reacted with the isocyanate functional urea prepolymer(s) to form poly(ureaurethane)s of the present invention. The polyol shown in Step 3 can be a diol (m=2), triol (m=3) or higher hydroxyl functional material (m=4 or more) as described above in which R1 is any linking group, such as aliphatic, cycloaliphatic, aromatic, heterocycle, etc. as described in detail above with respect to the polyols. Examples of suitable polyols can be any of the polyols discussed above. In some non-limiting embodiments, the polyol can be polycarbonate polyol, trimethylolpropane and butanediol and/or pentanediol. Suitable amounts of polyols for reacting with the isocyanate functional urea prepolymer as polyisocyanate are discussed in detail above. In the above poly(ureaurethane), x can range from 1 to about 100, or about 1 to about 20.
In some non-limiting embodiments, to form the poly(ureaurethane) the isocyanate functional prepolymer is heated to a temperature of about 90° C., the polyol(s) are added and heated to about 90° C. The temperature can be increased to about 100° C. or about 110° C. to facilitate compatibilization, then about 2 to about 4 mm of vacuum can be applied for about 3 to about 5 minutes. Upon mixing, the reaction components can be maintained at a temperature of at least about 100° C., or 105° C., or 110° C., or 120° C., for at least about 10 minutes or about 20 minutes, prior to degassing and cure.
To prepare an article, for example, the mixture can be poured or pressure cast into a release-coated glass casting mold to form an article of desired thickness and dimensions. The interior of the mold can be coated with a release substance such as are well know to those skilled in the art. In some embodiments, the casting mold is preheated to a temperature of about 200° F. (93.3° C.), or about 100° C. to about 160° C. The filled mold or cell can be placed in an oven at a temperature of about 100° C. to about 200° C., or about 250° F. (121° C.) to about 320° F. (160° C.) and cured for about 24 to about 48 hours, for example. In some embodiments, the curing can be conducted at different temperatures for different periods of time. For example, the reaction product can be cured at a first predetermined temperature of about 100° C. to about 120° C. for at least about 0.5 hours to about 2 hours, then at a second predetermined temperature of about 140° C. to about 200° C., or about 140° C. to about 180° C., for about 5 to about 30 hours, or about 15 to about 30 hours. The cell can be removed from the oven and cooled to a temperature of about 25° C. and the cured polymer released from the casting mold.
In some non-limiting embodiments, the polyurethane can be cast into the final desired shape of the designed product such that no further processing is needed to achieve the final shape. For example, the polyurethane can be cast into the final shape of a transparency or a portion of a transparency, and the final shaped configuration can include both simple, compound and complex curvatures as well as variations in material thickness.
The reaction synthesis can be as described above with respect to Poly(ureaurethane) Synthesis A. Optionally, a portion of one or more polyols or diols as described above can be included in this reaction to form isocyanate functional urethane prepolymer which is then further reacted with another portion of polyol and/or diol, as shown in Poly(ureaurethane) Synthesis B, described in further detail below. Any of the other optional components discussed herein can be included in the reaction in amounts as described herein.
In some non-limiting embodiments, upon mixing, the components are maintained, for example, at a temperature of at least about 100° C., or at least about 105° C., or at least about 110° C. for at least about 10 minutes or at least about 20 minutes, prior to degassing and cure, as described herein.
Poly(ureaurethane) Synthesis B
As shown generally in Poly(ureaurethane) Synthesis B below, in other non-limiting embodiments urea linkages or units can be formed within the polyurethane matrix to the extent desired by reacting polyisocyanate(s) and a portion of the polyol(s) to form at least one isocyanate functional urethane prepolymer, and then reacting the isocyanate functional urethane prepolymer(s) with water. As shown in Step 1 of the reaction scheme of Poly(ureaurethane) Synthesis B below, a portion of the polyol(s) and/or diol(s) can be reacted with polyisocyanate(s) to form the at least one isocyanate functional urethane prepolymer. In some non-limiting embodiments, the equivalent ratio of NCO:OH functional groups ranges from about 1:0.05 to about 1:0.7, or about 1:0.05 to about 1:0.5, or about 1:0.05 to about 1:0.3. It is desirable to use excess isocyanate to ensure essentially complete conversion of the hydroxyl groups to urethane groups.
The isocyanate shown in Step 1 is a diisocyanate in which R is any linking group, such as aliphatic, cycloaliphatic, aromatic, heterocycle, etc. as described in detail above. However, one skilled in the art would understand that the isocyanate can have one or more, two or more, three or more or a higher number of isocyanate functional groups, as desired. Examples of suitable isocyanates can be any of the polyisocyanates discussed above. In some non-limiting embodiments, the polyisocyanate is one or more aliphatic polyisocyanates. In some non-limiting embodiments, the polyisocyanate is 4,4′-methylene-bis-(cyclohexyl isocyanate) (such as DESMODUR W).
The polyol shown in Step 1 can be a diol (m=2), triol (m=3) or higher hydroxyl functional material (m=4 or more) as described above in which R′ is any linking group, such as aliphatic, cycloaliphatic, aromatic, heterocycle, etc. as described in detail above with respect to the polyols. Examples of suitable polyols can be any of the polyols discussed above. In some non-limiting embodiments, the polyol can be trimethylolpropane and butanediol and/or pentanediol. In other non-limiting embodiments, the polyol can be one or more polycarbonate polyols, for example about 0.01 to about 0.5 equivalent of polycarbonate polyols. Optionally, one or more catalysts such as are described above can be used to facilitate the reaction. The polyisocyanate can be reacted with the polyol to form the isocyanate functional urethane prepolymer by charging the reactants into a kettle and adding about 10 ppm or more of catalyst, such as a tin, bismuth or zirconium catalyst. In some non-limiting embodiments, upon mixing, the components are maintained at a temperature of at least about 100° C., or at least about 105° C., or at least about 110° C. for at least about 10 minutes or at least about 20 minutes, prior to degassing and cure, as described herein. The mixture can be heated to a temperature of about 100° C. or about 110° C. for about 2 to about 4 hours until all of the hydroxyl functionality is reacted. FTIR spectroscopy can be used to determine the extent of reaction.
Urea linkages or units can be formed within the polyurethane matrix to the extent desired by reacting isocyanate functional groups of the isocyanate functional urethane prepolymer with water. As shown in Step 2 of the reaction scheme of Poly(ureaurethane) Synthesis B below, isocyanate functional groups are converted to carbamate functional groups by the reaction with water. In some non-limiting embodiments, the equivalent ratio of NCO:water ranges from about 1:0.05 to about 1:0.7, or about 1:0.05 to about 1:0.5, or about 1:0.05 to about 1:0.3.
Removal of carbon dioxide facilitates conversion of the carbamate groups into amine groups. Excess isocyanate is desirable to ensure essentially complete consumption of the water. Also, it is desirable to remove essentially all of the carbon dioxide generated to facilitate conversion to amine groups. To prevent the removal of water under vacuum, the reaction can be started at a temperature of about 25° C., then raised to a temperature of about 60° C. while applying vacuum to remove the carbon dioxide. After cessation of carbon dioxide formation, the reaction temperature can be increased to about 100° C. or about 110° C. for about 2 to about 4 hours.
As discussed above, certain amine curing agents (such as aliphatic amine curing agents) are highly reactive and impractical to use under normal production conditions. By forming the amine in situ as discussed above and shown in Step 2, amines can be generated in situ that normally are not practical to use under normal production conditions without formation of undesirable side products. Also, the rate of reaction can be more easily regulated. This reaction can be used for any type of polyisocyanate described above, but is especially useful for converting aliphatic polyisocyanates to amines as described above.
As shown in Step 3 below, the amine formed in situ reacts with another isocyanate to form a urea group. Use of excess polyisocyanate permits formation of an isocyanate functional ureaurethane prepolymer. The isocyanate functional ureaurethane prepolymer can be prepared by reacting a stoichiometric excess of the polyisocyanate with the amine under substantially anhydrous conditions at a temperature ranging from about 25° C. and about 150° C. or about 110° C. until the reaction between the isocyanate groups and the amine groups is substantially complete. The polyisocyanate and amine components are suitably reacted in such proportions that the ratio of number of isocyanate groups to the number of amine groups is in the range of about 1:0.05 to about 1:0.7, or within the range of about 1:0.05 to 1:03.
As shown in Step 4 of the reaction scheme of Poly(ureaurethane) Synthesis B below, the isocyanate functional ureaurethane prepolymer can be reacted with another portion of polyol and/or diol to form the poly(ureaurethane)s of the present invention. The polyol shown in Step 4 can be a diol, triol or higher hydroxyl functional material as described above in which R is any linking group, such as aliphatic, cycloaliphatic, aromatic, heterocycle, etc. as described in detail above with respect to the polyols. Examples of suitable polyols can be any of the polyols discussed above. In some non-limiting embodiments, the polyol can be trimethylolpropane and butanediol and/or pentanediol. Suitable amounts of polyols for reacting with the isocyanate functional ureaurethane prepolymer as polyisocyanate are discussed in detail above.
The isocyanate functional ureaurethane prepolymer can be reacted with the other portion of polyol and/or diol (n=2 or more) under substantially anhydrous conditions at a temperature ranging from about 120° C. to about 160° C. until the reaction between the isocyanate groups and the hydroxyl groups is substantially complete. In some non-limiting embodiments, upon mixing, the components are maintained at a temperature of at least about 100° C., or at least about 105° C., or at least about 110° C. for at least about 10 minutes or at least about 20 minutes, prior to degassing and cure, as described herein. The isocyanate functional ureaurethane prepolymer and polyol(s) and/or diol(s) components are suitably reacted in such proportions that the ratio of number of isocyanate groups to the number of hydroxyl groups is in the range of about 1.05:1 to about 1:1 In the poly(ureaurethane) of Group K, y can range from 1 to about 500 or higher, or about 1 to about 200.
The cure temperature depends upon the glass transition temperature of the final polymer. In some embodiments, for complete cure the cure temperature should be greater than the glass transition temperature. For example, the cure temperature can range from about 140° C. to about 180° C. or about 143° C. to about 180° C.







