WO1990009404A1

WO1990009404A1 - Bulk polyurethane ionomers

Info

Publication number: WO1990009404A1
Application number: PCT/US1990/000701
Authority: WO
Inventors: Sven H. Ruetman; Joginder N. Anand
Original assignee: The Dow Chemical Company
Priority date: 1989-02-08
Filing date: 1990-02-07
Publication date: 1990-08-23
Also published as: DE69014609T2; EP0457844B1; ES2064719T3; CA2009456A1; JPH04503226A; US4956438A; DE69014609D1; EP0457844A1; EP0457844A4; KR920701291A

Abstract

The invention relates to bulk polyurethane ionomers prepared by the reaction (A) an isocyanate terminated ionic prepolymer with (B) a hydrocarbon polyol chain extender, said prepolymer having been prepared from (i) an excess of diisocyanate, (ii) a mixture comprising a diol and an organic polyol having three or more reactive hydroxyl moieties each having a molecular weight of from 250 to 6,000 and (iii) a difunctional isocyanate-reactive component containing an ionic group or potential ionic group. The polyurethane can be molded into desired shapes such as films and sheets. The films are useful in many fields such as chip-resistant coatings in automotive applications.

Description

BULK POLYURETHANE IONOMERS

This invention relates to a bulk polymerized ionic polyurethane and is more particularly concerned with improved bulk polymerized ionic polyurethanes whose soft segment polyol component comprise high levels of triols along with the conventional diols.

Bulk polymerized polyurethanes are prepared in the absence of solvents. Such polyurethanes may be polymerized by a oneshot process wherein all of the ingredients are contacted under polymerization conditions. Alternatively, such polyurethanes may be prepared by a prepolymer process, wherein the polyol and isocyanate components are reacted such that an excess of isocyanate groups are present. Thereafter the prepolymer is reacted with a chain extender to form the polymer. The bulk polyurethanes may be polymerized into a final shape or processed into another form after polymerization. The bulk polyurethanes are useful in preparing shaped articles, films and in laminates. Bulk polyurethanes do not exhibit the toughness which is required for some uses. Further, bulk polyurethanes do not demonstrate the adhesion properties desired for certain laminate applications.

What is needed is a bulk polyurethane with improved toughness and adhesion properties.

The present invention relates to bulk polyurethane ionomers prepared by the reaction of (A) an isocyanate terminated ionic prepolymer with (B) a hydrocarbon polyol chain extender, said prepolymer having been prepared from (i) an excess of diisocyanate, (ii) a mixture comprising a diol and an organic polyol having three or more reactive hydroxyl moieties each having a molecular weight of from 250 to 6,000 and (iii) a difunctional isocyanate-reactive component containing an ionic group or potential ionic group.

The bulk polyurethanes of this invention demonstrate improved toughness and tensile properties and improved adhesion properties.

The term "hydrocarbon" as used herein with respect to the polyol chain extender component means a hydrocarbon residue having from 2 to 20 carbon atoms remaining after the replacement of the appropriate number of hydrogen atoms by primary or secondary hydroxy groups; inclusive of said hydrocarbon residue are aliphatic groups of C₂ to C-_|g, cycloaliphatic groups of C5 to C*_|β, aromatic groups of C5 to C₂o» and the like.

The term "aromatic diisocyanate" means an organic isocyanate containing one or two aromatically bound isocyanate groups wherein the aromatic divalent residue is an arylene or alkoxylene moiety having from 6 to 20 carbon atoms, inclusive, such as phenylene, benzylene and napthylene.

The term "aliphatic diisocyanate" means an organic isocyanate containing two aliphatically bound isocyanate groups wherein the aliphatic divalent residue is an alkylene radical having from 6 to 12 carbon atoms, inclusive, such as hexamethylene, heptamethylene, octamethylene, nonamethylene, decamethylene, undecamethylene, dodecamethylene, and isomeric forms thereof.

The term "cycloaliphatic diisocyanate" means an organic diisocyanate containing two cyfloaliphatically bound isocyanate groups wherein the cycloaliphatic divalent residue contains one or two cycloalkylene radicals each cycloalkylene having from 5 to 8 carbon atoms, inclusive, such as cyclopentylene-1,3_>

4-methylcyclopentylene-1,3» cyclohexylene-1,3_> » cyclohexylene-1,4, 2-methylcyclohexylene-1,4, 2,5-dimethylcyclohexylene-1,4, cycloheptylene-1 ,3, cycloheptylene-1 ,4, 6-methylcycloheptylene-1,4, cyclooctylene-1 ,3_> cyclooctylene-1,4, cyclooctylene-1 ,5, and the like; 4,4'-methylenebis(cyclohexylene), 4,4'-isopropylidenebis(cyclohexylene) and 4,4'-dicyclohexylene.

