Classifications

• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
  • C08G18/00—Polymeric products of isocyanates or isothiocyanates
  • C08G18/06—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
  • C08G18/08—Processes
  • C08G18/10—Prepolymer processes involving reaction of isocyanates or isothiocyanates with compounds having active hydrogen in a first reaction step
  • C08G18/12—Prepolymer processes involving reaction of isocyanates or isothiocyanates with compounds having active hydrogen in a first reaction step using two or more compounds having active hydrogen in the first polymerisation step
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
  • C08G18/00—Polymeric products of isocyanates or isothiocyanates
  • C08G18/06—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
  • C08G18/08—Processes
  • C08G18/0804—Manufacture of polymers containing ionic or ionogenic groups
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
  • C08G18/00—Polymeric products of isocyanates or isothiocyanates
  • C08G18/06—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
  • C08G18/08—Processes
  • C08G18/10—Prepolymer processes involving reaction of isocyanates or isothiocyanates with compounds having active hydrogen in a first reaction step
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
  • C08G18/00—Polymeric products of isocyanates or isothiocyanates
  • C08G18/06—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
  • C08G18/83—Chemically modified polymers
  • C08G18/831—Chemically modified polymers by oxygen-containing compounds inclusive of carbonic acid halogenides, carboxylic acid halogenides and epoxy halides
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
  • C08G18/00—Polymeric products of isocyanates or isothiocyanates
  • C08G18/06—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
  • C08G18/83—Chemically modified polymers
  • C08G18/84—Chemically modified polymers by aldehydes
• • C—CHEMISTRY; METALLURGY
  • C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
  • C09D—COATING COMPOSITIONS, e.g. PAINTS, VARNISHES OR LACQUERS; FILLING PASTES; CHEMICAL PAINT OR INK REMOVERS; INKS; CORRECTING FLUIDS; WOODSTAINS; PASTES OR SOLIDS FOR COLOURING OR PRINTING; USE OF MATERIALS THEREFOR
  • C09D175/00—Coating compositions based on polyureas or polyurethanes; Coating compositions based on derivatives of such polymers
  • C09D175/04—Polyurethanes

Definitions

• the present invention relates to a new process for the production of aqueous dispersions or solutions of isocyanate polyaddition products, the dispersions or solutions obtainable by this process and their use for the production of coatings and coatings.
• Processes for producing stable, aqueous polyurethane-polyurea dispersions are known (for example DT-PS 1 184 946, DT-PS 1 178 586, DT-AS 1 237 306, DT-OS 1 495 745, DT-OS 1 595 602 , DT-OS 1 770 068, DT-OS 2 019 324, DT-OS 2 314 512, see also D. Dieterich et al, Angew. Chem. 82, 53 (1970)).
• the dispersions described are based on the principle of incorporating hydrophilic centers in a macromolecular chain of a polyurethane (polyurea) molecule.
• these hydrophilic centers or so-called internal emulsifiers are polyether segments containing ionic groups or ethylene oxide groups. These hydrophilic centers are either built into the prepolymer in the form of special diols or used as modified amines to lengthen the prepolymers, which each min at least have two terminal NCO functions.
• the present invention now presents a new principle for the production of aqueous dispersions or solutions of isocyanate polyaddition products, in which such side reactions are largely excluded.
• the new principle according to the invention is that hydrophilic, ie water-soluble or dispersible urethane prepolymers with terminal amino or semicarbazide groups in the aqueous phase with a hydrophobic chain extenders, preferably a hydrophobic diisocyanate, with hardly any side reaction due to the hydrophobicity of the isocyanate with the water which forms the continuous phase.
• the present invention also relates to the dispersions or solutions obtainable by this process as well as their use for the production of coatings and coatings.
• the molecular weight of the oligourethanes is essential here. It should preferably be between 1000 and 10,000. In principle, P räpolymere with average molecular weights dispersible 10000-15000 if this considerable difficulties.
• the molecular weight of the oligourethane can be adjusted in a simple and known manner by the type and proportions of the structural components. For example, the use of an NCO excess in the preparation of the NCO prepolymers prevents high-molecular-weight polyurethanes from building up in the isocyanate polyaddition reaction.