In some non-limiting embodiments, the present invention provides polyurethane materials comprising a first portion of crystalline polyurethane particles having self-orientation and bonded together to fix their orientation along a first crystallographic direction and a second portion of polyurethane crystalline particles having self-orientation and bonded together to fix their orientation along a second crystallographic direction, the first crystallographic direction being different from the second crystallographic direction, wherein said crystalline particles comprise at least about 30% of the total volume of the polyurethane material.
The particles interact with one another or with a substrate surface to align their crystallographic axes in one, two or three dimensions. As used herein, “align” or “aligned” with respect to the crystalline particles means that the particles of that crystalline portion are arranged in an array of generally fixed position and orientation. The preferred degree of alignment will depend on the intended application for the material. For purposes of alignment, it is desirable that the particles have uniform shapes with dominant planar surfaces in a suitable orientation, such as perpendicular to or parallel to, with respect to the desired direction of alignment.
In some non-limiting embodiments, the first portion of the crystalline particles is aligned in two dimensions. In some non-limiting embodiments, the first portion of the crystalline particles is aligned in three dimensions. In some embodiments, the crystalline particles are aligned along a distance ranging from about 1 nm to about 50 nm along any direction.
In some non-limiting embodiments, the second portion of the crystalline particles is aligned in two dimensions. In some non-limiting embodiments, the second portion of the crystalline particles is aligned in three dimensions.
The crystalline particles of the present invention have at least “Self-Aligning” morphologies. As used herein, “Self-Aligning” morphologies include any particles that are capable of self-organizing to form a polycrystalline structure wherein the single particles are aligned along at least one crystallographic direction into areas of higher density and order, for example like lamellae. Examples of crystal particle morphologies with Self-Aligning morphologies include cubic particles, hexagonal platelets, hexagonal fibers, rectangular platelets, rectangular particles, triangular platelets, square platelets, tetrahedral, cube, octahedron and mixtures thereof.
Self-Aligning morphologies may establish an orientation that could be up to about 10 degrees from the desired alignment direction, yet still sufficiently capture the desired properties. Thus, particles having such morphologies include particles that essentially have the desired morphology. For instance, for particles that are cubes, the particles need not be perfect cubes. The axes need not be at perfect 90 degree angles, nor exactly equal in length. Corners may also be cut off of the particles. Furthermore, “cube” or “cubic” is intended to refer to morphology, and is not intended to limit the particles to cubic crystal systems. Instead, single crystal particles that have orthorhombic, tetragonal or rhombohedral crystal structure may also be employed as cubes if they possess the defined cubic morphology. In other words, any essentially orthogonal single crystal particles in which the faces are essentially square, essentially rectangular, or both, that possess an essentially cubic morphology are considered cubes for purposes of the present invention.
The crystalline particles can be aligned in monolithic structures consisting of a single layer of crystals or multiple layers of crystals. The layer or layers are generally planar, although the layers can conform to curved surfaces or complex geometries depending on the shape of the supporting substrate material during formation and curing of the polyurethane.
The polycrystalline materials of the present invention are prepared by packing and aligning a plurality of single crystal particles into an aligned array to achieve one, two and three-dimensional alignment. In some non-limiting embodiments, the particles can self-assemble into arrays upon aging or heat treatment. In some non-limiting embodiments, to obtain a level of solid state diffusion sufficient to bind together adjacent particles, a temperature above about half of the melting temperature is required, which is most generally in the range of about 35° C. to about 100° C. The temperature range selected will depend upon the material being bonded, but can be readily determined by those of ordinary skill in the art without undue experimentation within the defined range. The preparation steps may be repeated to form a polycrystalline material having multiple layers of aligned particles. The resulting material is essentially a three-dimensional object with one, two, or three dimensional alignment of single crystal particles within.
In some non-limiting embodiments, the polyurethane material comprises a monolithic agglomerate of the first portion of the crystalline particles with low-angle grain boundaries therebetween bonded together by a polymer phase.
In some non-limiting embodiments, the polyurethane material comprises a monolithic agglomerate of the second portion of the crystalline particles with low-angle grain boundaries therebetween bonded together by a polymer phase.
In some non-limiting embodiments, the polyurethane material comprises a monolithic agglomerate of the first portion of the crystalline particles with low-angle grain boundaries and a generally amorphous phase therebetween.
In some non-limiting embodiments, the polyurethane material comprises a monolithic agglomerate of the second portion of the crystalline particles with low-angle grain boundaries and a generally amorphous phase therebetween.
In some non-limiting embodiments, the thickness of the first portion of crystalline particles is less than about 50 nanometers. In some non-limiting embodiments, the thickness of the second portion of crystalline particles is less than about 50 nanometers. The length and width, respectively, of the first portion can vary, for example about 4 nm by about 8 nm.
In some non-limiting embodiments, the thickness of the first portion of crystalline particles can range from about 10 nanometers to about 100 nanometers. In some non-limiting embodiments, the thickness of the second portion of crystalline particles can range from about 4 nanometers to about 50 nanometers. The length and width, respectively, of the second portion can vary, for example about 4 nm by about 8 nm.
In some non-limiting embodiments, the crystalline particles comprise at least about 30% of the total volume of the material. In other non-limiting embodiments, the crystalline particles comprise at least about 40%, or at least about 50%, or at least about 60%, or at least about 70%, or at least about 80%, or at least about 90% of the total volume of the material. The percentage of crystalline particles can be determined using DSC. For example, an article prepared from Formulation 2 as described below, aged at ambient conditions (about 25° C.) for about 7 months had a crystallinity of about 43% by volume.
In some non-limiting embodiments, the impact resistance of polyurethanes and poly(ureaurethane)s according to the present invention can be improved by aging or heat treatment.
In some non-limiting embodiments, the polyurethane material can be aged for at least about 3 days or at least about 2 weeks after formation. In some non-limiting embodiments, the polyurethane material can be aged for at least about 2 months after formation. In some non-limiting embodiments, the polyurethane material has been aged for at least about 7 months after formation.
In some non-limiting embodiments, upon mixing, the components are maintained at a temperature of at least about 100° C., or at least about 105° C., or at least about 110° C. for at least about 10 minutes or at least about 20 minutes, prior to degassing and cure, as discussed herein. In some non-limiting embodiments, the polyurethane material has been heated to a temperature of about 90° C. to about 150° C. or about 200° F. (about 93° C.) to about 290° F. (about 143° C.) for about 1 to about 24 hours after formation. In some non-limiting embodiments, the polyurethane is heated at a temperature sufficient to induce grain boundary mobility, so that the particles grow until impingement of adjacent crystal grain boundaries prevent further growth. The net result is a polycrystalline microstructure, the grains of which for all practical purposes are aligned in two or three dimensions so that it performs like a single crystal with respect to some desired property.
Impact resistance or flexibility can be measured using a variety of conventional methods known to those skilled in the art. The flexibility of the materials can be measured by the Gardner Impact Test using a Gardner Variable Impact Tester in accordance with ASTM-D 5420-04, which consists of a 40-inch (101.6 cm) aluminum tube in which an 8- or 16-lb (17.6- or 35.2-kg) weight is dropped from various heights onto a metal dart resting onto the substrate being tested (2 inch by 2 inch by 1⁄8 inch (5.1 cm by 5.1 cm by 0.3 cm) specimen size. In a non-limiting embodiment, the impact strength results of the Gardner Impact Test of at least about 65 in-lb (7.3 Joules) or from about 65 in-lb (7.3 Joules) to about 640 in-lb (72 joules).
In another embodiment, the impact resistance can be measured using the Dynatup Test in accordance with ASTM-D 3763-02, which consists of a high velocity test with a load cell which measures total energy absorption in the first microseconds of the impact. The impact strength can be measured in Joules. In a non-limiting embodiment, the substrate can have an impact strength of at least about 35 Joules or from about 35 to about 105 Joules.
In some non-limiting embodiments, the present invention provides polyurethane powder coating compositions. The powder coating compositions can be prepared from any of the polyurethanes or poly(ureaurethane)s discussed in detail herein.
In some non-limiting embodiments, the present invention provides methods of preparing a polyurethane powder coating composition comprising the steps of: reacting at least one polyisocyanate with at least one aliphatic polyol to form a generally solid, hydroxy functional prepolymer; melting the hydroxy functional prepolymer; melting at least one generally solid polyisocyanate to form a melted polyisocyanate; mixing the melted hydroxy functional prepolymer and melted polyisocyanate to form a mixture; and solidifying the mixture to form a generally solid powder coating composition.
The generally solid, hydroxy functional prepolymer can be prepared by reacting the polyisocyanate(s) with excess aliphatic polyol(s) and catalyst in amounts as described above and heating the prepolymer to a temperature of about 140° C. or about 150° C. to about 180° C. for about 1 to about 24 hours to facilitate essentially complete reaction of the components and formation of a generally solid prepolymer. The equivalent ratio of isocyanate functional groups to hydroxyl functional groups can range from about 1:0.9 to about 1:1.1, or about 1:1, or about 1.05:1 to about 0.95:1, or about 1:1.
The generally solid polyisocyanate can be melted by, for example, heating at a temperature of about 35° C. to about 150° C. for about 2 to about 24 hours to form the melted polyisocyanate. The melted hydroxy functional prepolymer and melted polyisocyanate can be mixed and solidified to form a generally homogeneous mixture suitable for forming a powder coating, as discussed below.
In other non-limiting embodiments, the present invention provides methods of preparing a polyurethane powder coating composition comprising the steps of: reacting at least one polyisocyanate with at least one aliphatic polyol to form a generally solid, hydroxy functional prepolymer; dissolving the hydroxy functional prepolymer in a first solvent to form a first solution; dissolving at least one generally solid polyisocyanate in a second solvent that is the same as or compatible with the first solvent to form a second solution; mixing the first and second solutions; and removing substantially all of the solvent to form a generally solid powder coating composition.
The generally solid, hydroxy functional prepolymer can be prepared by reacting the polyisocyanate(s) with excess aliphatic polyol(s) and catalyst in types and amounts as described above. The hydroxy functional prepolymer is dissolved in a first solvent to form a first solution. The solvent can be any solvent capable of dissolving the hydroxy functional prepolymer, such as a dipolar aprotic solvent, for example m-pyrole (N-methyl-2-pyrrolidone), N,N-dimethylformamide, N,N-dimethylacetamide, dimethyl sulfoxide (DMSO), methylene chloride, dichlorobutane, cyclohexanone, dimethyl formamide and/or acetonitrile solvent. The amount of solvent can range from about 20 to about 95 weight percent based upon weight of solids of the hydroxy functional prepolymer.
The generally solid polyisocyanate in a second solvent that is the same as or compatible with the first solvent to form a second solution. The solvent can be any solvent capable of dissolving the generally solid polyisocyanate, such as a dipolar aprotic solvent, for example m-pyrole (N-methyl-2-pyrrolidone), N,N-dimethylformamide, N,N-dimethylacetamide, dimethyl sulfoxide (DMSO), methylene chloride, dimethyl formamide and/or acetonitrile solvent. The amount of solvent can range from about 20 to about 95 weight percent based upon weight of the solids of polyisocyanate.
The first and second solutions are mixed and substantially all of the solvent is removed, for example by vacuum in an oven, to form a generally solid powder suitable for use as a coating composition.
The solid or powder produced by the above methods can be milled or micronized, if desired.
Curable powder coating compositions useful in the present invention are typically prepared by first dry blending the polymer, e.g., polyurethane or poly(ureaurethane) polymer, the crosslinking agent (if present), the particles and additives, such as degassing agents, flow control agents and catalysts, in a blender, e.g., a Henshel blade blender. The blender is operated for a period of time sufficient to result in a homogenous dry blend of the materials charged thereto. The homogeneous dry blend is then melt blended in an extruder, e.g., a twin screw co-rotating extruder, operated within a temperature range sufficient to melt but not gel the components.
Optionally, curable powder coating compositions of the present invention may be melt blended in two or more steps. For example, a first melt blend is prepared in the absence of a cure catalyst. A second melt blend is prepared at a lower temperature, from a dry blend of the first melt blend and the cure catalyst. The melt blended curable powder coating composition is typically milled to an average particle size of from, for example, 15 to 30 microns.
Alternatively, the powder coating compositions of the present invention can be prepared by blending and extruding the ingredients as described above, but without the particles. The particles can be added as a post-additive to the formulation by simply mixing the particles into the milled powder coating composition, such as by mixing using a Henschel mixer. In some non-limiting embodiments, the powder coating composition is slurried in a liquid medium, such as water, which may be spray applied.
In some non-limiting embodiments, the polyurethane compositions of the present invention can further comprise one or more types of reinforcing materials. These reinforcing materials can be present in any physical form desired, for example as particles, including but not limited to nanoparticles, agglomerates, fibers, chopped fibers, mats, etc.
The reinforcing materials can be formed from materials selected from the group consisting of polymeric inorganic materials, nonpolymeric inorganic materials, polymeric organic materials, nonpolymeric organic materials, composites thereof and mixtures thereof that are chemically different from the polyurethane or poly(ureaurethane). As used herein, “chemically different” from the polyurethane or poly(ureaurethane) means that the reinforcing material has at least one different atom or has a different arrangement of atoms compared to the polyurethane or poly(ureaurethane).
As used herein, the term “polymeric inorganic material” means a polymeric material having a backbone repeat unit based on an element or elements other than carbon. See James Mark et al., Inorganic Polymers, Prentice Hall Polymer Science and Engineering Series, (1992) at page 5, incorporated by reference herein. Moreover, as used herein, the term “polymeric organic materials” means synthetic polymeric materials, semisynthetic polymeric materials and natural polymeric materials, all of which have a backbone repeat unit based on carbon.
An “organic material,” as used herein, means carbon-containing compounds wherein the carbon is typically bonded to itself and to hydrogen, and often to other elements as well, and excludes binary compounds such as the carbon oxides, the carbides, carbon disulfide, etc.; such ternary compounds as the metallic cyanides, metallic carbonyls, phosgene, carbonyl sulfide, etc.; and carbon-containing ionic compounds such as metallic carbonates, for example calcium carbonate and sodium carbonate. See R. Lewis, Sr., Hawley's Condensed Chemical Dictionary, (12th Ed. 1993) at pages 761-762, and M. Silberberg, Chemistry The Molecular Nature of Matter and Change (1996) at page 586, which are incorporated by reference herein.
As used herein, the term “inorganic material” means any material that is not an organic material.
As used herein, the term “composite material” means a combination of two or more differing materials. For example a composite particle can be formed from a primary material that is coated, clad or encapsulated with one or more secondary materials to form a composite particle that has a softer surface. In some non-limiting embodiments, particles formed from composite materials can be formed from a primary material that is coated, clad or encapsulated with a different form of the primary material. For more information on particles useful in the present invention, see G. Wypych, Handbook of Fillers, 2nd Ed. (1999) at pages 15-202, incorporated by reference herein.
The reinforcing materials suitable for use in the compositions of the invention can comprise inorganic elements or compounds known in the art. Suitable nonpolymeric, inorganic reinforcing materials can be formed from ceramic materials, metallic materials, and mixtures of any of the foregoing. Nonpolymeric, inorganic materials useful in forming the reinforcing materials of the present invention comprise inorganic materials selected from the group consisting of graphite, metals, oxides, carbides, nitrides, borides, sulfides, silicates, carbonates, sulfates, and hydroxides. Suitable ceramic materials comprise metal oxides, metal nitrides, metal carbides, metal sulfides, metal silicates, metal borides, metal carbonates, and mixtures of any of the foregoing. Non-limiting examples of suitable metals include molybdenum, platinum, palladium, nickel, aluminum, copper, gold, iron, silver, alloys, and mixtures of any of the foregoing. Non-limiting examples of metal nitrides are, for example, boron nitride; non-limiting examples of metal oxides are, for example, zinc oxide; non-limiting examples of suitable metal sulfides are, for example, molybdenum disulfide, tantalum disulfide, tungsten disulfide, and zinc sulfide; non-limiting examples of metal silicates are, for example aluminum silicates and magnesium silicates such as vermiculite. In some non-limiting embodiments, the reinforcing material is essentially free of (less than 5 weight percent or less than 1 weight percent) or free of fillers such as sodium carbonate, calcium carbonate, silicates, alginates, carbon black, and metal oxides such as titanium dioxide, silica, and zinc oxide.
In some non-limiting embodiments, the reinforcing materials can comprise a core of essentially a single inorganic oxide such as silica in colloidal, fumed, or amorphous form, alumina or colloidal alumina, titanium dioxide, cesium oxide, yttrium oxide, colloidal yttria, zirconia, e.g., colloidal or amorphous zirconia, and mixtures of any of the foregoing; or an inorganic oxide of one type upon which is deposited an organic oxide of another type. In some non-limiting embodiments, the reinforcing materials should not seriously interfere with the optical properties of the cured composition. As used herein, “transparent” means that the cured coating has a BYK Haze index of less than 50 as measured using a BYK/Haze Gloss instrument.
The composition can comprise precursors suitable for forming silica particles in situ by a sol-gel process. The composition according to the present invention can comprise alkoxy silanes which can be hydrolyzed to form silica particles in situ. For example tetraethylortho silicate can be hydrolyzed with an acid such as hydrochloric acid and condensed to form silica particles. Other useful particles include surface-modified silicas such as are described in U.S. Pat. No. 5,853,809 at column 6, line 51 to column 8, line 43, incorporated herein by reference.
Sols, such as an organosols, of reinforcement particles can be used in the present invention. These sols can be of a wide variety of small-particle, colloidal silicas having an average particle size in ranges such as are described below. The colloidal silicas can be surface modified during or after the particles are initially formed. These surface modified silicas may contain on their surface chemically bonded carbon-containing moieties, as well as such groups as anhydrous SiO2 groups and SiOH groups, various ionic groups physically associated or chemically bonded within the surface of the silica, adsorbed organic groups, or combinations of any of the foregoing, depending on the characteristics of the particular silica desired. Such surface modified silicas are described in detail in U.S. Pat. No. 4,680,204, incorporated by reference herein. Such small particle colloidal silicas are readily available, are essentially colorless and have refractive indices which permit their inclusion in compositions that, without additional pigments or components known in the art to color and/or decrease the transparency of such compositions, result in colorless, transparent compositions or coatings.
Other suitable non-limiting examples of reinforcing materials include colloidal silicas, such as those commercially available from Nissan Chemical Company under the trademark ORGANOSILICASOLSTM such as ORGANOSILICASOLTM MT-ST, and from Clariant Corporation as HIGHLINKTM; colloidal aluminas, such as those commercially available from Nalco Chemical under the trademark NALCO 8676®; and colloidal zirconias, such as those commercially available from Nissan Chemical Company under the trademark HIT-32M®.
In some non-limiting embodiments of the present invention, the reinforcing material is a nanostructure. As used herein, the term “nanostructure” refers to a three dimensional object wherein the length of the longest dimension ranges from 1 nm to 1000 nm, for example, from 1 nm to 500 nm, or from 1 nm to 100 nm, or from 1 to 40 nm.
Nanostructural reinforcing materials can be incorporated into the matrix of a polymer by dispersing pre-made nanostructures, such as for example nanoclays, into the polymer solution. Alternatively or additionally, nanostructural reinforcement materials can be incorporated into the polymer matrix by forming the nanostructures in situ. For example, the nanostructural reinforcement materials can be formed in situ by mixing a precursor solution for the polyurethane or poly(ureaurethane) with a precursor for the nanostructures to form a mixture, forming nanostructures in the matrix of the polymer from the precursor of the nanostructures, and forming a polymer from the precursor solution of the polymer.
As used herein, the phrase “precursor solution for the polyurethane or poly(ureaurethane)” refers to any material that can be used as a starting material to form the polyurethane or poly(ureaurethane), as discussed above. For example, if the desired end product is an aliphatic polyurethane, suitable precursors for the polymer include, but are not limited to, 1,4-butanediol, trimethylolpropane, and bis(4-isocyanatocyclohexyl)methane and thiodiethanol.
As used herein, the phrase “precursor for the nanostructures” refers to any material that can be used as a starting material to form the nanostructures.
In some non-limiting embodiments of the invention, a solvent such as water, ethanol, iso-propanol, butanol, etc. is added to the mixture.
The nanostructures are formed while the viscosity of the polymer is low so that the nanostructures can incorporate themselves into the matrix of the polymer. The formation of the nanostructures can be initiated using various techniques. In a non-limiting embodiment of the invention, the nanostructures are formed by adjusting the pH of the mixture. An acid or base, such as ammonia, can be used to adjust the pH of the solution. Depending on the exact precursor solution of the polymer and the exact precursor for the nanostructures, there is an optimum pH range in which the nanostructures will form. One of ordinary skill in the art would know what the optimum pH range is based on both precursors.
In another non-limiting embodiment, the mixture can be heated to initiate the formation of the nanoparticles. The mixture can be heated to any temperature provided the mixture is not heated to a temperature above that at which the precursor solution would break down. For example, a precursor solution comprising polyurethane or poly(ureaurethane) cannot be heated above 200° C. because that is the temperature at which polyurethane or poly(ureaurethane) begins to decompose. Similarly to the pH range, the optimum temperature range at which the particles will form depends on the exact precursor solution of the polyurethane or poly(ureaurethane) and the exact precursor for the nanostructures. One of ordinary skill in the art would know what the optimum temperature range is based on both precursors. Generally, the higher the temperature to which the mixture is heated and/or the longer the mixture is heated, the larger the size of the nanostructures that will be formed.
In yet another non-limiting embodiment of the invention, forming the nanostructures is accomplished by heating the mixture after the pH of the mixture is adjusted. In a further non-limiting embodiment of the invention, forming the nanostructures is accomplished by heating the mixture and then adjusting the pH of the mixture.
In various other non-limiting embodiments of the invention, the nanostructures can be formed by using one or more of the following: increasing the pressure on the mixture; by changing the concentration of the precursor solution for the polyurethane or poly(ureaurethane); by using an initiator for nanostructure formation; and by seeding (adding no greater than 5% of the desired nanostructure material based on the projected weight of the formed nanostructures as is well known in the art).
The formed nanostructures are charged species. If the pH of the solution was adjusted to cause the formation of the nanostructures, the charge is a result of the pH adjustment. If no pH adjustment was performed during the nanostructure formation step, a polymeric stabilizer such as, but not limited to, sodium polymethacrylate in water and ammonium polymethacrylate in water, which are both commercially available as Darvan® 7 and as Darvan® C, respectively, from R.T. Vanderbilt Company, Inc. in Norwalk, Conn. can be added to the solution to create the charge.
The third step involves forming the polyurethane or poly(ureaurethane) from a mixture including the precursor solution of the polyurethane or poly(ureaurethane). The formation of the polyurethane or poly(ureaurethane) can be initiated using various techniques (as discussed in detail above) based on the precursor solution of the polyurethane or poly(ureaurethane) and the precursor for the nanostructures.
In another embodiment of the present invention, the second and third steps described above are switched.
The method of making polymers having nanostructures incorporated into the matrix of the polymer according to the present invention is referred to as an “in-situ” process. This means the nanostructures are formed during the same process that produces the polymer as opposed to pre-formed nanostructures being dispersed into a polymer solution.
During some methods of the present invention, ions (cations and/or anions) can form in the mixture. The formed ions and other process variables, such as the pressure of the system in which the mixture is held, can affect the final polymer. For example, the amount of nanostructure formation and the morphology of the nanostructures will vary depending on the types and amount of ions present in the solution.
In the polymer matrix, the nanostructures typically continually approach one another and collide because they possess kinetic energy. Under normal circumstances, some of the nanostructures would become bound together and agglomerate due to various forces such as Van der Waals forces. As discussed above, agglomeration is not desirable because the nanostructures can effectively become regular sized particles and the desired effect of incorporating the nanostructures is reduced.
However, the methods described above can produce polymers having nanostructures in the matrix of the polymer that do not agglomerate to the extent that the performance of the polymer is compromised, for example to improve the thermal stability of the polymer and/or to decrease the chemical activity of the polymer. The nanostructures do not agglomerate because they are stabilized. The stabilization can occur via electrostatic stabilization and/or steric stabilization.
Because the nanostructures in the polymer matrix are similarly charged species, they repel each other. This prevents the nanostructures from coming so close together that they agglomerate. This phenomenon is referred to as electrostatic stabilization.
Because the nanostructures are surrounded by polymer precursor solution when they are formed, the nanostructures lose a degree of freedom which they would otherwise possess as the nanostructures approach each other. This loss of freedom is expressed, in thermodynamic terms, as a reduction in entropy, which provides the necessary barrier to hinder agglomeration. This phenomenon is referred to as steric stabilization. The same principle applies when the method involves forming the polymer before forming the nanostructures.
The concentration of the nanostructures in the polymer matrix can range from 0.1% to 90%, for example from 3% to 85% or from 15% to 80% based on total volume. The nanostructures in the polymer matrix can have the following shapes: spherical, polyhedral-like cubic, triangular, pentagonal, diamond shaped, needle shaped, rod shaped, disc shaped etc. The nanostructures in the polymer matrix can have an aspect ratio of 1:1 to 1:1,000, for example 1:1 to 1:100.
Non-limiting examples of suitable nanostructure materials include titania, alumina, indium tin oxide (ITO), antimony tin oxide (ATO), monobutyl tin tri-chloride, indium acetate, and antimony tri-chloride nanostructures incorporated into the polymer matrix is formed. Suitable precursors for titania nanostructures include, but are not limited to, titanium iso-propoxide, titanium (IV) chloride and potassium titanyl oxalate. Suitable precursors for alumina nanostructures include, but are not limited to, aluminum iso-propoxide, aluminum tri-tert-butoxide, aluminum tri-sec-butoxide, aluminum triethoxide, and aluminum pentanedionate. Suitable precursors for zirconia nanostructures include, but are not limited to, zirconium iso-propoxide, zirconium tert-butoxide, zirconium butoxide, zirconium ethoxide, zirconium 2,4-pentanedionate, and zirconium trifluoropentane-dionate.
In the first step, a precursor solution for polyurethane or poly(ureaurethane) is mixed with a precursor for the nanostructures.
In the second step, nanostructures are formed from the precursor of the nanostructures in the polymer matrix. The nanostructure formation can be caused by adjusting the pH of the mixture followed by heating. The pH can be adjusted by introducing an agent, such as ammonia, into the mixture. For ITO nanostructures in a urethane or ureaurethane aqueous solution, the nanostructures begin to form at a pH>8. After the pH is adjusted, the mixture is heated to a temperature of up to 100° C. Heating the solution to a temperature greater than 100° C. may cause the polymer matrix to decompose. As discussed above, heating the mixture for a longer time period can increase the size of the nanostructures.
In the third step, the precursor solution for the polymer is converted to the polymer, as discussed above for forming the polyurethane and poly(ureaurethane).
In a non-limiting embodiment of the invention, the final reinforced polymer is used as an interlayer in a laminated glass transparency for automotive and architectural applications. As is well known in the art, a laminated glass transparency can be manufactured by interposing an interlayer between at least two transparent glass sheets.
In this particular embodiment of the invention, a laminated glass transparency for an automotive and architectural applications embodiment, it is important that the nanostructures do not agglomerate. If the nanostructures were to agglomerate and effectively achieve a diameter of greater than 200 nm, the nanostructures would scatter visible light rays to such an extent that transmittance through the interlayer would be insufficient for the application. A polymer with nanostructures having an acceptable size for the application, can be determined using a “haze value”. The haze value is associated with the degree to which transparency is prevented. The larger the nanostructures present in the polymer matrix, the higher the haze value. According to the present invention, laminated glass for automotive and architectural applications has a haze value of less than or equal to about 1%, for example, less than or equal to about 0.3%, or less than or equal to about 0.2%, as measured using a Hazeguard System from BYK-Gardner in Columbia, Md.
In the embodiment where a polyurethane or poly(ureaurethane) is being formed having titania nanostructures incorporated into the polymer matrix, the first step can comprise mixing titanium iso-propoxide with a 1-10 wt % H2O2 solution and suitable polyurethane or poly(ureaurethane) precursors as discussed above. The H2O2 acts as an initiator for titania nanostructures; particularly, titania nanostructures in the anatase form. Optionally, polymers such as polyoxyethylene (20) sorbitan monooleate commercially available as Tween® 80 from ICI Ltd. (Bridgewater, N.J.) can be added to the solution to help stabilize the titania nanostructures.
In the second step, the titania nanostructures are formed from the precursor by heating the mixture to a temperature of up to 100° C.
In the third step, the precursor solution for the polymer is converted into polyurethane or poly(ureaurethane) as discussed in detail above.
In a non-limiting embodiment of the invention, polyurethane or poly(ureaurethane) having titania, alumina, or zirconia nanostructures incorporated into the matrix of the polymer can be used as an optical lens. A polymer with nanostructures having an acceptable size for optical lens applications can be determined using a “haze value”. According to the present invention, an optical lens has a haze value of less than or equal to 0.5%, for example less than or equal to 0.2%, as measured using a Hazeguard System from BYK Gardner.
In a non-limiting embodiment of the invention, a polyurethane having ITO or ATO nanostructures incorporated into the polymer matrix is formed. Such a polymer can be formed in the following manner. In the first step, a precursor solution for the trimethylol propane, methylene bis(4-cyclohexylisocyanate) and thiodiethanol is mixed with a precursor for ITO or ATO nanostructures.
A suitable precursor solution for the polyurethane is trimethylol propane, methylene bis(4-cyclohexylisocyanate), thiodiethanol and 1,4-butanediol. Suitable precursors for ITO nanostructures include monobutyl tin tri-chloride and indium acetate. A suitable precursor for ATO nanostructures is antimony tri-chloride.
In the second step, ITO or ATO nanostructures are formed from the precursor. The nanostructure formation can be caused by adjusting the pH of the solution by introducing an agent, such as ammonia, into the mixture followed by heating the mixture. For ITO nanostructures, the ITO nanostructures start to form at pH>8. After the pH is adjusted, the mixture is heated to a temperature of up to 100° C. As discussed above, heating the mixture for a longer time period can increase the size of the nanostructures.
In the third step, the 1,4-butanediol is mixed into trimethylol propane, methylene bis(4-cyclohexylisocyanate), thiodiethanol as is well known in the art. For example, 1,4 butanediol, thiodiethanol, trimethylol propane (TMP), and DESMODUR® W can all be mixed into a vessel and heated to 180° F. The mixture is mixed under vacuum for approximately 15 minutes, and then a tin catalyst, such as dibutyltindilaurate or bismuth carboxylate, is added to the mixture in a 25 ppm concentration. The mixture is then cast into a glass mold and cured for at least 20 hours at 250° F. (121° C.) to form the polyurethane.
In a non-limiting embodiment, trimethylol propane, methylene bis(4-cyclohexylisocyanate), thiodiethanol having ITO or ATO nanostructures incorporated into the polymer matrix is used to form an anti-static coating for aircraft windows. The polymer with the nanostructures has an elastic modulus that is greater than that of the standard trimethylol propane, methylene bis(4-cyclohexylisocyanate)thiodiethanol without ITO/ATO nanoparticles.
In other non-limiting embodiments, the reinforcement material is a nanostructural reinforcement material formed in situ by swelling the polyurethane in a solvent comprising a precursor for the nanostructures, and forming nanostructures in the matrix of the polyurethane from the precursor of the nanostructures. Non-limiting examples of suitable solvents for mild swelling of the polymer include methanol, propylene glycol methyl ether such as DOWANOL PM (commercially available from Dow Chemical Co. of Midland, Mich.), diacetone alcohol, 2-propanol, 1-propanol and acetylpropanol.
A polymer with nanostructures having an acceptable size for the aircraft window application can be determined using a “haze value”. According to the present invention, a laminated aircraft window has a haze value of less than or equal to about 1%, for example less than or equal to about 0.5%, as measured using a Hazeguard System from BYK Gardner.
In some non-limiting embodiments of the present invention, the reinforcing materials have a hardness value greater than the hardness value of materials that can abrade a polymeric coating or a polymeric substrate. Examples of materials that can abrade the polymeric coating or polymeric substrate include, but are not limited to, dirt, sand, rocks, glass, carwash brushes, and the like. The hardness values of the particles and the materials that can abrade the polymeric coating or polymeric substrate can be determined by any conventional hardness measurement method, such as Vickers or Brinell hardness, or can be determined according to the original Mohs' hardness scale which indicates the relative scratch resistance of the surface of a material on a scale of one to ten. The Mohs' hardness values of several nonlimiting examples of particles formed from inorganic materials suitable for use in the present invention are given in Table A below.









