Indian Patents. 268441:"AQUEOUS POLYURETHANE/POLYUREA DISPERSIONS"

Title of Invention	"AQUEOUS POLYURETHANE/POLYUREA DISPERSIONS"
Abstract	The present invention pertains to aqueous polyurethane-polyurea dispersions which are prepared by the acetone process using methyl acetate instead of ketones and are chain-extended using hydrazine or derivatives thereof, these dispersions having an improved stabilit y towards thermal yellowing and a relatively low residual hydrazine/hydrazine derivative content.

Full Text	AQUEOUS POLYURETHANE/POLYUREA DISPERSIONS The present invention pertains to aqueous polyurethane-polyurea dispersions which are prepared by the acetone process using methyl acetate instead of ketones and are chain-extended using hydrazine and/or derivatives thereof, these dispersions having an improved stability towards thermal yellowing and a relatively low residual hydrazine/hydrazine derivative content The preparation of aqueous polyurethane-polyurea dispersions by means of the acetone process is well established, being known for example from Prog Org Coat 9(1981) 281-340 In the process a prepolymer containing isocyanate groups is prepared in solution or, after the reaction has been accomplished, is dissolved in acetone or other solvents readily removable by distillation Subsequently the prepolymer solution is dispersed in water and a chain extension reaction is earned out, using polyamines The extension reaction may take place m part or else completely pnor to dispersing Finally the solvent is distilled off With regard to the problem of thermal yellowing it is known from US 5,137,967 and DE 10 2004 002 526 that the use of hydrazine or hydrazine hydrate for the chain extension, rather than pnmary or secondary amines, leads to polyurethanes having an improved thermal yellowing stability However, we have found, especially when using relatively unreactive isocyanates and acetone as solvent, that the hydrazine concentrations in the resulting polyurethane-polyurea dispersions are unacceptable, owing to the high toxicity of hydrazine Many other non-ketomc solvents are reactive towards isocyanates (e g alcohols, carboxylic acids), objectionable from a toxicological or ecological standpoint (e g benzene, halogenated solvents), or more difficult to distil off than acetone, owing to their higher boiling point For technical reasons it is not always possible, when preparing polyurethane-polyurea dispersions, to avoid a process using solvents As a consequence of this there continues to be a need to be able to prepare, using a solvent process, aqueous polyurethane-polyurea dispersions which are stable towards thermal yellowing and have low concentrations of non-polymerically attached hydrazine or derivatives thereof It has now been found that polyurethanes with improved thermal yellowmg stability and a lower residual hydrazine/hydrazine denvative content are obtained if, when prepanng polyurethane-polyurea dispersions, in contradiction to the conventional acetone process, the solvent used is methyl acetate, and the chain extension is earned out using hydrazine or denvatives thereof, a mixture with pnmary or secondary amines being possible but not preferred The invention accordingly provides a process for prepanng aqueous polyurethane-polyorea dispersions which are stable to thermal yellowing, by reaction of polyiso-cyanates, polymenc polyols or polymenc polyamines, or both, and isocyanate-reactive hydrophilicizing compounds to form an NCO-containing prepolymer, followed by a chain extension reaction with hydrazine or denvatives thereof, or both, charactenzed in that the reaction for preparing the prepolymer or the further chain extension reaction or else both reaction steps is or are carried out m the presence of methyl acetate The process is particularly suitable if A) first of all an NCO-containing polyurethane prepolymer is prepared by reacting Al) polyisocyanates with A2) polymenc polyols and/or polyamines having number-average molecular weights of 400 to 8000 g/mol, A3) if desired, low molecular weight polyalcohols, polyamines or amino alcohols, having number-average molecular weights of 17 to 400 g/mol, and A4) isocyanate-reactive, lonically, potentially lonically and/or nonionically hydrophilicizing compounds, A5) if desired, in plasticizers or solvents which boil above 100°C, which are non- ketonic and which are inert or only very slightly reactive towards isocyanate and hydrazine, A6) if desired, in methyl acetate. B) either the prepolymer obtained from step A is dissolved in a solvent A5) and/or A6) or, if the preparation has already been earned out in the presence of A5) and/or A6), the prepolymer solution is, where appropnate, diluted by further addition of solvents A5) and/or A6), and C) the remaining free NCO groups of the prepolymer are reacted with hydrazine or denvatives thereof so as to attain an anthmetic degree of chain extension of 40% to 150%, preferably 60% to 120%, more preferably 80% to 105%, and very preferably 85% to 100% The mvention further provides aqueous polyurethane-polyurea dispersions which are stable towards thermal yellowing and have a low residual hydrazine/hydrazine denvative content by this process Suitable polyisocyanates Al) of the formula X(NCO)p, in which p is a number from 1 to 4, preferably from 2 to 3, and X is an aliphatic, cycloaliphatic, aromatic or araliphatic hydrocarbon radical X is preferably an aliphatic hydrocarbon radical having 3 to 20 carbon atoms, a cycloaliphatic or aromatic hydrocarbon radical having 5 to 15 carbon atoms or an araliphatic hydrocarbon radical having 6 to 15 carbon atoms Examples of such dusocyanates are tetramethylene dusocyanate, hexamethylene dusocyanate, dodecamethylene dusocyanate, 1,4-dusocyanatocyclohexane, 1 -isocyanato-3,5,5-tnmethyl-5-isocyanatomethylcyclohexane (IPDI), 2,2-bis-(4-isocyanatocyclohexyl)propane, tnmethylhexane dusocyanate, 1,4-dusocyanatobenzene, 2,4-dusocyanatotoluene, 2,6-dusocyanatotoluene, 4,4'-dusocyanatodiphenylmethane, 2,4'-dusocyanatodiphenylmethane, p-xylylene dusocyanate, tetramethylxylylene dusocyanate (TMXDI), the isomers of 4,4'-dusocyanatodicyclohexylmethane such as the trans/trans, the cis/-cis and the cis/trans isomer, and mixtures of these compounds The advantage of increased resistance towards thermal yellowing and of the low residual hydrazine/hydrazine derivative content is particularly great in the case of isocyanates of low reactivity, such as araliphatic and aliphatic isocyanates Preference is given to 1,6-dusocyanatohexane (HDI), isophorone dusocyanate (IPDI), the isomers of 4,4'-dusocyanatodicyclohexylmethane, and mixtures of these compounds, particular preference is given to isophorone dusocyanate (IPDI), the isomers of 4,4'-dusocyanato-dicyclohexylmethane, and mixtures of these compounds Polymenc polyols or polyamines A2) come typically from the group of polycarbonates, polyesters, polyethers, polyacrylates, polyolefins and polysiloxanes, as are known from, for example, Ullmann's Encyclopedia of Industrial Chemistry 2005, DOI 10 1002/14356007 a21_665 pub2 "Polyurethanes", Chapter 3, W Fnedenchs Suitable polycarbonate polyols are those as may be obtained by, for example, reacting phosgene with an excess of polyhydnc alcohols Examples of suitable dihydnc alcohols include ethylene glycol, propane-1,2-diol, propane-1,3-diol, butane-1,3-diol, butene-l,4-diol, butyne-l,4-diol, pentane-l,5-diol, neopentyl glycol, 2-butyl-2-ethyl-1,3-propanediol, bis(hydroxymethyl)cyclohexanes such as 1,4-bis(hydroxyl-methyl)cyclohexane, 