PROCESS FOR PREPARING POLYMER POLYAHLS

Abstract: Process for preparing a polymer polyahl comprising polymerizing an ethylenically unsaturated monomer or mixtures thereof in a ployahl or polyahl mixture whereby a dispersion of polymer particles is prepared in a continuous polyahl phase. The process is characterized by conducting said polymerization in the presence of a halogen, interhalogen or iodine-releasing inorganic compound. The use of the halogen, interhalogen or iodine-releasing inorganic compound provides a more stable polymer polyahl having lower viscosity.

Description: PROCESS FOR PREPARING POLYMER POLYAHLS This invention relates to a graft polymer dispersion prepared by the polymerization of an ethylenically unsaturated monomer or mixtures thereof in a polyahl (hereinafter "polymer polyahl" or "copolymer polyahl"). More particularly, the invention relates to an improved process for preparing said copolymer polyahl. In recent years it has been known to prepare polymer dispersions in a polyahl mixture. In such dispersions, a polymer of an ethylenically unsaturated monomer or mixture of monomers is dispersed in a polyahl or mixture thereof. The dispersed polymer is normally grafted to the polyahl through some unsaturation in the polyahl. Such unsaturation is commonly introduced into the polyahl by reaction thereof with a small amount of an unsaturated acid, such as fumaric or maleic acid or their anhydrides, or more recently, isocyanatoethyl- methacrylate (IE ). In these copolymer polyahls, the polyahl makes up a continuous phase into which the copolymer is dispersed as a plurality of small particles These copolymer polyahls have found great utility in the production of diverse polyurethanes. In particular, the use of copolymer polyahls in preparing polyurethanes has been found to improve the process- ability of the polyurethane, as well as physical proper¬ ties such as load bearing or modulus. It is often desirable to provide a copolymer polyahl with as high a dispersed phase content as possible. However, it has heretofore been difficult to prepare and/or use copoly- mer polyahl containing more than about 35 to 40 percent by weight dispersed phase. A high concentration of dispersed phase greatly increases the viscosity of the copolymer polyahl. When the viscosity exceeds about 6500 cps (6.5 Pa-s), it is usually too viscous to be pumped using conventional urethane molding and/or foaming equipment. With conventional copolymer polyahl, a viscosity of 6500 cps (6.5 Pa-s) is usually reached at a dispersed phase concentration of 35 to 40 percent or lower. Even at a lower dispersed phase concentration, it is normally preferred to have a viscosity as low as possible to ease the handling of the copolymer polyahl. * Another problem associated with high dis¬ persed phase concentration is that the stability of the dispersed phase is greatly reduced as the dis¬ persed phase concentration exceeds about 35 to 40 percent. At higher dispersed phase concentration (higher solids), the copolymer particles tend to coalesce and phase separate. The phase separation of the copolymer greatly impares the utility of the copolymer polyahl and polyurethane prepared therewith. Yet another common disadvantage of conven¬ tional copolymer polyahls is that in order to provide a stable copolymer dispersion one must introduce substantial amounts of unsaturation into the polyahl through which to graft the dispersed phase. It is generally easier and cheaper to prepare copolymer polyahl having a lesser amount of unsaturation in the polyahl. It is known to prepare copolymer polyahls by polymerizing ethylenically unsaturated monomers in the presence of the polyahl and a chain transfer agent. The chain transfer agent is used in the preparation of copolymer polyahls in a manner analogous to the use thereof in conventional polymerizations, that is, to control the molecular weight distribution of the polymer. However, the choice of chain transfer agent has not heretofore been attributed to significant improvements in the properties of the copolymer polyahl. In addition, the use of iodine (I 2 ) i n making copolymer polyahls has not heretofore been known. In view of the aforementioned deficiencies of previously known copolymer polyahls, it would be desirable to provide a copolymer polyahl that exhibits high stability and an acceptable viscosity of a high solids content or a lower viscosity at an equivalent solids content, than that exhibited by a conventional copolymer polyahl. This invention is a process for preparing a polymer polyahl comprising polymerizing an ethyleni- cally unsaturated monomer or mixtures thereof in a polyahl or polyahl mixture