EP0000381B1 - Procédé de préparation de produits de polyaddition d'isocyanate contenant des groupes hydroxyles latéraux et produits obtenus par ce procédé - Google Patents

Procédé de préparation de produits de polyaddition d'isocyanate contenant des groupes hydroxyles latéraux et produits obtenus par ce procédé Download PDF

Info

Publication number
EP0000381B1
EP0000381B1 EP78100323A EP78100323A EP0000381B1 EP 0000381 B1 EP0000381 B1 EP 0000381B1 EP 78100323 A EP78100323 A EP 78100323A EP 78100323 A EP78100323 A EP 78100323A EP 0000381 B1 EP0000381 B1 EP 0000381B1
Authority
EP
European Patent Office
Prior art keywords
groups
water
parts
oxazolidine
prepolymers
Prior art date
Legal status (The legal status 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 status listed.)
Expired
Application number
EP78100323A
Other languages
German (de)
English (en)
Other versions
EP0000381A1 (fr
Inventor
Klaus Dr. Noll
Klaus Dr. Nachtkamp
Josef Dr. Pedain
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Bayer AG
Original Assignee
Bayer AG
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 Bayer AG filed Critical Bayer AG
Publication of EP0000381A1 publication Critical patent/EP0000381A1/fr
Application granted granted Critical
Publication of EP0000381B1 publication Critical patent/EP0000381B1/fr
Expired legal-status Critical Current

Links

Classifications

    • 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
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10STECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10S528/00Synthetic resins or natural rubbers -- part of the class 520 series
    • Y10S528/904Isocyanate polymer having stated hydrophilic or hydrophobic property

