LIQUID ORGANIC POLYISOCYANATE COMPOSITION FOR USE IN REACTION INJECTION MOLDING IN PRESENCE OF SILOXANE MOLD RELEASE AGENT

Abstract: Polyurethane products are made by reaction injection molding in the presence of a defined polysiloxane mold release agent which includes isocyanate reactive groups. The polysiloxane may be included in the polyol or in the isocyan­ ate, and in the latter case, an additional silicone surfactant is present to prevent premature reaction with the isocyanate.

Description: PROCESS FOR MAKING POLYURETHANE AND RELATED PRODUCTS BY REACTION INJECTION MOLDING IN PRESENCE OF SILOXANE MOULD RELEASE AGENT AND COMPOSITIONS THEREFOR. The invention is directed to polyurethane, polyurea and polyureaurethane polymers having improved mold release properties. Specifically, it is directed to a process for forming mold releasable polymers by reacting liquid poly-isocyanates, polyols, polyamines and polyolamines having incorporated therewith certain polysiloxane derivatives having hydroxy, amino or mercapto functional side chains as internal release agents. The process of the invention is especially useful in manufacturing shaped polymer components by a reaction injection molding process (RIM) wherein a liquid stream of polyisocyanate is impingement mixed with at least one other stream containing active hydrogen containing organic liquids, catalysts, fillers and the mold release agents of the invention into a metal mold to cure. Recent developments in the chemistry of the polymer systems have resulted in urethane and urethaneurea polymers which are sufficiently cured to be demolded within 20-30 seconds after injection. RIM equipment has improved so that the mechanics of opening and closing the mold also require only 30-40 seconds. Urethane polymers are excellent adhesives and bond tenaciously to metal so it is necessary to apply a release agent to the mold surface so that the parts can be easily and quickly removed without damage or distortion. The molds are complex and must be completely and uniformly covered, usually by spraying a solution or emulsion of soap or wax. This procedure requires 30-60 seconds and must be done at least after every 3-5 parts and more often after each part, thus increasing the part to part cycle time by as much as 50%. In addition, this constant spraying and respraying causes excessive mold release to build up on some parts of the mold surface causing loss of gloss of the molded part. This means that periodicaly the mold must be wiped off, to remove excess release agent and, about once every 150 to 200 parts, must be completely cleaned, and reprepared for molding. This can add another 10-20% to the time required to mold each part. Furthermore, the external release agent is, obviously, removed from the mold because it adheres to the molded part and must be washed off the part before it is painted, thus providing a possible source for part quality problems. Clearly, the reduction of the need to apply external release agent could reduce the present cycle time by 50% or more, thus increasing productivity and reducing unit cost. In addition, it would reduce quality problems by reducing surface blemishes resulting from build up of release agent on the mold and by reducing paint rejects by reducing the amount of external release agent left on the surface on each part. While the internal mold release agent dispersions of this invention can provide easy removal from an untreated mold surface at least for several parts, more efficient operation can be achieved by treating the mold surface with a standard release agent first and then again after each batch of about 10 to about 50 parts. In the operation of a reaction injection molding process multiple streams of reactants are metered into a mixer and immediately injected into a mold. For example a blend of isocyante reactive ingredient such as polyols, polyolamines, polyamines including catalysts, fillers, dyes, coloring agents are metered as one stream and impingement mixed with a polyisocyanate as a second stream and are thereafter injected into the mold for curing. In some instances a third or fourth stream is required to introduce an active ingredient which may prematurely react with one of the other components of the resin system. The polysiloxane mold release agents of the present invention are somewhat reactive with polyisocyanate and are therefore preferable added to the polyisocyanate stream shortly before it is mixed with the other active ingredients. However, the mold release agents can suitably be added with the polyol stream or metered in as a third stream where such equipment is available. If the reactive polyisocyanates are prematurely mixed with the polysiloxane mold release agent of this invention gelation occurs within a few hours and after a period of about 24 hours the isocyanate stream can no longer be metered due to complete gelation. Such premature gelation can be inhibited by incorporating a silicone surfactant with the polysiloxane ingredient. The present invention provides a process for preparing polymer products by the reaction injection molding technique which comprises mixing liquid organic polyisocyanates with reactants selected from polyols, polyamines, polyolamines and catalysts characterised in that there is dispersed therewith from 0.5-20 percent by weight based on the total reaction mix of a polysiloxane mold release agent which consists essentially of 0.5-20 mold percent of RaRtbsiO [ 4-(a+b) ] /2 units and from 80-99.5 mol percent of R"CSiO(4¯c)/2 units where R is an isocyanate reactive organic radical, a has an average value of from 1-3, R' and R" are both non-isocyanate reactive organic radicals, b has an average value of 0-2, a+b is from 1-3, and c has an average value of from 1-3, wherein the ratio of the total molecular weight to the total number of isocyanate reactive functional groups in the molecule ranges from 100-3500, the combined formula weights of all isocyanate reactive organic radicals, R do not exceed 40% of the total molecular weight of said polysiloxane mold release agent, the combined formula weights of all nonisocyanate reactive radicals, R'+ R" together do not exceed 40% of the total molecular weight of said polysiloxane mold release additive, the combined formula weights of all the organic radicals R + R' + R" in the molecule together do not exceed 60% of the total molecular weight of the molecule, said polysiloxane mold release agent contains an average of at least two isocyanate reactive functional groups per molecule, at least two of the isocyanate reactive functional groups in each molecule are located on separate organic radicals, R, attached independently to different silicon atoms in said polysiloxane, said isocyanate reactive functional grous (R) are selected from alcohols, phenols, thiols, primary or secondary aromatic amines, which contain no oxygen, and not more than one nitrogen, atoms attached directly to, in conjugation with, or incorporated within, the aromatic ring nucleus, and secondary aliphatic amines wherein at least one of the alkyl carbon atoms, bonded directly to the nitrogen atom, is not a primary carbon atom and carboxylic acids, the molecular weight of said polysiloxane mold release agent ranges from 1000 and 30,000, and said polysiloxane mold release agent being substantially insoluble in said liquid polyisocyanate. In these mold release agents the hydroxy, mercapto, or amino organic R radicals