EP0171394A1 - Synthese de produits de polyurethane - Google Patents

Synthese de produits de polyurethane

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Publication number
EP0171394A1
EP0171394A1 EP19840902667 EP84902667A EP0171394A1 EP 0171394 A1 EP0171394 A1 EP 0171394A1 EP 19840902667 EP19840902667 EP 19840902667 EP 84902667 A EP84902667 A EP 84902667A EP 0171394 A1 EP0171394 A1 EP 0171394A1
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EP
European Patent Office
Prior art keywords
polyol
flow modifier
polyurethane
parts
product
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EP19840902667
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German (de)
English (en)
Inventor
Fritz Hostettler
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Pirri Jaquelyn P
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Pirri Jaquelyn P
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Publication date
Application filed by Pirri Jaquelyn P filed Critical Pirri Jaquelyn P
Publication of EP0171394A1 publication Critical patent/EP0171394A1/fr
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    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
    • C08K5/00—Use of organic ingredients
    • C08K5/16—Nitrogen-containing compounds
    • C08K5/205—Compounds containing groups, e.g. carbamates

Definitions

  • This invention relates to the synthesis of polyurethane products obtained by the reaction of form- ulation(s) comprising polyol, polyisocyanate, and chain extender, in the presence of a flow modifier which is characterized by at least one urethane group, i.e.,
  • the reactants of choice such, as in a two package system, e.g., the isocyanate materials in one package and the materials forming the second package, e.g., polyol- (polyester polyol or polyether polyol), chain extender, blowing agents (organic and/or H 2 O) , cell regulation agent, etc., which may comprise this isocyanate-curable second package, can influence the kind of polyurethane product obtained as well as its over-all properties.
  • the polyurethane product can be, for instance, a dense elastomer or an integral skin microcellular elastomer or open cellular product and the like.
  • Plasticizers are widely used in polymer arts such as with polyvinyl chloride, chloroprene resins, acrylics, polyvinyl butyral, nitrile rubber, polyreuthanes, cellulosic products, and others.
  • the plasticizer should be compatible with and not "sweat out” from the plasticized resin. Desirably the plasticizer should act as a processing aid during the formation of the resin or ultimate resinous article.
  • the plasticizer should achieve the goals which dictated its use in the first place without detracting from the properties of the unplasticized resin.
  • formulations comprising flow modifier, isocyanate compound, polyol, chain extender, and other urethane-forming ingredients have been found to be extremely useful and, indeed preferred for the preparation of homogeneous and cellular polyurethane products, especially microcellular products such as, for example, integral skin microcellular polyurethanes.
  • microcellular products such as, for example, integral skin microcellular polyurethanes.
  • Such products exhibit a broad spectrum of highly desirable and/or improved characteristics.
  • 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 good flex life, high tear strength, and generally superior abrasion resistance.
  • Another object of this invention is to synthesize polyurethane products from formulations containing at least one non-hydroxyl flow modifier which is characterized by at least one urethane group, i.e., Another object of the invention is to provide novel compatible homogeneous liquid mixtures containing polyol and flow modifier which are isocyanate curable to yield improved polyurethane products, especially microcellular products including integral skin microcellular articles, flexible polyester and polyether urethane foams, and solid elastomers.
  • a further object of the invention pertains to novel flow modifiers per se and to the processes for their preparation.
  • a still further object of the invention relates to single and multipackage systems in which the single package or Component (A), an isocyanate curable system, comprises the polyol and chain extender reactants and at least one flow modifier, whereas the multipackage system includes Component (A) above and Component (B) which contains a polyisocyanate reactant.
  • non-hydroxyl flow modifiers which are contemplated in the preparation of polyurethane products have a boiling point above about 150°C and are normally- liquid, i.e., liquid at about room temperature, or are relatively low melting solids which form with the polyisocyanate compounds or the polyols compatible liquid mixtures at room temperature or at the temperature of use.
  • the flow modifier consists essentially of (a) carbon and hydrogen atoms preferably in the form of a monovalent and/or polyvalent hydrocarbon groups such as a C 1 -C 18 - acyclic group, a C 5 -Cycycloaliphatic group including the mono and poly C 1 -C 4 alkyl substituted counterparts thereof and/or a benzenoid ring nucleus, e.g., mono-, fused-, and bridged nuclei, including the partially or fully hydro genated ring nuclei and the unsubstituted- and mono and poly C 1 -C 4 alkyl substituted- counterparts thereof; (b) etheric oxygen in the form of oxyalkylene group (s), and optionally, also in the form of alkoxy, cycloalkoxy, and
  • aryloxy and (c) at least one urethane group and upwards to five such groups, preferably 2-3 such groups, each of the monovalent bonds of the urethane group being monovalently attached to separate carbon atoms of the flow modifier molecule.
  • oxyalkylene characterizes an oxy atom bonded to an acyclic or alicyclic carbon atom to form, as by way of illustrations, the unit
  • Illustrative divalent oxyalkylene groups include oxyethylene, oxypropylene, oxytrimethylene, oxytetramethylene, chloromethyl-substituted oxyethylene, phenyl-substituted oxyethylene, dimethyl-substituted oxyethylene, cyclohexyleneoxy cyclopentyleneoxy, and methyl-substituted cyclohexyleneoxy; the mixed oxyalkylenes of the above such as oxyethyleneoxypropylene, oxvethyleneoxybutylene, and oxypropyleneoxybutylene; mixed oxyalkylenes which contain minor amounts of oxymethylene groups and the random and block oxyalkylenes of the foregoing; and the like.
  • the flow modifiers contemplated in the practice of various embodiments of the invention are characterized by at least one oxyalkylene group and upwards to 25, and more, of such groups per urethane group, as shown in Formula I infra.
  • the terminal oxyalkylene group is "capped" by a monovalent hydrocarbon group such as a C 1 -C 17 ac ⁇ clic hydrocarbon group, desirably a C 1 -C 8 alkyl group.
  • a suitable upper limit is eight 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).
  • the average molecular weight of the flow modifiers which are employed in the preparation of the novel polyurethane products can vary over a wide range, e.g., upwards to a few thousand, e.g., approximately 3000.
  • the flow modifier as noted previously, is a normally-liquid material or a relatively low melting solid, and forms a compatible liquid with the polyisocyanate reactant and/or polyol reactant at room temperature or at the temperature of use (in the formation of polyurethane products).
  • Desirable flow modifiers are those which are prepared from readily available and relatively inexpensive starting materials, e.g., 2,4- 2,6-tolylene diiso ⁇ yanate, methoxyethanol, butoxyethanol, methyl Carbitol, butyl Carbitol, and the like.
  • flow modifiers having molecular weights of at least about 250-500 are particularly useful, though lower molecular weights are contemplated.
  • 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.
  • flow modifiers which are suitable in the practice of the invention (s) are shown structurally in Formula I infra.
  • 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 z is from 1 to 5, preferably 2 to 3; and wherein R 2 represents a monovalent acyclic, alicyclic or aromatic group when z is 1 or a polyvalent acyclic, alicyclic or aromatic group when z is 2 to 5, the valence of R 2 being equal to the value of z .
  • the maximum average number of oxyC 2 -C 3 alkylene 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 which at room temperature or at the temperature of use forms a compatible stable liquid with the polyisocyanate and/or polyol reactant(s).
  • 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, methylcyclohexyl, cyclohexyl, cyclohexylmethyl, cycloheptyl, and cyclohexenyl.