Definitions

  • the present invention relates to a new process for the preparation of new isocyanate polyaddition products having pendant hydroxyl groups and to the compounds obtainable by this process.
  • the process according to the invention is based on the principle of reacting reactive systems containing isocyanate groups and oxazolidine groups with water, the chain extension reaction taking place essentially with the formation of urea groups from the isocyanate groups and the amino groups hydrolytically released from the oxazolidines, while the hydrolytic cleavage of the oxazolidine groups also takes place comparatively inert hydroxyl groups do not participate in the reaction and are present laterally in the process products.
  • compositions of these publications are generally systems which are stable in the absence of moisture and have oxazolidines and isocyanates which, under the influence of atmospheric moisture, i.e. react under the influence of traces of water to form high-molecular, cross-linked structures.
  • the present invention in particular also relates to an embodiment of this method in which prepolymers which are hydrophilically modified and / or contain an external emulsifier and a preponderant excess of water with respect to the chain extension reaction are used, so that an aqueous dispersion or solution of the polyadducts is obtained directly.
  • the process according to the invention for the first time opens up a possibility of producing predominantly linear polyurethanes which are therefore soluble in common solvents and which have pendant hydroxyl groups and are therefore accessible to a subsequent crosslinking reaction, for example with organic polyisocyanates. Because of their linear structure, the process products according to the invention can be converted without difficulty into aqueous dispersions or solutions, with the simultaneous incorporation of hydrophilic groups and / or with the use of external emulsifiers, from which it is then also possible to subsequently produce simply crosslinkable fabrics.
  • Starting materials for the process according to the invention are essentially linear prepolymers which have a statistical average of 1.8 to 2.2, preferably 2, terminal isocyanate groups and which generally have an average molecular weight of 500 to 10,000, preferably 800 to 4,000.
  • the NCO prepolymers are prepared by known methods of polyurethane chemistry by reacting excess amounts of organic polyisocyanates, preferably diisocyanates, with suitable, preferably difunctional, compounds having groups which are reactive toward isocyanate groups. Starting materials for the preparation of the NCO prepolymers are accordingly.
  • 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.
  • 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.
  • Examples of such preferred diisocyanates are Tetramethylene diisocyanate, hexamethylene diisocyanate, dodecamethylene diisocyanate.
  • 1,4 - diisocyanato - cyclohexane 1 - isocyanato - 3,3,5 - trimethyl - 5 - isocyanatomethylcyclohexane, 4,4 '- diisocyanatodicyclohexylmethane, 4,4' - dilsocyanato - dicyclohexylpropane - (2,2), 1,4 - diisocyanatobenzene, 2,4 - diisocyanatotoluene, 2,6 - diisocyanatotoluene, 4,4 '- diisocyanatodiphenylmethane, 4,4' - diisocyanato - diphenylpropane - (2,2), p - xylylene - diisocyanate or ⁇ , a, a ', ⁇ '- Tetramethyl - m - or p - xylylene diisocyanate
  • 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 that are reactive toward isocyanate groups in particular a total of two amino groups, thiol groups, carboxyl groups and / or hydroxyl-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 branching is possible, as is the possible use of tri- or higher-functional polyisocyanates already mentioned for the same purpose.
  • 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.
  • the condensation products of thiodiglycol with itself 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, for example, 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, for example diphenyl carbonate, or phosgene, can be prepared.
  • diols such as propanediol - (1,3), butanediol - (1,4) and / or Hexanediol - (1,6)
  • diethylene glycol triethylene glycol
  • tetraethylene glycol for example diphenyl carbonate, or phosgene
  • polyester amides and polyamides include e.g. the predominantly linear condensates obtained from polyvalent saturated and unsaturated carboxylic acids or their anhydrides and polyvalent saturated and unsaturated amino alcohols, diamines, polyamines 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.
  • hydrophilically modified prepolymers are to be used, they are produced by known processes of the prior art, for example in accordance with DT-OSs 1 495 745, 1 495 847, 2 446 440, 2 340 ⁇ 512, US Pat 310, GB-PS'en 1 158 088 or 1 076 688 described methods.
  • references related to the preparation of aqueous polyurethane dispersions or solutions i.e. for example, diisocyanates, diamines or dihydroxy compounds or diisocyanates or glycols containing ionic or potential ionic groups or polyethylene oxide units can also be used.
  • the preferred hydrophilically modified structural components include in particular the sulfonate group-containing aliphatic diols according to DE-A 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 reactants are generally used in such proportions that a ratio of isocyanate groups to hydrogen atoms reactive towards NCO, preferably from hydroxyl groups, from 1.05 to 10, preferably from 1.1 to 3 correspond.
  • 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 of course also be produced in the presence of organic solvents.
  • Suitable solvents e.g. in an amount up to 25% by weight, based on the solid, could be used e.g. Acetone, methyl ethyl ketone, ethyl acetate, dimethylformamide or cyclohexanone.
  • NCO prepolymers in the process according to the invention, in the production of which none of the hydrophilic structural components mentioned have been used, in which the content of the groups mentioned above under b) or c) is therefore 0.
  • 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 alkylbenzenes with an average molecular weight of 500 to 10,000.