The term "difunctional isocyanate-reactive component" means any organic compound carrying two separate groups each capable of reacting with an isocyanate group because of active hydrogens according to the Zerewitinoff test, such as -OH, -NH₂, -SH and -C00H.

The term "ionic group or potential ionic group" means a group either already in an anionic or cationic form or else, by neutralization with a reagent, readily converted to said anionic or cationic form respectively. Illustrative of such potential anionic groups (and neutralized form) are -C00H(-C00^θ), -S0₂0H(-S0₂0^θ) , and =P00H(=P00^θ); illustrative of such potential cationic groups (and neutralized form) are ≡N(≡N-^Θ), ≡p(==p-^θ), and =S(=S-^Θ).

The permanent set properties of the films prepared from the bulk polyurethanes remain relatively constant in spite of the increase in Shore A hardness and modulus properties.

The preparation of the bulk polyurethanes of this invention is carried out using any of the conventional methods and ingredients known to those skilled in the art except for the novel use of the triol and the difunctional isocyanate-reactive component containing an ionic group or potential ionic groups which will be discussed in detail below. Typical preparative methods are disclosed in the U.S. Patent 4,621,113. Generally speaking, the bulk polyurethanes are preferably prepared by a two-stage process wherein an isocyanate-terminated prepolymer (A) is made in the first stage followed by chain-extending or finalizing the polymer formation in the second stage with a hydrocarbon polyol (B) defined above. The ionic portions of the bulk polyurethanes are preferably -5-

incorporated as part of the first stage prepolymer and will be discussed in detail below.

The diisocyanates (i) which can be employed for the isocyanate terminated prepolymer (A) preparation are defined above. Illustrative but non-limiting of the diisocyanates are 1 ,6-hexamethylene diisocyanate, 1 ,7-heptamethylene diisocyanate, 1 ,8-octamethylene diisocyanate, 1 ,9-nonamethylene diisocyanate, 1,10-decamethylene diisocyanate, 1, 11-undecamethylene diisocyanate, 1, 12-dodecamethylene diisocyanate, 2,2,4-trimethylhexamethylene diisocyanate, 2,4,4-trimethylhexamethylene diisocyanate, and the (3-isocyanatopropoxy)-(3-isocyanatopropyl)arylehes such as 1-(3-isocyanatopropoxy)-4-(3-isocyanatoprop^l)benzene described in U.S. Patent 4,051,166, 1,4-bis(2- -isocyanatoethyDcyclohexane, and the like; isophorone diisocyanate otherwise identified as 1-isocyanato-3- -isocyanatomethyl-3_>5,5-trimethylcyclohexane; and cycloaliphatic diisocyanates such as methylenebis- (cyclohexyl isocyanate) including the 4,4'-isomer, the 2,4'-isomer, and mixtures thereof, and all the geometric isomers thereof including trans/trans, cis/trans, cis/cis and mixtures thereof, (1,2-; 1,3-; or 1,4-) cyclohexylene diisocyanates, 1-methyl-2,5-cyclohexylehe diisocyanate, 1-methyl-2,4-cyclohexylene diisocyanate,*'^* 1-methyl-2,6-cyclohexylene diisocyanate, 4,4'-isopropylidenebis(cyclohexyl isocyanate), 4,4'-diisocyanatodicyclohexyl, 1,4-diisocyanatocyclo- heptylene and 1,4-diisocyanatocyclooctylene. Aromatic diisocyanates include 2,4- and 2,6-tolylene diisocyanate and mixtures of these isomers, 1,3- and/or 1 ,4-phenylene diisocyanate, 2,4'- and/or -4,4'-diphenyl methane diisocyanate, 1,3- and 1 ,4-phenylene diisocyanate, 2,4- and 2,6-tolylene diisocyanate and mixtures of these isomers, diphenyl methane-2,4'- and/or -4,4'-diisocyanate, and naphthylene-1,5-diisocyanate.

Preferred as a group are the aliphatic and cycloalphatic diisocyanates. More preferred as a group are the cycloaliphatic diisocyanates and preferred within this group are the methylenebis(cyclohexyl isocyanates) with the 4,4'-isomer being particularly preferred.

The organic diols (ii) can be any of the high molecular weight diols having a molecular weight of from 250 to 6,000 as described in U.S. Patent 4,621,113. Preferably, the molecular weight falls in the range of from 500 to 6,000, more preferably, from 1,000 to 3,000. The term "molecular weight" as used herein means the number average molecular weight as determined by end-group analysis or other colligative property measurement.