whereby a dispersion of polymer particles is prepared in a continuous polyahl phase, characterized by conducting said polymeriza¬ tion in the presence of a halogen, interhalogen (mixed halogen) or iodine-releasing inorganic compound. With the process of this invention, it is possible to prepare copolymer polyahls having a solids content up to 50 percent or more, and which have viscos¬ ities such that they are processable using conventional polyurethane molding and/or foaming equipment. At a given dispersed phase content, these have a lower viscosity than like copolymer polyahls prepared in the absence of the iodine or iodine-releasing inorganic compound. Moreover, the copolymer polyahl prepared according to this invention exhibits greater stability, i.e., a smaller tendency for the dispersed particles to agglomerate, tha conventionally prepared copolymer polyahl and exhibits good flame retardant properties. In this invention, the polymerization of the monomers(s) in a continuous polyahl phase is conducted in the presence of a halogen, interhalogen or iodine- -releasing inorganic compound. The halogen employed herein is chlorine, bromine, or iodine. Of these chlorine is least preferred due to more ionic character. Iodine is by far the most preferred halogen, because it provides a stable low viscosity copolymer polyol even when employed in small amounts. Interhalogens employed herein are diatomic molecules wherein each atom is different and is selected from chlorine, bromine or iodine. Preferably, one of the atoms is iodine. Bromine iodide, i.e. IBr, is the most preferred of the interhalogens. The iodine releasing inorganic compound useful herein is one which releases iodine, i.e. I 2 , or iodine radicals, i.e. I*, under the conditions of the polymerization of the monomers. Said iodine releasing inorganic compound contains at least one iodine atom bonded to a central atom other than carbon. Said central atom is preferably bonded to at least 2, more preferably at least 3, iodine atoms. Said central atom may also be bonded to other atoms or groups such as inertly substituted hydrocarbyl, alkoxyl, hydrogen, halogen, and the like. Even though the iodine-releasing inorganic compound may have carbon- -containing substituent groups, it is considered "inorganic" for the purposes of the invention if it contains iodine atoms which are attached to an atom other than carbon. Suitable iodine-releasing inorganic com¬ pounds include, for example, Asl 3 , Aul 3 , BI 3 , Csl 3 , Dyl 3 , Erl 3 , Gal 3 , Gdl 3 , Gel 3 , Hfl 3 , K 2 HgI 4 , Inl 3 , KAuI 4 , PI.., PI 3 , K 2 PtI 6 . ^tlg, Ptlg, Ndl 3 , P £ I 4 , Ptl 4 , Rhl 3 , Rul 3 , Sbl 3 , Sil 4 , Tal 5 , Tel 4 , Til 4 , 2rl 4# Bal 2 . Cdl 2 , CoI 2 , Fel 2 , Gel 2 , Hgl 2 , ^ 2 τ 2 ' MnI 2' MoI 2' Pbl 2 , Pdl 2 , Ptl 2 , Snl 2 , Srl 2 , and I 2 . Also suitable are iodine-containing organo- metal compounds such as, for example, triphenyl anti¬ mony diiodide, PC, 2 H 36 Ag.I 4 , and dibutyltin diiodide. The halogen, interhalogen or iodine-releasing inorganic compound (sometimes referred to herein as "reaction modifier") is employed in an amount suffi- cient to provide improved stability to the copolymer polyahl of this invention. However, certain reaction modifiers can adversely affect the polymerization of the monomers if present in too high a concentration. Preferably, the reaction modifier is employed in an amount typical for chain transfer agents, i.e. from 0.05 to 3, more preferably from 0.2 to 1.0, percent by weight of the monomers to be polymerized. The halogen, interhalogen or iodine-releasing compound may be added batchwise to the polyahl at the begin¬ ning of the polymerization of the ethylenically unsat- urated monomer. However, if present in too great a concentration, the halogen, interhalogen or iodine- -releasing compound may inhibit the polymerization reaction. Thus, it may be desirable to add the halogen, interhalogen or iodine-releasing compound incrementally or continuously during the polymer¬ ization reaction in order to maintain optimum amount, thereof at all times during the reaction. In the process of this invention, one or more ethylenically unsaturated monomers are polymer- ized in a polyahl or polyahl mixture. The polyahl or polyahl mixture preferably contains a quantity of graft polymerization sites. The term "polyahl" as used herein, includes any polyfunctional compound having at least two active hydrogen atoms. For the purposes of this invention, an active hydrogen moiety refers to a moiety contain¬ ing a hydrogen atom which, because of its position in the molecule, displays significant activity accord¬ ing to the Zerewitnoff test described by Woller in the