TABLE A






Particle material
Mohs' hardness (original scale)








Boron nitride
21



Graphite
0.5-12  



Molybdenum disulfide
13



Talc
  1-1.54



Mica
2.8-3.25



Kaolinite
2.0-2.56



Gypsum
1.6-27  



Calcite (calcium carbonate)
38



Calcium fluoride
49



Zinc oxide
  4.510



Aluminum
  2.511



Copper
2.5-312 



Iron
 4-513



Gold
2.5-314 



Nickel
 515



Palladium
  4.816



Platinum
  4.317



Silver
2.5-418 



Zinc sulfide
3.5-419 





1K. Ludema, Friction, Wear, Lubrication, (1996) at page 27, incorporated by reference herein.


2R. Weast (Ed.), Handbook of Chemistry and Physics, CRC Press (1975) at page F-22.


3R. Lewis, Sr., Hawley's Condensed Chemical Dictionary, (12th Ed. 1993) at page 793, incorporated by reference herein.


4Hawley's Condensed Chemical Dictionary, (12th Ed. 1993) at page 1113, incorporated by reference herein.


5Hawley's Condensed Chemical Dictionary, (12th Ed. 1993) at page 784, incorporated by reference herein.


6Handbook of Chemistry and Physics at page F-22.


7Handbook of Chemistry and Physics at page F-22.


8Friction, Wear, Lubrication at page 27.


9Friction, Wear, Lubrication at page 27.


10Friction, Wear, Lubrication at page 27.


11Friction, Wear, Lubrication at page 27.


12Handbook of Chemistry and Physics at page F-22.


13Handbook of Chemistry and Physics at page F-22.


14Handbook of Chemistry and Physics at page F-22.


15Handbook of Chemistry and Physics at page F-22.


16Handbook of Chemistry and Physics at page F-22.


17Handbook of Chemistry and Physics at page F-22.


18Handbook of Chemistry and Physics at page F-22.


19R. Weast (Ed.), Handbook of Chemistry Physics, CRC Press (71.sup.st Ed. 1990) at page 4-158