having preferably a molecular weight in the range of 100-400 can be attached to the silicon atom directly to carbon or through oxygen, nitrogen or sulfur carbon bonds. Particularly preferred R radicals are those of the formula HO-R111-, H2N-R#'-, HNR2"', HS-R"'-, wherein R"' is a divalent linking group composed of carbon and hydrogen; carbon, hydrogen and oxygen; carbon, hydrogen and sulfur; carbon, hydrogen and nitrogen; or carbon, hydrogen, oxygen and nitrogen. Specific examples of R"' include the methylene, ethylene, propylene, hexa-methylene, decamethylene, -CH2CH(CH3 )-CH2-, phenylene, butyl phenylene, naphthylene, -CH2CH2SCH2CH2-, -CH2CH2OCH2-, -CH2CH2-CH2-o(CH2-CHRXO)n- where n is 0-5 where R' is described as above or H, a preferred R group is #CH2CH2CH2O(CH2CH(CH3)O)nH where n=1-5 having an hydroxyl equivalent weight of 5002000. It is preferred that the R n linking group contains from 3-10 atoms in addition to hydrogen atoms. There can be from 1-33 functional R radicals, preferably 3-10, and from 1-3 attached to a silicon atom. As indicated above, the R' radical can be any hydro-carbon or substituted organic radical. Illustrative of the R' radicals that can be present are alkyl radicals such as the methyl, ethyl, propyl, butyl amyl, hexyl, octyl, decyl, dodecyl, and octadecyl, and myristyl radicals, alkenyl radicals such as the vinyl, allyl, and hexenyl radicals; cycloalkyl radicals such as the cyclobutyl and cyclohexyl radicals; aryl radicals such as the phenyl, and naphthyl radicals; aralkyl radicals such as the benzyl and 2-phenylethyl radicals; alkaryl radicals such as the tolyl, xylyl and mesityl radicals; the corresponding halohydrocarbon radicals such as 3-chloropropyl, 4-bromobutyl, 3,3, 3-tri-fluoropropyl, chlorocyclohexyl, bromophenyl, chlorophenyl, alpha,alpha,alphatrifluorotolyl and the dichloroxenyl radicals; the corresponding cyanohydrocarbon radicals such as 2-cyanoethyl, 3-cyanopropyl and cyanophenyl radicals; the corresponding radicals such as ether and ester hydrocarbon radicals such as -(CH2)30C2H5, -(CH2)3OCH3, -(CH2)3COOC2H5, and (CH2)3COOCH3, the corresponding thioether and thioester hydrocarbon radicals such as -(CH2)3SC2H5 and -(CH2)3COSCH3; and nitrohydrocarbon radicals such as the nitrophenyl and 3-nitropropyl radicals. It is preferred that the R' radical be an organic radical containing from 1 to 10 atoms. In the most preferred embodiment of tbis invention at least 90 percent of all the R' radicals are methyl radicals. There can be an average of from 0 to 2 R' radicals attached to the silicon atom, i.e., b has an average of from 0 to 2 in the above formula. The R" radical in the functional isocyanate reactive siloxanes of this invention can also be any hodrocarbon or substituted hydrocarbon radical. The illustrctive examples given with respect to R' above are equally applicable here and are not repeated for the sake of brevity. Likewise, the preferences set forth for R' above also apply to the R" radical. There can be from 0 to 3 R" radicals, on the average, per silicon atom, i.e., c has an average value of from 1 to 3 in the above formula. These polysiloxane mold release agents are made by well known techniques and are usually formed bj grafting an olefin containing organic modifying group or plyoxyalkylene oxide onto a "methylhydrogen siloxane" modifies polydimethylsiloxane using a platinum catalyzed hydrolisatrn reaction. The functional siloxanes of the mold release agent can be either solid or liquid in form and are required to be substantially insoluble in isocyanate liquid unbar RIM operating conditions. In order to use a solid functional siloxane it would be necessary to dissolve, disperse or suspend the siloxane in one or more silicone surfactants. Hence it is much preferred that the functional siloxane employed be in liquid form. While the viscosity of the liquid siloxane can vary over a wide range, for example from 1 to 100,000 cs., it is generally preferred that the viscosity be in the range of from 50 to 1000 cs. Molecular weight can vary from 1000 to 30,000, preferrably 2000-20,000 and most preferred 4000-8000. The formulations of the invention include from 0.5-15 percent by weight of a polysiloxane such as those included in the above described definition and specifically but not limited to those in the following list having RaR' b SiO [ 4-(a+b)#2 units and R" SIO /2 units and wherein the value listed for (d) is the equivalent weight, (e) is the combined formula weights or reactive radicals R expressed as percent of the molecular weight, (f) is the combined formula weights of non-isocyanate reactive groups R'+R" expressed as percent of the molecular weight: "Polysiloxane I" is a hydroxy functional polysiloxane polyether copolymer internal mold release agent having the approximate formula: : 3 3 3)2 6666666 having a molecular weight of about 6000, a hydroxy equivalent weight (d) of 2000, (e) is 13Z, (f) is 35Z, and a viscosity of 160 centistokes. "Polysiloxane II" is a hydroxy functional thioether copolymer internal mold release agent having the speculative formu: [HOCH2CH2SCH2CH2CH2(CH3)2SiO] [Si(CH3)2O]65[Si(CH3)2CH2CH2CH2SCR2CH2OH] having a hydroxy equivalent weight (d) of 2750, a molecular weight of 5500, a value for (e) of 4.7%, (f) is 37Z and a viscosity of about 55 centistokes. "Polysiloxane III" has a general formula as follows: (CH3)3SiO[Si(CH3)20]134[Si(CH3)(C3H6OC2H3(OH)CH2OH)-O]16Si(CH3)3 a molecular weight 13,136, (d) equivalent weight of 411, (e) is 16% and (f) is 33%. "Polysiloxane IV" has a general formula as follows: (cH3)3sio[si(CH3)2o]63[si(cH3) (C3H6OC2H3(oH)CH2oH)-o]7si(CH3)3 a molecular weight 6,154, (d) equivalent weight 440, (e) is 15%, and (f) is 34%. "Polysiloxane V" has a general formula: (CH3)3SiO [ Si(CH3)20 ] 65tSi(CH3) CC3H6OC2H3COH)CH2OH)-O15SiCCH3)3 a molecular weight of 6068, (d) equivalent weight 607, (e) is 11%, and (f) is 35%. "Polysiloxane VI" has a general formula: (CH3)33i0 [ SiCCH3)2O ] 56 [ Si(CH3)C3H60(C2H3 (OH)CH2OH)Ol14SiCCH3)3 a molecular weight of 6980, (d) equivalent weight 249, (e) is 26%, and (f) is 28%. N "Polysiloxane VII" has a general formula: CH3CH(OH)CH2OC3H6Si(CH3)2O[Si(CH3)2O]89Si(CH3)2C3H6OC2H4(OH)CH3 a molecular weight of 6962, (d) an equivalent weight of 3481, (e) is 3.7Z, and (f) is 39%. "Polysiloxane VIII" has a general formula: (CH3)3SIO[SI(CH3)2O]66[(CH3)SI(C4H8-PH-NH(C3H7)O]3SI(CH3)3 where PH = phenylene a molecular weight of 5782, and equivalent weight (d) of 3481, (e) is 9.9% and (f) is 37%. "Polysiloxane IX" has a general formula: (CH3)3SiO[Si(CH3)20]55[HOCH2CHOHCOHCH(CH2OH)CH(CH2OH)Si(CH3)0]14Si(CH3)3 a molecular weight of 7550, an equivalent weight (d) of 108, (e) is 33% and (f) is 26%. "Polysiloxane X" has a general formula: CCH3)3SiO [ SiCcH3)2O ] 61 [ 3)2Ol61[(CH3)Si(C3H6OCH2CH(OH)CH2OH)O] 9SiCCH3)3 a molecular weight of 6390, an equivalent weight (d) of 355, (e) is 19% and (f) is 322. "Polysiloxane XI" has a general formula: (CH3)3SiO[Si(CH3)2O]82[Si(CH3)(c3H6O(C2H3CH3O)2C2H4CO2H)O]3Si(CH3)3 For the purpose of carrying out processes according to the invention, the defined mold release agent may be incorporated into the isocyanate or the polyol or polyamine or may be introduced as a third stream on its own into a mixing head. Therefore, a further aspect of the present invention provides a liquid composition for use in a process of the type described above which comprises at least one organic polyol or polyamine having from 2 to 6 isocyanate reactive hydrogen atoms and a molecular weight of 1000 to 10,000 having dispersed therein from 0.5 to 8.0 percent by weight of a polysiloxane mold release agent of the type described above. The exact polyol or polyamine or mixture thereof employed depends upon the end use of the resin product to be produced. For example, when polyurethane foams are prepared the molecular weight or the hydroxyl number is selected to result in flexible or semiflexible foams. The polyols in this instance preferably possess a hydroxyl number of from about 50 to about 150 for semiflexible foams and from about 20 to about 70 for flexible foams. As a further example, for elastomer application would generally be desirably to utilize high molecular weight polyols having relatively low hydroxyl numbers for example 20-50-or-so.