Journal of American Chemical Society, Vol. 49, page 3181 (1927). Illustrative of such active hydro¬ gen moieties are -COOH, -OH, - H 2 , -NH-, -CON_ 2 , -SH and -CONH-. Typical polyahls include polyols, poly- amines, polyamides, polymercaptans and polyacids. Of the foregoing polyahls, the polyols are preferred. Examples of such polyols are the polyol polyethers, the polyol polyesters, hydroxy functional acrylic polymers, hydroxyl-containing epoxy resins, polyhydroxy terminated polyurethane polymers, polyhydroxyl- -containing phosphorus compounds and alkylene oxide adducts of polyhydric thioethers including polythioethers, acetals including polyacetals, polyalkylene carbonate polyols, aliphatic and aromatic polyols and thiols including polythiols, ammonia and amines including aromatic, aliphatic and heterocyclic amines including polyamines as well as mixtures thereof. Alkylene oxide adducts of compounds which contain two or more different groups within the above-defined classes may also be used such as amino alcohols which contain an amino group and a hydroxyl group. Also, alkylene adducts of compounds which contain one -SH group and one -OH group as well as those which contain an amino group and a -SH group may be used. Polyether polyols which are most advantageously employed as the polyahl in the practice of this invention are the polyalkylene polyether polyols including the polymerization products of alkylene oxides and other oxiranes with water or polyhydric alcohols having from two to eight hydroxyl groups. Exemplary alcohols that are advantageously employed in making the polyether polyol include ethylene glycol, 1,3-propylene glycol, 1,2-propylene glycol, 1,4-butylene glycol, 1,3-butylene glycol, 1,2-butylene glycol, 1,5-pentane diol, 1,7-heptane diol, glycerol, 1,1,1-trimethylolpropane, 1,1,1-trimethylolethane, hexane-l,2,6-triol, α_methyl glucoside, pentaerythritol, erythritol, pentatols and hexatols. Also included within the term "poly¬ hydric alcohol" are sugars such as glucose, sucrose, fructose and maltose as well as compounds derived from phenols such a 2,2-(4,4'-hydroxyphenyl)propane, commonly known as bisphenol A. Illustrative oxi- ranes that are advantageously employed in the prepar¬ ation of the polyether polyol include simple alkylene oxides such as ethylene oxide, propylene oxide, butyl- ene oxide, and amylene oxide; glycidyl ethers such as t-butyl glycidyl ether and phenyl glycidyl ether; and random or block copolymers of two or more of these oxiranes. The polyalkylene polyether polyols may be prepared from other starting materials such as tetrahydrofuran and alkylene oxide, tetrahydrofuran copolymers; epihalohydrins such as epichlorohydrin; as well as aralkylene oxides such as oxide. The polyalkylene polyether polyols may have primary, secondary or tertiary hydroxyl groups and, prefer¬ ably, are polyethers prepared from alkylene oxides having from two to six carbon atoms such as ethylene oxide, propylene oxide and butylene oxide. The poly¬ alkylene polyether polyols may be prepared by any known process such as, for example, the process dis¬ closed by Wurtz in 1859 and Encyclopedia of Chemical Technology, Vol. 7, pp. 257-262, published by Interscience Publishers, Inc. (1951), or in U.S. Patent No. 1,922,459. Also suitable are polyether polyols and processes for preparing them that are described in Schick, M. J., Nonionic Surfactants, Marcel Dekker, Inc., New York (1967), U.S. Patent Nos. 2,891,073; 3,058,921; 2,871,219 and British Patent No. 898,306. Polyether polyols which are most preferred include, for example, the alkylene oxide addition products of water, trimethylolpropane, glycerine, pentaerythritol, sucrose, sorbitol, propyl¬ ene glycol and blends thereof having hydroxyl equiv- alent weights of from 25 to 5000. Polyhydric thioethers which are sometimes advantageously condensed with alkylene oxides include the reaction product of thiodiglycol with alkylene oxides or dihydric alcohols such as disclosed above. Polyh droxyl-containing phosphorus compounds which are optionally used include those compounds disclosed in U.S. Patent No. 3,639,542. Preferred polyhydroxyl-containing phosphorus compounds are prepared from alkylene oxides and acids of phosphorus having a p ° equivalency of from 72 to 95 percent. Polyacetals (acetal resins) which are option¬ ally reacted with alkylene oxides or other oxiranes include, for example, the reaction product of formal¬ dehyde or other suitable aldehyde with a polyhydric alcohol or an oxirane such as those disclosed above. Polyacetals derived from acetone or from cyclic acetals are also suitably employed. Aliphatic and aromatic thiols which are optionally reacted