In some non-limiting embodiments, the reinforcing material can be formed from a primary material that is coated, clad or encapsulated with one or more secondary materials to form a composite material that has a harder surface. In other non-limiting embodiments, reinforcement particles can be formed from a primary material that is coated, clad or encapsulated with a differing form of the primary material to form a composite material that has a harder surface.
In some non-limiting examples, inorganic particles formed from an inorganic material such as silicon carbide or aluminum nitride can be provided with a silica, carbonate or nanoclay coating to form a useful composite particle. In other nonlimiting examples, a silane coupling agent with alkyl side chains can interact with the surface of an inorganic particle formed from an inorganic oxide to provide a useful composite particle having a “softer” surface. Other examples include cladding, encapsulating or coating particles formed from nonpolymeric or polymeric materials with differing nonpolymeric or polymeric materials. One non-limiting example of such composite particles is DUALITETM, which is a synthetic polymeric particle coated with calcium carbonate that is commercially available from Pierce and Stevens Corporation of Buffalo, N.Y.
In some non-limiting embodiments, the particles are formed from solid lubricant materials. As used herein, the term “solid lubricant” means any solid used between two surfaces to provide protection from damage during relative movement and/or to reduce friction and wear. In some non-limiting embodiments, the solid lubricants are inorganic solid lubricants. As used herein, “inorganic solid lubricant” means that the solid lubricants have a characteristic crystalline habit which causes them to shear into thin, flat plates which readily slide over one another and thus produce an antifriction lubricating effect. See R. Lewis, Sr., Hawley's Condensed Chemical Dictionary, (12th Ed. 1993) at page 712, incorporated by reference herein. Friction is the resistance to sliding one solid over another. F. Clauss, Solid Lubricants and Self-Lubricating Solids (1972) at page 1, incorporated by reference herein.
In some non-limiting embodiments, the particles have a lamellar structure. Particles having a lamellar structure are composed of sheets or plates of atoms in hexagonal array, with strong bonding within the sheet and weak van der Waals bonding between sheets, providing low shear strength between sheets. A non-limiting example of a lamellar structure is a hexagonal crystal structure. Inorganic solid particles having a lamellar fullerene (i.e., buckyball) structure can also be useful in the present invention.
Non-limiting examples of suitable materials having a lamellar structure that are useful in forming the particles of the present invention include boron nitride, graphite, metal dichalcogenides, mica, talc, gypsum, kaolinite, calcite, cadmium iodide, silver sulfide, and mixtures of any of the foregoing. Suitable metal dichalcogenides include molybdenum disulfide, molybdenum diselenide, tantalum disulfide, tantalum diselenide, tungsten disulfide, tungsten diselenide, and mixtures of any of the foregoing.
In some non-limiting embodiments, the reinforcing material can be glass fiber strands. The glass fiber strands are formed from glass filaments, a class of filaments generally accepted to be based upon oxide compositions such as silicates selectively modified with other oxide and non-oxide compositions. Useful glass filaments can be formed from any type of fiberizable glass composition known to those skilled in the art, and include those prepared from fiberizable glass compositions such as “E-glass”, “A-glass”, “C-glass”, “D-glass”, “R-glass”, “S-glass”, and E-glass derivatives that are fluorine-free and/or boron-free. As used herein, the term “fiberizable” means a material capable of being formed into a generally continuous filament, fiber, strand or yarn. As used herein, “E-glass derivatives” means glass compositions that include minor amounts of fluorine and/or boron or can be fluorine-free and/or boron-free. Furthermore, as used herein, “minor amounts of fluorine” means less than 0.5 weight percent fluorine, or less than 0.1 weight percent fluorine, and “minor amounts of boron” means less than 5 weight percent boron, or less than 2 weight percent boron. Basalt and mineral wool are examples of other fiberizable glass materials useful in the present invention. Non-limiting examples of suitable non-glass fiberizable inorganic materials include ceramic materials such as silicon carbide, carbon, quartz, graphite, mullite, aluminum oxide and piezoelectric ceramic materials. In some non-limiting embodiments, the glass filaments are formed from E-glass. Such compositions and methods of making glass filaments therefrom are well known to those skilled in the art, such glass compositions and fiberization methods are disclosed in K. Loewenstein, The Manufacturing Technology of Continuous Glass Fibres, (3d Ed. 1993) at pages 30-44, 47-60, 115-122 and 126-135, incorporated by reference herein.
The glass fibers can have a nominal filament diameter ranging from about 5.0 to about 30.0 micrometers (corresponding to a filament designation of D through Y). Typically, the glass fiber strands have a strand coating composition which is compatible with the composition applied to at least a portion of surfaces of the glass fiber strands, such as an essentially dried residue. The glass fiber strand reinforcements can be used in chopped form, generally continuous strands, mats, etc.
The particles also can be hollow particles formed from materials selected from polymeric and nonpolymeric inorganic materials, polymeric and nonpolymeric organic materials, composite materials, and mixtures of any of the foregoing. Non-limiting examples of suitable materials from which the hollow particles can be formed are described above. In some embodiments, the hollow particles are hollow glass spheres.
In some non-limiting embodiments, the reinforcing materials can be formed from nonpolymeric, organic materials. Nonlimiting examples of nonpolymeric, organic materials useful in the present invention include, but are not limited to, stearates (such as zinc stearate and aluminum stearate), diamond, carbon black, and stearamide.
In some non-limiting embodiments, the particles can be formed from inorganic polymeric materials. Nonlimiting examples of useful inorganic polymeric materials include polyphosphazenes, polysilanes, polysiloxane, polygeremanes, polymeric sulfur, polymeric selenium, silicones, and mixtures of any of the foregoing. A non-limiting example of a particle formed from an inorganic polymeric material suitable for use in the present invention is TOSPEARL1, which is a particle formed from cross-linked siloxanes and is commercially available from Toshiba Silicones Company, Ltd. of Japan. 1 See R. J. Perry “Applications for Cross-Linked Siloxane Particles” Chemtech. February 1999 at pp. 39-44.
The particles can be formed from synthetic, organic polymeric materials that are chemically different from the polyurethane or poly(ureaurethane). Nonlimiting examples of suitable organic polymeric materials include, but are not limited to, thermoset materials and thermoplastic materials. Nonlimiting examples of suitable thermoplastic materials include thermoplastic polyesters such as polyethylene terephthalate, polybutylene terephthalate, and polyethylene naphthalate, polycarbonates, polyolefins such as polyethylene, polypropylene, and polyisobutene, acrylic polymers such as copolymers of styrene and an acrylic acid monomer, and polymers containing methacrylate, polyamides, thermoplastic polyurethanes, vinyl polymers, and mixtures of any of the foregoing.
In some non-limiting embodiments, the polymeric organic material is a (meth)acrylic polymer or copolymer comprising at least one functional group selected from the group consisting of silane groups, carboxyl groups, hydroxyl groups and amide groups. In some non-limiting embodiments, these (meth)acrylic polymer or copolymers can be present as nanofibers having a diameter up to about 5000 nm, such as about 5 to about 5000 nm, or less than the wavelength of visible light, for example 700 nanometers or less, such as about 50 to about 700 nanometers. The fibers may have a ribbon shape and, in this case, diameter is intended to mean the largest dimension of the fiber. Typically the width of the ribbon shaped fibers can be up to about 5000 nanometers, such as about 500 to about 5000 nm and the thickness up to about 200 nm, such as about 5 to about 200 nm. The fibers can be prepared by electrospinning a ceramic melt, a polymer melt or a polymer solution.
Suitable (meth)acrylic polymers can be made by addition polymerization of unsaturated polymerizable materials that contain silane groups, carboxyl groups, hydroxyl groups and amine or amide groups. Non-limiting examples of useful silane groups include groups that have the structure Si—Xn (wherein n is an integer having a value ranging from 1 to 3 and X is selected from chlorine, alkoxy esters, and/or acyloxy esters). Such groups hydrolyze in the presence of water including moisture in the air to form silanol groups that condense to form —Si—O—Si— groups. The (meth)acrylic polymer can contain hydroxyl functionality, for example by using a hydroxyl functional ethylenically unsaturated polymerizable monomer such as hydroxyalkyl esters of (meth)acrylic acids having from 2 to 4 carbon atoms in the hydroxyalkyl group. The (meth)acrylic polymer optionally contains nitrogen functionality introduced from nitrogen-containing ethylenically unsaturated monomers, such as amines, amides, ureas, imidazoles and pyrrolidones. Further discussion of such (meth)acrylic polymers and fiberizing methods are disclosed in U.S. patent application Ser. No. 11/610,755 entitled “Transparent Composite Articles” and U.S. patent application Ser. No. 11/610,651 entitled “Organic-Inorganic Polymer Composites and Their Preparation by Liquid Infusion”, each filed on Dec. 14, 2006, and incorporated by reference herein.
Non-limiting examples of suitable fiberizable organic materials include cotton, cellulose, natural rubber, flax, ramie, hemp, sisal and wool. Non-limiting examples of suitable fiberizable organic polymeric materials include those formed from polyamides (such as nylon and aramids), (such as KEVLARTM aramid fibers), thermoplastic polyesters (such as polyethylene terephthalate and polybutylene terephthalate), acrylics (such as polyacrylonitriles), polyolefins, polyurethanes and vinyl polymers (such as polyvinyl alcohol). Non-glass fiberizable materials useful in the present invention and methods for preparing and processing such fibers are discussed at length in the Encyclopedia of Polymer Science and Technology, Vol. 6 (1967) at pages 505-712, which is specifically incorporated by reference herein.
It is understood that blends or copolymers of any of the above materials and combinations of fibers formed from any of the above materials can be used in the present invention, if desired. Moreover, the term “strand” can encompass at least two different fibers made from differing fiberizable materials. As used herein, the term “fiberizable” means a material capable of being formed into a generally continuous filament, fiber, strand or yarn.
Suitable thermoplastic fibers can be formed by a variety of polymer extrusion and fiber formation methods, such as for example drawing, melt spinning, dry spinning, wet spinning and gap spinning. Such methods are well known to those skilled in the art and further discussion thereof is not believed to be necessary in view of the present disclosure. If additional information is needed, such methods are disclosed in Encyclopedia of Polymer Science and Technology, Vol. 6 at 507-508.
Non-limiting examples of useful polyamide fibers include nylon fibers such as nylon 6 (a polymer of caprolactam), nylon 6,6 (a condensation product of adipic acid and hexamethylenediamine), nylon 12 (which can be made from butadiene) and nylon 10, polyhexamethylene adipamide, polyamide-imides and aramids such as KEVLARTM, which is commercially available from E. I. duPont de Nemours, Inc. of Wilmington, Del.
Non-limiting examples of useful thermoplastic polyester fibers include those composed of polyethylene terephthalate and polybutylene terephthalate.
Non-limiting examples of useful fibers formed from acrylic polymers include polyacrylonitriles having at least about 35% by weight acrylonitrile units, or at least about 85% by weight, which can be copolymerized with other vinyl monomers such as vinyl acetate, vinyl chloride, styrene, vinylpyridine, acrylic esters or acrylamide. See Encyclopedia of Polymer Science and Technology, Vol. 6 at 559-561.
Non-limiting examples of useful polyolefin fibers are generally composed of at least 85% by weight of ethylene, propylene, or other olefins. See Encyclopedia of Polymer Science and Technology, Vol. 6 at 561-564.
Non-limiting examples of useful fibers formed from vinyl polymers can be formed from polyvinyl chloride, polyvinylidene chloride, polytetrafluoroethylene, and polyvinyl alcohol.
Further non-limiting examples of thermoplastic fiberizable materials believed to be useful in the present invention include fiberizable polyimides, polyether sulfones, polyphenyl sulfones, polyetherketones, polyphenylene oxides, polyphenylene sulfides and polyacetals.
It is understood that blends or copolymers of any of the above materials and combinations of fibers formed from any of the above materials can be used in the present invention, if desired. Also, the thermoplastic fibers can have an antistatic agent coated thereon.
Suitable reinforcing materials can include mats or fabrics comprised of any of the fibers discussed above. An increasingly popular process for forming composites is by compression molding or stamping a moldable sheet of a thermoplastic resin reinforced with fibers such as a glass fiber mat, often referred to as glass mat thermoplastics or “GMT”. These composite sheets can be used to form articles such as automobile components and housings for computers. An example of a commercially successful GMT sheet is the AZDEL® moldable composite sheet which is formed by extruding layers of polypropylene resin sheet with needled mats of continuous glass fiber strand. The AZDEL® composite sheet is commercially available from Azdel, Inc. of Shelby, N.C.
For reinforcing a resin matrix material, U.S. Pat. Nos. 3,664,909, 3,713,962 and 3,850,723 disclose fibrous mats of unstranded filaments which can be layered with reinforcing mats of fiber strands.
U.S. Pat. No. 4,847,140 discloses an insulation medium formed by needling a loose layer of inorganic fibers, such as glass, bonded together by a carrier web which is a blend of inorganic and organic fibers, with the carrier web comprising up to about 10% by weight organic fibers.
U.S. Pat. Nos. 4,948,661, 5,011,737, 5,071,608 and 5,098,624 disclose fiber reinforced thermoplastic molded products produced by intimately blending reinforcing glass fibers and thermoplastic fibers into a web and heating the web to the melting point of the thermoplastic fibers while applying pressure to the web to press the web into a consolidated structure.
A non-limiting example of a useful polypropylene spun-bonded fiber mat is commercially available from Fiberweb N.A., Inc. of Simpsonville, S.C.
Nonlimiting examples of suitable thermoset reinforcement materials include thermoset polyesters, vinyl esters, epoxy materials, phenolics, aminoplasts, thermoset polyurethanes, and mixtures of any of the foregoing. A specific, nonlimiting example of a synthetic polymeric particle formed from an epoxy material is an epoxy microgel particle.
The concentration of reinforcement particles present in the cured article or coating can be determined, if desired, by a variety of analysis techniques well known in the art, such as Transmission Electron Microscopy (“TEM”), Surface Scanning Electron Microscopy (“X-SEM”), Atomic Force Microscopy (“AFM”), and X-ray Photoelectron Spectroscopy.
In some non-limiting embodiments, the present invention is directed to cured compositions as previously described wherein the reinforcement particles have an average particle size of less than about 100 microns prior to incorporation into the composition, or less than about 50 microns prior to incorporation into the composition. In other non-limiting embodiments, the present invention is directed to cured compositions as previously described wherein the reinforcement particles have an average particle size ranging from about 1 to less than about 1000 nanometers prior to incorporation into the composition, or about 1 to about 100 nanometers prior to incorporation into the composition.
In other non-limiting embodiments, the present invention is directed to cured compositions as previously described wherein the particles have an average particle size ranging from about 5 to about 50 nanometers prior to incorporation into the composition, or about 5 to about 25 nanometers prior to incorporation into the composition.
In an embodiment where the average particle size of the particles is at least about one micron, the average particle size can be measured according to known laser scattering techniques. For example the average particle size of such particles is measured using a Horiba Model LA 900 laser diffraction particle size instrument, which uses a helium-neon laser with a wave length of 633 nm to measure the size of the particles and assumes the particle has a spherical shape, i.e., the “particle size” refers to the smallest sphere that will completely enclose the particle.
In an embodiment of the present invention wherein the size of the particles is less than or equal to one micron, the average particle size can be determined by visually examining an electron micrograph of a transmission electron microscopy (“TEM”) image, measuring the diameter of the particles in the image, and calculating the average particle size based on the magnification of the TEM image. One of ordinary skill in the art will understand how to prepare such a TEM image, and a description of one such method is disclosed in the examples set forth below. In one nonlimiting embodiment of the present invention, a TEM image with 105,000× magnification is produced, and a conversion factor is obtained by dividing the magnification by 1000. Upon visual inspection, the diameter of the particles is measured in millimeters, and the measurement is converted to nanometers using the conversion factor. The diameter of the particle refers to the smallest diameter sphere that will completely enclose the particle.
The shape (or morphology) of the reinforcing material can vary depending upon the specific embodiment of the present invention and its intended application. For example generally spherical morphologies (such as solid beads, microbeads, or hollow spheres), can be used, as well as particles that are cubic, platy, or acicular (elongated or fibrous). Additionally, the particles can have an internal structure that is hollow, porous or void free, or a combination of any of the foregoing, e.g., a hollow center with porous or solid walls. For more information on suitable particle characteristics see H. Katz et al. (Ed.), Handbook of Fillers and Plastics (1987) at pages 9-10, incorporated by reference herein.
It will be recognized by one skilled in the art that mixtures of one or more particles having different average particle sizes can be incorporated into the compositions in accordance with the present invention to impart the desired properties and characteristics to the compositions. For example particles of varying particle sizes can be used in the compositions according to the present invention.
In some non-limiting embodiments, the reinforcing material(s) are present in the composition in an amount ranging from about 0.01 to about 75 weight percent, or about 25 to about 50 weight percent, based on total weight of the components which form the composition.
Reinforcement particles can be present in a dispersion, suspension or emulsion in a carrier. Nonlimiting examples of suitable carriers include, but are not limited to, water, solvents, surfactants, or a mixture of any of the foregoing. Nonlimiting examples of suitable solvents include, but are not limited to, mineral oil, alcohols such as methanol or butanol, ketones such as methyl amyl ketone, aromatic hydrocarbons such as xylene, glycol ethers such as ethylene glycol monobutyl ether, esters, aliphatics, and mixtures of any of the foregoing.
Dispersion techniques such as grinding, milling, microfluidizing, ultrasounding, or any other dispersing techniques well known in the art of coatings or molded article formulation can be used. Alternatively, the particles can be dispersed by any other dispersion techniques known in the art. If desired, the particles in other than colloidal form can be post-added to an admixture of other composition components and dispersed therein using any dispersing techniques known in the art.
A further embodiment of the present invention is directed to a coated automobile substrate comprising an automobile substrate and a cured composition coated over at least a portion of the automobile substrate, wherein the cured composition is selected from any of the foregoing compositions. In yet another embodiment, the present invention is directed to a method of making a coated automobile substrate comprising providing an automobile substrate and applying over at least a portion of the automotive substrate a coating composition selected from any of the foregoing compositions. Again, the components used to form the cured compositions in these embodiments can be selected from the components discussed above, and additional components also can be selected from those recited above.
Suitable flexible elastomeric substrates can include any of the thermoplastic or thermoset synthetic materials well known in the art. Nonlimiting examples of suitable flexible elastomeric substrate materials include polyethylene, polypropylene, thermoplastic polyolefin (“TPO”), reaction injected molded polyurethane (“RIM”), and thermoplastic polyurethane (“TPU”).
Nonlimiting examples of thermoset materials useful as substrates for coating with compositions of the present invention include polyesters, epoxides, phenolics, polyurethanes such as “RIM” thermoset materials, and mixtures of any of the foregoing. Nonlimiting examples of suitable thermoplastic materials include thermoplastic polyolefins such as polyethylene, polypropylene, polyamides such as nylon, thermoplastic polyurethanes, thermoplastic polyesters, acrylic polymers, vinyl polymers, polycarbonates, acrylonitrile-butadiene-styrene (“ABS”) copolymers, ethylene propylene diene terpolymer (“EPDM”) rubber, copolymers, and mixtures of any of the foregoing.
Nonlimiting examples of suitable metal substrates useful as substrates for coatings with compositions of the present invention include ferrous metals (e.g., iron, steel, and alloys thereof), nonferrous metals (e.g., aluminum, zinc, magnesium, and alloys thereof), and mixtures of any of the foregoing. In the particular use of automobile components, the substrate can be formed from cold rolled steel, electrogalvanized steel such as hot dip electrogalvanized steel, electrogalvanized iron-zinc steel, aluminum, and magnesium.
When the substrates are used as components to fabricate automotive vehicles (including, but not limited to, automobiles, trucks and tractors) they can have any shape, and can be selected from the metallic and flexible substrates described above. Typical shapes of automotive body components can include bodies (frames), hoods, doors, fenders, mirror housings, bumpers, and trim for automotive vehicles.
In embodiments of the present invention directed to automotive applications, the cured compositions can be, for example, the electrodeposition coating, the primer coating, the basecoat and/or the topcoat. Suitable topcoats include monocoats and basecoat/clearcoat composites. Monocoats are formed from one or more layers of a colored coating composition.
In some non-limiting embodiments, the polyurethanes and poly(ureaurethane)s can be reinforced with fiberglass to form a composite article, such as for example a windmill blade, blast-resistant panels, bullet resistant panels and radomes.
In some non-limiting embodiments, the polyurethanes and poly(ureaurethane)s can be useful as one or more layers in a multilayered article or assembly. If desired, the layers within the multilayered article can be laminated by heat and/or pressure, bonded by one or more adhesive materials or one or more layers in between having adhering properties, have one or more interlayers in between layers, or merely placed adjacent to another layer, for example.
In some non-limiting embodiments, the polymer is cut while warm, granulated, extruded and/or milled and calendered to sheets and assembled into a multilayered article, assembly or laminate and aged for several days, a week, or longer at ambient temperature (about 25° C.).
In some non-limiting embodiments, the present invention provides articles or assemblies having multiple layers of polyurethanes and/or poly(ureaurethanes) of the present invention. The thickness of each layer and overall thickness of the article or assembly can vary as desired. Non-limiting examples of suitable thicknesses of the layers and articles/assemblies are discussed below. The layers can be laminated and/or adhered together, if desired.
In some non-limiting embodiments, the present invention provides multilayered articles, assemblies or laminates comprising: (a) at least one layer of the polyurethane(s) or poly(ureaurethane)s of the present invention as discussed herein; and (b) at least one layer of a substrate selected from the group consisting of paper, glass, ceramic, wood, masonry, textile, metal or organic polymeric material and combinations thereof. In some non-limiting embodiments, the layer (a) of polyurethane(s) or poly(ureaurethane)s of the present invention is chemically or physically different from the organic polymeric material of layer (b), i.e., it has at least one different atom, arrangement of atoms or configuration. In other embodiments, two or more layers of the same or similar polyurethane(s) or poly(ureaurethane)s of the present invention can be used.
In some non-limiting embodiments, the substrate is an optically clear polymerized organic material prepared from a thermoplastic polycarbonate resin, such as the carbonate-linked resin derived from bisphenol A and phosgene, which is sold under the trademark LEXAN® by GE Plastics of Pittsfield, Mass.; a polyester, such as the material sold under the trademark MYLAR by E.I. duPont de Nemours Co. of Wilmington, Del.; a poly(methyl methacrylate), such as the material sold under the trademark PLEXIGLAS by Altuglas International of Philadelphia, Pa.; polyhexylene-polycarbonate-based polyurethanes; polymerizates of a polyol(allyl carbonate) monomer, especially diethylene glycol bis(allyl carbonate), which monomer is sold under the trademark CR-39 by PPG Industries, Inc., and polymerizates of copolymers of a polyol (allyl carbonate), e.g., diethylene glycol bis(allyl carbonate), with other copolymerizable monomeric materials, such as copolymers with vinyl acetate, and copolymers with a polyurethane having terminal diacrylate functionality, as described in U.S. Pat. Nos. 4,360,653 and 4,994,208; and copolymers with aliphatic urethanes, the terminal portion of which contain allyl or acrylyl functional groups, as described in U.S. Pat. No. 5,200,483; poly(vinyl acetate), polyvinylbutyral, polyurethane, polymers of members of the group consisting of diethylene glycol dimethacrylate monomers, diisopropenyl benzene monomers, and ethoxylated trimethylol propane triacrylate monomers; cellulose acetate, cellulose propionate, cellulose butyrate, cellulose acetate butyrate, polystyrene and copolymers of styrene with methyl methacrylate, vinyl acetate and acrylonitrile. In some non-limiting embodiments, the article comprises at least one layer of polyurethane or polyureaurethane of the present invention and at least one layer of polycarbonate.
A non-limiting example of a suitable polyhexylene-polycarbonate-based polyurethane can be prepared as follows: a hydroxyl—terminated prepolymer is made from 0.2 equivalents of a 1000 molecular weight hexanediol—based carbonate diol (PC-1733 commercially available from Stahl), 0.8 equivalents of 1,5 pentanediol, and 1.0 equivalents of trimethylhexanediisocyanate. The components are heated to 180° F. (82° C.) and using 100 ppm of dibutyltin dilaurate as a catalyst. The prepolymer has an equivalent weight of 218 grams/equivalent. The trimeric hydroxyl terminated prepolymer is dissolved into cyclohexanone solvent and 1 equivalent of Desmodur 3390 (triisocyanurate trimer of hexanediisocyanate) is added as a crosslinker and mixed. The coating solution is 95% solids with a viscosity of 3000 centipoise. The solution can be flow-coated onto any bisphenol A polycarbonate such as Lexan and cured in an oven at 250° F. (121° C.) for 4 hours. The coating thickness can range from 2 to 5 mils thick and is elastomeric.
The number and thickness of the layers can vary as desired. For example, the thickness of a single layer can range from about 0.1 mm to about 60 cm, or about 2 mm to about 60 cm, or about 0.3 cm to about 2.5 cm. The number of layers can range from 2 to 10, or 2 to 4, as desired. The overall thickness of the multilayer article, assembly or laminate can range from about 2 mm to about 15 cm or more, or about 2 mm to about 5 cm. For ballistics applications, the overall thickness of the polyurethane or poly(ureaurethane) of the present invention can range from about 2 mm to about 15 cm or more, or about 2 mm to about 5 cm. Also, for ballistics applications suitable substrates for layering with the polyurethane(s) and/or poly(ureaurethane)s of the present invention include polyesters, polycarbonates, or polyether thermoplastic elastomers, for example. The layer(s) of polyurethane or poly(ureaurethane) of the present invention can be positioned on the outside of the laminate (facing the potential ballistic impact), on the inside of the laminate, or elsewhere in between.
The laminate can be prepared by any method known to those skilled in the art, for example by positioning each layer in facing engagement as desired to form an assembly. In some non-limiting embodiments, the assembly is subjected to heat and/or pressure to bond the layers together. In some non-limiting embodiments, the assembly can be placed into an autoclave and heated at a temperature of about 80° C. to about 175° C., or about 350° F. (177° C.), or about 300° F. (149° C.), for about 0.5 to about 10 hours, or about 2 hours, to bond the layers together. In some non-limiting embodiments, pressure of about 0.1 MPa to about 2 MPa can be applied in lieu of or in addition to the heat applied. The bonding of the layers can be a mechanical bond and/or a chemical bond. A mechanical bond can be formed by application of heat and/or pressure. A chemical bond can be formed, for example, by covalent bonding, or ionic bonding, or crosslinking of components of adjacent layers through heating or solvent.
For example, the laminate or assembly can be formed from components and in a manner as described in U.S. Pat. Nos. 4,078,107, 4,081,581, 4,277,294, and 4,367,107, each incorporated by reference herein.
Alternatively or additionally, the layers can be adhered by using an adhesive. Suitable adhesives are well known to those skilled in the art, non-limiting examples of which include Norland Optical Adhesive 60 and CRL RTV408C. Alternatively or additionally, the layers can be adhered or secured adjacent to one another by using an interlayer. Suitable interlayers are well known to those skilled in the art, non-limiting examples of which include silicones, polyvinyl acetals such as polyvinyl butyral, vinyl materials, and polyurethanes (such as polyester polyurethanes), and can include plasticizers and other additives as desired. Non-limiting examples of interlayers include those disclosed in U.S. Pat. Nos. 4,078,107, 4,081,581, 4,277,294, and 4,367,107.
In some non-limiting embodiments, polyurethanes and poly(ureaurethane)s of the present invention can have a hard segment content of about 10 to about 100 weight percent, or about 20 to about 80 weight percent, or about 30 to about 75 weight percent. Hard segment calculation is discussed in detail above.
In some non-limiting embodiments, the polyurethanes and poly(ureaurethane)s of the present invention generally have a urethane content (Wu) of about 20 to about 40 weight percent, or about 21 to about 36 weight percent, or about 30 to about 40 weight percent. The urethane content is the percentage by weight of the urethane linkages present in the polymer and can be calculated by determining the total number of equivalents, and from this the total weight of all reactants, and dividing the total weight of the urethane linkages obtainable from these reactants by the total weight of the reactants themselves. The following example will further explain the calculation. In Example I, Formulation 1 which follows, a polyurethane article according to the invention was prepared by reacting 0.7 equivalents of 1,4-butanediol, 0.3 equivalents of trimethylolpropane and one equivalent of 4,4′-methylene-bis-(cyclohexyl isocyanate) (DESMODUR W). The equivalent weight of the 1,4-butanediol is 45, the equivalent weight of the trimethylolpropane is 44.7 (corrected for impurities) and the equivalent weight of the DESMODUR W is 131.2. Therefore, the actual weight of ingredients used is 31.54 parts by weight of 1,4-butanediol, 13.2 parts by weight of trimethylolpropane and 131.2 parts by weight of DESMODUR W or a total reactant weight of 175.9 parts by weight. One equivalent of DESMODUR W will yield one equivalent of urethane linkage. The equivalent weight of a urethane linkage is 59 so that the total weight of the urethane linkages determined by multiplying the equivalent weight by the number of equivalents would also be 59. Thus, the total weight of the urethane linkage, 59, divided by the total weight of the reactants, 175.9, multiplied by 100 to convert to percentages would give a percentage by weight of urethane linkage of 33.49 percent by weight.
In an analogous manner, the percentage by weight of cyclic structures (Wc) (such as for example cyclohexyl) can be calculated. In Example I, Formulation 1, the only material contributing cyclohexyl moieties is the DESMODUR W. One equivalent of DESMODUR W would yield one equivalent of cyclohexyl moiety which has an equivalent weight of 81. Thus, the total weight of cyclohexyl moiety would be equal to 81 and this divided by the total weight of reactants or 175.9 would yield a We of 46 percent. In some non-limiting embodiments, the polyurethanes and poly(ureaurethane)s of the present invention can have a cyclic content of about 10 to about 80 weight percent, about 20 to about 70 weight percent, about 30 to about 70 weight percent, or about 30 to about 60 weight percent.
In some non-limiting embodiments, the resulting polyurethanes or poly(ureaurethane)s of the present invention when cured can be solid, and essentially transparent. In some non-limiting embodiments, the polyurethane can be partially cured or fully cured such that essentially no further reaction occurs.
In some non-limiting embodiments, the polyurethanes and poly(ureaurethane)s of the present invention generally have a number average molecular weight, as estimated from inherent viscosity measurements, of at least about 20,000 grams/mole, or ranging from about 20,000 to about 1,000,000 grams/mole, or ranging from about 20,000 to about 800,000 grams/mole. The polyurethanes and poly(ureaurethane)s of the present invention generally have an average molecular weight per crosslink of at least about 500 grams per mole, in some embodiments ranging from about 500 and about 15,000 grams/mole, or ranging from about 1800 and about 15,000 grams/mole. The polyurethanes and poly(ureaurethane)s of the present invention generally have a crosslink density of at least about 11,000 grams per mole.
In some non-limiting embodiments, the polyurethane(s) and poly(ureaurethane)s of the present invention when cured can have low density. In some non-limiting embodiments, the density can be from at least 0.9 to less than 1.25 grams/cm3, or from at least 1.0 to less than 1.45 grams/cm3, or from 1.08 to 1.37 grams/cm3, or from 1.08 to 1.13. In some non-limiting embodiments, the density of polyurethanes and poly(ureaurethane)s of the present invention can be less than LEXAN (density about 1.21 g/cm3) and conventional stretched acrylic (density about 1.18 g/cm3). The density can be measured using a DensiTECH instrument manufactured by Tech Pro, Incorporated. In some non-limiting embodiments, the density is measured in accordance with ASTM D 792-00.
Also, some optically clear polyurethanes and poly(ureaurethane)s upon heating can exhibit a low temperature exotherm at about −70° C. (differential thermal analysis can be determined using a du Pont 900 thermal analyzer), and about 11° C., indicating that the polymers are generally amorphous.
In some non-limiting embodiments, softening points of about 65° C. to about 200° C., melting points of about 80° C. to about 220° C., and decomposition temperatures of about 280° C. to about 330° C. under nitrogen atmosphere are typical.
The polyurethanes and poly(ureaurethane)s of the present invention can be useful in applications in which one or more of the following properties are desired: transparency, high optical quality, high Abbe number, low color, energy-absorption, stiffness, moisture stability, ultraviolet light stability, weathering resistance, low water absorption, hydrolytic stability and bullet or explosive resistance.
In some embodiments, cured articles prepared from the polyurethanes and poly(ureaurethane)s of the present invention are generally clear, can have a luminous transmittance of at least about 80 percent, less than about 2 percent haze and show no visual change after 1,000 hours of light and water exposure according to ASTM D-1499-64.
Polyurethanes and poly(ureaurethane)s of the present invention can be formed into articles having a variety of shapes and dimensions, such as cast shapes, flat sheets, curved shapes, laminates, or assemblies. Non-limiting examples of useful methods for forming articles include heat treatment, pressure casting, heat and pressure casting, or pouring liquid polyurethane or poly(ureaurethane) into a mold and curing the product to form a molded article.
The polyurethanes an exhibit good ballistics resistance, e.g., resistance to perforation, penetration or cracking due to impact from a projectile such as a bullet or shot which is shot from a handgun, shotgun, rifle, AK-47, or other shooting device or explosives. In some embodiments, the polyurethanes of 0.75′′ (1.9 cm) thickness or greater will stop or deflect: a 9 mm, 125 grain bullet shot at an initial velocity of 1350 ft/sec (411.5 m/sec) from 20 feet; a .40 caliber bullet shot at an initial velocity of 987 ft/sec (300.8 m/sec) bullet from 20 feet (6.1 m); and/or a 12-gauge shotgun shot at an initial velocity of 1290 ft/sec (393.2 m/sec) from 20 feet (6.1 m).
The polyurethanes can be useful for any of the applications or uses described herein. In some non-limiting embodiments, the present invention provides polyurethanes suitable for use as transparencies or windows. Polyurethanes having good creep resistance (or low deflection) and high fracture toughness (K-factor) can be useful for airplane windows. Airplane windows typically deflect or deform over time due to extremes in temperature and pressure, which can increase interior cabin noise and decrease gas mileage due to increased drag. Therefore, resistance to creep or low deflection is a desirable characteristic. In some non-limiting embodiments, the maximum average deflection of the transparency or window is about 0.5 inch (about 1.3 mm). A flexural test (discussed in the Examples below) was developed to simulate the creep phenomenon under 3,294 psig (300 times the service pressure at 3,500 feet altitude) for 3 hrs. In some non-limiting embodiments for aircraft window applications, the values of Young's Modulus can be at least about 350,000 (about 2413 MPa). Thus, in some non-limiting embodiments, the present invention provides polyurethanes suitable for use as transparencies, such as airplane windows, which can have one or more of the following desirable properties: good deflection resistance, high fracture toughness (K-factor), lower weight than conventional airplane transparencies, and good abrasion resistance.
In some non-limiting embodiments in which articles having good optical properties are desired, such as low striation or no visible striation, the equivalent ratio of the prepolymer components of isocyanate functional material(s) (such as 4,4′-methylene-bis-(cyclohexyl isocyanate) to the polyol(s) having 2 to 18 carbon atoms (such as 1,5-pentane diol) can range from about 1.0:0.3 to about 1.0:0.4, or about 1.0:0.35. While not intending to be bound by any theory, it is believed that the formation of striations in a molded article may be related to the viscosity of the prepolymer. The higher viscosity prepolymer can wet the release-coated glass mold better so that flow into the casting cell is more uniform and smooth, and the urethane content is higher, making compatibility of the components occur faster. The striation of an article can be determined by forming a molded article, for example having a thickness of about one inch (2.54 cm), and holding the molded article in front of a white-coated board or substrate, and visually observing for the presence of striations when a light source is shined upon the molded article.
The polyurethanes and poly(ureaurethane)s of the present invention can be used to form articles having good impact resistance or flexibility, high impact strength, high tensile strength, resistance to heat distortion, resistance to deflection under pressure, good hardness, high Young's Modulus, high K factor, good solvent resistance, good clarity or transparency, high light transmittance, low haze, good weatherability, good energy absorption, good moisture stability, good ultraviolet light stability, and/or good ballistics resistance.
In some non-limiting embodiments, the polyurethanes and poly(ureaurethane)s of the present invention can be used to form articles having a Gardner Impact strength of at least about 100 in-lb, or at least about 200 in-lb, or at least about 400 in-lb (45 Joules), or at least about 500 in-lb or at least about 600 in-lb, according to ASTM-D 5420-04. Non-limiting examples of suitable methods and equipment for measuring impact resistance and impact strength are discussed in detail above.
In some embodiments, the heat distortion temperature of cured articles of the invention can be at least about 190° F. (88° C.) or above about 200° F. (93° C.), as determined according to ASTM-D-648.
Hardness of the polyurethanes and poly(ureaurethanes) can be determined by the Shore hardness and, accordingly, in some embodiments articles of the invention have a Shore D hardness at room temperature (25° C.) using a Shore D durometer of at least about 75 or at least about 80.
Tensile strength at yield or break can be measured according to ASTM-D 638-03. In some non-limiting embodiments, the tensile strength at yield is at least about 6,800 lb/in2 (47 MPa) according to ASTM-D 638-03, or about 6,800 to about 20,000 lb/in2 (about 47 to about 138 MPa), or about 12,000 to about 20,000 lb/in2 (about 83 to about 138 MPa).
Young's Modulus can be measured according to ASTM-D 638-03. In some non-limiting embodiments, the Young's Modulus is at least about 215,000 lb/in2 (about 1482 MPa), or about 215,000 (about 1482 MPa) to about 600,000 lb/in2 (about 4137 MPa), or about 350,000 (about 2413 MPa) to about 600,000 lb/in2 (about 4137 MPa). For commercial airplane cabin window applications, when the cabin pressure is 10 psi (0.07 MPa) or more greater than the external pressure, the cabin windows can deflect into the airstream, thereby increasing noise and decreasing fuel efficiency. Higher values of Young's Modulus indicate increased stiffness and less tendency for the window to deflect into the airstream. In some non-limiting embodiments for aircraft window applications, the values of Young's Modulus can be at least about 350,000 (about 2413 MPa). In typical ballistics applications, the outer plies are glass, which is hard enough to deform a bullet by spreading the impact stress over a large area before it penetrates the underlying plies.
K factor is a measure of crack propagation. Crack propagation can be measured according to U.S. Dept. of Defense MIL-PRF-25690B (Jan. 29, 1993). In some non-limiting embodiments, the polyurethanes and poly(ureaurethane)s of the present invention have a K-Factor crack propagation resistance of at least about 1000 lb/in3/2 (1,098,800 N/m3/2), or about 1000 lb/in3/2 (1,098,800 N/m3/2) to about 4000 lb/in3/2 (4,395,200 N/m312), or about 2000 lb/in3/2 (2,197,600 N/m3/2) to about 4000 lb/in3/2 (4,395,200 N/m3/2).
Compositions suitable for use in automobile windshields meet the standard requirement of minimum light transmission of 70 percent or 86.5 percent or above (Illuminant A. Tungsten lamp 2,840° K.) and less than 2 percent haze (ANSI CODE Z-26.1, 1966, Test No. 18). The percent light transmission and percent haze can be measured by a Hunter Pivotable Sphere Haze Meter according to ASTM E903-82.
The polyurethanes and poly(ureaurethane)s of the present invention can have outstanding weather characteristics as measured by UV light stability and hydrolytic stability. Fade-O-Meter® exposure can be conducted according to ASTM G-25-70, Method A using a Fade-O-Meter, Type FDA-R, Serial No. F02951, manufactured by Atlas Electric Devices Co., Chicago, Ill. The light source can be a carbon arc lamp enclosed in a fused silica globe. The operating temperature of the Fade-O-Meter (black panel) can be 140° F. (60° C.) and the instrument operated with no water in the atomizing unit. Sample sizes are 21⁄2 inches by 6 inches by 1⁄8 inch (6.35 cm by 15.24 cm by 0.32 cm). Weather-O-Meter® exposure can be conducted according to ASTM D-1499-64 using a Weather-O-Meter, Type DMC, Serial No. WO-1305. The type of light source can be a twin carbon arc lamp enclosed in a fused silica globe. The operating black panel temperature can be 140° F. (60° C.). The spray of water is deionized water at a temperature of about 70° F. (21° C.). The number and type of water spray nozzles which are used are four No. 50 nozzles. Alternatively, the UV resistance can be determined using QUV at 1000 hours according to ASTM G-53.
Abrasion resistance can be measured using a Taber Abrader having a CS-10F abrasion wheel with 500 grams of weight, for a sample size 3 inches by 3 inches by 1⁄8 inch (7.62 cm by 7.62 cm by 0.32 cm) according to ASTM D 1044-99. In some non-limiting embodiments, 100 cycles of Taber can result in 30% haze for stretched acrylic and from 5% to 40%, or from 10% to 15% or less than about 5% for the polyurethanes and poly(ureaurethane)s of the present invention.
The polyurethanes and poly(ureaurethane)s of the present invention can have good craze resistance to solvents and acids. Craze resistance can be measured according to U.S. Dept. of Defense MIL-PRF-25690B (Jan. 29, 1993). Non-limiting examples of solvents and acids for Stress Craze Testing include methanol, isopropanol, ethylene glycol, propylene glycol, ethyl acetate, acetone, toluene, isobutyl acetate, Skydrol (hydraulic fluid), jet fuel such as JP-4, and 75% aqueous solution of sulfuric acid. In some non-limiting embodiments, uncoated articles prepared from the polyurethanes and poly(ureaurethane)s of the present invention have a stress craze resistance in organic solvent and 75% by weight aqueous solution of sulfuric acid of at least about 1000 psi (6.9 MPa) tensile stress, or about 1000 psi (6.9 MPa) to about 4000 psi (27.6 MPa), or about 2000 psi (13.8 MPa) to about 4000 psi (27.6 MPa). In some non-limiting embodiments, the polyurethanes and poly(ureaurethane)s of the present invention when uncoated can withstand 75% sulfuric acid for up to thirty days or any organic solvent at between 1000 psi (6.9 MPa) and 4000 psi (27.6 MPa) membrane stress.
In some non-limiting embodiments, the polyurethanes and poly(ureaurethane)s of the present invention when polymerized can produce a polymerizate having a refractive index of at least 1.55, or at least 1.56, or at least 1.57, or at least 1.58, or at least 1.59, or at least 1.60, or at least 1.62, or at least 1.65. In other non-limiting embodiments, the poly(ureaurethane)s of the present invention when polymerized can produce a polymerizate having an Abbe number of at least 32, or at least 35, or at least 38, or at least 39, or at least 40, or at least 44, or at least 59, or having an Abbe number of 59. The refractive index and Abbe number can be determined by methods known in the art such as American Standard Test Method (ASTM) Number D 542-00. Further, the refractive index and Abbe number can be determined using various known instruments. In a non-limiting embodiment of the present invention, the refractive index and Abbe number can be measured in accordance with ASTM D 542-00 with the following exceptions: (i) test one to two samples/specimens instead of the minimum of three specimens specified in Section 7.3; and (ii) test the samples unconditioned instead of conditioning the samples/specimens prior to testing as specified in Section 8.1. Further, in a non-limiting embodiment, an Atago, model DR-M2 Multi-Wavelength Digital Abbe Refractometer can be used to measure the refractive index and Abbe number of the samples/specimens.
Solid articles that can be prepared using the polyurethanes or poly(ureaurethanes) of the present invention include but are not limited to optical articles or lenses, photochromic articles or lenses, windows, transparencies, such as generally transparent windows, windshields, sidelights and backlights, aircraft or airplane transparencies, ballistic resistant articles, windmill components such as blades, and glazings.
In some non-limiting embodiments, the polymeric substrate material, including the coating composition applied thereto, may be in the form of optical elements such as windows, plano and vision correcting ophthalmic lenses, exterior viewing surfaces of liquid crystal displays, cathode ray tubes, e.g., video display tubes for televisions and computers, clear polymeric films, transparencies, e.g., windshields, aircraft transparencies, plastic sheeting, etc.
The polyurethanes and poly(ureaurethane)s of the present invention are desirable for a wide variety of uses. They are particularly useful as glazing materials for aircraft safety glass windows. Besides aircraft glazing, the polyurethanes and poly(ureaurethane)s of the invention in sheet form can be used in architectural applications and can be tinted or made opaque by pigmenting if desired. In such applications, the polyurethanes and poly(ureaurethane)s of the invention can be in sheet form and may be used alone or laminated to other materials as discussed above. The layers in the composite can have the same or different modulus values, as desired. Also, in some embodiments the polyurethanes and poly(ureaurethane)s of the invention can be used for optical lenses since they can be optically clear, unaffected by ultraviolet light and humidity exposure and abrasion resistant.
In other non-limiting embodiments, the polyurethanes and poly(ureaurethane)s of the present invention can be used as low thermal expansion substrates for deposition of conductive films for electrochromic applications, microwave absorbing films or low resistance films. In other non-limiting embodiments, a stretched acrylic substrate can be coated with a cyanoethyl acrylate/acrylic copolymer and further coated with the polyurethanes and poly(ureaurethane)s of the present invention.
The polyurethanes and poly(ureaurethane)s of the invention can be used in sheet form and can vary in thickness from about 2 to 500 mils, although somewhat thinner and thicker sheets can be used, depending upon the application. For aircraft use, in some embodiments the thickness can vary between 1/16 inch and 1⁄2 inch (0.16 cm to 1.27 cm).
In some non-limiting embodiments, an automobile window can be prepared from a thermoplastic polycarbonate resin, such as that sold under the trademark LEXAN, with the coating composition of the present invention applied as a weather layer on the outboard side of the window to increase the weatherability of the window. Alternatively, an automobile window can be prepared as a glass/LEXAN laminate, with the glass as the outboard layer and the coating composition of the present invention applied as a layer on the inboard side of the laminate.
The coating composition of the present invention can be applied to the substrate surface using any known coating procedures. Desirably, the coating composition is flow coated over the substrate surface by an automated flow-coating system in which the surface tension of the liquid pulls a coherent sheet of liquid across the substrate surface as the mechanical flow-coating device traverses across the substrate sheet. An automatic flow-coating device typically consists of an articulating arm that holds a nozzle connected to a pressure pot where the resin solution is held. The arm runs on a track above the sheet to be coated. The rate of flow of the liquid is adjusted using the pressure pot. The rate of traverse of the articulating arm is set using a potentiometer. The nozzle distance from the sheet is optimized and kept constant, via the articulating arm. This is particularly important for curved sheets. The thickness of the coating is determined by the initial viscosity of the resin solution and the rate of solvent evaporation. The evaporation rate is mainly controlled by the solvent choice and the cubic feet/minute airflow in the ventilated coating booth. Alternatively, the coating compositions can be prepared and cast in an appropriate mold to form a desired structure, which can then be applied as a layer to a suitable substrate, such as through a lamination process, or may used as a monolithic structure.
The coating composition generally may be applied to a substrate by itself as a transparent or pigmented monocoat, or as the pigmented base coat and/or transparent topcoat in a color-plus-clear composite coating as known to those skilled in the art. In some embodiments, the coating can be applied before the isocyanate and hydroxyl groups are fully reacted, for example by spraying the isocyanate and hydroxyl components separately through a mixing nozzle to apply the coating to the substrate. Alternatively, the coating can be partially cured in an oven and then subjected to a high moisture environment, such as high humidity or water spray, to further react and cure the coating. If desired, the coating composition may contain additional materials well known in the art of formulated surface coatings, such as surfactants, flow control agents, thixotropic agents, fillers, antigassing agents, organic cosolvents, catalysts, and other customary auxiliaries. These materials can constitute up to 40 percent by weight of the total weight of the coating composition.
As aforementioned, although the cured compositions can be formed from liquid coating compositions, they also can be formed from coating compositions formulated as powder coating compositions.
In another non-limiting embodiment, the cured compositions of the present invention also can be useful as decorative or protective coatings for pigmented plastic (elastomeric) substrates or mold-in-color (“MIC”) plastic substrates. In these applications, the compositions can be applied directly to the plastic substrate or included in the molding matrix. Optionally, an adhesion promoter can first be applied directly to the plastic or elastomeric substrate and the composition applied as a topcoat thereover.
In another non-limiting embodiment, the compositions of the present invention also can be useful as a spalling shield layer, an anti-lacerative coating layer or a break-in resistant coating layer for glass or other substrates.
In a non-limiting embodiment, the polyurethane polymerizate of the present invention can be used to prepare photochromic articles. In a further embodiment, the polymerizate can be transparent to that portion of the electromagnetic spectrum which activates the photochromic substance(s), i.e., that wavelength of ultraviolet (UV) light that produces the colored or open form of the photochromic substance and that portion of the visible spectrum that includes the absorption maximum wavelength of the photochromic substance in its UV activated form, i.e., the open form.
Photochromic compounds exhibit a reversible change in color when exposed to light radiation involving ultraviolet rays, such as the ultraviolet radiation in sunlight or the light of a mercury lamp. Various classes of photochromic compounds have been synthesized and suggested for use in applications in which a sunlight-induced reversible color change or darkening is desired. The most widely described classes of photochromic compounds are oxazines, pyrans and fulgides.
The general mechanism responsible for the reversible change in color, i.e., a change in the absorption spectrum in the visible range of light (400-700 nm), exhibited by different types of photochromic compounds has been described and categorized. See John C. Crano, “Chromogenic Materials (Photochromic)”, Kirk-Othmer Encyclopedia of Chemical Technology, Fourth Edition, 1993, pp. 321-332. The general mechanism for the most common classes of photochromic compounds, e.g., indolino spiropyrans and indolino spirooxazines, involves an electrocyclic mechanism. When exposed to activating radiation, these compounds transform from a colorless closed ring compound into a colored open ring species. In contrast, the colored form of fulgide photochromic compounds is produced by an electrocyclic mechanism involving the transformation of a colorless open ring form into a colored closed ring form.
A wide variety of photochromic substances can be used in the present invention. In a non-limiting embodiment, organic photochromic compounds or substances can be used. In alternate non-limiting embodiments, the photochromic substance can be incorporated, e.g., dissolved, dispersed or diffused into the polymerizate, or applied as a coating thereto.
In a non-limiting embodiment, the organic photochromic substance can have an activated absorption maximum within the visible range of greater than 590 nanometers. In a further non-limiting embodiment, the activated absorption maximum within the visible range can be from at least 590 to 700 nanometers. These materials can exhibit a blue, bluish-green, or bluish-purple color when exposed to ultraviolet light in an appropriate solvent or matrix. Non-limiting examples of such substances that are useful in the present invention include but are not limited to spiro(indoline)naphthoxazines and spiro(indoline)benzoxazines. These and other suitable photochromic substances are described in U.S. Pat. Nos. 3,562,172; 3,578,602; 4,215,010; 4,342,668; 5,405,958; 4,637,698; 4,931,219; 4,816,584; 4,880,667; 4,818,096.
In another non-limiting embodiment, the organic photochromic substances can have at least one absorption maximum within the visible range ranging from 400 and less than 500 nanometers. In a further non-limiting embodiment, the substance can have two absorption maxima within this visible range. These materials can exhibit a yellow-orange color when exposed to ultraviolet light in an appropriate solvent or matrix. Non-limiting examples of such materials can include certain chromenes, such as but not limited to benzopyrans and naphthopyrans. Many of such chromenes are described in U.S. Pat. Nos. 3,567,605; 4,826,977; 5,066,818; 4,826,977; 5,066,818; 5,466,398; 5,384,077; 5,238,931; and 5,274,132.
In another non-limiting embodiment, the photochromic substance can have an absorption maximum within the visible range ranging from 400 to 500 nanometers and an absorption maximum within the visible range ranging from 500 to 700 nanometers. These materials can exhibit color(s) ranging from yellow/brown to purple/gray when exposed to ultraviolet light in an appropriate solvent or matrix. Non-limiting examples of these substances can include certain benzopyran compounds having substituents at the 2-position of the pyran ring and a substituted or unsubstituted heterocyclic ring, such as a benzothieno or benzofurano ring fused to the benzene portion of the benzopyran. Further non-limiting examples of such materials are disclosed in U.S. Pat. No. 5,429,774.
In some non-limiting embodiments, the photochromic substance for use in the present invention can include photochromic organo-metal dithizonates, such as, but not limited to (arylazo)-thioformic arylhydrazidates, such as, but not limited to mercury dithizonates which are described, for example, in U.S. Pat. No. 3,361,706. Fulgides and fulgimides, such as, but not limited to 3-furyl and 3-thienyl fulgides and fulgimides which are described in U.S. Pat. No. 4,931,220 at column 20, line 5 through column 21, line 38, can be used in the present invention. The relevant portions of the aforedescribed patents are incorporated herein by reference.
In other non-limiting embodiments, the photochromic articles of the present invention can include one photochromic substance or a mixture of more than one photochromic substances. In other non-limiting embodiments, various mixtures of photochromic substances can be used to attain activated colors such as a near neutral gray or brown.
The amount of photochromic substance employed can vary. In some non-limiting embodiments, the amount of photochromic substance and the ratio of substances (for example, when mixtures are used) can be such that the polymerizate to which the substance is applied, or in which it is incorporated, exhibits a desired resultant color, e.g., a substantially neutral color such as shades of gray or brown when activated with unfiltered sunlight, i.e., as near a neutral color as possible given the colors of the activated photochromic substances. In some non-limiting embodiments, the amount of photochromic substance used can depend upon the intensity of the color of the activated species and the ultimate color desired.
In some non-limiting embodiments, the photochromic substance can be applied to or incorporated into the polymerizate by various methods known in the art. In a non-limiting embodiment, the photochromic substance can be dissolved or dispersed within the polymerizate. In other non-limiting embodiments, the photochromic substance can be imbibed into the polymerizate by methods known in the art. The term “imbibition” or “imbibe” includes permeation of the photochromic substance alone into the polymerizate, solvent assisted transfer absorption of the photochromic substance into a porous polymer, vapor phase transfer, and other such transfer mechanisms. In a non-limiting embodiment, the imbibing method can include coating the photochromic article with the photochromic substance; heating the surface of the photochromic article; and removing the residual coating from the surface of the photochromic article. In alternate non-limiting embodiments, the imbibition process can include immersing the polymerizate in a hot solution of the photochromic substance or by thermal transfer.
In some non-limiting embodiments, the photochromic substance can be a separate layer between adjacent layers of the polymerizate, e.g., as a part of a polymer film; or the photochromic substance can be applied as a coating or as part of a coating placed on the surface of the polymerizate.
The amount of photochromic substance or composition containing the same applied to or incorporated into the polymerizate can vary. In some non-limiting embodiments, the amount can be such that a photochromic effect discernible to the naked eye upon activation is produced. Such an amount can be described in general as a photochromic amount. In some non-limiting embodiments, the amount used can depend upon the intensity of color desired upon irradiation thereof and the method used to incorporate or apply the photochromic substance. In general, the more photochromic substance applied or incorporated, the greater the color intensity. In some non-limiting embodiments, the amount of photochromic substance incorporated into or applied onto a photochromic optical polymerizate can be from 0.15 to 0.35 milligrams per square centimeter of surface to which the photochromic substance is incorporated or applied.
In another embodiment, the photochromic substance can be added to the polyurethane prior to polymerizing and/or cast curing the material. In this embodiment, the photochromic substance used can be chosen such that it is resistant to potentially adverse interactions with, for example, the isocyanate present. Such adverse interactions can result in deactivation of the photochromic substance, for example, by trapping them in either an open or closed form.
Further non-limiting examples of suitable photochromic substances for use in the present invention can include photochromic pigments and organic photochromic substances encapsulated in metal oxides such as those disclosed in U.S. Pat. Nos. 4,166,043 and 4,367,170; organic photochromic substances encapsulated in an organic polymerizate such as those disclosed in U.S. Pat. No. 4,931,220.
The invention will be further described by reference to the following examples. Unless otherwise indicated, all parts and percentages are by weight.
EXAMPLES
The physical properties set forth below were measured as follows:
Light Transmittance (%) was measured according to ASTM E903-82;
Yellowness Index was measured according to ASTM D 1925-70;
Refractive index was measured on a multiple wavelength Abbe Refractometer Model DR-M2 manufactured by ATAGO Co., Ltd.; the refractive index of liquids were measured in accordance with ASTM-D 1218; and the refractive index of solids were measured in accordance with ASTM-D 542-00 (2006);
Density (grams/cm3) and specific gravity of solids were measured in accordance with ASTM-D 792-00;
Taber Abrasion (% haze) was measured for up to 100 cycles using a Taber Abrader having a CS-10F abrasion wheel with 500 grams of weight, for a sample size 3 inches by 3 inches by 1⁄8 inch (7.62 cm by 7.62 cm by 0.32 cm) according to ASTM D 1044-99;
Bayer Abrasion (% haze) was measured for according to ASTM F 735-94 (Reapproved 2001);
K-Factor crack propagation resistance was measured according to U.S. Dept. of Defense MIL-PRF-25690B (Jan. 29, 1993).
Tensile strength at yield, percent elongation at yield, tensile stress at break, elongation at break, Modulus of elasticity, Poisson's ratio and Young's Modulus were measured at about 25° C. in accordance with ASTM-D 638-03;
Shear properties, such as Maximum shear force and Maximum shear strength were measured in accordance with ASTM D732-02;
Gardner Impact Strength was measured in accordance with ASTM-D 5420-04;
Dynatup Multiaxial Impact Strength was measured in accordance with ASTM-D 3763-02 or D3763-10e1;
Shore D Hardness was measured in accordance with a Shore D durometer;
Vickers hardness was measured in accordance with ASTM E384-06;
QUV-B testing was conducted for 333 hours or 1000 hours (as specified) according to ASTM G-53;
Glass transition temperature (Tg) was measured using Dynamic Mechanical Analysis; and
Linear Coefficient of Thermal Expansion was measured using a duPont Thermomechanical analyzer (TMA) according to ASTM E 228-95 or ASTM D696-03.
The following abbreviations were used herein:
CHDM: 1,4-cyclohexane dimethanol;
Des N 3400: 60% hexamethylene diisocyanate dimer and 40% hexamethylene diisocyanate trimer commercially available from Bayer;
Des W or DESMODUR W: 4,4′-methylene-bis-(cyclohexyl isocyanate) commercially available from Bayer;
PDO: 1,5-pentanediol;
Polycarbonate diol 1: KM-10-1733 polycarbonate diol prepared from hexanediol having a molecular weight of 1000 g/mol commercially available from Stahl (also known as PC-1733);
Polycarbonate diol 2: KM10-1667 polycarbonate diol prepared from hexanediol having a molecular weight of 1000 g/mol commercially available from Stahl (also known as PC-1667); and
TMP: trimethylolpropane.
Example A
Polyurethanes of Formulations 19, 21-25, 58-65, 86-109 and 115 were prepared from the components in amounts listed in Tables 1-18.
The polyurethanes were prepared in a glass kettle under nitrogen blanket with stirring. The polyisocyanate was preheated to a temperature of about 100° C. before addition of the other components. The mixture was heated to a temperature of about 110° C. over about 10 minutes and maintained at this temperature for about 30 minutes.
The poly(ureaurethane)s (formulations including water) also were prepared in a glass kettle under nitrogen blanket with stirring. The polyisocyanate was preheated to a temperature of about 60° C.
For Formulations 123-127, 131, and 132, the water was added to the polyisocyanate and the temperature was maintained for about 30 minutes to form an isocyanate functional urea prepolymer. The other components were added and the mixture was heated to a temperature of about 90° C. over about 10 minutes and maintained at this temperature for about 30 minutes.
Each of the polyurethane and poly(ureaurethane) mixtures was degassed to remove carbon dioxide and cast into a 12′′×13′′×0.125′′ (30.5 cm×33 cm×0.3 cm) casting cell which had been preheated to a temperature of about 121° C. The filled cell was then cured in an oven for a period of about 48 hours at about 121° C.