  • aryls mono-, fused-, and bridged- aryls, and the partially hydrogenated aryls
  • R 2 groups include alkyl, cycloalkyl, and the aryls illustrated previously as well as the corresponding higher polyvalent acyclic, alicyclic and aromatic groups, e.g., alkylene, cycloalkylene, arylene, and the like.
  • R 2 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, cyclohexenylene, phenylene, 1,5-naphthylene, 1-methoxy-2,4-phenylene, 1-chloro-2,4-phenylene, hexahydronaphthylene, 4,4'-dicyclohexylene-methane, 1-propoxy-2,4-phenylene, xylylene, and tolylene.
  • 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 z equals 2.
  • each R' individually is C 1 -C 8 alkyl, C 5 -C 7 cycloalkyl, methyl- or ethyl-substituted C 5 -C 7 cycloalkyl, or aryl-C 1 -C 3 alkyl; wherein A represents C 1 -C 8 alkylene, cyclohexylene, C 1 -C 2 alkyl- or C 1 -C 2 alkoxy-substituted cyclohexylene, unsubstituted, C 1 -C 3 alkyl-, or C 1 -C 3 alkoxy- substituted phenylene (preferably tolylene), or divalent (4,4'- and 4,4'-/4,2'-)diphenylenemethane, or the divalent hydrogenated counterparts of the foregoing; wherein x is at least one and upwards to 25, and more, preferably 1 to 4; and wherein the oxyC 2 C 3 alkylene unit is oxyethylene,
  • the flow modifiers of Formulas I and IA are readily prepared by reacting monohydroxyl-terminated oxyalkylene compounds, e.g., 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 monohydroxyl-terminated oxyalkylene compounds can be prepared by reacting a monofunctional initiator which contains an active hydrogen atom with an epoxide compound, the preferred initiator being a monohydric alcohol or a phenol and the preferred epoxide compound being the alkylene oxides such as ethylene oxide, propylene oxide, and mixtures thereof, in the presence of a base catalyst. Prior to reacting the resulting monohydroxyl-terminated polyether 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 aromatic 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 tolylene 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.
  • R, x and oxyalkylene have the meanings or values assigned in Formula I supra, wherein R 1 is a polyvalent (generally a di-, tri- or tetravalent) acyclic, alicyclic, or aromatic group having the broad and preferred meanings assigned to polyvalent R 2 of Formula I supra, the valence of R 1 being equal to c plus y, wherein each R 3 individually 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 y has a value of 1 to 2, preferably one, and wherein c 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
  • R', A, x and oxyC 6 -C 3 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) x 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
  • various aspects of the invention are to provide novel formulations and novel processes to prepare highly useful and improved polyurethane products.
  • Such formulations comprise polyol, chain extenders, organic polyisocyanates, and at least one flow modifier.
  • the invention contemplates the "one shot” process and the stepwise or prepolymer processes, including the total prepolymer process and the "quasi-prepolymer” process, wherein only a portion of the polyol is reacted stepwise with the polyisocyanate.
  • the quasi-prepolymer process is the most suitable and preferred in the production of improved microcellular products contemplated by the invention.
  • the one-shot process is the preferred process in the manufacture of flexible polyester and polyether polyurethane foams.
  • the prepolymer process is normally preferred. In this case it is highly preferable to combine the chain extender with the flow modifier as a separate stream.
  • Improved cellular polyurethane products, especially microcellular products including integral skin microcellular articles and flexible foams, can be obtained by using blowing agents as well as other known polyurethane-forming or polyurethane-aiding ingredients, as desired.
  • polyisocyanates suitable in the preparation of such useful polyurethane products include the acyclic, alicyclic and aromatic polyisocyanates, mixtures of these polyisocyanates and their carbodiimide derivatives, and in particular polyester and polyether prepolymers of these polyisocyanates. Mixtures of these prepolymers with diisocyanates per se and with their carbodiimides are also contemplated.
  • diisocyanates include 1,4-tetramethylene diisocyanate, 1,6-hexamethylene diisocyanate, isophorone diisocyanate the urea derivative of this isocyanate [OCN(CN 2 ) 6 NHCONH(CH 2 ) 6 NCO] , cis and trans isomers of methylene bis-(cyclohexyl isocyanate), 4,4'-benzidine diisocyanate, 3,3'-dimethyl-4,4'-benzidine diisocyanate, p-phenylene diisocyanate, 2,4/2,6-isomers of tolylene di-isocyanate, 1,5-naphthylene diisocyanate, 4,4'-diphenylmethane diisocyanate, 4,4'-diphenylmethane diisocyanate containing up to 25%, or more, of the 2,4'- and 2,2'-isomer, a mixture of 4,4'-diphen
  • Isocyanato-terminated prepolymers suitable in the practice of the invention are prepared by reacting a polyester polyol or polyether polyol described hereinafter with a polyisocyanate compound, e.g., acyclic, alicyclic and aromatic polyisocyanates.
  • a polyisocyanate compound e.g., acyclic, alicyclic and aromatic polyisocyanates.
  • Suitable polyisocyanates for this purpose include mixtures of 2,4- and 2,6-tolylene diisocyanates, and polyisocyanate compounds characterized by methylene groups (-CH 2 -), each valence of which is separately bonded to a carbon atom of a benzenoid nucleus such as a diphenylraethane diisocyanate (MDI), for example, 4,4'-diphenylmethane diisocyanate, 2,4'-diphenylmethane diisocyanate, mixtures of 4,4'-MDI and 2,4'-MDI, a mixture of 4,4'-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.
  • MDI diphenylraethane diisocyanate
  • the isocyanate compound and polyol are reacted in a ratio of NCO groups to OH group 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).
  • NCO 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.
  • Polyols useful in the preparation of a wide variety of polyurethane products have molecular weights in the range of from about 1800 to about 10,000 and preferably in the range from 2000 to 5000.
  • Polyethers containing at least 2 and preferably 2 to 3 hydroxyl groups are suitable for use in the invention, are known, and are obtained, for example, by the polymerization of epoxides, such as ethylene oxide, propylene oxide, butylene oxide, tetrahydrofuran, styrene oxide or epichlorohydrin alone, for example in the presence of BF 3 , or by the chemical addition of these epoxides, optionally in admixture with or in succession to starter components having reactive hydrogen atoms.
  • epoxides such as ethylene oxide, propylene oxide, butylene oxide, tetrahydrofuran, styrene oxide or epichlorohydrin alone, for example in the presence of BF 3 , or by the chemical addition of these e
  • Such starter compounds include water, alcohols, or amines, such as ethylene glycol, 1,3- or 1,2-propylene glycol, trimethylolpropane, 4,4'-dihydroxy-diphenylpropane, aniline, ammonia, ethanolamine and ethylenediamine.
  • polyethers of the kind which contain predominant amounts of primary hydroxyl (-OH) groups (up to 90% by weight, based on all the hydroxy groups present in the polyether).
  • Polyethers modified by vinyl polymers of the type obtained by the polymerization of styrene and/or acrylonitrile in the presence of polyethers (U.S. Pat. Nos. 3,383,351; 3,304,273; 3,523,093; 3,110,695; German Pat. No. 1,152,536) are also suitable, as are polybutadienes containing hydroxyl groups.