• the average molecular weight can be calculated from the stoichiometry of the reaction as follows.
• the hydrophilic groups mentioned are preferably incorporated into the oligourethane.
• the use of external emulsifiers is less preferred.
• the oligourethanes to be used in the process according to the invention are prepared via the intermediate stage of the corresponding prepolymers containing terminal isocyanate groups, which otherwise correspond to the statements made above with regard to their molecular weight and with regard to their content of hydrophilic groups, since the terminal isocyanate groups are converted into terminal semicarbazide or Amino groups no significant increase in molecular weight occurs.
• oligourethanes with ionic groups or with nonionic hydrophilic groups of the type mentioned are used, these are already present in the NCO prepolymers used as intermediates for the preparation of the starting materials according to the invention, with the only exception that when using ionically modified oligourethanes when
• the inventive method is also conceivable that a potential ionic groups, ie in particular NCO prepolymer containing carboxyl or sulfonic acid groups is produced, the potential ionic groups of which are only converted into ionic groups, in particular by neutralization, after the NCO prepolymers have been converted into terminal amino groups or oligourethanes containing semicarbazide groups.
• Oligourethanes which have a terminal average of 1.8-2.2, preferably 2, amino or semicarbazide groups are preferably used in the process according to the invention.
• difunctional NCO prepolymers are preferably used to prepare the oligourethanes to be used according to the invention.
• hydrophilic groups which determine their solubility or dispersibility in water.
• inherently hydrophobic NCO prepolymers if, before or after their conversion into terminal amino groups or oligourethanes containing semicarbazide groups, care is taken to ensure their solubility or dispersibility in water by the use of external emulsifiers.
• external emulsifiers it is also conceivable to increase the hydrophilicity of built-in hydrophilic group-containing NCO prepolymers or oligourethanes produced from them by additionally using external emulsifiers.
• NCO prepolymers As far as the chemical nature of the NCO prepolymers corresponds to the above statements, their exact chemical structure is not critical. This means in particular that, in principle, all NCO prepolymers are suitable which have previously been used in the production of aqueous polyurethane dispersions or solutions. They are produced using known methods of the prior art and are described, for example, in DT-OSen 1 495 745, 1 495 847, 2 446 440, 2 340 512, US Pat. No. 3,479,310, 3,756,992, GB-PSen 1 158 088 or 1 076 688.
• NCO prepolymers with chemically incorporated hydrophilic groups
• Starting materials for the production of these NCO prepolymers are accordingly 1. any organic polyisocyanates, preferably diisocyanates of the formula wherein Q represents an aliphatic hydrocarbon group having 4 to 12 carbon atoms, a cycloaliphatic hydrocarbon group having 6 to 15 carbon atoms, an aromatic hydrocarbon group having 6 to 15 carbon atoms or an araliphatic hydrocarbon group having 7 to 15 carbon atoms.
• diisocyanates examples include tetramethylene diisocyanate, hexamethylene diisocyanate, dodecamethylene diisocyanate, 1,4-diisocyanato-cyclohexane, 1-isocyanato-3,3,5-trimethylisocyanatomethylcyclohexane, isophorone diisocyanate, 4,4'-diisocyanatodicyclohexylmethane, 4,4'-diisocyanate, 4,4'-diisocyanate , 2), 1,4-diisocyanatobenzene, 2,4-diisocyanatotoluene, 2,6-diisocyanatotoluene, 4,4'-diisocyanatodiphenylmethane, 4,4'-diisocyanato-diphenylpropane- (2,2), p-xylylene diisocyanate or ,, ',' - -
• polyfunctional polyisocyanates known per se in polyurethane chemistry, or else modified polyisocyanates containing, for example, carbodiimide groups, allophanate groups, isocyanurate groups, urethane groups and / or biuret groups.
• Any organic compounds with at least two groups which are reactive toward isocyanate groups in particular a total of two amino groups, thiol groups, carboxyl groups and / or hydroxyl group-containing organic compounds of the molecular weight range 62-10,000, preferably 1,000 to 6,000.
• the corresponding dihydroxy compounds are preferably used.
