[go: up one dir, main page]

WO1992000336A1 - Use of aqueous polyurethane dispersions in leather dressing - Google Patents

Use of aqueous polyurethane dispersions in leather dressing Download PDF

Info

Publication number
WO1992000336A1
WO1992000336A1 PCT/EP1991/001132 EP9101132W WO9200336A1 WO 1992000336 A1 WO1992000336 A1 WO 1992000336A1 EP 9101132 W EP9101132 W EP 9101132W WO 9200336 A1 WO9200336 A1 WO 9200336A1
Authority
WO
WIPO (PCT)
Prior art keywords
oil
weight
parts
opened
polyurethane dispersion
Prior art date
Application number
PCT/EP1991/001132
Other languages
German (de)
French (fr)
Inventor
Michael Marschner
Werner Krause
Horst Schulz
Gerhard Kaindl
Original Assignee
Henkel Kommanditgesellschaft Auf Aktien
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Henkel Kommanditgesellschaft Auf Aktien filed Critical Henkel Kommanditgesellschaft Auf Aktien
Publication of WO1992000336A1 publication Critical patent/WO1992000336A1/en

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C14SKINS; HIDES; PELTS; LEATHER
    • C14CCHEMICAL TREATMENT OF HIDES, SKINS OR LEATHER, e.g. TANNING, IMPREGNATING, FINISHING; APPARATUS THEREFOR; COMPOSITIONS FOR TANNING
    • C14C11/00Surface finishing of leather
    • C14C11/003Surface finishing of leather using macromolecular compounds
    • C14C11/006Surface finishing of leather using macromolecular compounds using polymeric products of isocyanates (or isothiocyanates) with compounds having active hydrogen
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G18/00Polymeric products of isocyanates or isothiocyanates
    • C08G18/06Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
    • C08G18/08Processes
    • C08G18/0804Manufacture of polymers containing ionic or ionogenic groups
    • C08G18/0819Manufacture of polymers containing ionic or ionogenic groups containing anionic or anionogenic groups
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G18/00Polymeric products of isocyanates or isothiocyanates
    • C08G18/06Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
    • C08G18/08Processes
    • C08G18/10Prepolymer processes involving reaction of isocyanates or isothiocyanates with compounds having active hydrogen in a first reaction step
    • C08G18/12Prepolymer 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
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G18/00Polymeric products of isocyanates or isothiocyanates
    • C08G18/06Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
    • C08G18/28Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the compounds used containing active hydrogen
    • C08G18/30Low-molecular-weight compounds
    • C08G18/36Hydroxylated esters of higher fatty acids
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G18/00Polymeric products of isocyanates or isothiocyanates
    • C08G18/06Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
    • C08G18/28Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the compounds used containing active hydrogen
    • C08G18/40High-molecular-weight compounds
    • C08G18/64Macromolecular compounds not provided for by groups C08G18/42 - C08G18/63
    • C08G18/6407Reaction products of epoxy resins with at least equivalent amounts of compounds containing active hydrogen

