KR101137663B1 - Articles Comprising Aqueous Dispersions of Poly(urea/urethanes) - Google Patents

Abstract

Stable poly (urea / urethane) polymers and dispersions are prepared in the present invention that do not need to include chain extenders, hardeners or crosslinkers. The disclosed poly (urea / urethane) dispersions can be used to make articles such as films and gloves with reduced chances of chemical and biological allergic reactions to the skin, which articles have improved resistance to such articles made of other materials. It exhibits puncture resistance and tear resistance.

Description

Articles comprising aqueous dispersions of poly (urea / urethane) {Articles Comprising Aqueous Dispersions of Poly (urea / urethanes)}

This application claims the benefit of U.S. Provisional Application No. 60 / 423,617, filed November 4, 2002, which is incorporated by reference in its entirety for all purposes, and U.S. Provisional Application No. 60 / 448,971, filed February 20, 2003. Insist.

The present invention relates to urethane polymers that do not include residues of chain extenders, curing agents or crosslinking agents, and aqueous dispersions prepared therefrom. Polyurethane particles dispersed in water can be used to make articles such as films and gloves that reduce the chance of chemical and biological allergic reactions to the skin, which have improved puncture resistance and It shows tear resistance.

Methods for preparing elastomeric materials are known in the art from sources such as Kirk-Othmer Encyclopedia of Chemical Technology (4 ^th edition, Volume 10, Pages 624-638, John Wiley & Sons, Inc., New York, 1993). It is. Many elastomeric materials contain urethane bonds prepared by reacting hydroxy-terminated polyethers or polyesters with polyisocyanates in a molar ratio of about 1: 1.4 to 1: 2.5 (polyol to polyisocyanate). High molecular weight urea / urethane polymers are then prepared by typically reacting the resulting isocyanate-terminated prepolymer with a polyamine. Small amounts of monofunctional amines may also be included to control the molecular weight of the polymer. The mechanical properties of the final polymer can be modified by the selection of the polyether or polyester glycols used, diisocyanates, polyamines, and monoamines, and can also be modified by the selection of the polyol-diisocyanate molar ratio.

Long-chain elastomer urethane polymer molecules are substantially linear block copolymers containing relatively long blocks with weak molecular interactions interconnected by shorter blocks with strong interactions. Weak interaction blocks, commonly referred to as soft segments, are typically derived from polyether or polyester glycol components, whereas blocks with strong interaction are derived from the reaction of polyisocyanates with chain extenders and are called hard segments. Chain extension reactions usually produce urea bonds as coupling reactions between the isocyanate ends and the amino groups of the polyamine. Thus, the resulting combined hard- and soft-segmented polymers typically produce poly (urea / urethane).

The polymers described above have been used to prepare aqueous urethane dispersions. Urethane dispersions can be prepared, for example, by chain extending the reaction product of organic diisocyanates or polyisocyanates with organic compounds having at least two active hydrogen atoms (at the hydroxy or amino terminus), often using small amounts of organic solvents. . If diisocyanate is used in more than stoichiometric amounts, the reaction product, which may be a urea / urethane prepolymer, has isocyanate ends. Examples of such prepolymer preparation methods are described in particular in US Pat. Nos. 3,178,310, 3,919,173, 4,442,259, 4,444,976, and 4,742,095.

Urethane dispersions include coatings and binders (US Pat. No. 4,292,226); Flexible solvent barriers (US Pat. No. 4,431,763); Adhesives (US Pat. No. 4,433,095); And films (US Pat. No. 4,501,852) are reported to be useful for preparing various materials. Film applications include gloves, organ bags, condoms, colostomy bags, and the like. However, conventional urethane dispersions have sometimes been found to have insufficient physical handling properties to make them desirable materials for such applications. In addition, the use of certain relatively high-boiling solvents in the dispersion, such as N-methyl-2-pyrrolidone, may adversely affect some of the applications.

Although aromatic polyisocyanates such as toluene diisocyanate (TDI), methylene diphenyl diisocyanate (MDI) and polymethylene polyphenylisocyanate (PMDI) are widely used, sometimes aliphatic polyisocyanates are used to prepare aqueous urethane dispersions. It is preferable. As disclosed in US Pat. No. 5,494,960, aliphatic isocyanates were considered to have much higher stability against hydrolysis even if the prepolymer was dispersed in water. In this situation, it was common judgment that the chain-extension reaction between the isocyanate and the polyamine proceeds in a more controlled and predictable manner.

However, the reaction of the polyamine with the diisocyanate in water is judged to be dependent on diffusion, and thus it cannot be guaranteed that all the added polyamine is consumed during the reaction. Any unreacted polyamine remains in the polymer when prepared from the dispersion into the final product. In the case of using the product for use in contact with human skin, such unreacted polyamines (such as ethylene diamine and BK Kim, Colloid. Polym. Sci., 274, incorporated herein by reference in their entirety for all purposes): 599-611, 1996) (other diamines described in "Kim") can cause skin irritation or sensitivity to product users. The presence of unreacted polyamines in the urethane dispersion can also cause an unpleasant odor in any product made from the dispersion.

Films made from natural rubber latex are considered conventional and have desirable properties in terms of comfort and utility. Unfortunately, natural rubber latexes also contain other substances such as proteins and sulfur-containing hardeners that can irritate the skin and cause severe allergic reactions in some people.

Elastic films with good moisture control can provide protection from environments such as bacteria and chemicals. In particular, as the potential threat from chemicals and biologics increases, the need for such materials is increasing. Recent events show that there is a need for comfortable gloves that can be worn by law enforcement and postal workers for extended periods of time. Latex gloves usually have low puncture resistance and may further add additional health risks, including allergic reactions that are fatal to certain individuals. Nitrile gloves have good puncture resistance but can cause fatigue with prolonged use due to high modulus. Although polyurethane elastomers can be selected as an alternative material, some polyurethane gloves have been found to weaken when exposed to water or massage alcohol. This will impede the long term use of the glove.

