LOW TEMPERATURE, STORAGE STABLE MIXTURES OF POLYESTER PREPOLYMERS AND FLOW MODIFIERS

Abstract: Low temperature, storage stable, liquid mixtures of (1) isocyanato-containing prepolymers obtained from the reaction of linear and/or slightly branched polyols and a polyisocyanate characterized by a methylene group (CH2) bonded to two benzenoid nuclei, and (2) a non-hydroxyl-containing flow modifier which is compatible with the said prepolymer. Novel liquid mixtures thus prepared exhibit little tendency to crystallize or phase separate when stored for prolonged periods of time, i.e., well below room temperature for several days.

Description: LO TEMPERATURE, STORAGE STABLE MIXTURES OF POLYESTER PREPOLYMERS AND FLOW MODIFIERS BACKGROUND OF THE INVENTION It is well recognized that polyisocyanates which are liquid at room temperature have obvious processing advan¬ tages over solid polyisocyanates; see for instance U.S. Pat. No. 4,115,429. Polyisocyanates such as the commer¬ cially available and widely used toluene diisocyanate (TDI) and 1,6-hexamethylene diisocyanate are potentially harmful due to their relatively high vapor pressure and accordingly, certain safety precautions are employed to minimize harmful physiological effects. For this reason, various attempts have been made, either to start with di- isocyanates that are normally liquid at room temperature and to reduce their physiological effects by certain pro¬ cedures or to start with diisocyanates that are solid at room temperature and to convert these into liquid form. In both cases, however, one usually obtains either iso- cyanates of higher valency, i.e., tri- or higher polyiso¬ cyanates. or higher molecular weight diisocyanates or a combination of these effects. Important diisocyanates which are solid at room temperature and which are readily available on a large commercial scale. are 4,4'-diphenylmethane diisocyanate and the 2,4'-isomer thereof which melt at 39°C and 34.5°C, respectively. Attempts have already been made to liquefy both the 4,4'-diphenylmethane diisocyanate and a mixture of the 4,4'-diphenylmethane diisocyanate and a small amount of the 2,4 , -isomer. Thus, for example in U.S. Pat. No. 3,644,457, 1 mol of a diphenylmethane diiso¬ cyanate is reacted with from about 0.1 to about 0.3 mol of poly-l,2-propylene ether glycol. While the products made according to this patent have met with commercial success, they still suffer from a serious drawback. Specifically, it has been found that these adducts generally will crys¬ tallize anywhere from 5°C to as high as 25°C. In fact, " OREaCi OMPI when supplied in commercial quantities, these adducts are generally transported in heated trucks. Additionally, in order to thaw the materials it is generally necessary to heat them to somewhere in excess of 50°C to 60°C. While in warmer climates there may not be any problem, in colder areas where the product may be stored in tanks over a period of time, this tendency to crystallize can become a very serious problem. Similar attempts to form liquid diphenylmethane diisocyanates have been described, for example, in U.S. Pat. Nos. 3,384,653 and 3,394,164. The attempts to liquefy in both of these instances were based on the addition of, in one case, a trihydrocarbyl phos¬ phate, and, in the other case, small amounts of phosphoric acid. In any event, the storage stability of both of these types of products is again quite good around room temperature, but as the temperature decreases, both types of materials tend to crystallize. Isocyanato-terminated prepolymers of about 600 to- about 4500 molecular weight, e.g., prepared from the reaction of an excess of 4,4*-diphenylmethane diisocyanate (MDI) with (i) linear or slightly branched polyesterdiols with/without polyestertriols (reaction products of lower aliphatic glycols with/without small amounts of glycerol and alkanedicarboxylic acids), or (ii) dipropylene glycol, comprise products generally having melting points of about 10°C to about 30°C, and higher, depending primarily on the amount and structure of the polyol employed. Quasi- prepolymers containing, by weight, from about 50% to about 60% of the polyol segment (e.g., a polyol from adipic acid, ethylene glycol, 1,4-butanediol) are generally liquid products at room temperature. When the MDI content is increased to about 60%, or more, the resulting quasi- prepolymers are oftentimes crystalline products in the 15°C-20°C range. Quasi-prepolymers comprised of MDI and about 10-15% of the di- and/or tripropylene glycol(s) are oftentimes crystalline at about 15°C-20°C. In this state. the quasi-prepolymers are more difficult to process, exhibit greater tendency towards dimerization and tri- merization reactions, and detract from optimal physical characteristics of the end polyurethane product. SUMMARY OF THE INVENTION It has now been found quite unexpectedly indeed that there can be prepared novel low temperature, storage stable, liquid mixtures of (1) isocyanato-containing pre¬ polymers derived from the reaction of (i) a polyol and (ii) an organic polyisocyanate characterized by a methyl¬ ene group bonded to two benzene nuclei as, for example, 4,4'-diphenylmethane diisocyanate, and (2) a norihydroxyl- containing flow modifier, hereinafter developed in detail. The non-hydroxyl flow modifier is a normally- liquid compound and compatible with the prepolymer, or it may be a low melting solid which forms a normally-liquid, compatible mixture with the prepolymer. The addition of a few parts (by weight), e.g., about 3 parts of flow modifi¬ er per 100 parts (by weight) of prepolymer can result in compatible mixtures whose melting points are measurably lower than the prepolymer per se. In general, a practical commercial lower limit is approximately 5 parts flow modi¬ fier per 100 parts prepolymer. Thus, in the practice of the invention, there can be prepared novel liquid compat¬ ible mixtures comprising prepolymer(s) and flow modifi¬ er(s) which exhibit storage stability for long periods of time at temperatures substantially below room temperature, for example, at about +5°C to +10°C, and lower, for several days to several weeks, e.g., at least 100 hours, and longer. Many of the novel liquid mixtures exhibited compatibility, did not crystallize or phase separate, and remained chemically stable for at least one week (and up¬ wards to several weeks) at temperatures at about 0°C, and lower, e.g., -5 β C. Thus, the novel mixtures can be trans¬ ported over great distances and stored for prolonged peri¬ ods of time at low temperature, and remain in a compatible liquid state ready for the intended use. ' Handling and processing problems which are associated with polyiso¬ cyanate compounds crystallizing or melting in the 15°C to 30°C and higher range are substantially eliminated by using the novel mixtures described herein. Moreover, it has been observed that dimerization and trimerization reactions are greatly reduced. The novel storage stable liquid mixtures are readily cast or metered through pumps, and have very low vapor pressure and therefore are sub¬ stantially physiologically harmless. The novel liquid mixtures comprising prepolymer and non-hydroxyl flow modifier can be employed in the NCO/OH polyaddition reactions to prepare a wide variety of poly- urethane products, especially microcellular products such as, for example, integral skin microcellular poly- urethanes. Such products exhibit a broad spectrum of highly desirable and/or improved characteristics. DETAILED DESCRIPTION OF THE INVENTION. It has now been found that a wide variety of non- hydroxyl-containing flow modifiers can be admixed with the prepolymers to form novel low temperature, storage stable, liquid mixtures. The flow modifier and prepolymer are compatible and soluble with each other forming a solution which does not phase separate for long periods of time at low temperatures. The flow modifier has a boiling point above about 150°C and is normally-liquid, i.e., liquid at about 20°C or is a relatively low melting solid which forms with the prepolymer a compatible, storage stable, low temperature liquid mixture. The flow modifier con¬ sists essentially of (a) carbon and hydrogen atoms, pref¬ erably in the form of a monovalent and/or polyvalent hydrocarbon group such as a Ci-Cisacyclic group, a C5-C7- cyclo-aliphatic group including unsubstituted- and the mono and poly C1-C4 alkyl substituted- C5-C7cycloalkyl, and/or a benzenoid ring nucleus, e.g., mono-, fused-, and bridged nuclei, including the partially or fully hydro- genated ring substituted- counterparts thereof; (b) etheric oxygen in the form of oxyalkylene group(s); and (c) at least one group having the following structural configuration: O O it II (1) -NHCO- (urethane group; (2) -CO- (ester group); (3) -OC ?O- (carbonate group); (4) -O TCO 1 - (acetal group); or I *ι (5) -OR (hydrocarbyloxy group); wherein each RJL, individually, is hydrogen or a monovalent hydrocarbon group, and wherein each of the unsatisfied bonds of the above structural units is monovalently attached to separate carbon atoms of the flow modifier molecule. In one aspect of the invention, novel flow modifiers are contemplated which contain one to five O il * - -NHCO- groups, preferably 2 to 3 such groups. The term "oxyalkylene", as used herein, characterizes an oxy atom. bonded to an acyclic or alicyclic carbon atom to form, as by way of illustrations, the unit -OCH2CH3-, -OCH2 wherein <3 is an integer of from 3 to 6. Illustrative di¬ valent oxyalkylene groups include oxyethylene, oxypro- pylene, oxytrimethylene, oxytetramethylene, chloromethyl- substituted oxyethylene, phenyl-substituted oxyethylene, dimethyl-substituted oxyethylene, cyclohexyleneoxy cyclo- pentyleneoxy, and methyl-substituted cyclohexyleneoxy; the mixed oxyaϊkylenes of the above such as oxyethyleneoxy- propylene, oxyethyleneoxybutylene, and