  • These external emulsifiers are thoroughly mixed with the NCO prepolymers before the process according to the invention is carried out. They are generally used in amounts of 1 to 30, preferably 5 to 20,% by weight, based on the weight of the NCO prepolymer. It is also possible to increase the hydrophilicity of the hydrophilic modified NCO prepolymers by using such external emulsifiers, although this is generally not necessary.
  • the reactants are preferably used in proportions such that 0.37-0.53, preferably 0.4-0.51 mol, hydroxyl groups of the hydroxyoxyzolidine are present in each mole of isocyanate groups in the NCO prepolymer.
  • Reaction mixtures are obtained on these which have about 0.6-1.1, preferably about 0.65-1.05, oxazoline groups per remaining isocyanate group. Since the monohydroxyoxazolidines are monofunctional compounds, there is no appreciable increase in molecular size in this reaction.
  • the reaction products like the NCO prepolymers used as starting materials, are therefore essentially linear compounds.
  • hydroxyoxazolidines and the bisoxazolidines mentioned are compounds known from the literature (see, for example, the references mentioned at the beginning with regard to the moisture-curing oxazolidine compositions of the prior art).
  • Bisoxazolidines or hydroxyoxazolidines to be used with particular preference are the corresponding compounds mentioned in US Pat. No. 4,002,601 and DE-A 2,446,438.
  • Bis- (2-hydroxyethyl) amine and bis- (2-hydroxypropyl) amine are particularly suitable. In principle, however, bis- (2-hydroxybutyt) amine, bis- (2-hydroxyhexyl) amine, bis- (3-hydroxyhexyl) amine, or N- (2-hydroxypropyl) -N- ( 6-hydroxyhexyl) amine.
  • the bisoxazolidines to be used according to the invention can be reacted with diisocyanates of the formula (in which Z has the meaning given above), for example hexamethylene diisocyanate.
  • diisocyanates of the formula (in which Z has the meaning given above)
  • Z has the meaning given above
  • diisocyanates of the formula (in which Z has the meaning given above) for example hexamethylene diisocyanate.
  • IPDI 3,3,5-trimethyl-5-isocyanatomethyl-cyclohexyl isocyanate
  • 4'-diisocyanatodicyclohexyl methane 2,4- and 2,6-diisocyanatotoluene or 4,4'-diisocyanatodiphenytmethane.
  • dicarboxylic acids, aliphatic, cycloaliphatic or aromatic in nature of the formula leads to bisoxazolidines containing ester groups which can be used according to the invention.
  • a decisive advantage over the previously known methods of the prior art for the solvent-free or low-solvent production of aqueous polyurethane dispersions is that an intimate mixing with the chain extender takes place even before being brought together with water, or chemical fixation even before being brought together with water the chain-extending group (oxazolidine group) takes place, so that the chain extension leads to particularly homogeneous products.
  • the process according to the invention is particularly suitable for the production of aqueous dispersions or solutions, which have a solids content of 10 to 70, preferably 30 to 65 wt .-%.
  • the particles of the discontinuous phase in the dispersions generally have a diameter of 50 to 1000 nm.
  • the preparation of sols with an average particle diameter of the discontinuous phase of about 1-50 nm or clear, aqueous solutions in which the solid is present in molecularly disperse form or at most in the form of associates is also possible according to the invention.
  • solutions or dispersions of the polyurethanes in water are obtained in the process according to the invention depends above all on the molecular weight and the hydrophilicity of the dissolved or dispersed particles, which in turn depends on the suitable choice of type and quantitative ratio of the starting materials, in particular in the preparation of the NCO prepolymers , can be adjusted according to the known principles of polyurethane chemistry.
  • the use of an NCO prepolymer with a mean NCO functionality slightly below 2 leads to the polyaddition reaction being terminated before excessively high molecular weights are reached.
  • the polyurethanes produced by the process according to the invention and present in aqueous dispersion or solution are on a par with the known polyurethanes produced in organic solvents. Films made from them have excellent mechanical strength and hydrolysis resistance and can be used for a wide variety of applications.
  • pendant hydroxyl groups incorporated in the process products according to the invention can be crosslinked after shaping, for example by evaporation of the solvent or water after a chemically or thermally activatable crosslinking agent has been added to the solution or the dispersion.
  • Suitable crosslinking agents are e.g. Polyisocyanates with blocked isocyanate groups or melamine resins which are reactive towards hydroxyl groups. Even if the process products according to the invention are not chemically crosslinked via the pendant hydroxyl groups, these can be advantageous since they often increase the physical affinity of the process products according to the invention for substrates which are coated with the compounds according to the invention.
  • the film was not sticky after moistening with toluene and acetone and did not dissolve in hot DMF.
  • the NCO prepolymer from Example 1 was at 60 ° C with 361.8 parts of a bisoxazolidine of the formula transferred. 5100 parts of deionized water were added with vigorous stirring. The resulting one Dispersion had a solids content of 30% and a viscosity of 18 seconds (Ford cup, 4 mm). It showed a Tyndall effect in the translucent light.
  • the dispersion dries to a clear, colorless and tack-free film which, after the water has been completely removed, has a Shore A hardness of 78. After heating to 130 ° C. for 20 minutes, the hardness had risen to 85 (Shore-A) and the film was only swellable in hot DMF, but no longer soluble.
  • the resulting aqueous dispersion had a solids content of 30% and a viscosity of 15 seconds (Ford cup, 4 mm).
  • the dispersion showed a Tyndall effect in the translucent light.
  • the dispersion After pouring, the dispersion dried into a clear, hard film, which was easy to scratch with a fingernail.
  • the pencil hardness was HB-H. After heating at 130 ° C. for 20 minutes, the temperature had risen to 3 hours.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Health & Medical Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Organic Chemistry (AREA)
  • Polyurethanes Or Polyureas (AREA)

