AU720369B2 - Composition, for use in coatings, based on a mixture of emulsion(s) and of dispersion(s) of polyol polymer and coating(s) produced therefrom - Google Patents

Composition, for use in coatings, based on a mixture of emulsion(s) and of dispersion(s) of polyol polymer and coating(s) produced therefrom Download PDF

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AU720369B2
AU720369B2 AU44414/96A AU4441496A AU720369B2 AU 720369 B2 AU720369 B2 AU 720369B2 AU 44414/96 A AU44414/96 A AU 44414/96A AU 4441496 A AU4441496 A AU 4441496A AU 720369 B2 AU720369 B2 AU 720369B2
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composition according
equal
emulsion
masked
composition
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AU4441496A (en
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Gilles Guerin
Bruno Langlois
Roland Reeb
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Rhodia Chimie SAS
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Rhone Poulenc Chimie SA
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    • 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
    • C08G18/70Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the isocyanates or isothiocyanates used
    • C08G18/72Polyisocyanates or polyisothiocyanates
    • C08G18/80Masked polyisocyanates
    • C08G18/8061Masked polyisocyanates masked with compounds having only one group containing active hydrogen
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L75/00Compositions of polyureas or polyurethanes; Compositions of derivatives of such polymers
    • 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
    • C08G18/0838Manufacture of polymers in the presence of non-reactive compounds
    • C08G18/0842Manufacture of polymers in the presence of non-reactive compounds in the presence of liquid diluents
    • C08G18/0861Manufacture of polymers in the presence of non-reactive compounds in the presence of liquid diluents in the presence of a dispersing phase for the polymers or a phase dispersed in the polymers
    • C08G18/0866Manufacture of polymers in the presence of non-reactive compounds in the presence of liquid diluents in the presence of a dispersing phase for the polymers or a phase dispersed in the polymers the dispersing or dispersed phase being an aqueous medium
    • 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
    • C08G18/70Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the isocyanates or isothiocyanates used
    • C08G18/703Isocyanates or isothiocyanates transformed in a latent form by physical means
    • C08G18/705Dispersions of isocyanates or isothiocyanates in a liquid medium
    • C08G18/706Dispersions of isocyanates or isothiocyanates in a liquid medium the liquid medium being water
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B82NANOTECHNOLOGY
    • B82YSPECIFIC USES OR APPLICATIONS OF NANOSTRUCTURES; MEASUREMENT OR ANALYSIS OF NANOSTRUCTURES; MANUFACTURE OR TREATMENT OF NANOSTRUCTURES
    • B82Y30/00Nanotechnology for materials or surface science, e.g. nanocomposites

Abstract

A compsn. comprising (i) at least one opt. masked polyisocyanate (I) in the form of an aq. emulsion with an average particle size d50 of 0.1-10 mm., pref. less than 2 and greater than 0.2 mm. and (ii) at least one polyhydroxylated polymer (II), esp. a polyol, in the form of an aq. dispersion with an average particle size d50 of 10-200 nm., whereby the (I) is present in an amt. of at least 5/6R-20 pref. at least 5/6R-18 and esp.5/6R-16 wt.% where R = d50(I)/d50(II). Coating obtained from above composition is also claimed.

Description

i n -1-
AUSTRALIA
PATENTS ACT 1990 COMPLETE SPECIFICATION FOR A STANDARD PATENT
ORIGINAL
0 *o *4 Name of Applicant: Actual Inventors: Address of Service: RHONE-POULENC CHIMIE Gilles GUERIN, Bruno LANGLOIS and Roland REEB SHELSTON WATERS 60 MARGARET STREET SYDNEY NSW 2000 Invention Title: "COMPOSITION, FOR USE IN COATINGS, BASED ON A MIXTURE OF EMULSION(S) AND OF DISPERSION(S) OF POLYOL POLYMER AND COATING(S) PRODUCED
THEREFROM"
The following statement is a full description of this invention, including the best method of performing it known to us:la COMPOSITION, FOR USE IN COATINGS, BASED ON A MIXTURE OF EMULSION(S) AND OF DISPERSION(S) OF POLYOL POLYMER AND COATING(S) PRODUCED THEREFROM The present invention relates to mixtures of emulsions with dispersions of polymer. It relates more particularly to the stability of a particularly fine polyol dispersion, advantageously a (nano)latex, conjointly with an emulsion of isocyanate which is in most cases masked.