Exemplary of the diols which can be employed are: polyether diols, polyester diols, hydroxy- -terminated polycarbonates, hydroxy-terminated poly- butadienes, hydroxy-terminated polybutadiene- -acrylonitrile copolymers, hydroxy-terminated copolymers of dialkyl siloxane and alkylene oxides such as ethylene oxide and propylene oxide, and mixtures in which any of the above polyols are employed as major component (greater than 50 weight percent) with difunctional amine-terminated polyethers and amino-terminated polybutadiene-acrylonitrile copolymers. Illustrative of polyether diols are polyoxy- ethylene glycols, polyoxypropylene glycols, polyσxy- butylene glycols which, optionally, have been capped with ethylene oxide residues, random and block ; copolymers of ethylene oxide, propylene oxide, and butylene oxide, random and block copolymers of tetra- hydrofuran and ethylene oxide and or propylene oxide. Illustrative of polyether diols further include products derived from any of the above by reaction with difunctional carboxylic acids or esters derived from said acids in which latter case ester interchange occurs and the esterifying radicals are replaced by polyether polyol radicals. The preferred polyether polyols are random and block copolymers of ethylene and propylene oxide of functionality approximately 2.0 and polytetramethylene glycol polymers.

Illustrative of polyester diols are those prepared by polymerizing ε-caprolactone using an initiator such as ethylene glycol and ethanolamine a ά those prepared by esterification of polycarboxylic acids such as phthalic, terephthalic, succinfc, glutaric, adipic, azelaic and the like acids with dihydric alcohols such as ethylene glycol, butanediol and cyclohexanedimethanol.

Illustrative of the amine-terminated polyethers are the aliphatic primary diamines structurally derived from polyoxypropylene glycols. Polyether diamines of this type are available from Texaco under the trademark

JEFFAMINE. *^• v.

Illustrative of polycarbonates containing hydroxyl groups are those prepared by reaction of diols such as propane-1,3-diol, butane-1,4-diol, hexane-1,6 -diol, 1,9-πonanediol, 2-methyloctane-1,8-diol, diethylene glycol, triethylene glycol and dipropylene glycol with diarylcarbonates such as diphenylcarbonate or with phosgene.

Illustrative of the silicon-containing poly- ethers are the copolymers of alkylene oxides with dialkylsiloxanes such as dimethylsiloxane. This type of polyesters are described in, for example, U.S. Patent No. 4,057,595.

Illustrative of the dihydroxy-terminated polybutadiene copolymers are the compounds available under the tradename Poly BD Liquid Resins from Arco Chemical Company. Illustrative of the dihydroxy- and diamine-terminated butadiene/acrylonitrile copolymers are the materials available under the trade name HYCAR hydroxyl-terminated (HT) Liquid Polymers and amine-terminated (AT) Liquid Polymers, respectively.

The most preferred diols comprise random and block polyether diols and polytetramethylene glycols set forth above otherwise referred to as polyalkyleneoxy diols. Polyethyleneoxy-capped polypropyleneoxy diols are most specifically preferred.

Preferably the molar ratios of the diol and polyol (1) to the diisocyanate (X+Y) to the component containing an ionic or potential ionic group (Z) to the chain extender (X-1-Z) is represented by the formula 1/X+Y/Z/X-1-Z wherein -9-

X is between 2.0 and 9.0; Z is between 0.25 and 7.0; Y is between 0 and 0.10;

with the proviso that X+Z>1+Y+(X-1-Z). X is the molar ratio of diisocyanate equal to the molar ratios of the isocyanate reactive components. Y is the excess diisocyanate over that amount which is equal to the molar ratios of isocyanate reactive components. Preferably there is an excess of diisocyanate of 3 to 5 percent, that is Y is 0.03. to 0.05.

One of the essential features of the present invention resides in the replacement of a portion of &he t above diol component with an organic polyol having three or more reactive hydroxyl moieties (polyfunctional polyol) having a molecular weight of from 250 to 6,000_. preferably from 500 to 3,000, and most preferably from

500 to 2,000. Accordingly, the component (ii) fo«r preparing said isocyanate terminated ionic prepolymer comprises a mixture of at least one diol with at least one polyol with more than three or more reactive^ hydroxyl groups. The proportions in which the triol is to be employed will vary somewhat according to its molecular weight. Branching and eventual cross-linking of the final polymer will be controlled largely by the molecular weight factor. As molecular weight of the polyfunctional polyol decreases, then branching in the prepolymer leading to possible cross-linking therein, and, most assuredly, in the final polyurethane will occur. Accordingly, the ultimate film properties desired will dictate polyfunctional polyol molecular weight and the proportions in which to use it.

Advantageously, the polyfunctional polyol can be present in the mixture in up to 50 hydroxyl equivalent percent. That is to say, of the total hydroxyl equivalents employed in the prepolymer preparation, up to 50 percent can be contributed by the polyfunctional polyol component. Above the 50 percent level the thermoplastic nature of the bulk polyurethanes may be lost. Preferably, the polyol mixture (ii) comprises from 5 to 50 equivalent percent of said polyfunctional polyol and from 95 to 50 percent of said diol. More preferably, the polyfunctional polyol falls in a range of from 10 to 40 percent with diol being 90 to 60 percent.