Claims (2)

1. Procédé de production de polymères essentiellement linéaires d'addition d'isocyanates porteurs de groupes hydroxyl latéraux par réaction avec l'eau de systèmes réactionnels porteurs de groupes isocyanato et oxazolidino libres, caractérisé en ce qu'il consiste à allonger la chaîne, par mélange avec l'eau:
a) de prépolymères essentiellement linéaires, qui portent en position terminale tant des groupes isocyanato que des groupes oxazolidino, ou
b) d'un mélange formé de prépolymères d'isocyanates essentiellement linéaires et de bis-oxazolidines, la quantité d'eau étant calculée de manière qu'il y ait au moins une mole d'eau par mole de groupes oxazolidino présents dans le mélange réactionnel.
2. Procédé suivant la revendication 1, caractérisé en ce qu'on utilise comme prépolymères des prépolymères à modification hydrophile et/ou comportant un émulsionnant externe et un grand excès d'eau par rapport à la réaction d'allongement de chaîne, de manière à obtenir directement une dispersion ou solution aqueuse des polymères d'addition.
EP78100323A 1977-07-15 1978-07-07 Procédé de préparation de produits de polyaddition d'isocyanate contenant des groupes hydroxyles latéraux et produits obtenus par ce procédé Expired EP0000381B1 (fr)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
DE19772732131 DE2732131A1 (de) 1977-07-15 1977-07-15 Verfahren zur herstellung von seitenstaendige hydroxylgruppen aufweisenden isocyanat-polyadditionsprodukten
DE2732131 1977-07-15

Publications (2)

Publication Number Publication Date
EP0000381A1 EP0000381A1 (fr) 1979-01-24
EP0000381B1 true EP0000381B1 (fr) 1980-08-06

Family

ID=6014055

Family Applications (1)

Application Number Title Priority Date Filing Date
EP78100323A Expired EP0000381B1 (fr) 1977-07-15 1978-07-07 Procédé de préparation de produits de polyaddition d'isocyanate contenant des groupes hydroxyles latéraux et produits obtenus par ce procédé

Country Status (6)

Country Link
US (1) US4192937A (fr)
EP (1) EP0000381B1 (fr)
JP (1) JPS5420098A (fr)
DE (2) DE2732131A1 (fr)
ES (1) ES471750A1 (fr)
IT (1) IT1105095B (fr)