Accordingly, there is also a need for urethane polymers that can be easily formed and prepared into dispersions and that have a reduced likelihood of exhibiting properties that the user would feel harmful or unpleasant in the form of articles of manufacture. Applicants have found that reducing or eliminating the content of unreacted polyamines in polyurethane polymers produces polyurethanes that are useful for preparing from dispersions and that are unlikely to cause skin irritation or release an unpleasant odor. In conclusion, Applicants have proposed reducing and preferably removing the content of unreacted polyamines in such urethane polymers by preparing polymers without the use of polyamine chain extenders. Films formed from such polymers have been found to exhibit useful barrier properties for some conventional alcoholic solvents such as water and isopropanol as well as useful mechanical properties such as low modulus at 100% stretching.

Summary of the Invention

One embodiment of the invention relates to a repeat unit derived from (a) hydroxy-terminated copolymers prepared from one or both of tetrahydrofuran and alkylene oxide and cyclic acetals, and (b) derived from polyisocyanates. A repeat unit;

Formula -RN (R ² ) -C (O) -N (R ² ) -R ^1- (R is an aromatic hydrocarbon radical, R ¹ is an aliphatic hydrocarbon radical, R ² is H or a formula -C (O)- Less than about 2 mole percent of a urea unit described by NH-R-;

(R⁴ 중 임의의 하나는 C₁ 내지 C₄ 알킬 라디칼이고 나머지 R⁴는 수소일 수 있음)으로 기재되는 우레아/우레탄 중합체이다.Tetrahydrofuran has the formula

(R ⁴ Any one of which is a C ₁ to C ₄ alkyl radical and the remaining R ⁴ may be hydrogen).

Another embodiment of the invention comprises repeating units derived from aliphatic polyether polyols having a molecular weight of about 700 to about 1500, and (b) repeating units derived from polyisocyanates;

Formula -RN (R ² ) -C (O) -N (R ² ) -R ^1- (R is an aromatic C ₆ -C ₂₀ hydrocarbon radical, R ¹ is an aliphatic C ₁ -C ₂₀ hydrocarbon radical, R ² Is an ionomer urea / urethane polymer containing less than about 2 mole percent of a urea unit described by H or an amide group described by the formula -C (O) -NH-R-.

A further embodiment of the invention comprises (a) repeating units derived from aliphatic polyester polyols, and (b) repeating units derived from polyisocyanates;

Formula -RN (R ² ) -C (O) -N (R ² ) -R ^1- (R is an aromatic C ₆ -C ₂₀ hydrocarbon radical, R ¹ is an aliphatic C ₁ -C ₂₀ hydrocarbon radical, R ² Is an ionomer urea / urethane polymer containing less than about 2 mole percent of a urea unit described by H or an amide group described by the formula -C (O) -NH-R-.

Another embodiment of the present invention is an article such as a glove made of an aqueous polyureaurethane dispersion.

The tensile strength of the article is greater than 2030 psi, the puncture resistance is greater than 200 lbs / in, and the tear strength per thickness is greater than 20 N / mm. They also show improved solvent resistance.

Another embodiment of the invention is (a) the mold is immersed in a coagulant solution and dried at elevated temperature; (b) the coagulant solution-coated mold is immersed in an aqueous polyureaurethane dispersion and dried; (c) introducing the coated mold into a salt effluent bath; (d) A method of making the article by drying the coated mold at elevated temperature and then peeling off the article from the mold.

1 is a graph of shear rate (seconds ⁻¹ ) versus shear time (minutes) for the preparation of an aqueous poly (urea / urethane) dispersion.

The present invention discloses a process for the preparation of stable aqueous poly (urea / urethane) dispersions, including materials which are sometimes referred to herein as "urethane" polymers or dispersions. The dispersions are based on the use of polyether homopolymers and / or copolymers, or polyesters such as glycols, and aromatic polyisocyanates and do not require the use of typical chain extenders, hardeners or crosslinkers such as polyamines. In the dispersion process, stable colloidal particles of elastomeric polyurethanes are produced with a wide range of uses.

Typically, for the production of aqueous colloids of polyurethanes, aliphatic polyisocyanates are preferred (see generally Kim). The aliphatic polyisocyanates react with various glycols to form oligomeric prepolymers, which are then dispersed in water containing the equivalents of diamine. The amount of diamine is added in an equivalent amount to the NCO ratio in the prepolymer determined by n-butylamine titration and reverse calculation. Because aliphatic polyisocyanates have a relatively high stability in water, diamines react with isocyanates to chain extend prepolymers through urea bonds.

However, in the urethane polymers and urethane dispersions of the present invention, it has been found that isocyanate groups are hydrolyzed to form -NH ₂ groups. The -NH ₂ groups then form urea bonds in amounts that react with other isocyanate groups to form high polymers (e.g., molecular weights suitable for free standing film formation-typically greater than 100,000 and preferably greater than 200,000) and This reaction takes place without the addition of conventional polyamines such as ethylene diamine and other diamines as described in Kim. This is important because the reaction of polyamine and isocyanate groups in water is governed by diffusion and it cannot be ensured that all added polyamine is consumed during the reaction. Any unreacted polyamine remaining in the material during further manufacture may cause skin irritation or sensitivity upon the end use of a particular product.

Omitting the polyamine chain extender from the reaction to form the poly (urea / urethane) is represented by the formula -RN (R ² ) -C (O) -N (R ² ) -R ^1- (R is an aromatic hydrocarbon radical, R ¹ is an aliphatic hydrocarbon radical and R ² is less than about 2 mol%, preferably less than about 1 mol%, of a urea unit described by H or an amide group described by the formula -C (O) -NH-R-, and More preferably enables the production of polymers containing less than about 0.5 mole percent. In a further embodiment, the polymer is free or substantially free of the urea units described above, and the content of unreacted polyamine in the polymer is sufficiently low such that this amount of polyamine is undesirable to the product, or to users of film products made therefrom. It is substantially free of such urea units unless they cause any skin reactions that do not.