Definitions

  • the invention relates to the use of an aqueous polyurethane dispersion which, based on 100 parts by weight of di- and / or polyisocyanates, contains 61 to 450 parts by weight of castor oil and / or epoxidized fatty acid esters ring-opened with C 8 alkyl alcohols in the leather finishing.
  • leather finishing is the protective layer that is applied to the leather that has been dried after tanning and oiling in order to protect it against moisture, dirt and damage (Ull anns Encyclopedia of Technical Chemistry, 4th edition, volume 16, pages 159-163, Verlag Chemie Weinheim, 1978).
  • the finishing film must adhere firmly to the leather and satisfy extremely high bending and expansion requirements during further processing and during later use. Furthermore, the surface of the
  • Dressing film must be hard enough to ensure adequate resistance to damage from dry and wet rubbing, bumping and scratching. So that the dressing film can meet these different requirements, it is applied in several thin layers of different dressing liquors, in particular priming and finishing liquors, with respective intermediate drying and, if necessary, intermediate hangers and embossing. In many cases, the finishing liquors contain polyurethanes, thermoplastic polyacrylates and / or butadiene copolymers as film-forming substances.
  • DE 37 02 615 describes polyurethane dispersions as coating and finishing agents for leather whose polyurethane solids, based on 100 parts by weight of isocyanate component, 6 to 60 parts by weight of castor oil, alkoxylated castor oil and / or epoxidized triglycerides which are ring-opened with C 8 alkyl alcohols are optionally alkoxylated.
  • leather that has been finished with these polyurethane dispersions have good fastness properties.
  • the subject of the invention is the use of an aqueous polyurethane dispersion with a solids content of between 10 and 50% by weight and a Brookfield viscosity at 20 ° C. of between 10 and 5000 mPas, the polyurethane solids, based on 100 parts by weight of di- and / or Contains polyisocyanates, 61 to 450 parts by weight of castor oil and / or epoxidized fatty acid esters ring-opened with C ⁇ _8-alkyl alcohols, in the leather finishing.
  • a polyurethane dispersion is used, the polyurethane solids, based on 100 parts by weight of di- and / or polyisocyanates, 80 to 200 parts by weight of castor oil and / or with Ci-8-alkyl alcohols contains ring-opened epoxidized fatty acid esters.
  • Epoxidized fatty acid esters are preferably epoxidized fatty acid mono-, di- and / or triglycerides which are obtained by epoxidation of unsaturated oils, especially soybean oil, linseed oil, talc oil, construction oil seed oil, peanut oil , Palm oil, sunflower oil, rape oil and / or claw oil are accessible.
  • unsaturated fatty acid esters can be epoxidized by reaction with peracetic acid in the presence of acidic catalysts or with performic acid formed in situ from formic acid and hydrogen peroxide.
  • the epoxidized fatty acid esters with monohydric C 8 alkyl alcohols for example methanol, ethanol, n-propanol, isopropanol, n-butanol, n-pentanol, n-hexanol, 2-ethylhexanol, n-heptanol and / or n-octanol , but preferably with methanol in the presence of catalysts, for example sodium methylate or potassium hydroxide, at temperatures between 40 and 160 ° C and pressures between 10 4 and 3 * 10 ⁇ Pa.
  • catalysts for example sodium methylate or potassium hydroxide
  • the polyurethanes to be used according to the invention may contain polyester polyols which are composed of aliphatic and / or aromatic dicarboxylic acids and diols.
  • Suitable aliphatic dicarboxylic acids are, for example, succinic acid, adipic acid, suberic acid, azelaic acid, sebacic acid, brassylic acid and / or dimer fatty acids.
  • suitable aromatic dicarboxylic acids are phthalic acid, isophthalic acid, terephthalic acid and / or tetrahydrophthalic acid. Adipic acid is preferred as the aliphatic dicarboxylic acid and isophthalic acid is preferred as the aromatic dicarboxylic acid.
  • dicarboxylic acids mentioned are mixed in a manner known per se with diols, for example ethylene glycol, 1,2-propanediol, 1,3-propanediol, diethylene glycol, 1,4-butanediol, 1,6-hexanediol, 1,10-decanediol, dimerocenol (SovermolR 650NS, Henkel KGaA) and / or neopentylglycol, esterified.
  • diols for example ethylene glycol, 1,2-propanediol, 1,3-propanediol, diethylene glycol, 1,4-butanediol, 1,6-hexanediol, 1,10-decanediol, dimerocenol (SovermolR 650NS, Henkel KGaA) and / or neopentylglycol, esterified.
  • polyurethanes to be used according to the invention may also contain polyether polyols with average molecular weights between 1,000 and 20,000, preferably between 3,000 and 12,000. Polyether polyols of the general formula are particularly preferred
  • R denotes an alkoxy radical which is derived from glycerol, diglycerol, polyglycerol with a degree of polymerization x between 3 and 6, trimethylolpropane or trimethylolethane
  • the index x means the degree of polymerization of the alkoxy radical
  • the indices y are a number between 1 and 8
  • z means a number between 0 and 8, with the proviso that the sum y + z is between 1 and 8
  • d is a number between 20 and 150
  • e is a number between 1 and 15, with the proviso that - based on all ethylene oxide and propylene oxide units of the polyether polyol - the sums a + c + e between 3 and 40, b + d are between 40 and 300 and c + e between 1 and 15.
  • the polyether polyols of the general formula are known compounds which are prepared in a manner known per se by alkoxylation of glycerol, diglycerol, polyglycerol with a degree of polymerization between 3 and 6, trimethylolpropane or trimethylolethane with ethylene oxide and propylene oxide at temperatures between 110 and 200 ° C. and pressures between 10 ⁇ and 2-10 ⁇ Pa are accessible.
  • dihydroxy and / or diamino compounds which contain at least one anionic group, preferably one or more carboxylate, sulfonate and / or ammonium groups, for example dimethylolpropionic acid, are used in the production of polyurethanes to be used according to the invention.
  • anionic group preferably one or more carboxylate, sulfonate and / or ammonium groups, for example dimethylolpropionic acid
  • the polyurethanes to be used according to the invention contain, based on 100 parts by weight of isocyanate component, 61 to 450 parts by weight of castor oil and / or epoxidized fatty acid esters ring-opened with C8 -8 alkyl alcohols, 0 to 300 parts by weight of polyester polyols, 0 to 60 parts by weight of polyether polyols and 5 to 50 parts by weight bearing at least one anionic group Dihydroxy and / or diamino compounds, preferably 80 to 200 parts by weight of castor oil and / or epoxidized fatty acid esters opened with C 8 alkyl alcohols, 1 to 180 parts by weight of polyester polyols, 0 to 20 parts by weight of polyether polyols and 5 to 30 parts by weight of dihydroxy and at least one anionic group / or diamino compounds, with the proviso that the proportion of the OH equivalents of the polyester polyols, polyether polyols and at least one anionic group Dihydroxy compounds is between 10
  • Suitable organic di- and / or polyisocyanates are aliphatic and / or aromatic di- and / or triisocyanates, for example dicyclohexylmethane-4,4'-diisocyanate, 1,6-hexane diisocyanate, 3-isocyanatomethyl-3,5,5-trimethylcyclohexyl isocyanate ( Isophorone diisocyanate), tetramethylene diisocyanates, trimethylhexamethylene diisocyanate, dimer fatty acid diisocyanates, 1,4-phenylene diisocyanate, diphenyl ethane diisocyanate, toluene-2,4- and / or toluene-2,6-diisocyanate, 2.4 f 4'- Tr ⁇ isocyanato-diphenyl ether and / or 4 ', 4'',4' -Triisocyanato-triphenyl ethane.
  • Aliphatic diisocyanates in particular isophorone diisocyanate, dicyclohexylmethane-4,4'-diisocyanate, 1,6-hexane diisocyanate and / or dimer fatty acid diisocyanates, are preferred.
  • blocked di- and / or polyisocyanates can be used alone or in combination with the above-mentioned unblocked di- and / or polyisocyanates.
  • the blocked di- and polyisocyanates are resistant to hydroxyl groups at room temperature and only react at temperatures above 50 ° C.
  • the content of blocked di- and / or polyisocyanates is preferably between 0 and 60% by weight, particularly preferably between 0 and 10% by weight.
  • Blocked di- and polyisocyanates are produced by reacting organic di- or polyisocyanates, for example isophorone diisocyanate, with an alcohol, for example phenol or m-cresol, in amounts such that all isocyanate groups are blocked.
  • organic di- or polyisocyanates for example isophorone diisocyanate
  • alcohol for example phenol or m-cresol
  • the polyurethanes to be used according to the invention can be produced by known processes (Ullmann's Encyclopedia of technical chemistry, volume 19, pages 302 ff., Verlag Chemie Wein ⁇ heim, 1980).
  • Di- and / or polyisocyanates with polyols and at least one anionic group containing dihydroxy and / or diamino compounds in the presence of solvents, for example N-methylpyrrolidone and / or methyl ethyl ketone, and, if appropriate, catalysts, such as N-methylmorpholine, are preferably added Temperatures between 60 and 120 ° C converted to prepolymers.
  • the polyurethane prepolymer composition is then dispersed in water and then, if appropriate, reacted with chain extenders, such as alkoxylated glycerols and / or diamines, for example ethylenediamine, hexamethylenediamine and / or piperazine.
  • chain extenders such as alkoxylated glycerols and / or diamines, for example ethylenediamine, hexamethylenediamine and / or piperazine.
  • the NCO groups still present in the polyurethane prepolymer react with water to form carbon dioxide, which leads to not inconsiderable, disruptive foam formation.
  • a polyurethane dispersion with a high content of castor oil and / or epoxidized fatty acid esters ring-opened with C8-alkyl alcohols as polyol component in the polyurethane solid, a solids content between 10 and 50 wt .-% and a Brookfield viscosity at 20 ° C between 10 and 5000 mPas can be used according to the invention in leather finishing in primer, color and / or finishing liquors.
  • the additive liquors may contain pigment preparations, film-forming substances in the form of aqueous dispersions, such as polyacrylates and / or polyurethanes, binders and fillers, matting agents, penetrators and / or plasticizers as further constituents.
  • finishing liquors can be applied using all of the technologies customary in leather finishing, for example by spraying, plushing, pouring and / or roller application.
  • the finishing liquors contain polyurethane dispersions to be used according to the invention in amounts of 1 to 60% by weight.
  • Tl means parts by weight
  • Base material natural crust leather
  • Head coloring 100 parts of metal complex dye solution 200 parts of polyglycol ether 200 parts of water

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Organic Chemistry (AREA)
  • Health & Medical Sciences (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • General Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Manufacturing & Machinery (AREA)
  • Polyurethanes Or Polyureas (AREA)

Abstract

The invention concerns the use, in the dressing of leather, of an aqueous polyurethane dispersion containing 100 parts by weight of di- and/or polyisocyanates, 61 to 450 parts by weight (relative to the isocyanate content) of castor oil and/or epoxidized fatty-acid esters ring-opened with C1-8? alkyl alcohols.