The polyfunctional polyol can be any of the organic polyols known in the urethane art to be polyhydric in functionality, i.e., have three or more reactive hydroxyl moieties and which fall into the molecular weight ranges set forth above. The polyfunctional polyols can be identically obtained to those diols described above except for the use of initiators and starting materials leading to functionality of three or more. Examples of such initiators include glycerol, trimethylol propane, 1,2,6-hexane triol, 1,2,4-butane triol, trimethylol ethane, pentaerythritol, mannitol, sorbitol, and methyl glycoside. Preferred polyfunctional polyols are the triols. Polyether triols are readily available or easily prepared in the form of polyoxyethylene triols, polyoxypropylene triols, polyoxybutylene triols or random or block copolymers thereof. The polyoxypropylene triols and the polyoxybutylene triols can optionally be capped with ethyleneoxy residues. All of these polyether triols are generically identified as polyalkyleneoxy triols and are prepared by the reaction of the corresponding ethylene, propylene, butylene oxides with trifunctional initiators such as glycerine and trimethylolpropane. Optionally, the triols can be prepared from tetrahydrofuran and a trifunctional starter to yield the corresponding polytetramethyleneoxy triols. Polyester triols while more difficult to synthesize with the overall trifunctionality than the polyalkyleneoxy triols above, are nevertheless still useful as triol components. Typical trifunctional polyester triols are those prepared from ε-caprolactone with an initiator such as glycerine and trimethylolpropane. Further illustrative examples of triols include polycarbonate triols prepared by reaction of triols such as trimethylolpropane or glycerine with diphenylcarbonate or phosgene; and mixtures of any of the above triols as the major component (greater than 50 weight percent) with trifunctional amine-termiriated polyethers. ^θ

A preferred class of triols comprises the polyalkyleneoxy triols, particularly those having a molecular weight of from 500 to 3,000. E en morfe preferred are the polyethyleneoxy-capped polypropyleneoxy triols having a molecular weigh£ frorή" 500 to 2,000. r

Known difunctional chain extenders may be used in this invention. Examples of the chain extenders^'are aliphatic C to C-_| diols such as ethylene glyeof, 1 ,4-butanediol, 1,3-propane diol, 1,5-pentane dioY and 1,6-hexanediol.

The difunctional isocyanate-reactive components (iii) contain an ionic group or potential ionic group as defined above and include any of those compounds disclosed in U.S. Patent 4,408,008, particularly column 6, line 63 through column 7, line 57. In U.S. Patent 3,479,310; 3,419,533; 3,412,054; and 4,108,814, the difunctional isocyanate-reactive ionic or potential ionic compounds are also disclosed.

As noted and defined above, the ionic defini-' tion includes both anionic and cationic character. Additionally, the term "neutralize" as used herein for

10 converting potential ionic to ionic groups refers not only to neutralization using true acids and bases but also includes quaternarization, and ternarization. The potential anionic groups typically include carboxylic acid groups, sulfonic acid groups, and phosphoric acid

15 groups. When incorporated into the difunctional isocyanate-reactive component (iii) these anionic groups can be neutralized before, during, or after the prepolymer formation to form the corresponding carboxylate anion, sulfonate anion, and phosphate anion.

20 The neutralization can be carried out by treatment with such inorganic or organic bases as sodium hydroxide, potassium hydroxide, potassium carbonate, ammonia, tertiary amines such as triethylamine, tripropylamine, _pj- tributylamine and triethylene diamine. In respect of the potential cationic groups, these typically include tertiary amine, phosphine, and sulfide groups. When incorporated into the difunctional isocyanate-reactive component (iii), these cationic groups can be

30 quaternated or ternated by neutralization or quaternarization of the tertiary amine, or reacting the phosphine or sulfide with compounds capable of alkylating the phosphine or sulfide groups. Sometimes it is more convenient to have the precursor phosphine or sulfide groups as a separate reagent with the actual quaternizing or ternarizing moiety in the difunctional component (iii).

The isocyanate-reactive groups themselves as defined above are those having active hydrogen atoms and include hydroxyl, amino, thiol, and carboxylic acid. Preferred of the functional groups are the dihydroxy and diamino compounds with dihydroxy functionality most preferred.