It has also been found that the polyisocyanates in the urethane polymers and dispersions of the present invention need not be limited to aliphatic polyisocyanates and that aromatic polyisocyanates are suitable for use herein. Examples of suitable polyisocyanates to be used for preparing the isocyanate-terminated prepolymers according to the invention include organic diisocyanates having the general formula R ¹⁰ (NCO) ₂ (R ¹⁰ having a molecular weight of about 112 to 1,000, and preferably about 140 to 400 Organic groups is obtainable by removing isocyanate groups from the organic diisocyanate). Preferred diisocyanates for the process according to the invention are the general formulas mentioned above (R ¹⁰ is a divalent aliphatic hydrocarbon group having 4 to 18 carbon atoms, a divalent cycloaliphatic hydrocarbon group having 5 to 15 carbon atoms, 7 to A divalent araliphatic hydrocarbon group having 15 carbon atoms or a divalent aromatic hydrocarbon group having 6 to 15 carbon atoms). Examples of particularly suitable organic diisocyanates for the process are tetramethylene diisocyanate, 1,6-hexamethylene diisocyanate, dodecamethylene diisocyanate, cyclohexane-1,3- and -1,4-diisocyanate, 1-isocysi Anatoto-3-isocyanatomethyl-3,5,5-trimethylcyclohexane (isophorone diisocyanate or IPDI), bis- (4-isocyanatocyclohexyl) -methane, 1,3- and 1 , 4-bis (isocyanatomethyl) -cyclohexane, bis- (4-isocyanato-3-methyl-cyclohexyl) -methane, 2,4-diisocyanatotoluene, 2,6-di Isocyanatotoluene, mixtures of these isomers, 4,4'-diisocyanato diphenyl methane and 2,4'- and optionally 2,2'-diisocyanato diphenylmethane and isomer mixtures thereof, and 1, 5-diisocyanatonatophthalene. Of course, mixtures of diisocyanates can be used. Preferred diisocyanates include 1,6-hexamethylene diisocyanate, isophorone diisocyanate, bis- (4-isocyanatocyclohexyl) -methane, 2,4- and / or 2,6-diisocyanatotoluene And 4,4'- and / or 2,4'-diisocyanato diphenylmethane.

(q는 2 내지 4이고, 각각의 R³은 독립적으로 수소 또는 메틸임)의 구조로 나타낸 것이다. 공단량체로서 사용될 수 있는 테트라히드로푸란은 화학식

(R⁴ 중 임의의 하나는 C₁ 내지 C₄ 알킬 라디칼이고 나머지 R⁴는 수소일 수 있음)의 구조로 나타낸 것이다. 그러나, 바람직한 테트라히드로푸란 (THF)에서, 모든 R⁴는 수소이다. Preference is given to using hydrophilic soft segments with polarity which enhance the formation of dispersions in urea / urethane polymers and dispersions thereof. In one embodiment, the soft segments can be formed from hydroxy-terminated copolymers prepared from one or both of tetrahydrofuran and alkylene oxide and cyclic acetal. The alkylene oxides used to prepare such copolymers may be those containing two or three carbon atoms in the alkylene oxide ring. Alkylene oxides may be unsubstituted or substituted with, for example, alkyl groups, aryl groups or halogen atoms. Examples of such alkylene oxides are ethylene oxide and 1,2-propylene oxide, with ethylene oxide (EO) being preferred. Cyclic acetals that can be used as comonomers are of the general formula

(q is 2 to 4 and each R ³ is independently hydrogen or methyl). Tetrahydrofuran, which can be used as comonomer,

Wherein any one of R ⁴ is a C ₁ to C ₄ alkyl radical and the remaining R ⁴ may be hydrogen. However, in preferred tetrahydrofuran (THF), all R ⁴ is hydrogen.

The portion of the copolymer derived from alkylene oxide and / or cyclic acetal may be greater than about 20 weight percent and is preferably about 25 to about 60 weight percent. The molecular weight of the copolymer may be about 1,000 to about 3,500, and preferably about 1,500 to about 2,500. These copolymers are prepared from monomers such as trifluorovinylsulfonic acid, linear or branched-vinyl monomers containing α-fluorosulfonic acid group precursors and perfluoroalkylvinyl ethers containing α-fluorosulfonic acid group precursors. It can be produced by a process of applying a polymer catalyst. The process can be carried out at ambient temperatures up to 80 ° C., or higher, under pressures up to 5000 atmospheres. The reaction is preferably carried out in an inert atmosphere such as nitrogen. If the copolymer is capped ester-terminated as prepared, it can be converted to copolyether glycols by an alcoholic reaction. Suitable soft segment copolymers, and methods for their preparation, are described in US Pat. Nos. 4,127,513, 4,139,567, 4,153,786, 4,228,272 and 4,235,751; DE 86-3606479 and DE 83-3346136; J. M. Hammond et al, J. Polym. Sci., Part A, Vol. 9, page 295 (1971); And in Hongzhi Zhang et al, J. Appl. Polym. Sci., Vol. 73, page 2303 (1999).

In another embodiment of the invention, the urea / urethane polymer is an ionomer polymer and the soft segments of the polymer and its dispersions are derived from isocyanate-reactive ionic or potential ionic compounds, and aliphatic polyester polyols or low molecular weight aliphatic polyether polyols Can be.

Suitable polyester polyols include reaction products of aliphatic dihydric alcohols and aliphatic dihydric carboxylic acids, one or both of which may be, for example, C ₂ to C ₁₂ molecules. Other examples of dihydric alcohols suitable for use for this purpose are ethylene glycol, trimethylene glycol, 1,4-butanediol, 1,5-pentanediol, 1,6-hexanediol, diethylene glycol, propylene glycol and neopentyl Glycols; Polyether compounds such as polyethylene glycol, polypropylene glycol and polybutylene glycol; Diols of cycloaliphatic hydrocarbons such as 1,3-cyclohexanedimethanol and 1,4-cyclohexanedimethanol.

Other examples of dicarboxylic acids suitable for use for this purpose include aliphatic dicarboxylic acids such as succinic acid, glutaric acid, adipic acid, pimelic acid, suberic acid, azelaic acid, sebacic acid, decandicarboxylic acid , Dicarboxylic acids derived from dodecanedicarboxylic acid, cyclohexanedicarboxylic acid, norbornanedicarboxylic acid, tricyclodecane-dicarboxylic acid and pentacyclododecanedicarboxylic acid. Instead of free dicarboxylic acids, the corresponding dicarboxylic anhydrides or dicarboxylic acid esters of lower alcohols or mixtures thereof can be used to prepare the polyesters.

The dihydric alcohol and the diacid unit may each be contained in the polyester resin in an amount of about 5 to about 95 mole percent. The manufacturing process of a polyester resin is not specifically limited, A conventional process can be applied. Examples of processes include melt polymerization reaction processes such as transesterification reaction processes and direct esterification processes, solution polymerization reaction processes and solid polymerization reaction processes.