Description

Verwenduno wäßriger Polyurethandispersionen in der Lederzurichtuno Use of aqueous polyurethane dispersions in the leather trimmings
Die Erfindung betrifft die Verwendung einer wäßrigen Polyurethandispersion, die, bezogen auf 100 Gewichtsteile Di- und/oder Polyisocyanate, 61 bis 450 Gewichtsteile Rizinusöl und/oder mit Cι_8-Alkylalkoholen ringgeöffnete epoxidierte Fett¬ säureester enthält, in der Lederzurichtung.The invention relates to the use of an aqueous polyurethane dispersion which, based on 100 parts by weight of di- and / or polyisocyanates, contains 61 to 450 parts by weight of castor oil and / or epoxidized fatty acid esters ring-opened with C 8 alkyl alcohols in the leather finishing.
Als Lederzurichtung wird die Schutzschicht bezeichnet, die auf das nach der Gerbung und Fettung getrocknete Leder aufgetragen wird, um es gegen Feuchtigkeit, Verschmutzung und Beschädigung zu schützen (Ull anns Encyclopädie der technischen Chemie, 4. Auflage, Band 16, Seiten 159 - 163, Verlag Chemie Weinheim, 1978). Der Zurichtfilm muß auf dem Leder fest haften und extrem hohen Biege- und Deh¬ nungsanforderungen während der weiteren Verarbeitung sowie während des späteren Gebrauchs genügen. Des weiteren muß die Oberfläche desLeather finishing is the protective layer that is applied to the leather that has been dried after tanning and oiling in order to protect it against moisture, dirt and damage (Ull anns Encyclopedia of Technical Chemistry, 4th edition, volume 16, pages 159-163, Verlag Chemie Weinheim, 1978). The finishing film must adhere firmly to the leather and satisfy extremely high bending and expansion requirements during further processing and during later use. Furthermore, the surface of the
Zurichtfilms hart genug sein, um ausreichenden Widerstand gegen Beschädigung durch trockenes und nasses Reiben, Stoßen und Kratzen zu gewährleisten. Damit der Zurichtfilm diesen unterschiedlichen Anforderungen genügen kann, wird er in mehreren dünnen Schichten aus verschiedenen Zurichtflotten, insbesondere Grundierungs- und Abschlußflotten, mit jeweiliger Zwischentrocknung und gegebenen¬ falls Zwischenbügeln und Prägen appliziert. Die Zurichtflotten enthalten in vielen Fällen als filmbildende Substanzen Polyurethane, thermoplastische Polyacrylate und/oder Butadien-Mischpolymerisate. In DE 37 02 615 werden Polyurethandispersionen als Beschichtungs- und Zurichtmittel für Leder beschrieben, deren Polyurethanfestkörper, bezogen auf 100 Gewichtsteile Isocyanat-Ko ponente, 6 bis 60 Gewichtsteile Rizi¬ nusöl, alkoxyliertes Rizinusöl und/oder mit Cι_8-Alkylalkoholen ringgeöffnete epoxidierte Triglyceride, die gegebenenfalls alkoxyliert sind, enthält. Leder, die mit diesen Polyurethandispersionen zugerichtet wurden, besitzen gute Echt¬ heiten.Dressing film must be hard enough to ensure adequate resistance to damage from dry and wet rubbing, bumping and scratching. So that the dressing film can meet these different requirements, it is applied in several thin layers of different dressing liquors, in particular priming and finishing liquors, with respective intermediate drying and, if necessary, intermediate hangers and embossing. In many cases, the finishing liquors contain polyurethanes, thermoplastic polyacrylates and / or butadiene copolymers as film-forming substances. DE 37 02 615 describes polyurethane dispersions as coating and finishing agents for leather whose polyurethane solids, based on 100 parts by weight of isocyanate component, 6 to 60 parts by weight of castor oil, alkoxylated castor oil and / or epoxidized triglycerides which are ring-opened with C 8 alkyl alcohols are optionally alkoxylated. Leather that has been finished with these polyurethane dispersions have good fastness properties.
Es wurde nun gefunden, daß die mit den aus DE 37 02 615 bekannten Polyurethandispersionen erzielten Echtheiten deutlich verbessert werden, wenn eine Polyurethandispersion verwendet wird, deren Polyurethanfestkörper, bezogen auf 100 Gewichtsteile Isocyanat- Komponente, 61 bis 450 Gewichtsteile Rizinusöl und/oder mit Cι_8-Alkylalkoholen ringgeöffnete epoxidierte Fettsäureester ent¬ hält.It has now been found that the fastness properties achieved with the polyurethane dispersions known from DE 37 02 615 are significantly improved if a polyurethane dispersion is used whose polyurethane solids, based on 100 parts by weight of isocyanate component, 61 to 450 parts by weight of castor oil and / or with Cι_8- Alkyl alcohols contains ring-opened epoxidized fatty acid esters.
Erfindungsgegenstand ist dementsprechend die Verwendung einer wä߬ rigen Polyurethandispersion mit einem Feststoffgehalt zwischen 10 und 50 Gew.-% und einer Brookfield-Viskosität bei 20 °C zwischen 10 und 5000 mPas, deren Polyurethanfestkörper, bezogen auf 100 Ge¬ wichtsteile Di-und/oder Polyisocyanate, 61 bis 450 Gewichtsteile Rizinusöl und/oder mit Cι_8-Alkylalkoholen ringgeöffnete epoxidierte Fettsäureester enthält, in der Lederzurichtung.Accordingly, the subject of the invention is the use of an aqueous polyurethane dispersion with a solids content of between 10 and 50% by weight and a Brookfield viscosity at 20 ° C. of between 10 and 5000 mPas, the polyurethane solids, based on 100 parts by weight of di- and / or Contains polyisocyanates, 61 to 450 parts by weight of castor oil and / or epoxidized fatty acid esters ring-opened with Cι_8-alkyl alcohols, in the leather finishing.
Vorzugsweise wird eine Polyurethandispersion verwendet, deren Polyurethanfestkörper, bezogen auf 100 Gewichtsteile Di- und/oder Polyisocyanate, 80 bis 200 Gewichtsteile Rizinusöl und/oder mit Ci-8-Alkylalkoholen ringgeöffnete epoxidierte Fettsäureester ent¬ hält.Preferably a polyurethane dispersion is used, the polyurethane solids, based on 100 parts by weight of di- and / or polyisocyanates, 80 to 200 parts by weight of castor oil and / or with Ci-8-alkyl alcohols contains ring-opened epoxidized fatty acid esters.
Als epoxidierte Fettsäureester, deren Epoxidringe mit Ci-8-Alkylalkoholen geöffnet werden, eignen sich vorzugsweise epoxidierte Fettsäuremono-, -di- und/oder -triglyceride, die durch Epoxidierung ungesättigter Öle, insbesondere Sojaöl, Leinöl, Tal1- öl, Bau wollsaatöl, Erdnußöl, Palmöl, Sonnenblumenöl, Rüböl und/oder Klauenöl, zugänglich sind. Gemäß dem in DE-PS 857-364 be¬ schriebenen Verfahren können ungesättigte Fettsäureester durch Um¬ setzung mit Peressigsäure in Anwesenheit saurer Katalysatoren oder mit in situ aus Ameisensäure und Wasserstoffperoxid gebildeter Perameisensäure epoxidiert werden. Anschließend' werden die epoxidierten Fettsäureester mit einwertigen Cι_8-A1kylalkoholen, beispielsweise Methanol, Ethanol, n-Propanol, iso-Propanol , n- Butanol, n-Pentanol, n-Hexanol, 2-Ethylhexanol, n-Heptanol und/oder n-Octanol, vorzugsweise jedoch mit Methanol in Gegenwart von Kata¬ lysatoren, beispielsweise Natriummethylat oder Kaliumhydroxid, bei Temperaturen zwischen 40 und 160 °C und Drücken zwischen 104 und 3*10^ Pa umgesetzt.Epoxidized fatty acid esters, the epoxy rings of which are opened with Ci-8-alkyl alcohols, are preferably epoxidized fatty acid mono-, di- and / or triglycerides which are obtained by epoxidation of unsaturated oils, especially soybean oil, linseed oil, talc oil, construction oil seed oil, peanut oil , Palm oil, sunflower oil, rape oil and / or claw oil are accessible. According to the process described in DE-PS 857-364, unsaturated fatty acid esters can be epoxidized by reaction with peracetic acid in the presence of acidic catalysts or with performic acid formed in situ from formic acid and hydrogen peroxide. Then ' the epoxidized fatty acid esters with monohydric C 8 alkyl alcohols, for example methanol, ethanol, n-propanol, isopropanol, n-butanol, n-pentanol, n-hexanol, 2-ethylhexanol, n-heptanol and / or n-octanol , but preferably with methanol in the presence of catalysts, for example sodium methylate or potassium hydroxide, at temperatures between 40 and 160 ° C and pressures between 10 4 and 3 * 10 ^ Pa.