Such compositions are especially useful for varnishes and paint, but they can be useful for any application employing the condensation properties of isocyanates. They can also be useful in any field in which emulsions of isocyanates, in most cases blocked ones, need to coexist with dispersions of insoluble alcohols of different particle size and especially in formulations for agriculture.
In the remainder of the present description *the term dispersion will be employed for polymers 20 containing hydroxyl functional groups and especially polyols, while the expression emulsions will be employed for isocyanates, whether blocked or not.
The use of organic solvents is increasingly frequently criticized by the authorities responsible for safety at work because these solvents, or at least some of them, are reputed to be toxic or chronically toxic. This is why attempts are being made to develop more and more techniques which replace techniques in a 2 solvent medium in order to overcome the disadvantages associated with the solvents.
One of the most frequently employed solutions lies in the use of emulsions or dispersions in water.
To produce paint or varnish films, two dispersions are mixed, an emulsion containing the isocyanate, which may be blocked, and a dispersion of polyol.
The mixture of the dispersions, which may also contain pigments and fillers, is then deposited on a substrate in the form of a film with the aid of conventional techniques for applying industrial paints.
When the preparation contains blocked isocyanates the "combination of film plus substrate is cured at a sufficient temperature to ensure the deblocking of the isocyanate functional groups and the condensation of "the latter with the hydroxyl groups of the polyol particles.
In the present description the particle size characteristics frequently refer to notations of the d.
type, where n is a number from 1 to 99; this notation is well known in many technical fields but is a little S*rarer in chemistry, and therefore it may be useful to give a reminder of its meaning. This notation represents the particle size such that n (by weight, or more precisely on a mass basis, since weight is not a quantity of matter but a force) of the particles are smaller than or equal to the said size.
3 In the remainder of the description the polydispersity index will be employed, which is defined as follows I (d 9 o-do,)/d 50 Typically the ratios of the mean sizes (dso) between the isocyanate emulsion and the polyol dispersion are between 2 and 200. Thus, the mean sizes of the isocyanate emulsions manufactured according to the technique described in the French Patent Application filed on 31.3.1993 under No. 93 03795 and published under No. 2703358 on 7.10.94 have mean sizes of between 0.1 and 10 micrometres and more generally between 0.3 and 2 micrometres. The polyol dispersions employed in combination with these emulsions have mean sizes measured by quasielastic scattering of light which are between 20 and 200 nanometres and more generally between 50 and 150 nanometres.
When dispersions of different sizes are mixed, which is generally the case, so as to obtain 20 molar ratios between the NCO and OH groups of between 0.3 to 10 and more preferably between 0.8 and 1.5, an instability is observed in the mixtures of the two dispersions.
To give an example, this instability is reflected in a fast macroscopic separation, generally over a few minutes, to give, on the one hand, a fluid phase and, on the other hand, a very viscous phase.
This results not only in it being impossible [A918 ON XY/XLJ SO:/T n1H1 00, 0O/90 -4to preserve (store) these mixtures, but also in extreme difficulty in applying this mixture to the surface which it is desired to cover according to the usual techniques for the application of paints and varnishes. If these unstable mixtures are applied onto a substrate, such as onto a sheet of glass or metal, the resulting film is not transparent but looks opaque and heterogeneous and is therefore not suitable.
These problems are particularly acute in the case of isocyanates, whether masked or not, when the latter are mixed with insoluble polyols dispersed in water and when the dispersion is very fine, that is to say when the ratio R is higher than or equal to 30 (one significant digit).
10 It is an object of the present invention to overcome or ameliorate at least one of the disadvantages of the prior art, or to provide a useful alternative.
S. In one or more embodiments, the present invention may provide a technique which makes it possible to provide fluid and stable mixtures of an isocyanate emulsion with 4.o. very fine dispersions of polyols which are stable per se, especially without there being 15 any need to add any additional or neutralising additive, for example to adjust a pH.
In one or more embodiments, the present invention may provide compositions comprising an emulsion of masked isocyanates and a dispersion of polyols which are physically stable for at least a month.
In one or more embodiments, the present invention provides films exhibiting good gloss, transparency and solvent resistance properties obtainable from these stable and fluid mixtures of the emulsion with a polyol dispersion.