Families Citing this family (78)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE3048085A1 (de) * 1980-12-19 1982-07-22 Bayer Ag, 5090 Leverkusen Dispersionen von sulfonatgruppen aufweisenden polymeren, ein verfahren zu ihrer herstellung, sowie ihre verwendung als beschichtungsmittel
DE3137748A1 (de) * 1981-09-23 1983-03-31 Bayer Ag, 5090 Leverkusen Verfahren zur herstellung von hitzeaktivierbare vernetzer enthaltenden waessrigen dispersionen oder loesungen von polyurethan-polyharnstoffen, die nach dem verfahren erhaeltlichen dispersionen oder loesungen, sowie ihre verwendung zur herstellung von ueberzuegen
JPS58144961A (ja) * 1982-02-24 1983-08-29 Fujitsu Ltd 記憶領域管理方式
DE3313237A1 (de) * 1983-04-13 1984-10-18 Bayer Ag, 5090 Leverkusen Waessrige, vernetzerhaltige polyurethanzubereitungen und ihre verwendung zur thermoaktiv-einstrich-umkehrbeschichtung
DE3521618A1 (de) 1985-06-15 1986-12-18 Bayer Ag, 5090 Leverkusen In wasser dispergierbare polyisocyanat-zubereitung und ihre verwendung als zusatzmittel fuer waessrige klebstoffe
DE3630045A1 (de) * 1986-09-04 1988-03-17 Bayer Ag Klebstoff und die verwendung des klebstoffs zur herstellung von verklebungen
US4879365A (en) * 1988-11-14 1989-11-07 Nl Chemicals, Inc. High preformance one-component urethane compositions with excellent weathering properties and method for making and using same
DE4028704A1 (de) * 1990-09-10 1992-03-12 Bostik Gmbh 2-komponenten-polyurethan-dichtungsmassen
DE4418157A1 (de) 1994-05-25 1995-11-30 Basf Ag Thermokoagulierbare wässerige Polyurethan-Dispersionen
BR9607155A (pt) * 1995-01-13 1997-11-11 Essex Specialty Prod Composição adesiva bicomponente processo para ligar dois substratos entre si
EP0774475A3 (fr) 1995-11-17 1997-10-01 Basf Ag Dispersions aqueuses contenant un polyuréthane ayant des groupes isocyanates bloqués par de l'oxime et/ou des groupes carbonyles dans une fonction céto ou aldéhyde
US5922809A (en) * 1996-01-11 1999-07-13 The Dow Chemical Company One-part moisture curable polyurethane adhesive
AR005429A1 (es) * 1996-01-11 1999-06-23 Essex Specialty Prod Prepolimeros de poliuretano, composiciones adhesivas en un solo envase que incluyen dichos prepolimeros y procedimiento para adherir substratos con dichascomposiciones
US5852103A (en) * 1996-05-08 1998-12-22 Essex Specialty Products, Inc. Two-part moisture curable polyurethane adhesive
US7459167B1 (en) 2000-07-27 2008-12-02 3M Innovative Properties Company Biocidal polyurethane compositions and methods of use
AU2001283149A1 (en) 2000-08-07 2002-02-18 Dow Global Technologies Inc. One-part moisture curable polyurethane adhesive
US6573375B2 (en) 2000-12-20 2003-06-03 Union Carbide Chemicals & Plastics Technology Corporation Liquid thickener for surfactant systems
DE10133789A1 (de) * 2001-07-16 2003-02-06 Basf Ag Wässrige Dispersionen für hydrolysefeste Beschichtungen
DE10238146A1 (de) 2002-08-15 2004-02-26 Basf Ag Wasseremulgierbare Isocyanate mit verbesserten Eigenschaften
DE10306243A1 (de) * 2003-02-14 2004-08-26 Bayer Ag Einkomponenten-Beschichtungssysteme
DE102004026118A1 (de) 2004-05-28 2005-12-15 Bayer Materialscience Ag Klebstoffe
EP2965751A1 (fr) 2004-10-08 2016-01-13 Forward Pharma A/S Compositions pharmaceutiques à libération contrôlée comportant un ester d´acide fumarique
WO2006089935A1 (fr) 2005-02-24 2006-08-31 Basf Aktiengesellschaft Dispersions de poluyrethanne aqueuses durcissables par rayonnement
DE102006036220A1 (de) * 2006-08-03 2008-02-07 Clariant International Limited Polyetheramin-Makromonomere mit zwei benachbarten Hydroxylgruppen und ihre Verwendung zur Herstellung von Polyurethanen
EP1918314A1 (fr) 2006-10-31 2008-05-07 Sika Technology AG Composition de polyuréthane ayant une résistance initiale élevée
KR101463277B1 (ko) * 2006-12-22 2014-11-26 바스프 에스이 카르보디이미드 기를 가지는 화합물을 포함하는 미세캡슐
DE102008000270A1 (de) 2007-02-14 2008-08-28 Basf Se Verfahren zur Herstellung von Polyurethandispersionen mit geringem Gehalt an hochsiedenden Lösungsmitteln
DE102008000478A1 (de) 2007-03-05 2008-09-11 Basf Se Polyurethan-Dispersionen mit Polyethercarbonatpolyolen als Aufbaukomponente
EP1975187A1 (fr) * 2007-03-28 2008-10-01 Sika Technology AG Procédé de fabrication de composition de polyuréthane ayant une teneur en isocyanat monomère moindre
DE102007020523A1 (de) 2007-05-02 2008-11-06 Helling, Günter, Dr. Metallsalz-Nanogel enthaltende Polymere
DE102007026196A1 (de) 2007-06-04 2008-12-11 Basf Se Verfahren zur Herstellung wasseremulgierbarer Polyurethanacrylate
DE102008004178A1 (de) 2008-01-11 2009-07-16 Basf Se Textile Flächengebilde, Verfahren zu ihrer Herstellung und ihre Verwendung
DE102008014211A1 (de) 2008-03-14 2009-09-17 Bayer Materialscience Ag Wässrige Dispersion aus anionisch modifizierten Polyurethanharnstoffen zur Beschichtung eines textilen Flächengebildes
DE102008038944A1 (de) * 2008-08-11 2010-02-18 Borealis Agrolinz Melamine Gmbh Thermoplastische Polymere auf Basis von N-haltigen Verbindungen
ATE539131T1 (de) * 2008-08-26 2012-01-15 Basf Se Klebstoffzusammensetzung für selbstklebende, wiederablösbare artikel auf basis von adhäsiven polymeren und organischen nanopartikeln
ES2651930T3 (es) 2009-04-14 2018-01-30 Basf Se Adhesivo de polímeros con dominios cristalinos, poliuretano amorfo y compuestos de silano