  • Polyesters, polythioethers, polyacetals, polycarbonates, and polyesteramides containing hydroxyl groups of the type commonly used for the production of homogeneous and cellular polyurethanes may also be used in appropriate proportions.
  • suitable polyesters containing hydroxyl groups are reaction products of polyhydric (preferably dihydric and, optionally, trihydric) alcohols with polybasic (preferably dibasic carboxylic acids).
  • polyhydric preferably dihydric and, optionally, trihydric
  • polybasic preferably dibasic carboxylic acids
  • the corresponding polycarboxylic acid anhydrides or corresponding polycarboxylic acid esters of lower alcohols or mixtures thereof may also be used for the production of the polyesters.
  • the polycarboxylic acids may be aliphatic, cycloaliphatic, aromatic and/or heterocyclic, and may optionally be substituted, for example, by halogen atoms, and/or may be unsaturated.
  • These polycarboxylic acids 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, tetrachlorophthalic acid anhydride, endomethylene tetrahydrophthalic acid anhydride, glutaric acid anhydride, maleic acid, maleic acid anhydride, fumaric acid, dimeric and trimeric fatty acids such as oleic acid, optionally in admixture with monomeric fatty acids, terephthalic acid dimethyl ester and terephthalic acid-bisglycol ester
  • Suitable polyhydric alcohols include ethylene glycol, 1,2- and 1,3-propylene glycol, 1,4- and 2,3-butylene glycol, 1,6-hexanediol, 1,8-octanediol, neopentyl glycol, cyclohexanedimethanol (1,4-bis-hydroxy-methylcyclohexane), 2-methyl-1,3-propanediol, glycerol, trimethylolpropane, 1,2,6-hexanetriol, 1,2,4-butanetriol, trimethylolethane, pentaerythritol, quinitol, mannitol and sorbitol, methyl glycoside, diethylene glycol, triethylene glycol, tetraethylene glycol, polyethylene glycols, dipropylene glycol, polypropylene glycols, dibutylene glycol and polybutylene glycols.
  • the polyesters may contain terminal carboxyl groups. Polyester
  • polythioethers are the condensation products of thiodiglycol with itself and/or with other glycols, dicarboxylic acids, formaldehyde, aminocarboxylic acids or amino alcohols. Depending upon the co-components, these products are polythio mixed ethers, polythioether esters or polythioether ester amides.
  • Suitable polyacetals include those compounds which can be obtained from glycols, such as diethylene glycol, triethylene glycol, 4,4'-dioxethoxydiphenyldimethyl-methane, hexanediol and formaldehyde. Other suitable polyacetals may be obtained by polymerizing cyclic acetals.
  • Suitable polycarbonates containing hydroxyl groups are those known per se. They are obtained for example, by reacting diols such as 1,4-propanediol, 1,4-butanediol and/or 1,6-hexanediol, diethylene glycol, triethylene glycol, tetraethylene glycol; with diaryl carbonates such as diphenyl carbonate or phosgene.
  • polyester amides and polyamides are the predominantly linear condensates obtained from polyhydric saturated and unsaturated amino alcohols, diamines, polyamines, and mixtures thereof.
  • the flow modifiers may also be admixed with a wide variety of polyols illustrated herein with/without other ingredients normally used in the formation of polyurethane products to form novel compatible liquid blends at room temperature or at the temperature of use. Accordingly, desirable aspects of the invention are directed to such novel blends in which there can be included the flow modifier in the "polyol resin" side, e.g., polyol, chain extender, with/without blowing agent, and other typical urethane ingredients.
  • polyol resin e.g., polyol, chain extender
  • Flow modifiers of the present invention which perform well in the manufacture of polyurethane articles, especially in the manufacture of microcellular parts such as normal polyurethane shoe soles or integral skin shoe soles having a lower density microcellular core, flexible polyether and polyester polyurethane foams possessing the ability to conduct static electricity, and solid polyurethane elastomers characterized by relatively low hardness and high coefficient of friction, have generally been observed to form soluble, compatible homogeneous liquid mixtures with the polyol or with polyol/chain extender blends.
  • chain extenders are illustrated by glycols, amino alcohols, diamines and water, as well as mixtures of these extenders.
  • the flow modifiers can decrease the viscosity of the polyol reactant mixture, a highly desirable aspect for low temperature processing on polyurethane machinery.
  • Their inclusion with the urethane-forming ingredients also improves the flow of materials, slows down the gel-formation of the polymer, thus bringing about capability to obtain exacting molded products, e.g., shoe soles, vehicle tires, integral-skin parts for automotive applications such as arm rests, instrument panels, and the like, from mold cavities of intricate pattern and design.
  • the concentration of the flow modifiers can be in the range of from about 5 parts to as high as 50 parts and higher of flow modifier per 100 parts of polyol.
  • the amount of flow modifier utilized is generally dictated, among other considerations, by its upper limit of compatibility with the resulting polyurethane product. Such compatibility depends upon many variables such as composition of the polyol backbone, the nature of the polyisocyanate and chain extender, and of course upon the chemical composition of the flow modifier contemplated in the present invention.
  • suitable proportions of flow modifier generally range from about 5 to 35 parts, desirably from about 10 to 30 parts, per 100 parts of polyol.
  • flow modifier levels of from about 20 to 50 parts per 100 parts of polyol are generally suitable.
  • soft elastomers microcellular and/or solid
  • the use of about 5 to 20 parts of flow modifier per 100 parts of polyol is generally desirable.
  • One or more than one flow modifier can be employed in the practice of the inventions.
  • Chain extenders which are especially useful in the invention are the glycols, amino alcohols, diamines and water.
  • Typical glycols are illustrated by the alkanediols of the formula wherein n is 2 to 10 or more, e.g., ethylene glycol, 1,3-propanediol, 1,4-butanediol, 1,5-pentanediol, 1, 6-hexanediol, 1 ,10-decanediol, and the like.
  • glycols that are suitable include diethylene glycol-, thiodiglycol, triethylene glycol, tetraethylene glycol, p-xylylenediol, quinitol, neopentylene glycol, dihydroxyethylhydroquinone, and mixtures thereof, and the like. It is also possible to use glycols characterized by hetero atoms such as nitrogen and/or sulfur; double bonds; and bromine or other halogen atoms.
  • N-methyldiethanolamine N-t-butyldiethanolamine, di-beta-hydroxyethylaniline, triethanolamine, triisopropanolamine, di-beta-hydroxyethyl sulfide, 2-butene- 1,4-diol, 2,3-dibromo-1,4-butanediol, di-beta-hydroxyethylurea, and di-beta-hydroxyethyl urethane.
  • Suitable triol chain extenders further include glycerol, trimethylolpropane, 1,2,6-hexanetriol, and the like.
  • Short chain glycol extenders such as ethylene glycol, 1,4-butanediol, 1, 6-hexanediol, di-beta-hydroxyethylaniline and mixtures thereof are preferred.
  • Suitable amino alcohol and polyamine chain extenders include ethanolamine, p-hydroxyethylaniline, ethylenediamine, 1, 6-hexanediamine, 4,4'-diphenylmethane diamine, methylene-bis-(o-chloroaniline), 3,3'-dichloro-4, 4'- benzidine, perethylated 2,4- and 2,6-tolylenediamines, 1,4-cyclohexylenediamine, m-xylylenediamine, piperazine, hydrazine, N,N'-dimethylhydrazine, diethylenetriamine, and the like.
  • water and polycarboxylic acids, and the like may be used as chain extenders.