Useful polyester polyols, hydroxyl terminated linear polyesters are described, for example, in the Fomrez® product of Uniroyal Chemical Company: Pomrez® G24-56 [2000 Mw, Hydroxyl terminated linear polyester, poly (ethylene / butylene adipate) glycol with ethylene glycol / 1,4-butanediol in 60/40 molar ratio], Pomrez® G24-112 [1000 Mw, hydride Hydroxyl terminated linear polyester, poly (ethylene / butylene adipate) glycol with ethylene glycol / 1,4-butane diol in 60/40 molar ratio], and Pomrez® 22-56 (2000 Mw, poly Hydroxyl terminated saturated linear polyesters using (ethylene adipate) glycols.] Thus, polyester polyols are composed of ethylene adipate, butylene adipate, ethylene / butylene adipate, and mixtures thereof. Dihydroxy such as those selected - may be terminated polymer.

Suitable polyether polyols are of the formula HO-[(CR ⁶ H) _m -O-] _n -H (R ⁶ is hydrogen, halogen or a C ₁ to C ₄ alkyl radical; m is 3 or 4; n is about 8 To about 20, or more preferably about 11 to about 17). The molecular weight of the polyol may be about 700 to about 1500, or preferably about 900 to about 1150. Suitable polyether polyols are Terethane® brand polytetramethyleneetherglycol (PTMEG) available from DuPont.

Urethane polymers in this embodiment are referred to as ionomers because they contain ionic or potentially ionic compounds. Ionic or potentially ionic compounds are hydrophilic compounds that provide the urethane polymer with ionic (eg anionic or cationic) functionalities to act as internal emulsifiers to promote the formation of dispersions. The compounds are isocyanate-reactive because they contain two or more atoms, such as oxygen or nitrogen, which can react with isocyanate groups so that active hydrogens are removed as a result of the reaction mechanism involving the isocyanate groups.

Ionic or potentially ionic groups are chemically incorporated into the poly (urea / urethane). Ionic or potentially ionic groups are up to about 120 milliequivalents per 100 g of poly (urea / urethane), preferably about 10 to 80 milliequivalents, more preferably about 10 to 60 milliequivalents, and most preferably about It may be incorporated in an amount sufficient to provide an ionic group content of 10 to 30 milliequivalents.

및

을 포함한다.Compounds suitable for incorporating such groups include (1) monoisocyanates or diisocyanates containing ionic or potentially ionic groups, and (2) monofunctional or difunctional and isionic or potentially ionic in isocyanate-polyaddition reactions. And compounds containing groups. While anionic groups are preferred, the potential ionic groups or their corresponding ionic groups can be cationic or anionic. Examples of anionic groups include -COO ^- and a ^- and -S0 _3. Examples of cationic groups are

And

It includes.

Said ionic groups are formed by neutralizing the corresponding potential ionic groups during or after the formation of the isocyanate-terminated prepolymer. In case the potential ionic group is neutralized prior to isocyanate-terminated prepolymer formation, the ionic group is incorporated directly. If neutralization is carried out after forming the prepolymer, potential ionic groups are incorporated.

Suitable compounds for incorporating carboxylate, sulfonate and quaternary nitrogen groups discussed above are described in US Pat. Nos. 3,479,310, 4,303,774 and 4,108,814. Suitable compounds for incorporating tertiary sulfonium groups are described in US Pat. No. 3,419,533. Neutralizers for converting potential ionic groups to ionic groups are also described in this patent. In the context of the present invention, the term "neutralizing agent" is meant to include all types of agents useful for converting potential ionic groups to ionic groups. Thus, the term also includes quaternization agents and alkylating agents.

Preferred sulfonate groups for incorporation into isocyanate-terminated prepolymers are diol sulfonates disclosed in US Pat. No. 4,108,814. Suitable sulfonates also include H ₂ N—CH ₂ —CH ₂ —NH— (CH ₂ ) _r —SO ₃ Na (r is 2 or 3); And HO-CH ₂ -CH ₂ -C (S0 ₃ Na) H-CH ₂ -OH. Preferred carboxylate groups for incorporation in isocyanate-terminated prepolymers are the general formula (HO) _x R ⁷ (COOH) _y (R ⁷ represents a straight or branched hydrocarbon radical containing 1 to 12 carbon atoms, x and y Are each independently derived from a value of 1 to 3). Examples of such hydroxy-carboxylic acids include citric acid and tartaric acid.

Preferred acids are those of the above-mentioned formula (x is 2 and y is 1). Such dihydroxy alkanoic acid is described in US Pat. No. 3,412,054. Preferred groups of dihydroxy alkanoic acid are α, α-dimethylol alkanoic acids represented by the formula R ⁹ -C- (CH ₂ 0H) ₂ -COOH, where R ⁹ is hydrogen or an alkyl group containing from 1 to 8 carbon atoms. to be. Most preferred dihydroxy alkanoic acid is 2,2 'dimethanol propionic acid ("DMPA"). Suitable carboxylates are also H ₂ N- (CH ₂ ) ₄ -C (C0 ₂ H) H-NH ₂ + bases, and H ₂ N-CH ₂ -CH ₂ -NH-CH ₂ -CH ₂ -CO ₂ Contains Na.

In addition, cationic centers such as tertiary amines having one alkyl group and two alkylol groups can also be used as ionic or potentially ionic groups.

In order to convert the desired potential anionic groups to anionic groups during or before incorporation in the prepolymer, volatile or nonvolatile cations are used to form the counterions of the anionic groups. Volatile cations are volatilized under the conditions used in at least about 90% of the basic organic compounds used to form the counterions of the anionic groups to cure films formed from poly (urea / urethane) dispersions, preferably poly (urea / Urethane) At least about 90% of the basic organic compound is volatilized when the film formed from the dispersion is cured under ambient conditions. The nonvolatile cations do not volatilize at least 90% of the cations under the conditions used to cure the film formed from the poly (urea / urethane) dispersion, and preferably if the film formed from the polyurethane-urea dispersion is cured under ambient conditions More than about 90% of the cations do not volatilize. As the amount of counterions formed from volatile basic organic compounds increases, the resistance to water swelling of coatings or films made from aqueous polyurethane-urea dispersions is further improved, but as the amount of counterions formed from nonvolatile cations increases, Stability against hydrolysis of films or coatings made from aqueous polyurethane-urea dispersions is further improved. Thus, it is possible to control the properties of the final resulting coating or film by simply adjusting the ratio between the volatile and nonvolatile cations used to form the counterion of the anionic group.