2-methylpropane-l,3-diol, methylpentanediols, and also diethylene glycol, triethylene glycol, tetraethylene glycol, polyethylene glycol, dipropylene glycol, polypropylene glycol, dibutylene glycol and polybutylene glycols Preferred alcohols are of the general formula H0-(CH2)x-0H, where x is a number from 1 to 20, preferably an even number from 2 to 20 Examples of such alcohols are ethylene glycol, butane-1,4-diol, hexane-l,6-diol, octane-1,8-diol and dodecane-1,12-diol Additionally preferred are neopentyl glycol and 2-butyl-2-ethyl-l,3-propanediol Proportionally it is also possible to use higher polyhydnc alcohols such as glycerol, tnmethylolpropane, 1,2,6-hexanetriol, 1,2,4-butanetriol, pentaerythritol, quinitol, mannitol and sorbitol Also suitable, furthermore, are polyester polyols, which are obtained by reacting polyhydnc alcohols with polybasic carboxylic acids In place of the free polycarboxylic acids It IS possible to use the corresponding polycarboxylic anhydndes or corresponding polycarboxylic esters of lower alcohols, or mixtures thereof, to prepare the polyester polyols The polycarboxylic acids may be aliphatic, cycloaliphatic, araliphatic, aromatic or heterocyclic and may where appropnate be substituted, by halogen atoms for example, and/or unsaturated Examples that may be mentioned thereof include the following subenc acid, azelaic acid, phthalic acid, isophthalic acid, phthalic anhydnde, tetrahydrophthahc anhydnde, hexahydrophthalic anhydnde, tetrachlorphthalic anhydnde, endomethylenetetrahydrophthalic anhydnde, glutanc anhydnde, maleic acid, maleic anhydnde, fumanc acid, dimenc fatty acids Preferred dicarboxylic acids of the general formula HOOC-(CH2)y-COOH, where y is a number from 1 to 20, preferably an even number from 2 to 20, such as succinic acid, adipic acid, sebacinic acid and dodecanedicarboxylic acid, for example Suitable polyhydnc alcohols, preferably diols, include the low molecular weight alcohols specified as synthesis components for the polycarbonate polyols Also suitable are lactone-based polyester diols, which are homopolymers or copolymers of lactones, preferably hydroxy 1-terminal adducts of lactones with suitable polyfunctional starter molecules Suitable lactones are preferably those denving from compounds of the general formula H0-(CH2)z-C00H, where z is a number from 1 to 20 and where one hydrogen atom of a methylene unit can also be substituted by a Ci to C4 alkyl radical Examples of e-caprolactone, P-propiolactone, y-butyrolactone and/or methyl-e-caprolactone, and mixtures thereof Examples of suitable starter components include the low molecular weight polyhydnc alcohols specified above as synthesis components for the polycarbonate polyols The corresponding polymers of €-caprolactone are particularly preferred Lower polyester diols or polyether diols as well can be used as starters for prepanng the lactone polymers In place of the polymers of lactones it is also possible to use the corresponding, chemically equivalent polycondensates of the hydroxyl carboxyhc acids corresponding to the lactones Likewise suitable as monomers are polyether diols They are obtainable in particular by addition polymenzation of ethylene oxide, propylene oxide, butylene oxide, tetrahydro-fiiran, styrene oxide, epichlorohydrine, or part-fluonnated or perfluormated denvatives of these compounds, with itself or with themselves, in the presence for example of BF3, or by addition reaction of these compounds, where appropnate in a mixture or in succession, with starter components containing reactive hydrogen atoms, such as alcohols or amines, examples being water, ethylene glycol, propane-1,2-diol, propane-1,3-diol, 1,2-bis(4-hydroxyphenyl)propane or aniline Likewise suitable as monomers are polyhydroxy olefins, preferably those having 2 terminal hydroxyl groups, such as a,(o-dihydroxypolybutadiene, a,co-dihydroxy-polymethacryhc esters or a,co-dihydroxypolyacrylic esters Such compounds are known for example from EP-A-0 622 378 Further suitable polyols are polyacetals, polysiloxanes and alkyd resins Suitable low molecular weight compounds A3) are the low molecular weight polyhydnc alcohols, preferably diols and tnols, specified above as synthesis components for the polycarbonate polyols Hydrophilicizing compounds according to A4) are all compounds which have at least one isocyanate-reactive group, preferably hydroxyl groups or ammo groups, and also at least one functionality which is lonically, potentially lonically and/or nonionically hydrophilicizing Examples of ionic and potentially ionic groups are -COOY, -SO3 Y, -PO(OY)2 (Y for example = hydrogen, NH4+, metal cation), -NR2, -NR3+ (R = hydrogen, alkyl, aryl) Examples of non-ionic hydrophilicizing groups are polyoxy-alkylene ethers Suitable hydrophilicizing compounds are known to the person skilled in the art and are specified and/or explained in DE 10 2004 002 526 in paragraphs [0032] and [0035] to [0039] The job of reaction with the remaining free NCO groups in accordance with C) is that of hydrazine and its denvatives These may be hydrazides (e g dicarboxylic dihydrazides) or monosubstituted or 1,2-disubstituted hydrazines of the formula (I) to (IV) (Formula Removed) in which Rl is an alkyl radical having 1 to 20 carbon atoms, an aryl radical having 5 to 20 carbon atoms or an arylalkyl radical having 6 to 20 carbon atoms, m is = 1, preferably 1 to 3, R2, R3 is hydrogen or has the same definition as Rl, R4 is an alkyl radical having 2 to 6 carbon atoms or an arylalkyl radical having 6 to 20 carbon atoms It is preferred to use hydrazine, hydrazine hydrates, aqueous hydrazine solution or dicarboxylic dihydrazides such as oxalic dihydrazide or adipic dihydrazide, for example Of particular preference are hydrazine hydrates and aqueous hydrazine solutions The amount used of components Al) in the process of the invention is preferably 7% to 45% and more preferably 10% to 35% by weight The amount used of components A2) in the process of the invention is preferably 50% to 91% and more preferably 60% to 90% by weight The amount used of components A3) in the process of the invention is preferably 0% to 30%, more preferably 0% to 15% and very preferably 0% to 8% by weight The amount used of components A4) in the process ot the invention is preferably 0% to 25%, more preferably 0% to 20% and very preferably 0% to 15% by weight The amount used of components A5) in the process of the invention is preferably 0% to 50%, more preferably 0% to 30% and very preferably 0% to 25% by weight The sum of the products Al) to A5) is 100% of the NCO-containmg prepolymer The process of the invention for preparing aqueous PU dispersions can be earned out in one or more stages in homogeneous phase or, in the case of multi-stage reaction, partly in disperse phase Following complete or partial polyaddition of Al)/-A6) there is a dispersing, emulsifying or dissolving step This may be followed by a further polyaddition or modification in disperse phase Typically, in step A) of the process, the constituents A2) to A4) and the polyisocyanate component Al) for the preparation of a polyurethane prepolymer, are included in whole or in part in an initial charge, which if desired is diluted with a solvent A5) and/or A6) and is heated to relatively high temperatures, preferably in the range from 50 to 120°C In the process of the invention it is additionally possible to include in the initial charge, or to meter in later on, the catalysts that are known for accelerating the isocyanate addition reaction, such as triethylamine, 