10

Illustrative but non-limiting of the compounds containing a potential anionic (ionic) group are tartaric acid (mono-, or di-sodium salt), 2,6-dihydroxy - benzoic acid (sodium salt, potassium salt, triethyl-

15 ammonium salt), 2,8-dihydroxynaphthoic acid-3 (sodium salt, potassium salt, triethylammonium salt), 3,4-diaminobenzoic acid (sodium salt, potassium salt, triethylammonium salt), 1 ,7-dihydroxynaphthalenesulfonic acid-3 (sodium salt, potassium salt, triethylammohium

20 salt), 1 ,8-dihydroxynaphthalenedisulfonic acid-2,4 (sodium salt, potassium salt, triethylammonium salt), 2,4-diaminotoluenesulfonic acid-5 (sodium salt, potassium salt, triethylammonium salt), the sulfonate _pj- diols described in U.S. Patent 4,108,814 (incorporated herein by reference), bis(β-hydroxyethyl)phosphinic acid (sodium salt, potassium salt, triethylammonium salt), and the like; illustrative of the compounds containiag a potential cationic (ionic) group are methyldiethanoj-

30 amine (hydrochloride salt, acetic acid salt), N,N-di(2- -hydroxypropyDaniline (hydrochloride salt, acetic acid salt) , N-cyclohexyl-N-(3-aminopropyl)propanol-2-amine (hydrochloride salt, acetic acid salt), ethyldiethanol- amine (hydrochloride salt, acetic acid salt), glycerol- -α-bromohydrin quaternated with tributylamine (ammonium salt), or triethyl phosphine (phosphonium salt), and glycerol-α-bromohydrin ternated with dimethyl sulfide (sulfonium salt).

Preferred for the component (iii) is a class of dihydroxy alkanoic acids described in U.S. Patent 3,412,054. When they are neutralized with any of the inorganic or organic bases they result in the preferred anionic moieties. Accordingly, the preferred component (iii) is a carboxylic acid containing diol which can be neutralized with an inorganic or organic base to form said ionic group before, during or after said prepolymer formation. The most preferred dihydroxy alkanoic acids are the α,α-dimethylol alkanoic acids having the formula QC(CH₂0H)₂C00H wherein Q is hydrogen or C - to Cg alkyl, preferably C-_j to C__j alkyl. Preferred as the neutralizing agents are the aliphatic C₂ to C__j tertiary amines inclusive of triethylamine, tripropylamine, tributylamine, triisopropylamine and triethylene diamine and aqueous or anhydrous ammonia.

The proportions in which component (iii) is to be employed are not particularly critical except to the extent that it be sufficient to result in enhanced adhesive properties of the prepolymer and final polyurethane. Advantageously, the component is employed within a range of proportions such that the milliequivalents of ionic groups per 100 grams of prepolymer (A) falls within a range of from 2 to 150, preferably 10 to 150, more preferably 10 to 100, more preferably 20 to 125, most preferably 15 to 80. The equivalent weight of the ionic component is the precursor molecular weight divided by the number of ionic groups. Accordingly, the proportion of (iii) employed divided by its equivalent weight and multiplied by 1,000 provides the ultimate milliequivalents of potential and/or ionic groups present in the total prepolymer weight.

The isocyanate terminated prepolymer (A) as noted above is readily prepared using the conventional procedures known to a person skilled in the art. The polyurethanes of this invention are prepared in the

10 absence of a solvent or diluent. The excess diisocyanate (i) along with the polyol mixture (ii) and the difunctional isocyanate-reactive component (iii) ,are brought together in any convenient manner, preferably v under the exclusion of moisture. This is, best achieved 15 by reacting the components under an inert gas such as nitrogen or argon. It is also preferred to react the components in the absence of water. In a preferred embodiment the isocyanate reactive components of (ii) and (iii) are first thoroughly blended together followed

20 by the excess diisocyanate.

The exact proportion of excess of isocyanate is chosen so that the final polymer properties desired will _pr- be obtained. Advantageously, the proportions of components (i), (ii) which includes both diol and - polyfunctional polyol, and component (iii) are such that the ratio of isocyanate equivalents to total isocyanate- -reactive equivalents in said prepolymer (A) preferably

30 falls in a range of from 1.1 to 3, more preferably . om 1.5 to 3, most preferably from 1.2 to 2.

*"}J ^*

The reaction temperature during prepolymer formation is normally maintained below 150°C. Generally speaking, the reactants will be heated to a temperature 90/09404

- 16-

within the range of 30°C to 125°C, preferably 50°C to 100°C. In some cases, reaction exotherm will provide heat thereby contributing to these temperature ranges.

Catalysts for the reaction of the polyether and chain extender with the polyisocyanate are advantageously used. Conventional urethane forming catalysts are preferred. Preferred catalysts include organometallic catalysts, especially organotin

10 catalysts, and tertiary amine compounds. The preferred organotin catalysts include, for example, stannous octoate, dimethyltindilaurate and dibutyltindilaurate. Preferable tertiary amine catalysts include triethylenediamine. Zero decimal zero zero one (0.001) 15 to 0.5 part of the organometallic catalyst is advantageously used per 100 parts of reactive components. Tertiary amine catalysts are suitably employed in an amount from 0.01 to 2 parts per 100 parts of reactive components. Of course, other catalysts

20 useful in catalyzing polyurethane reactions are also useful herein.