One or more advantages of the present invention may be attained by means of a l\ composition comprising: 871D-oO" lss7l--O.DOC S00d 9TW'ON 2692SK~9 F-0 T9 A3NGAS MS9 80:9T 00/V/90 [SSZR ON XHl/XIL 90:LT 11H1 00, 170/90 at least one masked or unmasked polyisocYanate in the form Of anl aqueous emulsion whose mean size is between 0.1 and 10 mirromnetres and preferably smaller than 2 and larger than 0.2 micrometres, at least one polyhydroxylated polymer, advantageously a polyol, in the form of an aqueous dispersion whose mean size is between 10 and 200 nanometreS- According to the first aspect, the present invention provides a composition comprising: -at least one masked or unmasked polyisocyanate in the form of an aqueous emulsion whose mean size is between 0. 1 and 10 micronietres; *O9 10 at least one polyhydroxylated polymer, in the form of an aqueous dispersion whose mean size is between 10 and 200 nanometres; wherein the quantity of polyhydroxylated polymer in the mixture is chosen so as to meet the following constraint; -the content of polyhydroxylated, polymer, excpressed in mass per cent, is at least equal to (5/6R)-20, with R equal to the ratio of the mean size of the emulsion to that of the dispersion of polyhydroxylated polymer, The ratio between the mean sizes of the elementary particles (d 5 0 of thc emulsion and that of the polyol dispersion is at least equal to 30 (one significant digit) and preferably at most equal to 200.
It is highly desirable that the emulsion and/or the dispersion should be dispersed as little as possible.
Thus, in the case of the polyhydroxylated polymers, the polydispersity index (defined as I (d 90 -dj 10 )/d 50 is at most equal to 2 advantageously equal to 1. These t971-Q.X 900d 9WON 2692SBE9 EO T9 A3NCLAS MSE 80:9T 00/pO/90 [Sszg ON XH/MI 9o:LT flH.L 00, values are particularly satisfac-tory for latices. With thle other types of polymers the best results are obtained with values of 0.2 to 0.1 or even less, Thus in the case of the polyisocya1ates, masked or otherwise, the polydispersity index defined 18.....DO ,0dc -9TV'ON EGS98ZB9 ZO T9 4- AANaIAS MSE 80:91 00/tp0/90 6 as (d,g-d 0 /ds is at most equal to 2 advantageously equal to 1. The best results are obtained with values of 0.9 to 0.8 or even less.
The formulation regions depend on the ratio R of the mean sizes between the isocyanate emulsion and those of the dispersion of polyhydroxylated polymer(s), advantageously of polyols.
R is equal to the mean size of the emulsion over the mean size of the dispersion of polyhydroxylated polymer, advantageously of polyol.
According to the invention, the quantity of polyhydroxylated polymer, advantageously of polyol, in the mixture is chosen so as to meet the following constraint: 15 the content of polyhydroxylated polymer, advantageously of polyol, expressed in mass per cent, is at least equal to(5/6R- advantageously at least equal to(5/6R 18, o preferably to 5/6R 16; with R equal to the ratio of the mean size (dso) of the emulsion to that of the dispersion of polyhydroxylated polymer, advantageously of polyol.
In other words R (d 50 of the emulsion)/(d 50 of the dispersion).
The ratio of the number of hydroxyl functional groups to the number of isocyanate functional groups, masked or otherwise, can vary very widely, as shown above.
7 Ratios which are lower than the stoichiometry promote plasticity, while ratios which are higher than the stoichiometry produce coatings of great hardness.
It is rare to have ratios which depart from the range extending from 0.5 to 2.
However, in the majority of cases and for the most common applications, to obtain varnish or paint films which are satisfactory, it is preferable that the quantity, expressed in equivalents, of reactive blocked isocyanates should be substantially equal to that of the free and reactive alcohol functional groups, expressed in equivalents, that is to say corresponding to the stoichiometry. By way of guidance, it may be indicated that a tolerance of plus or minus 20 15 relative to the stoichiometry exists, but it is preferably to employ only a tolerance of plus or minus or 20 The isocyanate emulsions are advantageously Smade according to the technique described in the French 20 Patent Application published under No. 2703358 on 7.10.94, filed on 31.3.1993 under No. 93 03795 and entitled: "Process for the preparation of aqueous emulsions of advantageously masked (poly)isocyanate oils and/or gums and/or resins and emulsions obtained".
With regard to the additional components of a composition according to the present invention, it is possible that it additionally comprises at least one catalyst for releasing the masked isocyanates, and [GSgg ON XH/Xl 90:LT M1HJ 00, t0/9O especially tin-based catalysts which are latent or otherwise. It may be stated that these catalysts may be present either within the poiyoi phase or within the masked isocyanate phase or in dispersed form within the continuous aqueous phase. Finally, they may bc dissolved in the aqueous phase.