• tri-functional or higher-functional compounds in the sense of the isocyanate polyaddition reaction in small proportions to achieve a certain degree of refusal is possible, as is the possible use of tri- or higher-functional polyisocyanates already mentioned for the same purpose.
• Hydroxyl compounds which are preferably used are the hydroxypolyesters, hydroxypolyethers, hydroxypolythioethers, hydroxypolyacetals, hydroxypolycarbonates and / or hydroxypolyesteramides known per se in polyurethane chemistry.
• the hydroxyl group-containing polyesters are, for example, reaction products of polyhydric, preferably dihydric and optionally additionally trihydric alcohols with polyhydric, preferably dihydric, carboxylic acids.
• the corresponding polycarboxylic anhydrides or corresponding polycarboxylic esters of lower alcohols or mixtures thereof can also be used to produce the polyesters.
• the polycarboxylic acids can be aliphatic, cycloaliphatic, aromatic and / or heterocyclic in nature and optionally substituted, for example by halogen atoms, and / or unsaturated. Examples include:
• polyhydric alcohols are e.g.
• the polyethers which are preferred according to the invention and preferably have two hydroxyl groups are those of the type known per se and are, for example, polymerized by themselves with epoxides such as ethylene oxide, propylene oxide, butylene oxide, tetrahydrofuran, styrene oxide or epichlorohydrin, for example in the presence of BF 3 , or by addition of these epoxides, optionally in a mixture or in succession to starting components with reactive hydrogen atoms such as alcohols and amines, for example water, ethylene glycol, propylene glycol (1,3) or - (1,2), 4,4'-dihydroxy-diphenylpropane , Aniline.
• epoxides such as ethylene oxide, propylene oxide, butylene oxide, tetrahydrofuran, styrene oxide or epichlorohydrin
• reactive hydrogen atoms such as alcohols and amines
• Polyethers modified by vinyl polymers e.g. by polymerization of styrene or acrylonitrile in the presence of polyethers (American patents 3,383,351, 3,304,273, 3,523,093, 3,110,695, German patent 1,152,536) are also suitable.
• the proportionally higher-functionality polyethers to be used, if appropriate, are formed in an analogous manner by known alkoxylation of higher-functionality starter molecules, e.g. Ammonia, ethanolamine, ethylenediamine or sucrose.
• polythioethers the condensation products of thiodiglycol with themselves and / or with other glycols, dicarboxylic acids, formaldehyde, aminocarboxylic acids or amino alcohols should be mentioned in particular.
• the products are polythio ether, polythio ether ester, polythio ether ester amide.
• polyacetals e.g. the compounds which can be prepared from glycols, such as diethylene glycol, triethylene glycol, 4,4'-diethoxy-diphenyldimethylmethane, hexanediol and formaldehyde.
• glycols such as diethylene glycol, triethylene glycol, 4,4'-diethoxy-diphenyldimethylmethane, hexanediol and formaldehyde.
• Polyacetals suitable according to the invention can also be prepared by polymerizing cyclic acetals.
• Suitable polycarbonates containing hydroxyl groups are those of the type known per se, which e.g. by reacting diols such as propanediol (1,3), butanediol (1,4) and / or hexanediol (1,6), diethylene glycol, triethylene glycol, tetraethylene glycol with diaryl carbonates, e.g. Diphenyl carbonate or phosgene can be produced.
• diols such as propanediol (1,3), butanediol (1,4) and / or hexanediol (1,6)
• diethylene glycol triethylene glycol
• tetraethylene glycol e.g. Diphenyl carbonate or phosgene
• polyester amides and polyamides include e.g. the predominantly lienear condensates obtained from polyvalent saturated and unsaturated carboxylic acids or their anhydrides and polyvalent saturated and unsaturated amino alcohols, diamines, polyamides and their mixtures. Polyhydroxyl compounds already containing urethane or urea groups can also be used.
• Low molecular weight polyols can also be used, e.g. Ethanediol, 1,2-and 1,3-propanediol, 1,4-and 1,3-butanediol, pentanediols, hexanediols, trimethylolpropane, hexanetriols, glycerol and pentaerythritol or diamines such as e.g. Hexamethylenediamine or 1-amino-3,3,5-trimethyl-5-amino-cyclohexane.