  • water is highly preferred.
  • Cellular products in particular, microcellular products including integral skin microcellular polyurethanes can be prepared by using well-known blowing agents.
  • the choice of the blowing agent(s) is significantly influenced by the polyol reactant employed and the type of cellular polyurethane product desired.
  • the use of water as the blowing agent in a formulation containing a polyether polyol and prepolymer (from polyether polyol and MDI) in the presence of the flow modifier will yield an open cell foamed product whereas the use of an organic blowing agent with/without a small amount of water in a formulation comprising polyester polyol, glycol chain extender, and prepolymer (derived from polyester polyol and MDI) in the presence of the flow modifier, in a closed mold system, results in an improved integral skin microcellular polyurethane product.
  • Illustrative blowing agents include water, the halogenated hydrocarbons, in particular fluorocarbons such as trichlorofluoromethane, 1 ,1-difluoro-1-chloro-2-fluoro-2-dichloro-ethane, difluorodichloromethane, and mixtures of the same and the like halogenated hydrocarbons. It is also feasible to use mixtures of low boiling hydrocarbons, ethers, and ketones with halogenated hydrocarbons. Additional blowing agents are well known in the art. Flexible polyurethane foams exhibiting the capability to conduct static electricity can be prepared by employing flow modifiers described in the present invention that contain a high amount of oxyethylene units.
  • Suitable flow modifiers contain at least about 50%, by weight, of oxyethylene units in the polyether chain, preferably about 75%, by weight of oxyethylene units, and highly preferably about 85%, by weight, or more of such oxyethylene units, in the polyether chain of said flow modifier.
  • Such polyurethane foams can, for example, be prepared from suitable branched polyether polyols, water as the blowing agent and chain extender, and the commercially known 80: 20isomeric mixture of 2,4- and 2,6-tolylene diisocyanate.
  • Typical flow modifier concentrations in the polyurethane foam can vary from about 15-40 weight %, based on the weight of the polyurethane foam, preferably from about 20-30% by weight.
  • Antistatic modifiers of this type can also be used in microcellular elastomers for shoe soles and the like. Such products have excellent utility as carpet underlayments for computer rooms, or for footwear applications where static electricity presents a hazard or other problem.
  • the flow modifers of the present invention are eminently suitable for the manufacture of polyurethane elastomers of relatively low hardness, for example, from 50-65 Shore A. These hardness ranges can be attained at flow modifier levels of from about 5-15 % by weight, based upon the combined ingredients employed in the preparation of said polyurethane elastomers. These products have the capability to approach the friction properties of natural and synthetic rubbers, and lend themselves to use as skidresistant footwear products having outstanding toughness, durability, and wear resistance, while exhibiting outstanding flexibility at low temperatures. Catalysts which are employed for the purpose of accelerating the well-known NCO/active hydrogen chemical reactions include tertiary amines, metallic catlaysts and combinations thereof.
  • Typical amine catalysts include tertiary amines, such as triethylamine, tributylamine, N-methylmorpholine, N -ethylmorpholine, N-cocomorpholine, N,N,N',N'-tetramethylethylenediamine, 1,4-diazabicyclo- [2.2.2] octane, N-methyl-N'-dimethylaminoethylpiperazine, N,N-dimethylbenzylamine, bis-(N,N-diethylaminoethyl)-adipate, N,N-diethylbenzylamine, pentamethyldiethylenetriamine, N,N-dimethylcyclohexylamine, N,N,N'-N'-tetramethyl-1,3-butanediamine, N,N-dimethyl-beta-phenylethylamine, 1, 2-dimethylimidazole and 2-methylimidazole.
  • Suitable catalysts are known Mannich bases of secondary amines such as dimethylamine, and aldehydes, preferably formaldehyde; or ketones such as acetone, methyl ethyl ketone, and cyclohexanone; or the phenols such as phenol, nonylphenol and bisphenol.
  • Tertiary amines containing isocyanate-reactive hydrogen atoms may also be used as catalysts and include triethanolamine, triisopropanolamine, N-methyldiethanolamine, N-ethyldiethanolamine, N,N-dimethylethanolamine, also their reaction products with alkylene oxides such as propylene oxide and/or ethylene oxide.
  • Suitable catalysts are sila-amines with carbonsilicon bonds of the type described, for example, in U.S. Pat. No. 3,620,984. Specific examples include 2,2,4-trimethyl-2-silamorpholine and 1,3-diethylaminomethyltetramethyldisiloxane.
  • nitrogen-containing bases such as tetraalkylammonium hydroxides; alkali metal hydroxides such as sodium phenolate; or alkali metal alcoholates such as sodium methylate.
  • Hexahydrotriazines may also be used as catalysts.
  • Organotin compounds and organomercury compounds may also be used as catalysts.
  • Preferred organotin compounds include tin (II) salts of carboxylic acids, such as tin (II) acetate, tin (II) octoate, tin (II) ethylhexoate and tin (II) laurate, and tin (IV) compounds such as dibutyltin oxide, dibutyltin dichloride, dibutyltin diacetate, dibutyl dilaurate, dibutyltin maleate or dioctyltin diacetate. It is of course possible to use any of the above-mentioned catalysts in the form of mixtures. Organic mercury catalysts are described in U.S. Pat. No. 3,642,044.
  • the catalyst can be employed in catalytically significant quantities, for example, from about 0.01 to about 1 percent by weight, based on the curable formulation.
  • emulsifiers include the sodium salts of castor oil sulphonates or salts of fatty acids with amines, such as diethylamine oleate or diethanolamine stearate.
  • amines such as diethylamine oleate or diethanolamine stearate.
  • Alkali metal or ammonium salts of sulphonic acids for example, of dodecylbenzenesulphonic acid or dinaphthylmethanedisulphonic acid, or of fatty acids, such as ricinoleic acid or of polymeric fatty acids, may also be used as surface-active additives.
  • Suitable foam stabilizers include polyether siloxanes, especially those which are water-soluble. These compounds are generally synthesized in such a way that a copolymer of ethylene oxide and propylene oxide is attached to a polydimethylsiloxane radical. Foam stabilizers of this type are described, for example, in U.S. Pat. Nos. 2,834,748; 2,917,480; and 2,629,308.
  • cell regulating agents such as polydimethylsiloxanes having viscosities of from about 2 to about 100 centistokes at 25°C., preferably from about 2 to about 50 centistokes at 25°C.; polyphenylmethylsiloxanes like the products described in U.S. Pat. No. 4,042,537; mineral oils; polyether polyols comprising copolymers and block copolymers of ethylene and propylene oxides; and the like.
  • Such polyether polyols can be linear or branched copolymers and block copolymers having molecular weights of, for example, from 1000 or lower to 6000 or higher.
  • the preferred polyether polyols are linear copolymers and block copolymers having molecular weights of from about 2000 to about 3500. They can be utilized in proportions from 1 to as high as 20 parts per 100 parts of the polyol, preferably polyester polyols such as described above. These polyether polyols can also be advantageously used with the silicone fluids described below in various proportions in an effective amount to control the cell size as described herein.
  • Highly preferred cell regulating agents are the polydimethylsiloxanes having viscosities of from about 2 to about 20 centistokes at 25°C.
  • examples of these products include DC 200 fluids (available from Dow Corning Corporation), having viscosities of from about 5 to about 100 centistokes at 25°C., and also Dow Corning Fluid DCF-1-1630, having a viscosity of about 3.5 centistokes at 25°C. (the viscosity being an indicator of the molecular weight of these silicon fluids).