The polyoi dispersions which can be used for the invention are, except as regards their fineness, conventional products employed in the paint and varnish industry. In most cases they are (co)polymers manufactured in emulsion according to the conventional processes of radical or bulk polymerisation.
The nanolatices are advantageously those which can be obtained by the processes too: 10 described or mentioned in the EP 694615 or those which are described in their use as too.
binder in EP' 652269.
are made more particularly froam alkylenediol acrylate and especially from ethylene glycol methacrylate, which has one of the "oF' functional groups free.
The technique described in EP 694615 may be recalled hereinafter.
This process makes it possible to prepare latices as emulsion of ultrafine size, too. which do not discolour, have a narrow particle size distribution and are easily reproducible, employing a minimum quantity 71
C)
197I- .0 800d 9TV'ON BO~~d S~~t'0N £GS~879 ZO T 9 4- A,3NcAS Ms9 09 0t09 80:9T 00/VO/90 9 of surfactant. This process is characterized in particular by the incremental introduction of monomers and of initiators into an aqueous reaction medium so that the ionicity of the reaction medium remains constant.
An embodiment of the process for producing a water-based dispersion containing between approximately and approximately 50 by weight of solid products comprises the following stages: incremental addition of one or more ethylenically unsaturated monomers capable of polymerizing in an aqueous environment, to a reactor containing water and up to 6.3 parts, per 100 parts of the said monomers, of one or more surfactants; incremental addition of one or more 0 "polymerization initiators to the said reactor; and o 0" polymerization of the said ethylenically unsaturated monomer(s) such that the mean size of 20 the particles of the said polymerized monomers is 0 smaller than 100 nm.
In the preferred embodiments the process employs monomers derived from acrylic acids and esters and gives latices of ultrafine size which have a mean particle size smaller than 50 nm.
The polymer latex of ultrafine size which is obtained by this process is stable to coagulation and can therefore be diluted with water. The polymer particles have a number of physical attributes such as good film formation, good penetration into porous substrates, a very high ratio of specific surface to volume, a monomodality and the like.
If one returns to non-nanolatex polyols, by way of example or rather as paradigm, the product sold under the trademark: Rhoplex® AC-1024 may be mentioned (compare the datasheet published in 1984).
A pigment known per se may be added in the case of paints, provided that it is inert towards the constituents of the composition.
Although it is possible according to the present invention to employ unmasked isocyanates, and 15 as the latter are not very stable in water, the preferred isocyanates are those which are masked, especially by masking agents which are themselves known, such as phenols, ketone oximes and especially methyl ethyl ketone oxime and various pyrazoles.
20 The preferred isocyanates are those in which
S.
the nitrogen of at least one of the isocyanate groups is attached to a carbon with sp 3 hybridization advantageously carrying one, and preferably two, hydrogen atom(s). The isocyanates in which all the functional groups have this characteristic (possibly with its preferred options) are highly valued.
It is possible in particular to mention isocyanates, masked or otherwise, which have one or ON XH/tl] 90:L a1HUL 00, V0/90 -11more isocyanuric rings and/or at least one of the functionalities of biuret or dimer type.
It is preferable that the isocyanates should exhibit the abovementioned two characteristics, namely oligomerism and aliphatic character on at least one of the isocyanate functional groups.
The water content of the said compositions is advantageously at least equal to one third of the mass of the composition, advantageously at least The preferred polyols are in the form of an aqueous dispersion ofnanolatex; they have a mean size smaller than 50 nanometres. Preference is given to aqueous dispersions with a low content of water-soluble compounds such as alcohols and amines, 10 which can result in the coagulation of the isocyanate emulsion. It is therefore highly desirable that the cumulative content of various alcohols and amines should be lower Than that which would produce a coagulation of the isocyanate emulsion.
The present invention is also aimed at the coatings obtained from the compositions in accordance with the present invention. These coatings may be obtained by 15 crosslinking, in particular by curing at a temperature close to that corresponding to the release of the masked isocyanates, optionally in the presence of one or more catalysts.
Accordingly, in one embodiment, the present invention provides a coating obtainable by crosslinking from the compositions according to the first aspect.
Unless the context clearly requires otherwise, throughout the description and the claims, the words 'comprise', 'comprising', and the like are to be construed in an inclusive sense as opposed to an exclusive or exhaustive sense; that is to say, in the sense of "including, but not limited to".