Suitable volatile basic organic compounds for neutralizing potential anionic groups are primary, secondary or tertiary amines. Preferred among these amines are trialkyl-substituted tertiary amines. Examples of such amines are trimethyl amine, triethyl amine, triisopropyl amine, tributyl amine, N, N-dimethyl-cyclohexyl amine, N, N-dimethylstearyl amine, N, N-dimethylaniline, N-methyl Morpholine, N-ethylmorpholine, N-methylpiperazine, N-methylpyrrolidine, N-methylpiperidine, N, N-dimethyl-ethanol amine, N, N-diethyl-ethanol amine, triethanolamine , N-methyldiethanol amine, dimethylaminopropanol, 2-methoxyethyldimethyl amine, N-hydroxyethylpiperazine, 2- (2-dimethylaminoethoxy) -ethanol and 5-diethylamino-2-penta It's rice fields. The most preferred tertiary amines do not contain active hydrogen (s) as measured by Zerewitinoff test, because they can react with isocyanate groups of the prepolymer and cause gelation, formation of insoluble particles or chain termination. .

If triethyl amine is used as the base, it is recommended to use less than 1 equivalent of amine relative to the acid to minimize any potential odor. Dispersed water generally contains less than 1 equivalent of base to neutralize the acid, wherein the pH of the 1 molar aqueous solution does not exceed 10.

Suitable nonvolatile cations also include monovalent metals, preferably alkali metals, more preferably lithium, sodium and potassium and most preferably sodium. The cations can be used in the form of inorganic or organic salts, preferably salts in which no anions remain in the dispersion, such as hydrides, hydroxides, carbonates or bicarbonates. For example, when acid-containing diols are used as ionic groups, relatively mild inorganic bases such as NaHCO ₃ , Na (C0 ₃ ) ₂ , NaAc (Ac represents acetate), NaH ₂ PO _4, etc., represent dispersions. Can help to improve The inorganic base tends to be relatively odorless and not skin irritant.

If the potential cationic or anionic groups of the prepolymer are neutralized, the prepolymer may be hydrophilic to allow more stable dispersion in water. The neutralization step can be carried out prior to prepolymer formation or (2) after prepolymer formation but before dispersing the prepolymer by treatment with (1) a component containing the potential ionic group (s). The reaction between the neutralizing agent and the potential anionic group can be carried out at about 20 ° C. to about 150 ° C. but usually below about 100 ° C., preferably about 30 ° C. to about 80 ° C., and most preferably about 50 ° C. while stirring the reaction mixture. It is carried out at a temperature of 50 ℃ to about 70 ℃. Ionic or potentially ionic groups can be used in amounts of about 3 to about 5 weight percent.

In the above discussion of ionic and potentially ionic groups, the referenced patent and US Pat. No. 4,742,095 are each incorporated by reference in their entirety as part of the present application for all purposes.

Isocyanate-terminated prepolymers of the present invention are prepared by reacting a polyisocyanate component with a polyol component, in embodiments, a component containing at least one ionic group or at least one potential ionic group. Potential ionic groups are groups that can be converted to ionic groups by treatment with neutralizing agents. The ratio of isocyanate groups to isocyanate-reactive groups is maintained at about 1.1 to 3, preferably about 1.2 to 2 and most preferably about 1.3 to 1.5 on an equivalent basis. The components can be reacted simultaneously or sequentially to produce isocyanate-terminated prepolymers. Simultaneous reactions can induce the production of random copolymers, while sequential type reactions can induce the production of block copolymers. The order of addition of the compounds containing isocyanate-reactive hydrogen (s) in the sequential-type reaction process is not critical but it is particularly desirable to maintain excess isocyanate groups during the reaction of the compounds to control the molecular weight of the prepolymer and prevent high viscosity Do.

During the prepolymer preparation the reaction temperature is usually maintained at less than about 150 ° C, preferably from about 50 ° C to about 130 ° C. The reaction continues until the content of unreacted isocyanate groups decreases to a theoretical amount or slightly below. The final prepolymer should have a free isocyanate content of about 1 to about 8 weight percent, preferably about 1 to about 5 weight percent, and more preferably about 2 to about 4 weight percent based on the weight of the prepolymer solids.

Although it is possible to carry out the prepolymer reaction in the presence of a catalyst known to promote the reaction between isocyanate groups and isocyanate-reactive groups, such as organotin compounds or tertiary amines, the use of catalysts is generally not necessary and often reactions without catalysts. It is preferable to carry out.

In one embodiment, the dispersion of the present invention is prepared by mixing isocyanate and glycol for several hours at a temperature of about 80 ° C. to about 100 ° C. under nitrogen to form a prepolymer. The shear rate and shear force experienced by the dispersion mixture are important and are described in FIG. 1. If too large shear force is applied, the dispersion may become unstable and break down. In general, the preferred range of shear force is 500 to 1700 newtons for a mixing time which is generally 2 to 5 minutes. In other embodiments, shear rates may be used in the range of about 19000 to about 48000 seconds ⁻¹ for a mixing time that is generally 2 to 7 minutes.

At the end of the mixing time, the amount of excess isocyanate in the prepolymer can be determined by n-butylamine titration and inverse calculation. After cooling the reaction product to room temperature, a solvent [generally a water miscible organic solvent such as acetone and methyl ethyl ketone (MEK)] can be used to optionally dilute the prepolymer to about 75% by weight solution.