oxypropyleneoxy- butyϊene; mixed oxyalkylenes which contain minor amounts O ?I of oxymethylene groups and the random and block oxy- akylenes of the foregoing; and the like. The flow modifi¬ ers contemplated in the practice of the invention are characterized by at least one oxyalkylene group and up¬ wards to 25, and more, of such groups. In various embodi¬ ments a suitable upper limit is 8 oxyalkylene groups. Preferred flow modifiers are characterized by oxyethylene or oxypropylene group(s) or mixtures of such groups with/ without minor amounts of other oxyalkylene group(s) with at least one of the foregoing structural units. The average molecular weight of the flow modifiers which are employed in the preparation of the novel storage, stable liquid mixtures can vary over a wide range, e.g., from about 100 to a few thousand, e.g., approximately 3000.. The flow modifier, as noted previous¬ ly, is a normally-liquid material or a relatively low melting solid, and forms a compatible liquid with the prepolymer component which is stable at low temperature over prolonged periods of time. In general, however, many flow modifiers suitable in the practice of the invention have molecular weights in the range of from about 135 to about 1000 and even 2000, desirably from about 150 to about 750. The flow modifiers are characterized by the absence of groups which are normally reactive with an isocyanato group (-NCO) at typical storage and shipping temperatures such as hydroxyl, carboxyl, thiol, primary amino, secondary amino, and the like. In one embodiment flow modi iers which are particularly suitable in the practice of the invention(s) are shown structurally in Formula I infra. wherein the oxyalkylene group generally contains from 2 to 4 carbon atoms in the oxyalkylene chain; wherein each R individually represents a monovalent acyclic, alicyclic or aromatic group; wherein x. is at least one and upwards to 25, and more, but generally 1 to 8; wherein is from 1 to 5, preferably 2 to 3; and wherein R_ represents a mono¬ valent acyclic, alicyclic or aromatic group when is 1 or a polyvalent acyclic, alicyclic or aromatic group when jz is 2 to 5, the valence of R> being equal to the value of JZ. The maximum average number of oxyC2~C3alkylene units in the flow modifier of choice is realistically governed by the restriction that the flow modifier employed in the practice of the invention is a liquid or a relatively low melting solid having the capability of forming, at low temperatures, stable, compatible, homogenous liquid mix¬ tures with the isocyanato-terminated prepolymer for pro¬ longed periods of time. Illustrative R groups include straight and branched alkyls, aralkyls, cycloalkyls, and the aryls (mono-, fused-, and bridged- aryls, and the partially hydrogenated aryls) such as methyl, ethyl, n- butyl, isobutyl, 2-ethylhexyl, lauryl, stearyl, oleyl, phenethyl, phenylpropyl, phenyl, tolyl, xylyl, benzyl, cyclopentyl, methylσyclohexyl, cyclohexyl, cyclohexyl- methyl, cycloheptyl, and cyclohexenyl. Illustrative R groups include alkyl, cycloalkyl, and the aryls illustrat¬ ed previously as well as the corresponding higher poly¬ valent acyclic, alicyclic and aromatic groups, e.g., alkylene, cycloalkylene, arylene, and the like. Examples of R? groups include methyl, ethyl, n-butyl, phenethyl, 3-methoxyhexyl, xylyl, phenyl, mesityl, tolyl, indenyl, 2-methoxyphenyl, 4-biphenylyl, naphthyl, cyclohexyl, cyclopentyl, methylcyclohexyl, cycloheptyl, 1,4-butylene, 1,6-hexamethylene, cyclopentylene, cyclohexylene, cyclo- hexenylene, phenylene, 1,5-naphthylene, l-methoxy-2,4- phenylene, l-chloro-2,4-phenylene, hexahydronaphthylene, 4,4'-dicyclohexylenemethane, l-propoxy-2,4-phenylene, xylylene, and tolylene. It is preferred that the fore¬ going acyclic groups contain no more than 17 carbon atoms (most preferably, no more than 10 carbon atoms), that the alicyclic groups contain from 5 to 7 carbon atoms in the ring nucleus and up to 2 carbon atoms in any substituent bonded to the ring nucleus, and that the aromatic groups contain up to 12 carbon atoms and one or two benzenoid nucleus, and that jz equals 2. A particularly preferred subclass of flow modifiers is shown in Formula IA below: IA O O li « RI—(.oxyC2-C3alkylene-)- jr -OCNH-A-NHCO—(C2-C3alkyleneo y-)^—R' wherein each R' individually is Ci-Cβalkyl, C5-C7cyclo- alkyl, methyl- or ethyl-substituted Cs-C7cycloalkyl, or aryl-Ci-C3alkyl; wherein A represents Ci-Cβalkylene, cyclohexylene, Cτ.-C2alkyl- or Cτ.-C2alkoxy-substituted cyclohexylene, unsubstituted, Cι-C3alkyl-, or Cι-C3alkoxy- substituted phenylene (preferably tolylene), or divalent (4,4'- and 4,4 , -/4,2'-)diphenylenemethane, or the divalent hydrogenated counterparts of the foregoing; wherein J is at least one and upwards to 25, and more, preferably 1 to 4; and wherein the oxyC-aC-salkylene unit is oxyethylene, oxypropylene, and mixed and/or block oxyethyleneoxy- propylene unit(s), and mixtures of the foregoing. The flow modifiers of Formulas I and IA are readily prepared by reacting monohydroxyl-terminated oxyalkylene compounds, e.g., R—(-oxyalkylene)-_j—OH, with organic mono- or polyisocyanate compounds using an amount of the mono- 'hydroxyl compound sufficient to react with all the NCO groups present in the isocyanate compound. The mono¬ hydroxyl-terminated oxyalkylene compounds can be prepared by reacting a monofunctional initiator which contains an active hydrogen atom with an epoxide compound, the pre¬ ferred initiator being a monohydric alcohol or a phenol and the preferred epoxide compound being the alkylene *gJRE oxides such as ethylene oxide, propylene oxide, and mix¬ tures thereof, in the presence of a base catalyst. Prior to reacting the resulting monohydroxyl-terminated poly- ether product with the isocyanate, it is preferred to remove the basic catalyst. These reactions are well documented in the art. Illustrative mono- and polyisocyanates which can be employed in the OH/NCO reaction to form the flow modifiers of Formulas I and IA include aliphatic, alicyclic and aro¬ matic isocyanates, such as phenyl isocyanate, the alkyl isocyanates such as butyl isocyanate; the polymethylene diisocyanates such as hexamethylene diisocyanate; and the aromatic diisocyanates such as 2,4-/2,6-isomers of toly¬ lene diisocyanate, 4,4'-diphenylmethane diisocyanate, 4,4'-dicyclohexylmethane diisocyanate. Others are described, for example, in the text by W. Siefken and Justus Liebigs Annalen der Chemie, 562, pages 75 to 136. In another embodiment flow modifiers which can be employed are depicted in Formula II infra: II O 0 II II roxyalkylene -__ OCNH- -R! (NHCOR3) c wherein R, JC and oxyalkylene have the meanings or values assigned in Formula I supra, wherein Rj_ is a polyvalent (generally a di-, tri- or tetravalent) acyclic, alicyclic, or aromatic group having the broad and preferred meanings assigned to polyvalent R^ of Formula I supra, the valence of Rj_ being equal to plus y_, wherein each j ^ individual¬ ly is an acyclic, alicyclic or aromatic group, e.g., straight and branched alkyl, cycloalkyl, aryl, etc., as illustrated in Formula I with respect to the R_ group. wherein _ has a value of 1 to 2, preferably one, and wherein £ has a value of 1 to 2. A preferred subclass of flow modifiers within the scope of Formula II are shown structurally in Formula IIA below: IIA O O lι it R' oxyC2-C3alkylene-τ-j; OCHN-A-NHCOR' wherein R_, A, x_ and oxyC 2 -C^alkylene have the meanings or values assigned in Formula IA supra. The flow modifiers of Formulas II and IIA can be prepared by reacting monohydroxyl-terminated oxyalkylene compounds, e.g., R-— oxyalkylene-J-JJ—OH, with an organic polyisocyanate having 2 to 4 -NCO groups, preferably 2 to 3 -NCO groups, such as those illustrated previously, at a 1:1 molar ratio of polyisocyanate to monohydroxyl compound, to form which in turn is reacted with an excess of a monohydric alcohol or a phenol, or an admixture of same with —(-oxyalkylene}-£—OH, to form the products of Formula II supra. Excess monohydric or phenolic compound can be removed via distillation or other means known to the art. A third subclass of flow modifiers is exemplified by Formula III below: III R (oxyalkylene) x OR4 wherein oxyalkylene has the meanings and values assigned in Formula I supra; wherein each R^ individually is a monovalent acyclic, alicyclic, or aromatic group as exemplified in Formula I supra with respect to the EL group and, additionally, each R_[_ individually can be acyl, i.e., O _ 11 RC-, the R_ group of which has the meanings of the said R_ grσup of Formula I, and wherein x. has the values assigned in Formula I supra. A preferred subclass of flow modifiers within the scope of Formula III above is shown below in Formula IIIA: IIIA R' (•oxyC2-C3alkylene)- x OR' wherein each R_*_- individually, and oxyC 2 ~C;_alkylene have the significance assigned in Formula IA above, and wherein j has a value of at least one, and preferably at least 2, and upwards to 5, and higher. Another preferred subclass of the compounds within the scope of Formula III is: IIIB O O II If R5C-—— o yC2-C3alkylene-)- n OCR5 wherein oxyC 2 ~C-^alkylene has the significance stated in Formula IA above, wherein ri is 2 to 4, and each Rj^ individually is Ci-Cjsalkyl such as methyl, ethyl, propyl, 2-ethylpentyl, stearyl, and -oleyl; unsubstituted- and Cι-C2alkyl-substituted C5-C7cycloalkyls; aralkyls such as aryl-Cχ-C4alkyls, benzyl, and phenethyl; cinnamyl; aryls, ' e.g., phenyl, tolyl, xylyl, naphthyl, methylnaphthyl, and the like. A still further preferred subclass of liquid flow modifiers within the scope of Formula III is shown below: IIIC: O II R' (-oxyC2-C3alkylene)-jζ OCR5 wherein R_^, R^, j£ and oxyC?