with alkylene oxides and other oxiranes include, for example, alkane thiols such as 1,2-ethane dithiol, 1,2-propane dithiol and 1,6-hexane dithiol; alkene thiols such as 2-butene- -1,4-dithiol; and alkyne thiols such as 3-hexyne- -1,6-dithiol; and arene thiols such as 1,4-benzene dithiol. Other thiols suitable for this purpose are hydrogen sulfide as well as thiol functional polymers such as polyvinylbenzyl thiol. Acids and amides which are optionally reacted with alkylene oxides and other oxiranes include, for example, difunctional fatty acids such as hydroxy- stearic and dihydroxystearic acid as well as amides such as fatty acid alkanol amides, e.g., lauroyl mono- ethanolamide; diacids such as adipic and terephthalic acid; sulfonamides and other acids and amides set forth in Schick, supra. Amines which are optionally reacted with alkylene oxides and other oxiranes include, for example, aromatic amines such as aniline, o-chloro- aniline, p-amino aniline, 1,5-diamino naphthalene, methylene dianiline, the condensation products of aniline and formaldehyde and 2,4-diamino toluene; aliphatic amines such as methylamine, triisopropanol- amine, isopropanolamine, diisopropanolamine, ethylene- diamine, 1,3-propylenediamine, 1,4-butylenediamine and 1,3-butylenediamine, and mixtures thereof. Additional polyethers and methods for their preparation are set forth in Schick, supra. Examples of suitable hydroxy-containing polyesters include those obtained from polycarboxylic acids and polyhydric alcohols. Examples of suitable polycarboxylic acids include oxalic acid, malonic acid, succinic acid, glutaric acid, adipic acid, pimelic acid, suberic acid, azelaic acid, sebacic acid, brassylic acid, thapsic acid, maleic acid, fumaric acid, glutaconic acid, α-hydromuconic acid, β-hydromuconic acid, α-butyl-α-ethyl-glutaric acid, α,β-diethylsuccinic acid, isophthalic acid, terphthalic acid, hemimel- litic acid., and 1,4-cyclohexane-dicarboxylic acid. Any suitable polyhydric alcohol including both ali¬ phatic and aromatic may be used such as, for example, ethylene glycol, 1,3-propylene glycol, 1,2-propylene glycol, 1,4-butylene glycol, 1,3-butylene glycol, 1,2-butylene glycol, 1,5-pentane diol, 1,4-pentane diol, 1,3-pentane diol, 1,6-hexane diol, 1,7-heptane diol, glycerol, 1,1,1-trimethylolpropane, 1,1,1- -trimethylolethane, hexane-l,2,6-triol, α-methyl glucoside, pentaerythritol and sorbitol. Also included with the term "polyhydric alcohol" are compounds derived from phenols such as 2,2(4,4'- -hydroxyphenyl)proρane, commonly known as bisphenol A, bis(4,4'-hydroxyphenyl)sulfide and bis(4,4'- -hydroxyphenyl)sul one. Other polyahls suitably employed include, for example, polylactones; hydroxy functional acrylic polymers such as polymers of hydroxyethyl acrylate and hydroxypropyl acrylate; polyvinyl acetate and other polymers of vinyl'acetate and other ethyleni¬ cally unsaturated carboxylic acids; hydroxyl-contain- ing epoxy resins, urea-formaldehyde and melamine- -formaldehyde resins; hydroxyl-containing poly¬ carbonates and polyurethanes; methylol resins; starches and other cellulosic polymers; esters of phosphonic, sulfonic, sulfuric and boric acid; and polypeptides. The polyahl or polyahl mixture preferably contains a proportion of graft polymerization sites. The polyahl or polyahl mixture may contain a single polyahl species, a portion of which contains graft polymerization sites. Alternatively, the polyahl may be a mixture of two or more polyahl species, of which at least one contains graft polymerization sites. The graft polymerization sites are any functional groups on the polyahl through which the polymer of the ethylenically unsaturated monomer or monomer mixture becomes grafted to the polyahl. Preferably, the graft polymerization sites are carbon-carbon double bonds which are copolymerizable with the ethylenically unsaturated monomer or monomer mixture. Said graft polymerization sites may be formed in side reactions which occur in the prepara¬ tion of the polyahl, such as the unsaturated sites commonly formed in preparing a pol (propylene oxide) polyether polyol. Such normally occuring graft polymerization sites are most commonly adequate when the monomers being polymerized comprise a major portion of acrylonitrile. More commonly, however, the graft polymer¬ ization sites are purposefully introduced into the polyahl or polyahl mixture. The graft polymerization site is advantage¬ ously introduced into the polyahl or polyahl mixture by reacting said polyahl or polyahl mixture or a com¬ ponent or portion thereof with a difunctional compound having an additional polymerizable ethylenically unsat- urated group especially vinyl