-Such-limits are not intended to be restrictive but are merely illustrative of the large number of possible combinations of the polyols or polyols used. The relatively high molecular weight hydroxylcontaining polyols which can be employed herein are those polyether and polyester polyols which have an average hydroxyl functionality of from 2 to 6, preferably from 2 to 4 and most preferably from 2 to 3 and an average hydroxyl equivalent weight of from 500 to 5000, preferably from 1000 to 3000 and most preferably from 1500 to 2500 including mixtures thereof. Suitable relatively high molecular weight polyether polyols which can be employed herein include those which are prepared by reacting an alkylene oxide, halogen substituted or aromatic substituted alkylene oxide or mixtures thereof with an active hydrogencontaining initiator compound. Suitable oxides include, for example, ethylene oxide, propylene oxide, 1,2-butylene oxide, 2,3-butylene oxide, styrene oxide, epichlorohydrin, epibromohydrin, mixtures thereof and the like. Su'itable initiator compounds include water, ethylene glycol, propylene glycol, butanediol, hexanediol, glycerine, trimethylol propane, pentaerythritol, hexanetriol, sorbitol, sucrose, hydroquinone, resorcinol, catechol, bisphenols, novolac resins, phosphoric acid, mixtures thereof and the like. Also suitable as initiators for the relatively high molecular weight polyols include, for example, ammonia, ethylenediamine, dianinopropanes, diaminobutanes, diaminopentanes, diaminohexanes, diethylenetriamine, triethylenetetramine, tetraethylenepentamine, pentaethylenehexamine, ethanolamine, aminoethylethanolamine, aniline, 2, 4-toluenediamine, 2, 6-toluene- diamine, diaminodiphenyloxide (oxydianiline), 2,4' -diaminodi- phenylmethane, 4,4'-diaminodiphenylmethane, 1,3-phenylenediamine, 1,4 -phenylenediamine, naphthylene-1,5-diamine, triphenylmethane 4,4'-di(methylamino)-diphe ,,4"-triamine,4,4'-di(methylamino)-diphenylmethane, l-methyl 2-methylamino-4-aminobenzene, 1,3-diethyl-2,4-diaminobenzene, 2,4-diaminomesitylene, 1-methyl-3 ,5-diethyl-2 ,4-diaminobenzene, 1-methyl-3 ,5-diethyl-2 ,6-diaminobenzene, 1,3,5-triethyl-2,6-diaminobenzene, 3,5,3' ,5' -tetraethyl-4,4'-diaminodiphenylmethane and amine aldehyde condensation products such as the polyphenylpolymethylene polyamines produced from aniline and formaldehyde, mixtures thereof and the like. Suitable polyester polyols which may be employed herein include, for example, those prepared by reacting a polycarboxylic acid or anhydride thereof with a polyhydric alcohol. The polycarboxylic acids may be aliphatic, cycloaliphatic, aromatic and/or heterocyclic and may be substituted (e.g., with halogen atoms) and/or unsaturated. Example of carboxylic acids of this kind include succinic acid; adipic acid; suberic acid; azelaic acid; sebacic acid; phthalic- acid; isophthalic acid; trimellitic acid; phthalic acid anhydride; tetrahydrophthalic acid anhydride; hexahydrophthalic acid anhydride; tetraclorophthalic acid anhydride; endomethylene tetrahydrophthaic acid anhydride; glutaric acid anhydride; maleic acid; maleic acid anhydride; fumaric acid; dimeric and trimeric fatty acids; such as oleic acid, which may be in admixture with moncmeric fatty acids, terephthalic acid dimethyl ester; terephtaalic acid bisglycol ester and the like. Mixtures of such acids or anhydrides may also be employed. Examples of suitable polyhydric alcohols include ethylene glycol, 1,2-propylene glycol; 1,3-propylene glycol; 1,4-, 1,2- and 2,3-butylene glycol; 1,6-hexane diol; 1,8-octane diol; neopentyl glycol; cyclohexane dimethanol (1,4-bis-hydroxy-methyl cyclohexane) 2-methyl-1,3-propane diol; glycerol; tri-methylol propane; 1,2 ,6-hexane triol; 1,2,4-butane triol; tri-methylol ethane; pentaerythritol; quinitol; mannitol; sorbitol; methyl glycoside; diethylene glycol; triethylene glycol; tetraethylene glycol; polyethylene glycol; dipropylene glycol; polypropylene glycols; dibutylene glycol; polybutylene glycols and the like. The polyesters may contain some terminal carboxyl groups. It is also possible to use polyesters of lactones such as caprolactone, or hydroxy carboxylic acids such as hydroxy caproic acid. Other polyols which can be employed herein include polymer-containing polyols such as, for example, those disclosed in U.S. Patent Nos. RE 29,118 (Stamberger), RE 28,715 (Stamberger), RE 29,014 (Pizzini et al.) and 3,869,413 (Blankenship et al.) all of which are incorporated herein by reference. In addition to those above-described polyols are the polymer/polyol blends which are normally liquid stable polymer/ polyol compositions formed by polymerizing in the presence of a free radical catalyst from about 10 to about 50 weight percent of a mixture of an ethylenically unsaturated monomer such as acrylonitrile or styrene of mixtures thereof dissolved or dispersed in a polyol mixture. Amine equivalents of the above described polyols and blends therewith are used in making polyurea and polyureaurethanes. Polyoxyalkylene polyamines and cyano-alkylated polyoxyalkylene polyamines having a molecular weight of 1000-10,000 with a preferred range of 2000 to 7000 which have the general formula: H2NCH2#CXH(OCH2CHX)yNH2 where X is H or alkyl group having 1-18 carbon atoms and where y is a number of about 20-200; and triamines of poly-alkoxylated trimethylol propane having the general formula: CH3CH2C [ CH2(OCH2-CHX)zNH233 where z is an average of 10-100 are also useful materials for the blends of the invention. These amines are prepared according to the procedure outlined in a U.S. Patent No. 3,666,788 the teachings of which are hereby incorporated by reference. These materials have the general formula: R [ (OCH2CHX)nOCHYCHZNHA ] m where R is the nucleus of an oxyalkylation-susceptible aliphatic polyhydric alcohol containing 2-20 carbon atoms and 2-6 hydroxyl groups, A is hydrogen or a cyano or lower alkyl radic-al having one or two carbon atoms between the nitrogen and cyano radical provided at least one A is a cyano-lower-alkyl radical, Z is an alkyl group containing 1-18 carbon atoms, n has an average value 10-100 and m is 2-6, R is saturated and consists of carbon and hydrogen. The methyl and ethyl alkyl groups of A may be substituted by lower alkyl groups The blends may-include lower molecular weight polyols and polyamines than those listed above, Polyols and polyamines useful in the process of the invention can be demonstrated by but not limited to those in the following list some of which are well known in the art and are readily commercially available "Polyol A" is a polypropylene oxide triol (the designation of this and subsequent