-C alkylene have the significance assigned in Formulas IIIA and IIIB above. The flow modifiers of Formula III and the preferred subclasses can be prepared by conventional etherification and esterification reactions. For example, monohydroxyl- terminated or dihydroxyl-terminated oxyalkylene compounds, e.g., R (oxyalkylene)-■ £ OH or H—■—(-oxyalkylene __ OH, can be reacted with an anhydride of a monocarboxylic acid. or the monocarboxylic acid per se, in an amount which is sufficient to react with all the hydroxyl groups. Typical anhydrides or acids include acetic anhydride, propionic anhydride, 2-ethylhexanoic acid, lauric acid, oleic acid, stearic acid, benzoic acid, cinnamic acid, naphthoic acid; and the like. Illustrative compounds within the scope of Formula III above include the diesters of aliphatic and aromatic ono . carboxylic acids with polyoxyalkylene glycols, for example, polyoxyethylene glycols and polyoxypropylene glycols, or mixed polyoxyethylene-oxypropylene glycols, or mixtures of these glycols. Preferred compounds are the diesters of diethylene glycol, of triethylehe glycol and of tetraethylene glycol, and hexanoic acid, 2-ethyl- hexanoic acid .and benzoic acid. Highly further preferred compounds are the dibenzoyl diesters of diethylene glycol and of dipropylene glycol known by the Benzoflex mark of the Velsicol Chemical Corporation. Other preferred di- ester compounds include the diesters of tripropylene glycol and 2-ethylhexanoic acid or benzoic acid. Pre¬ ferred diether flow modifiers can be illustrated by the lower dialkyl diethers of mono- and polyalkylene glycols, e.g., the dimethyl-, diethyl-, dipropyl-, dibutyl-, and di-2-ethylhexyl diether of ethylene glycol, of propylene glycol, of butylene glycol, of diethylene glycol, of tri- ethylene glycol, of tetraethylene glycol, of dipropylene glycol, of tripropylene glycol, and of the mono- and poly- (oxyethyleneoxypropylene) copolyether glycols. A fourth subclass of flow modifiers is structurally depicted in Formula IV below: IV O II ■(oxyalkylene)- OCO (alkyleneoxy)■ wherein R, x_, and oxyalkylene have the values and meanings assigned in Formula I above. - URE A preferred subclass of the compound of Formula IV is shown in Formula IVA infra: IVA 0 II R'—(oxyC2-C3alkylene) x —OCO—(C2~C3alkyleneoxy) x —R* wherein R__, __, and oxyC2-C~- t alkylene have the values and meanings assigned in Formula IA above. The flow modifiers of Formulas IV and IVA are pre¬ pared by well-known prior art processes, for example, by reacting the monohydroxyl-terminated oxyalkylene compound, R (oxyalkylene) x OH, with phosgene in the presence of a basic catalyst to form the carbonate product. Another method involves the ester interchange of ethyl carbonate, ethylene carbonate, or propylene carbon¬ ate with the monohydroxyl-terminated oxyalkylene compound, in the presence of an ester interchange catalyst, followed by removal of the by-product alcohol or diol via distil¬ lation or other means. A fifth subclass of liquid flow modifiers nclude: wherein each R , individually, has the significance of Rg_ in Formula III above, wherein x and the oxyalkylene unit have the meanings and values assigned in Formula I supra, wherein m has a value of 0 to 8, wherein £ has a value of 1 to 8, and wherein the sum of m and £ (m + p) is 2 to 8, desirably 3 to 8, and wherein B is a polyvalent acyclic, alicyclic, or aromatic group composed of carbon (desirably up to 12 carbon atoms) and hydrogen atoms, and optionally etheric oxygen and/or amino nitrogen atoms. B_ represents the remainder of a polyfunctional initiator compound with¬ out any active hydrogen groups, e.g., hydroxyl, which polyfunctional initiator is characterized by its reactiv¬ ity with an epoxide compound, preferably C2~C10 a ϋ hat i c and C5-C7cycloaliphatic epoxides having a group. The valence of B_ is equal to the sum of m + £. A preferred subclass of liquid flow modifiers encom¬ passed within the metes and bounds of Formula V is structurally depicted below: VA ( R5θ ϊ D— -(oxyC2~C3alkylene) x —OR5 wherein each R^ individually has the significance shown in Formula IIIB above and additionally can be wherein has a value of 0 to 5, wherein v_ has a value of 1 to 6, wherein the sum of and r_ (q + r) is 3 to 6, wherein ?c has an average value of from 1 to about 3, wherein the oxyC 2 ~C;-_alkylene group has the significance set out in Formula IA supra, and wherein £ is a polyvalent group composed of carbon and hydrogen atoms and whose valence equals the sum of £ + r_. The flow modifiers of Formulas V and VA including mixtures thereof are prepared by reactions well known in the art. For example, polyfunctional initiator compound containing 3 to 8 hydroxyl groups are reacted with epoxide compounds, preferably vicinal epoxides, and the resulting hydroxyl-containing polyoxyalkylated products can be capped with an anhydride of a monocarboxylic acid or the monocarboxylic acid per se (ester termination) or capped with alkyl halide or alkyl sulfate (ether termination) according to well-known processes. Typical polyfunctional initiator compounds include, by way of illustrations, glycerol, 1,2,4-butanetriol, 1,2,6-hexanetriol, 1,1,1-tri- methylolethane, 1,1,1-trimethylolpropane, erythritol, tri- ethanolamine, mixtures thereof, and the like. Illustra¬ tive epoxides include ethylene oxide, propylene oxide. 1,2-butylene oxide, 2,3-butylene oxide, epichlorohyd in, 1,2-epoxycyclohexane, styrene oxide, tetrahydrofuran, mixtures thereof, and the like. Vicinal epoxides, i.e., epoxide compounds characterized by the I j group. —C C— V are preferred. Particularly preferred epoxides are ethylene oxide, propylene oxide, and mixtures thereof. Another subclass of liquid flow modifiers useful in the practice of the invention includes: wherein R_ is a monovalent or polyvalent acyclic, ali¬ cyclic, or aromatic group composed of carbon (desirably up to 12 carbon atoms) and hydrogen atoms, and optionally etheric oxygen and/or amino nitrogen atoms, and represents the remainder of a mono- or polyfunctional initiator com¬ pound without the active hydrogen group(s), e.g., hydroxyl(s), as discussed and illustrated in respect of Formulas V and VA supra, the valence of R^ being equal to the value of _t; wherein each R_ individually is a mono¬ valent acyclic, alicyclic or aromatic group of the signif¬ icance noted in Formula I supra; wherein oxyethylene has the meanings assigned in Formula I supra; wherein x. has the values assigned in Formula I supra; wherein a_ is zero or jc; wherein y_ has a value of 1 to 3; wherein r_ has a value of 1 to 3; wherein has a value of 1 to 5; and wherein is the remainder, excluding the carboxyl groups, of an acyclic, alicyclic or aromatic polycarboxylic acid. "gTfREA " OMPI preferably of 2 to 10 carbon atoms, and has a valence equal to y_ plus one (y_ + 1) . Preferred liquid flow modifiers within the subclass designated as Formula VIA include: VIA o II II R (oxyalkylene) a OC R6 CO (alkyleneoxy) x R wherein R, x_ and oxyethylene have the meanings and values assigned in Formula I supra; wherein R& is a divalent or trivalent acyclic, alicyclic or aromatic group having the meanings of R^ in Formula I supra when R_2 is divalent or trivalent; wherein has a value of zero or x.; and wherein s is 1 or 2. Additional preferred flow modifiers falling within Formula VI are noted below: VIB wherein each R^ individually has the significance assigned to RΪ in Formula IIIB supra, wherein x. has the value assigned in Formula IA supra, wherein C2~C3alkyleneoxy has the meaning assigned in Formula IA supra, and wherein R7 represents a divalent acyclic, alicyclic or aromatic group (the remainder of a dicarboxylic acid without the 2 carboxylic groups) having up to 10 carbon atoms. The products of Formulas VI, VIA and VIB are easily prepared by well-known esterification techniques; see, for instance, U.S. Pat. Nos. 3,502,601 and 3,882,072. For example, dicarboxylic acids or their anhydrides are pref¬ erably reacted with a monohydroxyl-terminated oxyalkylene corapound(s) , e.g., R (-oxyalkylene)-_ ■ _ OH, or a mixture of such oxyalkylene compound and a monohydric alcohol, in amounts sufficient to produce the esterified products of Formula VI and VIA above. Excess hydroxyl reactant can be removed from the esterification product mixture by conven¬ tional techniques. Illustrative polycarboxylic acids or anhydrides useful in preparation of the above products are glutaric anhydride, maleic anhydride, £-phthalic anhy¬ dride, succinic acid, adipic acid, sebacic acid, phthalic acid, and the like. A further subclass of flow modifiers include the formal acetal and ketal compounds of Formula VII infra: VII R ( alkyleneoxy.