• oligourethanes which have chemically fixed ionic or nonionic hydrophilic groups are used in the process according to the invention, they are prepared via the appropriately modified NCO prepolymers.
• These hydrophilically modified prepolymers are produced by known processes of the prior art, for example in accordance with DT-OSen 1 495 745, 1 495 847, 2 446 440, 2 340 512, US Pat. Nos. 3,479,310, 3,756,992, GB PSen 1 158 088 or 1 076 688.
• the preferred hydrophilically modified structural components include in particular the sulfonate group-containing aliphatic diols according to DT-OS 2 446 440, the cationic or also anionic internal emulsifiers which can be incorporated according to German patent application P 26 51 506.0 and also the monofunctional incorporable polyethers described in this patent application.
• the conversion of the potential ionic groups, which may have been initially incorporated into the polyaddition product, into ionic groups takes place in a manner known per se by neutralizing the potential anionic and cationic groups, by quaternizing tertiary, aminic nitrogen atoms or of tertiary phosphinic phosphorus atoms which are present in the polyaddition products according to the invention can, if instead of the exemplified tertiary amines with hydrogen atoms reactive towards isocyanate groups, these tertiary amines analogous tertiary phosphines were incorporated, or by converting any thioether groups present into the corresponding sulfonium salts with quaternizing agents.
• Suitable neutralizing and quaternizing agents are described in US Pat. No. 3,479,310, column 6.
• the conversion of the potential ionic groups into ionic groups can take place both before the conversion of the NCO prepolymers into the starting materials according to the invention and afterwards. Particularly when carboxyl or sulfonic acid groups are present as potential ionic groups, these groups must be neutralized after the NCO prepolymers have been converted into the Oligourethanes to be used as starting material according to the invention are conceivable.
• the reactants are generally used in such proportions that a ratio of isocyanate groups to hydrogen atoms reactive toward NCO, preferably from hydroxyl groups, of from 1.05 to 10, preferably from 1.1 to L 2.5.
• the order in which the individual reactants are added is largely arbitrary. You can either mix the hydroxyl compounds and add the polyisocyanate, or you can gradually add the mixture of hydroxyl compounds or the individual hydroxyl compounds to the polyisocyanate component.
• the NCO prepolymers are preferably produced in the melt at 30 to 190 ° C., preferably at 50 to 120 ° C.
• the prepolymers could also be produced in the presence of organic solvents.
• Suitable solvents e.g. in an amount up to 25 parts by weight, based on the solid, could be used e.g. Acetone, methyl ethyl ketone, ethyl acetate, dimethylformamide or cyclohexanone.
• the NCO prepolymers mentioned by way of example are preferably modified by one of the following two methods:
• the NCO prepolymers are reacted with hydrazines of the type exemplified below or with diamines whose amino groups differ greatly in their reactivity towards isocyanate groups.
• Suitable hydrazines are any hydrazines which have 2-NH groups, ie both hydrazine or hydrazine hydrate itself and any mono- or N, N'-disubstituted hydrazines.
• Suitable substituents for the hydrazines are in particular C 1 -C 4 -alkyl radicals. Accordingly, examples of suitable hydrazines are hydrazine, hydrazine hydrate, N-methylhydrazine, N, N'-dimethylhydrazine, N-butylhydrazine or N, N'-dibutylhydrazine.
• Suitable diamines with amino groups of different reactivity are any diamines having primary and / or secondary amino groups corresponding to these conditions.
• the different reactivity of the amino groups of the diamines can be caused by steric and / or mesomeric effects and / or by different types of binding of the anino groups.
• the first-mentioned type of suitable diamines included 2,4-diaminotoluene, 1-methyl-2,4-diamino-cyclohexane or 2,4'-diaminodiphenylmethane.
• Diamines with amino groups of different reactivity are e.g. 2- (2-aminoethyl) aniline, 2- (3-aminopropyl) aniline, N- (3-aminopropyl) aniline, N- (6-aminohexyl) aniline, 2- (2-aminoethyl) naphthalene, N- (2-aminoethyl) aniline, 2- (2-aminoethylamino) naphthalene, 2-aminophenyl- (3-aminopropyl) thioether or 2-aminomethylaniline.