group, i.e., -CHR'=CHR', wherein each R 1 is independently hydrocarbyl, prefer¬ ably lower alkyl or hydrogen, and another functional group which reacts with polyahl to form a bond between the difunctional compound and the polyahl. Suitable such functional groups include, for example, carboxylic acid or anhydride, hydroxyl, epoxy and isocyanate groups. Preferably, the functional group is carboxylic acid or isocyanate. Suitable difunctional compounds include, for example, ethylenically unsaturated carboxylic acids such as arcylic acid, methacrylic acid, furmaric acid, maleic acid, and itaconic acid. The preparation of such adducts are described for example, in European Patent Application 0091036. Also pre- ferred are ethylenically unsaturated isocyanates, in particular isocyanatoalkyl esters of an ethyleni¬ cally unsaturated carboxylic acid. Suitable such isocyanates include the isocyanatoalkyl esters of acrylic or methacrylic acid, α,β-ethylenically unsat- urated isocyanates, monovinylidene aryl isocyanates and monovinylidene arylmethyl isocyanates. Exemplary isocyanatoalkyl esters include 2-isocyanatoethyl methacrylate, 2-isocyanoethyl acrylate, 3-isocyanatopropyl methacrylate, 1-methyl- -2-isocyanatoethyl methacrylate and l,l-dimethyl-2- -isocyanatoethyl acrylate with 2-isocyanatoethyl methacrylate being most preferred. Suitable methods of preparing said isocyanato esters are well known, e.g. as shown in U.S. Patent Nos. 2,718,516 and 2,821,544 and British Patent No. 1,252,099. Exemplary monovinylidene aromatic isocyanates and monovinylidene arylmethyl isocyanates include styrene isocyanate and vinylbenzyl isocyanate. Exemplary α,β-ethylenically unsaturated isocyanates include vinyl isocyanate and isopropenyl isocyanate. Isocyanatoethyl methacrylate is especially preferred. The preparation of adducts of a mono- or polyahl with such ethylenically unsaturated isocyanates is described, for example, in U.S. Patent Nos. 4,390,645 and 4,394,491. An ethylenically unsaturated monomer or mixture of monomers are polymerized in the polyahl or polyahl mixture in the presence of the aforementioned iodine or iodine-releasing inorganic compound. Suitable ethylenically unsaturated monomers include,, for example, aliphatic conjugated dienes such as butadiene and iso- prene; monovinylidene aromatic monomers such as styrene, α-methyl styrene, ar-methyl styrene, ar-(t-butyl)styrene, ar-chlorostyrene, ar-cyanostyrene and ar-bromostyrene; α,β-ethylenically unsaturated carboxylic acids and esters thereof such as acrylic acid, methacrylic acid, methyl methacrylate, ethyl acrylate, 2-hydroxyethyl acrylate, butyl acrylate, itaconic acid, and maleic anhydride; a,β-ethylenically unsaturated nitriles and amides such as acrylonitrile, methacrylonitrile, acrylamide, me hacrylamide, N,N-dimethyl acrylamide, and N-(dimethylaminomethyl)acrylamide; vinyl esters such as vinyl acetate; vinyl ethers; vinyl ketones; vinyl and vinylidene halides as well as a wide vari¬ ety of other ethylenically unsaturated materials which are copolymerizable with the aforementioned adduct, many of which have heretofore been employed in the formation of copolymer polyahls as described in U.S. Patent Nos. 3,823,201 and 3,383,351. It is understood that mixtures of two or more of the aforementioned monomers are also suitably employed in making the copolymer. Of the foregoing monomers, the monovinylidene aromatic monomers, particularly styrene, and the ethylenically unsaturated nitriles, particularly acr lonitrile, are especially preferred. The amount of ethylenically unsaturated monomer(s) employed in the copolymerization reaction is generally an amount sufficient to provide good reinforce¬ ment in urethane polymers and cell openings in urethane foams. Preferably, the amount of unsaturated monomer(s) is from 1 to 70, more preferably from 5 to 60, most preferably from 10 to 55, weight percent based on the weight of the copolymer dispersion. The amount of the graft polymerization sites employed in the polyahl or polyahl mixture is an amount sufficient to produce a stable dispersion and provide particle size control. Preferably, the amount of the adduct employed is suf¬ ficient to provide from 0.0002 to 1, more preferably from 0.005 to 0.5, most preferably from 0.02 to 0.5, moles of graft polymerization sites per mole of polyahl or polyahl mixture. The copolymerization is readily carried out by simultaneously adding a monomer(s) and a free radical catalyst to the polyahl or polyahl mixture in the presence of the reaction modifier under conditions sufficient to cause free radical addition polymerization. The temperature of the copolymerization is dependent upon the initiator and is