-JJ R wherein each R, x, and oxyalkylene have the values and meanings assigned in Formula ' I supra, and wherein each R' ' ' individually is hydrogen, a Cl-Csalkyl, or a C5-C7- cycloalkyl. Preferred subclasses of formals, acetals and ketals include the compounds within Formula VIIA below: VIIA RO I R* -roxyC2~C3alkylene r-_ OCO C2~C3alkyleneoxy j R' - RO wherein RJ_, , and oxyC2-C3alkylene have the meanings and -values assigned in Formula IA, and R is hydrogen, methyl and ethyl. Particularly desirable flow modifiers shown in Formula VII supra are the formals from formaldehyde, the OMPI acetals from acetaldehyde, and the ketals from acetone and methyl ethyl ketone, with monoalkyl ether glycols, such as the mono-Cχ-C6-alkyl ethers of ethylene glycol, of diethylene glycol, of triethylene glycol, of propylene glycol, of dipropylene glycol, and mixtures thereof. Pre¬ ferred monoalkyl ether glycols include methoxyethanol, raethoxypropanol, methoxyethoxyethanol (also called methoxydiglycol) , methoxydipropylene glycol, ethoxy- ethanol, butoxyethanol, hexoxyethanol, ethoxydiglycol, butoxydiglycol, hexoxydiglycol, methoxytriglycol, ethoxy- triglycol, butoxytriglycol, isopropoxypropylene glycol, butoxypropylene glycol, and butoxyethoxyisopropanol. Still other glycol ethers of considerable interest are the aryloxy glycols, for example, phenoxyethanol and phenoxy- diglycol. The preparation of these compounds is document¬ ed in the literature; see, for example, " U.S. Pat. No. 4,287,307. It is also feasible to use as flow modifiers the acyloxy or alkoxy endblocked esterification products obtained by the esterification reaction of hydroxy- carboxylic acid, e.g., 6-hydroxycaproic acid, lower oligomers thereof, lactones, e.g., epsilon-caprolactone, with glycols or higher polyols, including mixtures there¬ of; see U.S. Pat. No. 3,169,945, 3,666,724, and 3,957,753, the disclosures of which are incorporated by reference into this specification. The flow modifiers embraced by Formula I supra are apparently novel compositions, and when the variable x. is greater than 1 such as 2 or 3 and upwards to 8 and even 25, many of them are particularly preferred from a commer-. cial viewpoint such as those depicted structurally in Formulas IA, II, and IIA. Novel flow modifiers which are especially preferred include the urethane products resulting from the reaction of 2,4- and or 2,6-toluene diisocyanate and monoether of mono- and of ol C2-C3alkylene glycol of the formula VIII 2 , 4- and/or 2 , 6-tolylene wherein R_ is alkyl or aryl, preferably methyl, ethyl, propyl, isopropyl, butyl, isobutyl, sec-butyl, pentyl, hexyl and phenyl; wherein x is at least one, preferably 1 or 2 and upwards to 8; and wherein oxyC 2 ~C^alkylene repre¬ sents oxyethylene (preferred) and oxypropylene and when x is 2 or more oxyC2"C3alkylene can also be oxyethyleneoxy- propylene, desirably where the mol ratio of the oxy¬ propylene moiety to the oxyethylene moiety is in the range of from about 75:25 to about 25:90. Additional novel flow modifiers which are preferred include the urethane reaction products resulting from the reaction of R* (oxyC2~C3alkylene) x OH, the R_, x., and oxyC 2 --C alkylene unit having the significance assigned in Formula IIA supra, and a diphenylmethane diisocyanate (MDI) such as 4,4'-diphenylmethane diisocyanate, 2,4'- diphenylmethane diisocyanate, mixtures of 4,4'-MDI and carbodiimides thereof, e.g., Isonate 143-L, mixtures of 4,4'-MDI and minor amount of the 2,4'- and 2,2'-MDI isomers, and the like. The isocyanate compound and polyol are reacted in amounts to give a ratio of NCO groups to OH groups of one. Other preferred flow modifiers are shown in Formula IX below: IX O RJ 6xyC2-C3alkylene )--_- OC IINH- wherein j[ represents 4,4'- and/or 2,4'-diphenylenemethane or C4-C6alkylene; and wherein R_, x , and the oxyC^-C^- alkylene unit have the meanings assigned in Formula VIII above. Further preferred flow modifiers include the dipropylene glycol diester of benzoic acid; the tri- ethylene glycol and tetraethylene glycol diesters of 2- ethylhexanoic acid; the alkanedioic diesters of diethylene glycol monobutyl ether of the formula O O II I! C4H90C2H40C2H40CYCOC2H40C2H40C4H9 wherein _ is propylene, butylene, octylene, and £-phenylene; and the formal reaction product of formalde¬ hyde and the monobutyl ether of diethylene glycol of the formula ■ C4H9OC2H4OC2H4OCH2OC2H4OC2H4OC4H9. The prepolymer component of the novel low temper¬ ature, storage stable, liquid mixtures comprises the reaction product(s) of a diphenylmethane diisocyanate with linear and/or slightly branched chain polyesterpolyols. Suitable polyesterpolyols are those having hydroxyl equivalent weights in the range of from about 400 to about 2250, although polyesterpolyol outside this range can be used to produce useful urethane products. However, novel liquid mixtures comprising quasi-prepolymers from a diphenylmethane diisocyanate and polyesterdiol, and optionally, a small amount of higher polyesterpolyol(s) having hydroxyl equivalent weights between about 500 to about 2000 are most desirable in the manufacture of high performance microcellular urethane elastomers including integral skin microcellular urethane products. For instance, integral skin microcellular urethane articles, e.g., shoe soles, can be obtained which are characterized by a resilient core of substantially uniform density and an integrally formed, tough, substantially continuous surface skin surrounding said core, the boundary between said skin and said core being characterized by a rather abrupt change in density. The skin is itself flexible, essentially devoid of blemishes, impervious to oil and water, directly accepts paint without first requiring primers to its surface, and exhibits superior flex life, high tear strength, and generally superior abrasion resistance. In the practice of preferred embodiments of the invention, there can be achieved liquid, compatible, low temperature, long-standing, storage stable solutions comprising prepolymer and flow modifier and outstanding urethane products therefrom, e.g., molded microcellular integral skin shoe soles, by utilizing prepolymers derived from a diphenylmethane diisocyanate and linear polyester- diols and/or slightly branched higher polyesterpolyols which have hydroxyl equivalent weight in the range of from about 500 to about 1500, preferably from about 750 to about 1250, and most preferably approximating 1000. In general, the functionality (OH) of the polyesterpolyol is in the range of from 2 to about 3, desirably 2 to about 2.5, preferably 2 to about 2.2, and most preferably 2 to about 2.1. The linear and/or branched polyesterpolyols may be prepared by processes which are well known in the prior art. For example, the polyesterpolyols may be manufactur¬ ed by polyesterification of polycarboxylic acids, hydroxy- carboxylic acids including lower oligo ers thereof, or lactones with glycols or higher polyols, including mix¬ tures of the foregoing, generally in the presence of a suitable catalyst and at an elevated temperature. The polyesterpolyols derived from epsilon-caprolactones and other monomers are adequately described in U.S. Pat. No. 3,169,945 and generally comprises the reaction of one or more lactones with one or more polyols. Additional poly¬ esterpolyols are described in U.S. Pat. Nos. 3,666,724 and 3,957,753. The disclosure of the foregoing patents are incorporated into this disclosure to the extent necessary to illustrate the.scope of the invention. Q!ΛΪ1_ Other polyesterpolyols, as indicated previously, are derived from the esterification reaction of at least one polycarboxylic acid with at least one polyol. Illustra¬ tive polycarboxylic acids include succinic acid, glutaric acid, adipic acid, pimelic acid, suberic acid, azelaic acid, and the like. Anhydrides of the acids can also be used. Illustrative polyhydric compounds include the ali¬ phatic glycols such as ethylene glycol, diethylene glycol, 1,3-propanediol, 1,4-butanediol, 1,5-pentanediol, 1,6- hexanediol, 1,10-hexanediol, neopentylene glycol, dipropylene glycol, and others. Examples of other poly¬ hydric compound include the trihydric alcohols such as glycerol, 1,1,1-trimethylolethane, 1,1,1-trimethylol- propane, and 1,2,6-hexanetriol; pentaerythritol; sorbitol; and the like. The C4-Cχo a lkanedioic a cids are preferred, in particular, glutaric acid and adipic acid, whereas the saturated C2-Cgaliphatic diols are most suitable. The polyisocyanate compound used in the preparation of the isocyanato-terminated prepolymer is characterized by a methylene group (-CH2-), each valence of which is separately bonded to a carbon atom of a benzenoid nucleus such as a diphenylmethane diisocyanate (MDI), for example, 4,4*-diphenylmethane diisocyanate, 2,4*-diphenylmethane diisocyanate, mixtures of 4,4*-MDI and 2,4'-MDI, a mixture of ,4'-MDI and the carbodiimide thereof such as Isonate 143-L, mixtures of 4,4'-MDI and minor amount of the 2,4'- and 2,2'-MDI isomers, and the like. The isocyanate com¬ pound and polyesterpolyol are reacted in a ratio of NCO groups to OH groups of at least about 2.5:1, but a more suitable range of NCO equivalents per OH equivalent is from about 2.7 to about 24 (NCO) to one (OH). A NCO/OH ratio in the range of from about 3.7:1 to about 12:1 is preferred with a most preferred ratio being from about 7 to about 12 NCO equivalents per one OH equivalent. Avail¬ able polyester-MDI prepolymers which are particularly use¬ ful in the practice of the invention include Isonate 240 and Mondur E-501. These two products are polyester pre¬ polymers from ethylene glycol/l,4-butanediol adipates and .carbodiimide modified 4,4'-diphenylmethane diisocyanate. They have improved low temperature stability in comparison with the corresponding prepolymers derived from the essentially pure 4,4'-MDI isomer. The addition of the flow modifiers of the invention to these carbodiimide- modified prepolymers not only further improves their low temperature stability but very unexpectedly and surpris¬ ingly, indeed, also improves their chemical stability. It has been observed that the tendency towards the formation of insoluble isocyanate trimers and dimers under ambient storage conditions of from about 10°C to 30°C is markedly reduced. Mixtures of flow modifier and .prepolymer have been observed to be clear after one year whereas Isonate 240 and Mondur E-501 normally will turn milky in 6 months or less, indicating dimer and trimer formation. A few parts, e.g., 2-3 parts, of flow modifier added to 100 parts of prepolymer can. esult in a compatible solution whose melting point is measurably lower than the prepolymer per se. In general, it is desirable to incor¬ porate at least about 5 parts (by weight) of flow modifier into 100 parts (by weight) of prepolymer. Though in some instances 35 parts, and even more, of flow modifier per 100 parts of prepolymer can be admixed together to form low temperature, storage stable, compatible solutions, it is desirable to employ about 5 to about 30 parts, prefer¬ ably from about 7 to about 25 parts, and preferably still from about 7 to about 20 parts, of flow modifier.per 100 parts of prepolymer. The optimum commercial range will, to a