The solution is then injected into a cooled aqueous solution containing a surfactant which has a tendency to reverse solubility, i.e., at least one group has affinity for the phase in which the molecules or ions are dissolved and the at least one group is a molecule consisting of groups opposed to the medium. do. Surfactants are classified according to the charge on the surface-active moiety. In anionic surfactants, the moiety has a negative charge; In cationic surfactants, the charge is positive; In nonionic surfactants, there is no charge on the molecule and a dissolution effect can be supplied by, for example, long chains of hydroxyl groups or ethylene oxide groups; In amphoteric surfactants, dissolution effects are provided by both positive and negative charges in the molecule. For anionic surfactants, hydrophilic, solubilizing groups include carboxylates, sulfonates, sulfates (including sulfated alcohols and sulfated alkyl phenols), phosphates (including phosphate esters), N-acylsarcosyls Nates, and acylated protein hydrolysates. Cationic surfactants are dissolved by amine groups and ammonium groups. In addition to polyoxyethylene, nonionic surfactants include carboxylic acid esters, anhydrosorbitol esters, glycol esters of fatty acids, alkylpolyglycosides, carboxyl amides, and fatty acid glucamides. Any surfactant or equivalent described above is suitable, but a particularly suitable surfactant is sodium dodecylbenzenesulfonate. Surfactants may be used in amounts of about 0.1 to about 2 weight percent, and preferably about 0.5 to about 1 weight percent.

Dispersion temperature is important for small particle formation. Preferred dispersion temperatures are from about 0 to about 10 ° C. The solids content of the dispersion is about 10 to 60%, and typically 10 to 30%.

The final product is a stable, aqueous dispersion of poly (urea / urethane) particles having a solids content of about 60% by weight or less, preferably about 10 to 60% by weight, and most preferably about 30 to 45% by weight. However, it is always possible to dilute the dispersion to any desired minimum solids content. The solids content of the resulting dispersion can be measured by drying the sample in an oven at 100 ° C. for 2 hours and comparing the weight before and after drying. The particle size is generally less than about 1.0 micron, and preferably about 0.01 to 0.5 micron. The average particle size should be less than about 0.5 microns, and preferably 0.01 to 0.3 microns. Small particle size enhances the stability of the dispersed particles.

Fillers, plasticizers, pigments, carbon black, silica sol and known leveling agents, wetting agents, defoamers, stabilizers, and other known additives may also be incorporated into the dispersions.

The dispersions are widely used for applications such as fabric coating, elastic film formation, fiber sizing, and the like. The dispersion can be processed into a water vapor permeable film if necessary. Examples of end-use articles made from the films formed from such dispersions include gloves, cots, condoms, colostomy bags, organ bags, and the like for all medical, sterile, hygienic and personal care related applications. The film-based article exhibits improved solvent resistance when compared to articles made of other materials.

The dispersions of the present invention include woven and nonwoven textiles, leather, paper, wood, metals, ceramics, stone, concrete, bitumen, hard fibers, straw, glass, porcelain, many different types of plastics, static and anti-wrinkle finishes. For coating and impregnation of woven glass fibers; As binders for nonwovens, adhesives, adhesion promoters, laminating agents, hydrophobicizing agents, plasticizers; As binders for cork powder or sawdust, glass fibers, asbestos, paper-like materials, plastics or waste rubber, ceramic materials, for example; As an aid in the textile printing and paper industry; As a polymer additive, eg, a sizing agent for glass fibers; And rubber finish.

The dispersions are applied to woven or nonwoven textile structures and fiber substrates that immediately cure the coating due to the absorbing action and porous substrates that remain bound to the final product, such as fiber mats, felt or nonwovens, or paper webs, foam seating or split leather. Can also be. Drying and then optionally pressing at elevated temperatures. However, drying is also carried out on smooth porous or nonporous materials, for example metals, glass, paper, cardboard, ceramic materials, sheet steel, silicone rubber, aluminum foil, and the final sheet structure is subsequently removed and used as such. Or may be applied to the substrate using an inverse process by bonding, flame lamination or calendering. The application can be carried out at any time by a reverse process.

The polyurethane dispersions are also suitable as coatings on vinyl fabrics used in automobile seats and commercial upholstery. In these areas of application, properties such as plasticizer barrier effect, improved wear resistance and good hydrolysis and UV-resistance are important. They are also useful as coatings of textiles, such as waterproof coats, such as in military articles where good toughness-like properties and properties retained after aging are essential.

When the polymers and dispersions of the invention are used as films and gloves, these materials exhibit improved solvent resistance, including isopropyl alcohol and N, N-dimethylacetamide. It also reduces the gas evolution of the film material, making these films and gloves generally available for use in clean rooms. These films and gloves not only exhibit improved chemical and solvent resistance, but also show improved puncture and tear resistance as shown in the examples below. Since they have a modulus of 100% elongation of about 200 to 500 psi, the film or glove can be easily stretched. It also exhibits a low set, allowing it to return to its original form after stretching. The preferred thickness of the glove is 3 to 6 mils, although other thicknesses may be used. The data below shows that the materials of the present invention are more similar to natural rubber because they have a more flexible stretchable or flatter strain curve than other materials tested.

For example, a glove made of the poly (urea / urethane) and dispersion herein may be a contact point between the thumb and index finger after immersing the thumb and index finger in isopropyl alcohol and rubbing each other for a time of about 30 to about 60 seconds. No perforation or destruction in the same way (for example, when the skin is exposed).

The following examples illustrate but do not limit the invention. Particularly advantageous features of the invention will be appreciated in comparison with comparative examples which do not have the unique properties of the invention.

Unless otherwise noted, all chemicals and reagents from Aldrich Chemical Company, Milwaukee, WI, Milwaukee, WI, were used. Various chemicals and reagents are represented by the following abbreviations:

MDI 4, 4'-diphenylmethane diisocyanate

Poly (EO-co-THF) Poly (ethylene oxide-co-tetrahydrofuran)

NCO Isocyanate Group

DMPA 2,2'-bis (hydroxymethyl) propionic acid

MEK methylethyl ketone (2-butanone)

TEA triethylamine

SDBS Sodium Dodecylphenyl Sulfate

Substance preparation

US Patent Nos. 4,127,513, 4,139,567, 4,153,186, 4,228,272 and 4,235,751; DE 86-3606479 and DE 83-3346136; J. M. Hammond, et al, J. Polym. Sci., Part A, Vol. 9, page 295 (1971); And in Hongzhi Zhang, et al, J. Appl. Polym. Sci., Vol. 73, p. 2303 (1999) can be used to obtain poly (ethylene glycol-co-THF). PTMEG-1000 and PTMEG-1800 are trade names for DuPont Terathane® polyether glycols. All glycols were dried under vacuum at 90 ° C. for 12 hours before use. MDI was purified by heating to 50 ° C. DMPA, MEK, TEA and SDBS were purchased and used without further purification. The mixer used to prepare the dispersion was an IKA® mixer, model T25 BASIC SI (IKA® Works, Inc.), and a Ross mixer / emulsifier, model HSM-100LC (Hex) Ross Ross and Son Company. The IKA® mixer was run at 11,000 rpm and the Ross mixer was run at 7,000-8,000 rpm.