The reaction time for the formation of the -_- prepolymer may be any time sufficient to form the prepolymer. Preferably the reaction time is between 0.5 and 5 hours, with between 1 and 3 hours more preferred.

Completion of the bulk polyurethane formation, 30 otherwise known as chain extension is readily accomplished by mixing the prepolymer (A) with the chain extender (B) neat. Efficient intermixing of the components is highly desirable. -17-

Preferably the prepolymer and chain extender are reacted with mixing at ambient or elevated temperatures until a homogeneous continuous mass is formed. This reaction is exothermic. Heating speeds up this reaction. Temperatures from 15°C to 55°C are preferred for this step. After a homogeneous continuous mass is formed, the reaction mixture is exposed to ♦ elevated temperatures to complete the polymerization. The temperatures used for completion of the

10 polymerization are those temperatures at which polymerization goes to completion at a reasonable rate. The upper limit is that temperature at which the polyurethane undergoes degradation. Preferable temperatures are between 55°C and 220°C with between 6^'0°C 15 and 150°C being preferred, and between 8θ°C and 1^r10°C being more preferred. The polymerization completion step is continued for sufficient time to complete the polymerization. The time is dependent on the ^: temperature used, the catalyst amount, and final

20 properties desired. Preferable times are between 30 seconds and 16 hours.

The proportion of extender (B) employed is _pj- governed by the isocyanate content of the prepolymer component. Generally speaking, the proportions of (B) are such that the ratio of isocyanate equivalents in (A) to extender equivalents in (B) falls in a range of from 1.25 to 0.90, and preferably from 1.10 to 0.95.

30

It is preferable to perform the chain extension under an inert or a dry atmosphere, as the presence of water during this stage may deleteriously affect the properties of the final polymer. Preferably a polyurethane catalyst is added to the reaction mixture during the chain extension step. Those polyurethane catalyst described hereinbefore may be used. Preferably the catalyst is added after the prepolymer and chain extender have been contacted and mixed for a time sufficient to allow dispersion of the components in one another. The catalyst is used in an amount which facilitates the formation of the polyurethane over a reasonable time frame. Preferable catalyst amounts are between 0.01 mg and 0.08 mg per 100 parts of reactive components, with between 0.02 mg and 0.06 mg being preferred.

If the bulk polyurethane is to undergo a neutralization, quaternarization or ternarization step, whatever the case may be, it should be performed before chain extension. Therefore, the neutralizing acid, base, alkylating agent, or whatever as required to convert the potential ionic group to its ionic form is added to the rapidly stirred prepolymer in sufficient amount to react with at least 75 percent, preferably at least 90 percent of the potential ionic moieties.

The physical properties of the final polymers obtained whether in the form of films, coatings, or even stoving lacquers can vary. Such properties include tensile properties, abrasion resistance, solvent resistance, water absorption, etc. The bulk polyurethanes preferably have tensile properties of 10342 kPa (1500 psi) or greater, and more preferably 17238 kPa (2500 psi) or greater. Such polyurethanes preferably have an abrasion resistance of no more than 25 percent delta haze after 600 strokes (ASTM F-735). The bulk polyurethanes preferably demonstrate solvent resistance after 100 methyl ethyl ketone double rubs. The bulk polyurethanes preferably exhibit a water absorption of four percent or less, more preferably two percent or less. Such bulk polyurethanes preferably r) demonstrate a permanent set of 50 percent or less, more preferably 25 percent or less. Using extenders of functionality greater than 2 in combination with prepolymers having the highest isocyanate contents results in the harder thermosets due to the high hard segment content of the polymer and cross-linkin-g. This is particularly true when the soft segments in the prepolymer are derived from the lowest molecular weight polyols. The terms "soft and hard segments" refer to " the polymer linkages derived from the diisocyanate component with the high molecular weight polyols (ii) and with the extender (iii) respectively. Reversing all of the above conditions leads to the softer materials.

The polyurethanes can be modified further by the addition of colorants, antioxidants, UV stabilizers, fillers, fire-retardants, antistatic agents and the like known to those skilled in the art.

The bulk polyurethanes may be pressure molded into desired shapes. Alternatively they may be extruded into desired forms, for example into films or sheets. The films or sheets may be laminated to substrates. '^* Alternatively the polyurethanes may be coextruded with a desired substrate.

In a pressure molding application the polyurethane is placed into a mold of the desired shape and heated to a temperature at which the polyurethane is flowable, preferably between 130°C and 190°C, more preferably between 145°C and 170°C. Thereafter the polyurethane is exposed to sufficient pressure to mold the polyurethane to the desired shape, preferable pressures are between 172375 kPa (25,000 lb/in²) and 482650 kPa (70,000 lb/in²), with between 344750 kPa (50,000 lb/in²) and 413700 kPa (60,000 lb/in²) being more preferred.