large degree, depend on the choice of the flow modifier and prepolymer. One or more flow modifiers can be employed in the practice of the invention providing the :resulting novel mixture is a normally-liquid, compatible mixture. Additional ingredients which do not contain hydrogen activ with isocyanato groups, e.g., surfactant. blowing agent, dye, can be incorporated into the novel mixture. Inasmuch as a number of components employed in the practice of the invention have been identified by their trade names, for the sake of convenience, these are tabulated herein and their chemical structure or specifi¬ cations further amplified so that any of these components can be readily obtainable or made by those of ordinary skill in the art. The components are marked with a double asterisk (**) in the Examples. TRADE NAME DESIGNATION TABLE Trade Identification of Component(s) and Designation source of same ISONATE 240 The Upjohn Company. Isocyanate A prepolymer comprising the reaction product of about 40 parts by weight of (a) a difunctional copolyester polyol of adipic acid, ethylene glycol and 1,4- butanediol having a molecular weight of about 2000, and (b) about 60 parts by weight of carbodiimide modified 4,4'-di- phenylmethane diisocyanate; said pre¬ polymer having an isocyanate content of about 18.8% by weight, an isocyanate equivalent of about 223, and a viscosity at 30°C. of about 1000 centipoises. The product crystallizes at approximately l$ β C. MONDUR E-501 Mobay Chemical Corporation, -Isocyanate Polyurethane Division. A carbodiimide modified diphenylmethane diisocyanate terminated polyester pre¬ polymer having an isocyanate content of -25- Trade Identification of Component(s) and Designation source of same about 18.9% by weight, an isocyanate equivalent of about 222.5, and a viscos¬ ity at 30°C. of about 830 centipoises. MONDUR MR Mobay Chemical Corporation, Isocyanate Polyurethane Division. A crude polyraethylene polyphenyl polyiso¬ cyanate having an isocyanate content of about 31.5% and an isocyanate equivalent of about 133.4. ISONATE 125M The Upjohn Company. Isocyanate A high-purity grade of diphenylmethane diisocyanate containing approximately 98% 4,4'-diphenylmethane diisocyanate and 2% 2,4'-diphenylmethane diisocyanate. The average- isocyanate equivalent is 125. BUTYL Union Carbide Corporation. CARBITOL Diethylene glycol monobutyl ether with a molecular weight of 162. METHYL Union Carbide Corporation. CARBITOL Diethylene glycol mono ethyl ether with a molecular weight of 120. HEXYL Union Carbide Corporation. CARBITOL Diethylene glycol monohexyl ether with' a molecular weight of 190. UCON Union Carbide Corporation. LUBRICANT A monobutyl ether of a polyoxyalkylene 50HB660 glycol with an average molecular weight of about 2000. TP-759 Thiokol Corporation. PLASTICIZER An ether-ester plasticizer exhibiting the following typical properties: Specific Gravity ' s 77°F (25°C) 1.032 Refractive Index @ 77°F (25°C) 1.142 OMPI Trade Identification of Component(s) and Designation source of same Viscosity cps. @ 77°F (25°C) 25 Moisture % 0.2 Flash Point (ASTM-D-73-73) °F (°C) 338°F (170°C) Fire Point (ASTM-D-73-73) °F (°C) 409.6°F (192°C) Volatility % loss after 2 hrs. (ASTM-D-22-88) @ 311°F (155°C) 0.72 HALLCO C-504 The C.P. Hall Company. Dibutoxyethyl sebacate. A high boiling plasticizer exhibiting the ' following typical properties: Acid Value, mg KOH/G 2.0 Appearance Clear, oily liquid Color, APHA 70 Odor Faint, characteristic Saponification Value, mg KOH/G 278 Specific Gravity @ 25°C/25°C 0.967 TP-90B Thiokol Corporation. Plasticizer Formal from Butyl Carbitol C4Hg(OC2H4)2 OH and formaldehyde, i.e., C 4 H9(OC2H4)2θCH 2 0(C2H4θ)2C4H9. TEGMER 804 The C. P. Hall Company. •Plasticizer Tetraethylene Glycol Di(2-Ethylhei£anoate) . HALLCO C-311 The C. P-. Hall Company ■ Butoxyethyl Laurate HALLCO C-325 The C. P. Hall Company Butoxyethyl Oleate Examples 1-15 Various flow modifiers were examined for compatibility with Mondur E-501** (isocyanato-terminated prepolymer). Each flow modifier was tested at three concentrations by weight (90 parts isocyanate/10 parts flow modifier, 80 parts isocyanate/20 parts flow modifier and 70 parts isocyanate/30 parts flow modifier). The flow modifiers were predried using molecular sieves. Type 4A, from the Linde Division of Union Carbide Corporation. Karl Fischer tests (ASTM D-2849) for % H2O show no detectable levels of water. The samples were prepared by weighing into a test tube the following: 90/10 80/20 70/30 Flow Modifier (gms) 1.5 3.0 4.5 Isocyanate (gms) 13.5 12.0 10.5 The test tubes were tightly capped and heated to 70°C for 20-30 minutes. The samples were agitated by vigorous shaking while hot and observations with respect to miscibility at this temperature (70°C) were made. The samples were cooled in a constant temperature bath to 25°C for 4-6 hours and the observations at 25°C were then made. Compatible mixtures were then further cooled in a constant temperature bath to 20°C, 15°C, 10°C, 5°C, 0°C, -5°C, and -10°C, respectively, and allowed to ' -remain at each temperature for a minimum of 24 hours. Observations regarding separation, cloud point (the temperature when haze is first observed), and freezing point (the temperature when crystals are first observed) were made at each temperature interval. A 15 gram sample of Mondur E-501 was tested as a control. Hazy mixtures at 25°C were subjected to further treatment as indicated in the footnotes of Table I. Mixtures which reacted or separated (at 25°C) were not further tested.. The data are set forth in Table I supra. O PI TABLE I COMPATIBILITY AND FREEZE POINT DETERMINATION IN MONDUR E- -501 CONCENTRATION OOMt>AlϊBILi Y SEPARATION CLOUD FREEZE No. FLOW MODIFIER BY WEIGHT @ 70°C @25°C POINT, °C POINT, °C POINT, C 1. Dibutoxyethyl 10 YES Y S^) — 0°C -10°C Adipate 20 YES -5°C • -10°C 30 . YES Yβ ^P) - -5°C < -10°C / 2. Dibutoxyethyl Phthalate 30 YES « (2) - <-10°C <-10°C 3. Dibutojcyethyl 10 YES YES* 1 )* 2 ) 5°C -5°C Azelate 30 YES Separates ' >25°C >25°C N.T. < > 4. Tetraethylene 10 YES VEs(l) <-10°C <-10°C Glycol Dimethyl Ether 20 YES YES* 1 ' <-10°C <-10°C 30 YES ΪES* 1 ' — <-10°C <C-10°C TABLE I (cont'd.) COMPATIBILITY AND FREEZE POINT DETERMINATION IN MONDUR E-501 CONCENTRATION COMPATIBILITY SEPARATION CLOUD FREEZE NO. FLOW MODIFIER BY WEIGHT @ 70°C @25°C POINT, °C POINT, °C POINT, C 5. TP-90B** 10 YES yggd) — -5°C -5°C Plasticizer 20 YES YES* - <-10°C ■ -10 o C 30 YES . YES* 1 * , - -io°c <-10°C 6. TP-759** 10 YES YES* 1 * * • -5°C -5°C Plasticizer 20 YES YES* 1 * - -5°C <-10°C 30 YES YES* 1 * - <-10°C <-10°C 7. Triethylene 10 YES YES* 1 ' 2 ' - 10°C -5°C Glycol Dihexanoate 20 YES YES '* -5°C <-10°C 30 YES yES (l / 2) o - <-10°C <-10 C TABLE I (cont'd.) COMPATIBILITY AND FREEZE POINT DETEIΦttNATION IN MONDUR E-501 CONCENTRATION GQt-lPATIBILITY SEPARATION CLOUD FREEZE No. FLOW MODIFIER BY WEIGHT @ 70°C @25°C POINT, °C POINT, °C POMP, °C 9. Dipropylene 1Q YES YES* 1 ' — 0°C 0°C Glycol Dibenzoate 20 YES YES- 1 ' 10°C • -10°C 30 YES HS' 1 ' 15°C <-10°C I 10. HALLOO C-504** 10 Reaction* ' - - - N.T. * 4 > ω o (4) I 20 Reaction* * - N.T. 30 Reactio - - N.T. * 4 > 11. TEGMER 804** 10 YES ES(1,2) - 5°C -10°C • 20 YES YES(1,2) - -5°C -10°C 30 YES YES' 1 ' 2 ' - <10°C <-10°C 12. HALLOO C-311** • 10 YES y E _< 1 ' 2 > - 10°C -5°C 20 YES Separates , (i) >25°C - N.T. * 4 > • 30 HAZY Separates : (U 25°C — N.T.* ) > tn] TABLE I (cont'd. ) COMPATIBILITY AND FREEZE POINT DETERMINATION IN MONDUR E-501 CONCENTRATION COMPATIBILITY SEPARATION CLOUD FREEZE No. FLOW MODIFIER BY WEIGHT @ 70°C @25°C POINT, °C POINT, °C POINT, °C 13. Triethylene 10 YES YES* 1 * — -10°C <-10°C Glycol Diirethyl (!) Ether 20 YES YES <-10°C -10°C 30 YES YES* - <-10°C <-10°C 14, HALLOO C-325** 10 YES YES* . _ 5°C -5°C 20 Separates* 1- * N.T.* 4 ' (4) 30 Separates - N.T. 15. MONDUR E-501** None - - 4°b ( 5) 4°C (5 > Control TABLE I (cont'd.) FOOTNOTES: (1) Test tube heated to 70°C for 20-30 minutes, the contents agitated by vigorous shaking, and then allowed to cool to 25°C and maintained thereat for 4-6 hours Compatible mixtures were further cooled as " stated previously. (2) Test tμbe was reheated to 80°C, contents were reagitated and held at 80°C for 3 hours, and then allowed to cool to 22°C for at least 16 hours. Compatible mixtures were further cooled as stated previously. (3) These mixtures were not compatible at 70°C and some reaction with the isocyanate was observed. It appears that catalyst may have been present I in the mixture. The flow modifier was analyzed for % ^0 and showed no •Ul to detectable levels of water present. I (4) Not tested. (5) After 16 hours at 4°C crystal formation was observed, After one week approximately one-half of the control is solid. ** See Trade Name Designation Table supra. Examples 16-21 A series of flow modifiers designated, for convenience, as Reaction Products A, B, C, D, and E, were prepared by reacting a diisocyanate with an ether alcohol. The resulting isocyanate-ether alcohol reaction products were then examined for compatibility with Mondur E-501 following the procedure described with respect to Examples 1-15 supra. Example 16 Synthesis of Reaction Product A. In this experiment. Butyl Carbitol** (diethylene glycol monobutyl ether having a molecular weight of 162 and a functionality of 1) was reacted with tolylene diisocyanate (80% 2,4- and 20% 2,6-tolylene diisocyanate) having a molecular weight of 174 and a functionality of 2 at an OH/NCO ratio of 1. Starting at room temperature, a clean dry jar was charged with 32.5 gms of Butyl Carbitol and to this 17.4 gms of tolylene diisocyanate was added. The jar was capped tightly and agitated by gentle shaking to mix the components. No heat was applied for the first 10 minutes. The resulting exotherm of the reaction raised the temperature to 55°C. At this ppint, additional heating was used. The jar was placed