ACTIVE HYDROGEN-CONTAINING COMPOSITIONS CONTAINING A SECONDARY AMINE-TERMINATED ADDUCT OF A PRIMARY AMINE COMPOUND AND A POLYEPOXIDE AND POLYUREA-CONTAINING POLYMERS PREPARED THEREFROM

Abstract: Active hydrogen-containing compositions comprising a relatively high equivalent weight compound having hydroxyl and/or amine groups and a secondary amine-terminated adduct of a primarily monofunctional primary amine compound and a polyepoxide and polyurea-containing polymers prepared by reacting the active hydrogen-containing compositions with polyisocyanates. Polymers of this invention have high impact strength, high flexural modulus and high heat distorsion temperatures. These polymers are especially useful as structural polymers as well as static or dynamic elastomers.

Description: ACTIVE HYDROGEN-CONTAINING COMPOSITIONS CONTAINING A SECONDARY AMINE-TERMINATED ADDUCT OF A PRIMARY AMINE COMPOUND AND A POLYEPOXIDE AND POLYUREA-CONTAINING POLYMERS PREPARED THEREFROM This invention relates to active hydrogen- -containing compositions comprising a relatively high equivalent weight compound having hydroxyl and/or amine groups and a secondary amine-terminated adduct of a primarily monofunctional primary amine compound and a polyepoxide and to polyurea-containing polymers prepared by reacting the active hydrogen-containing compositions with polyisocyanates. In the preparation of polyurea and/or poly- urethane polymers it is often desirable to prepare a polymer having the properties of high heat distortion temperature, good impact strength and high modulus. In practice, however, it has often been found that opti¬ mization of one of these properties tends to cause a decrease in one or more of the others. For example, high heat distortion polymers have often been found to be lacking in impact strength. Similarily, high modu¬ lus polymers have often been found to be lacking in both heat distortion and impact properties. Accord¬ ingly, it would be desirable to provide a polyurea and/or polyurethane polymer having good heat distor¬ tion, modulus and impact strength. This invention is directed to an active hydrogen-containing composition comprising (a) a relatively high equivalent weight compound having from 2 to 4 hydroxyl groups, primary and/or secondary amine groups or mixtures thereof and an equivalent weight from 250 to 5000, and (b) a secon¬ dary a ine-terminated adduct of a primarily monofunc¬ tional primary amine compound and a polyepoxide. This invention is also directed to a polyurea-containing polymer comprising the reaction product -of a polyisocyanate and the active hydrogen- -containing composition described above. The polymer of this invention is characterized in having good heat distortion, impact strength and flexural modulus. As such, these polymers are especially useful as structural polymers as well as static or dynamic elastomers. The polymer of this invention is prepared by reacting the polyisocyanate with the active hydrogen- -containing composition containing the secondary amine- -terminated adduct of a monofunctional primary amine compound and a polyepoxide. Among the polyepoxides usefully employed herein to prepare the secondary amine-terminated adduct are those represented by the general structural formula 0 [H 2 C-CH-CH 2 X] n R I. wherein X is the residue of an active hydrogen-con¬ taining moiety after removal of said active hydrogen, R is an organic polyradical and n is at least 2, prefer¬ ably from 2 to 4, more preferably 2 to 3 and most preferably 2 to 2.3. Such polyepoxides are advantage¬ ously prepared by reacting a compound having a plural¬ ity of groups containing active hydrogen atoms with a halogen-containing oxirane such as epichlorohydrin or epibromohydrin. In structure I, the group X is advantageously 0 0 0 0 II II II II -0-, -NH-, -NR'-, -C-, -0-C-, -S-, -NR-C-, -O-C-N- or a similar group, wherein R' is lower alkyl. Preferably, the group X is -0- and the polyepoxide is one prepared in the reaction of a polyhydroxyl containing compound with a halogenated oxirane as discussed above. Exemplary polyepoxides include epoxy-terminated derivatives of bisphenols, such as are represented by the structural formula wherein each A is independently a lower alkylene group such as methylene, ethylene, or isopropylidine, 0 II or -0-, -S-, or -C-, each B is as defined by A, and/or -OCH 2 CHOHCH 2 0-, each R 5 is independently hydrogen, halogen or lower