• Simple aromatic diamines such as, for example, 1,4-diaminobenzo are also suitable, since the second amino group, due to mesemory effects, has less willingness to react to isocyanate groups after the first amino group has reacted.
• diamines are suitable whose pKb values for the two amino groups in an aqueous medium at 25 ° C. differ by at least a factor of 10 3 , preferably by a factor of 10 6 .
• the diamines or hydrazines have a molecular weight of 32 to 400.
• the reaction of the NCO prepolymers with the hydrazines or diamines is generally carried out in the melt or in the presence of inert solvents of the type already mentioned by way of example at 10 to 120 ° C., the reactants being used preferably in amounts such that for every mole of NCO -Groups of the NCO prepolymer 0.8-1.2, preferably 1 mol of the hydrazine or diamine is omitted.
• Solvents containing keto groups such as e.g. Acetone, methyl ethyl ketone, methyl isobutyl ketone or cyclohexanone are suitable.
• N-hydroxyalkyl-oxazolidines are prepared by methods known from the literature, a ketone or an aldehyde being condensed with a bis- (hydroxyalkyl) amine with cyclizing dehydration and the water of reaction usually being removed azeotropically by an inert entrainer or by the excess carbonyl compound becomes.
• Carbonyl compounds to be used preferably correspond to the above definition of the preferred radicals R 2 and R 3 formaldehyde and the aliphatic aldehydes or ketones mentioned.
• Bis- (2-hydroxyethyl) amine and bis- (2-hydroxypropyl) amine are particularly suitable. In principle, however, bis- (2-hydroxybutyl) amine, bis (2-hydroxyhexyl) amine, bis (3-hydroxyhexyl) amine, or N- (2-hydroxypropyl) -N- ( 6-hydroxyhexyl) amine.
• the hydroxyalkyloxazolidines are reacted with the NCO prepolymers at 20 to 120 ° C in the presence or in the absence of solvents, the quantitative ratios of the reactants being chosen so that for each Mol isocyanate groups of the NCO prepolymer in the reaction mixture 0.8-1.2, preferably 1 mol of the oxazolidine derivative is present.
• Another also conceivable, but less preferred, method of converting the NCO prepolymers into starting materials suitable according to the invention consists in the reaction the NCO prepolymers with a high excess of any organic diamine, for example with ethylenediamine or hexamethylenediamine and subsequent removal of the unreacted excess, for example by distillation in vacuo.
• a large excess as with the first two methods mentioned, it is ensured that a significant increase in the molecular size due to chain extension does not occur.
• the use of continuously running, high-speed machines would be an advantage.
• the NCO prepolymer with terminal semicarbazide groups, amino groups or oxazolidine groups modified as described is now dispersed or dissolved in water, and when compounds containing oxazolidine groups are used, hydrolysis occurs immediately with release of the corresponding amino groups from the oxazolidine residue.
• the amount of water in this dispersing or dissolving process is generally such that the weight ratio of prepolymer to water is between 65:35 and 5:95, preferably 55:45 and 20:80.
• the temperature of the dispersing process should be above the softening point of the prepolymer, namely above the softening point to ensure that the melt is stirred. In the case of purely non-ionic dispersions or solutions, the dispersion temperature should not be substantially above 60 ° C.
• the dispersing process can also be supported by adding external emulsifiers.
• these external emulsifiers are already added to the NCO prepolymers or to the starting materials to be used according to the invention and prepared from them. If you go through at all, generally in amounts of 1 to 30, preferably 5 to 20,% by weight, based on the NCO prepolymer or oligourethane. Suitable such emulsifiers are described, for example, by R. Heusch in "Emulsions", Ullmann, Volume 10, pages 449-473, Weinheim 1975.
• ionic emulsifiers such as alkali and ammonium salts of long-chain fatty acids or long-chain aryl (alkyl) sulfonic acids are suitable, as are nonionic emulsifiers such as ethoxylated alkylphenols with an average molecular weight of 400 to 10,000.
• the actual process according to the invention now consists in chain extension of the oligourethanes present in aqueous solution or dispersion with suitable chain extenders.