1,4- diazabicyclo[2,2,2]octane, dibutyltin oxide, tin dioctoate or dibutyltin dilaurate, tin bis(2-ethylhexanoate) or other organometallic compounds Subsequently any of constituents Al) - A6) not added at the beginning of the reaction are metered in In the case of the preparation of the polyurethane prepolymer in step A) the molar amount-of-substance ratio of isocyanate groups to isocyanate-reactive groups is 1 0 to 3 5, preferably 1 1 to 3 0, more preferably 1 1 to 2 5 and very preferably 11-20 The reaction of components Al) - A4) to form the prepolymer is partial or complete, but preferably complete The degree of conversion is typically monitored by following the NCO content of the reaction mixture This can be done using either spectroscopic measurements, examples being infrared or near-infrared spectra, determinations of the refractive index, or else using chemical analyses, such as titrations, on samples taken In this way, polyurethane prepolymers containing free isocyanate groups are obtained, in bulk (without solvent) or in solution Dunng or after the preparation of the polyurethane prepolymers from Al) to A4), and if It has not already been earned out in the starting molecules, the anionically and/or catiomcally dispersing groups are converted partly or fully to the salt form In the case of anionic groups this is done using bases such as ammonia, ammonium carbonate or ammonium hydrogen carbonate, tnmethylamine, tnethylamine, tnbutylamine, diisopropylethylamine, dimethylethanolamine, diethylethanolamme, tnethanolamine, potassium hydroxide or sodium carbonate, preferably tnethylamine, tnethanolamine, dimethylethanolamine or dusopropylethylamine The molar amount of substance of the bases is between 50% and 150%, preferably between 75% and 125%, more preferably 85-115% of the amount of substance of the anionic groups In the case of cationic groups, dimethyl sulfate, succinic acid or flimanc acid is used Where only nonionically hydrophihcized compounds A4) with ether groups are used, the neutralization step is not needed Neutralization may also take place simultaneously with dispersion, with the dispersing water already containing the neutralizing agent Subsequently, in a further step of the process, step B), if it has not taken place or has taken place only partly in A), the resulting prepolymer is dissolved using the solvent A5) and/or A6) In step C) of the process the hydrazine and/or its denvates are reacted with the remaining isocyanate groups This chain extension/termination may be earned out either in solvent prior to dispersing, dunng dispersing, or in water after dispersing The degree of chain extension, in other words the equivalents ratio of the newly added reactive groups of the compounds used for chain extension in C) to free NCO groups of the prepolymer is typically between 50-200%, preferably between 60-120%, more preferably between 80-105% and very preferably between 85-100% Hydrazine and its denvatives can be used in C) optionally in dilution with water and/or the solvent A5) and/or A6) in the process of the invention, individually or in mixtures, with any sequence of addition being possible in pnnciple The PU dispersions of the invention are typically prepared either by introducing the dissolved prepolymer or the chain-extended polyurethane polymer into the dispersing water, where appropnate with strong sheanng, such as vigorous stimng, for example, or, conversely, the dispersing water is added to the prepolymer or polymer solutions It is preferred to add the water to the dissolved prepolymer The solvent A6) still present in the dispersions after the dispersing step is typically then removed distillatively The distillation is preferably earned out under reduced pressure Removal actually during dispersing is likewise possible The dispersions obtained in this way have a solids content of 10% to 70%, preferably 20% to 65% and more preferably 25% to 65% by weight Depending on degree of neutralization and ionic group content, the dispersion can be made very finely particulate, so that it has virtually the appearance of a solution, or alternatively, very coarsely particulate formulations are possible, and likewise have adequate stability The mvention further provides mixtures of the polyurethane-polyurea dispersions of the invention with other aqueous binders and crosslinkers which are used for producing coating matenals In this context it is also possible to use the auxilianes and additives known per se from coating technology, such as thickeners, fillers, pigments, waxes, texture agents, dyes, solvents, flow control assistance, and crosslinkers, for example The use of additives for reducmg the thermal yellowing is an additional possibility The mvention further provides coatings of the polyurethane-polyurea dispersions of the invention and/or their abovementioned mixtures on any desired substrates, such as metal, wood, glass, glass fibres, carbon fibres, stone, ceramic minerals, concrete, hard and flexible plastics of any of a very wide vanety of kinds, woven and non-woven textiles, leather, paper, hard fibres, straw and bitumen, for example, which prior to coating may also be provided with typical pnmer coats if desired The invention additionally provides the above-described coated substrates and articles manufactured from them EXAMPLES Determination of thermal yellowing 25 g of the polyurethane-polyurea dispersion are introduced into a glass dish (10x20 cm2) and dried at 60°C overnight A portion of the resulting film is placed on a glass plate and stored at 120°C for 168 h The discoloration is assessed by visual comparison of the samples Detection of hydrazine in polyurethane-polyurea dispersions The dispersion is diluted 1000 times To 5 ml of this dilute solution there are added 5 ml of Aquamerck® hydrazine (colorimeter determmation with 4-dimethylamino-benzaldehyde) A yellow coloration indicates hydrazine The determination of the effective particle diameter is earned out using the Particle Size Analyzer 90 Plus from Brookfield Instruments Corporation The determination of the viscosity of the dispersion is earned out using a DIN CUP 4 at 20°C, the efflux time is measured in seconds Example 1 (comparative) 254 0 g (124 5 mmol) of polycarbonatediol based on 3-methyl-l,5-pentanedio 1/1,6-hexanediol (Placed CD220PL, OHZ = 55), 12 1 g (90 mmol) of dimethylolpropionoic acid, 1 34 g (10 mmol) of tnmethylolpropane, 17 0 g (10 mmol) of Polyglykol Bl 1/50 (monofiinctional polyether based on ethylene oxide/propylene oxide) and 90 g of N-methylpyrrolidone are mixed at 65°C Subsequently a mixture of 50 4 g (228 mmol) of isophorone dusocyanate and 26 2 g (100 mmol) of 4,4'-dissocyanatodlcyclohexyl-methane is added and the mixtures are stirred at 90°C until the theoretical NCO value is reached After allowing the prepolymer to cool somewhat, 150 g of acetone are added, cooling is continued to 40-50°C, and 9 1 g (90 mmol) of tnethylamine are added Subsequently 713 g of cold water (5-10°C) are stirred in over the course of 10 minutes This low-viscosity dispersion is admixed over the course of 10 minutes with a solution of 5 35 g (89 mmol) of 1,2-ethylenediamine in 40 g of water, after which stirring takes place for 15 minutes The acetone is then removed by vacuum distillation (2 h at up to 40°C and approx 200 mbar) This gives a storage-stable dispersion having a solids content of 30% by weight, an effective particle diameter of 54 nm and a viscosity of 14 s Example 2 (comparative) The prepolymer is prepared as in Example 1 After allowing the prepolymer to cool