alkyl, and m is a number from 0 to 30, preferably 0 to 10 and more preferably 0.1 to 3. In addition, derivatives of the materials represented by structural formula II in which one or more of the positions on the group A is substituted with an inert substitutent such as, for example, halo¬ gen, aryl, or alkyl are also useful herein. Suitable such epoxides in include the commerically available resinous reaction products of an epihalohydrin with the the diverse bisphenols and halogenated bisphenols, particularly the reaction products of an epihalohydrin with bisphenol A or bisphenol F or halogenated deri- vates thereof. These resins preferably have an average epoxide equivalent weight from 170 to 2000. Suitable such epoxy resins include those sold commercially as DER* 317, DER 330, DER 331, DER 332, DER 333, DER 337, • DER 642U, DER 661, DER 662, DER 663U, DER 664, DER 664U, DER 667, DER 673MF, DER 542, DER 511-A80, DER 521-A75, and DER 599 epoxy resins all available from The Dow Chemical Company. Also suitable are the cor¬ responding aromatic glycidyl amine resins wherein the various ether linkages are replaced by -NH- groups. Also useful herein are the so called poly- nuclear phenol glycidyl ether derived resins. Also suitable, but less prefered due to the higher epoxy functionality, are the so-called epoxy phenol novolac resins and epoxy cresol novolac resins which can be represented by the structure *Trademark of The Dow Chemical Company I wherein n is a number from 0 to 20 and each R 3 is independently hydrogen, halogen, lower alkyl, aryl or aralkyl. Halogenated derivatives of such resins are also useful herein. In addition, epoxy resins prepared by reacting an organic diene with an aromatic hydroxyl-containing compound and subsequently reacting the resulting product with an epihalohydrin, as are described in U.S. Patent 4,390,680 to Nelson, are useful herein. Suitable aliphatic epoxy resins include the hydrogenated derivatives of the foregoing aromatic epoxy resins as well as those in which the group R of Structure I is lower alkylene, especially ethylene and isopropylene, a dialkylene ether or a polyoxyalkylene group. Such resins are advantageously prepared by reacting an alkylene glycol or polyether polyol with an epihalohydrin. Examples of such resins include DER 732 and DER 736, both of which are available from The Dow Chemical Company. Also useful are aliphatic epoxy resins prepared in reaction of cycloolefins with peracetic acid, as well as diglycidyl ethers of cyclic dicarboxylic acids. The epoxy resin is reacted with a stoichiometric excess of a primarily monofunctional organic primary amine in order to "cap" the resin with a terminal secondary amine group. The primary amine is preferably primarily monofunctional in order to minimize the polymerization of the epoxy resin. Preferably, the primary amine contains less than 15, preferably less than 10, more preferably less than 5 weight percent of polyamine compounds. The primary amine is advantage¬ ously represented by the structure R 4 NH 2 wherein R 4 is alkyl, aryl or aralkyl having from 2 to 30 carbon atoms. Suitable such amines include, for example, ethylamine, N-propylamine, isopropylamine, N-, -iso-, or sec-butyl amine, stearyl amine, oleyl amine, aniline, and o-ethyl aniline. Preferred are alkyl amines having from 2 to 8 carbon atoms, and aromatic amines having from 6 to 12 carbon atoms. The adduct of the -primary amine in the poly¬ epoxide can be prepared by simply heating the polye¬ poxide and primary amine together for a period of time sufficient to complete the reaction thereof. A temper¬ ature of from 20 to 150°C is typically employed. Typ¬ ically a large excess, i.e. 2 to 15 molar excess, of the amine is employed in order to minimize the form¬ ation of high molecular weight materials. The excess amine also acts as a diluent. It is often advantageous, particularly when a viscious or solid polyepoxide is employed, to conduct the reaction in a suitable solvent for the polyepoxide. Ketones and alcohols, particu¬ larly methylethyl ketone and propylene glycol mono- methyl ether, are suitable solvents. The time and temperature employed in the reaction depends somewhat on the particular amine employed. Lower molecular weight amines generally react more readily than higher molecular weight amines. In general, a temperature from 0 to 120°C, preferably from 30 to 80°C, and a reaction time from 