Als weitere Polyol-Komponente können die erfindungsgemäß zu ver¬ wendenden Polyurethane Polyesterpolyole enthalten, die aus aliphatischen und/oder aromatischen Dicarbonsäuren und Diolen auf¬ gebaut sind. Als aliphatische Dicarbonsäuren eignen sich bei¬ spielsweise Bernsteinsäure, Adipinsäure, Korksäure, Azelainsäure, Sebacinsäure, Brassylsäure und/oder Dimer-fettsäuren. Beispiele geeigneter aromatischer Dicarbonsäuren sind Phthalsäure, Isophthalsäure, Terephthalsäure und/oder Tetrahydrophthalsäure. Als aliphatische Dicarbonsäure wird Adipinsäure und als aromatische Dicarbonsäure Isophthalsäure bevorzugt. Die genannten Dicarbonsäuren werden in an sich bekannter Weise mit Diolen, beispielweise Ethylenglykol , 1,2-Propandiol, 1,3-Propandiol, Diethylenglykol , 1,4-Butandiol , 1,6-Hexandiol, 1,10-Decandiol , Dimerocenol (SovermolR 650NS, Henkel KGaA) und/oder Neopentylglykol , verestert.As a further polyol component, the polyurethanes to be used according to the invention may contain polyester polyols which are composed of aliphatic and / or aromatic dicarboxylic acids and diols. Suitable aliphatic dicarboxylic acids are, for example, succinic acid, adipic acid, suberic acid, azelaic acid, sebacic acid, brassylic acid and / or dimer fatty acids. Examples of suitable aromatic dicarboxylic acids are phthalic acid, isophthalic acid, terephthalic acid and / or tetrahydrophthalic acid. Adipic acid is preferred as the aliphatic dicarboxylic acid and isophthalic acid is preferred as the aromatic dicarboxylic acid. The dicarboxylic acids mentioned are mixed in a manner known per se with diols, for example ethylene glycol, 1,2-propanediol, 1,3-propanediol, diethylene glycol, 1,4-butanediol, 1,6-hexanediol, 1,10-decanediol, dimerocenol (SovermolR 650NS, Henkel KGaA) and / or neopentylglycol, esterified.
Die erfindungsgemäß zu verwendenden Polyurethane können ferner Polyetherpolyole mit mittleren Molekulargewichten zwischen 1 000 und 20000, vorzugsweise zwischen 3 000 und 12000, enthalten. Be¬ sonders bevorzugt werden Polyetherpolyole der allgemeinen FormelThe polyurethanes to be used according to the invention may also contain polyether polyols with average molecular weights between 1,000 and 20,000, preferably between 3,000 and 12,000. Polyether polyols of the general formula are particularly preferred
Figure imgf000006_0001
in der R einen Alkoxyrest bedeutet, der sich von Glycerin, Digly- cerin, Polyglycerin mit einem Polymerisationsgrad x zwischen 3 und 6, Trimethylolpropan oder Trimethylolethan ableitet, der Index x den Polymerisationsgrad des Alkoxyrestes bedeutet, die Indices y eine Zahl zwischen 1 und 8 und z eine Zahl zwischen 0 und 8 bedeu¬ ten, mit der Maßgabe, daß die Summe y + z zwischen 1 und 8 liegt, die Indices a eine Zahl zwischen 1 und 15, b eine Zahl zwischen 20 und 100, c eine Zahl zwischen 1 und 15, d eine Zahl zwischen 20 und 150 und e eine Zahl zwischen 1 und 15 bedeuten, mit der Maßgabe, daß - bezogen auf alle Ethylenoxid- und Propylenoxideinheiten des Polyetherpolyols - die Summen a + c + e zwischen 3 und 40, b + d zwischen 40 und 300 und c + e zwischen 1 und 15 liegen. Bevorzugt werden solche Polyetherpolyole der allgemeinen Formel, in der R eine Alkoxyrest bedeutet, der sich von Glycerin oder Trimethylol¬ propan ableitet, die Indices y 2 oder 3 und z 0 oder 1 bedeuten, mit der Maßgabe, daß die Summe y + z 2 oder 3 ist, und die Indices af c und e jeweils eine Zahl zwischen 1 und 5 und b und d jeweils eine Zahl zwischen 30 und 100 bedeuten, mit der Maßgabe, daß bezogen auf alle Ethylenoxid- und Propylenoxideinheiten des Polyetherpolyols - die Summen a + c + e zwischen 3 und 20, b + d zwischen 60 und 200 und c + e zwischen 1 und 10 liegen. Die Polyetherpolyole der allgemeinen Formel sind bekannte Verbindungen, die in an sich bekannter Weise durch Alkoxylierung von Glycerin, Diglycerin, Polyglycerin mit einem Polymerisationsgrad zwischen 3 und 6, Trimethylolpropan oder Trimethylolethan mit Ethylenoxid und Propylenoxid bei Temperaturen zwischen 110 und 200 °C und Drücken zwischen 10^ und 2-10^ Pa zugänglich sind.
Figure imgf000006_0001
in which R denotes an alkoxy radical which is derived from glycerol, diglycerol, polyglycerol with a degree of polymerization x between 3 and 6, trimethylolpropane or trimethylolethane, the index x means the degree of polymerization of the alkoxy radical, the indices y are a number between 1 and 8 and z means a number between 0 and 8, with the proviso that the sum y + z is between 1 and 8, the indices a a number between 1 and 15, b a number between 20 and 100, c a number between 1 and 15, d is a number between 20 and 150 and e is a number between 1 and 15, with the proviso that - based on all ethylene oxide and propylene oxide units of the polyether polyol - the sums a + c + e between 3 and 40, b + d are between 40 and 300 and c + e between 1 and 15. Preference is given to those polyether polyols of the general formula in which R is an alkoxy radical derived from glycerol or trimethylolpropane, the indices y 2 or 3 and z are 0 or 1, with the proviso that the sum y + z 2 or 3, and the indices a f c and e each represent a number between 1 and 5 and b and d each represent a number between 30 and 100, with the proviso that based on all ethylene oxide and propylene oxide units of the polyether polyol - the sums a + c + e between 3 and 20, b + d between 60 and 200 and c + e between 1 and 10. The polyether polyols of the general formula are known compounds which are prepared in a manner known per se by alkoxylation of glycerol, diglycerol, polyglycerol with a degree of polymerization between 3 and 6, trimethylolpropane or trimethylolethane with ethylene oxide and propylene oxide at temperatures between 110 and 200 ° C. and pressures between 10 ^ and 2-10 ^ Pa are accessible.