somewhat, 150 g of acetone are added, cooling is continued to 40-50°C, and 9 1 g (90 mmol) of triethylamme are added Subsequently 713 g of cold water (5-10°C) are stirred in over the course of 10 minutes This low-viscosity dispersion is admixed over the course of 10 minutes with a solution of 4 45 g (89 mmol) of hydrazine monohydrate in 40 g of water, after which stirring takes place for 15 minutes The acetone is then removed by vacuum distillation (2 h at up to 40°C and approx 200 mbar) This gives a storage-stable dispersion having a solids content of 30% by weight, an effective particle diameter of 52 nm and a viscosity of 14 s Example 3 (comparative) The polyurethane-polyurea dispersion is prepared as in Example 2 However, instead of the 150 g of acetone, the same amount of ethyl acetate is used When water is added a dispersion of relatively high viscosity is obtained with a gel-like consistency, its viscosity dropping only slightly even when the hydrazine hydrate is added The distillation takes place at up to 40°C and approximately 200 mbar In the course of the distillation there is a marked drop in the viscosity of the dispersion After 2 h there is still a strong odour perceptible, after 4 h only a slight odour of ethyl acetate A storage-stable dispersion is obtained which has a solids content of 30% by weight, an effective particle diameter of 90 nm and a viscosity of 18 s Example 4 (inventive) The polyurethane-polyurea dispersion is prepared as in Example 2 However, the 150 g of acetone are replaced by the same amount of methyl acetate This gives a storage-stable dispersion having a solids content of 30% by weight, an effective particle diameter of 48 nm and a viscosity of 14 s Example 5 (inventive) 403 g (204 mmol) of polycaprolactonediol (OHZ = 56 8), 105 1 g (103 mmol) of polypropylene glycol (OHZ = 110), 34 3 g (256 mmol) of dimethylolpropiomc acid and 17 4 g (100 mmol) of adipic dihydrazide are introduced at 60°C and 300 g of methyl acetate and 0 1 g of dibutyltin dilaurate are added Subsequently 194 0 g (878 mmol) of isophorone dusocyanates are added and the mixture is stirred under reflux until the theoretical NCO value is reached This prepolymer is cooled to 40-50°C and then 25 9 g (256 mmol) of triethylamine are added Then 1200 g of cold water (5-10°C) are stirred in over the course of 10 minutes This dispersion is admixed over the course of 10 minutes with a solution of 10 2 g (204 mmol) of hydrazine monohydrate in 40 g of water, and stimng takes place for 15 minutes This is followed by the removal of the methyl acetate by vacuum distillation This gives a storage-stable dispersion having a solids content of 32 5% by weight, an effective particle diameter of 50 nm and a viscosity of 14 s Evaluation of results In comparison to inventive Example 4, comparative Example 1 shows a much more severe thermal yellowing With comparative Example 2, in contrast to inventive Example 4, hydrazine can be detected With comparative Example 3, in contrast to comparative Example 2, there is no hydrazine detectable, and the thermal yellowing is similar to that for inventive Example 4 However, distinct processing disadvantages are in evidence as compared with inventive Example 4 For instance, the viscosity of the dispersion prior to distillation imposes significantly more exacting requirements on the apparatus and is possibly no longer manageable on the production scale Moreover, the removal of the ethyl acetate takes significantly greater time and energy than in the case of acetone or methyl acetate As compared with inventive Example 4, the viscosity of the dispersion is increased and the effective particle diameter is significantly enlarged, this being clearly perceptible to the naked eye and leading to performance disadvantages on application, such as a lower depth of penetration into absorbent substrates, for example In processing terms, Example 4 and comparative Example 2 are virtually identical, with the consequence that methyl acetate does not carry any disadvantages as compared with acetone Example 5 shows thermal yellowing at a low level similar to that of Example 4 No significant amounts of hydrazine are detectable. WE CLAIMS :- 1. Process for preparing aqueous polyurethane-polyurea dispersions which are stable to thermal yellowing, by reaction of polyisocyanates, polymeric polyols or polymeric polyamines, or both, and isocyanate-reactive hydrophilicizing compounds to form an NCO-containing prepolymer, followed by a chain extension reaction with hydrazine or derivatives thereof, or both, characterized in that the reaction for preparing the prepolymer or the further chain extension reaction or else both reaction steps is or are carried out in the presence of methyl acetate. 2. Process according to Claim 1, characterized in that A) first of all an NCO-containing polyurethane prepolymer is prepared by reacting Al) polyisocyanates with A2) polymeric polyols and/or polyamines having number-average molecular weights of 400 to 8000 g/mol, A3) if desired, low molecular weight polyalcohols, polyamines or amino alcohols, having number-average molecular weights of 17 to 400 g/mol, and A4) isocyanate-reactive, ionically, potentially ionically and/or nonionically hydrophilicizing compounds, A5) if desired, in plasticizers or solvents which boil above 100°C, which are non- ketonic and which are inert or only very slightly reactive towards isocyanate and hydrazine, A6) if desired, in methyl acetate, B) either the prepolyner obtained from step A is dissolved in a solvent A5) and/or A6) or, if the preparation has already been carried out dissolved in the presence of A5) and/or A6), the prepolymer solution is, where appropriate, dissolved diluted by fiirther addition of solvents A5 and/or A6, and C) the remaining free NCO groups of the prepolymer are reacted with hydrazine or derivatives thereof so as to attain an arithmetic degree of chain extension of 40% to 150%. 3. Process according to Claim 2, characterized in that an arithmetic degree of chain extension of 60% to 120% is attained. 4. Process according to Claim 3, characterized in that an arithmetic degree of chain extension of 80% to 105% is attained. 5. Process according to Claim 4, characterized in that an arithmetic degree of chain extension of 85% to 100% is attained. 6. Process according to Claims 1 to 5, characterized in that the chain extenders are hydrazides or monosubstituted or 1,2-disubstituted hydrazines of the formula (I) to (IV) (Formula Removed) in which Rl is an alkyl radical having 1 to 20 carbon atoms, an aryl radical having 5 to 20 carbon atoms or an arylalkyl radical having 6 to 20 carbon atoms, m is = 1, R2, R3 is hydrogen or has the same definition as Rl, R4 is an alkyl radical having 2 to 6 carbon atoms or an arylalkyl radical having 6 to 20 carbon atoms. 7. Process according to Claim 6, characterized in that m is 1 to 3 is, and R4 is an alkyl radical having 2 to 6 carbon atoms. 8. Process according to Claim 7, characterized in that the chain extenders are hydrazine hydrates, aqueous hydrazine solution or dicarboxylic dihydrazides. 9. Process according to Claim 8, characterized in that the chain extenders are hydrazine hydrates or aqueous hydrazine solution. 10. Aqueous polyurethane-polyurea dispersions stable towards thermal yellowing, obtainable by the process according to Claims 1 to 9. 11.. Coatings, adhesive bonds, sealants and/or mouldings obtainable from polyurethane/polyurea dispersions according to Claim H-. 10. 12. Substrates coated with coatings according to Claim 11.