in a hot air oven and maintained for 3 hours at 70°C. to complete the reaction. After allowing the reaction product to cool to room temperature overnight, the following observations were made. The reaction product, hereafter referred to as Reaction Product A, was slightly viscous, clear liquid with a dark yellow color. Example 17 Synthesis of Reaction Product B. In this experiment 29.0 gms of Methyl Carbitol** (diethylene glycol monomethyl ether with a molecular weight of 120 and a functionality of 1) were reacted with 21.0 gms of 80/20 2,4- 2,6-tolylene diisocyanate using the process noted in Example 16 above. After 10 minutes the exother of this reaction had increased the temperature of the mixture to 60°C. The reaction mixture was heated for 3 hours at 70°C. and cooled overnight to room tempera¬ ture. The product (Reaction Product B) was a transparent dark yellow viscous liquid. Example 18 Synthesis of Reaction Product C. In this experiment Butyl Carbitol** was reacted with Isonate 125M** (high purity 4,4'-diphenylmethane diiso¬ cyanate). In this reaction 405.6 gms of Butyl Carbitol were charged to a 1 liter reaction flask, maintained under a nitrogen atmosphere, fitted with a stirrer, thermometer, reflux condenser, and feed inlet. The internal temperature of the reaction flask was raised as necessary by heating the outside of the flask with a heat mantle controlled by a rheostat. The Butyl Carbitol was pre¬ heated to 94°C. The 4,4'-MDI was added in three incre¬ ments with good agitation. The first addition of 4,4'-MDI of 125.7 gms brought the temperature of the mixture to 139°C. within 5 minutes. This being an exothermic reaction, the reaction product mixture was allowed to cool to 62°C. before the second 4,4'-MDI addition of 127.7 gms was made. After 20 minutes a temperature of 94°C. was recorded and the third addition of 4,4'-MDI (59.2 gms) was made. The total amount of Isonate 125M added was 312.6 gms. With moderate heating a temperature of 92°C. to 118°C. was maintained for 2 hours to complete the reaction. Agitation was maintained throughout the entire procedure. Upon cooling to room temperature the product (Reaction Product C) of th:s reaction was observed to be a very viscous liquid with large crystals forming. At 35°C it. was a hazy liquid with a viscosity of 12,620 centipoises. At temperatures above 95°C, it was a clear light yellow liquid. Example 19 Synthesis of Reaction Product D. Reaction Product D was prepared by reacting Butyl Carbitol** and Mondur MR** (a crude polymethylene poly- phenyl polyisocyanate having an isocyanate content of about 31.5% by weight and an isocyanate equivalent of about 133.4). A 1 liter reaction flask was charged with 405.6 gms of Butyl Carbitol. A total of 333.5 gms of Mondur MR was required for a complete reaction at a stoichiometric NCO/OH ratio of one. The Butyl Carbitol was preheated to 82°C, and with good agitation the poly¬ isocyanate added in three increments. The exotherm from the first addition of 144.1 gms of polyisocyanate raised the temperature to 120°C, within 10 minutes. A second addition of 109.7 gms of polyisocyanate was made when the temperature subsided to 92°C, and after 20 minutes a peak temperature of 109°C was noted. The third increment of 79.7 gms of polyisocyanate was added at 99.5°C. Moderate heating and continued agitation was used to maintain the temperature between 99°C. and 107°C for 2 hours to complete the reaction. The resulting product (Reaction Product D) was a dark brown liquid with a viscosity of 342,800 centipoises at 23°C, and 66,400 centipoises at 35°C. Although the color was very dark it was transparent with no solids evident. Example 20 Preparation of Reaction Product E (UCON Lubricant 50HB550/TDI). In a manner similar to the preceeding Examples and using the appropriate equivalents (1:1) of UCON 50HB660** and 2,4-/2,6-tolylene diisocyanate, there was prepared Reaction Product E, a yellow transparent liquid with a viscosity of 536 centipoises at 23°C. Reaction Products A, B, C, D, and E were examined as flow modifiers for Mondur E-501 in the manner described f OMPI with respect to Examples 1-15 supra. The data are set forth in Table II infra. Mondur E-501 (the control) is set forth as Example 21 in Table II below. TABLE II ■ COMPATIBILITY AND FREEZE POINT DETERMINATION IN MONDUR E-501 CONCENTRATION COMPATIBILITY SEPARATION CLOUD FREEZE No. FLOW MODIFIER BY WEIGHT @ 70°C @25°C POINT, °C POINT, °C POINT, C (1) 16. Reaction 10 . YES YES 0°C . 0°C Product A (1) (Butyl Carbitol/ 20 YES YES , 0°C -5°C TDI) 30 YES YES (i) 5°C -5°C 17. Reaction 10 YES YES' 1 ' 0°C -5°C Product B (Mathyl Carbitol/ 20 YES YES* 1 * " 0°C 0°C TDI) 30 YES YES* 1 ' 0°C -5°C 18. Reaction 10 YES YES* 1 ' 2 * - 15°C -5°C Product C (Butyl Carbitol/ 20 Slight HAZY * 1,2) >25°C -5°C Isonate 125M) Haze TABLE II (cont'd.) COMPATIBILITY AND FREEZE POINT DETERMINATION IN MONDUR E-501 OONCENTRATION COMPATIBILITY SEPARATION CLOUD FREEZE No. FLOW MODIFIER BY WEIGHT @ 70°C @25°C POINT, °C POINT, °C POINT, °C o 19. Reaction 10 YES YES *~* 10 C 5°C Product D (Butyl Carbitol/ 20 YES YES * 1 * 5°C. 0°C Mondur MR) 30 YES YES* 1 * ' 5°C 0°C I Ul 20, Reaction 10 YES YES * 1 -* - -5°C CO Product E I (U00N 50HB660/TDI) 20 YES YES * 1 * -5°C -10°C 30 YES YES * 1 * ^ -5°C -10°C (3) 21. MONDUR E-501 Nbne - - 4°C* 3 ' 4 o c Control (1) See footnote (1), Table I. (2) See footnote (2), Table I-. (3) See footnote (5), Table I Examples 22-41 Following the procedure of Examples 1-15 supra, various flow modifiers were tested for compatibility with Isonate 240** (isocyanato-terminated prepolymer). The data are set forth in Table III supra. TABLE III COMPATIBILITY AND FREEZE POINT DETERMINATION IN ISONATE 240** CONCENTRATION COMPATIBILITY SEPARATION CLOUD FREEZE No. FLOW MODIFIER BY WEIGHT @ 70°C @25°C POINT, °C POINT, °C POINT, . C 22. Dibutoxyethyl 10 YES YES * 1 ' - 20°C -5°C Adipate 20 YES HAZY * 3 ' >25°C <-10°C • (3) 30 YES HAZY >25°C <-10°C I O 23. Dibutoxyethyl 10 YES HAZY (1 ' 3 ' 4 * - 25°C -5°C I Phthalate 20 HAZY WHITE* 1 ' 3 ' 4 * - 70°C N.T.* 6 * 30 HAZY HAZY* 1 ' 3 ' 4 * - • >25°C <-10°C J4. Dibutoxyethyl 10 YES HAZY* 2 * - >25°C -5°C Azelate 20 YES WHITE* 1 ' 3 ' 4 * — >25°C N.T. (6 ' 30 YES WHITE* ' ' ' ._ >25°C N.T. (6 ' TABLE III (cont.»d) COMPATIBILITY AND FREEZE POINT DETERMINATION IN ISONATE 240** CONCENTRATION COMPATIBILITY SEPARATION CLOUD FREEZE No . FLOW MODIFIER BY WEIGHT @ 70°C @25°C POINT, °C POINT, °C POINT , . C 25. Tetraethylene 10 YES YES* 1 ' 0°C -5°C Glycol Dimethyl Ether 20 YES (i) ■YES -10°C <-10°C 30 YES YES* 1 * <-10°C -10°C 26. TP-90B** 10 YES YES* 1 * 5°C -5°C Plasticizer 20 YES . YES' 1 ' 5°C <-10°C 30 YES YES* 1 ' -10°C <-10°C o 27. TP-759** 10 YES YES' 1 ' 20 C -5°C Plasticizer 20 YES . YES' 1 ' 20°C -10°C TABLE III (cont'd.) COMPATIBILITY AND . FREEZE POINT DETERMINATION IN ISONATE 240** CONCENTRATION COMPATIBILITY SEPARATION CLOUD FREEZE No . FLOW MODIFIER BY WEIGHT @ 70°C @25°C POINT-, °C POINT, °C POINT, . q 29. Tetraethyl-ene 10 YES YES * 1 ' 4 * — 0°C -5°C Glycol Di(2- o Ethylhexanoate) 20 YES , YES * 1 ' 4 * -10 C <-10°C 30 YES HAZY * 1 ' 4 * - 25°C <-10°C 30. Dipropylene Glycol Dibenzoate 20 YES YES * 1 * 20°C -5°C 30 YES YES ' 1 ' - 20°C -10°C 31. HALLCO C-504** 10 Reaction* * _ _ N.T. * 6 ' Reacti .on (2) 20 - - - N.T. * 6 ' • (2) . *6) 30 Reaction v ' N.T. TABLE III (cont'd.) COMPATIBILITY AND FREEZE POINT DETERMINATION IN ISONATE 240** CONCENTRATION COMPATIBILITY SEPARATION CLOUD FREEZE No . FLOW MODIFIER BY WEIGHT @ 70°C @25°C ; POINT, °C POINT, °C POINT, . C 33. HALLCO C-311** 10 YES YES t 1 ' 3 ' 4 * - 0°C -10°C • 20 YES SEPARATES (D ' >25°C >25°C N.T. * 6 * 30 HAZY SEPARATES * 1 * >25°C >25°C N.T. * 6 * 34. Triethylene 10 YES YES * 1 * . - 5°C -5°C Glycol Dύnethyl Ether 20 YES YES 1 * -10°C <-10°C • 30 YES YES * 1 * - <-10°C <-10°C 35. HALLCO C-325** 10 YES YES * 1 ' 3 * - >5°C -10°C 20 Separates * • *-* >70°C - N . T. ( l 6) 30 Separates * , - 70°C - (6) N . T . COMPATIBILITY AND FREEZE POINT DETERMINATION IN ISONATE 240* * CONCENTRATION COMPATIBILITY SEPARATION CLOUD FREEZE No . FLOW MODIFIER BY WEIGHT @ 70°C @25°C POINT, °C POINT , °C POINT, . C 36. Reaction 10 YES YES * 1 * 0°C 0°C Product A (Butyl Carbitol/ 20 YES YES * 1 ' 0°C 0°C TDI) (1) 30 YES YES 5°C 0°C 0°C 37. Reaction 10 YES Si. HAZE * 1 ' 4 * 20°C > 5°C 0°C I Product B I*. I (Mathyl Carbitol/ 20 YES SI. HAZE * 1 ' 4 * 20°C 5°C 0°C TDI) 30 YES SI. HAZE * 1 ' 4 ' 20°C 0°C 0°C 38. Reaction 10 HAZY WHITE * 1 ' 4 ' *.τ. * 6 * Product C (Butyl Carbitol/ 20 HAZY WHITE * 1 ' 4 ' N.T. * 6 * Isonate 125M) 30 HAZY WHITE* 1 ' 4 * N.T. * 6 ' TABLE III (cont'd.) COMPATIBILITY AND FREEZE POINT DETERMINATION IN ISONATE 240** CONCENTRATION COMPATIBILITY SEPARATION No, FLOW MODIFIER BY WEIGHT @ 70°C @25°C POINT , °C POINT, °C POINT , . c 39. - Reaction 10 YES YES * 1 * 5°C 5°C Product D (Butyl Carbitol/ 20 YES YES * 1 * 5°C 5°C Mondur MR) 30 YES ES ' 11 5°C 0°C 40, Reaction 10 YES YES (-•) 0°C 0°C . Product E (UCON 50HB660/TDI) 20 YES YES * 1 * 0°C -5°C 30 YES YES (-1.) -10°C -10°C 41. ISONATE 240** NONE 4°C ' * 5 ' 4°C* 5 * Control TABLE III (cont'd.) , FOOTNOTES: (1) See footnote (1), Table I. (2) These mixtures were not ' compatible at 70°C and some reaction with the isocyanate was observed. It appears that catalyst may have been present in the mixture. The flow modifier was analyzed for % H 2 0 and showed no detectable levels of water present. (3) Test tube was reheated to 80°C, contents were reagitated and held at 80°C for one hour, and then allowed to cool to 22°C for at least 4-6 hours. (4) Test tube was reheated to 80°C, contents were reagitated and held at 80°C for en 16 hours, and then allowed to cool for at least 16 hours. ' (5) After 16 hours at 4°C control is a solid mass indicating that crystal formation occurs appreciably above 4°C. (6) Not tested. ** See Trade Name Designation Table supra.