US9051409B2 (en) 2009-04-14 2015-06-09 Basf Se Use of polyurethane adhesive formed from polyester diols, polyether diols and silane compounds in the manufacture of film/foil-coated furniture
DE102010043486A1 (de) 2009-11-16 2011-05-19 Basf Se Kaschierverfahren unter Verwendung von Carbodiimid- und Harnstoffgruppen enthaltenden Klebstoffen
EP2368928B1 (fr) 2010-03-24 2013-10-30 Basf Se Isocyanates hydroémulsifiants ayant des caractéristiques améliorées
EP2368926B1 (fr) 2010-03-25 2013-05-22 Basf Se Isocyanates hydroémulsifiants ayant des caractéristiques améliorées
EP2388283A1 (fr) 2010-05-18 2011-11-23 Bayer MaterialScience AG Procédé de réglage de la viscosité de dispersions de polyuréthane anioniques
BR112013001530A2 (pt) 2010-07-29 2016-05-24 Basf Se uso de um adesivo de dispersão de poliuretano aquoso, processo para produzir películas compostas, e, película composta
US8956497B2 (en) 2010-07-29 2015-02-17 Basf Se Biodisintegratable composite foils
US9089624B2 (en) 2010-08-23 2015-07-28 Basf Se Ultrathin fluid-absorbent cores comprising adhesive and having very low dry SAP loss
DK2655458T3 (en) 2010-12-20 2017-06-06 Basf Se PROCEDURE FOR PREPARING POLYURETHAN-POLYACRYLATE HYBRID DISPERSIONS
DE102011015459A1 (de) 2011-03-29 2012-10-04 Basf Se Polyurethane, ihre Herstellung und Verwendung
US8841369B2 (en) 2011-03-30 2014-09-23 Basf Se Latently reactive polyurethane dispersion with activatable crosslinking
WO2012130711A2 (fr) 2011-03-30 2012-10-04 Basf Se Dispersion de polyuréthane réactif latent à réticulation activable
CN103608375B (zh) 2011-06-14 2015-09-09 巴斯夫欧洲公司 可辐射固化聚氨酯水分散体
EP2788447B1 (fr) 2011-12-09 2015-09-16 Basf Se Utilisation de dispersions aqueuses de polyuréthane pour le contrecollage de films composites
US9005762B2 (en) 2011-12-09 2015-04-14 Basf Se Use of aqueous polyurethane dispersions for composite foil lamination
WO2014005879A1 (fr) 2012-07-04 2014-01-09 Basf Se Système d'emballage collé pour produits alimentaires
US20150247076A1 (en) 2012-09-18 2015-09-03 Basf Se Polymers comprising a polyurethane backbone endcapped with reactive (meth)acrylic terminating groups and their use as adhesives
EP2900735B1 (fr) 2012-09-28 2016-09-14 Basf Se Isocyanates émulsionnables dans l'eau à brillance améliorée
US9669610B2 (en) 2012-11-02 2017-06-06 Basf Se Use of aqueous polyurethane dispersions for laminating molded articles
CN105074013B (zh) 2013-02-22 2018-10-02 巴斯夫欧洲公司 制备含水聚氨酯配制剂的方法
KR20160003851A (ko) 2013-05-02 2016-01-11 바스프 에스이 개선된 광택을 가지는 코팅을 위한 수-유화성 이소시아네이트
RU2656392C2 (ru) 2013-10-16 2018-06-06 Басф Се Способ получения водоэмульгируемых полиуретанакрилатов
WO2015107078A1 (fr) 2014-01-17 2015-07-23 Basf Se Encre d'impression complexage comportant une dispersion aqueuse comprenant du polyurethanne
DE102014204582A1 (de) 2014-03-12 2015-09-17 Basf Se Neue Polymerdispersionen
KR20170018892A (ko) 2014-06-10 2017-02-20 바스프 에스이 아실모르폴린을 함유하는 중합체 분산액
BR112017001895A2 (pt) 2014-08-01 2017-11-28 Basf Se dispersão híbrida aquosa de poliuretano-poliacrilato, processos para preparação de uma dispersão híbrida aquosa de poliuretano-poliacrilato e para dispersão híbrida de poliuretano-poliacrilato aquosa, uso de uma dispersão híbrida aquosa de poliuretano-poliacrilato, composição de revestimento, e, superfície revestida
MX2017007329A (es) 2014-12-05 2017-10-20 Basf Se Dispersion adhesiva acuosa que contiene poliuretanos y alcoholes grasos etoxilados.
WO2016162215A1 (fr) 2015-04-07 2016-10-13 Basf Se Dispersions polymères contenant de la n-acylpyrrolidine
CN109963909A (zh) 2016-08-01 2019-07-02 斯塔尔国际有限公司 乙醛释放量降低的聚合物分散体
WO2018108631A1 (fr) 2016-12-14 2018-06-21 Basf Se Isocyanates émulsifiables dans l'eau qui présentent des propriétés améliorées
US10385261B2 (en) 2017-08-22 2019-08-20 Covestro Llc Coated particles, methods for their manufacture and for their use as proppants
WO2019072590A1 (fr) 2017-10-11 2019-04-18 Basf Se Films protecteurs produits à partir d'un matériau support polyoléfinique, d'une couche de fond et d'un adhésif thermofusible réticulable sous l'effet d'un rayonnement
US11814558B2 (en) 2018-02-21 2023-11-14 Basf Se Method for producing articles coated with adhesive
EP3775084A1 (fr) 2018-04-13 2021-02-17 Basf Se Composition adhésive de stratification aqueuse piégeant l'oxygène
WO2020144052A2 (fr) 2019-01-11 2020-07-16 Basf Se Procédé de revêtement par une feuille au moyen d'un système de cylindre de gravure
WO2020260133A1 (fr) 2019-06-24 2020-12-30 Basf Se Isocyanates émulsifiables dans l'eau qui présentent des propriétés améliorées
EP4114875A1 (fr) 2020-03-02 2023-01-11 Basf Se Feuilles composites biodésintégrables dans des conditions de compost domestique
WO2021249749A1 (fr) 2020-06-09 2021-12-16 Basf Se Procédé de recyclage d'articles collés
WO2022179912A1 (fr) 2021-02-24 2022-09-01 Basf Se Étiquettes adhésives comprenant un adhésif sensible à la pression à base de polyuréthane aqueux biodégradable
EP4326804A1 (fr) 2021-04-22 2024-02-28 Basf Se Procédé pour la préparation de corps façonnés enrobés et leur utilisation
WO2023117877A1 (fr) 2021-12-21 2023-06-29 Basf Se Attributs environnementaux pour compositions d'isocyanate
WO2024083787A1 (fr) 2022-10-18 2024-04-25 Basf Se Particules enrobées stables au stockage et leur préparation