Full Text

AQUEOUS POLYURETHANE/POLYUREA DISPERSIONS
The present invention pertains to aqueous polyurethane-polyurea dispersions which are prepared by the acetone process using methyl acetate instead of ketones and are chain-extended using hydrazine and/or derivatives thereof, these dispersions having an improved stability towards thermal yellowing and a relatively low residual hydrazine/hydrazine derivative content
The preparation of aqueous polyurethane-polyurea dispersions by means of the acetone process is well established, being known for example from Prog Org Coat 9(1981) 281-340 In the process a prepolymer containing isocyanate groups is prepared in solution or, after the reaction has been accomplished, is dissolved in acetone or other solvents readily removable by distillation Subsequently the prepolymer solution is dispersed in water and a chain extension reaction is earned out, using polyamines The extension reaction may take place m part or else completely pnor to dispersing Finally the solvent is distilled off
With regard to the problem of thermal yellowing it is known from US 5,137,967 and DE 10 2004 002 526 that the use of hydrazine or hydrazine hydrate for the chain extension, rather than pnmary or secondary amines, leads to polyurethanes having an improved thermal yellowing stability However, we have found, especially when using relatively unreactive isocyanates and acetone as solvent, that the hydrazine concentrations in the resulting polyurethane-polyurea dispersions are unacceptable, owing to the high toxicity of hydrazine
Many other non-ketomc solvents are reactive towards isocyanates (e g alcohols, carboxylic acids), objectionable from a toxicological or ecological standpoint (e g benzene, halogenated solvents), or more difficult to distil off than acetone, owing to their higher boiling point
For technical reasons it is not always possible, when preparing polyurethane-polyurea dispersions, to avoid a process using solvents As a consequence of this there continues
to be a need to be able to prepare, using a solvent process, aqueous polyurethane-polyurea dispersions which are stable towards thermal yellowing and have low concentrations of non-polymerically attached hydrazine or derivatives thereof
It has now been found that polyurethanes with improved thermal yellowmg stability and a lower residual hydrazine/hydrazine denvative content are obtained if, when prepanng polyurethane-polyurea dispersions, in contradiction to the conventional acetone process, the solvent used is methyl acetate, and the chain extension is earned out using hydrazine or denvatives thereof, a mixture with pnmary or secondary amines being possible but not preferred
The invention accordingly provides a process for prepanng aqueous polyurethane-polyorea dispersions which are stable to thermal yellowing, by reaction of polyiso-cyanates, polymenc polyols or polymenc polyamines, or both, and isocyanate-reactive hydrophilicizing compounds to form an NCO-containing prepolymer, followed by a chain extension reaction with hydrazine or denvatives thereof, or both, charactenzed in that the reaction for preparing the prepolymer or the further chain extension reaction or else both reaction steps is or are carried out m the presence of methyl acetate
The process is particularly suitable if
A) first of all an NCO-containing polyurethane prepolymer is prepared by reacting
Al) polyisocyanates with
A2) polymenc polyols and/or polyamines having number-average molecular weights
of 400 to 8000 g/mol, A3) if desired, low molecular weight polyalcohols, polyamines or amino alcohols,
having number-average molecular weights of 17 to 400 g/mol, and A4) isocyanate-reactive, lonically, potentially lonically and/or nonionically
hydrophilicizing compounds, A5) if desired, in plasticizers or solvents which boil above 100°C, which are non-
ketonic and which are inert or only very slightly reactive towards isocyanate and
hydrazine, A6) if desired, in methyl acetate.
B) either the prepolymer obtained from step A is dissolved in a solvent A5) and/or A6) or, if the preparation has already been earned out in the presence of A5) and/or A6), the prepolymer solution is, where appropnate, diluted by further addition of solvents A5) and/or A6), and
C) the remaining free NCO groups of the prepolymer are reacted with hydrazine or denvatives thereof so as to attain an anthmetic degree of chain extension of 40% to 150%, preferably 60% to 120%, more preferably 80% to 105%, and very preferably 85% to 100%
The mvention further provides aqueous polyurethane-polyurea dispersions which are stable towards thermal yellowing and have a low residual hydrazine/hydrazine denvative content by this process
Suitable polyisocyanates Al) of the formula X(NCO)p, in which p is a number from 1 to 4, preferably from 2 to 3, and X is an aliphatic, cycloaliphatic, aromatic or araliphatic hydrocarbon radical X is preferably an aliphatic hydrocarbon radical having 3 to 20 carbon atoms, a cycloaliphatic or aromatic hydrocarbon radical having 5 to 15 carbon atoms or an araliphatic hydrocarbon radical having 6 to 15 carbon atoms
Examples of such dusocyanates are tetramethylene dusocyanate, hexamethylene dusocyanate, dodecamethylene dusocyanate, 1,4-dusocyanatocyclohexane, 1 -isocyanato-3,5,5-tnmethyl-5-isocyanatomethylcyclohexane (IPDI), 2,2-bis-(4-isocyanatocyclohexyl)propane, tnmethylhexane dusocyanate, 1,4-dusocyanatobenzene, 2,4-dusocyanatotoluene, 2,6-dusocyanatotoluene, 4,4'-dusocyanatodiphenylmethane, 2,4'-dusocyanatodiphenylmethane, p-xylylene dusocyanate, tetramethylxylylene dusocyanate (TMXDI), the isomers of 4,4'-dusocyanatodicyclohexylmethane such as the trans/trans, the cis/-cis and the cis/trans isomer, and mixtures of these compounds
The advantage of increased resistance towards thermal yellowing and of the low residual hydrazine/hydrazine derivative content is particularly great in the case of isocyanates of low reactivity, such as araliphatic and aliphatic isocyanates Preference is given to 1,6-dusocyanatohexane (HDI), isophorone dusocyanate (IPDI), the isomers of 4,4'-dusocyanatodicyclohexylmethane, and mixtures of these compounds, particular
preference is given to isophorone dusocyanate (IPDI), the isomers of 4,4'-dusocyanato-dicyclohexylmethane, and mixtures of these compounds
Polymenc polyols or polyamines A2) come typically from the group of polycarbonates, polyesters, polyethers, polyacrylates, polyolefins and polysiloxanes, as are known from, for example, Ullmann's Encyclopedia of Industrial Chemistry 2005, DOI 10 1002/14356007 a21_665 pub2 "Polyurethanes", Chapter 3, W Fnedenchs
Suitable polycarbonate polyols are those as may be obtained by, for example, reacting phosgene with an excess of polyhydnc alcohols Examples of suitable dihydnc alcohols include ethylene glycol, propane-1,2-diol, propane-1,3-diol, butane-1,3-diol, butene-l,4-diol, butyne-l,4-diol, pentane-l,5-diol, neopentyl glycol, 2-butyl-2-ethyl-1,3-propanediol, bis(hydroxymethyl)cyclohexanes such as 1,4-bis(hydroxyl-methyl)cyclohexane, 2-methylpropane-l,3-diol, methylpentanediols, and also diethylene glycol, triethylene glycol, tetraethylene glycol, polyethylene glycol, dipropylene glycol, polypropylene glycol, dibutylene glycol and polybutylene glycols
Preferred alcohols are of the general formula H0-(CH2)x-0H, where x is a number from 1 to 20, preferably an even number from 2 to 20 Examples of such alcohols are ethylene glycol, butane-1,4-diol, hexane-l,6-diol, octane-1,8-diol and dodecane-1,12-diol Additionally preferred are neopentyl glycol and 2-butyl-2-ethyl-l,3-propanediol Proportionally it is also possible to use higher polyhydnc alcohols such as glycerol, tnmethylolpropane, 1,2,6-hexanetriol, 1,2,4-butanetriol, pentaerythritol, quinitol, mannitol and sorbitol
Also suitable, furthermore, are polyester polyols, which are obtained by reacting polyhydnc alcohols with polybasic carboxylic acids In place of the free polycarboxylic acids It IS possible to use the corresponding polycarboxylic anhydndes or corresponding polycarboxylic esters of lower alcohols, or mixtures thereof, to prepare the polyester polyols The polycarboxylic acids may be aliphatic, cycloaliphatic, araliphatic, aromatic or heterocyclic and may where appropnate be substituted, by halogen atoms for example, and/or unsaturated Examples that may be mentioned thereof include the following subenc acid, azelaic acid, phthalic acid, isophthalic acid, phthalic anhydnde,
tetrahydrophthahc anhydnde, hexahydrophthalic anhydnde, tetrachlorphthalic anhydnde, endomethylenetetrahydrophthalic anhydnde, glutanc anhydnde, maleic acid, maleic anhydnde, fumanc acid, dimenc fatty acids Preferred dicarboxylic acids of the general formula HOOC-(CH2)y-COOH, where y is a number from 1 to 20, preferably an even number from 2 to 20, such as succinic acid, adipic acid, sebacinic acid and dodecanedicarboxylic acid, for example Suitable polyhydnc alcohols, preferably diols, include the low molecular weight alcohols specified as synthesis components for the polycarbonate polyols