  • DC 200 fluid 5 cs has a molecular weight of 680
  • 10 cs oil corresponds to 1000, 20 cs to 1600, 50 cs to 3200, and 100 cs to 5000 molecular weight.
  • the left and right foot soles are cast as plaques, removed from the cast, and then attached to the shoe uppers by a suitable adhesive.
  • the shoe uppers i.e., left and right foot
  • the molds are closed wall molds so as to obtain the mold defined sole shape.
  • This sole shape may not necessarily be smooth (although it is typically so), but may have build in mold ridges such as for resiliency, cushioning, etc.
  • the typical adhesives also called “cements” for attaching (also called “cementing") the soles to the uppers are well known.
  • the adhesive may be the cast polyurethane minus the blowing agent which is cured with the cast foam as it cures, or it may be a different polyurethane adhesive.
  • the curable formulation is in a prepackaged form with the isocyanate and prepolymer thereof as one package and the polyol, chain extender, and other additives as another.
  • the additives the presently disclosed flow modifiers are included.
  • a further package may contain the catalyst and the cell control agents such as in a three package system.
  • an aspect of the invention includes the "kit” form or "package” form combinations of the components.
  • package (A) or Component (A) containing polyol and flow modifier as a compatible homogeneous liquid, by itself is believed to be novel as is its combination with/without additional ingredients such as glycol chain extender, blowing agent, cell regulating agent, catalyst, etc.
  • one package (A) comprises polyol and flow modifier with/without additional ingredients mentioned above and a second package (B) contains the polyisocyanate, especially as a quasi-prepolymer obtained by reacting all the isocyanate component with a predetermined partial quantity of the polyol component in amounts sufficient to result in quasi-prepolymers having NCO/OH ratios of the order stated previously.
  • the polyether polyurethane products exhibit improved low temperature characteristics, e.g., resistance to cut tear at extremely low temperatures (-30°C).
  • the elongation characteristic is increased, a property which is particularly useful when the polyurethane product is considered for sealant and adhesive applications.
  • a higher coefficient of friction characteristic is obtained in the flow modified systems. This property is highly desirable in, for example, tire tread applications.
  • the flow modifier e.g., polyol, glycol chain extender with/without other ingredients
  • the flow-modified polyester polyurethane products exhibit many of the foregoing advantages. Though improvement in the low temperature property is noticed, this improvement is seen at a relatively higher temperature, e.g., -20 °C.
  • the flow modifiers are, in general, excellent viscosity reducers for polyester polyol
  • the group(s) of the flow modifier is believed to further enhance the solubility and compatibility of polyester polyol systems.
  • This particular property, i.e., viscosity .reducer, is not of particular importance in polyether polyol formulations since commercial polyether polyols are generally low viscosity products.
  • the flow-modified polyester polyol systems are particularly useful in the manufacture of high performance microcellular polyurethane elastomer products, in particular shoe soles.
  • the characteristics and properties of preferred polyester products of the invention are detailed in U.S. Patent No. 4,287,307, issued September 1, 1981, and for sake of completeness are summarized herein-below.
  • the microcellular polyester elastomers have cell diameters in the range of from 0.3 to 0.01 mm, or less, with a minimum density of 160 kg/m 3 (10 lbs/ft. 3 ).
  • a broad density range is from 160 to 900 kg/m 3 , corresponding to a specific gravity of from 0.06 to 0.09 gm/cm 3 ; a preferred range is from 350 to 700 kg/m 3 , corresponding to a specific gravity from 0.35 to 0.7 gm/cm 3 .
  • the foam portion of the microcellular polyester polyurethane elastomer comprises a blown cell structure that has a minimum number of about 30-40 cells/cm to 1,000 cells/cm, or more.
  • a preferred range is from 50 cells/cm to 1,000 cells/cm.
  • the surface skin of integral skin microcellular polyester polyurethane products obtained by the practice of the present invention generally has a thickness of 0.5 to 4 mm, or more, preferably from 1-3 mm.
  • the flex life as measured by the Ross flex test (ASTM D-1052), or the de Mattia flex test (ASTM D-430), has been found to be extremely good, in comparison with microcellular polyurethane elastomers which result from formulations employing water as the blowing agent (such products having no clearly defined integral-skin surface).
  • the flow modifiers of the present invention have the unique capability of imparting to the polyurethane foam the characteristic to pick up substantial quantities of water without leaching the modifier out of the polyurethane foam. This is believed to be partially due to the fact that reactive urethane hydrogen atoms in the flow modifier have the capability to react with a portion of the isocyanate groups of the foam ingredients, rendering the foam surface highly hydrophilic.
  • These foams, both of the polyester and polyether type are particularly interesting as household sponges, sponges for car washing, hydrophilic plant growing medium sponges, and the like.
  • the polyurethane foam can be made by incorporating, in addition to the flow modifier, soaps, detergents, shampoos, fertilizers, plant growth hormones, enzymes, and the like.
  • the flow modifiers of the present invention can be employed to act as convenient solvents for the glycol and/or amine chain extender.
  • Polyurethane elastomers are often prepared at prepolymer:extender ratios of 100:10 or less. Such dissimilar ratios are difficult to meter.
  • the extender is often quite insoluble in the prepolymer.
  • the flow modifier of the present invention oftentimes will greatly facilitate the preparation of a stable extender system that is more readily dispersed (a system oftentimes much lower melting than the pure extender), and yielding additional processing advantages such as the ability to obtain much longer pot-lives due to the lower operating temperature that can be employed.
  • the application of compatible flow modifier-chain extender combination packages represents a further important aspect of the invention.
  • each R' individually is alkyl, desirably C 1 -C 8 -alkyl; a C 5 -C 7 cycloalkyl desirably methyl- or ethyl- substituted C 5 -C 7 cycloalkyl, or aralkyl, desirably phenyl-C 1 -C 3 alkyl; wherein A represents alkylene, desirably C 1 -C 8 alkylene; a C 5 -C 7 -cycloalkylene, desirably cyclohexylene, C 1 -C 2 alkyl- or C 1 -C 2 alkoxy-substituted cyclohexylene; C 1 -C 4 cyclohexylenealkylene such as isopropylcyclohexylenemethylene; unsubstituted, C 1 -C 3 alkyl-, or C 1 -C 3 alkoxy substituted phenylene (preferably tolylene), or di
  • the mol ratio of the oxypropylene moiety to the oxyethylene moiety is in the range of from abubt 75:25 to about 25:90.
  • a further subclass of flow modifiers which is useful in the practice of the invention(s) include the following :
  • R', A, x, and oxyC 2 -C 3 alkylene have the meaning assigned in Formula III above.
  • 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 polyC 2 -C 3 alkylene glycol of the formula
  • 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 3 alkylene represents oxyethylene (preferred) and oxypropylene and when x is 2 or more oxyC 2 -C 3 alkylene can also be oxyethyleneoxypropylene, desirably where the mol ratio of the oxypropylene 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 the R', x , and oxy-C 2 -C 3 alkylene unit having the significance assigned in Formula IV 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.
  • MDI diphenylmethane diisocyanate
  • the isocyanate compound and polyol are reacted in amounts to give a ratio of NCO groups to OH groups of one.