preferably in the range from 25° to 180°C, most preferably from 110° to 140°C, when azo-type catalysts are used. Alternatively, the free radical catalyst may be dispersed in a portion of the polyahl and thereafter added along with the monomer to the remaining portion of the polyahl or polyahl mixture. Other polymerization processes, both continuous and batch, may be suitably employed. Suitably, the concentration of polymeriz¬ ation catalyst is any amount sufficient to cause copolymerization of the graft polymerization sites in the polyahl or polyahl mixture if any, and the ethyl¬ enically unsaturated monomer(s). Preferably, however, the concentration of catalyst is in the range from 0.1 to 20, more preferably from 0.5 to 5, weight percent based on the combined weight of the mono-adduct and other monomer(s). Catalysts suitably employed in the practice of the copolymerization are free radical type polymer¬ ization catalysts such as, for example, the peroxides, persulfates, perborates, percarbonates, and azo com¬ pounds. Examples of such catalysts include hydro¬ gen peroxide, t-butyl perioxide, di(t-butyl)peroxide, t-butyl peroctoate, lauroyl peroxide, cumene hydro- peroxide, t-butyl hydroperoxide, azobis(isobutyronitrile) as well as mixtures of such catalysts. Of the fore¬ going catalysts, the azo catalysts particularly azobis- (isobutyronitrile) and azobis(methylbutyronitrile) are preferred. The resulting copolymer polyahl is generally more stable and less viscous than a like copolymer polyahl prepared in the absence of the halogen, inter¬ halogen or iodine-releasing inorganic compound used herein. Accordingly, copolymer polyahls having a higher solids content can be prepared at any given viscosity according to this invention than according to conventional processes. Further reduction in viscosity can be achieved by diluting the copolymer polyahl with an additional polyahl (which may be the same or different from that used in preparing the copolymer polyahl) to obtain a lower solids blend. The lower solids blend normally exhibits a lower viscosity than that exhibited by a similar copolymer polyahl prepared directly with the same solids content. For example, a 50 percent solids copolymer polyahl prepared according to the invention may be diluted with additional polyahl to obtain 40 percent solids material. The diluted copolymer polyahl will generally exhibit a lower viscosity than a copolymer polyahl prepared accord¬ ing to this invention having 40 percent solids prior to any dilution. The resulting copolymer dispersion is readily reacted with an organic polyisocyanate to form desirable polyurethane products using conventional polyurethane reaction conditions and procedures. Such reaction and procedures are optionally carried out in the presence of additional polyahls, chain extending agents, cata¬ lysts, surface active agents, stabilizers, blowing agents, fillers and pigments. In the preparation of foamed polyurethane, suitable procedures for the preparation of same are disclosed in U.S. Patent No. RE 24,514. When water is added as the blowing agent, corresponding quantities of excess isocyanate to react with the water and produce carbon dioxide may be used. It is also possible to prepare poly- urethane plastics by a prepolymer technique wherein an excess of organic polyisocyanate is reacted in a first step with the graft copolymer dispersion of the present invention to prepare a prepolymer having free isocyanate groups which is then reacted in a second step with water to prepare a foam. Alter¬ natively, the components may be reacted in a single working step commonly known as the "one-shot" tech¬ nique of preparing polyurethanes. Furthermore, instead of water, low boiling hydrocarbons such as pentane, hexane, heptane, pentene, and heptene; azo compounds such as azohexahydrobenzodinitrile; halogenated hydrocarbons such as dichlorodifluoro- methane, trichlorofluoromethane, dichlorodifluoro- ethane, vinylidene chloride and methylene chloride may be used as blowing agents. The foams may also be prepared by the froth technique as described in U.S. Patent Nos. 3,755,212; 3,849,156 and 3,821,130. Organic polyisocyanates which may be employed include aromatic aliphatic and eyeloaliphatic polyiso¬ cyanates and combinations thereof. Representative of these types are the diisocyanates such as m-phenylene diisocyanate, tolylene-2,4-diisocyanate, tolylene-2,6- diisocyanate, hexamethylene-l,6-diisocyanate, tetra- methylene-1,4-diisocyanate, cyclohexane-1,4-diisocy- anate, hexahydrotolylene diisocyanate (and isomers), naphthylene-1,5-diisocyanate, 1-methoxphenyl- -2,4-diisocyanate, diphenylmethane-4,4-diisocyanate, 4,4'-biphenylene