General Procedure for Preparing Aqueous-Polyurethane Dispersions

Prepolymers were prepared by mixing MDI, glycol (and DMPA if necessary) at 90 ° C. under nitrogen for 3-5 hours. The amount of excess NCO remaining after the coupling reaction was determined by titration. In the case of dilution of the prepolymer with a solvent, the reaction product is cooled to room temperature and then a solvent is added to typically prepare a 75% by weight solution. The prepolymer was introduced into the tube and added slowly through a pneumatic pump in a cooled aqueous solution containing a surfactant, and sometimes a base. The solids content of the dispersion is about 10-30%.

How to form gloves

In order to form the glove, the mold was immersed in the coagulant solution. This coagulant solution is typically 10-20% Ca (N0 ₃ ) ₂ and 0-10% CaCO ₃ . The mold was then dried at 100 ° C. for 5 minutes. This mold was then immersed in an aqueous polyurethane dispersion at 10-50 ° C. and then cooled to 10-40 ° C. Salt exudation was then effected by immersing the coated mold in water at 20-70 ° C. followed by drying at 90 ° C.-150 ° C. for 30 minutes. The glove was then removed from the mold.

[Example]

≪ Example 1 >

In a dry box, 156.4 g (0.624 mole) of MDI were mixed with 391 g (0.391 mole) of PTMEG-1000 glycol and 19.9 g (0.149 mole of 3.5% by weight of total weight) in a 3-neck round bottom flask. . The flask was then moved to the hood and equipped with an overhead stirrer. The mixture was stirred at 90 ° C. for 4 hours under nitrogen. Titration of the mixture indicated that the NCO content was 5.32%.

200 ml of MEK was added to the mixture to prepare a solution of 74% solids in MEK. At 0 ° C. the glycol / MEK solution was then slowly added through a caulking tube in 4 liters of 2% SDBS solution with 15 g of TEA. The ratio of TEA to DMPA was 1: 1. The dispersion was made with a Ross mixer and a small amount of precipitate was observed. After the precipitate was filtered off, a final 11.5% solids content dispersion was obtained. The particle size of the precipitate measured by Coulter N4MD analyzer was 1063 nm. The molecular weight of the resulting material was 237,000 as measured by GPC (relative to polystyrene standard).

Comparative Example A

The mixture was prepared as described in Example 1 above except that 1.7 g of NaHCO ₃ was used as the base without the addition of the SDBS surfactant. The ratio of NaHC0 ₃ to DMPA was 1: 1. No dispersion was produced.

Once again a similar dispersion was prepared and this time a solution of 2% by weight SDBS surfactant in NaHCO ₃ was added. A precipitate was observed. After the precipitate was filtered off an 8.2 wt% solids content dispersion was obtained. The film was cast but had little strength.

Comparative Example B

In a dry box 78 g (0.624 mole) of MDI were mixed with 360 g of PTMEG-1800 glycol and 16 g of DMPA (preparing 3.5% by weight of total weight) in a three-neck round bottom flask. The flask was then moved to the hood and equipped with an overhead stirrer. The mixture was stirred at 90 ° C. for 4 hours under nitrogen. Titration of the mixture indicated that the NCO content was 5.32%.

400 ml of MEK was added to the mixture. Then 204 g of glycol / MEK solution with 2.85 g of TEA at 0 ° C. were slowly added through a caulking tube in 1.1 liters of 2% SDBS solution. The ratio of TEA to DMPA was 1: 1. No dispersion was produced from this mixture.

When the same procedure was used except that NaHC0 ₃ was used as the base, a sponge-type polymer was formed.

Comparative Example C

The experiment described in Comparative Example B was conducted except that 30% EO / THF material (obtained from Sanyo) was used. When using 2% surfactant / TEA, no dispersion was prepared and a large amount of precipitate was observed.

No dispersion was prepared even when the experiment was performed as described in the paragraph above using 0.5% surfactant / NaHCO ₃ . Large amounts of precipitate were observed.

Comparative Example D

The procedure described in Example 1 above was followed except that a 1.25% surfactant / NaHC0 ₃ solution was used. A precipitate was observed. A 10.1% solids content dispersion was observed after the precipitate was filtered off. The film was cast after evaporating the water. The film exhibited insufficient elasticity.

Test Results of Articles Made from Aqueous Dispersions

The puncture strength of the glove prepared from the dispersion by the method described above was measured according to ASTM method F1342. The elongation and thickness of the material was measured. The puncture load was calculated as inches in lbs / thickness. The results are shown in Table 1 below.

Glove number Drilling load (lbs) Elongation (in) Thickness (in) Drilling load / thickness (lbs / thickness inch) Lycra (R) Polymer Gloves 1.20 0.4040 0.0038 320 CR100 Latex Baxter 0.71 0.5039 0.0087 82 Hypoclean Critical 0.66 0.4742 0.0077 85 Hippoline 100 0.77 0.5282 0.0085 91 Seti Clean Latex 0.61 0.4679 0.0077 79 CR10 Nitrile 1.40 0.4974 0.0049 287 Nitrile 1.45 0.2830 0.0047 311 Hippoline Nitrile 1.49 0.3387 0.0047 318 Nitrilon 1.77 0.3995 0.0049 363 Niprotect 529 1.70 0.4178 0.0042 407 Trilites 0.34 0.4488 0.0053 64 PVC 0.50 - 0.0064 80 DuPont Aq PUU 0.89 0.4929 0.0029 281

Tear strength of the glove produced by the present invention was measured using ASTM test D-624-98. This test requires cutting the film with a die and then tearing the sample by placing it in an Instron® device. The load on the kidney was recorded. Dies B and C were used. The specimen for die B was carved with a razor blade and the initial tear position was identified. Die C does not engrave with a sharp 90 degree corner as a location for tearing. The test results are shown in Table 2 below and indicate the tear strength (N / mm) per unit thickness.