polyols as a "triol" or "diol" represents the nominal functionality based solely on the starter used; the actual functionality will be somewhat less) having about 10 percent external ethylene oxide content, a hydroxyl number of about 48 and a number average molecular weight of about 3300. "Polyol B" is a polypropylene oxide diol having about 15 percent external ethylene oxide content, a hydroxyl number of about 38 and a number average molcular weight of about 2800. "Polyol C" is a polypropylene oxide triol having about 14 percent internal ethylene oxide content, a hydroxyl number of about 47 and a number average molecular weight of about 3300. "Polyol D" is a polyol produced from propylene oxide, sorbitol and glycerine having an external ethylene oxide content of about 15 percent, a hydroxyl number of about 28 and a number average molecular weight of about 7100. "Polyol E" is a polypropylene oxide triol having an external ethylene oxide content of about 15 percent, a hydroxyl number of about 27 and a number average molecular weight of about 4400. "Polyol F" is a polypropylene oxide triol having an internal ethylene oxide content of about 14 percent, a hydroxyl number of about 24 and a number average molecular weight of about 5000. "Polyol G" is a polypropylene oxide triol having an internal ethylene oxide content of about 8 percent, a hydroxyl number about 56 and a number average molecular weight of about 2800. "Polyol H" is a polypropylene oxide triol having an internal ethylene oxide content of about 16.5 percent, a hydroxyl number of about 35 and a number average molecular weight of about 4000. "Polyol I" is a polypropylene oxide triol having an external ethylene oxide content of about 17 percent, a hydroxyl number of about 39 and a number average molecular weight of about 4200. "Polyol J" is a polypropylene oxide triol having an internal ethylene oxide content of about 10 percent, a hydroxyl number of about 50 and a number average molecular weight of about 3100. "Polyol K" is a polypropylene oxide triol having an external ethylene oxide content of about 15 percent, a hydroxyl number of about 35 and a number average molecular weight of about 4000. "Polyol L" is a polypropylene oxide triol having an external ethylene oxide cap with a 6000 M.W. and a hydroxyl value of 27.4 mg KOH/gm grafted to 20Z by weight polyacrylonitrile polymer commercially available as Niax D-440 (Union Carbide). "Polyol M" is a polypropylene oxide/polyethylene oxide triol having a molecular weight of 10,000 and a hydroxyl number of 17. "Polyol N" is a polypropylene oxide/polyethylene oxide triol having molecular weight of 1000 and a hydroxyl number of 150. "Polyamine O" is a polypropylene oxide/polyethylene oxide triamine of molecular weight 3000 and is commercially available as Jeffamine T3000 (Jefferson Chem). "Polyamine P" is a 5000 molecular weight polypropylene oxide/polyethylene oxide polyamine having total amine content of 0.48 mg/gram, .58 mg/gram of primary amine and commercially available Jeffamine T5000. Alternatively, the defined mold release agent may be incorporated into the isocyanate component. Simple mixtures of isocyanate and a reactive siloxane could be used but owing to the possibility of premature reaction, such compositions are preferably prepared only just before, or as part of the reactive mixing with polyol or polyamine. Reacted isocyanate and hydroxy terminated siloxanes of a certain type have already been described in US Patent 4 033 912. It has been found that the polysiloxane mould release agents of the type described herein may be incorporated into the isocyanate component provided that an additional non-reactive silicone surfactant is also present. There is therefore provided, in accordance with a further aspect of the present invention, a liquid organic polyisocyanate composition for use in a process of the type described above which comprises a polyisocyanate having dispersed therein from 1 to 15 percent by weight of a polysiloxane mold release agent of the type described herein said polysiloxane mold release agent being substantially insoluble in said liquid polyisocyanate and from 1 - 25 percent by weight based on the weight of said polysiloxane mold release agent of a liquid silicone surfactant substantially free of isocyanate reactivity whereby said liquid remains substantially ungelled and fluid up to 250C. These dispersions are preferably made by adding the silicone surfactant and isocyanate reactive polysiloxane mold release agent to the liquid polyisocyanate employing high shear mixing equipment at room temperature. If ingredients are added separately it is preferred to add the surfactant to the polyisocyanate liquid before adding the isocyanate reactive polysiloxane mold release agent. Alternatively, the surfactant and polysiloxane mold release agent may be preblended before mixing with the isocyanate. In most instances stable liquid dispersions are obtained from blends which contain 1-15 percent by weight of the functional polysiloxane compound and based upon the weight of the polysiloxane mold release agent from 2-25 and preferably from 5-15 percent by weight of a silicone surfactant. Since these dispersions are not stable without the silicone surfactant it is theorized that the surfactant acts as an inhibitor agent for the isocyanate reactive groups in the polysiloxane mold release agent and that the surfactant silicone must be present in amounts sufficient to at least coat the mold release agent to inhibit reaction with the isocyanate at temperatures up to 25 C. It is important to mix the components with high shear mixing equipment especially since the polysiloxane mold release agent is substantially incompatible or insoluble in the polyisocyanate liquid. The organic polyisocyanates that are useful in producing polyurethane products in accordance with this invention are organic compounds that contain at least two isocyanate groups. Such compounds are well known in the art. The preferred polyisocyanates used in the invention are aromatic derivatives which are liquids at room temperatures. Such materials are readily commercially available such as the isomers of toluenediisocyanate, diphenylmethane diisocyanate and methylene bridged polyphenylmethane polyisocyanates isophorane diisocyanate and hydrogenated derivatives of MDI. Many of the polyphenyl polymethylene polyisocyanates which are prepared by aniline formaldehyde condensations followed by phosgenation ("crude MDI") and polyisocyanates which contain carbodiimide groups, uretonimine groups, urethane groups, sulfonate groups, isocyanurate groups, urea groups or biuret groups. Derivatiyes containing small amounts of pre-reacted low molecular weight polyols such as butylene glycol and propylene glycol or hydroxy esters to form stable liquids are useful. Such combinations are readily available and well known in the urethane manufacturing art. Of particular interest to this invention are compositions containing the 2,4' and 4,4' diphenylmethane diisocyanate isomers which are quasi prepolymers containing 1-18% by weight or about .1-.3 mol percent of polyols having a molecular weight of 75-700 and especially 75-200 such as propylene glycol, butylene, and poly1,2-propylene ether glycols having a molecular weight of from 134 to 700. Of additional interest to the invention are carbodiimide, uretonimine modified derivatives of diphenylmethane diisocyanates which have been further modified