TABLE 1








Molecular
Hard















Polyisocyanate
Branched Polyol
Diol
Urethane
Cyclic
Weight per
Segment

















Formulation

Equiv-

Equiv-

Equiv-
Content
Content
Crosslink
Content


No.
Type
alents
Type
alents
Type
alents
(wt. %)
(wt. %)
(g/mole)
(wt. %)




















19
Des W
1.00
TMP
0.3
1,10-decanediol
0.65
26.52
36.40
2225
63.00







Polycarbonate diol 1
0.05


















TABLE 2








Molecular
Hard















Polyisocyanate
Branched Polyol
Diol
Urethane
Cyclic
Weight per
Segment

















Formulation

Equiv-

Equiv-

Equiv-
Content
Content
Crosslink
Content


No.
Type
alents
Type
alents
Type
alents
(wt. %)
(wt. %)
(g/mole)
(wt. %)




















21
Des W
1.00
TMP
0.3
1,4-butanediol
0.6
27.54
37.81
2142
49.00







Polycarbonate diol 1
0.1






23
Des W
1.00
TMP
0.4
1,10-decanediol
0.5
25.08
34.44
2352
46.00







Polycarbonate diol 1
0.1






24
Des W
1.00
TMP
0.3
1,10-decanediol
0.6
24.64
33.83
2395
46.00







Polycarbonate diol 1
0.1






25
Des W
1.00
TMP
0.3
1,4-butanediol
0.5
23.38
32.10
2523
54.00







Polycarbonate diol 1
0.2


















TABLE 4








Molecular
Hard















Polyisocyanate
Branched Polyol
Diol
Urethane
Cyclic
Weight per
Segment

















Formulation

Equiv-

Equiv-

Equiv-
Content
Content
Crosslink
Content


No.
Type
alents
Type
alents
Type
alents
(wt. %)
(wt. %)
(g/mole)
(wt. %)




