  • Y represents 4, 4'-and/or 2,4'-diphenylenemethane or C 4 -C 6 alkylene; and wherein R', x, and the oxyC 2 -C 3 alkylene unit have the meanings assigned in Formula V above.
  • Hand foams are prepared by weighing all the ingredients of the polyol component (i.e., the polyester polyol, the flow modifier, any extenders, surfactants and catalysts, and the blowing agents as required into a polyethylene lined paper cup. This component is then mixed well. The required amount of isocyanate is then weighed into the polyol component and mixed at high speed for 8 to 10 seconds. The mixture is then cast into a clean cup or a mold as required.
  • the polyol component i.e., the polyester polyol, the flow modifier, any extenders, surfactants and catalysts, and the blowing agents as required into a polyethylene lined paper cup. This component is then mixed well. The required amount of isocyanate is then weighed into the polyol component and mixed at high speed for 8 to 10 seconds. The mixture is then cast into a clean cup or a mold as required.
  • Cream Time The time interval between the final mixing and the point at which the mixture turns creamy or cloudy and starts to expand.
  • Rise Time The time interval between the liquid mixture poured into the container (mold) and the completion of expansion of the foaming mass.
  • Tack Free The time interval between pouring the Time: liquid mixture and the time that the surface of the foam can be touched with a finger without sticking.
  • Snap Time When the reacted polymer can no longer be separated when pinched between two fingers and pulled. Free Blowing The density in lbs./ft.
  • 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' -diphenylmethane 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 15°C. MONDUR E-501 Mobay Chemical Corporation, Isocyanate Polyurethane Division.
  • a carbodiimide modified diphenylmethane diisocyanate terminated polyester prepolymer having an isocyanate content of about 18.9% by weight, an isocyanate equivalent of about 222.5, and a viscosity at 30°C. of about 830 centipoises.
  • 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.
  • a clear yellow liquid isocyanatoterminated polyether prepolymer made by reacting about 85 weight percent 4,4'- diphenylmethane diisocyanate and about 15 weight percent dipropylene glycol and tripropylene glycol. It has an isocyanate content of about 22.6% by weight and an isocyanate equivalent of about 186.
  • POLYESTER A A diethylene glycol-glycerol adipate polyol having a degree of branching of about 2.35, a hydroxyl number of 42.7, an acid number of 0.4, and an equivalent weight of about 1300.
  • POLYESTER B An ethylene glycol-1,4 butanediol glycerol adipate polyol having a functionality of about 2.3, a hydroxyl number of 40.7, a carboxyl number of 0.2, and an equivalent weight of about 1370.
  • SILICONE A A dimethylpolysiloxane silicone fluid having a viscosity of 3.5 centistokes at
  • FREON 11B E.I. duPont deNemours Company. Blowing Agent A stabilized version of trichloromonofluoromethane having a boiling point of 23.8°C.
  • CARBITOL Diethylene glycol monobutyl ether with a molecular weight of 162.
  • CARBITOL Diethylene glycol monomethyl ether with a molecular weight of 120.
  • CARBITOL Diethylene glycol monohexyl ether with a molecular weight of 190.
  • CARBITOL Diethylene glycol monomethyl ether with a molecular weight of 120.
  • CELLOSOLVE Ethylene glycol monophenyl ether with a molecular weight of 138.
  • CARBITOL Diethylene glycol monophenyl ether with a molecular weight of 182.
  • Methoxypolyethyleneoxyglycol found by analysis to have a hydroxyl number of about 76.8 or an equivalent weight of about 730.
  • SILICONE UNION CARBIDE CORPORATION SURFACTANT A non-hydrolyzable polyoxyalkylene L-548 polydimethylsiloxane liquid having an apparent specific gravity of 25/ 25°C of 1.03 and a viscosity 25°C (centistokes) of 1250.
  • NIAX POLYOL UNION CARBIDE CORPORATION 12-56 High primary hydroxyl-containing polyoxyethyleneoxypropylene diol of 2000 molecular weight, having an ethyleneoxy content of about 50% by weight.
  • NIAX POLYOL UNION CARBIDE CORPORATION 11-27 High primary hydroxyl-containing polyoxyethyleneoxypropylene triol/ diol mixture containing about 15% by weight of ethyleneoxy-capped end- blocks, having a hydroxyl number of about 27, and a hydroxyl equivalent weight of about 2000.
  • Room temperature refers to a temperature of 20°C-23°C unless a different temperature is indicated.
  • Percent refers to percent by weight unless indicated otherwise. Parts refers to parts by weight unless indicated otherwise.
  • 80/20 TDI refers to an isomeric mixture of 80 parts of 2,4-tolylene diisocyanate and 20 parts of 2,6-tolylene diisocyanate.
  • MDI refers to a diphenylmethane diisocyanate.
  • 4,4'-MDI refers to 4, 4'-diphenylmethane diisocyanate.
  • Isocyanate Index is the quotient obtained by dividing the equivalents of NCO by the sum of the equivalents of active hydrogen group(s), multiplied by 100.
  • a conventional formulation for the manufacture of integral skin microcellular shoe soles may comprise Isonate 240** (quasi-prepolymer of modified 4,4'-MDI and a copolyester diol) as Component A and, as Component B, a mixture comprising polyester polyol, 1,4-butanediol chain extender, water, etc.
  • the isocyanate index expressed in equation form, is shown below: wherein " ⁇ total equivalent OH" represents the sum of the equivalent(s) of polyol, 1,4-butanediol and water.
  • the isocyanate index is generally a number in the range of from about 90 to about 120 depending on the resulting polyurethane product, e.g., flexible foam, microcellular elastomer, solid elastomer, and the like.
  • the ratio of NCO/OH equivalents is generally in the range of from about 0.9:1.2, desirably from about 0.9:1.1, preferably from about 0.95:1.05, and for many applications generally about 1:1.
  • compatible homogeneous liquid mixture of polyol(s) and flow modifier(s) shall mean that such mixture (of polyol(s) and flow modifier(s) and optionally chain extender, with/without other well-known urethane ingredients which may be included in the polyol resin package such as catalyst, blowing agent, cell regular, etc.) is a stable, homogeneous liquid blend at approximately room temperature, e.g., 20°C-23°C, or if otherwise, the mixture can be made into a stable, homogeneous liquid state at 20°C-40°C by heating to a moderately elevated temperature, e.g., 80 °C to 100 °C for 0.5 to 2 hours, followed by slow cooling to about 20°C-40°C.
  • a moderately elevated temperature e.g. 80 °C to 100 °C for 0.5 to 2 hours, followed by slow cooling to about 20°C-40°C.
  • mixture of polyol(s) and flow modifier (s) shall mean, unless the text indicates otherwise, a compatible homogeneous liquid mixture referred to above as well as mixtures of polyol(s) and flow modifier(s) that are not compatible at the aforesaid lower temperatures but which, under the reaction conditions employed to form polyurethane products, are liquid and convertible by reaction with organic polyisocyanate compounds to such polyurethane products.
  • 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.
  • tolylene diisocyanate 80% 2,4- and 20% 2,6-tolylene diisocyanate
  • OH/NCO ratio OH/NCO ratio
  • Reaction Product A was slightly viscous, clear liquid with a dark yellow color. It was also noted that this product was compatible with Polyester A** (a polyester polyol) at a weight ratio of 80 parts of polyester polyol to 20 parts of the Reaction Product A. The resulting polyester polyol/Reaction Product A mixture had a viscosity of 25,800 centipoises at 23°C. and 13,500 centipoises at 30°C.