3 minutes to 20 hours is suitable. It is desirable to add the polyepoxide to the amine gradually in order to facilitate control of the reaction. Following the reaction of the primary amine and the polyepoxide, any unreacted primary amine (and solvent, if any) are advantageously removed from the product adduct by any suitable technique. Vacuum distillation is a useful technique for this purpose. The aforementioned adduct contains terminal secondary amine groups which can react with an isocy- anate group to form a urea linkages. These amine groups can be reacted with a polyisocyanate to form a polyurea containing polymer. The reaction of the adduct with a polyisocyanate can be conducted at ambient or a somewhat elevated temperature. A catalyst such as a tertiary amine compound or an organo metallic compound can be used if desired. Suitable conditions for conducting polyamine-polyisocyanate polymerization reactions are described in U.S. Patent No. 4,444,910. In addition, the adduct of the primary amine and the polyepoxide also contains secondary hydroxyl groups which can also react with a polyisocyanate to form a urethane linkage. This secondary hydroxyl is significantly less reactive than the secondary amine groups, and generally requires more strigent reaction conditions, i.e. higher temperatures and/or the use of a catalyst, to react. Thus, the reaction conditions can be chosen such that few if any of these hydroxyl groups react with the polyisocyanate, thereby forming a more linear polymer, or such that a significant propor¬ tion thereof react, forming a more crosslinked struc¬ ture. The active hydrogen-containing composition of this invention contains a relatively high equivalent weight compound having from 2 to 4 hydroxyl groups, primary and/or secondary amine groups or mixtures thereof and an equivalent weight from 250- to 5000 (based on the number of hydroxyl and/or amine groups). Other suitable polyols include polyhydroxyl-containing phosphorous compounds, hydroxyl-terminated acetyl resins, hydroxyl.-terminated amines and polyamines, and the so-called polymer or copolymer polyols which com¬ prise a dispersion of polymer or copolymer in a con¬ tinuous polyol phase. Examples of these and other suitable polyols are described more fully in U.S. Patent No. 4,294,491, particularly in columns,.3-5 thereof. Suitable copolymer polyols include those described in U.S. Patent No. RE 29118, RE 28715 and 4,394,491. Of particular interest herein are the polyether polyols, polyester polyols and corresponding amine-terminated polyether and polyester polyols. Suitable amine-terminated polyethers include, for example, those described in U.S. Patent No. 3,666,788 to Rowton and those commercially available from Texaco Chemical Company under the tradenames Jeffamine D-2000 and Jeffamine T-5000. It has also been found most pre¬ ferred to employ at least one of an amine-terminated polyether or an amine-initiated polyol in preparing polymers according to this invention. Suitable amine initiated polyols include alkylene oxide adducts of ammonia polyamines such as, for example, ethylene diamine, diethylene triamine, and aminoethylpiper- azine having an equivalent weight from 250 to 2000. Other isocyanate-reactive materials which may optionally be incorporated in the active hydrogen- -containing composition of this invention include rela¬ tively low equivalent weight polyols or polyamines. Such relatively low equivalent weight materials include those having from 2 to 8 hydroxyl groups, primary and/or secondary amine groups or mixtures thereof and an equivalent weight (based on the number of amine and/or hydroxyl groups) from 30 to 250. Typical rela- tively low equivalent weight hydroxyl terminated mater¬ ials include, but are not limited to, ethylene glycol, diethylene glycol, triethylene glycol, propylene glycol, low molecular weight polymers of ethylene or propylene oxide, 1,4 butane diol, 1,6 hexane diol, neopentyl glycol, dibromoneopenyl glycol, and triisopropanol amine. Typical relatively low equivalent weight polyamines include aliphatic polyamines such as ethylene diamine, hexamethylene diamine 1,4-diamino- cyclohexane, aminoethylpiperazine, aminated poly- (alkylene oxides) such as are available commercially under the names of Jeffamine D-400 and Jeffamine T-403 and aromatic polyamines such as described in U.S. Patent No. 4,374,210. The secondary amine-terminated adduct