by the addition of high molecular weight polyols such as polyether diols and triols having a molecular weight of 1000-8000. In general the polyol modified isocyanate have a free -NCO content of 15-47Z by weight and more often 20-30Z. Typical polyisocyanates for use in the invention are exemplified but not limited to the following: "Polyisocyanate 1" is made by prereacting pure diphenylmethanediisocyanate with 10Z by weight of a polyol mixture containing 19 parts 1,2 propylene glycol, 22 parts 2,3 butylene glycol and 59 parts tripropylene glycol and the resultant product having 23Z by weight free isocyanate commercially available as Rubinatet 179 isocyanate from Rubicon Chem. "Polyisocyanate 2" is uretonimine modified 4,4' diphenylmethane diisocyanate having 29.3Z free -NCO and a functionality of 2.1 which is further reacted with 1.3Z by weight 1,3 butylene glycol to give a free isocyanate content of 27.4z. "Polyisocyanate 3" is similar to "Polyisocyanate 1" made by reacting 18Z by weight mixed polyols to a free isocyanate content of 15%. "Polyisocyanate 4" is similar to "Polyisocyanate 2" made by reacting a uretonimine modified polyisocyanate having a free -NCO content of 31Z further reacted with 1.3Z by weight 1,2 propylene glycol to a free isocyanate content of 29.3%. "Polyisocyanate 5" is similar to "Polyisocyanate 2" made by reacting 2% by weight of 1,2 propylene glycol to a free -NCO content of 27.4%. "Polyisocyanate 6" is similar to "Polyisocyanate 2" made by prereacting with 2% by weight tripropylene glycol. "Polyisocyanate 7" is similar to "Polyisocyanate 2" made by prereaction with 10% by weight of the polyol mixture described in "Polyisocyanate 1" to given an -NCO content of 20%. "Polyisocyanate 8" is similar to "Polyisocyanate 7" using 5% by weight of the polyol mixture to give an -NCO content of 24.5%. "Polyisocyanate 9" is similar to "Polyisocyanate 2" made by prereaction with 2% by weight 1,3 butylene glycol. The silicone surfactants which are used as dispersing agents and inhibitors for the polysiloxane mold release agent containing polyisocyanate liquid dispersions of the invention are modified polydialkyl siloxane polymers especially polydimethyl-siloxanes. These materials are well known and readily commercially available in numerous modifications having side chains linked to the silicon atoms through linking groups composed of carbon and hydrogen; carbon, hydrogen and oxygen; carbon, hydrogen and sulfur; carbon, hydrogen and nitrogen; or carbon, hydrogen, oxygen and nitrogen. Those which are substantially free of isocyanate reactivity at temperatures below 250C and which are completely or partly stable to moisture are preferred. For the most part these silicone surfactants are made by grafting on organic side chains which are substantially free of isocyanate reactivity. Silicone surfactants generally conform to the general formula: (CH3)3Si[OSI(CH3)2]y[(CH3)R+SiO]y[(CH3)R*SiO]zSi(CH3)3 x [ (CH3)R SiOly[CH3)R*SiO]zSi(CH3)3 * where the value of x, y or z vary from 10-1000 and where R+ and R may be the same or different and be selected from alkyl pendant radicals such as polyalkyl ether or alkoxyether groups such as #CH2CHROCCH2#CHRO)m#CmH2m+l or -OCH2CHRO(CH2CHRO) -C H2 where R is H, -CH3, -C2H5 where the sum of m+n is such that the total formula weight of the polyoxyalkylene block and other grafted radicals ranges from 800-40,000, the polysiloxane block ranges from 15-70Z of the molecular weight and n is 1-5; or grafted monovalent radicals selected from methoxy, ethoxy, ethylene, styrene, trifluoropropene, allyltetrahydro-furfuryl ether, allyloxyethyl acetate, acrolein diethylacetal, allylcyanide, allyloxyethyl cyanide, allylmorpholine, allyl-chloride and others. Surfactant of particular interest for use in the invention are polydimethylsiloxane-poly (polyethylene oxide/polypropylene oxide) block copolymers having the general formula: Me3SiO(Me2SiO)Y[Z'-O(CHMeCH2O)m(C2H4O)n-Z-Si(Me)O] ySiMe3 where Me = CH3, x is 42-125; y is 3-15; m is 15-30; n is 10-30; and Z' is alkyl, aryl or an aralkyl radical and most often methyl; and Z is an alkylene, arylene or an aralkylene radical and most often propylene or ethyl#ene. Preparation and use of these materials are described in U.S. Patents 3,505,377; 3,703,489; 3,980,688; and 4,071,483 of which are hereby incorporated by reference. Similar compositions wherein the divalent Z radical is linked to silicon through an oxygen, carbonyl, acetyl, sulfur, nitrogen or carbo nitrogen group are also included. Non-hydrolyzable surfactants are usually prepared by the platinum catalyzed addition reaction of a siloxane containing silanic hydrogens with a polyether whose chain is end blocked at one end by an alkenyloxy group (e.g., allyloxy) and at the other end by an alkoxy, aryloxy, or aralkyloxy group. Surfactants having a viscosity of at least 50 centistokes are operable and have molecular weights of 300-100,000. Illustrative of silicone polyethylene oxide/polypropylene oxide block surfactants for use in the invention are the following: "Silicone Surfactant All is a polydimethylsiloxane/oxygen linked alkyl terminated polyethylene oxide/polypropylene oxide copolymer having a specific gravity of 1.03 and a viscosity of 1100 centistoked at 250c commercially available by Union Carbide as L550. "Silicone Surfactant Bll is a nonhydrolyzable polydimethylsiloxane - carbon linked alkyl terminated polyethylene oxide/polypropylene oxide copolymer having a specific gravity of 1.03 and viscosity of 1200 centistokes at 250C commercially available by Union Carbide as L540. "Silicone Surfactant C" is a nonhydrolyzable polydimethylsiloxane - alkyl terminated polyethylene oxide/polypropylene oxide copolymer having a specific gravity of 1.03 and a viscosity of 1000-1500 centistokes commercially available by Union Carbide as L560. "Silicone Surfactant D" is a nonhydrolyzable surfactant similar to L560 having a specific gravity of 1.03 and a visocity of 1000-1500 commercially available by Union Carbide as L-5304. "Silicone Surfactant E" is a polydimethyl siloxane, polyether copolymer having a specific gravity of 1.035 and viscosity of 1000-1500 and commercially available by Dow Corning as DC-190. "Silicone Surfactant F" is a polydimethyl siloxane polyether copolymer available from B.F. Goldschmidt as BF-2270 having a viscosity of 1400 centipoise. "Silicone Surfactant G" is a polydimethyl siloxane polyether copolymer available commercially by General Electric as SF1188. Returning now to the reaction injection molding process of the invention, there is normally present a catalyst for the reaction of isocyanate with the other reactive species, and this is usually added to the polyol or polyamine component. Any known catalyst useful in producing polyurethanes may be employed. Representative catalysts includes (a) tertiary amines such as (dimethylaminoethyl) ether, tri-ethylamine, tri-methylamine, N,N-dimetbyl- ethanolamine, and the like; (b) tertiary phosphenes; (c) strong bases such as alkali or alkaline earth metal hydroxides and alkoxides ; (d) acidic metal salts of strong acids such as ferric chloride, stannic chloride, bismuth nitrite and the like; (e) chelates of various metal such as those which can be obtained from acetylacetone, benzoylacetone, salisyl aldehydeamine and the like with various metals such as zinc, titanium, tin, iron, molybdenum and the like; (f) alcoholates of titanium, tin and aluminum and the like; (g) salts