Claims: WHAT IS CLAIMED IS: 1. A stable, compatible liquid mixture which does . not phase separate when stored for several days at temperatures substantially below normal room temperature comprising: (a) an isocyanato-containing prepolymer obtained from the reaction of (i) a diphenyl ethane diisocyanate and (ii) linear or slightly branched polyesterpolyols having hydroxyl equivalent weights of from about 400 to about 2250 and an average hydroxyl functionality of from 2 to about 3, said diisocyanate and said polyesterpolyol being used in such quantities so as to provide at least about 2.5 NCO equivalents per OH equivalent, and (b) from about 3 to about 35 parts by weight, per 100 parts by weight of said prepolymer, of a non-hydroxyl flow modifier, said flow modifier having the following characteristics: (i) a boiling point above about 150°C, (ii) normally-liquid at 20°C or relatively low melting solid which forms a compatible liquid mixture with said prepolymer, (iii) an average molecular weight of from about 100 to approximately 3000, and (iv) consisting essentially of carbon and hydrogen atoms in the form of monovalent or polyvalent hydrocarbon groups or mixtures of such groups; etheric oxygen in the form of oxyalkylene; and at least of a group having the following structural configuration: 0 O O Ri II II II I -NHCO-; -CO-.; - ^ OCO-; -OCO-; and -OR; I Rl wherein each Riindividually, is hydrogen or a monovalent hydrocarbon group, and wherein R is a hydrocarbyl group, and wherein each of the unsatisfied bonds of the above structural units are monovalently bonded to separate carbon atoms of the flow modifier molecule. 2. The liquid mixture of claim 1 wherein: (a) said polyesterpolyols have hydroxyl equiv¬ alent weights of from about 500 to about 2000; (b) said flow modifier is characterized by (i) at least one group consisting of oxyethylene, oxypropylene and mixtures thereof, and (ii) an average molecular weight of at least 135; and (c) said liquid mixture contains from about 5 to about 30 parts of said flow modifier per 100 parts of said prepolymer 3. The liquid mixture of claim 2 wherein: (a) said isocyanato-containing prepolymer is obtained from the reaction of (i) a diphenylmethane diiso¬ cyanate and (ii) linear or slightly branched polyester¬ polyols which have hydroxyl equivalent weights of from about 500 to about 1500 and an average hydroxyl function¬ ality of from about 2 to about 2.5; said diisocyanate and said polyesterpolyol being used in such quantities so as to provide from about 2.7 to about 24 NCO equivalents per OH equivalent, (b) said non-hydroxyl flow modifier has an average molecular weight of about 150 to about 750, and (c) said liquid mixture contains from about 7 parts to about 25 parts of said flow modifier per 100 parts of said prepolymer. 4. The liquid mixture of claim 2 wherein said flow modifier is of the group consisting of compounds of the following seven formulas: R 2 wherein the oxyalkylene group contains from 2 to 4 carbon atoms in the oxyalkylene chain; wherein each R individually is of the group con¬ sisting of a monovalent acyclic group containing up to 17 carbon atoms, a monovalent alicyclic group containing from 5 to 7 carbon atoms in the alicyclic nucleus and up to 2 carbon atoms in any substituent monovalently bonded to the alicyclic nucleus, and a monovalent aromatic group con¬ taining 1 to 2 benzenoid nuclei; wherein J£ has a value of at least 1; wherein has a value of 1 to 5; and wherein R>. is of the group consisting of an acyciic group containing up to 17 carbon atoms., an alicyclic group containing from 5 to 7 carbon atoms in the alicyclic nucleus and up to 2 carbon atoms in any substituent mono¬ valently bonded to the alicyclic nucleus, and an aromatic group containing up to 12 carbon atoms and from 1 to 2 benzenoid nuclei, the valence of R being equal to the value of z; II O O II II R -roxyalkylene■)■_■; OCNH -Rl (.NHCOR 3 ) y wherein R, J , and the oxyalkylene group have the meanings assigned in Formula I supra; wherein R_L iέ an acyclic, alicyclic, or aromatic group having the meanings assigned to R^ in Formula I supra, with the proviso that the valence of Rj_ is equal to the sum of £ plus \[_; wherein each R_^ individually has the meanings assigned to R of Formula I supra; wherein has a value of 1 to 2; and wherein £ has a value of 1 to 2; III - R4 (oxyalkylene) x : —OR4 wherein JC and the oxyalkylene group have the meanings assigned in Formula I supra; and wherein each R^ individually is of the group consisting of acyl and the meanings assigned to R in Formula I supra; IV O R- -(•oxyalkylene ^--_- OCO alkyleneoxy) • wherein R, JC and the oxyalkylene group have the meanings assigned in Formula I supra; V (R4O7m ■ B- -oxyalkylene -g OR4 wherein each R^ individually has the mea 0nings assigned in Formula III supra; . wherein JC and the oxyalkylene group have the meanings assigned in Formula I supra; wherein πi has a value of 0 to 8; wherein £ has a value of 1 to 8; wherein m plus £ is 2 to 8; and wherein B is a polyvalent acyclic, alicyclic or aro¬ matic group and represents the remainder of a poly¬ functional initiator compound without the active hydrogen groups and is composed of up to 12 carbon atoms, hydrogen, and optionally etheric oxygen, the valence of B_ being equal to m plus alicyclic or aromatic group and represents the remainder of a functional initiator compound without the active hydrogen groups and is composed of up to 18 carbon atoms. hydrogen, and optionally etheric oxygen, the valence of R" being equal to the value of t; wherein R is a monovalent group having the meanings in Formula I supra; wherein x is at least 1 and upwards to 8; wherein a_ is zero or JC; wherein has a value of 1 to 3; wherein r_ has a value of 1 to 3; wherein _ has a value of 1 to 5; and wherein Z_ is the remainder, excluding the carboxyl groups of an acyclic, alicyclic or aromatic polycarboxylic acid of 2 to 10 carbon atoms, and having a valence equal to y_ + 1; VII R (oxyalkylene)-J-J O yleneoxy) x R R'" wherein R, JC and the oxyalkylene group have the meanings in Formula I supra; and wherein each R' ' ' individually is hydrogen, a Cχ-C8- alkyl or a C5-C7cycloalkyl. 5. The liquid mixture of claim 4 wherein (a) said prepolymer is obtained from the reaction of (i) a diphenylmethane diisocyanate containing at least 75 weight percent of the 4,4'-isomer and (ii) the said polyester¬ polyol; and wherein (b) said flow modifier is represented by Formula I. . 6. The liquid mixture of claim 4 wherein (a) said prepolymer is obtained from the reaction of (i) a diphenylmethane diisocyanate containing at least 75 weight percent of the 4,4'-isomer and (ii) the said polyester¬ polyol; and wherein (b) said flow modifier is represented by Formula II. 7. The liquid mixture of claim 4 wherein (a) said prepolymer is obtained from the reaction of (i) a diphenylmethane diisocyanate containing at least 75 weight percent of the 4,4'-isomer and (ii) the said polyester¬ polyol; and wherein (b) said flow modifier is represented by Formula III. 8. The liquid mixture of claim 4 wherein (a) said prepolymer is obtained from the reaction of (i) a diphenylmethane diisocyanate containing at least 75 weight percent of the 4,4'-isomer and (ii) the said polyester¬ polyol; and wherein (b) said flow modifier is represented by Formula IV. 9. The liquid mixture of claim 4 wherein (a) said prepolymer is obtained from the reaction of (i) a diphenylmethane diisocyanate containing at least 75 weight percent of the 4,4'-isomer and (ii) the said polyester¬ polyol; and wherein (b) said flow modifier is represented by Formula V.- 10. The liquid mixture of claim 4 wherein (a) said prepolymer is obtained from the reaction of (i) a diphenylmethane diisocyanate containing at least 75 weight percent of the 4,4*-isomer and (ii) the said polyester¬ polyol; and wherein (b) said flow modifier is represented by Formula VI. 11. The liquid mixture of claim 4 wherein (a) said prepolymer is obtained from the reaction of (i) a diphenylmethane diisocyanate containing at lest 75 weight percent of the 4,4'-isomer and (ii) the said polyester¬ polyol; and wherein* (b) said flow modifier is represented by Formula VII. 12. The compatible liquid mixture of claim 3 which is stable and liquid at a temperature of 5°C for at least 100 hours wherein: (a) said flow modifier conforms to the following formula: O 0 II. II Rl_ oxyC2-C3alkylene 3r -OCNH-A-NHCO(C2-C3alkyleneoxy j—R' wherein each R_[_ is Cχ-C8alkyl, a Cs-C cycloalkyl, or aryl- Cι-C3alkyl, wherein A is Ci-Cβalkylene, a cyclohexylene, or a phenylene, and wherein each JC has a value of 1 to 25; and (b) the quantities of said diisocyanate and said polyesterpolyol employed in the preparation of said prepolymer provide from about 3.7 to about 12 NCO equivalents per OH equivalent. 13.. The compatible liquid mixture of claim 3 which is stable and liquid at a temperature of 5°C for at least 100 hours wherein: (a) said flow modifier conforms.to the following formula: O O - II II R » ■ r oxyC2-C3alkylene->-_ζ OCNH-A-NHCOR' wherein each _V_ individually is Ci-Csalkyl, a C5-C7cycloalkyl, or aryl-Cι-C3alkyl, wherein A is Ci-Csalkylene, a cyclohexylene, or a phenylene, and wherein each x. has a value of 1 to 4; and (b) the quantities of said diisocyanate and said polyesterpolyol employed in the preparation of said prepolymer provide from about 3.7 to about 12 NCO equivalents per OH equivalent. 14. The compatible liquid mixture of claim 3 which is stable and liquid at a temperature of 5°C for at least 100 hours wherein: (a) said flow modifier conforms to the following formula: R » - oxyC 2 -C3alkylene) x OR' wherein each R_\_ individually is Cχ-C8alkyl, a C5-C7- cycloalkyl, or aryl-Cι-C3alkyl, and wherein JC has a value of 2 to 5; and (b) the quantities of said diisocyanate and said polyesterpolyol employed in the preparation of said prepolymer provide from about 3.7 to about 12 NCO equivalents per OH equivalent. 15. The compatible liquid mixture of claim 3 which is stable and liquid at a temperature of 5 β C for at least 100 hours wherein: (a) said flow modifier conforms to the following formula: O O II II R5C ( o yC2~C3alkylene π OCR5 wherein each R^ individually is Ci-Csalkyl, a C5-C7- cycloalkyl, aryl-Cχ-C4alkyl, or aryl, and wherein n is 2 to 4; and - (b) the quantities of said diisocyanate and said polyesterpolyol employed in the preparation of said prepolymer provide from about 3.7 to about 12 NCO equivalents per OH equivalent. 16. The compatible liquid mixture of claim 3 which is stable and liquid at a temperature of 5°C for at least 100 hours wherein: (a) said flow modifier conforms to the following formula: O 4oxyC2-C3alkylene) x OCR5 wherein R is Cj-Csalkyl, a C5-C7cycloalkyl, or aryl-Cι-C3alkyl, wherein JC is 2 to 5, and wherein R^ is C l-Ci8alkyl, a C5-C 7 cycloalky, aryl-Cι-C 4 alkyl, or aryl; and ( REΛ (b) the quantities of said diisocyanate and said polyesterpolyol employed in the preparation of said prepolymer provide from about 3.7 to about 12 NCO equivalents per OH equivalent. 