Um die Dispergierbarkeit in Wasser zu gewährleisten, werden bei der Herstellung erfindungsgemäß zu verwendender Polyurethane Dihydroxy- und/oder Diaminoverbindungen eingesetzt, die mindestens eine an¬ ionische Gruppe, vorzugsweise eine oder mehrere Carboxylat-, Sulfonat- und/oder Ammoniumgruppen enthalten, beispielsweise Dimethylolpropionsäure, Weinsäure und/oder 2,4- Diaminobenzolsulfonsäure.In order to ensure dispersibility in water, dihydroxy and / or diamino compounds which contain at least one anionic group, preferably one or more carboxylate, sulfonate and / or ammonium groups, for example dimethylolpropionic acid, are used in the production of polyurethanes to be used according to the invention. Tartaric acid and / or 2,4-diaminobenzenesulfonic acid.
Die erfindungsgemäß zu verwendenden Polyurethane enthalten, bezogen auf 100 Gewichtsteile Isocyanatkomponente, 61 bis 450 Gewichtsteile Ricinusöl und/oder mit Cι_8-Alkylalkoholen ringgeöffnete epoxidierte Fettsäureester, 0 bis 300 Gewichtsteile Polyesterpolyole, 0 bis 60 Gewichtsteile Polyetherpolyole und 5 bis 50 Gewichtsteile mindestens eine anionische Gruppe tragende Dihydroxy-und/oder Diaminoverbindungen, vorzugsweise 80 bis 200 Gewichtsteile Ricinusöl und/oder mit Cι_8-Alkylalkoholen riπgge- öffnete epoxidierte Fettsäureester, 1 bis 180 Gewichtsteile Polyesterpolyole, 0 bis 20 Gewichtsteile Polyetherpolyole und 5 bis 30 Gewichtsteile mindestens eine anionische Gruppe tragende Dihydroxy-und/oder Diaminoverbindungen, mit der Maßgabe, daß der Anteil der OH-Äquivalente der Polyesterpolyole, Polyetherpolyole und mindestens eine anionische Gruppe tragenden Dihydroxyverbindungen zwischen 10 und 80 %, vorzugsweise zwischen 20 und 70 % aller OH-Äquivalente liegt.The polyurethanes to be used according to the invention contain, based on 100 parts by weight of isocyanate component, 61 to 450 parts by weight of castor oil and / or epoxidized fatty acid esters ring-opened with C8 -8 alkyl alcohols, 0 to 300 parts by weight of polyester polyols, 0 to 60 parts by weight of polyether polyols and 5 to 50 parts by weight bearing at least one anionic group Dihydroxy and / or diamino compounds, preferably 80 to 200 parts by weight of castor oil and / or epoxidized fatty acid esters opened with C 8 alkyl alcohols, 1 to 180 parts by weight of polyester polyols, 0 to 20 parts by weight of polyether polyols and 5 to 30 parts by weight of dihydroxy and at least one anionic group / or diamino compounds, with the proviso that the proportion of the OH equivalents of the polyester polyols, polyether polyols and at least one anionic group Dihydroxy compounds is between 10 and 80%, preferably between 20 and 70% of all OH equivalents.
Als organische Di- und/oder Polyisocyanate eignen sich aliphatische und/oder aromatische Di- und/oder Triisocyanate, beispielsweise Dicyclohexylmethan-4,4'-diisocyanat, 1,6-Hexandiisocyanat, 3- Isocyanatomethyl-3,5,5-trimethylcyclohexylisocyanat (Isophorondi- isocyanat) , Tetramethylendiisocyanate, Trimethylhexamethylendi- isocyanate, Dimer-fettsäurediisocyanate, 1 ,4-Phenylendiisocyanat, Diphenyl ethandiisocyanate, Toluol-2,4- und/oder Tolu- ol-2,6-diisocyanat, 2,4f4'-Trιisocyanato-diphenylether und/oder 4' ,4' ' ,4 '-Triisocyanato-triphenyl ethan. Bevorzugt werden ali¬ phatische Diisocyanate, insbesondere Isophorondiisocyanat, Di- cyclohexylmethan-4,4'-diisocyanat, 1,6-Hexandiisocyanat und/oder Dimer-fettsäurediisocyanate.Suitable organic di- and / or polyisocyanates are aliphatic and / or aromatic di- and / or triisocyanates, for example dicyclohexylmethane-4,4'-diisocyanate, 1,6-hexane diisocyanate, 3-isocyanatomethyl-3,5,5-trimethylcyclohexyl isocyanate ( Isophorone diisocyanate), tetramethylene diisocyanates, trimethylhexamethylene diisocyanate, dimer fatty acid diisocyanates, 1,4-phenylene diisocyanate, diphenyl ethane diisocyanate, toluene-2,4- and / or toluene-2,6-diisocyanate, 2.4 f 4'- Trιisocyanato-diphenyl ether and / or 4 ', 4'',4' -Triisocyanato-triphenyl ethane. Aliphatic diisocyanates, in particular isophorone diisocyanate, dicyclohexylmethane-4,4'-diisocyanate, 1,6-hexane diisocyanate and / or dimer fatty acid diisocyanates, are preferred.
Des weiteren können sogenannte blockierte Di- und/oder Polyisocya¬ nate alleine oder in Kombination mit den obengenannten nicht blok- kierten Di- und/oder Polyisocyanaten eingesetzt werden. Die blok- kierten Di- und Polyisocyanate sind bei Raumtemperatur gegenüber Hydroxylgruppen beständig und reagieren erst bei Temperaturen oberhalb von 50 °C. Bezogen auf die Gesamtmenge der eingesetzten Di- und/oder Polyisocyanate liegt der Gehalt blockierter Di- und/oder Polyisocyanate vorzugsweise zwischen 0 und 60 Gew.-%, be¬ sonders bevorzugt zwischen 0 und 10 Gew.-%. Die Herstellung blok- kierter Di- und Polyisocyanate erfolgt durch Umsetzung organischer Di- oder Polyisocyanate, beispielsweise Isophorondiisocyanat, mit einem Alkohol, beispielsweise Phenol oder m-Kresol, in solchen Mengen, daß alle Isocyanatgruppen blockiert werden.Furthermore, so-called blocked di- and / or polyisocyanates can be used alone or in combination with the above-mentioned unblocked di- and / or polyisocyanates. The blocked di- and polyisocyanates are resistant to hydroxyl groups at room temperature and only react at temperatures above 50 ° C. Based on the total amount of the di- and / or polyisocyanates used, the content of blocked di- and / or polyisocyanates is preferably between 0 and 60% by weight, particularly preferably between 0 and 10% by weight. Blocked di- and polyisocyanates are produced by reacting organic di- or polyisocyanates, for example isophorone diisocyanate, with an alcohol, for example phenol or m-cresol, in amounts such that all isocyanate groups are blocked.
Die erfindungsgemäß zu verwendenden Polyurethane können nach be¬ kannten Verfahren hergestellt werden (Ullmanns Encyclopädie der technischen Chemie, Band 19, Seiten 302 ff., Verlag Chemie Wein¬ heim, 1980). Vorzugsweise werden Di- und/oder Polyisocyanate mit Polyolen und mindestens eine anionische Gruppe tragenden Dihydroxy- und/oder Diaminoverbindungen in Gegenwart von Lösungsmitteln, bei¬ spielsweise N-Methylpyrrolidon und/oder Methylethylketon, und ge¬ gebenenfalls Katalysatoren, wie N-Methylmorpholin, bei Temperaturen zwischen 60 und 120 °C zu Präpolymeren umgesetzt. Danach wird die Polyurethan-Präpolymermasse in Wasser dispergiert und anschließend gegebenenfalls mit Kettenverlängerern, wie alkoxylierten Glycerinen und/oder Diaminen, beispielsweise Ethylendiamin, Hexamethylendiamin und/oder Piperazin, umgesetzt. Während der Dispergierung und Ket¬ tenverlängerung von Polyurethanen reagieren die im Polyurethan- Präpolymer noch vorhandenen NCO-Gruppen mit Wasser unter Kohlendioxidbildung, wodurch es zu nicht unbeträchtlicher, stören¬ der Schaumbildung kommt. Bei der Herstellung einer erfindungsgemäß zu verwendenden Polyurethandispersion werden jedoch, wenn über¬ haupt, so geringe Schaummengen gebildet, daß fast immer auf einen Zusatz an Entschäumern verzichtet werden kann.The polyurethanes to be used according to the invention can be produced by known processes (Ullmann's Encyclopedia of technical chemistry, volume 19, pages 302 ff., Verlag Chemie Wein¬heim, 1980). Di- and / or polyisocyanates with polyols and at least one anionic group containing dihydroxy and / or diamino compounds in the presence of solvents, for example N-methylpyrrolidone and / or methyl ethyl ketone, and, if appropriate, catalysts, such as N-methylmorpholine, are preferably added Temperatures between 60 and 120 ° C converted to prepolymers. The polyurethane prepolymer composition is then dispersed in water and then, if appropriate, reacted with chain extenders, such as alkoxylated glycerols and / or diamines, for example ethylenediamine, hexamethylenediamine and / or piperazine. During the dispersion and chain extension of polyurethanes, the NCO groups still present in the polyurethane prepolymer react with water to form carbon dioxide, which leads to not inconsiderable, disruptive foam formation. When producing a polyurethane dispersion to be used according to the invention, however, such small amounts of foam are formed, if at all, that it is almost always possible to dispense with the addition of defoamers.