Family Cites Families (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3533983A (en) * 1966-06-01 1970-10-13 Furane Plastics Thermosetting phenyl glycidyl ether derivatives of isocyanate-terminated organic compounds
US3743626A (en) * 1968-10-18 1973-07-03 Rohm & Haas Hydrocurable oxazolidine-isocyanate compositions
US3702839A (en) * 1969-07-25 1972-11-14 Monsanto Res Corp Process for preparing 2-oxazolidone polymers
BE757998A (fr) * 1969-10-28 1971-04-26 Henkel & Cie Gmbh Procede de fabrication de matieres synthetiques contenant des groupes urethane
US3763070A (en) * 1970-06-03 1973-10-02 Ici Ltd Hydraulic cement with polyisocyanate and aliphatic polyepoxide
US3817938A (en) * 1971-02-12 1974-06-18 K Ashida Polyoxazolidone catalyst
DE2632513C3 (de) * 1976-07-20 1979-09-06 Bayer Ag, 5090 Leverkusen Mit Wasser härtbare in Abwesenheit von Wasser lagerfähige Gemische auf Polyurethanbasis
US4118373A (en) * 1977-05-04 1978-10-03 The Dow Chemical Company Preparation of urethane elastomers from epoxy resin, polyols and polyisocyanates using a catalyst composition of an organometal salt with either nitrogen or phosphorus compounds