of organic acids with a variety of metal such as alkali metals, alkaline earth metals, aluminum tin, lead, maganese, cobalt, nickel, and¯copper including for example, sodium acetate, stannus oleate, and maganese and cobalt naphthanate and the like; (h) organo metallic derivatives of tetravalent tin, trivalent and penta-valent arsenic antamony and bismuth. Among such derivatives are most commonly used the dialkyltin salts of carboxylic acids such as dibutyltindiacetate, dibutyltindilaurate and the like. The tertiary amines may be used as primary catalyst for accelerating the reactive hydrogen/isocyanate reaction or as secondary catalyst in combination with one or more of the above noted metal catalyst. Metal catalyst or combination of metal catalyst may also be employed as the accelerating agents without the use of the amines. Catalyst are employed in small amounts for example, from about 0.001 percent to about 5 percent based on the weight of the reaction mixture. In addition the reacted components may contain minor amounts of chain extenders selected from high and low molecular weights of polyamines, such as diethyltoluene diamine, thiols, and low molecular weight glycol such as ethylene glycol, butane diol, propylene glycol, and glycerine. It may be advantageous in some instances to reduce the specific gravity of the polyurethane products by the incorporation therewith of non-reactive gases such as nitrogen, air, carbon-dioxide, and the chlorofloromethane and ethane derivatives in concentrations ranging from 1-2 percent by volume. Such gases are incorporated with polyol employing conventional mechanical mixing procedures. The invention is illustrated by the following Examples in which parts are by weight. Specific components referred to in the text above are named in the examples by the reference used in the text, as follows - Polysiloxane mold release agent : "Polysiloxane I to XI" - Polyol/polyamine : "Polyol A to N" and "Polyamine 0 and P" - Polyisocyanate : "Polyisocyanate 1 to 9" - Silicone surfactant : "Silicone Surfactant A to G". Examples 1 to 28 describe isocyanate compositions containing siloxane mold release agent and silicone surfactant. Examples 29 to 38 show the improvement in mold release using the RIM process of the invention with, for comparison, a text ("control") using an isocyanate and no intend mold release composition. Examples 39 to 48 describe polyol compositions containing polysiloxane release agent. Examples 49 to 60 describe RIM processes using compositions with polysiloxane in the polyol component. Example 1 1000 Parts liquid diphenylmethane diisocyanate quasi-prepolymer containing 10% low molecular weight glycols (Rubinate0 LF-179, Rubicon Inc.) was mixed with 0.1 parts polydimethylsiloxane-polyoxypropylene/polyoxyethylene block (Silicone Surfactant D) copolymer. To this liquid was added 1 part of "Polysiloxane I". The mold release agent was added to the surfactant containing polyisocyanate liquid under high shear mixing with a Cowles high speed mixer rotating at 2430 rpm. High speed mixing is employed to obtain a fine stable dispersion. The dispersion remained stable until used in molding operations. Similar compositions made without the silicone surfactant start to gel in less than 25 hours and were not suitable for further use. Similar compositions made according to the procedure of Example 1 are listed in Table 1. Table 1 Mold Release Agent Silicone Polyiso- Stability Example Polysiloxane Surfactant cyanate Type 20-250C No. Type /parts Type /parts (100 parts) (days) 1 I / 1.0 B / 0.1 1 > 180 2 " / 3.0 " / 0.33 11 1I 3 " " " / 0.15 " IT 4 " / 6.0 " / 0.66 I1 5 Ii " " / 0.3 " " 6 " / 12.0 " / 0.66 7 " / 15.0 " 1 0.23 11 " 8 11 / 6.0 C / 0.66 It It 9 11 It E / 0.66 " 11 10 V / 6.0 B / 0.66 It > 10 11 IV / 6.0 " / " " " 12 IX / 6.0 " / " " " 13 I / 5.0 F / 0.8 5 14 o / " E / 0.8 " > 30 15 " / " D / 0.8 11 " <RTI ID=26.15> 16 " / " G / 0.8 " " 17 " / " / " B / 0.8 " " 18 " / c C / 0.8 " " 19 11 / " A / 0.52 ¯l ¯" " 20 " / ¯l" B I 0.66, A / 0.13 21 " / " C / 0.56 2 > 180 22 / II / " 9 23 / " " / " " / " 6 24 III / 4.5 1I / " 5 " 25 IV / 4.5 It 5 " 26 IX / 4.5 " / " 5 " 5 27 I / 6.0 B I 0.66 7 28 I" / " " /" " / " 8/ " ¯8 " Indications of improved mold release are provided by laboratory techniques wherein 4mm thick 2.54 cms x 15 cms strips of conventional polyurethane RIM formulations are cast on a clean steel surface cured at 480C for one minute then peeled off with a metal clip attached to a spring balance. Coatings containing no mold release have release values of ranging from 800-1100 gms/in while typical RIM formulations containing from 0.5-5% by weight of the mold release agents of the invention have mold release values substantially lower. For example a RIM urethane formulation containing the blend of Example 1 gives mold release values of 200-300 grams/inch. While the laboratory peel strength is a good indication of the effectiveness of internal mold release agents their true worth can only be determined in actual commercial scale use in formulations employed in making complicated three dimensional shapes where large cured moldings must be pulled off directly from the mold surface. In the following example the use of the internal mold release blends of the invention in commercial scale RIM application is best demonstrated. The following examples were run on a standard two component Cinncinati Milacron RIM 90 machine equipped with a heated metal mold for forming an automobile fascia having a surface area of at about 2 sq. meters and 3.68 kilograms in weight. All proportions are expressed in parts by weight unless otherwise specified. General Procedure The polyurethane composition used represent typical RIM two component systems where the "A" component is a composition# selected from Table 1. The "B" component is a mixture of a polyether polymer polyol such as (Niax D440) with a chain extender such as ethylene glycol and dibutyl tin dilaurate (Catalyst T-12 M and T Corp.) as the catalyst. The temperature of the "A" component is maintained at 260C and the "B" component at 440C. The polyol or "B" component is nucleated with nitrogen under pressure to result in a molded density of 1.05. The surface of the mold is pretreated with a conventional external mold release wax, XMR-136, supplied by Chem-Trend, Inc. The mold temperature is maintained at 680C. Components "A" and "B" are blended in an impingement mixer and dispensed directly into the mold, the cure time is 60 seconds. The mold is then opened and the molding removed. There must be no surface sticking or tearing of the polyurethane, the part should release without the need for undue force. Example 29-38 According to the previously described general procedure a series of automobile fascias were made employing various "A" Components which are isocyanate dispersions of polysiloxanes and silicon surfactants. The "A" component of the invention were impingement mixed with typical "B" Components which are polyol blends containing catalysts and in some formulations, fillers at "A Component/B Component" ratios to provide an isocyanate index of 103-105, with a mold temperature of 680C with one coating of external mold release. "B Components" Parts by Weight B-l B-2 B-3 B-4 B-5 B-6 B-7 Dow Corning Polyol 100 100 XAS-10771 Union Carbide Polyol - 81 53.66 89 69 Niax D442 Union Carbide Polyol - 100 Niax W136 Ethylene glycol 16 16 19 12.6 11 8 Diethyltoluene diamine 22.5 Dibutyl