Eine Polyurethandispersion mit einem hohen Gehalt an Rizinusöl und/oder mit Cι_8-Alkylalkoholen ringgeöffneten epoxidierten Fett¬ säureestern als Polyolko ponente im Polyurethanfestkörper, einem Feststoffgehalt zwischen 10 und 50 Gew.-% und einer Brookfield- Viskosität bei 20 °C zwischen 10 und 5000 mPas kann erfindungsgemäß in der Lederzurichtung in Grundierungs-, Farb-und/oder Abschlu߬ flotten eingesetzt werden. Als weitere Bestandteile können die Zu¬ richtflotten Pigmentzubereitungen, filmbildende Substanzen in Form wäßriger Dispersionen, wie Polyacrylate und/oder Polyurethane, Binde- und Füllmittel, Mattierungs ittel, Penetratoren und/oder Weichmacher enthalten. Die Applikation der Zurichtflotten kann mit allen in der Lederzurichtung üblichen Technologien, beispielsweise durch Spritzen, Plüschen, Gießen und/oder Walzenauftrag erfolgen. Die Zurichtflotten enthalten erfindungsgemäß zu verwendende Poly¬ urethandispersionen in Mengen von 1 bis 60 Gew.-%.A polyurethane dispersion with a high content of castor oil and / or epoxidized fatty acid esters ring-opened with C8-alkyl alcohols as polyol component in the polyurethane solid, a solids content between 10 and 50 wt .-% and a Brookfield viscosity at 20 ° C between 10 and 5000 mPas can be used according to the invention in leather finishing in primer, color and / or finishing liquors. The additive liquors may contain pigment preparations, film-forming substances in the form of aqueous dispersions, such as polyacrylates and / or polyurethanes, binders and fillers, matting agents, penetrators and / or plasticizers as further constituents. The finishing liquors can be applied using all of the technologies customary in leather finishing, for example by spraying, plushing, pouring and / or roller application. The finishing liquors contain polyurethane dispersions to be used according to the invention in amounts of 1 to 60% by weight.
Leder, die mit einer erfindungsgemäß zu verwendenden Polyurethan¬ dispersion zugerichtet wurden, besitzen im Vergleich zu Ledern, die mit einer gemäß DE 37 02 615 hergestellten Polyurethandispersion zugerichtet wurden, deutlich verbesserte Echtheiten, insbesondere eine deutlich verbesserte Naßreibechtheit. Leather which has been finished with a polyurethane dispersion to be used according to the invention has significantly improved fastness properties, in particular a clearly improved wet rub fastness, compared to leathers which have been finished with a polyurethane dispersion prepared in accordance with DE 37 02 615.
BeispieleExamples
Herstellung erfindunqsqe äßer wäßriger PolyurethandispersionenProduction of inventive aqueous polyurethane dispersions
Zur Bestimmung des Feststoffgehaltes der wäßrigen Polyurethan¬ dispersionen wurden 10,0 g der jeweiligen Polyurethan-Dispersion in einer Aluminiumschale eingewogen. Nach 15 stündigem Trocknen im Trockenschrank bei 125 °C wurde durch Wiegen der Aluminiumschale der Trockenrückstand ermittelt.To determine the solids content of the aqueous polyurethane dispersions, 10.0 g of the respective polyurethane dispersion were weighed into an aluminum dish. After drying in the drying cabinet at 125 ° C. for 15 hours, the dry residue was determined by weighing the aluminum pan.
Berechnungcalculation
Trockenrückstand (g) • 100Dry residue (g) • 100
= Feststoffgehalt (Gew.-%)= Solids content (% by weight)
Einwaage (g)Weight (g)
Beispiel 1example 1
In einen gut getrockneten Laborreaktor aus Glas mit 3-stufigem Edelstahl-MIG-Rührer wurden bei 25 °C 182,6 g Polyester aus Adipinsäure, Isophthalsäure und Diethylenglykol mit einer OH-Zahl (OHZ) von 59, 129,2 g Sojaölepoxid, ringgeöffnet mit Methanol (OHZ = 200), 30,0 g Di ethylolpropionsäure, 27,2 g N-Methylmorpholin und 45,1 g N-Methylpyrrolidon gegeben. Nach der Homogenisierung wurden 146,7 g Isophorondiisocyanat zu dem Polyolge isch gegeben. Nachdem das Reaktionsgemisch nach 2,5 Stunden bei 80 °C einen NCO-Gehalt von 2,4 Gew.-% erreicht hatte, wurden 528,7 g voll entsalztes Was¬ ser mit einer Temperatur von 15 °C zu der Prepolymer asse gegeben.In a well-dried glass laboratory reactor with a 3-stage stainless steel MIG stirrer, 182.6 g of polyester from adipic acid, isophthalic acid and diethylene glycol with an OH number (OHZ) of 59, 129.2 g of soybean oil epoxide were ring-opened at 25 ° C with methanol (OHZ = 200), 30.0 g of diethylolpropionic acid, 27.2 g of N-methylmorpholine and 45.1 g of N-methylpyrrolidone. After homogenization, 146.7 g of isophorone diisocyanate was added to the polyfolder. After the reaction mixture had reached an NCO content of 2.4% by weight after 2.5 hours at 80 ° C., 528.7 g of completely demineralized water at a temperature of 15 ° C. were added to the prepolymer.
Danach wurden zur Kettenverlängerung 3,3 g Glycerin-7 Mol Ethylenoxid 81 Mol Propylenoxid (OHZ = 34) zu der 35 °C warmen Polyurethandispersion gegeben. Nach Erwärmen auf 60 °C, wobei die Polyurethandispersion durch das aus der Reaktion zwischen den NCO-Gruppen und Wasser gebildete Kohlendioxid aufschäumte (Schaumhöhe: 3 cm), wurde 4 Stunden bei dieser Temperatur gerührt und anschließend auf Raumtemperatur abgekühlt. Es wurde eine weiße, stabile, 39,6 gew.-%ige wäßrige Polyurethandispersion mit einem pH-Wert von 7,1 und einer Bookfield-Viskosität bei 20 °C von 550 mPas erhalten.Then 3.3 g of glycerol-7 mol of ethylene oxide 81 mol of propylene oxide (OHZ = 34) were added to the 35 ° C. warm polyurethane dispersion for chain extension. After heating to 60 ° C., the polyurethane dispersion foaming due to the carbon dioxide formed from the reaction between the NCO groups and water (Foam height: 3 cm) was stirred at this temperature for 4 hours and then cooled to room temperature. A white, stable, 39.6% by weight aqueous polyurethane dispersion with a pH of 7.1 and a bookfield viscosity at 20 ° C. of 550 mPas was obtained.
Beispiel 2Example 2