Also Published As

Publication number Publication date
DE2732131A1 (de) 1979-01-25
JPS6131728B2 (fr) 1986-07-22
JPS5420098A (en) 1979-02-15
DE2860113D1 (en) 1980-11-27
IT7850255A0 (it) 1978-07-12
IT1105095B (it) 1985-10-28
US4192937A (en) 1980-03-11
ES471750A1 (es) 1979-02-01
EP0000381A1 (fr) 1979-01-24

Similar Documents

Publication Publication Date Title
EP0000381B1 (fr) Procédé de préparation de produits de polyaddition d'isocyanate contenant des groupes hydroxyles latéraux et produits obtenus par ce procédé
EP0004069B1 (fr) Procédé de préparation de solutions ou de dispersions aqueuses de polyuréthanes et leur application pour la préparation de revêtements ou de vernis
EP0000029B1 (fr) Procédé de préparation de dispersions ou de solutions aqueuses de polyuréthanes, leur application pour le revêtement de substrats flexibles
EP0009760B1 (fr) Procédé de préparation de dispersions ou de solutions aqueuses de polyuréthane-polyurées et leur utilisation
EP0269972B1 (fr) Procédé de préparation des polyuréthanessolubles ou dispersables dans l'eau et leur utilisation pour le revêtement de substrats divers
DE2446440C3 (de) Verfahren zur Herstellung von wäßrigen Dispersionen von Sulfonatgruppen aufweisenden Polyurethanen
EP0392352B1 (fr) Dispersions aqueuses de polyuréthanes réticulables par radiation à haute énergie
EP0000568B1 (fr) Procédé de préparation de dispersions ou solutions aqueuses de produits de polyaddition d'isocyanate; application de ces dispersions ou solutions pour la préparation de revêtements et de films
EP0792900B1 (fr) Utilisation de dispersions aqueuses de polyuréthane ioniques ou non-ioniques pour l'encollage de fibres de verre et ces dispersions-mêmes
DE3630045A1 (de) Klebstoff und die verwendung des klebstoffs zur herstellung von verklebungen
EP0044460A1 (fr) Prépolymères solides, dispersables dans l'eau, contenant des groupes isocyanate et procédé de préparation de dispersions aqueuses de polymères par utilisation de ces prépolymères
EP0242731A2 (fr) Procédé pour la préparation de dispersions aqueuses de polyuréthane-polyurées et leur utilisation comme ou pour la préparation de masses de revêtement
EP0154768B1 (fr) Procédé de préparation de polyuréthanes, polyuréthanes ayant des groupes amino terminaux aromatiques et leur utilisation
DE3140873A1 (de) Stabile waessrige polyutheran-dispersion
EP1845120B2 (fr) Dispersions de polyuréthane liquide à stabilité de stockage améliorée
DE2744544A1 (de) Waessrige harnstoff-urethan-dispersionen
EP0000171A1 (fr) Produits d'addition de polyisocyanates contenant des groupes carboxylates et leur procédé de préparation
EP0003521A1 (fr) Solutions ou dispersions aqueuses de produits de polyaddition de polyisocyanates, leur procédé de préparation et leur utilisation comme adhésifs
DE2721985A1 (de) Verfahren zur herstellung von urethan- und/oder harnstoffgruppen aufweisenden polyisocyanat polyadditionsprodukten
EP0006204B1 (fr) Dispersions aqueuses de matières plastiques oligomères ou polymères, procédé pour leur fabrication et leur utilisation
EP0538649B1 (fr) Polyurées modifiées
EP0097869B1 (fr) Composés contenant des groupes amines primaires aromatiques, des groupes uréthanes et des groupes polyesters, procédé pour leur fabrication et leur application comme matières premières de polyuréthanes
EP1306398A1 (fr) Dispersions de polyuréthane ayant un poids moléculaire élevé
EP0013923A1 (fr) Suspensions d'isocyanates à groupes urée dans des prépolymères d'isocyanates, procédé pour leur préparation et leur utilisation dans la préparation de matières plastiques de polyuréthane à haut poids moléculaire
EP0581159A1 (fr) Polyurées modifiés par des groupes anioniques à adhésivité réduite pour le revêtement du cuir

Legal Events

Date Code Title Description
PUAI Public reference made under article 153(3) epc to a published international application that has entered the european phase

Free format text: ORIGINAL CODE: 0009012

AK Designated contracting states

Designated state(s): BE DE FR GB NL

17P Request for examination filed
GRAA (expected) grant

Free format text: ORIGINAL CODE: 0009210

AK Designated contracting states

Designated state(s): BE DE FR GB NL

REF Corresponds to:

Ref document number: 2860113

Country of ref document: DE

Date of ref document: 19801127

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: FR

Payment date: 19900628

Year of fee payment: 13

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: BE

Payment date: 19900718

Year of fee payment: 13

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: BE

Effective date: 19910731

BERE Be: lapsed

Owner name: BAYER A.G.

Effective date: 19910731

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: FR

Effective date: 19920331

REG Reference to a national code

Ref country code: FR

Ref legal event code: ST

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: DE

Payment date: 19940615

Year of fee payment: 17

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: GB

Payment date: 19940628

Year of fee payment: 17

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: NL

Payment date: 19940731

Year of fee payment: 17

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: GB

Effective date: 19950707

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: NL

Effective date: 19960201

GBPC Gb: european patent ceased through non-payment of renewal fee

Effective date: 19950707

NLV4 Nl: lapsed or anulled due to non-payment of the annual fee

Effective date: 19960201

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: DE

Effective date: 19960402

PLBE No opposition filed within time limit

Free format text: ORIGINAL CODE: 0009261

STAA Information on the status of an ep patent application or granted ep patent

Free format text: STATUS: NO OPPOSITION FILED WITHIN TIME LIMIT