Also suitable are lactone-based polyester diols, which are homopolymers or copolymers of lactones, preferably hydroxy 1-terminal adducts of lactones with suitable polyfunctional starter molecules Suitable lactones are preferably those denving from compounds of the general formula H0-(CH2)z-C00H, where z is a number from 1 to 20 and where one hydrogen atom of a methylene unit can also be substituted by a Ci to C4
alkyl radical Examples of e-caprolactone, P-propiolactone, y-butyrolactone and/or
methyl-e-caprolactone, and mixtures thereof Examples of suitable starter components include the low molecular weight polyhydnc alcohols specified above as synthesis
components for the polycarbonate polyols The corresponding polymers of €-caprolactone are particularly preferred Lower polyester diols or polyether diols as well can be used as starters for prepanng the lactone polymers In place of the polymers of lactones it is also possible to use the corresponding, chemically equivalent polycondensates of the hydroxyl carboxyhc acids corresponding to the lactones
Likewise suitable as monomers are polyether diols They are obtainable in particular by addition polymenzation of ethylene oxide, propylene oxide, butylene oxide, tetrahydro-fiiran, styrene oxide, epichlorohydrine, or part-fluonnated or perfluormated denvatives of these compounds, with itself or with themselves, in the presence for example of BF3, or by addition reaction of these compounds, where appropnate in a mixture or in succession, with starter components containing reactive hydrogen atoms, such as alcohols or amines, examples being water, ethylene glycol, propane-1,2-diol, propane-1,3-diol, 1,2-bis(4-hydroxyphenyl)propane or aniline
Likewise suitable as monomers are polyhydroxy olefins, preferably those having 2 terminal hydroxyl groups, such as a,(o-dihydroxypolybutadiene, a,co-dihydroxy-polymethacryhc esters or a,co-dihydroxypolyacrylic esters Such compounds are known for example from EP-A-0 622 378 Further suitable polyols are polyacetals, polysiloxanes and alkyd resins
Suitable low molecular weight compounds A3) are the low molecular weight polyhydnc alcohols, preferably diols and tnols, specified above as synthesis components for the polycarbonate polyols
Hydrophilicizing compounds according to A4) are all compounds which have at least one isocyanate-reactive group, preferably hydroxyl groups or ammo groups, and also at least one functionality which is lonically, potentially lonically and/or nonionically hydrophilicizing Examples of ionic and potentially ionic groups are -COOY, -SO3 Y, -PO(OY)2 (Y for example = hydrogen, NH4+, metal cation), -NR2, -NR3+ (R = hydrogen, alkyl, aryl) Examples of non-ionic hydrophilicizing groups are polyoxy-alkylene ethers Suitable hydrophilicizing compounds are known to the person skilled in the art and are specified and/or explained in DE 10 2004 002 526 in paragraphs [0032] and [0035] to [0039]
The job of reaction with the remaining free NCO groups in accordance with C) is that of hydrazine and its denvatives These may be hydrazides (e g dicarboxylic dihydrazides) or monosubstituted or 1,2-disubstituted hydrazines of the formula (I) to (IV)
(Formula Removed)
in which
Rl is an alkyl radical having 1 to 20 carbon atoms, an aryl radical having 5 to 20
carbon atoms or an arylalkyl radical having 6 to 20 carbon atoms,
m is = 1, preferably 1 to 3,
R2, R3 is hydrogen or has the same definition as Rl,
R4 is an alkyl radical having 2 to 6 carbon atoms or an arylalkyl radical having 6
to 20 carbon atoms
It is preferred to use hydrazine, hydrazine hydrates, aqueous hydrazine solution or dicarboxylic dihydrazides such as oxalic dihydrazide or adipic dihydrazide, for example Of particular preference are hydrazine hydrates and aqueous hydrazine solutions
The amount used of components Al) in the process of the invention is preferably 7% to 45% and more preferably 10% to 35% by weight
The amount used of components A2) in the process of the invention is preferably 50% to 91% and more preferably 60% to 90% by weight
The amount used of components A3) in the process of the invention is preferably 0% to 30%, more preferably 0% to 15% and very preferably 0% to 8% by weight
The amount used of components A4) in the process ot the invention is preferably 0% to 25%, more preferably 0% to 20% and very preferably 0% to 15% by weight
The amount used of components A5) in the process of the invention is preferably 0% to 50%, more preferably 0% to 30% and very preferably 0% to 25% by weight
The sum of the products Al) to A5) is 100% of the NCO-containmg prepolymer
The process of the invention for preparing aqueous PU dispersions can be earned out in one or more stages in homogeneous phase or, in the case of multi-stage reaction, partly in disperse phase Following complete or partial polyaddition of Al)/-A6) there is a dispersing, emulsifying or dissolving step This may be followed by a further polyaddition or modification in disperse phase
Typically, in step A) of the process, the constituents A2) to A4) and the polyisocyanate component Al) for the preparation of a polyurethane prepolymer, are included in whole or in part in an initial charge, which if desired is diluted with a solvent A5) and/or A6) and is heated to relatively high temperatures, preferably in the range from 50 to 120°C
In the process of the invention it is additionally possible to include in the initial charge, or to meter in later on, the catalysts that are known for accelerating the isocyanate addition reaction, such as triethylamine, 1,4- diazabicyclo[2,2,2]octane, dibutyltin oxide, tin dioctoate or dibutyltin dilaurate, tin bis(2-ethylhexanoate) or other organometallic compounds
Subsequently any of constituents Al) - A6) not added at the beginning of the reaction are metered in
In the case of the preparation of the polyurethane prepolymer in step A) the molar amount-of-substance ratio of isocyanate groups to isocyanate-reactive groups is 1 0 to 3 5, preferably 1 1 to 3 0, more preferably 1 1 to 2 5 and very preferably 11-20
The reaction of components Al) - A4) to form the prepolymer is partial or complete, but preferably complete The degree of conversion is typically monitored by following the NCO content of the reaction mixture This can be done using either spectroscopic measurements, examples being infrared or near-infrared spectra, determinations of the refractive index, or else using chemical analyses, such as titrations, on samples taken In this way, polyurethane prepolymers containing free isocyanate groups are obtained, in bulk (without solvent) or in solution
Dunng or after the preparation of the polyurethane prepolymers from Al) to A4), and if It has not already been earned out in the starting molecules, the anionically and/or catiomcally dispersing groups are converted partly or fully to the salt form In the case of anionic groups this is done using bases such as ammonia, ammonium carbonate or ammonium hydrogen carbonate, tnmethylamine, tnethylamine, tnbutylamine, diisopropylethylamine, dimethylethanolamine, diethylethanolamme, tnethanolamine, potassium hydroxide or sodium carbonate, preferably tnethylamine, tnethanolamine,
dimethylethanolamine or dusopropylethylamine The molar amount of substance of the bases is between 50% and 150%, preferably between 75% and 125%, more preferably 85-115% of the amount of substance of the anionic groups In the case of cationic groups, dimethyl sulfate, succinic acid or flimanc acid is used Where only nonionically hydrophihcized compounds A4) with ether groups are used, the neutralization step is not needed Neutralization may also take place simultaneously with dispersion, with the dispersing water already containing the neutralizing agent
Subsequently, in a further step of the process, step B), if it has not taken place or has taken place only partly in A), the resulting prepolymer is dissolved using the solvent A5) and/or A6)
In step C) of the process the hydrazine and/or its denvates are reacted with the remaining isocyanate groups This chain extension/termination may be earned out either in solvent prior to dispersing, dunng dispersing, or in water after dispersing
The degree of chain extension, in other words the equivalents ratio of the newly added reactive groups of the compounds used for chain extension in C) to free NCO groups of the prepolymer is typically between 50-200%, preferably between 60-120%, more preferably between 80-105% and very preferably between 85-100%
Hydrazine and its denvatives can be used in C) optionally in dilution with water and/or the solvent A5) and/or A6) in the process of the invention, individually or in mixtures, with any sequence of addition being possible in pnnciple
The PU dispersions of the invention are typically prepared either by introducing the dissolved prepolymer or the chain-extended polyurethane polymer into the dispersing water, where appropnate with strong sheanng, such as vigorous stimng, for example, or, conversely, the dispersing water is added to the prepolymer or polymer solutions It is preferred to add the water to the dissolved prepolymer