of a primary amine and polyepoxide generally comprises at least 3, preferably from 10 to 95, more preferably from 10 to 60 percent of the combined weight of the adduct and the other isocyanate-reactive materials. It is generally advantageous to blend the relatively high equivalent weight compound with the secondary amine-terminated adduct prior to reacting them with a polyisocyanate. The conditions employed in preparing a polymer using a mixture of the secondary amine-terminated adduct and the relatively high equivalent weight com¬ pound depends somewhat on the reactivity of the rela¬ tively high equivalent weight compound and the par- ticular catalyst (if any) employed. Mixtures contain¬ ing relatively large amounts of amine-terminated adducts tend to be highly reactive with polyisocyanates and are most typically reacted therewith in low or high pressure impingement mixing equipment such as the so called RIM (reaction injection molding) equipment. Such mixtures tend to require . the use of little or no catalyst. On the other hand, mixtures containing significant propor¬ tions of polyols tend to react more slowly and are more readily adaptable to other casting methods if desired. Catalysts are generally required when significant proportions of polyols are used, particularly if a RIM processible system is desired. Organic polyisocyanates which may be employed include aromatic, aliphatic and cycloaliphatic poly- isocyanates and combinations thereof. Representative of these types are diisocyanates such as m-phenylene diisocyanate, tolylene-2,4-diisocyanate, tolylene-2,6- -diisocyanate, hexamethylene-l,6-diisocyanate, tetra- ethylene-1,4-diisocyanate, cyclohexane-1,4-diisocyanate, hexahydrotolylene diisocyanate (and isomers), naph- thylene-1,5-diisocyanate, 1-methoxyphenyl-2,4-diiso¬ cyanate, diphenylmethane-4,4'-diisocyanate, 4,4'-bi- phenylene diisocyanate, 3,3"-dimethoxy-4,4•-biphenyl diisocyanate, and 3,3'-dimethyl-4,4'-diphenyl diiso¬ cyanate, the triisocyanates such as trifunctional polymethylene polyphenylisocyanates and tolylene-2,- 4,6-triisocyanate; and tetraisocyanates such as 4,4'-dimethyldiphenylmethane-2,2' ,5,5'-tetraisocyanate. A crude polyisocyanate may also be used in the practice of the present invention, such as the crude toluene diisocyanate obtained by the phosgenation of a mixture of toluene diamines or the crude diphenyl- methylene diisocyanate obtained by the phosgenation of crude diphenylmethylenediamine. The preferred undistil- led or crude isocyanates are disclosed in U.S. Patent No. 3,215,652. Alternatively, an isocyanate-terminated prepolymer or quasi-prepolymer prepared by reacting an excess of a polyisocyanate with a polyol of low or high equivalent weight may be employed as the polyisocyanate herein. In addition to the aforementioned components, other optional ingredients may be employed herein for their usual purposes. Flame retardants are usefully employed herein, particularly phosphate esters and halogenated materials such as dibromoneopentyl glycol. It is often desirable to employ a blowing agent herein to produce lower density polymers. Suit¬ able blowing agents include those materials which vaporize or otherwise generate a gas under the condi¬ tions encountered in the polymerization reaction. Materials which boil under such conditions include low boiling halogenated hydrocarbons such as, for example, chlorotrifluoromethane, dichlorodifluoromethane, trichlorofluoromethane, methylene chloride, chloroform, and trichloroethane. Suitable materials which react to form a gas under such conditions include water and the so-called azo blowing agents. Materials which dehydrate to release gaseous water under such conditions include, for example, magnesium sulfate heptahydrate, sodium carbonate decahydrate, sodium phosphate dodecahydrate, calcium nitrate tetrahydrate, and ammonium carbonate tetrahydrate, are less preferably used as a blowing agent. High surface area particulate solids are also useful blowing agents, as described in U.S. Patent No. 3,753,933. Preferred are water, halogenated hydrocar¬ bons and mixtures thereof. Preferably, sufficient of the blowing agent is employed to provide a polymer having a specific gravity from 0.4 to 1.2, more preferably from 0.8 to 1.0. However, low density polymers, i.e. foams, can also be prepared according to this invention. A surfactant is often used in preparing polymers according to this