The excellent properties of the films include good clarity, high gloss, good weather resistance

10 including water repellency and abrasion resistance. This makes them particularly useful in the manufacture of waterproof clothing, tarpaulins, chip-resistant coatings in automotive applications such as protective coatings applied after a car has been painted, and 15 coatings for high grade paper. The present films provide excellent protective coatings on aircraft acrylic canopies and in ballistic glazing applications,

The above utilities can be achieved without the

20 need for using organic solvents which, for the most part, are required in the prior art coatings. Of even more significance is the fact that the present polymers can be prepared with increasing hardness and stiffness p_c- values while at the same time keeping relatively constant permanent set properties. Heretofore, this has not been possible. Accordingly, the present compositions are provided with increased hardness and tensile modulus properties without having to resort to

30 the need of higher hard segment linkages derived from higher diisocyanate concentrations.

The following examples further illustrate the present invention. All parts and percentages are by weight unless otherwise stated. Example 1

Into a dry 1-liter round-bottom flask, equipped with mechanical stirrer, thermometer and gas inlet/outlet tubes, was added 209.6 g (0.2^ equivalent weight) of polypropylene oxide diol (equivalent weight 998) and 20.5 g (0.09 equivalent weight) of polypropylene oxide triol (equivalent weight 228). The mixture was heated under vacuum at 135°C for one hour. The temperature was lowered to 80°C and 20.1 g (0.3Q. equivalent weight; 0.15 mole) of 2,2-bis(hydroxymethyl)- propionic acid, 162.1 g (1.236 equivalent weight) of ,r 4,4-methylene bis(cyclohexyl isocyanate) and 30 μl of stannous octoate were added. The mixture was heated at 100°C for 2 hours under a nitrogen blanket. The mixtures cooled to 80°C and 26.7 g (0.144 mole) of tributylamine was added. The stirring was continued for 20 minutes. One decimal seven g (1.7 g) of octadecyl- 3,5-ditertbutyl-4-hydroxy-hydrocinnamate (Irganox 1076 stabilizer) was added and stirring continued for 5 minutes. The mixture was cooled to 30°C and 27.0 g (0.60 equivalent weight) of 1,4-butanediol and 194 μl of stannous octoate was added. A slow exotherm started. When the temperature reached 50°C, the mixture was poured into a polypropylene tray and heated in an air oven at 100°C for 12 hours.

The bulk ionomers were compression molded at 165°C to uniform, transparent sheets by the following procedures. The rubbery polyurethane ionomer sheets were cut into small pieces and placed between two metal sheets, which had previously been coated with RELEASE ALL™ #100 (trademark of Airtech International, Inc.) mold release. The metal sheets with samples are placed in a press at 166°C and the following pressure cycle was used:

10 minutes at 3448 kPa (500 lb/in²) 5 minutes at 17238 kPa (2500 lb/in²) 15 minutes at 413700 kPa (60000 lb/in²).

The tensile properties were determined on Instron Model 4206 according to ASTM D1708084. The results from this study are compiled in Table I.

Comparative Example 1

A bulk polyurethane was prepared using the process described in Example 1 using the following materials; 180 g of polypropylene oxide diol (equivalent weight 998), 12.1 g 2,2-bis(hydroxymethyl)propionic acid, 97-5 g of 4,4-methylene bis(cyclohexyl isocyanate), 18 μl stannous octoate (for prepolymer step) 1 g octadecyl-3,5-ditertbutyl-4 hydroxy hydrocinnamate, 16.3 g 1,4-butanediol, and 117 μl stannous octoate (for chain extension step).

Samples were prepared and tested for tensile properties as described in Example 1. The results are compiled in Table I.

Comparative Example 2

A bulk polyurethane was prepared using the process described in Example 1 using the following materials; 180.1 g of polypropylene oxide diol (equivalent weight 998), 12.1 g 2,2- bis(hydroxymethyl)propionic acid, 97.6 g of 4,4-methylene bis(cyclohexyl isocyanate), 18 μl stannous octoate (for prepolymer step), 11.2 g N,N-diisopropylethylamine, 1 g octadecyl-3,5- ditertbutyl-4 hydroxy hydrocinnamate, 16.3 g 1,4-butanediol, and 117 μl stannous octoate (for chain extension step).

Example 2

A bulk polyurethane was prepared using the process described in Example 1 using the following materials; 171.0 of polypropylene oxide diol (equivalent weight 998), 2.1 g of polypropylene oxide triol

(equivalent weight 228), 12.1 g 2,2- bis(hydroxymethyl)propionic acid, 97.6 g of 4,4-methylene bis(cyclohexyl isocyana€e), 18 μl

octoate (for prepolymer step), 11.2 N,N-diisopropylethyl amine, 1.0 g octadecyl-3,5-ditertbutyl-4 hydroxy _* hydrocinnamate, 16.3 g 1,4-butanediol, and 117 μl stannous octoate (for chain extension step).