Tin Dilaurate .09 .09 00.1 .07 .1 .08 .15 Catalyst DABCO-DC-2 Catalyst .09 00.1 .07 .1 Catalyst UL28 .09 Flaked Glass 33.7 Milled Glass 28.9 23 The number of molding made from various "A" Component Isocyanate Disperions from Table 1 are listed in the following Table 2. A cure-time of 60 seconds was permitted before mold was opened. Table 2 "A" Component Number Isocyanate Isocy- of Release Example Dispersion "B" anate Ratio before No. of Example No. Component Index "A"/"B" Sticking Control "Polyisocyanate 2" 3-1 103 0.774 5 29 20 3-1 103 0.871 > 30 30 19 B-2 103 0.66 > 30 31 20 B-3 105 1.08 > 30 32 20 B-5 104 0.627 > 25 33 20 B-6 104 0.487 > 25 34 20 B-5 103 0.667 > 25 35 20 B-4 105 0.687 > 30 36 3 B-7 105 0.534 12 37 7 B-7 106 0.55 14 38 2 B-7 103 .5 10 Samples 39-48 The following Examples describe the use of polyol formulations including polysiloxanes, according to the invention. Polyol compositions are given in Table 3. Table 3 Example Polyol Polysiloxane (parts) (parts) 39 L 97 I 3 40 A 98 I 2 41 A 95 I 4 42 K 99.5 I 0.75 43 D 92.5 II 7.5 44 G 92.5 II 7.5 45 B 99.25 II 4.75 46 M 99.5 IV 0.5 47 L 96 IV 2.5 48 K 94 IV 6 Machine molding or RIM polyurethanes provides the only real method of assessing the efficiency of internal mold release agents and their effect on processing and properties. Indications of improved mold release are provided by laboratory techniques wherein 4mm thick 2.54 cm. x 15 cm. strips of conventional polyurethane RIM formulations are cast on a clean steel sur-ace in a single layer, cured for 1 minute at 600C and thereafter peeled off with a metal clip attached to a spring balance. Castings containing no internal mold release have release values of from 800-1100 grams per inch while typical RIM formulations containing from 0.5-5 percent by weight of the mold release agents of the invention have mold release values substantially lower. For example, a RIM urethane formulation containing 2 percent of "Polysiloxane I" as provided for the polyol blend of Example 40 gives mold release value of 100 to 300 grams per inch. While the laboratory peel strength is a good indication of the effectiveness of internal mold release agents there true worth can only be determined in actual commercial scale equipment in formulations employed in making complicated three dimensional shapes where large cured moldings must be pulled off directly from the mold surface. In the following example the use of the internal mold release polyol blends of the invention in commercial scale RIM application is best demonstrated. The following examples were run on a standard two component Cinncinati Milacron RIM 90 machine equipped with a heated metal mold for forming an automobile fascia having a surface area of at about 2 sq. meters and 3.68 kilograms in weight. All proportions are expressed in parts by weight unless otherwise specified. Example -49 The polyurethane composition used represents a typical RIM two component system where the "A" component is a uretonimine modification of 4,4' diphenylmethane diisocyanate with a free isocyanate content of 29.3% and a viscosity of 40 cps at 250C. The "B" component is a mixture of a polyether polymer "Polyol L" (Niax D440) with ethylene glycol as the chain extender and dibutyl tin dilaurate (Catalyst T-12 - M and T Corp.) as the catalyst. This system is designed to give a flexural modulus of 26,000 psi at 23 C. Component A RUMINATES LF-168 (Rubicon Chemicals) - 55.8 pbw Component B Component B (with Internal Mold Release) Union Carbide Polymer/Polyol Niax D 440 - 89.5 pbw 89.5 pbw Ethylene Glycol - 10.5 pbw 10.5 pbw Catalyst T12 - 0.15 pbw 0.15 pbw Polysiloxane "1" 3.2 pbw The temperature of the "A" component is maintained at 260C and the "B" component at 440C. The polyol or "B" component is nucleated with nitrogen under pressure to result in a molded density of 1.05. The surface of the mold is pretreated with a conventional external mold release wax, XMR-136, supplied by Chem-Trend, Inc. The mold-temperature- is maintained at 68 C. Components "A" and "B" are blended in an impingement mixer and dispensed directly into the mold, the cure time is 30 seconds. The mold is then opened and the molding removed. There must be no surface sticking or tearing of the polyurethane, the part should release without the need for undue force. This formulation gave five releases before tearing or sticking occurred. The addition of the polyol/polysiloxane blend of Example 1 increased the number of releases to thirty using the same conditions. The physical property data of Table 5 indicates that the siloxane mold release has little detrimental effect. Table 5 Table 5 PHYSICAL PROPERTIES IN FASCIA FORMULATION Unfilled Filled Milled Glass Content, % 0 0 15 Mold Release Content, Z 0 2 2 Tensile Strength, psi 3500 3400 3400 Elongation at Break, % 220 190 90 Flexural Modulus, psi x103 230C 26 34 77 -30 C 62 92 165 700C 17 23 46 Ratio -30/70 3.6 4.0 3.6 Tear Strength, Die C, pli 375 380 460 Heat Sag, 250 F, in/hr. 4" 0.2 0.2 0.1 6" 1.0 0.8 0.3 Number of Releases 5-7 > 25 > 25 Example 50 A series of fascia moldings were made as described in Example 49 with the exception that Polysiloxane I is blended with a different polymer/polyether polyol wherein the polyol has a hydroxyl value of 22.6 mg KOH/gm (Niax D-442, Union Carbide) and additional ethylene glycol. The polyurethane is a more rigid type having a flex modulus of 121,000 psi at 23 C. Component A RUBINATE LF-168 (Rubicon Chemicals) - 105 index Component B Component B (with Internal Mold Release) Niax D442 - 81.0 pbw 81.0 pbw Ethylene Glycol - 19.0 pbw 19.0 pbw Catalyst T12 - 0.1 pbw 0.1 pbw Catalyst DC-2 - 0.1 pbw 0.1 pbw Polysiloxane "I" - 0 2.0 pbw The temperature of the "A & B" Components were preheated to 26 C and 620C respectively. The formulation without mold release gave three releases without tearing or sticking while with the polysiloxane I in component B gave over 25 releases before sticking. Example 51 Example 50 was repeated using the polyol component "B" containing 30% by weight flaked glass to increase the flexural modulus to 300,000 psi. The formulation without mold release gave two releases before sticking while that containing the polysiloxane '1111/polyol blend gave over twenty-five releases. Example 52 Using the equipment of Example 49 a series of low density fascias were made: Component A RUBINATE¯ LF-168 - 96.0 pbw Freons 11 - 4.0 pbw (fluoro trichloromethane) Component B Component B (with Internal Mold Release) Niax 31-23 polymer polyol - 85.0 pbw 85.0 pbw (OHNo23) 1-4 Butane Diol - 15.0 pbw 15.0 pbw Dibutyl Tin Dilaurate - 0.075 pbw 0.075 pbw Polysiloxane "I" - 0 4.0 pbw The temperature of the "A" component was maintained at 220C and the "B" component at 600 C. The components were blended in an impingement mixer at a weight ratio of B/A of 1,7/1 and injected. The cure time was 60 sacs. The series with mold release gave over 25 releases while only 4 without mold release. Example 53 Employing the equipment of Example 49 , Rubinate LF-168 as the "A" component, and a blend of 100 parts polyether polyol (DOW XAS-10771), 17 parts ethylene glycol, 3.6 parts polysiloxane "I", dibutyl tin dilaurate and tin catalyst UL-28 as the "B" component a series of fascias were molded. The temperature of the "A" component was 24 C, the "B" component 49 C. The "B" component was nucleated with nitrogen to result in a molded density of 1.05. Components "A" and "B" were impingement mixed at A/B