diisocyanate, 3,3'-dimethoxy-4,4'- -biphenyl diisocyanate, 3,3'-dimethyl-4,4'-diphenyl diisocyanate, and 3,3'-dimethyldiphenypropane-4,4' ,4'- -diisocyanate; the triisocyante polymethylene poly- phenylisocyante and tolylene-2,4,6-triisocyanate; and the tetraisocyanates such as 4,4'-dimethyl- diphenylmethane-2,2' ,5,5'-tetraisocyanate. Especially useful due to their availability and properties are tolylene diisocyanate, diphenylmethane- -4, '-diisocyanate and polymethylene polyphenylisocyanate. Crude polyisocyanate may also be used in the practice of the present invention, such as crude toluene diisocyanate obtained by the phosgenation of a mixture of toluene diamines or crude diphenylmethylene diisocy¬ anate obtained by the phosgenation of crude diphenyl- methylenediamine. The preferred undistilled or crude isocyanates are disclosed in U.S. Patent No. 3,215,652. The copolymer dispersions of this invention are preferably employed in combination with other polyahl(s) commonly employed in the art. Accordingly, any of the polyahls which are described above for use in the preparation of the polymer dispersions of the present invention may be employed. Chain extending agents which may be employed in the preparation of the polyurethane compositions of the present invention include relatively low equivalent weight compounds having at least two functional groups bearing active hydrogen atoms such as, for example, water, hydrazine, primary and secondary diamines, amino alcohols, amino acids, hydroxy acids, glycols or mixtures thereof. A preferred group of chain extending agents includes, for example, water and primary and secondary aromatic diamines which react more readily with the isocyanate than does water such phenylenedia ine, bis(3-chloro-4-aminophenyl)methane, 2,4-diamino-3,5-diethyl toluene, trisecondary butanol- amine, isopropanolamine, diisopropanolamine, N-(2- -hydroxypropyl)ethylenediamine, and N,N'-di(2- -hydroxypropyl)ethylenediamine. The reaction of polyisocyanate with the copolymer polyahl is advantageously carried out in the presence of an amount of urethane-type catalyst which is effective to catalyze reaction of the polyahl of the copolymer dispersion with the polyisocyanate. Prefer¬ ably, the amount of urethane catalyst is an amount comparable to that used in conventional urethane-type reactions. Any suitable urethane catalyst may be used including tertiary amines, such as, for example, tri- ethylenediamine, N-methyl morpholine, N-ethyl morpho- line, diethyl ethanolamine, N-coco morpholine, 1-methyl- 4- dimethylaminoethyl piperazine, 3-methoxy-N-dimethyl- propyl amine, N,N-dimethyl-N' ,N'-methyl isopropyl propylenediamine, N,N-diethyl-3-diethylaminopropyl amine, and dimethyl benzyl amine. Other suitable catalysts are, for example, tin compounds such as stannous chloride, tin salts of carboxylic acids such as dibutyltin di-2-ethyl hexoate, as well as other organometallic compounds such as are disclosed in U.S. Patent No. 2,846,408. A wetting agent(s) or surface-active agent(s) is generally necessary for production of high grade polyurethane foam according to the present invention, since in the absence of same, the foams collapse or contain very large uneven cells. Numerous wetting agents have been found satisfactory. Nonionic sur¬ factants and wetting agents are preferred. Of these, the nonionic surface-active agents prepared by the sequential addition of propylene oxide and then ethylene oxide to propylene glycol and the solid or liquid organosilicones have been found particularly desirable. Other surface-active agents which are operative, although not preferred include polyethyl¬ ene glycol ethers of long chain alcohols, tertiary amine or alkylolamine salts of long chain alkyl acid sulfate esters, alkyl sulfonic esters and alkyl arylsulfonic acids. The following examples are given to illus¬ trate the present invention and are not to be con¬ strued as limiting the scope thereof in any manner. All parts and percentages are by weight unless other¬ wise indicated. Example I In this and following examples, Polyol A refers to a 3000 MW triol prepared by reacting a trifunctional initiator with a mixed ethylene oxide/- propylene oxide feed. Polyol B is a 4600 MW triol prepared by reacting a trifunctional initiator with a mixed ethylene oxide/propylene oxide feed and then capping about 20 percent of the terminal hydroxyl groups with isocyanatoethyl methacrylate. To a one gallon agitated vessel are added 143 grams of Polyol A and 181 grams Polyol B. This mixture is heated to 130°C under a nitrogen atmos¬ phere. Then, 826 grams of Polyol A, 27 grams of azobis (methyl butyronitrile), 1050 grams of styrene, 450 grams