Glove number Tear Strength, Die B (N / mm) Tear strength, Die C (N / mm) Lycra® Polymer Gloves 95.36 74.79 CR100 Latex 63.25 45.47 CR10 Nitrile 15.53 23.76 Nitrile 18.98 34.03 DuPont Aq.PUU --- 25.82

Claims (21)

Method for producing a film comprising the following steps:
(A) from repeating units derived from hydroxy-terminated copolymers prepared from (a) tetrahydrofuran and alkylene oxide or cyclic acetal or both alkylene oxide and cyclic acetal, and (b) from aromatic polyisocyanate Preparing a urea / urethane prepolymer comprising derived repeating units, the prepolymer is prepared without the use of additional chain extenders,
The urea / urethane prepolymer is of the formula -RN (R ² ) -C (O) -N (R ² ) -R ^1- (R is an aromatic hydrocarbon radical, R ¹ is an aliphatic hydrocarbon radical, R ² is H or Less than 2 mol% of urea units represented by the formula -C (O) -NH-R-,
The tetrahydrofuran is represented by the formula

Wherein one of R ⁴ is a C ₁ to C ₄ alkyl radical and the remaining R ⁴ is hydrogen or all R ⁴ is hydrogen;
(B) mixing the urea / urethane prepolymer with a water miscible organic solvent and an anionic surfactant to prepare a urea / urethane polymer dispersion; And
(C) forming a film from the urea / urethane polymer dispersion. The method of claim 1, wherein the alkylene oxide is selected from the group consisting of 1,2-propylene oxide and ethylene oxide. The method of claim 1, wherein the alkylene oxide is ethylene oxide. The process of claim 1 wherein each R ⁴ in tetrahydrofuran is hydrogen. The process of claim 1 wherein each R ⁴ in tetrahydrofuran is hydrogen, the hydroxy-terminated copolymer is prepared from alkylene oxide and the alkylene oxide is ethylene oxide. The method of claim 1, wherein the urea / urethane prepolymer further comprises repeating units derived from an ionic compound or a potential ionic compound. Method for producing a film comprising the following steps:
(A) preparing an ionomer urea / urethane prepolymer comprising (a) repeating units derived from aliphatic polyether polyols having a weight average molecular weight of 700 to 1500, and (b) repeating units derived from aromatic polyisocyanates. The prepolymer is prepared without the use of an additional chain extender,
The ionomer urea / urethane prepolymer is of formula -RN (R ² ) -C (O) -N (R ² ) -R ^1- (R is an aromatic C ₆ -C ₂₀ hydrocarbon radical, R ¹ is aliphatic C _1- A C ₂₀ hydrocarbon radical and R ² contains less than 2 mol% of a urea unit described by H or an amide group represented by the formula —C (O) —NH—R—;
(B) mixing the ionomer urea / urethane prepolymer with a water miscible organic solvent and an anionic surfactant to prepare an ionomer urea / urethane polymer dispersion; And
(C) forming a film from the ionomer urea / urethane polymer dispersion. 8. The polyether polyol of claim 7 wherein the polyether polyol is of the formula HO — [(CR ⁵ H) _m —O—] _n —H (R ⁵ is hydrogen, halogen or a C ₁ to C ₄ alkyl radical; m is 3 or 4 n is 8 to 20). The method for producing a film according to claim 8, wherein R ⁵ is hydrogen. The method for producing a film according to claim 7, wherein the weight average molecular weight of the polyether polyol is 900 to 1150. Method for producing a film comprising the following steps:
(A) preparing an ionomer urea / urethane prepolymer comprising (a) repeating units derived from aliphatic polyester polyols, and (b) repeating units derived from aromatic polyisocyanates, the prepolymer further comprising an additional chain Manufactured without the use of extenders,
The ionomer urea / urethane prepolymer is of formula -RN (R ² ) -C (O) -N (R ² ) -R ^1- (R is a C ₆ -C ₂₀ aromatic hydrocarbon radical, R ¹ is C ₁ -C ₂₀ aliphatic hydrocarbon radical, and R ² contains less than 2 mol% of a urea unit described by H or an amide group represented by the formula C (O) —NH—R—;
(B) mixing the ionomer urea / urethane prepolymer with a water miscible organic solvent and an anionic surfactant to prepare an ionomer urea / urethane polymer dispersion; And
(C) forming a film from the ionomer urea / urethane polymer dispersion. 12. The method of claim 7 or 11, wherein the ionomer urea / urethane prepolymer further comprises repeating units derived from an ionic compound or a potential ionic compound. 13. The compound according to claim 12, wherein the ionic compound or potential ionic compound represents a general formula (HO) _x R ⁷ (COOH) _y (R ⁷ represents a straight or branched hydrocarbon radical containing 1 to 12 carbon atoms, x and y each independently represent a value of 1 to 3). 13. The method of claim 12, wherein the ionic compound or potential ionic compound comprises 2,2 'dimethanol propionic acid. The process for producing a film according to claim 1, wherein the polyisocyanate is selected from the group consisting of toluene diisocyanate, methylene diphenyl diisocyanate and polymethylene polyphenylisocyanate. 12. The method of claim 11, wherein the polyester polyol is a dihydroxy-terminated polymer selected from the group consisting of ethylene adipate, butylene adipate, ethylene / butylene adipate, and mixtures thereof. The method for producing a film according to claim 1, wherein the urea / urethane polymer contains less than 1 mol% of the described urea units. The method for producing a film according to any one of claims 1 to 7, wherein the film is made in the form of a glove. 19. The method of claim 18, wherein the glove is not perforated or broken at the point of contact between the thumb and forefinger after dipping the thumb and forefinger into isopropyl alcohol and rubbing each other for a time of 30 to 60 seconds. The method of claim 1, wherein the step of forming the film comprises the following steps:
(A) immersing the mold in the coagulant solution;
(B) immersing the mold in the urea / urethane polymer dispersion;
(C) drying the mold; And
(D) peeling off the film from the mold. 19. The method of claim 18 wherein the step of making the film in the form of a glove comprises the following steps:
(A) dipping the glove mold into the coagulant solution;
(B) immersing the mold in the urea / urethane polymer dispersion;
(C) drying the mold to form a glove; And
(D) peeling off the glove from the mold.

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