58
Des W
1.00
TMP
0.3
1,5-pentanediol
0.5
22.99
31.56
2566
35.00







Polycarbonate diol 1
0.2






59
Des W
1.00
TMP
0.3
1,5-pentanediol
0.6
26.96
37.01
2188
50.00







Polycarbonate diol 1
0.1






60
Des W
1.00
TMP
0.3
1,5-pentanediol
0.3
26.25
36.04
2247
64.00







CHDM
0.3











Polycarbonate diol 1
0.10






61
Des W
1.00
TMP
0.4
1,5-pentanediol
0.1
22.55
30.95
2617
37.00







CHDM
0.3











Polycarbonate diol 1
0.20


















TABLE 5








Molecular
Hard















Polyisocyanate
Branched Polyol
Diol
Urethane
Cyclic
Weight per
Segment

















Formulation

Equiv-

Equiv-

Equiv-
Content
Content
Crosslink
Content


No.
Type
alents
Type
alents
Type
alents
(wt. %)
(wt. %)
(g/mole)
(wt. %)




















62
Des W
1.00
TMP
1.0
Polycarbonate diol 1
0.05
30.24
41.52
616
0.00


63
Des W
1.00
TMP
1.0
Polycarbonate diol 1
0.25
31.81
43.67
560
0.00


64
Des W
1.00
TMP
0.9
Polycarbonate diol 1
0.1
27.53
37.80
716
0.00


65
Des W
1.00
TMP
1.0
Polycarbonate diol 1
0.01
32.82
45.06
543
0.00


86
Des W
1.00
TMP
0.30
1,5-pentanediol
0.46
21.71
29.80
2718
31.00







Polycarbonate diol 1
0.24






87
Des W
1.00
TMP
0.30
1,5-pentanediol
0.47
22.02
30.22
2680








Polycarbonate diol 1
0.23






88
Des W
1.00
TMP
0.30
1,5-pentanediol
0.48
22.33
30.66
2642








Polycarbonate diol 1
0.22


















TABLE 6








Molecular
Hard















Polyisocyanate
Branched Polyol
Diol
Urethane
Cyclic
Wt. per
Segmt

















Formulation

Equiv-

Equiv-

Equiv-
Content
Content
Crosslink
Content


No.
Type
alents
Type
alents
Type
alents
(wt. %)
(wt. %)
(g/mole)
(wt. %)




















89
Des W
1.00
TMP
0.30
1,5-pentanediol
0.49
22.65
31.10
2604








Polycarbonate diol 1
0.21






90
Des W
1.00
TMP
0.30
1,5-pentanediol
0.51
23.33
32.03
2529








Polycarbonate diol 1
0.19






91
Des W
1.00
TMP
0.30
1,5-pentanediol
0.52
23.69
32.52
2491








Polycarbonate diol 1
0.18






92
Des W
1.00
TMP
0.30
1,5-pentanediol
0.53
24.05
33.02
2453








Polycarbonate diol 1
0.17






93
Des W
1.00
TMP
0.30
1,5-pentanediol
0.54
24.43
33.54
2415








Polycarbonate diol 1
0.16






94
Des W
1.00
TMP
0.30
1,5-pentanediol
0.55
24.82
34.07
2377
42.00







Polycarbonate diol 1
0.15






95
Des W
1.00
TMP
0.3
1,5-pentanediol
0.5
22.80
31.30
2020








Polycarbonate diol 2
0.2






96
Des W
1.00
TMP
0.3
1,5-pentanediol
0.65
29.43
40.41
2005
59.00







Polycarbonate diol 2
0.05






97
Des W
1.00
TMP
0.3
1,4-butanediol
0.65
30.11
41.34
1959








Polycarbonate diol 2
0.05






98
Des W
1.00
TMP
0.3
1,5-pentanediol
0.6
26.83
36.84
2199








Polycarbonate diol 2
0.1






99
Des W
1.00
TMP
0.3
1,4-butanediol
0.5
23.31
32.00
2532








Polycarbonate diol 1
0.2






100
Des W
1.00
TMP
0.3
1,4-butanediol
0.6
27.49
37.73
2147








Polycarbonate diol 1
0.1






101
Des W
1.00
TMP
0.30
1,4-butanediol
0.46
21.97
30.16
2686








Polycarbonate diol 1
0.24






102
Des W
1.00
TMP
0.30
1,4-butanediol
0.47
22.29
30.60
2647








Polycarbonate diol 1
0.23






103
Des W
1.00
TMP
0.30
1,4-butanediol
0.48
22.62
31.05
2609








Polycarbonate diol 1
0.22






104
Des W
1.00
TMP
0.30
1,4-butanediol
0.49
22.96
31.52
2570








Polycarbonate diol 1
0.21






105
Des W
1.00
TMP
0.30
1,4-butanediol
0.51
23.67
32.49
2493








Polycarbonate diol 1
0.19


















TABLE 7








Molecular
Hard















Polyisocyanate
Branched Polyol
Diol
Urethane
Cyclic
Weight per
Segment

















Formulation

Equiv-

Equiv-

Equiv-
Content
Content
Crosslink
Content


No.
Type
alents
Type
alents
Type
alents
(wt. %)
(wt. %)
(g/mole)
(wt. %)




















106
Des W
1.00
TMP
0.30
1,4-butanediol
0.52
24.04
33.00
2455








Polycarbonate diol 1
0.18






107
Des W
1.00
TMP
0.30
1,4-butanediol
0.53
24.42
33.52
2416








Polycarbonate diol 1
0.17






108
Des W
1.00
TMP
0.30
1,4-butanediol
0.54
24.81
34.07
2378








Polycarbonate diol 1
0.16






109
Des W
1.00
TMP
0.30
1,4-butanediol
0.55
25.22
34.63
2339








Polycarbonate diol 1
0.15






115
Des W
1.00
TMP
0.05
CHDM
0.95
26.69
36.64
10965








Polycarbonate diol 1
0.05




















TABLE 8






Light





Formulation
Transmittance
Yellowness
Refractive
Density


No.
(%)
Index
Index
(g/cm3)



















19


1.521
1.0886


21


1.517
1.1327


23


1.523
1.1043


24


1.517
1.0971


25


1.521
1.1372


58



1.145





















TABLE 9










Tensile

Gardner



Bayer

Modulus
Elongation
Impact













Formulation
Taber Abrasion
Abrasion

at Yield
at Yield
Strength














No.
# Cycles
% Haze
% Haze
K-Factor
(lb/in2)
(%)
(In-lbs)

















19

33.9
45.9
4309
260000
14
595


21

28
40.77
3211
312000
14
536


23

38
43.08
4628
265000
12
461


24

39.1
43.17
4869
251000
15
497


25

24.5
37.83
4528
246000
14
627





















TABLE 10










Tensile

Gardner



Bayer

Modulus
Elongation
Impact













Formulation
Taber Abrasion
Abrasion

at Yield
at Yield
Strength














No.
# Cycles
% Haze
% Haze
K-Factor
(lb/in2)
(%)
(In-lbs)

















58




215000
20
365


59



4035
283000
10
299


60



1598
284000
18
379


61




260000
17
546


62



876
346000
3.2
24


63



737
334000
4.2
14


64



1119
349000
2.9
27


65



669
357000
2.8





















TABLE 11










Tensile

Gardner



Bayer

Modulus
Elongation
Impact













Formulation
Taber Abrasion
Abrasion

at Yield
at Yield
Strength














No.
# Cycles
% Haze
% Haze
K-Factor
(lb/in2)
(%)
(In-lbs)

















86






317


87






328


88






451


89




227000
15
472


90




244000
11
445


91




255000
21
411


92




263000
19
426


93




266000
9
443


94




270000
12
403


95




259000
13
406


96




280000
19
255


97




299000
5
290


98




272000
13
405


99






346


100






333


101






363


102






364





















TABLE 12










Tensile

Gardner



Bayer

Modulus
Elongation
Impact













Formulation
Taber Abrasion
Abrasion

at Yield
at Yield
Strength














No.
# Cycles
% Haze
% Haze
K-Factor
(lb/in2)
(%)
(In-lbs)





103






367


104






367


105






360


106






404


107






362


108






371


109






327




















TABLE 13









Coefficient



Dynatup

Glass
of Thermal


Formulation
Impact
Shore D
Transition
Expansion


No.
Strength
Hardness
Temp.
(in/in)



















19
44.3
81
89.1



21
39.6
81
97



23
17.9
79
87
101.11


24
33.4
80
79.2
97.2


25
44.9
78
76.1
95.66




















TABLE 14









Coefficient



Dynatup

Glass
of Thermal


Formulation
Impact
Shore D
Transition
Expansion


No.
Strength
Hardness
Temp.
(in/in)



















58
62.3

66



59
36.6





60
37.4





61
38.9





62


152



63


134



64


150



65


174



89
42.6





90
48.4





91
50.2





92
48





93
56.5





94
45.1





95
47.5





96
47.5





97
34.3





98
39.2



















TABLE 15








Molecular
Hard

















Polyisocyanate
Branched Polyol
Diol
Urethane
Cyclic
Weight per
Segment
Water


















Formulation

Equiv-

Equiv-

Equiv-
Content
Content
Crosslink
Content
(Equiv-


No.
Type
alents
Type
alents
Type
alents
(wt. %)
(wt. %)
(g/mole)
(wt. %)
alents)





















123
Des W
1.00
TMP
0.3
1,5-pentanediol
0.554
29.67
40.74
1988

0.19







Polycarbonate diol 1
0.57







124
Des W
1.00
TMP
0.3
1,5-pentanediol
0.374
27.73
38.07
2128

0.22







Polycarbonate diol 1
0.11







126
Des W
1.00
TMP
0.3
1,5-pentanediol
0.45
30.85
42.35
1913

0.20







Polycarbonate diol 1
0.05







127
Des W
1.00
TMP
0.3
1,5-pentanediol
0.4
28.08
38.55
2101

0.20







Polycarbonate diol 1
0.1







131
Des W
1.00
TMP
0.3
1,5-pentanediol
0.55
30.17
41.42
1956

0.10







Polycarbonate diol 1
0.05







132
Des W
1.00
TMP
0.3
1,5-pentanediol
0.5
27.52
37.78
2144

0.10







Polycarbonate diol 1
0.1




















TABLE 16






Light





Formulation
Transmittance
Yellow
Refractive
Density


No.
(%)
Index
Index
(g/cm3)







125



1.119


126



1.125


127



1.133


131



1.127


132



1.129





















TABLE 17










Tensile

Gardner



Bayer

Modulus
Elongation
Impact













Formulation
Taber Abrasion
Abrasion

at Yield
at Yield
Strength














No.
# Cycles
% Haze
% Haze
K-Factor
(lb/in2)
(%)
(In-lbs)

















125




355000
13
51


126



1113
305000
4
24


127



1551
282000
12
244


131




290000
7.7
126


132




289000
19
328




















TABLE 18









Coefficient



Dynatup

Glass
of Thermal


Formulation
Impact
Shore D
Transition
Expansion


No.
Strength
Hardness
Temp.
(in/in)



















125


137



126
14.6

115



127
30

67



131
32.5





132









The above samples exhibited low yellowness, high light transmittance, high impact strength and good ballistic resistance.
A 6′′×6′′ (15.2 cm×15.2 cm) laminate of 2′′ (5.1 cm) of molded Formulation 2 below facing outward, laminated to a 1′′ (2.5 cm) ply of molded Formulation 9 below, and 0.5′′ (1.3 cm) of molded Formulation 60 stopped or deflected four consecutive AK-47, 7.62 mm×39 mm shots from 150 feet (45.7 m). Each layer was molded as described above. No glass ply was used in the laminate. The laminate was heated in an autoclave at about 300° F. (149° C.) for about 2 hours.









TABLE 20







Sample of




Formulation 84


Property
Polycarbonate
of Example A

















Light Transmission
88
92


Density
1.2
1.08


Solvent Resistance
Poor OH, H+,
Good OH, H+,



Acetone
Acetone










Gardner Impact Mean
588
in-lb
>640 in-lbs


Failure Energy


(>72 J)











High Speed
72
joules
105
Joules


Multiaxial Impact













% Haze, 100 cycles
60%
15%


Taber Abrader




Refractive Index
1.586
1.519


Tensile Modulus
320,000
300,000











Tensile Strength
8000
psi
8500
psi









% Elongation (at break)
100% 
200% 


% Elongation
severe
97%


(1000 hrs QUV-B)
degradation




brittle-yellow












Heat Distortion Temp.
275°
F.
220°
F.


Glass Transition
305
F.
240
F.


Temperature













Shore D Durometer
85
80









Example AC
A 6′′×6′′×1′′ (15.2 cm×15.2 cm×2.5 cm) thick sample of Formulation 93 from Example A above was cured by heating at 290° F. (143° C.) for 48 hours. Three 9 mm bullets shot from 20 feet (6.1 m) at a velocity of 1350 ft/sec (411 msec) stuck in the sample. A photograph of a front elevational view of the test sample is shown in FIG. 1.
Example AD
A 6′′×6′′×1′′ (15.2 cm×15.2 cm×2.5 cm) thick sample of Formulation 94 from Example A above was cured by heating at 290° F. (143° C.) for 48 hours. A 9 mm bullet shot from 20 feet (6.1 m) at am initial velocity of 1350 ft/sec (411 m/sec) stuck in the sample. Photographs of the test sample is shown in FIGS. 2 and 3. FIG. 2 is a perspective view of the sample showing the bullet embedded in the sample surface. FIG. 3 is a side elevational view of the sample showing the bullet entrance into the sample.
Example AE
A 6′′×6′′×1′′ (15.2 cm×15.2 cm×2.5 cm) thick sample of Formulation 2 from Example A above was cured by heating at 290° F. (143° C.) for 48 hours. A 6′′×6′′×1′′ thick sample of Formulation 9 from Example A above was cured by heating at 290° F. (143° C.) for 48 hours. A 6′′×6′′×0.5′′ (15.2 cm×15.2 cm×1.75 cm) thick sample of Formulation 58 from Example A above was cured by heating at 290° F. (143° C.) for 48 hours. A composite was prepared by assembling a 1′′ (2.5 cm) thick layer of the sample of Formulation 2, a 1′′ (2.5 cm) thick layer of the sample of Formulation 9, and a 0.5′′ (1.25 cm) thick layer of the sample of Formulation 58 such that the layer of Formulation 2 faced the rifle.
Four 7.62×39 mm bullets having a steel core were shot from an AK-47 rifle from a distance of 30 yards (27.4 m) at an initial velocity of 2700 ft/sec (823 m/sec). The first bullet stopped in the middle layer of Formulation 9, generally parallel to the initial shot direction. The second through fourth bullets stopped in the far layer of Formulation 58, generally parallel to the initial shot direction. Photographs of the test sample is shown in FIGS. 4 and 5. FIG. 4 is a front elevational view of a portion of the sample showing bullet entry points and two bullets embedded in the sample surface. FIG. 5 is a rear perspective view of the sample showing the two exiting bullets lodged in the Formulation 58 layer of the sample.
Example AF
Samples prepared from Formulations 58 and 89-97 of Example A above performed similarly, i.e., all “caught” bullets. A sample prepared from Formulation 94 showed the least amount of sample penetration with about 1⁄8′′ of the back of the bullet protruding from the surface. No ductile bulge was observed in the back of the sample prepared from Formulation 94. Penetration was greatly reduced compared to samples prepared from Formulations 58 and 89-92
Example D2
A polyurethane polymer according to the present invention was prepared from the components listed below in Table 23:










TABLE 23








Desired




Polymer
Batch



Solids
Wt. (g)
Size (g)





















Monomer
PC-1733
1,5-
TMP
Des W
239.04
300.00


Name

pentanediol






OH #
—
—
—
—




Acid #
—
—
—
—




Equivalent
440
52.08
44.00
131.2




Wt.








Equivalents
0.15
0.55
0.3
1.0




desired








Mass
66.00
28.64
13.20
131.20




Monomer








Weight %
27.61%
11.98%
5.52%
54.89%




Monomer








Monomer
82.83
35.95
16.57
164.66




masses for








experiment








Weight %
35.84







Hard








Segment








Weight %
24.68







Urethane








Molecular
2390.4







Weight per








Crosslink








(g/mole) (Mc)









The 1,5-pentanediol, PC-1733, and trimethylolpropane and DESMODUR W preheated to 80° C. were added to a glass kettle. Under nitrogen blanket and with constant stirring, the mixture was heated to  ̃105° C. and allowed to compatibilize. Once clear, the mixture was degassed, and cast into a 12′′×12′′×0.125′′ (30.5 cm×30.5 cm 0.3 cm) casting cell preheated to 121° C. The filled cell was cured for 48 hours at 143° C. A similar procedure was used to prepare a 1 inch thick casting for ballistic testing.
This formulation passed multiple 9 mm, 115 grain, 1350 ft/sec shots by “catching” in bulk of the polymer in a 6′′×6′′×1′′ (15.2 cm×15.2 cm×2.5 cm) sample. The bullet penetration was approximately 0.25′′ (0.6 cm) with no ductile bulge in the back of the sample. The same formulation 4′′×4′′×1′′ (10.1 cm×10.1 cm×2.5 cm) sample also passed multiple .40 caliber shots in which the bullet was not caught or ricocheted. The bullet was sitting, slightly deformed, at the base of the sample. In a 3⁄8′′ (1 cm) thickness, this formulation passed three 12-gauge shotgun shots from 30 feet (9.1 m). Most of the shots were embedded in the surface of the sample.
Example D5
A polyurethane polymer according to the present invention was prepared from the components listed below in Table 26:










TABLE 26








Desired




Polymer
Batch



Solids
Wt. (g)
Size (g)





















Monomer
KM10-1733
1,5-
TMP
Des W
258.44
300.00


Name

pentanediol






OH #
—
—
—
—




Acid #
—
—
—
—




Equivalent
440
52.075
44.00
131.2




Wt.








Equivalents
0.2
0.5
0.3
1.0




desired








Mass
88.00
26.04
13.20
131.20




Monomer








Weight %
34.05%
10.07%
5.11%
50.77%




Monomer








Monomer
102.15
30.22
15.32
152.30




masses for








experiment








Weight %
44.20







Hard








Segment








Weight %
22.83







Urethane








Molecular
2584.38







Weight per








Crosslink








(g/mole) (Mc)









The 1,5 pentanediol, KM10-1733 polycarbonate diol, and trimethylolpropane and DESMODUR W preheated to 80° C. were added to a glass kettle. Under nitrogen blanket and with constant stirring, the mixture was heated to  ̃105° C. and allowed to compatibilize. Once clear, the mixture was degassed, and cast into a 12′′×12′′×0.125′′ (30.5 cm×30.5 cm 0.3 cm) casting cell preheated to 143° C. The filled cell was cured for 48 hours at 121° C. A similar procedure was used to prepare a 1 inch thick casting for ballistic testing.
This formulation passed multiple 9 mm, 115 grain, 1350 ft/sec (393 m/sec) shots by “catching” in bulk of the polymer in a 6′′×6′′×1′′ (15.2 cm×15.2 cm×2.5 cm) sample. The bullet penetration was approximately 0.5′′ (1.2 cm) with a slight ductile bulge in the back of the sample. The same sample 4′′×4′′×1′′ (10.1 cm×10.1 cm×2.5 cm) also passed multiple .40 caliber shots in which the bullet was not caught or ricocheted. It was sitting, slightly deformed at the base of the sample. In a 3⁄8′′ (1 cm) thickness this formulation passed three 12-gauge shotgun shots from 30 feet (9.1 m). Most of the shots were embedded in the surface of the sample.
All 9 mm shots were 115 grain, 1350 ft/sec (411 m/sec) muzzle velocity shot from a Ruger 9 mm pistol. All .40 caliber shots were shot at 987 ft/sec (300 m) muzzle velocity from a Smith & Wesson .40 caliber pistol. All 12-gauge shotgun shots were shot using a Remington 12-gauge shotgun using lead shot, heavy game load, at 1290 ft/sec (393 m/sec) muzzle velocity. Samples were shot attached to a 12′′ thick wooden block using Velcro® with no framing to hold the sample. Shooting was conducted outdoors at temperatures ranging from about 60° F. (15° C.) to about 80° F. (27° C.).
Example G
Elastoplastic Polyurethane Examples
Example G1
The weights of the components below were increased proportionately to provide sufficient quantity of material. The following reactants: 131.2 grams of DESMODUR W, 13.41 grams of trimethylolpropane, 26.015 grams of 1,5 pentanediol, and 81.712 grams Stahl KM-1733 1000 molecular weight polycarbonate diol based on hexanediol were mixed together, heated to 80° C. and degassed. Ten ppm of dibutyltindiacetate was added and mixed until the solution was homogeneous. The mixture was poured into a glass mold and cured for 48 hours at 290° F. (143° C.). After curing, the cell was allowed to cool to room temperature (25° C.) and the polymer was released from the mold. The polymer had a Young's Modulus of 215,000 psi (about 1482 MPa). The weight % urethane content was 23.4%. The molecular weight per crosslink was 2548 grams/mole. The weight % cyclic content was 32%.
An article of 6′′×6′′×1′′ (15.2 cm×15.2 cm×2.5 cm) thickness prepared from this polymer stopped a 9 mm, 125 grain, bullet shot an initial velocity of 1350 ft/sec (411 m/sec) (from 20 feet (6.1 m) distance by trapping the bullet in the polymer. The back of the bullet penetrated approximately 1⁄8′′ (0.3 cm) into the sample with a very small raise on the backside.
Example G2
The weights of the components below were increased proportionately to provide sufficient quantity of material. The following reactants: 131.2 grams of DESMODUR W, 13.41 grams of trimethylolpropane, 28.096 grams of 1,5 pentanediol, and 65.370 grams Stahl KM-1733 1000 molecular weight polycarbonate diol based on hexanediol were mixed together, heated to 80° C. and degassed. Ten ppm of dibutyltindiacetate was added and mixed until the solution was homogeneous. The mixture was poured into a glass mold and cured for 48 hours at 290° F. (143° C.). After curing, the cell was allowed to cool to room temperature (25° C.) and the polymer was released from the mold. The polymer had a Young's Modulus of 215,000 psi (about 1482 MPa). The weight % urethane content was 24.8%. The molecular weight per crosslink was 2404 grams/mole. The weight % cyclic content was 34%.
An article of 6′′×6′′×1′′ (15.2 cm×15.2 cm×2.5 cm) prepared from this polymer stopped a 9 mm, 125 grain, bullet shot an initial velocity of 1350 ft/sec (411 m/sec) from 20 feet (6.1 m) distance by trapping the bullet in the polymer. Four/fifths (4⁄5) of the length of the bullet penetrated the sample with the back of the bullet protruding out of the impacted surface approximately 1⁄8′′ (0.3 cm).
Example G3
The weights of the components below were increased proportionately to provide sufficient quantity of material. The following reactants: 131.2 grams of DESMODUR W, 13.41 grams of trimethylolpropane, 28.617 grams of 1,5-pentanediol, and 61.284 grams Stahl KM-1733 1000 molecular weight polycarbonate diol based on hexanediol were mixed together, heated to 80° C. and degassed. Ten ppm of dibutyltindiacetate was added and mixed until the solution was homogeneous. The mixture was poured into a glass mold and cured for 48 hours at 290° F. (143° C.). After curing, the cell was allowed to cool to room temperature (25° C.) and the polymer was released from the mold. The polymer had a Young's Modulus of 215,000 psi (about 1482 MPa). The weight % urethane content was 25.15%. The molecular weight per crosslink was 2369 grams/mole. The weight % cyclic content was 34.53%.
An article of 6′′×6′′×1′′ (15.2 cm×15.2 cm×2.5 cm) prepared from this polymer stopped a 9 mm, 125 grain, bullet shot an initial velocity of 1350 ft/sec (411 msec) from 20 feet (6.1 m) distance by trapping the bullet. Four/fifths (4⁄5) of the length of the bullet penetrated the sample with the back of the bullet protruding out of the impacted surface approximately 1⁄8′′ (0.3 cm).
Example L
Sample J
A polyurethane was prepared from the following components:















Equivalent

Weight
Weight


Component
Weight
Equivalents
(g)
(%)



















1,4-butanediol
45.1
0.63
28.4
14.1


PC-1733
407.6
0.07
28.5
14.2


TMP
44.7
0.30
13.4
6.7


Des W
131.2
1.0
131.2
65.1









The weights of the components in the table above were increased proportionately to provide sufficient quantity of material. The 1,4-butanediol, PC-1733 polycarbonate diol, TMP and DESMODUR W (preheated to 80° C.) were added to a glass reaction kettle preheated to a temperature of between 60° C.-80° C. before the addition of the components. The kettle was placed into a preheated heating mantle for about 20 minutes and heated to a temperature of approximately 121° C. while the formulation was stirred and outgassed under a vacuum pressure of −28 mmHg. Next, the mixture was cast between release coated 1′′×15′′×15′′ (2.5 cm×38.1 cm×38.1 cm) casting cell glass molds with a resin capacity of 3600 grams which had been preheated to a temperature of about 120° C. The mixture was cured for 2 hours at approximately 120° C., followed by 22 hours at 160° C. The mold was removed from the oven and the plastic released. A similar process was used to prepare a sheet of 1⁄8′′ thickness. The plastic sheet was then removed from the glass mold and cut into 2′′×2′′×1⁄8′′ (5.1 cm×5.1 cm×0.3 cm) samples for Gardner Impact testing. The Gardner Impact strength was 520 in-lbs (59 J). The Weight % Hard Segment was 55%, the Weight % Urethane was 29.276, and the Mc was 2015.3 g/mol.
Sample K
A polyurethane was prepared from the following components:















Equivalent





Component
Weight
Equivalents
Weight (g)
Weight (%)



















CHDM
72.1
0.80
57.7
24.6


PC-1733
407.6
0.10
40.8
17.4


TMP
44.7
0.10
4.5
1.9


Des W
131.2
1.0
131.2
56.0









The weights of the components in the table above were increased proportionately to provide sufficient quantity of material. The CHDM, PC-1733, TMP and DESMODUR W (preheated to 80° C.) were added to a glass reaction kettle preheated to a temperature of between 60° C.-80° C. before the addition of the components. The kettle was placed into a preheated heating mantle for about 20-25 minutes and heated to a temperature of approximately 121° C. while the formulation was stirred and outgassed under a vacuum pressure of −28 mmHg. Next, the mixture was cast between release coated 1′′×15′′×15′′ (2.5 cm×38.1 cm×38.1 cm) casting cell glass molds with a resin capacity of 3600 grams which had been preheated to a temperature of about 120° C. The mixture was cured for two hours at approximately 120° C., followed by 22 hours at 160° C. The mold was removed from the oven and the plastic released. The Wc was 34.7%, the Weight % Urethane was 25.33, and the Mc was 7094.5.
Sample L
A polyurethane was prepared from the following components:















Equivalent





Component
Weight
Equivalents
Weight (g)
Weight (%)



















CHDM
72.1
0.70
50.5
20.2


PC-1733
407.6
0.15
61.1
24.5


TMP
44.7
0.15
6.7
2.7


Des W
131.2
1.0
131.2
52.6









The weights of the components in the table above were increased proportionately to provide sufficient quantity of material. The CHDM, PC-1733, TMP and DESMODUR W (preheated to 80° C.) were added to a glass reaction kettle preheated to a temperature of between 60° C.-80° C. before the addition of the components. The kettle was placed into a preheated heating mantle for about 20-25 minutes up to a temperature of approximately 122° C. while the formulation was stirred and outgassed under a vacuum pressure of −28 mmHg. Next, the mixture was cast between release coated 1′′×15′′×15′′ (2.5 cm×38.1 cm×38.1 cm) casting cell glass molds with a resin capacity of 3600 grams which had been preheated to a temperature of about 120° C. The mixture was cured for two hours at approximately 120° C., followed by 22 hours at 160° C. The mold was removed from the oven and the plastic released. The Weight % Hard Segment was 57.1%, the Weight % Urethane was 25.2%, and the Mc was 4680.
Sample M
A polyurethane was prepared from the following components:















Equivalent





Component
Weight
Equivalents
Weight (g)
Weight (%)



















CHDM
72.1
0.70
50.5
21.8


PC-1733
407.6
0.10
40.8
17.6


TMP
44.7
0.20
8.9
3.9


Des W
131.2
1.0
131.2
56.7









The weights of the components in the table above were increased proportionately to provide sufficient quantity of material. The CHDM, PC-1733, TMP and DESMODUR W (preheated to 80° C.) were added to a glass reaction kettle preheated to a temperature of between 60° C.-80° C. before the addition of the components. The kettle was placed into a preheated heating mantle for about 20-25 minutes up to a temperature of approximately 121° C. while the formulation was stirred and outgassed under a vacuum pressure of −28 mmHg. Next, the mixture was cast between release coated 1′′×15′′×15′′ (2.5 cm×38.1 cm×38.1 cm) casting cell glass molds with a resin capacity of 3600 grams which had been preheated to a temperature of approximately 120° C. The mixture was cured for two hours at approximately 120° C., followed by 22 hours at 160° C. The mold was removed from the oven and the plastic released. The Weight % Hard Segment was 61.5%, the Weight % Urethane was 25.5, and the Mc was 3505.7.
Example R16
In a glass kettle under nitrogen blanket with stirring, were charged 28.29 weight % 1,10-decanediol (101.2 equivalent wt.); 5.69 weight % TMP (44.0 equivalent wt.); and 56.54% DESMODUR W (131.2 equivalent wt.) and 9.48 weight % PC-1733 or KM-1733 (a 1000 MW carbonate diol made from hexanediol and diethylcarbonate, and commercially available from ICI) (428 equivalent wt.) which was preheated to a temperature of 80° C. The mixture was heated to a temperature of 115° C.
The mixture was then degassed and cast into a 12′′×13′′×0.125′′ (30 cm×33 cm×0.3 cm) casting cell which had been preheated to a temperature of 121° C. The filled cell was then cured in an oven for a period of 48 hours at 121° C.
Example Z1
A polyurethane was prepared from the following components:















Equivalent





Component
Weight
Equivalents
Weight (g)
Weight (%)



















Des W
131.2
1.0
131.2
51.9


PC-1733
414.3
0.2
82.9
32.8


TMP
44.7
0.7
31.3
12.4


CHDM
72.1
0.1
7.2
2.9









The PC-1733 and DESMODUR W (each preheated to 80° C.) were added to a glass reaction kettle preheated to a temperature of about 80° C. before the addition of the components. The kettle was placed into a preheated heating mantle and heated to a temperature of approximately 110° C. for less than one hour while the formulation was stirred and outgassed under a vacuum pressure of 28 mmHg. The temperature of the mixture peaked near 140° C. after about 1⁄2 hour, and returned to a temperature of about 110° C. within an hour. The temperature of the reactants was maintained at about 110° C. for about 1 hour. The reaction product (isocyanate functional prepolymer) was stored in a sealed glass jar for about 24 hours in an oven at a temperature of about 75° C. to about 80° C.
The prepolymer was placed in a glass reaction kettle preheated to a temperature of about 80° C. before the addition of the components. The CHDM and TMP were each individually preheated to a temperature of about 80° C., and added to the prepolymer in the reaction kettle. The reaction kettle was placed in a heating mantle set at 50-60% power and stirred while heating under vacuum at a pressure of 20 mmHg until the mixture reached about 120° C. (about 30 minutes).
Next, the mixture was cast between release coated 15′′×15′′×0.125′′ (38.1 cm×38.1 cm×0.3 cm) casting cell glass molds with a resin capacity of 420 grams each which had been preheated to a temperature of about 120° C. The mixture was cured for two hours at approximately 120° C., followed by 22 hours at 160° C. The molds were removed from the oven and the plastic sheets were released.
The plastic sheets were cut into 6′′×2′′×1⁄8′′ (15.2 cm×5.1 cm×0.3 cm) to provide samples for determination of crack propagation resistance (K-Factor), glass transition temperature, and coupons for tensile testing and determining stress craze resistance. The K-factor crack propagation resistance was 2,873 lb/in3/2. The glass transition temperature was 94° C. The modulus of elasticity was 283,000 psi, the tensile strength at yield was 10,600 psi and the elongation at break was 6.5%.
Example Z2
A poly(ureaurethane) was prepared as follows:
Prepolymer Components:















Equivalent





Component
Weight
Equivalents
Weight (g)
Weight (%)



















DesW
131.2
1
131.2
61.29


PC-1733
414.33
0.20
82.87
38.71









A prepolymer was prepared by preheating DesW to 80° C. and adding the preheated DesW to a glass reaction kettle (preheated to 80 C before the addition of the components). The 1st aliquot of a polycarbonate diol PC-1733 (0.1 equivalents) which had also been preheated to 80° C. was added directly into the same reaction kettle. The kettle was then placed into a preheated heating mantle with the controller set to 110° C. and the mixture was stirred under a nitrogen blanket. The temperature of the mixture was  ̃74° C. when mixing was started. The mixture was heated and stirred 21⁄2 hours reaching a maximum temperature of  ̃115° C. in  ̃2 hours. The heating mantle controller was then reduced to a temperature of 90° C. while stirring continued under the nitrogen blanket. In  ̃85 minutes the mixture had cooled to  ̃94° C. and the 2nd aliquot of PC-1733 was added while stirring. After 30 minutes the mantle controller was raised to 110° C. and stirring continued for another 4 hours then stirring was stopped, the nitrogen turned off, and the kettle was removed from the mantle. The mixture was then poured into a glass jar and sealed loosely with a lid and placed into a 90° C. oven for storage. The prepolymer was clear and slightly viscous when removed from stirring at  ̃111° C.















Equivalent





Component
Weight
Equivalents
Weight (g)
Weight (%)



















DesW
131.2
1
131.2
52.69


PC-1733
414.33
0.20
82.87
33.28


DI H2O
9.0
0.10
0.90
0.36


CHDM
72.11
0.10
7.21
2.90


TMP
44.70
0.60
26.82
10.77









The 1 equivalent DesW/0.2 equivalents PC-1733 prepolymer was preheated to 80° C. and added to a glass reaction kettle (preheated to 80° C. before the addition of the components). The 0.1 equivalent of deionized H2O was added to the same kettle. The kettle was placed into a preheated heating mantle with the controller set to 80° C. and the mixture was stirred under a nitrogen blanket. The temperature of the mixture was about 76° C. when mixing was started. The mixture was heated and stirred 11⁄2 hours, then the CHDM and TMP (both preheated to 80° C.) were combined and added to the mixture while stirring. The mantle temperature was then set to 50% of its maximum output. Ten minutes after the CHDM and TMP were added, the nitrogen blanket was turned off. The mixture was outgassed for 20 minutes at a vacuum pressure of 29 inHg, after which the mixture had reached a temperature of 122° C. The stirring was stopped at this point, the vacuum was released, and the kettle removed from the heating mantle. The mixture was then poured into a 15′′×15′′×1⁄8′′ (38.1 cm×38.1 cm×0.3 cm) release coated glass cell preheated to 121° C. (250° F.). The cell was cured 2 hours at 121° C. (250° F.) followed by 22 hours at 160° C. (320° F.). Samples were prepared from the cured polymer as described above. The test data is reported below:
Modulus of elasticity=269,800 psi
Tensile strength at break=9,311 psi
Elongation at break=7%
Tg=82° C.
Mean failure energy in Gardner impact test=89 in-lb
K-factor=3,810 lb×inch−3/2 
Example Z3
A polyurethane was prepared as follows:
Prepolymer Components:















Equivalent





Component
Weight
Equivalents
Weight (g)
Weight (%)



















DesW
131.2
1
131.2
72.95


PC-1733
414.33
0.1
41.43
23.04


CHDM
72.11
0.1
7.21
4.01









The weight amounts in the table were proportionately increased and a batch of the prepolymer was prepared as follows: DesW (preheated to 70° C.) was added to an epoxy phenolic lined 5 gallon steel pail. The PC-1733 (polycarbonate diol from Stahl) was preheated to 80° C. The PC-1733 (0.1 equivalents) was added directly into the same pail as the DesW. The pail was placed in an exhaust hood and covered with a lid that had provisions for an overhead stirrer, nitrogen feed, and a thermocouple for monitoring temperatures. The mixture was stirred vigorously forming a vortex with the overhead stirrer under a nitrogen blanket (the starting temperature was approximately 64° C.). The mixture was stirred with the heating controller set to 90° C. for approximately 70 minutes. The controller setting was then increased to 110° C. and the mixture was allowed to stir for 90 minutes. The controller setting was reduced to 90° C. and the mixture stirred and allowed to cool to approximately 91° C. in 30 minutes. The CHDM (1,4-cyclohexanedimethanol) was then added while stirring and stirred for 1⁄2 hour with the controller set at 90° C. The controller was then set to 110° C. and the mixture was stirred under the nitrogen blanket for an additional 1 hour 40 minutes. The heat band was then removed the nitrogen blanket turned off and stirring was stopped. A normal lid was placed loosely over the mixture after capping with nitrogen and then was siphoned directly in the prepolymer tank of the Max machine and held at 70° C. overnight awaiting casting use.
















Equivalent


Weight (%)
Prepolymer


Component
Weight
Equivalents
Weight (g)
Total Formula
Weight %




















DesW in prepolymer
131.2
1
131.2

72.95


PC-1733 in prepolymer
414.33
0.1
41.43

23.04


CHDM in prepolymer
72.11
0.1
7.21

4.01


prepolymer totals:



78.43
100


TMP
44.7
0.3
13.41
5.85


CHDM
72.11
0.50
36.06
17.72









A polymer was made (0.1 eq PC-1733, 0.6 eq CHDM/0.3 eq TMP/1.0 eq DesW) using a Max urethane processor as described above with the use of a prepolymer (1 eq DesW/0.1 eq PC-1733 (a carbonate diol from Stahl)/0.1 eq CHDM). The prepolymer was preheated to 120° C. and loaded into the A1 tank. The remaining CHDM (1,4-cyclohexanedimethanol) and TMP (trimethylolpropane) were preheated to 80° C., then combined at the proper ratio and added to the B2 polyol tank. Both tanks were then heated to 120° C. while stirring under vacuum for approximately 1 hour until the components had individually reached the set point temperature. Both materials were then recirculated through the Max machine lines for approximately 1 hour to make sure that they are uniformly heated throughout the system. The components were then calibrated individually to ensure the proper delivery rate (1176.43 g/min. for the prepolymer and 323.57 g/min. for the polyol mix). The mixture was passed through the 250 cc heated mixing head that was set to 120° C. and the stir rate at approximately 3000 RPM. The mixture was cast into a glass jar from an elbow shaped tip directly attached to the mix head. The mixture cleared immediately out of the mix head. The material was then cast into two 15×15×1⁄8′′ (38.1 cm×38.1 cm×0.3 cm) release treated glass cells that had been preheated to 121° C. They were then cured 2 hours at 121° C. followed by 22 hours at 160° C. The samples were allowed to cool and then released from the glass cells. The samples cured clearly and without any cracking.
Example Z4
A polyurethane was prepared from the following components:















Equivalent





Component
Weight
Equivalents
Weight (g)
Weight (%)



















DesW
131.2
1
131.2
60.39


PDO
52.03
0.6
31.22
14.37


TMP
44.7
0.3
13.41
6.17


PC-1733
414.33
0.10
41.43
19.07









A polymer was made (0.1 eq PC-1733, 0.6 eq PDO/0.3 eq TMP/1.0 eq DesW) using a Max urethane processor without the use of a prepolymer. DesW (preheated to 70° C.) was loaded into the tank used typically for prepolymer while the PC-1733 (a carbonate diol from Stahl), PDO (1,5-pentanediol) and TMP (trimethylolpropane) were all preheated to 80° C. then combined at the proper ratio and added to the polyol tank. Both tanks were heated to 120° C. while stirring under vacuum for approximately 1 hour until the components had individually reached the set point temperature. Both materials were recirculated through the Max machine lines for approximately 1 hour to make sure that they are uniformly heated throughout the system. Both components were calibrated individually to ensure the proper delivery rate (905.82 g/min. for the DesW and 594.18 g/min. for the polyol mix). The mixture was passed through the 250 cc heated mixing head that was set to 120° C. and the stir rate at approximately 3000 RPM. The mixture was cast into a glass jar from an elbow shaped tip directly attached to the mix head. The mixture cleared immediately out of the mix head but exothermed too rapidly and the material gelled within a few seconds. The gelled material showed heavy striation and large bubbles generated by the high exotherm.
Example Z5
A polyurethane was prepared as follows:
Components:















Equivalent





Component
Weight
Equivalents
Weight (g)
Weight (%)



















Des W
131.2
1.0
131.2
51.9


PC-1733
414.3
0.1
41.4
16.6


PC-1667
391.8
0.1
39.2
15.7


TMP
44.7
0.7
31.3
12.5


CHDM
72.1
0.1
7.2
2.9









A prepolymer was prepared by adding PC-1733, PC-1667 and DESMODUR W (each preheated to 80° C.) to a glass reaction kettle preheated to a temperature of about 80° C. before the addition of the components. The kettle was placed into a preheated heating mantle and heated to a temperature of approximately 110° C. for less than one hour while the formulation was stirred and outgassed under a vacuum pressure of −28 mmHg. The temperature of the mixture peaked near 128° C. after about 1⁄2 hour, and returned to a temperature of about 110° C. within an hour. The temperature of the reactants was maintained at about 110° C. for about 1 hour. The reaction product (isocyanate functional prepolymer) was stored in a sealed glass jar for about 24 hours in an oven at a temperature of about 75° C. to about 90° C.
The prepolymer was placed in a glass reaction kettle preheated to a temperature of about 80° C. before the addition of the components. To prepare the polymer, CHDM and TMP were each individually preheated to a temperature of about 80° C., and added to the prepolymer in the reaction kettle. The reaction kettle was placed in a heating mantle set at 50-60% power and the mixture was stirred while heating under vacuum at a pressure of 29 mm Hg until the mixture reached about 125° C. (about 30 minutes).
Next, the mixture was cast between release coated 15′′×15′′×0.125′′ (38.1 cm×38.1 cm×0.3 cm) casting cell glass molds with a resin capacity of 420 grams each which had been preheated to a temperature of about 120° C. The mixture was cured for two hours at approximately 120° C., followed by 22 hours at 160° C. The mold was removed from the oven and the plastic released.
The plastic sheet was cut into 6′′×2′′×0.125′′ (15.2 cm×5.1 cm×0.3 cm) samples for the determination of crack propagation resistance (K-Factor), and coupons for tensile tests. The K Factor crack propagation resistance was 1085 lb/in3/2. The tensile strength at yield was 10,500 psi, the modulus of elasticity was 342,000 psi, and the elongation at break was 4.6%.
Example Z6
A polyurethane was prepared as follows:
Components:




















Weight to



Equivalent
Equiv-
Weight
Weight
Measure


Component
Weight
alents
(g)
(%)
(g)




















Desmodur W
131.2
1
131.2
61.589
277.15


ETERNACOLL ®
482.66
0.025
12.067
5.664
25.48


UH-100W


polycarbonate diol


Trimethylolpropane
44.7
0.02
0.894
0.420
1.89


(TMP)