• Suitable chain extenders are any, preferably difunctional organic compounds which react largely selectively with the amino or semicarbazide groups of the oligourethane in the presence of water with these groups in the sense of an addition reaction or a condensation reaction.
• Suitable chain extenders are accordingly hydrophobic bis-epoxides such as the reaction product of bisphenol A with 2 moles of epichlorohydrin or higher molecular weight bis-epoxides with a maximum molecular weight of 3000 and in particular hydrophobic diisocyanates of the formula Q (NCO) 2 of the type already mentioned above as examples.
• Particularly preferred chain extenders are hexamethylene diisocyanate, 1-isocyanato-3,3,5-trimethyl-5-isocyanatomethylcyclohexane, 2,4-diisocyanatotoluene, 2,6-di isocyanatotoluene, 4,4'-diisocyanato-diphenyl-methane or any mixture of these diisocyanates.
• difunctional NCO prepolymers with a maximum molecular weight of 3000 as can be obtained in a manner known per se by reacting the low molecular weight diisocyanates mentioned by way of example with suitable dihydroxy compounds, are suitable according to the invention as chain extenders.
• the chain extenders are generally used in amounts such that 0.4 to 1.0 mol, preferably 0.5 mol, of the difunctional chain extender are available for each mole of amino groups or semicarbazide groups of the oligourethane.
• the chain extension reaction according to the invention is generally carried out by stirring the chain extender optionally dissolved in an inert solvent into the initially introduced dispersion or solution. Liquid chain extenders without solvents are preferably used.
• the chain extension reaction according to the invention generally takes place in the temperature range from 0 to 100, preferably 10 to 70 ° C. In principle, it is also possible to use capped di- or polyisocyanates which, if appropriate, only have an elongating or crosslinking effect after the dispersion has been applied when baking out by removing the capping agent.
• the dispersions or solutions accessible according to the invention are suitable for the known fields of application of the aqueous polyurethane dispersions. They can be used, for example, for leather finishing or wool finishing. or can be used to coat a wide variety of materials, such as textiles, plastics, glass, metals, paper or wood, where they are used, among other things, as paints or adhesives. Other possible uses are in the areas of glass fiber sizing or dis purging aids. These products can also be used as additives for plastic dispersions or as binders for, for example, cork or wood flour, glass fibers, asbestos, paper-like materials, plastic or rubber waste and ceramic materials.
• the dispersions or solutions according to the invention can be provided with any additives before their application. These include in particular crosslinking agents such as Formaldehyde, formaldehyde releasing compounds or melamine resins; Polymer latices of various origins, e.g. those based on polyacrylonitrile, butadiene-acrylonitrile copolymers or else based on grafted copolymers based on acrylonitrile, butadiene and styrene, and those based on poly (meth) acrylates. Aftertreatment of the dispersions or solutions according to the invention is also possible in accordance with the process of German patent application P 27 08 442.
• crosslinking agents such as Formaldehyde, formaldehyde releasing compounds or melamine resins
• Polymer latices of various origins e.g. those based on polyacrylonitrile, butadiene-acrylonitrile copolymers or else based on grafted copolymers based on
• the polyester (PE) and the adduct (AD) are dewatered at 110 ° C. in a water jet vacuum with stirring for 45 minutes, cooled to 80 ° C. and reacted with the diisocyanate (H) at 80 ° C. After about 40 minutes, an NCO value of 2.75% is reached.
• the melt is cooled to 45 to 50 ° C. and stirred with hydrazine hydrate until no more isocyanate is found. With rapid stirring, the melt is dispersed with water at 50 ° C.
• a finely divided dispersion with a Ford cup viscosity (4 mm nozzle) of 21 seconds at 29.8% solids is obtained.
• the average molecular weight of the oligourethane is 3080.
• the solid contains 1.9% SO 3 ⁇ groups.
• IPDI is stirred into the semicarbazide-terminal dispersion at room temperature. After stirring for 5 to 10 minutes, no isocyanate is found.
• the tensile strength of the film is 14.7 MPa with an elongation at break of 340%.