Das Polyurethanprepolymer wurde analog Beispiel 1 in der gleichen Apparatur hergestellt. Anstelle von 129,2 g wurden 226,1 g Sojaölepoxid, ringgeöffnet mit Methanol (OHZ = 200) eingesetzt. Zu dem erhaltenen Prepoly er wurden anschließend 528,7 g voll ent¬ salztes Wasser einer Temperatur von 15 °C gegeben. Nach Erwärmen auf 60 °C wurde 4 Stunden bei dieser Temperatur gerührt (Schaumhö¬ he: 1 cm) und danach auf Raumtemperatur abgekühlt. Es wurde eine weiße, stabile, 40,4 gew.- ige wäßrige Polyurethandispersion mit einem pH-Wert von 7,2 und einer Brookfield-Viskosität bei 20 °C von 3500 mPas erhalten.The polyurethane prepolymer was prepared in the same apparatus as in Example 1. Instead of 129.2 g, 226.1 g of soybean oil epoxide, ring-opened with methanol (OHZ = 200), were used. 528.7 g of completely deionized water at a temperature of 15.degree. C. were then added to the prepoly obtained. After heating to 60 ° C., the mixture was stirred at this temperature for 4 hours (foam height: 1 cm) and then cooled to room temperature. A white, stable, 40.4% by weight aqueous polyurethane dispersion with a pH of 7.2 and a Brookfield viscosity at 20 ° C. of 3500 mPas was obtained.
Verαleichsbeispiel 1 (gemäß DE 3702615)Comparative Example 1 (according to DE 3702615)
Analog Beispiel 1 wurde in der gleichen Apparatur eine Polyurethandispersion hergestellt. Anstelle von 129,2 g wurden je¬ doch 64,6 g Sojaölepoxid, ringgeöffnet mit Methanol (OHZ = 200) eingesetzt. Nach Zugabe von 3,3 g Glycerin 7 Mol Ethylenoxid 31 Mol Propylenoxid (OHZ = 34) und Erwärmen auf 60 °C trat Schaumbil¬ dung auf (Schaumhöhe: 9 cm). Nach 4-stündigem Rühren bei 60 °C wurde auf Raumtemperatur abgekühlt. Es wurde eine weiße, stabile, 40,2 gew.-%ige wäßrige Polyurethandispersion mit einem pH-Wert von 7,0 und einer Brookfield-Viskosität bei 20 °C von 800 mPas erhal¬ ten. Beispiel 3A polyurethane dispersion was prepared in the same apparatus as in Example 1. Instead of 129.2 g, however, 64.6 g of soybean oil epoxide, ring-opened with methanol (OHZ = 200), were used. After adding 3.3 g of glycerol 7 mol of ethylene oxide 31 mol of propylene oxide (OHZ = 34) and heating to 60 ° C., foam formation occurred (foam height: 9 cm). After stirring for 4 hours at 60 ° C., the mixture was cooled to room temperature. A white, stable, 40.2% by weight aqueous polyurethane dispersion with a pH of 7.0 and a Brookfield viscosity at 20 ° C. of 800 mPas was obtained. Example 3
Die Polyurethandispersion wurde analog Beispiel 1 in der gleichen Apparatur bei gleichem Füllstand hergestellt. Anstelle von 129,2 g Sojaölepoxid, ringgeöffnet mit Methanol wurden 129,2 g Rizinusöl (OHZ = 158) eingesetzt. Nach Zugabe von 3,3 g Glycerin 7 Mol Ethylenoxid 81 Mol Propylenoxid (OHZ = 34) und Erwärmen auf 60 °C wurden geringe Schaummengen gebildet (Schaumhöhe: 3 cm). Es wurde eine weiße, stabile, 39,3 gew.-%ige wäßrige Polyurethandispersion mit einem pH-Wert von 7,1 und einer Brookfield-Viskosität bei 20 °C von 2500 mPas erhalten.The polyurethane dispersion was prepared analogously to Example 1 in the same apparatus at the same level. Instead of 129.2 g soybean oil epoxide, ring-opened with methanol, 129.2 g castor oil (OHZ = 158) were used. After adding 3.3 g of glycerol 7 mol of ethylene oxide 81 mol of propylene oxide (OHZ = 34) and heating to 60 ° C, small amounts of foam were formed (foam height: 3 cm). A white, stable, 39.3% by weight aqueous polyurethane dispersion with a pH of 7.1 and a Brookfield viscosity at 20 ° C. of 2500 mPas was obtained.
Beispiel 4Example 4
Die Polyurethandispersion wurde analog Beispiel 2 in der gleichen Apparatur hergestellt. Anstelle von 226,1 g Sojaölepoxid, ringgeöffnet mit Methanol wurden 226,1 g Rizinusöl (OHZ = 158) eingesetzt. Nach Erwärmen der Dispersion auf 60 °C wurden geringe Mengen an Schaum gebildet (Schaumhöhe: 2 cm). Es wurde eine weiße, stabile, 40,9 gew.-%ige wäßrige Polyurethandispersion mit einem pH-Wert von 7,4 und einer Brookfield-Viskosität bei 20 °C von 4200 mPas erhalten.The polyurethane dispersion was prepared in the same apparatus as in Example 2. Instead of 226.1 g of soybean oil epoxide, ring-opened with methanol, 226.1 g of castor oil (OHZ = 158) were used. After the dispersion had been heated to 60 ° C., small amounts of foam were formed (foam height: 2 cm). A white, stable, 40.9% by weight aqueous polyurethane dispersion with a pH of 7.4 and a Brookfield viscosity at 20 ° C. of 4200 mPas was obtained.
Vergleichsbeispiel 2 (gemäß DE 3702 615)Comparative Example 2 (according to DE 3702 615)
Die Polyurethandispersion wurde analog Beispiel 3 in der gleichen Apparatur hergestellt. Anstelle von 129,2 g wurden 32,3 Rizinusöl (OHZ = 158) eingesetzt. Nach Zugabe von 3,3 g Glycerin 7 Mol Ethylenoxid • 81 Mol Propylenoxid (OHZ = 34) und Erwärmen auf 60 °C schäumte die Polyurethandispersion auf (Schaumhöhe: 14,5 cm). Es wurde eine weiße, stabile, 39,9 gew.-%ige wäßrige Polyurethandispersion mit einem pH-Wert von 7,0 und einer Brookfield-Viskosität bei 20 °C von 1800 mPas erhalten. AnwendungsbeispieleThe polyurethane dispersion was prepared in the same apparatus as in Example 3. Instead of 129.2 g, 32.3 castor oil (OHZ = 158) was used. After adding 3.3 g of glycerol 7 moles of ethylene oxide • 81 moles of propylene oxide (OHZ = 34) and heating to 60 ° C, the polyurethane dispersion expanded (foam height: 14.5 cm). A white, stable, 39.9% by weight aqueous polyurethane dispersion with a pH of 7.0 and a Brookfield viscosity at 20 ° C. of 1800 mPas was obtained. Examples of use
Tl. bedeutet GewichtsteileTl means parts by weight
Ausgangsmaterial: naturelle Crust-OberlederBase material: natural crust leather
Kopffärbung: 100 Tl. Metallkomplexfarbstoff-Lösung 200 Tl. Polyglykolether 200 Tl. WasserHead coloring: 100 parts of metal complex dye solution 200 parts of polyglycol ether 200 parts of water
1 mal Kreuz spritzenSpray cross once
Grundierung: 100 Tl. PigmentPrimer: 100 parts of pigment
30 Tl. Wachsdispersion30 parts of wax dispersion
10 Tl. Ölemulsion10 parts oil emulsion
200 Tl. Polyacrylat-Dispersion200 parts of polyacrylate dispersion
300 Tl. Wasser300 parts of water
2 mal Kreuz spritzen bügeln 80 °C / 100 bar 1 mal Kreuz spritzenSpray 2 times cross iron 80 ° C / 100 bar Spray 1 time cross
Abschluß: 100 Tl. erfiπdungsgemäße Polyurethan-Disper¬ sion (siehe Tabelle) 100 Tl. WasserConclusion: 100 parts of polyurethane dispersion according to the invention (see table) 100 parts of water
2 mal Kreuz spritzenSpray cross twice
Die Naßreibechtheit der zugerichteten Leder wurde nach Veslic be¬ stimmt. Bewertuπgsskala der Naßreibechtheit: Note 5 = kein Abrieb, Note 4 = geringer Abrieb, Note 3 = deutlicher Abrieb, Note 2 = starker Ab¬ rieb, Note 1 = sehr starker Abrieb.The wet rub fastness of the finished leather was determined according to Veslic. Rating scale of the wet rub fastness: grade 5 = no abrasion, grade 4 = low abrasion, grade 3 = significant abrasion, grade 2 = strong abrasion, grade 1 = very strong abrasion.
Tabelle 1Table 1
Polyurethandispersion Naßreibechtheit hergestellt nach Beispiel Anzahl Hübe NotePolyurethane dispersion wet rub fastness produced according to the example number of strokes
500500
500500
Vergleich 1 200Comparison 1,200
300300
300300
Vergleich 2 200 3 - 4 Comparison 2,200 3-4