  • B Synthesis of Reaction Product B.
  • Reaction Product A was repeated using 34.3 gms of Hexyl Carbitol** (diethylene glycol monohexyl ether with a molecular weight of 190 and a functionality of 1) and 15.7 gms of 80/20 2,4-2,6-tolylene diisocyanate. After 10 minutes the temperature of this reaction was 43°C. The reaction mixture was heated at 70°C. for 3 hours as in the preparation of Reaction Product A to complete the reaction. The resulting product, hereafter referred to as Reaction Product B, was a clear, light yellow, slightly viscous liquid at room temperature. It proved to be compatible with Polyester A** at a weight ratio of 80 parts of Polyester A to 20 parts of Reaction Product B. The viscosity of Polyester A/Reaction Product B mixture was 22,600 centipoises at 23°C., and 11,500 centipoises at 30°C.
  • Hexyl Carbitol** diethylene glycol monohexyl ether with a molecular weight of 190
  • Reaction Product D was prepared using 35.2 gms of butoxy triglycol having a molecular weight of 206 and a functionality of 1 and 14.8 gms of 80/20 2,4- 2,6-tolylene diisocyanate. The temperature of the mixture after the first 10 minutes, without added heat, was 44°C. Following the heating and cooling procedure of A above, the product was observed to be a clear, light yellow, slightly viscous liquid at room temperature. This product (Reaction Product D) was compatible with Polyester A** at a weight ratio of 80 parts Polyester A to 20 parts of Reaction Product D. The resulting polyester polyol Reaction Product D blend had a viscosity of 21,000 centipoises at 23°C., and 13,400 centipoises at 30°C.
  • Reaction Product E was prepared following the same procedure used in (A) above. The temperature observed after 10 minutes, without added heat, was 37°C. The reaction mixture was heated and cooled as described previously. There was obtained a transparent, light yellow, viscous liquid (Reaction Product E) which was compatible with Polyester A** at a weight ratio of 80 parts of Polyester A to 20 parts of Reaction Product E. The viscosity of this blend was 27,400 centipoises at 23°C., and 13,600 centipoises at 30°C.
  • Propasol Solvent B** butoxypropanol
  • TDI 2,4- 2,6-tolylene diisocyanate
  • Butyl Carbitol** was reacted with Isonate 125M** (high purity 4,4'-diphenylmethane diisocyanate).
  • Isonate 125M** high purity 4,4'-diphenylmethane diisocyanate
  • 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 preheated to 94°C.
  • the 4,4'-MDI was added in three increments with good agitation.
  • Reaction Product G Upon cooling to room temperature the product (Reaction Product G) of this 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. Reaction Product G was also examined for compatibility with Polyester A. In view of the hazy, semicrystalline nature of this product at room temperature, an 80/20 Polyester A/Reaction Product G mixture was heated to 95°C., agitated, and then allowed to cool to room temperature. The result was a clear, compatible mixture with a viscosity of 30,750 centipoises at 23°C., and 13,530 centipoises at 30°C.
  • Reaction Product H was prepared by reacting Butyl Carbitol** and Mondur MR** (a crude polymethylene polyphenyl 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 polyisocyanate added in three increments.
  • reaction Product H 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.
  • reaction Product I This product (Reaction Product I) was blended with Niax Diol 12-56** at a ratio of 75/25 Niax Diol 12-56 to Reaction Product I, heated to 50°C., whereupon there was formed a homogeneous mixture. Upon cooling to room temperature, the mixture remained compatible.
  • Reaction Product K was prepared by reacting the ethylene oxide adduct of nonylphenol, having a hydroxyl value of 51, and a hydroxyl equivalent weight of 1100, corresponding to an addition product of about 20 ethyleneoxy units per phenolic hydroxyl group, with the 80/20 mixture of 2,4- and 2,6-tolylene diisocyanate in an equivalent ratio of NCO/OH equal to one.
  • a one liter reaction flask was charged with 700 gms of the phenolethylene oxide reaction product (corresponding to 0.636 equivalent of OH), the waxy material was heated to 50°C., and agitated under a stream of nitrogen.
  • Hand foam experiments comprising the manufacture of microcellular polyurethane foams from a diethylene glycol adipate polyester polyol (Polyester A), ethylene glycol extender, and an isocyanate prepolymer (Mondur E-501* or Isonate 240**) were conducted to test the suitability of using the Reaction Products A through H of Example 1 in polyurethane foams.
  • Control foams were also made without flow modifier (blank) or with TP-90B** (di [2-(2-butoxyethoxy) ethoxy] methane). The resulting foams had open cells with good cell structure. These foams were prepared using a hand-mixe process at room temperature.
  • Shoe sole parts were also prepared using the same hand-mix process and casting the foam mixture into an epoxy mold held at a temperature of 30°C.-35°C. Excellent polyurethane parts were produced with the exception of Reaction Products G and H which produced shoe sole parts exhibiting slight shrinkage at the 90/10 polyester polyol/Reaction Product level. All other shoe sole parts did not shrink at the density tested.
  • Reaction Products G and H were prepared using a 4,4'-diphenylmethane diisocyanate as a reactant. The formulations might have to be optimized with regard to the catalyst and surfactant type to avoid all shrinkage, as had been the case with the other flow modifiers tested (Reaction Products A, B, C, D, E, F).
  • Reaction Product J is a larger batch of Reaction Product A supra and was prepared for evaluation as follows.
  • the internal temperature of the reactor was raised as necessary by heating the outside of the flask with a heating mantlecontrolled by a rheostat.
  • To this flask 2593 gms of Butyl Carbitol** were charged with moderate heat being applied.
  • Reaction Product J The product of this reaction, hereafter referred to as Reaction Product J, was a dark yellow transparent liquid with a viscosity of 7,600 centipoises at 23°C. This product was tested for compatibility with Polyester A** polyester polyol and Polyester B** polyester polyol with/without Niax Polyol 12-56**, a high primary hydroxyl-containing polyoxyethyleneoxypropylene diol of 2000 molecular weight, and fluorocarbon blowing agents FREON 11B** and FREON 113**. The results of this study are described in Table II.
  • Reaction Product L was prepared using Ucon Lubricant 50HB660** and 80/20 2,4- 2,6-tolylene diisocyanate (TDI). To the 5 liter reaction flask described in Example 2 supra and maintained under a nitrogen atmosphere, there were charged 4000 gms of Ucon Lubricant 50HB660. Beginning at room temperature, 174.3 gms of the TDI were added under stirring. Moderate heat was applied and the temperature of the mixture rose to 85°C over a period of two hours. The temperature of the reaction product mixture was maintained between 85°C and 90°C under continuous stirring for five hours. Upon cooling to room temperature there was obtained a yellow transparent liquid (Reaction Product L) with a viscosity of 536 centipoises at 25°C.
  • TDI 2,4- 2,6-tolylene diisocyanate
  • Reaction Product L was also examined for compatibility with polyester polyols (Polyester A** and Polyester B**), with/without polyether polyol (Niax Polyol 12-56**), and the fluorocarbon blowing agents (Freon 11B** and Freon 113**). The results of this study are described in the Table III infra.