invention, particularly when a blowing agent is employed. Suitable surfactants are well known and their use in preparing low density polymers is well understood. Preferred are silicone surfactants including B 8404, B 8014, B 8020, and B 8200 all available from Goldschmidt Chemicals; L-5303, L-5305, L-520 and L-540, all available from Union Carbide Corporation; and DC-190, DC-193, DC-196, and DC-197, all available from Dow Corning Corporation, and other silicone surfactants. Suitable catalysts which may be employed herein include organometal compounds such as organotin, organomercur , and organolead compounds as described in U.S. Patent No. 2,846,408. Tertiary amine catalysts such as, for example, triethylene diamine, triethyl amine, N-methyl morpholine, and N,N-dimethylaminoethyl piperadine are also useful catalysts for the polymer¬ ization reaction. Generally, such catalysts, when used, are employed in amounts from 0.002 to 2, prefer- ably from 0.01 to 1, part per 1.00 parts by weight of isocyanate-reactive materials employed in the prepar¬ ation of the polymer. In addition, other additives such as, for example, pigments, reinforcing fibers, fillers < anti- oxidants, stabilizers, flame retardants, and inhibitors are optionally employed herein for their usual purposes. Generally, it is convenient to blend said optional ingredients with the adduct and materials (if any) prior to the reaction thereof with the polyiso- cyanate to prepare a polymer according to this inven¬ tion. The polymers of this invention are character¬ ized by having high modulus, high impact strength, and high heat distortion temperatures. Accordingly, such polymers are particularly useful in structural applica¬ tions, such as in cabinetry, window frames, sporting goods and applications wherein the polymer is required to maintain a constant load. The following examples are provided to illus- trate the invention but not to limit the scope thereof. All parts and percentages are by weight unless other¬ wise indicated. Preparation of Isopropylamine-Terminated Adducts of Epoxy-Ter inated Tetrabromobisphenol A/ Epichlorohydrin Resins To reactor equipped with a stirrer, reflux condenser, nitrogen sparge and temperature control are added 22.5 moles (1329.7 g. ) of isopropyl amine and 691 grams of propylene glycol mono methyl ether. After heating to 40°C, 1.5 moles (1388.6 grams) of a 463 equivalent weight epoxy resin prepared from tetra¬ bromobisphenol A and epichlorohydrin are added over 165 minutes. During the reaction the temperature increases to 55°C. A small portion of methylethyl ketone is added during the reaction. After the addition is complete, the reaction mixture is digested for 2 hours at 65°C. The mixture is then vacuum distilled to remove unreacted isopropyl amine and the solvents. The distillation is completed at 104°C and 8 mm Hg (1.1 kPa) pressure. The product is a clear resinous material with a melting point of 91°C and an theoretical equivalent weight of 522. This product is hereinafter referred to as Adduct A. Adduct B is prepared in like manner except that this time the epoxy resin has an equivalent weight of 451, and 18 moles of isopropyl amine are used. Adduct B has a melting point of 94°C, a theoretical equivalent weight of 510, and an observed equivalent weight of 517. Preparation of Aniline-Terminated Adducts of Epoxy Resins In a reactor equipped as described in Example 1 are added 15 moles (1396.5 grams) of aniline. After heating to 70°C, 250 grams of the same epoxy resin employed to prepare Adduct A (dissolved in methylethyl ketone) and 322 grams of propylene glycol methyl ether are added. After heating to 85°C, 1138.6 additional grams of the epoxy resin are added over 160 minutes. The mixture is then digested for about 2 hours at a temperature between 90 and 120°C and the unreacted aniline and solvents are removed by vacuum distilla¬ tion. The distillation is concluded at about 157°C and 6 mm mercury (0.8 kPa) pressure. The product is a clear resinous material with a melting point of 90°C and"a theoretical equivalent weight of 556. This product is referred to hereinafter as Adduct C. Adduct D is prepared in like manner, this time using 1.5 moles of a bisphenol A-epichlorohydrin adduct having an equivalent weight of about 947 as the epoxy resin. Adduct D has a melting point of 112°C and an observed equivalent weight of 1042 (theoretical equivalent weight = 1040). Adduct