The solvent A6) still present in the dispersions after the dispersing step is typically then removed distillatively The distillation is preferably earned out under reduced pressure Removal actually during dispersing is likewise possible
The dispersions obtained in this way have a solids content of 10% to 70%, preferably 20% to 65% and more preferably 25% to 65% by weight
Depending on degree of neutralization and ionic group content, the dispersion can be made very finely particulate, so that it has virtually the appearance of a solution, or alternatively, very coarsely particulate formulations are possible, and likewise have adequate stability
The mvention further provides mixtures of the polyurethane-polyurea dispersions of the invention with other aqueous binders and crosslinkers which are used for producing coating matenals In this context it is also possible to use the auxilianes and additives known per se from coating technology, such as thickeners, fillers, pigments, waxes, texture agents, dyes, solvents, flow control assistance, and crosslinkers, for example The use of additives for reducmg the thermal yellowing is an additional possibility
The mvention further provides coatings of the polyurethane-polyurea dispersions of the invention and/or their abovementioned mixtures on any desired substrates, such as metal, wood, glass, glass fibres, carbon fibres, stone, ceramic minerals, concrete, hard and flexible plastics of any of a very wide vanety of kinds, woven and non-woven textiles, leather, paper, hard fibres, straw and bitumen, for example, which prior to coating may also be provided with typical pnmer coats if desired
The invention additionally provides the above-described coated substrates and articles manufactured from them
EXAMPLES
Determination of thermal yellowing
25 g of the polyurethane-polyurea dispersion are introduced into a glass dish (10x20 cm2) and dried at 60°C overnight A portion of the resulting film is placed on a glass plate and stored at 120°C for 168 h The discoloration is assessed by visual comparison of the samples
Detection of hydrazine in polyurethane-polyurea dispersions
The dispersion is diluted 1000 times To 5 ml of this dilute solution there are added 5 ml of Aquamerck® hydrazine (colorimeter determmation with 4-dimethylamino-benzaldehyde) A yellow coloration indicates hydrazine
The determination of the effective particle diameter is earned out using the Particle Size Analyzer 90 Plus from Brookfield Instruments Corporation
The determination of the viscosity of the dispersion is earned out using a DIN CUP 4 at 20°C, the efflux time is measured in seconds
Example 1 (comparative)
254 0 g (124 5 mmol) of polycarbonatediol based on 3-methyl-l,5-pentanedio 1/1,6-hexanediol (Placed CD220PL, OHZ = 55), 12 1 g (90 mmol) of dimethylolpropionoic acid, 1 34 g (10 mmol) of tnmethylolpropane, 17 0 g (10 mmol) of Polyglykol Bl 1/50 (monofiinctional polyether based on ethylene oxide/propylene oxide) and 90 g of N-methylpyrrolidone are mixed at 65°C Subsequently a mixture of 50 4 g (228 mmol) of isophorone dusocyanate and 26 2 g (100 mmol) of 4,4'-dissocyanatodlcyclohexyl-methane is added and the mixtures are stirred at 90°C until the theoretical NCO value is reached After allowing the prepolymer to cool somewhat, 150 g of acetone are added, cooling is continued to 40-50°C, and 9 1 g (90 mmol) of tnethylamine are added Subsequently 713 g of cold water (5-10°C) are stirred in over the course of 10 minutes This low-viscosity dispersion is admixed over the course of 10 minutes with a solution of 5 35 g (89 mmol) of 1,2-ethylenediamine in 40 g of water, after which stirring takes place for 15 minutes The acetone is then removed by vacuum distillation (2 h at up to
40°C and approx 200 mbar) This gives a storage-stable dispersion having a solids content of 30% by weight, an effective particle diameter of 54 nm and a viscosity of 14 s
Example 2 (comparative)
The prepolymer is prepared as in Example 1 After allowing the prepolymer to cool somewhat, 150 g of acetone are added, cooling is continued to 40-50°C, and 9 1 g (90 mmol) of triethylamme are added Subsequently 713 g of cold water (5-10°C) are stirred in over the course of 10 minutes This low-viscosity dispersion is admixed over the course of 10 minutes with a solution of 4 45 g (89 mmol) of hydrazine monohydrate in 40 g of water, after which stirring takes place for 15 minutes The acetone is then removed by vacuum distillation (2 h at up to 40°C and approx 200 mbar) This gives a storage-stable dispersion having a solids content of 30% by weight, an effective particle diameter of 52 nm and a viscosity of 14 s
Example 3 (comparative)
The polyurethane-polyurea dispersion is prepared as in Example 2 However, instead of the 150 g of acetone, the same amount of ethyl acetate is used When water is added a dispersion of relatively high viscosity is obtained with a gel-like consistency, its viscosity dropping only slightly even when the hydrazine hydrate is added The distillation takes place at up to 40°C and approximately 200 mbar In the course of the distillation there is a marked drop in the viscosity of the dispersion After 2 h there is still a strong odour perceptible, after 4 h only a slight odour of ethyl acetate A storage-stable dispersion is obtained which has a solids content of 30% by weight, an effective particle diameter of 90 nm and a viscosity of 18 s
Example 4 (inventive)
The polyurethane-polyurea dispersion is prepared as in Example 2 However, the 150 g of acetone are replaced by the same amount of methyl acetate This gives a storage-stable dispersion having a solids content of 30% by weight, an effective particle diameter of 48 nm and a viscosity of 14 s
Example 5 (inventive)
403 g (204 mmol) of polycaprolactonediol (OHZ = 56 8), 105 1 g (103 mmol) of polypropylene glycol (OHZ = 110), 34 3 g (256 mmol) of dimethylolpropiomc acid and 17 4 g (100 mmol) of adipic dihydrazide are introduced at 60°C and 300 g of methyl acetate and 0 1 g of dibutyltin dilaurate are added Subsequently 194 0 g (878 mmol) of isophorone dusocyanates are added and the mixture is stirred under reflux until the theoretical NCO value is reached This prepolymer is cooled to 40-50°C and then 25 9 g (256 mmol) of triethylamine are added Then 1200 g of cold water (5-10°C) are stirred in over the course of 10 minutes This dispersion is admixed over the course of 10 minutes with a solution of 10 2 g (204 mmol) of hydrazine monohydrate in 40 g of water, and stimng takes place for 15 minutes This is followed by the removal of the methyl acetate by vacuum distillation This gives a storage-stable dispersion having a solids content of 32 5% by weight, an effective particle diameter of 50 nm and a viscosity of 14 s
Evaluation of results
In comparison to inventive Example 4, comparative Example 1 shows a much more severe thermal yellowing
With comparative Example 2, in contrast to inventive Example 4, hydrazine can be detected
With comparative Example 3, in contrast to comparative Example 2, there is no hydrazine detectable, and the thermal yellowing is similar to that for inventive Example 4 However, distinct processing disadvantages are in evidence as compared with inventive Example 4 For instance, the viscosity of the dispersion prior to distillation imposes significantly more exacting requirements on the apparatus and is possibly no longer manageable on the production scale Moreover, the removal of the ethyl acetate takes significantly greater time and energy than in the case of acetone or methyl acetate As compared with inventive Example 4, the viscosity of the dispersion is increased and the effective particle diameter is significantly enlarged, this being clearly perceptible to the naked eye and leading to performance disadvantages on application, such as a lower depth of penetration into absorbent substrates, for example
In processing terms, Example 4 and comparative Example 2 are virtually identical, with the consequence that methyl acetate does not carry any disadvantages as compared with acetone
Example 5 shows thermal yellowing at a low level similar to that of Example 4 No significant amounts of hydrazine are detectable.