  • Reaction Product M was prepared using Ucon Lubricant LB285** and Isonate 125** (4,4'-MDI). To a 500 ml. reaction flask equipped as described in Example 2 and maintained under a nitrogen atmosphere, there were charged 222.5 gms of Ucon Lubricant LB285 and heated to 70°C. Under continuous stirring 56.8 gms of the 4, 4' -MDI were added and the temperature of the resulting reaction mixture rose to 90 °C within 10 minutes. The temperature was maintained between about 90°-95°C for four hours. There was obtained a white hazy liquid with a viscosity of 2,530 centipoises at 23°C.
  • Reaction Product J-2 In a manner similar to Example 2 supra in the preparation of Reaction Product J, there were charged 2593 gms of Butyl Carbitol** to the flask and heated to 68°C. The 80/20 TDI was added to the flask in three increments and the exotherm recorded. The total amount of 80/20 TDI added was 1393.1 gms. There was obtained a light amber liquid product with a viscosity of 6120 centipoises at 23°C (hereinafter Reaction Product J-2).
  • Foam formulations were prepared and foamed on a Martin Sweets two-component foam machine (Model MOD.MOD 3A, The Martin Sweets Co., Louisville, KY.).
  • One component comprised Polyester A**, Reaction Product J-2, ethylene glycol extender, surfactants (L 5340** and Silicone A**), catalysts (Dabco 33LV** and Syncat M601**), and water.
  • the second component comprised Mondur E-501**.
  • test specimens were maintained under ambient conditions for at least one week prior to conducting the tests.
  • polyester A/20 Reaction Product J-2 flow modifier the flex properties of the molded polyurethane specimen were clearly superior to the control while retaining acceptable tensile and tear properties.
  • the data and results are shown in Table V infra.
  • Reaction Product J (Example 2), Reaction Product J-2 (Example 6), and Reaction Product J-3 (Example 7) involved the addition reaction of a weight ratio of 13 parts of Butyl Carbitol to 7 parts of 80/20 TDI, there were employed 13 parts of Butyl Carbitol and 20 parts of Reaction Product J-3 in the following experiments documented in Table VI and VII infra.
  • Reaction Product K (Example 3) involved the addition reaction of a weight ratio of 19.2 parts of Ucon Lubricant 50HB660 and 0.8 part of 80/20 TDI, there were employed 19.2 parts of Ucon Lubricant 50HB660.
  • Reaction Product J-3 In a manner similar to Example 5 supra in the preparation of Reaction Product J-2, there were charged 6500 gms of Butyl Carbitol to a 12 liter flask and heated to 68°C. The 80/20 TDI was added to the flask in three increments and the exotherm recorded. The total amount of 80/20 TDI added was 3500 gms. There was obtained a clear, slightly viscous, medium amber liquid product with a viscosity of 7010 centipoises at 21°C and 2537 centipoises at 35°C (hereinafter Reaction Product J-3).
  • EXAMPLE 8 A series of foam formulations comprising Reaction Product J-3, Ucon Lubricant 50HB660**, or TP-90B** were prepared and run on a Desma two component foam machine (Desma Maschinene GMbH, 2807, Achim bei GmbH, Germany).
  • Component A of the formulations comprised Polyester A** with/without Reaction Product J-3, Ucon Lubricant 50HB660 or TP-90B plus ethylene glycol extender, surfactants, catalysts, and fluorocarbon blowing agent;
  • Component B consisted of the polyisocyanate (Mondur E-501**).
  • Component A was maintained at 30°C and Component B at 32°C in pressurized tanks under constant agitation to prevent phase separation.
  • the foam mix was cast into aluminum mold cavities 6 inches x 8 inches x 0.5 inch thick which was held at a temperature of 46°C. Test plaques of varied densities were prepared. The data and results are shown in Table VIII infra.
  • 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 -10oC, 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.
  • reaction product mixture was degassed quickly and cast into a warm 1/4" aluminum mold cavity having a dimension of 6" x 8".
  • the reaction product gelled in 5-6 minutes.
  • a strong, tough polyurethane elastomer exhibiting a Shore A hardness of 55-60, and was found to possess an electrical resistance that was appreciably lower than the product made from the same formulation but not containing Reaction Product I. This property of electrical resistance imparts utility in elastomeric applications requiring antistatic properties.
  • a flexible polyether/polyurethane foam was prepared from Niax Polyol 11-27**, Reaction Product K, and the 80/20 mixture of 2,4- and 2,6-tolylene diisocyanate. The following foam recipe was employed
  • the ingredients were mixed at about 1500 rpm by means of a laboratory mixer, poured into a paper mold, allowed to rise and cure at room temperature for about 30 minutes. The resulting foamed product was dry to the touch.
  • the foam was cut into one inch thick slabs.
  • the foam exhibited good strength characteristics and was found to exhibit a substantially lower electrical resistivity than the foamed product made from the corresponding fomulation without flow modifier. This property highlights the utility of the foamed product as an antistatic carpet underlayment in computer rooms and the like.

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  • Chemical & Material Sciences (AREA)
  • Health & Medical Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Organic Chemistry (AREA)
  • Polyurethanes Or Polyureas (AREA)

Abstract

La présente invention prévoit un grand choix de produits de polyuréthane, par exemple des produits cellulaires, élastomères denses et microcellulaires à pellicule intégrale, obtenus par la réaction (A) d'un composé de polyisocyanate, (B) d'un polyol, (C) facultativement d'un extendeur de chaîne et/ou d'un agent soufflant avec/sans autres additifs connus, (D) en présence d'un modificateur d'écoulement non hydroxyle caractérisé par des atomes de carbone et d'hydrogène, au moins un et généralement, plusieurs groupes oxyalcènes et au moins un groupe uréthane, $(1,5)$. Plusieurs produits de polyuréthane présentent des propriétés uniques, par exemple des articles en mousse conducteurs d'électricité statique, des élastomères souples caractérisés par une amélioration du coefficient de friction, etc. Plusieurs classes de modificateurs d'écoulement sont nouvelles per se. Les produits de polyuréthane peuvent être synthétisés par le procédé à étape unique ou le procédé prépolymère. Des systèmes multiples (en particulier des systèmes à deux et trois composants sont utiles pour des opérations de moulage, par exemple la fabrication de semelles de chaussures.
EP19840902667 1984-02-15 1984-06-27 Synthese de produits de polyurethane Withdrawn EP0171394A1 (fr)

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US508434 1984-02-15

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WO2019224235A1 (fr) * 2018-05-22 2019-11-28 Basf Polyurethanes Gmbh Élastomère de polyuréthane

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DE1720705B2 (de) * 1967-08-26 1977-03-31 Hoechst Ag, 6000 Frankfurt Konzentrat von biociden thiophosphorsaeureestern
JPS5235399B2 (fr) * 1973-07-31 1977-09-08
US4189544A (en) * 1979-02-21 1980-02-19 The Upjohn Company Polyisocyanurate polymers prepared using carbamate modifier
US4334032A (en) * 1979-09-21 1982-06-08 Basf Wyandotte Corporation Foamed polymers containing low molecular weight urethane modifier compound
EP0027498B1 (fr) * 1979-09-21 1985-03-27 Basf Wyandotte Corporation Composition de polyuréthane rigide non-cellulaire modifiée avec le produit de réaction d'un isocyanate et d'un alcool et procédé pour sa préparation
US4288577A (en) * 1979-12-14 1981-09-08 E. I. Du Pont De Nemours And Company Novel urethanediols and polyurethanes therefrom

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AU3102884A (en) 1985-09-10

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