E is prepared in like manner, this time employing as the epoxy resin a bisphenol A-epi- chlorohydrin resin having an equivalent weight of 549. Adduct E has a theoretical equivalent weight of 642 and a melting point of 93°C. Preparation of o-Ethyl Aniline-Terminated Adduct of Epoxy-Terminated Tetrabromobisphenol A Epichlorohydrin Resin According to the procedure described in Example 2, 15 moles of ortho-ethyl aniline is reacted with 1.5 moles of the epoxy resin used to prepare Adduct B. The resulting product has a theoretical calculated equivalent weight of 570 and a elting point of 87°C. This adduct is referred to herein as Adduct F. Example 1 Hand-cast plaques are prepared from each of the following formulations. Table I Parts By Weight Ingredient Sample No. 1 Sampli 5 No. 2 Polyol A 1 53 53 Polyol B 2 25 25 Diethylene glycol 30 30 Adduct C 10 20 Silicone Surfactant 3 0. .5 0. ,5 R-8020 4 0. .05% 0. 05% Freon 11 6 6. ,5 Tin Catalyst 5 0. .05% 0. 05% 135 eq. wt. MDI 6 105 index L05 index The reaction product of aminoethylethanolamine and about 3 moles propylene oxide. A trifunctional copolymer of propylene oxide and ethylene oxide having a molecular weight of about 3000. A silicone surfactant commercially available as B-8404 from Goldschmidt. 4 An amine catalyst commercially available from Air Products and Chemicals. 5 UL-6, commercially available from Witco Chemical. 6 A 135 equivalent weight polymethylene polyphenyl polyisocyanate commercially available as Rubinate M from Rubicon Chemical Corp. All ingredients except the polyisocyanate are mixed in a large container. The polyisocyanate is added and the mixture is then vigorously stirred for about 10 seconds. The mixture is then poured into a V (1.27 mm) deep mold which has been preheated to 140°F (60°C). The mold is closed and maintained at about 140°F (60°C) for about 2.5 minutes. The molding is then removed and evaluated, with results as indicated in Table II. Additional ' (6.35 mm) moldings are prepared in like manner from Sample No. 1. Table II Sample No. 1 Sample No. 2 V' (12.7 mm) moldings Specific Gravity 0.75 0.75 Heat Distortion Temp., °C, at 264 psi (1.82 MPa) 102 91 Charpy Impact Strength, ft-lb/in of notch (J/m of notch) 4.84 (258) 5.34 (285) . V' (6.35 mm) moldings Specific Gravity 0.823 Tensile Strength psi (MPa) 2500 (17) Elongation, % 5-10 Flexural Strength, psi (MPa) 6700 (46) Flexural Modulus, psi (GPa) 233,000 (1.61) The resulting moldings are seen to'exhibit excellent thermal and mechanical properties. Example 2 In a manner similar to that described in Example 1, y (12.7) mmmoldings are prepared and tested. Th formulations and test results are as indicated in Table III. rTable III Parts By Weight Sample Sample Sample Sample Ingredient No. 3 No. 4 No. 5 No. 6 Polyol A 1 53 50 50 53 Polyol B 2 25 25 25 25 Diethylene glycol 30 30 30 30 Silicone Surfactant A 3 1 1 1 1 Adduct A 0 0 0 20 Adduct D 20 0 0 0 Adduct E 0 30 0 0 Adduct F 0 0 30 0 Silicone Surfactant B 4 0 0 0 1 Freon 11 3.2% 3.1% 2.0% 4.8% 135 eq. wt. MDI 5 192.4 187.7 188.8 196.4 R-8020 6 0.05 0.03 0.03 0.05 Test Results Specific Gravity 0.80 0.79 0.80 0.83 Heat Distortion Temp., °C at 264 psi (1.82 MPa) 100 92 95 97 Charpy Impact 7 ft-lb/in of notch 5.05 4.12 3.00 3.84 (J/m of notch) (270) (220) (160) (205) 1 The reaction product of aminoethylethanolamine and about 3 moles propylene oxide. 2 A trifunctional copolymer of propylene oxide and ethylene oxide having a molecular weight of about 3000, 3 A silicone surfactant commercially available as B-8404 from Goldschmidt. 4 DC-193, sold by Dow Corning Corporation 5 A 135 equivalent weight polymethylene polyphenyl polyisocyanate commercially available as Rubinate M from Rubicon Chemical Corp. 6 An amine catalyst sold by Air Products and Chemicals. 7 Unnotched Example 3 Plaques of ' (6.35 mm) and y (12.7 mm) thickness are prepared from Formulation Nos. 7 and 8 by reaction injection molding using a Krauss-Maffei PU-40 RIM machine. The "A" and "B" sides are preheated to a temperature of 115°F (46°C). Demold time is about two minutes. The mold temperature is about 135°F(57°C). The formulations used and the results of testing are indicated in Table IV. Tensile, flexural and Gardner Impact testing is preformed on 1 (6.35 mm) moldings. Heat distortion and Charpy Impact testing is done on 1 (12.7 mm) samples. Table IV Parts By Weight Ingredient Sample No. 1 Sampli 2 No. 2 Polyol A 1 50 50 Polyol B 2 25 25 Diethylene glycol 30 30 Adduct C 20 0 Adduct B 0 20 Silicone Surfactant 3 1 1 135 eq. wt. MDI 4 103 index 103 index R-8020 5 0. 