Claims

Patentansprüche Claims
1. Verwendung einer wäßrigen Polyurethandispersion mit einem Feststoffgehalt zwischen 10 und 50 Gew.-% und einer Brookfield-Viskosität bei 20 °C zwischen 10 und 5000 mPas, de¬ ren Polyurethanfestkörper, bezogen auf 100 Gewichtsteile Di- und/oder Polyisocyanate, 61 bis 450 Gewichtsteile Rizinusöl und/oder mit Cι_8-Alkylalkoholen ringgeöffnete epoxidierte Fettsäureester enthält, in der Lederzurichtung.1. Use of an aqueous polyurethane dispersion with a solids content between 10 and 50 wt .-% and a Brookfield viscosity at 20 ° C between 10 and 5000 mPas, their polyurethane solids, based on 100 parts by weight of di- and / or polyisocyanates, 61 to Contains 450 parts by weight of castor oil and / or epoxidized fatty acid esters ring-opened with C8 alkyl alcohols in the leather finishing.
2. Verwendung nach Anspruch 1, dadurch gekennzeichnet, daß eine Polyurethandispersion, deren Polyurethanfestkörper, bezogen auf 100 Gewichtsteile Di- und/oder Polyisocyanate, 80 bis 200 Ge- wichtsteile Rizinusöl und/oder mit Cι_8-Alkylalkoholen ring¬ geöffnete epoxidierte Fettsäureester enthält, verwendet wird.2. Use according to claim 1, characterized in that a polyurethane dispersion whose polyurethane solids, based on 100 parts by weight of di- and / or polyisocyanates, contains 80 to 200 parts by weight of castor oil and / or epoxidized fatty acid esters ring-opened with C 8 alkyl alcohols becomes.
3. Verwendung nach einem oder beiden der Ansprüche 1 bis 2, da¬ durch gekennzeichnet, daß in der zu verwendenden Polyurethandispersion Rizinusöl und/oder mit Cι_8-Alkylalkoholen riπggeöffnete epoxidierte Fettsäuremono-, -di- und/oder -triglyceride enthalten sind.3. Use according to one or both of claims 1 to 2, characterized in that the polyurethane dispersion to be used contains castor oil and / or epoxidized fatty acid mono-, di- and / or triglycerides opened with C8_8 alkyl alcohols.
4. Verwendung nach Anspruch 3, dadurch gekennzeichnet, daß mit Ci-8-Alkylalkoholen ringgeöffnete epoxidierte Fettsäuremono-, -di- und/oder -triglyceride mit Methanol ringgeöffnetes Soja¬ öl-, Leinöl-, Tallöl-, Baumwollsaatöl-, Erdnußöl-, Palmöl-, Sonnenblumenöl-, Rüböl- und/oder Klauenölepoxid sind. 4. Use according to claim 3, characterized in that with Ci-8-alkyl alcohols ring-opened epoxidized fatty acid mono-, di- and / or triglycerides with methanol ring-opened soybean oil, linseed oil, tall oil, cottonseed oil, peanut oil, Palm oil, sunflower oil, rape oil and / or claw oil epoxy are.
PCT/EP1991/001132 1990-06-27 1991-06-19 Use of aqueous polyurethane dispersions in leather dressing WO1992000336A1 (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
DEP4020456.1 1990-06-27
DE19904020456 DE4020456A1 (en) 1990-06-27 1990-06-27 USE OF AQUEOUS POLYURETHANE DISPERSIONS IN LEATHER MAKING

Publications (1)

Publication Number Publication Date
WO1992000336A1 true WO1992000336A1 (en) 1992-01-09

Family

ID=6409185

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/EP1991/001132 WO1992000336A1 (en) 1990-06-27 1991-06-19 Use of aqueous polyurethane dispersions in leather dressing

Country Status (2)

Country Link
DE (1) DE4020456A1 (en)
WO (1) WO1992000336A1 (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US8076001B2 (en) 2008-09-02 2011-12-13 Ppg Industries Ohio, Inc Crosslinked coatings comprising lactide
US8614286B2 (en) 2008-09-02 2013-12-24 Ppg Industries Ohio, Inc. Biomass derived radiation curable liquid coatings
US9650540B2 (en) 2008-09-02 2017-05-16 Ppg Industries Ohio, Inc. Radiation curable coating compositions comprising a lactide reaction product
CN118126278A (en) * 2024-05-06 2024-06-04 旭川化学(苏州)有限公司 Tall oil-based polyurethane synthetic leather and preparation method and application thereof

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE29806416U1 (en) * 1998-04-08 1998-07-30 Schaefer, Philipp, 30519 Hannover Goat leather with a grained coating

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0152585A1 (en) * 1983-12-24 1985-08-28 Henkel Kommanditgesellschaft auf Aktien Two-component polyurethane adhesive
EP0260499A2 (en) * 1986-09-06 1988-03-23 Henkel Kommanditgesellschaft auf Aktien Use of fatty polyols in the preparation of aqueous polyurethane dispersions
EP0278394A2 (en) * 1987-02-12 1988-08-17 Henkel Kommanditgesellschaft auf Aktien Water-dilutable coatings
EP0278278A1 (en) * 1987-01-29 1988-08-17 Henkel Kommanditgesellschaft auf Aktien Coating and finishing agent for leather

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0152585A1 (en) * 1983-12-24 1985-08-28 Henkel Kommanditgesellschaft auf Aktien Two-component polyurethane adhesive
EP0260499A2 (en) * 1986-09-06 1988-03-23 Henkel Kommanditgesellschaft auf Aktien Use of fatty polyols in the preparation of aqueous polyurethane dispersions
EP0278278A1 (en) * 1987-01-29 1988-08-17 Henkel Kommanditgesellschaft auf Aktien Coating and finishing agent for leather
EP0278394A2 (en) * 1987-02-12 1988-08-17 Henkel Kommanditgesellschaft auf Aktien Water-dilutable coatings

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US8076001B2 (en) 2008-09-02 2011-12-13 Ppg Industries Ohio, Inc Crosslinked coatings comprising lactide
US8614286B2 (en) 2008-09-02 2013-12-24 Ppg Industries Ohio, Inc. Biomass derived radiation curable liquid coatings
US9650540B2 (en) 2008-09-02 2017-05-16 Ppg Industries Ohio, Inc. Radiation curable coating compositions comprising a lactide reaction product
CN118126278A (en) * 2024-05-06 2024-06-04 旭川化学(苏州)有限公司 Tall oil-based polyurethane synthetic leather and preparation method and application thereof

Also Published As

Publication number Publication date
DE4020456A1 (en) 1992-01-02

Similar Documents

Publication Publication Date Title
DE1964998C3 (en) Process for the production of polyurethane elastomers
EP0533730B1 (en) Coating materials
EP0379007B1 (en) Method for the preparation of aqueous, oxidatively drying alkyd resins and their use in or as aqueous lacquers or coating compositions
DE3630045A1 (en) ADHESIVE AND THE USE OF THE ADHESIVE TO MAKE ADHESIVES
DE2644923C2 (en) Process for the coating of textile fabrics
EP2287260A1 (en) Networkable polyurethane dispersions
DE2829199C2 (en)
EP0666276A1 (en) Polyisocyanate mixtures which are liquid above 5 C
DE2215080A1 (en) POWDER-FORMED COATING COMPOSITIONS
EP0507053B1 (en) Aqueous, photocurable urethaneacrylate dispersions
EP0709414B1 (en) Use of partially dehydrated castor oils for the preparation of aqueous polyurethane dispersions and coatings prepared by use of these aqueous polyurethane disperions
EP0778303B1 (en) Polyisocyanates containing allophanate groups based on diphenylmethanediisocyanate and having predominantly or completely blocked isocyanate groups
DE2708442A1 (en) PROCESS FOR THE MANUFACTURE OF MODIFIED, AQUEOUS PLASTIC DISPERSIONS
DE3630422A1 (en) USE OF FAT POLYOLS FOR THE PRODUCTION OF AQUEOUS POLYURETHANE DISPERSIONS
EP0407829B1 (en) Thermosetting mixtures and their use for the production of coatings for heat-resistant substrates
EP0073389B1 (en) Coating and finishing agent for leather, and leather substitute based on a polyurethane-polyurea coating composition
EP1506242A1 (en) Aqueous polyurethane preparations
WO1992000336A1 (en) Use of aqueous polyurethane dispersions in leather dressing
DE2845784A1 (en) METHOD FOR MANUFACTURING POLYURETHANE ELASTOMERS
EP0623591B1 (en) Olefinically unsaturated isocyanates and their use as binder in coating materials
WO1992001817A1 (en) Polyurethanes for priming leather
DE2044803A1 (en) Polyurethane elastomers
EP0160907B1 (en) Polyurethanes soluble or dissolved in aromatic hydrocarbons, process for their preparation and thier use
DE4020455A1 (en) AQUEOUS POLYURETHANE DISPERSION, THEIR PRODUCTION AND USE IN LEATHER MAKING
EP0318751A2 (en) Finishing agent for natural and synthetic leather

Legal Events

Date Code Title Description
AK Designated states

Kind code of ref document: A1

Designated state(s): US

AL Designated countries for regional patents

Kind code of ref document: A1

Designated state(s): AT BE CH DE DK ES FR GB GR IT LU NL SE