• the polyester (PE) and the adduct (AD) are dewatered at 110 ° C. with stirring in a water jet vacuum. It is cooled to 80 ° C. and butanediol is stirred in. After stirring for 10 minutes, the diisocyanate (H) is added and the mixture is stirred at 80 ° C. until an NCO value of 5% is reached (approx. 30 minutes). The IPDA in acetone is then added and the mixture is stirred at 80 ° C. for 30 minutes. An NCO value of 3.0% is found. The melt is then stirred with the oxazolidine at 80 ° C. until no more isocyanate is found (about 1 hour). The small amount of acetone is drawn off in vacuo. The mixture is then dispersed at 80 ° C. with vigorous stirring with water.
• the extremely fine-particle dispersion has a Ford cup viscosity (4 mm nozzle) of 18 seconds with a solid of 28.75%.
• the average molecular weight of the oligourethane is 2350.
• the solid contains 21.5 milliequivalents per 100 g (1.72%) of SO 3 ⁇ groups.
• the polyester (PE) and the adduct (AD) are dewatered at 110 ° C. with stirring in a water jet vacuum. It is cooled to 80 ° C. and butanediol is stirred in. After stirring for 10 minutes, the diisocyanate (H) is added and the mixture is stirred at 80 ° C. until an NCO value of 2.8% is reached (about 2 hours). Then the NPDA is added at 60 ° C. and the mixture is stirred at 60 ° C. until the melt is free of NCO (approx. 30 minutes). The solid is dissolved very well with water at 60 ° C.
• the amine-terminated oligourethane dispersion is stirred at room temperature with 38.6 g IPDI for 2 hours. A further 30.5 g of IPDI are then added in order to coat the dispersion particles with a urea shell in accordance with German patent application P 27 08 442. The dispersion is then baked at 80 ° C. for 1 hour.
• the Ford cup viscosity (4 mm nozzle) of the dispersion with a solids content of 32.5% is 12.7 seconds.
• the dispersion is centrifuge stable (3600 rpm for 15 minutes without sedimentation) and has a Tyndall effect in the translucent light.
• the pH is 5.4.
• the films from this dispersion become clear and transparent; they do not stick, but have a pleasantly dry grip.
• the dispersion is for the coating of textiles suitable.
• the tensile strength of the film is 23.1 MPa with an elongation at break of 916%.
• a finely divided amine-terminal dispersion is obtained which has a Tyndall effect in the translucent light.
• the Ford cup viscosity (4 mm nozzle) for a solid of 30% is 38 seconds.
• the average molecular weight of the solid is 3320.
• the solid contains 23.4 milliequivalents per 100 g. (1.87%) of SO 3 ⁇ groups.
• a sediment-stable dispersion is obtained which shows a Tyndall effect in the translucent light.
• the dispersion has a Ford cup viscosity (4 mm nozzle) of 12.7 seconds. Your pH is 4.5.
• the film from this dispersion is very hard and does not stick.
• a finely divided dispersion is obtained which has a Tyndall effect in the translucent light.
• the dispersion has a pH of 7.5.
• the F ordbecherauslaufzeit (4 mm nozzle) is 35.3 seconds at a solids content of 35.3%.
• the film from the dispersion is tack-free and hard.
• the dispersion is baked out at 80 ° C.
• a finely divided dispersion with a Tyndall effect in translucent light is obtained, which has a Ford cup viscosity (4 mm nozzle) of 11.5 seconds at a solids content of 31.4%.
• the pH is 5.4.
• the films do not stick and have a pleasant dry grip.

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• 1977
  • 1977-07-30 DE DE19772734576 patent/DE2734576A1/de not_active Withdrawn
• 1978
  • 1978-07-18 US US05/925,674 patent/US4240942A/en not_active Expired - Lifetime
  • 1978-07-21 EP EP78100476A patent/EP0000568B1/fr not_active Expired
  • 1978-07-21 DE DE7878100476T patent/DE2860231D1/de not_active Expired
  • 1978-07-28 IT IT50523/78A patent/IT1105392B/it active
  • 1978-07-28 ES ES472137A patent/ES472137A1/es not_active Expired
  • 1978-07-29 JP JP9208178A patent/JPS5426897A/ja active Pending

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