ratios of .757/1 to yield a polyurethane with an isocyanate index of 104. The mix was injected immediately and cured in 60 sacs. The formulation gave over 30 releases before sticking in the mold. Example 54 The procedure of Example 53 was repeated and included 25% by weight of flaked glass in the "B" component. The ratio of A/B through the impingement mixer was 0.578 to yield a polyurethane with an isocyanate index of 104. The formulation gave over 30 releases before sticking occured. Example 55 The procedure of Example 54 was repeated wherein 35Z flaked glass was included in the "B" component. The ratio A/B through the impingement mixer was 0.736/1 to yield a polyurethane stoichiometry index of 104. Over 30 releases were obtained before sticking occured. Only five releases were obtained without the internal mold release. Example 56 A series of fascias were made employing the equipment of Example 49 using a system to give a flexural modulus of 36,000 psi at 23 C. Component "A" Rubinate LF-179 - partial prepolymer modification of pure MDI (4,4' diphenylmethane diisocyanate) using short chain glycols) Isocyanate Index = 105 Component 'tub" 100 pbw Niax-W-136 (Union Carbide) polyether triol having hydroxyl number 30 mg. KOH/gn. 22.5 pbw Diethyl toluene diamine .15 pbw Catalyst T-12 (dibutyl Tin dilaurate) 4.0 pbw Polysiloxane "I" mold release The surface of the mold was treated with external mold release Rimlease 1535. The mold temperature was 54 C. The "A" and "B" components were preheated to 26 C and 380C respectively. The "B" component was nucleated with nitrogen under pressure to result in a molded density of 1.05. The "B" component with siloxane containing material gave 12 releases without sticking while the untreated "B" component gave two. The physical properties were unaffected by the inclusion of mold release. Example 57 Example 56 was repeated with the inclusion of 15% milled glass in the total formulation and yielded the same improvement in mold release. Example 58 According to the procedures of Example 49 a series of fascias were made. The component "A" was an isocyanate blend containing 50% Rubinate LF-168 and 50% Rubinate LF-179. Component "B" 100 pbw polyether triol (trimethylolpropane reacted with propylene oxide to a MW 4500 and further reacted with ethylene oxide to give E¯ 5300 (equivalent weight 1765), hydroxyl number 32, viscosity 900 centipoises at 250C) 15 pbw ethylene glycol 0.05 pbw dibutyltin dilaurate catalyst 0.7 pbw DABCO 33LD catalyst (triethylene diamine) 3.4 pbw polysiloxane I mold release. Over twenty-five moldings were made before sticking occured. Physical properties were not effected. Example 59 Employing the polyol/polysiloxane blend of Example47, ethylene glycol and Rubinate LF-168 isocyanate several 4mm thick castings on clean steel surfaces were made Values of low mold release of 90-120 grams per inch indicate that most excellent mold release may be obtainable even without the application of external mold release coatings. Example 60 Improved mold releasable polyurea compositions giving over 25 releases can be expected by impingement mixing a polyamine "B" component containing 62.3 parts "Polyamine 0", 18.9 parts diethyltoluene diamine, 1 part "Polysiloxane I" and as "A" component a blend of 38 parts of a quasi prepolymer having 13.5% free -NCO (Thanate¯ L55-0) with 19 parts Rubinate LF-168 at an isocyanate index of 1.04, in a mold at 620C.

Claims: PROCESS FOR MAKING POLYURETHANE AND RELATED PRODUCTS BY REACTION INJECTION MOLDING IN PRESENCE OF SILOXANE MOLD RELEASE AGENT AND COMPOSITIONS THEREFOR. CLAIMS 1. In A process for preparing polymer products by the reaction injection molding technique which comprises mixing liquid organic polyisocyanates with reactants selected from polyols, polyamines, polyolamines and catalysts dispersed therewith from 0.5-15 percent by weight based on the total reaction mix of a polysiloxane mold release agent which consists essentially of 0.5-20 mol percent of RaR' bSiO [ 4#(a+b)i/2 units and from 80-99.5 mol percent of R"cSiO(4#c)/2 units where R is an isocyanate reactive organic radical, a has an average value of from 1-3, R' and R" are both non-isocyanate reactive organic radicals, b has an average value of 0-2, a+b is from 1-3, and c has an average value of from 1-3, wherein the ratio of the total molecular weight to the total number of isocyanate reactive functional groups in the molecule ranges from 100-3500, the combined formula weights of all isocyanate reactive organic radicals, R do not exceed 40% of the total molecular weight of said polysiloxane mold release agent, the combined formula weights of all nonisocyanate reactive radicals, R'+R" together do not exceed 40% of the total molecular weight of said polysiloxane mold release additive, the combined formula weights of all the organic radicals R + R' + R" in the molecule together do not exceed 60% of the total molecular weight of the molecule, said polysiloxane mold release agent contains an average of at least two isocyanate reactive functional groups per molecule, at least two of the isocyanate reactive functional groups in each molecule are located on separate organic radicals, R, attached independently to different silicon atoms in said polysiloxane, said isocyanate reactive functional groups (R) are selected from alcohols; phenols, thiols, primary or secondary aromatic amines, which contain no oxygen, and not more than one nitrogen, atoms attached directly to, in conjugation with, or incorporated within, the aromatic ring nucleus, and secondary aliphatic amines wherein at least one of the alkyl carbon atoms, bonded directly to the nitrogen atom, is not a primary carbon atom and carboxylic acids, the molecular weight of said polysiloxane mold release agent ranges from 1000 and 30,000, and said polysiloxane mold release agent being substantially insoluble in said liquid polyisocyanate. 2. A liquid composition for use in a process according to claim 1 which comprises at least one organic polyol or polyamine having 2 to 6 isocyanate reactive hydrogen atoms and a molecular weight of 1,000-10,000 having dispersed therein from 0.5-8.0 percent by weight o a polysiloxane mold release agent as defined in claim 1. 3. A liquid organic polyisocyanate composition for use in a process according to claim 1 having dispersed therein from 1-15 percent by weight of a polysiloxane mold release agent as defined in claim 1 said polysiloxane mold release agent being substantially insoluble in said liquid polyisocyanate, and from 1-25 percent based on the weight of said polysiloxane mold release agent of a liquid silicone surfactant substantially free of isocyanate reactivity. 4. A composition according to claim 3 wherein said silicone surfactant has the general formula (CH3)3Si [ OSi(CH3)2#x [ CH3R+SiO ] y [ CH3R*SiO ] zOSi(CB3)3 where the value of x, y or z vary from 10-1000 and R+ and R* may be the same or different, where the sum of the total formula weight for R+ and R* ranges from 800 40,000 and the polysiloxane block ranges from 15-70% of the molecular weight. 5. A process according to claim 1 and compositions according to claims 2 to 4 wherein R is -CH2CH2CH28 [ CH2CH(CH3)O ] n#H where n=1-5. 6. A composition according to claim 5 having a hydroxyl equivalent weight of between 500 and 2,000.

Inventors: ROBERTSON, JOHN RUSSELL
Applicants: ICI AMERICAS INC.
Application year: 1984
Main classification: C08G18
IPC codes: B29C67, C08G18, B29C33