04% 0.04% Test Results Specific Gravity 1.19 1.16 Heat Distortion Temp., °C at 264 psi (1.82 MPa) (V' (12.7 mm) samples)) 125 126 Charpy Impact ft-lb/in of notch (V' (12.7 mm) samples)) 4.6 (250) 5.2 (250) (280) Gardner Impact, in-lb (m-kg) 55 (0.63) 45 (0.63) (0.52) Flexural Strength psi (MPa) 15,500 17,900 (107) (123) Flexural Modulus, psi (GPa) 325,000 357,000 (2.24) (2.46) Tensile Strength psi (MPa) 9,800 10,300 (68) (71) Elongation, % 8.0 9.1 1 The reaction product of aminoethyl ethanol amine and about 3 moles propylene oxide. A trifunctional copolymer of propylene oxide and ethylene oxide having a molecular weight of about 3000, A silicone surfactant commercially available as B-8404 from Goldschmidt. A 135 equivalent weight polymethylene polyphenyl polyisocyanate commercially available as Rubinate M from Rubicon Chemical Corp. An amine catalyst sold by Air Products and Chemicals. Example 4 A series of V-0 fire rated polymers are prepared from the formulation specified in Table V, and molded under the conditions described in Example 6, except the "A-side" temperature is about 100°F (38°C) and the mold temperature is about 140°F (60°C). The results of testing of the resulting moldings are as reported in Table V. In Sample Nos. 9 and 12 the isocyanate index is 105, and in Sample Nos. 10 and 11 the index is 110. Tensile and flexural testing is performed on ' (6.35 mm)moldings and heat-distortion and Charpy Impact testing is " done on 1 (12.7 mm) moldings. Table V Ingredient Parts By Weight Polyol A 1 53 Polyol B 2 25 Diethylene glycol 10 Triethylene glycol 5 Adduct C 30 Phosphate Ester 3 15 Silicone Surfactant 4 1 Freon 11 15 R-8020 5 0.05% 135 eq. wt. MDI 6 variable Sample Sample Sample Sample Test Results No, . 9 No. 10 No. 11 No. 12 Specific Gravity 1.17 1.15 0.81 0.68 Heat Distortion Temp., °C, at 264 psi (1.82 MPa) 112 112 98 98 Charpy Impact, ft-lb/in of notch (J/m of notch) 6.7 4.9 5.3 3.0 (360) (360) (280) (160) Flexural Strength, psi 13,900 13,200 8,750 6,100 (MPa) (96) (91) (60) (42) Flexural Modulus, psi 334,000 306,000 229,000 171,000 (GPa) (2.30) (2.10) (1.58) (1.18 Tensile Strength, psi 10,200 8,000 5,200 2,600 (MPa) (70) (55) (36) (18) UL-94 Rating 7 V-0 V-0 V-0 Not test 1 The reaction product of aminoethylethanolamine and about 3 moles propylene oxide. 2 A trifunctional copolymer of propylene oxide and ethylene oxide having a molecular weight of about 3000. 3 FYROL PCF, available from Stauffer Chemical Company. 4 A silicone surfactant commercially available from Goldschmidt. 5 An amine catalyst available from Air Products and Chemical 6 A 135 equivalent weight polymethylene polyphenyl polyisocyanate commercially available as Rubinate M from Rubicon Chemical Corp. 7 UL-94 testing performed by The Dow Chemical Company. Example 5 Plaques are prepared and tested according to procedure described in Example 3 from Formulation Sample Nos. 13 and 14. These formulations and the results of testing the product plaques are as reported in ' Table VI. Tensile and flexural properties are tested on ' (6.35 mm) samples. Table VI Parts By Weight Ingredient Sample No. 13 Sample No. 14 Polyol A 1 53 53 Polyol B 2 25 25 Diethylene glycol 10 0 Triethylene glycol 5 0 1,4-butane diol 0 15 DBNPG 3 5 5 Adduct C 30 30 Aminated Polyether A 4 20 0 Aminated Polyether B 5 0 25 Phosphate Ester 6 15 15 Silicone Surfactant 7 ' 1.5 1.5 R-8020 8 0.05% 0.02% Tin catalyst 9 0.02% 0 Freon 11 % 6.5 5.5 135 eq. wt ' . MDI 10 102 index " A ' blended MDI 11 102 index Test Results Specific Gravity 0.81 0.93 Heat Distortion Temp., °C at 264 psi (1.82 MPa) 71 78 Flexural Strength, psi (MPA) 8,000 (55) 8,000 (55) Flexural Modulus, psi (GPa) 203,000 (1.40) 202,000 (1.39 Tensile Strength, psi (MPa) 3,300 (23) 4,300 (30) Elongation, % 9.0 16.0 UL-94 rating 12 Not tested V-l See Footnotes on next page 1 The reaction product of aminoethylethanolamine and about 3 moles propylene oxide. 2 A trifunctional copolymer of propylene oxide and ethylene oxide having a molecular weight of about 3000. 3 Dibromoneopentylglycol 4 Jeffamine D-2000, sold by Texaco Chemicals 5 A 50% aminated, 1650 equivalent weight, ethylene oxide- capped polypropylene oxide triol. 6 Fryol PCF, sold by Stauffer Chemical Company. 7 A silicone surfactant commercially available as B-8404 from Goldschmidt. 