1,4 cyclohexane-
72.11
0.955
68.865
32.327
145.47


dimethanol


(CHDM)









The DesW (preheated to 70° C.) was added to a glass reaction kettle (preheated to 80° C. before the addition of the components). The ETERNACOLL® UH-100W 1,6-hexanediol based polycarbonate diol (molecular weight of 1000, OH value of from 100-120 KOH mg/PCD g, melting point 45° C., viscosity 360-460 cP @ 75° C.) from UBE Industries, the TMP, and the CHDM were each preheated to 80° C., weighed, and added to the DesW in the same kettle. The kettle was then placed into a preheated heating mantle set to 40% power and the mixture was stirred. The temperature of the mixture was  ̃60° C. when mixing was started. Once the temperature of the mixture reached 80° C. in  ̃22 minutes it was placed under a vacuum pressure of −29 mm Hg. The mixture was heated and stirred until reaching a temperature of 108° C. in  ̃10 minutes. The vacuum was released and the reaction kettle was removed from the heating mantle. The mixture was then poured into a 15′′×15′′×1⁄8′′ release treated glass mold that had been preheated to  ̃120° C. The mold was then cured 2 hours at 120° C., followed by 22 hours at 160° C. The mold was allowed to cool slowly then removed from the oven and the plastic was released.
Gardner impact was performed on a few samples after standing at room temperature for three days and again at eleven days. The results, as ‘high pass’, were 48 inch·pounds at three days and 352 inch·pounds at eleven days. The improvement in Gardner impact over time most likely indicates the formation of hard and soft domains within the polymer.
Example Z7
A polyurethane was prepared as follows:
Components:




















Weight to



Equivalent
Equiv-
Weight
Weight
Measure


Component
Weight
alents
(g)
(%)
(g)




















Desmodur W
131.2
1
131.2
65.564
295.04


ETERNACOLL ®
482.66
0.025
12.067
6.030
27.14


UH-100W


polycarbonate diol


Trimethylolpropane
44.7
0.02
0.894
0.447
2.01


(TMP)


1,4 Butanediol
45.06
0.47750
21.516
10.752
48.38


(BDO)


1,4 cyclohexane-
72.11
0.47750
34.433
17.207
77.43


dimethanol


(CHDM)









The DesW (preheated to 70° C.) was added to a glass reaction kettle (preheated to 80° C. before the addition of the components). The UH-100W polycarbonate diol, the TMP, the BDO, and the CHDM were each preheated to 80° C., weighed, and were added to the DesW in the same kettle. The kettle was then placed into a preheated heating mantle set to 40% power and the mixture was stirred. The temperature of the mixture was  ̃43° C. when mixing was started. Once the temperature of the mixture reached 80° C. in approximately 25 minutes it was placed under a vacuum pressure of −29 mm Hg. The mixture was heated and stirred until reaching a temperature of 111° C. in 10 minutes. The vacuum was released and the reaction kettle was removed from the heating mantle. The mixture was then poured into a 15′′×15′′×1⁄8′′ release treated glass mold that had been preheated to  ̃120° C. The mold was then cured 2 hours at 120° C., followed by 22 hours at 160° C. The mold was allowed to cool slowly then removed from the oven and the plastic was released.
Gardner impact was performed on a few samples after standing at room temperature for three days and again at eleven days. The results, as “high pass”, were 44 inch·pounds at three days and 352 inch·pounds at eleven days. The improvement in Gardner impact over time most likely indicates the formation of hard and soft domains within the polymer.
Example Z8
A polyurethane was prepared as follows:
Components:
















Equivalent

Weight
Weight
Weight to


Component
Weight
Equivalents
(g)
(%)
measure




















Desmodur W
131.2
1
131.2
62.308
280.39


1,4 cyclohexanedimethanol
72.11
0.875
63.096
29.965
133.58


(CHDM)


H3PO4 0.1% in CHDM




1.26


ETERNACOLL ® UH-100W
482.66
0.02445
11.8
5.604
25.22


polycarbonate diol


Trimethylolpropane (TMP)
44.7
0.1
4.47
2.123
9.55









The above formulation was made by incorporating a small amount (50 ppm to the amount of UH-100W) of crystalline phosphoric acid (0.1% H3PO4 dissolved in CHDM) to dampen the reactivity of the added UH-100W polycarbonate diol. The CHDM used to dissolve the phosphoric acid is compensated for in the calculation for the CHDM added. The DesW (preheated to 70° C.) was added to a glass reaction kettle (preheated to 80° C. before the addition of the components). The CHDM, H3PO4 0.1% in CHDM, the UH-100W polycarbonate diol and the TMP (each preheated to 80° C.) were weighed directly into the DesW in the same kettle. The kettle was then placed into a preheated heating mantle set to 50% power and the mixture was stirred. The temperature of the mixture was  ̃53° C. when mixing was started under a vacuum pressure of −30 mm Hg. The mixture was heated and stirred until reaching a temperature of 117° C. in  ̃20 minutes. The vacuum was released and the reaction kettle was removed from the heating mantle. The mixture was then poured into a 15′′×15′′×1⁄8′′ release treated glass mold that had been preheated to  ̃120° C. The mold was then cured 2 hours at 120° C., followed by 22 hours at 160° C. The mold was allowed to cool slowly, then removed from the oven and the plastic was released.
The sample was allowed to age at room temperature. After 3 days of aging, and again after 22 days of aging, four 2′′×2′′ samples were tested for Gardner impact, using a screening method with only a few samples. The sample at 3 days aging had a maximum pass of 224 inch·pounds. After 22 days, a sample had a maximum pass of 192 inch·pounds.
Example Z9
A polyurethane was prepared as follows:
Components:
















Equivalent



Weight to


Component
Weight
Equivalents
Weight (g)
Weight (%)
measure




















Desmodur W
131.2
1
131.2
59.484
267.68


1,4 cyclohexanedimethanol
72.11
0.850
61.294
27.790
122.65


(CHDM)


H3PO4 0.1% in CHDM




2.41


ETERNACOLL ® UH-
482.66
0.0489
23.60
10.70
48.15


100W polycarbonate diol


Trimethylolpropane (TMP)
44.7
0.1
4.47
2.027
9.12









The above formulation was made by incorporating a small amount (50 ppm to the amount of UH-100W) of crystalline phosphoric acid (0.1% H3PO4 dissolved in CHDM) to dampen the reactivity of the UH-100W polycarbonate diol. The CHDM used to dissolve the phosphoric acid is compensated for in the calculation for the CHDM added. The DesW (preheated to 70° C.) was added to a glass reaction kettle (preheated to 80° C. before the addition of the components). The CHDM, H3PO4 0.1% in CHDM, the UH-100W polycarbonate diol and the TMP, (all preheated to 80° C.) were weighed directly into to the DesW in the same kettle. The kettle was then placed into a preheated heating mantle set to 50% power and the mixture was stirred. The temperature of the mixture was  ̃60° C. when mixing was started under a vacuum pressure of −30 mm Hg. The mixture was heated and stirred until reaching a temperature of 118° C. in  ̃15 minutes. The vacuum was released and the reaction kettle was removed from the heating mantle. The mixture was then poured into a 15′′×15′′×1⁄8′′ release treated glass mold that had been preheated to  ̃120° C. The mold was then cured for 2 hours at 120° C., followed by 22 hours at 160° C. The mold was allowed to cool slowly then removed from the oven and the plastic was released.
The sample was allowed to age at room temperature. After 5 days of aging, and again after 20 days of aging, four 2′′×2′′ samples were tested for Gardner impact, using a screening method with only a few samples. The sample at 5 days aging had a maximum pass of 224 inch·pounds. After 20 days, the sample had a maximum pass of 448 inch·pounds.
Hypothetical Example
The following Example is a hypothetical example.
Example A
A polyurethane of the present invention can be prepared according to the following method. First, a prepolymer can be prepared from the following components:
Prepolymer Components:
















Equivalent



Weight to


Component
Weight
Equivalents
Weight (g)
Weight (%)
measure




















DesW
131.2
1
131.2
75.68
13244


UH-100W
482.66
0.05
24.133
13.921
2436.175


CHDM
72.11
0.25
18.0275
10.431
(1819.825 − 121.687) =







11698.138


Totals


172.3605
100
17378.313


H3PO4 0.1% in




121.809


CHDM




(50 ppm







based on







UH100W)









The prepolymer can be prepared as follows: DesW (preheated to 70° C.) can be added to an epoxy phenolic lined 5 gallon steel pail. The pail can be placed in an exhaust hood and covered with a lid that has provisions for an overhead stirrer, nitrogen feed, and a thermocouple for monitoring temperatures. The mixture can be stirred vigorously forming a vortex with the overhead stirrer under a nitrogen blanket. The mixture can be stirred with the heating controller set to 90° C. until the DesW reaches 90° C. The UH-100W (polycarbonate diol from UBE) can be preheated to 80° C. The UH-100W (0.05 equivalents) can be added directly into the same pail as the DesW while stirring and stirred for 1⁄2 hour with the controller set at 90° C. The controller setting can be increased to 110° C. and the mixture allowed to stir for 90 minutes. The controller setting can be reduced to 90° C. and the mixture stirred and allowed to cool to approximately 90° C. The CHDM (1,4-cyclohexanedimethanol) and the H3PO4 0.1% in CHDM can be combined and preheated to 80° C. They can be added to the mixture while stirring and stirred for 1⁄2 hour with the controller set at 90° C. The controller can be set to 110° C. and the mixture stirred under the nitrogen blanket for an additional 2 hours. The heat band can be removed, the nitrogen blanket turned off and the stirring stopped. A normal lid can be placed loosely over the mixture after capping with nitrogen and then siphoned directly in the prepolymer tank of the Max machine and held at 70° C. overnight awaiting casting use.




















Weight %
Weight %




Equivalent

Weight
in
Total
Weight to


Component
Weight
Equivalents
(g)
Prepolymer
Formula
measure





















DesW
131.2
1
131.2
75.68
59.34



UH-100W
482.66
0.05
24.133
13.921
10.92



CHDM in
72.11
0.25
18.0275
10.399
8.15



prepolymer








Prepolymer


173.3605
100
78.41
1176.15


Totals








CHDM
72.11
0.6
43.266

19.57
293.55


TMP
44.7
0.1
4.47

2.02
30.3


Total

2
221.0965

100
1500





*Note:


The prepolymer contains 50 ppm H3PO4 based on the amount of UH-100W






The prepolymer made from one equivalent DesW, 0.05 equivalents UH-100W (polycarbonate diol from UBE), and 0.25 equivalents 1,4 cyclohexanedimethanol (CHDM) can be preheated to 120° C. and placed directly into the A1 tank of a Max Urethane Processor. The remaining CHDM and TMP needed to complete the formulation can be preheated to 80° C. to melt and then combined in the proper ratio and placed in the B2 tank of the Max machine. Both tanks can be stirred and heated to 125° C. under vacuum and circulated through the lines for a minimum of 2 hours. Each tank can be calibrated to insure the proper flow rates of 1175.25 g/min for A1 and 324.75 g/min for the B2 tank. The materials can be passed through a 250 cc heated mix head stirring at approximately 3000 RPM. The material can be flowed through a heat traced line through an external filter then directly into an oven containing casting cells. The 15′′×15′′×1⁄8′′ release treated glass casting cells can be preheated to 121° C. (250° F.) for a minimum of 2 hours prior to casting. The cells can be cured for 2 hours at 121° C. (250° F.), then ramped to 160° C. (320° F.) in 20 minutes and held at 160° C. (320° F.) for 22 hours. The cells can be allowed to cool overnight and the cast parts released from the cells.

It will be appreciated by those skilled in the art that changes could be made to the embodiments described above without departing from the broad inventive concept thereof. It is understood, therefore, that this invention is not limited to the particular embodiments disclosed, but it is intended to cover modifications which are within the spirit and scope of the invention, as defined by the appended claims.

## Claims

1. A polyurethane comprising a reaction product of components comprising:
(a) at least one isocyanate functional prepolymer comprising a reaction product of:
(1) about 1 equivalent of at least one polyisocyanate; and
(2) about 0.01 to about 0.5 equivalent of at least one polycarbonate polyol based upon the about 1 equivalent of the at least one polyisocyanate; and
(b) about 0.01 to about 1 equivalent of at least one polyol having at least 3 hydroxyl groups based upon the about 1 equivalent of the at least one polyisocyanate,
wherein the components further comprise about 0.01 to about 0.5 equivalent of water based upon the about 1 equivalent of the at least one polyisocyanate.

2. The polyurethane according to claim 1, wherein the water is reacted with the polyisocyanate and polycarbonate polyol to form an isocyanate functional ureaurethane prepolymer.

3. A polyurethane comprising a reaction product of components comprising:
(a) about 1 equivalent of at least one polyisocyanate;
(b) about 0.01 to about 0.5 equivalent of at least one polycarbonate polyol based upon the about 1 equivalent of the at least one polyisocyanate; and
(c) about 0.01 to about 1 equivalent of at least one polyol having at least 3 hydroxyl groups based upon the about 1 equivalent of the at least one polyisocyanate, and
(d) about 0.01 to about 0.5 equivalent of water based upon the about 1 equivalent of the at least one polyisocyanate.

4. A process for preparing a polyurethane article comprising:
(a) heating a mixture of about 1 equivalent of at least one polyisocyanate and about 0.01 to about 0.5 equivalent of at least one polycarbonate polyol based upon the about 1 equivalent of the at least one polyisocyanate, to a temperature of about 110° C. to about 130° C. for at least about an hour to form a reaction product;
(b) mixing the reaction product (a) with about 0.01 to about 1 equivalent of at least one polyol having at least 3 hydroxyl groups based upon the about 1 equivalent of the at least one polyisocyanate until the mixture reaches a temperature of at least about 110° C. to about 130° C., optionally by heating if necessary;
(c) casting the reaction product into a mold preheated to a temperature of at least about 100° C. to about 130° C.; and
(d) curing the reaction product at a first predetermined temperature of about 100° C. to about 120° C. for at least about 0.5 hours; and then at a second predetermined temperature of about 140° C. to about 180° C. for about 15 to about 30 hours,
wherein the at least one polyol of step (b) is selected from the group consisting of glycerol, glycerin, tetramethylolmethane, trimethylolmethane, trimethylolpropane, erythritol, pentaerythritol.

5. The process of claim 4, wherein the polyisocyanate of step (a) is selected from the group consisting of diisocyanates, triisocyanates, dimers, trimers and mixtures thereof.

6. The process of claim 4, wherein the polycarbonate polyol of step (a) is prepared from hexanediol and dialkyl carbonate.

7. The process of claim 4, wherein the at least one polyol of step (b) is trimethylolpropane.

8. The process of claim 4, wherein step (b) further comprises mixing about 0.001 to about 0.5 equivalent of at least one polyol different from the at least one polyol of step (b), based upon the about 1 equivalent of the at least one polyisocyanate, with the reaction product (a) and the at least one polyol of step (b).

9. The process of claim 8, wherein the at least one polyol different from the at least one polyol of step (b) is a diol.

10. The process of claim 8, wherein the at least one polyol different from the at least one polyol of step (b) is selected from the group consisting of ethylene glycol, diethylene glycol, triethylene glycol, tetraethylene glycol, 1,2-ethanediol, propanediol, butanediol, pentanediol, hexanediol, heptanediol, octanediol, nonanediol, decanediol, dodecane diol, sorbitol, mannitol, cyclopentanediol, 1,4-cyclohexanediol, cyclohexanedimethanol, 1,4-benzenedimethanol, xylene glycol, hydroxybenzyl alcohol, dihydroxytoluene bis(2-hydroxyethyl) terephthalate, 1,4-bis(hydroxyethyl)piperazine, N,N′,bis(2-hydroxyethyl)oxamide and mixtures thereof.

11. The process of claim 4, wherein the mixture of step (a) and/or step (b) further comprises one or more polyurethane polyols, acrylamides, polyvinyl alcohols, hydroxy functional acrylates, hydroxy functional methacrylates, allyl alcohols, dihydroxy oxamides, dihydroxyamides, dihydroxy piperidines, dihydroxy phthalates, dihydroxyethyl hydroquinones and mixtures thereof.

12. The process of claim 4, comprising:
(a) heating a mixture of about 1 equivalent of at least one polyisocyanate and about 0.01 to about 0.5 equivalent of at least one polycarbonate polyol based upon the about 1 equivalent of the at least one polyisocyanate, to a temperature of about 110° C. to about 130° C. for at least about an hour to form a reaction product;
(b) mixing the reaction product (a) with about 0.5 to about 0.8 equivalent of trimethylolpropane based upon the about 1 equivalent of the at least one polyisocyanate and about 0.1 to about 0.5 equivalent of butanediol, pentanediol or cyclohexane dimethanol based upon the about 1 equivalent of the at least one polyisocyanate until the mixture reaches a temperature of at least about 110° C. to about 130° C., optionally by heating if necessary;
(c) casting the reaction product into a mold preheated to a temperature of at least about 100° C. to about 130° C.; and
(d) curing the reaction product at a first predetermined temperature of about 100° C. to about 120° C. for at least about 0.5 hours; and then at a second predetermined temperature of about 140° C. to about 180° C. for about 15 to about 30 hours.

13. The process of claim 4, comprising:
(a) heating a mixture of about 1 equivalent of at least one polyisocyanate and about 0.2 equivalent of at least one polycarbonate polyol based upon the about 1 equivalent of the at least one polyisocyanate, to a temperature of about 110° C. to about 130° C. for at least about an hour to form a reaction product;
(b) mixing the reaction product (a) with about 0.7 equivalent of trimethylolpropane based upon the about 1 equivalent of the at least one polyisocyanate and about 0.1 equivalent of butanediol, pentanediol or cyclohexane dimethanol based upon the about 1 equivalent of the at least one polyisocyanate until the mixture reaches a temperature of at least about 110° C. to about 130° C., optionally by heating if necessary;
(c) casting the reaction product into a mold preheated to a temperature of at least about 100° C. to about 130° C.; and
(d) curing the reaction product at a first predetermined temperature of about 100° C. to about 120° C. for at least about 0.5 hours; and then at a second predetermined temperature of about 140° C. to about 180° C. for about 15 to about 30 hours.

14. A polyurethane article prepared by a process comprising:
(a) heating a mixture of about 1 equivalent of at least one polyisocyanate and about 0.01 to about 0.5 equivalent of at least one polycarbonate polyol based upon the about 1 equivalent of the at least one polyisocyanate, to a temperature of about 110° C. to about 130° C. for at least about an hour to form a reaction product;
(b) mixing the reaction product (a) with about 0.01 to about 1 equivalent of at least one polyol having at least 3 hydroxyl groups based upon the about 1 equivalent of the at least one polyisocyanate until the mixture reaches a temperature of at least about 110° C. to about 130° C., optionally by heating if necessary;
(c) casting the reaction product into a mold preheated to a temperature of at least about 100° C. to about 130° C.; and
(d) curing the reaction product at a first predetermined temperature of about 100° C. to about 120° C. for at least about 0.5 hours; and then at a second predetermined temperature of about 140° C. to about 180° C. for about 15 to about 30 hours,
wherein the at least one polyol of step (b) is selected from the group consisting of glycerol, glycerin, tetramethylolmethane, trimethylolmethane, trimethylolpropane, erythritol, pentaerythritol.

15. The polyurethane article of claim 14 prepared by a process comprising:
(a) heating a mixture of about 1 equivalent of at least one polyisocyanate and about 0.01 to about 0.5 equivalent of at least one polycarbonate polyol based upon the about 1 equivalent of the at least one polyisocyanate, to a temperature of about 110° C. to about 130° C. for at least about an hour to form a reaction product;
(b) mixing the reaction product (a) with about 0.5 to about 0.8 equivalent of trimethylolpropane based upon the about 1 equivalent of the at least one polyisocyanate and about 0.1 to about 0.5 equivalent of butanediol, pentanediol or cyclohexane dimethanol based upon the about 1 equivalent of the at least one polyisocyanate until the mixture reaches a temperature of at least about 110° C. to about 130° C., optionally by heating if necessary;
(c) casting the reaction product into a mold preheated to a temperature of at least about 100° C. to about 130° C.; and
(d) curing the reaction product at a first predetermined temperature of about 100° C. to about 120° C. for at least about 0.5 hours; and then at a second predetermined temperature of about 140° C. to about 180° C. for about 15 to about 30 hours.

16. The polyurethane article of claim 14 prepared by a process comprising:
(a) heating a mixture of about 1 equivalent of at least one polyisocyanate and about 0.2 equivalent of at least one polycarbonate polyol based upon the about 1 equivalent of the at least one polyisocyanate, to a temperature of about 110° C. to about 130° C. for at least about an hour to form a reaction product;
(b) mixing the reaction product (a) with about 0.7 equivalent of trimethylolpropane based upon the about 1 equivalent of the at least one polyisocyanate and about 0.1 equivalent of butanediol, pentanediol or cyclohexane dimethanol based upon the about 1 equivalent of the at least one polyisocyanate until the mixture reaches a temperature of at least about 110° C. to about 130° C., optionally by heating if necessary;
(c) casting the reaction product into a mold preheated to a temperature of at least about 100° C. to about 130° C.; and
(d) curing the reaction product at a first predetermined temperature of about 100° C. to about 120° C. for at least about 0.5 hours; and then at a second predetermined temperature of about 140° C. to about 180° C. for about 15 to about 30 hours.