of acrylonitrile, 4.8 grams of iodine and 120 grams of Polyol B are added to the vessel over a period of one hour. Then, an additional 230 grams of Polyol A that has been mixed with 8 grams of the azo initiator are added over a period of from 15 to 30 minutes. During these additions, the temperature in the vessel is maintained at 135±5°C. The resulting copolymer polyol is vacuum stripped for a period of 1 to 2 hours to remove the remaining unreacted monomers The product copolymer polyol contains 47 percent solids and has a BrooKfield viscosity of 4680 cps (4.68 Pa*s) at 25°C. There is minimal agglomeration of the suspended copolymer particles seen on visual inspection. In comparison, a similar copolymer polyol prepared in the absence of the iodine has a viscosity well in excess of 10,000 cps (10 Pa«s) and is severely agglomerated. Example II Copolymer polyol Sample Nos. A-G are pre- pared by adding 201 grams Polyol A and 276 grams Polyol B to a one gallon agitated vessel. This mixture is heated to 125°C under a nitrogen atmos¬ phere. To the heated mixture are added over a period of one hour a mixture of 924 grams styrene, 396 grams acrylonitrile, 3.3 grams of a reaction modifier as indicated in Table I, 327 grams of Polyol A and 337 grams of Polyol B. Starting at the same time, a mixture of 30 grams azobis (methyl- butyronitrile) and 839 grams of Polyol A are added over a 76 minute period. During these additions, the temperature inside the reaction vessel is main¬ tained at 130±5°C. The resulting copolymer polyol is vacuum stripped for one to two hours to remove residual monomer, and cooled to room temperature. Comparative Sample No. I-C is prepared in like manner in the absence of any reaction modifier. The Brookfield viscosity at 25°C of Sample Nos. A-G and Comparative Sample No. I-C are measured and are as reported in Table I following. None of the samples of this invention have more than slight agglomeration of the suspended copolymer particles. The comparative sample, however, is severely agglomerated. TABLE I - Reaction % Solids Sample No. Modifier (Calculated) Viscosity Cps (Pa « s) A T 2 40 4400 (4.40) B IBr 40 4840 (4.84) C IC1 40 3950 (3.95) D Br 2 40 7940 (7.94) E Zrl 4 40 4920 (4.92) F sbi 3 40 4330 (4.33) G CSI 3 40 6050 (6.05) I-C None 40 13,520 (13.52) It is seen that the presence of the halogen, interhalogen or inorganic iodine releasing compound in all cases except Sample No. D causes the viscosity of the copolymer polymer below 6000 cps (6.0 Pa*s). A viscosity below 6000 cps (6.0 Pa*s) using Br 2 as reaction modifier is readily achieved by slightly increasing the amount used.

Claims: CLAIMS 1. A process for preparing a polymer polyahl comprising polymerizing an ethylenically unsaturated monomer or mixtures thereof in a polyahl or polyahl mixture whereby a dispersion of polymer particles is prepared in a continuous polyahl phase, characterized by conducting said polymerization in the presence of a halogen, inter¬ halogen or iodine-releasing inorganic compound. 2. The process of Claim 1 characterized in that the polymerization is conducted in the presence of iodine. 3. The process of Claim 1 characterized in that the polymerization is conducted in the presence of iodine chloride or iodine bromide. 4. The process of Claim 1 characterized in that the iodine-releasing inorganic compound is Zrl 4 , Sbl 3 , Csl 3 , PI 3 / Pi c or Asl 3 - 5. The process of Claim 1 characterized in that the iodine-releasing inorganic compound is an organometal iodide. 6. The process of Claim 1 characterized in that the iodine or iodine-releasing inorganic compound is employed in an amount from 0.1 to 2 per¬ cent by weight of the ethylenically unsaturated monomer or mixture of monomers. 7. The process of Claim 1 characterized in that the polyahl or polyahl mixture contains graft polymerization sites. 8. The process of Claim 7 characterized in that the polyahl or polyahl mixture contains pur¬ posefully introduced ethylenic unsaturation. 9. The process- of Claim 8 characterized in that the polyahl or polyahl mixture comprises the reaction product of a polyahl and a difunctional com¬ pound having an additional polymerizable ethylenically unsaturated group and another functional group which reacts with a polyahl to form a bond between the difunc¬ tional compound and the polyahl. 10. The process of Claim 9 characterized in that the difunctional compound is an ethylenically unsaturated isocyanate.

Inventors: NORTON MICHAEL A, SERRATELLI JOHN F, NORTON, MICHAEL, A., SERRATELLI, JOHN, F.
Applicants: DOW CHEMICAL CO, THE DOW CHEMICAL COMPANY
Application year: 1985
Main classification: C08K5
IPC codes: C08F2, C08F283, C08F290, C08G18