8 An amine catalyst sold by Air Products and Chemicals 9 UL-6, sold by Witco Chemical 10 A 135 equivalent weight polymethylene polyphenyl polyisocyanate commercially available as Rubinate M from Rubicon Chemical Corp. 1 1 A blend of 75 weight percent Rubinate M (see note 10) and 25 weight percent of a 170 equivalent weight prepolymer of 4, '-methylene diphenyl/diisocyanate and a 5000 molecular weight, trifunctional, ethyleneoxide- capped poly(propylene oxide). 12 Tested by The Dow Chemical Company. Example 6 Following the general procedure of Example 3, V (12.7 mm) and ' (6.35 mm) plaques are prepared from each of Formulation Sample Nos. 15 and 16. The compositions of these formulations and results of test¬ ing of the plaques prepared therefrom are as indicated in Table VII. All testing is done on the ' (6.35 mm) plaques except for Charpy Impact and Heat Distortion testing. Table VII Parts By Weight Ingredient Sample No. 15 Sample No. 16 Polyol A 1 53 50 Aminated Polyether C 2 25 25 Diethylene glycol 10 30 Triethylene glycol 5 0 DBNPG 3 5 12 Adduct C 30 24 Phosphate Ester 4 15 15 Freon 11 (%) 16.2 18 R-8020 5 0.05% 0. Tin catalyst 6 0 0. 135 eq. wt. MDI 7 16Ϊ.6 0 143 eq. wt. MDI 8 0 211.4 Specific " Gravity 0.82 0.82 Flexural Modulus, psi (GPA) 230,000 (1.59) 215,000 (1.48) Flexural Strength, psi (MPa) 10,150 (70) 9,225 (64) Tensile Strength, psi (MPa) 4,300 (30) 4,300 (30) Elongation, % 4.58 6.19 Gardner Impact, in-lb (m-kg) 52 (0.60) 100 (1.15) Charpy Impact ft-lb/in of notch Not tested 5.49 (293) (J/m of notch) Heat Distortion Temp., at 264 psi (1.82 MPa) Not tested 143 (62) See next page for Footnotes 1 The reaction product of aminoethylethanolamine and about 3 moles propylene oxide. 2 Jeffamine T-5000, sold by Texaco Chemical Company. 3 dibromoneopentylglycol 4 Fyrol PCF, sold by Stauffer Chemical Company. 5 An amine catalyst commercially available from Air Products and Chemicals. 6 UL-6, sold by Witco Chemical 7 A 135 equivalent weight polymethylene polyphenyl polyisocyanate commercially available as Rubinate M from Rubicon Chemical Corp. 8 A 143 equivalent weight polypropylene polyphenyl- polyisocyanate sold as LF-168 by Rubicon Chemical Company.

Claims: 1. An active-hydrogen containing composi¬ tion comprising (a) a relatively high equivalent weight compound having from 2 to 4 hydroxyl groups, primary and/or secondary amine groups or mixtures thereof and an equivalent weight from 250 to 5000, and (b) a secondary amine-terminated adduct of a primarily monofunctional primary amine-containing compound and a polyepoxide. 2. The compositon of Claim ϊ wherein the secondary amine-terminated adduct comprises from 10 to 95 percent of the combined weight of the adduct and the other isocyanate-reactive materials. V 3. The of Claim 1 wherein the relatively high equivalent weight compound comprises at least one of an amine-terminated polyether and an amine-initiated polyol. 4. The composition of Claim 2 wherein the other isocyanate-reactive materials further comprise a relatively low equivalent weight material having from 2 to 8 hydroxyl groups, primary and/or secondary amine groups or mixtures thereof and an equivalent weight from 30 to 250. 5. The composition of Claim 1 wherein the secondary amine-terminated adduct is the reaction product of a monofunctional amine containing from 2 to 30 carbon atoms and a polyepoxide having the general structural formula wherein X is the residue of an active hydrogen- -containing moiety after removal of said active hydrogen, R is an organic polyradical, and n is at least 2. 6. The composition of Claim 5 wherein the monofunctional amine is an alkyl amine having from 2 to 8 carbon atoms or an aromatic amine having from 6 to 12 carbon atoms. 7. The composition of Claim 5 wherein the polyepoxide comprises a reaction product of a bis¬ phenol or a halogenated bisphenol and an epihalodyrin, and has an average equivalent weight of from 170 to 2000. 8. The composition of Claim 5 wherein the polyepoxide comprises a reaction product of an epi¬ halohydrin and an alkylene glycol or a polyether polyol. 9. A polyurea-containing polymer comprising the reaction product of a polyisocyanate and the active hydrogen-containing composition of Claim 1.

Inventors: NELSON DONALD L, NELSON, DONALD, L.
Applicants: DOW CHEMICAL CO, THE DOW CHEMICAL COMPANY
Application year: 1986
Main classification: C08G18
IPC codes: C08G18