WE CLAIMS :-
1. Process for preparing aqueous polyurethane-polyurea dispersions which are stable to thermal yellowing, by reaction of polyisocyanates, polymeric polyols or polymeric polyamines, or both, and isocyanate-reactive hydrophilicizing compounds to form an NCO-containing prepolymer, followed by a chain extension reaction with hydrazine or derivatives thereof, or both, characterized in that the reaction for preparing the prepolymer or the further chain extension reaction or else both reaction steps is or are carried out in the presence of methyl acetate.
2. Process according to Claim 1, characterized in that
A) first of all an NCO-containing polyurethane prepolymer is prepared by
reacting
Al) polyisocyanates with
A2) polymeric polyols and/or polyamines having number-average molecular
weights of 400 to 8000 g/mol, A3) if desired, low molecular weight polyalcohols, polyamines or amino
alcohols, having number-average molecular weights of 17 to 400 g/mol, and A4) isocyanate-reactive, ionically, potentially ionically and/or nonionically
hydrophilicizing compounds, A5) if desired, in plasticizers or solvents which boil above 100°C, which are non-
ketonic and which are inert or only very slightly reactive towards isocyanate
and hydrazine, A6) if desired, in methyl acetate,
B) either the prepolyner obtained from step A is dissolved in a solvent A5) and/or A6) or, if the preparation has already been carried out dissolved in the presence of A5) and/or A6), the prepolymer solution is, where appropriate, dissolved diluted by fiirther addition of solvents A5 and/or A6, and
C) the remaining free NCO groups of the prepolymer are reacted with hydrazine or derivatives thereof so as to attain an arithmetic degree of chain extension of 40% to 150%.
3. Process according to Claim 2, characterized in that an arithmetic degree of chain
extension of 60% to 120% is attained.
4. Process according to Claim 3, characterized in that an arithmetic degree of chain
extension of 80% to 105% is attained.
5. Process according to Claim 4, characterized in that an arithmetic degree of chain
extension of 85% to 100% is attained.
6. Process according to Claims 1 to 5, characterized in that the chain extenders are
hydrazides or monosubstituted or 1,2-disubstituted hydrazines of the formula (I) to
(IV)
(Formula Removed)
in which
Rl is an alkyl radical having 1 to 20 carbon atoms, an aryl radical having 5
to 20 carbon atoms or an arylalkyl radical having 6 to 20 carbon atoms,
m is = 1,
R2, R3 is hydrogen or has the same definition as Rl,
R4 is an alkyl radical having 2 to 6 carbon atoms or an arylalkyl radical
having 6 to 20 carbon atoms.
7. Process according to Claim 6, characterized in that
m is 1 to 3 is, and
R4 is an alkyl radical having 2 to 6 carbon atoms.
8. Process according to Claim 7, characterized in that the chain extenders are
hydrazine hydrates, aqueous hydrazine solution or dicarboxylic dihydrazides.
9. Process according to Claim 8, characterized in that the chain extenders are hydrazine hydrates or aqueous hydrazine solution.
10. Aqueous polyurethane-polyurea dispersions stable towards thermal yellowing, obtainable by the process according to Claims 1 to 9.
11.. Coatings, adhesive bonds, sealants and/or mouldings obtainable from polyurethane/polyurea dispersions according to Claim H-. 10.
12. Substrates coated with coatings according to Claim 11.

Documents:

http://ipindiaonline.gov.in/patentsearch/GrantedSearch/viewdoc.aspx?id=FR1weGv7bJSsLdYwBhvZIA==&loc=+mN2fYxnTC4l0fUd8W4CAA==

« Previous Patent

Next Patent »

Patent Number

268441

Indian Patent Application Number

1851/DELNP/2009

PG Journal Number

36/2015

Publication Date

04-Sep-2015

Grant Date

31-Aug-2015

Date of Filing

20-Mar-2009

Name of Patentee

CLARIANT FINANCE (BVI) LIMITED

Applicant Address

CITCO BUILDING, WICKHAMS CAY, P.O. BOX 662, ROAD TOWN, TORTOLA,VIRGIN ISLANDS, BRITISH.

Inventors:

#	Inventor's Name	Inventor's Address
1	JURGEN MUNTER	THEODOR-HEUSS-STRASSE 54, 70736 FELLBACH, GERMANY.

PCT International Classification Number

C08G 18/08

PCT International Application Number

PCT/EP2007/059230

PCT International Filing date

2007-09-04

PCT Conventions:

#	PCT Application Number	Date of Convention	Priority Country
1	06121040.7	2006-09-21	EUROPEAN UNION