Example 3

A bulk polyurethane was prepared using the process described in Example 1 using the following materials; 179.6 g of polypropylene oxide diol (equivalent weight 998), 4.6 g of polypropylene oxide triol (equivalent weight 228), 13.4 g 2,2-bis(hydroxy- methyDpropionic acid, 108.1 g of 4,4-methylene bis(cyclohexyl isocyanate), 20 μl stannous octoate (for prepolymer step), 12.9 N,N-diisopropylethylamine, 1.1 g octadecyl-3,5-ditertbutyl-4 hydroxy hydrocinnamate, 18.0 g 1 ,4-butanediol, and 130 μl stannous octoate (for chain extension step).

Samples were prepared and tested for tensile

10 properties as described in Example 1. The results are compiled in Table I.

Example 4

« _- A bulk polyurethane was prepared using the process described in Example 1 using the following materials; 199.6 g of polypropylene oxide diol (equivalent weight 998), 11.4 g of polypropylene oxide triol (equivalent weight 228), 16.8 g 2,2-bis(hydroxy-

20 methyl)propionic acid, 135.1 g of 4,4-methylene bis(cyclohexyl isocyanate), 25 μl stannous octoate (for prepolymer step), 22.2 g tributylamine, 1.4 g octadecyl-3,5-ditertbutyl-4 hydroxy hydrocinnamate, 22.5 g 1 ,4-butanediol, and 162 μl

25 stannous octoate (for chain extension step).

Samples were prepared and tested for tensile properties as described in Example 1. The results are ,₀ compiled in Table I. -25-

Example 5

A bulk polyurethane was prepared using the process described in Example 1 using the following materials; 179.6 g of polypropylene oxide diol (equivalent weight 998), 27.4 g of polypropylene oxide triol (equivalent weight 228),

20.1 g 2,2-bis-(hydroxymethyl)propionic acid, 162.1 g of 4,4-methylene bis(cyclohexyl isocyanate), 30 μl stannous octoate (for prepolymer step), 26.7 tributylamine, 1.7 g

10 octadecyl-3,5-ditertbutyl-4 hydroxy hydrocinnamate, 27.0 g 1 ,4-butanediol, and 194 μl stannous octoate (for chain extension step).

,,- Samples were prepared and tested for tensile properties as described in Example 1. The results are compiled in Table I.

Table I 0 Example, 300%

Comparative Equiv.% Tensile Elongation

Exam les ofTriol Stren th si Elon ation % Modulus si e

25

30

Claims

CLAIMS:

1. A bulk polyurethane ionomer prepared by the reaction of (A) an isocyanate terminated ionic prepolymer with (B) a hydrocarbon polyol chain extender said prepolymer having been prepared from (i) an excess of a diisocyanate, (ii) a mixture comprising a diol and an organic polyol having three or more reactive hydroxyl groups each having a molecular weight of from 250 to 6,000 and (iii) a difunctional isocyanate-reactive component containing an ionic group or potential ionic group.

0

2. A bulk polyurethane ionomer according to Claim 1 wherein the hydrocarbon polyol chain extender comprises a hydrocarbon diol; the diisocyanate comprises an aliphatic or cycloaliphatic diisocyanate; and the 5 organic polyol is a triol.

3. A bulk polyurethane ionomer according to Claim 1 wherein said chain extender comprises an _Q alkylene diol.

4. A bulk polyurethane ionomer according to Claim 1 wherein said diisocyanate (i) comprises

4,4*-methylenebis(cyclohexyl isocyanate). 5 -27-

5. A bulk polyurethane ionomer according to Claim 2 wherein said triol comprises a polyethyleneoxy capped polypropyleneoxy triol.

6. A bulk polyurethane ionomer according to _j- Claim 2 wherein said triol is present in up to 50 hydroxyl equivalent percent of said mixture (ii).

7. A bulk polyurethane ionomer according to Claim 1 wherein component (iii) is present in sufficient

10 proportions to provide from 10 to 150 milliequivalents of ionic groups per 100 grams of said prepolymer (A).

8. A bulk polyurethane ionomer according to Claim 1 wherein the proportions of components (i), (ii),

15 and (iii) are such that the ratio of isocyanate equivalents to the total isocyanate-reactive equivalents in said prepolymer (A) falls in a range of from 1.5 to 3.

20

9. A bulk polyurethane ionomer according to

Claim 1 wherein the proportions of said isocyanate terminated prepolymer (A) and polyol chain extender (B) are such that the ratio of equivalents of isocyanate in 25 (A) to amine equivalents in (B) falls in a range of from 1.25 to 0.90.

10. A bulk polyurethane ionomer according to Claim 1 wherein component (iii) is neutralized with

- triethylamine.