17. The compatible liquid mixture of claim 3 which is stable and liquid at a temperature of 5°C for at least 100 hours wherein: (a) said flow modifier conforms to the following formula: . O II R' (OxyC2-C3al ylene)>ζ OCO (C2~C3alkyleneoxy) x R' wherein each R_ individually is Cχ-C8alkyl, a C5-C7- cycloalkyl, or aryl-Cι-C3alkyl, and wherein each x. s 1 to 4; and - - (b) the quantities of said diisocyanate and said polyesterpolyol employed in the preparation of said prepolymer provide from about 3.7 to about 12 NCO equivalents per OH equivalent. 18. The compatible liquid mixture of claim 3 which is stable and liquid at a temperature of 5°C for at least 100 hours wherein: " (a) said flow modifier conforms to the wherein each R individually is Ci-Cisalkyl, a C5-C7- cycloalkyl, aryl-Cχ-C4alky, aryl, or O O R5C-, the R5 moiety of R5C II- having the aforesaid meanings, wherein has a value of 0 to 5, wherein r. has a value of . 1 to 6, wherein the sum £ + equals 3 to 6, wherein __ has an average value of 1 to about 3, and wherein D is a poly¬ valent acyclic, alicyclic or aromatic group and represents OMPI. the remainder of a polyfunctional initiator compound with¬ out the active hydrogen groups and is composed of hydrogen and up to 12 carbon atoms, the valence of being equal to + ; and (b) the quantities of said diisocyanate and said polyesterpolyol employed in the preparation of said prepolymer provide from about 3.7 to about 12 NCO equivalents per OH equivalent. 19. The compatible liquid mixture of claim 3 which is stable and liquid at a temperature of 5°C for at least 100 hours wherein: (a) said flow modifier conforms to the following formula: 0 0 II II R5—(oxyC2-C3al ylene-)- 5 j—OC—R7-CO-4C2-C3alkyleneoxy)-χ R5 wherein each R^ individually is Ci-Cisalkyl, a C5-C7- cycloalkyl, aryl-Cχ-C4alkyl,- or aryl, wherein Rj. repre¬ sents the remainder of a dicarboxylic acid having up to 10 carbon atoms and lacking the two carboxyl groups, and wherein JC is 1 to 4; and (b) the quantities of said diisocyanate and said polyesterpolyol employed in the preparation of said prepolymer provide from about 3.7 to about 12 NCO equivalents per OH equivalent. 20. The compatible liquid mixture of claim 3 which is stable and liquid at a temperature of 5°C for at least 100 hours wherein: (a) said flow modifier conforms to the followig formula: Rθ I R' toxyC2-C3alkylene) x - OCO - C2~C3alkyleneoxy ) x ■ RO OMPI wherein each R°_ individually is hydrogen, methyl, or ethyl, wherein each R__ individually is Ci-Csalkyl, a C5-C7cycloalkyl, or aryl-Cι-C3alkyl, and wherein each x is 1 to 4; and (b) the quantities of said diisocyanate and said polyesterpolyol employed in the preparation of said prepolymer provide from about 3.7 to about 12 NCO equivalents per OH equivalent. 21. The compatible liquid mixture of claim 15 which is stable and liquid at 5°C for at least 100 hours where¬ in: (a) said flow modifier has the following formula: O . O • II II ...C6H5COCHCH2OCH2CHOCC6H5, and CH3, . . CH 3 (b) said prepolymer is the product, of the reaction of (i) a diphenylmethane diisocyanate and (ii) linear or slightly branched polyesterpolyols having hydroxyl equivalent weights of from about "" 750 to " about 1250 and an average hydroxyl functionality of from 2 to about 2.2, the amounts of said diisocyanate and said poly¬ esterpolyol used in the reactio providing from about -7 to about 12 NCO equivalents per OH equivalent. 22. The compatible liquid mixture of claim 15 which is stable and liquid at 5°C for at least 100 hours where¬ in: (a) said flow modifier has the following formula: O O II II CH 3 ( CH2 ) 3CHCO (C 2 H4θ j CCH (CH 2 ) 3CH 3 C2H5 C2H5 wherein x has a value of 3 to 4., and OMPI (b) said prepolymers are the products of the reaction of (i) a diphenylmethane diisocyanate and (ii) linear or slightly branched polyesterpolyols having hydroxyl equivalent weights of from about 750 to about 1250 and an average hydroxyl functionality of from 2 to about 2.2, the amounts of said diisocyanate and said polyesterpolyol used in the reaction providing from about 7 to about 12 NCO equivalents per OH equivalent. 23. The compatible liquid mixture of claim 19 which is stable and liquid at 5°C for at least 100 hours wherein: (a) said flow modifier has the following formula: O O II II C4H9OC2H40C2H40CYC0C2H40C2H40C4H9 wherein jf is propylene, butylene, octylene, or ortho-phenylene, and (b) said prepolymers are the products of the reaction of (i) a diphenylmethane diisocyanate and (ii) linear or slightly branched polyesterpolyols having hydroxyl equivalent weights of from about 750 to about 1250 and an average hydroxyl functionality of from 2 to about 2.2, the amounts of said diisocyanate and said " polyesterpolyol used in the reaction providing from about 7 to about 12 NCO equivalents per OH equivalent. 24. The compatible liquid mixture of claim 20 which is stable and liquid at 5°C for at least 100 hours wherein: (a) said flow modifier has the following formula: C4H9OC2H4OC2H4OCH2OC2H4OC2H4OC4H9, and (b) said prepolymers are the products of the reaction of (i) a diphenylmethane diisocyanate and (ii) OMPI linear or slightly branched polyesterpolyols having hydroxyl equivalent weights of from about 750 to about 1250 and an average hydroxyl functionality of from 2 to about 2.2, the amounts of said diisocyanate and said poly¬ esterpolyol used in the reaction providig from about 7 to about 12 NCO equivalents per OH equivalent. 25. The compatible liquid mixture of claim 12 which is stable and liquid at 5°C for at least 100 hours where¬ in: (a) said flow modifier has the following formula: ,4- and/or 2,6-tolylene wherein R_[_ is Cχ-C6alkyl or phenyl, and wherein JC is, at least 1, and (b) said prepolymers are the products of the reaction of Ci) a diphenylmethane diisocyanate and (ii) linear or slightly branched polyesterpolyols having hydroxyl equivalent weights of from about 750 to about 1250 and an. average hydroxyl functionality of from 2 to about 2.2, the amounts of said diisocyanate and said poly¬ esterpolyol used in the reaction providing from about 7 to about 12 NCo equivalents per OH equivalent. 26. The compatible liquid mixture of claim 25 where¬ in the variables of the flow modifier have the following significance: R' represents methyl, JC equals 2, and the oxy-C2-C3- alkylene group is oxyethylene. 27. The compatible liquid mixture of claim 25 where¬ in the variables of the flow modifier have the following significance: R' represents butyl, JC equals 2, and the oxy-C2"~ c 3"" alkylene group is oxyethylene. 28. The compatible liquid mixture of claim 25 wherein the variables of the flow modifier have the following significance: R' represents hexyl, JC equals 2, and the oxy-C2-C3alkylene group is oxyethylene. 29. The compatible liquid mixture of claim 25 wherein the variables of the flow modifier have the following significance: R' represents butyl, JC equals 1, and the oxy-C2 _ C3alkylene group is oxypropylene. 30. The compatible liquid mixture of claim 25 wherein the variables of the flow modifier have the following significance: R 1 represents propyl, JC equals 1, and the oxy-C2-C3alkylene group is oxypropylene. 31. The compatible liquid mixture of claim 25 wherein the variables of the flow modifier have the following significance: R 1 represents phenyl, JC equals 1 or 2, and the oxy-C2-C3alkylene group is oxyethylene. ••»£.■ 32. As a composition, a non-hydroxyl. flow modifier of the group consisting of Formula A infra: A. - wherein the oxyalkylene group contains from 2 to 4 carbon atoms in the oxyalkylene chain; wherein each R, individually, represents a monovalent acyclic, alicyclic or aromatic group; wherein JC is at least one and upwards to 25; wherein is from 1 to 5; and wherein R^ represents a monovalent acyclic, alicyclic or aromatic group when z_ is 1 or a polyvalent acyclic, alicyclic or aromatic group when is 2 to 5, the valence of R^ being equal to the valence of ; and Formula B infra: B O O II II R (oxyalkylene -)-__ OCNH- ■ Rl (NHCOR3 c wherein R, x and oxyalkylene have the meanings assigned in Formula A supra, wherein Rj ^ is a polyvalent acyclic, alicyclic, or aromatic group having the polyvalent meanings assigned to R_ of Formula I supra, the valence of R l being equal to £ plus y_, wherein each R^ individually is an acyclic, alicyclic or aromatic group; wherein _ has a value of 1 to 2; and wherein £ has a value of 1 to 2. 33. The compositions of claim 32 wherein the oxyalkylene units in Formulas A and B are oxyethylene. 34. The composition of claim 32 wherein said flow modifiers are defined by Formula A. 35. * The composition of claim 32 wherein said flow modifiers are defined by Formula B. 36. As a composition, a non-hydroxyl flow modifer of the group consisting of Formula C infra: C O O . II II R , -(-oxyC2-C3alkylene • h ^ —OCNH- - HCO-(.C2-C3alkyleneoxy)χ_R , wherein each R_^, individually, is of the group consisting of alkyl, a C5-C7cycloalkyl, and aralkyl; wherein A represents Ci-Csalkylene, a cyclohexylene, Cι-C4cyclohexylenelalkylene, a phenylene, a divalent diphenylenemethane, and the divalent hydrogenated OMPI counterparts thereof; wherein JC is at least one and up¬ wards to * 25; and wherein the oxyC2~C3alkylene unit is oxy¬ ethylene, oxypropylene, oxyethyleneoxypropylene, or mix¬ tures thereof; and Formula D infra: D O O II II - roxyC2-C3alkylene-)-χ- OCNH- 'NHCOR' wherein R_, A, JC, and oxyC2-C;_alkylene have the meanings assigned in Formula C above. 37. The compositions of claim 36 wherein the oxyC2~ C3alkylene unit in Formulas C and D is oxyethylene. 38. The compositions of claim 36 wherein the variable JC in Formulas C and D is 2 to 25. 39. The compositions of claim 36 wherein the variable JC in Formulas C. and D is 2 to 8. 40. As a composition, a non-hydroxyl flow modifier of the group consisting of Formula E infra: E O II R*—-froxyC2-C3alkylene -__—OCNH- -2,4-and/or 2,6-tolylene wherein each R_, individually, is of the group consisting of alkyl and phenyl; wherein JC is from 2 to 8; and wherein oxyC2-C3alkylene is oxyethylene, oxypropylene, or oxy¬ ethyleneoxypropylene; and Formula F infra: F 0 II 4oxyC2-C3alkylene )_z—OCNH- wherein- Y represents a 4,4'-and/or 2,4'-diphenylenemethane ^ m E { or C4-C6alkylene; and wherein R__, JC, and the oxyC2~C 3 alkylene unit have the meanings assigned in Formula E above. 41. The compositions of claim 40 wherein the oxyC2-C3alkylene units in the Formulas E and F are oxyethylene units.

Inventors: HOSTETTLER FRITZ, HOSTETTLER, FRITZ
Applicants: HOSTETTLER FRITZ, PIRRI JAQUELYN P, HOSTETTLER, FRITZ, PIRRI, JAQUELYN, P.
Application year: 1984
Main classification: C09K3
IPC codes: C08G18, C08J9, C08K5, C08L75