Rqi R FThe following nonlimiting examples illustrate the invention.
1971 -00 DOC 600d 9TP'ON 269298Z9 F- T9 A3NQaS MSG 60:9T 00/V0/90 Example 1 Tolonate D2® is a mixture of oligomers containing an isocyanuric ring essentially of the trimer masked with methyl ethyl ketone oxime.
Tolonate D2® is a mixture of oligomers containing an isocyanuric ring essentially of the trimer masked with dimethylpyrazole.
Nanolatex 42 is a nanolatex dispersion prepared according to the technique described below. It has a mean diameter of 32.5 nm (hydrodynamic diameter of between 30 and 35 nm), measured by quasielastic light scattering. It consists of 30% of methyl methacrylate unit, of 50% of butyl acrylate unit and of i 20% of ethylene glycol methacrylate (2-hydroxyethyl 15 methacrylate) unit. Its solids content is 29%, its pH is 2.5 and its Tg (glass transition temperature) is equal to The isocyanate is emulsified in the form of an emulsion in which the dso is 1.1 micrometres. The 20 ratio of the sizes is equal to The mixture containing 20% by weight of Nanolatex 42 and 10% by weight of Tolonate® is fluid and stable.
The corresponding 9 Nanolatex 42/ Tolonate® mixture gives rise to a macroscopic phase separation between a fluid phase and a flocculated mixture.
Example 2 Nanolate R27 is a nanolatex dispersion prepared according to the technique described below. It has a mean diameter of 27.5 nm (hydrodynamic diameter of between 20 and 35 nm), measured by quasielastic light scattering. It consists of 40% of methyl methacrylate unit, of 50% of butyl acrylate unit and of of ethylene glycol methacrylate (2-hydroxyethylmethacrylate) unit. Its solids content is 30%, its pH is 2.5 and its Tg (glass transition temperature) is equal to 20 0
C.
The isocyanate is emulsified in the form of an emulsion in which the d 50 is 1.1 micrometres. The ratio of the sizes is equal to 42. The mixture 15 containing 20% by weight of Nanolatex R27 and 10% by weight of Tolonate® is fluid and stable.
*ge The corresponding 12%/12% Nanolatex 42/ Tolonate® mixture gives rise to a macroscopic phase S" separation between a fluid phase and a flocculated 20 mixture.
Example 3 synthesis of the nanolatices of Examples 1 and 2 A charge solution is prepared by mixing acrylic monomers in the proportions shown in each of the examples.
In a separate feed receptacle, 0.25 pph of ammonium peroxydisulphate are added to 65 pph of water.
In a separate reactor, 3 pph of sodium dodecyl sulphate 14 are added to 195 pph of water and heated to 85 0 C with continuous stirring. The reason for the separate preparation of the aqueous initiator solution is to allow a constant ionicity in the reactor throughout the length of the operating method of synthesis. Ten per cent of the total volume of the ammonium peroxydisulphate solution are added to the heated mixture, and the solutions of initiator and of monomer begin to be introduced at a rate which permits a steady introduction of the charge solutions over a period of three hours. The reaction mixture is stirred for a further 30 minutes and then cooled to 62°C. 0.10 pph of sodium metabisulphite are dissolved in 24 pph of water and introduced into the reaction mixture over a period a 15 of 1 hour. The reaction temperature is then raised to 85°C over 1 hour. The mixture is then cooled to ambient a..
temperature and filtered. This charge results in an aqueous polymer latex.

Claims (8)

1. A compositionl comprising: at least one masked or UnMasked polyisocyaflate in the form of an aqueous emulsion whose mean size is between 0. 1 and 10 mnictrnetres at least one polyhydroxYlated. polymer, in the formD of an aqueou.s dispersion whose mean size is between 10 and 200 nanoifletres; 'wherein the quantity of polyhydroxYlated polymer in the mixture is chosen so as to meet the following constraint; -the content of polyhydroxylated polymer, expressed in mass per cent, is at least io equal to (5/6R)-20, 4 with R equal to the ratio of the mean siZe (d 5 of the emulsion to that of the dispersion of polyhydroxylated polymer.
2. A composition according to claim 1, wherein the mean size of the aqueous .4 emulsion of the at least one masked or unmasked polyisocyanate is smaller than 2 and o larger 0.2 micrometes.
3. A compositionl accordinlg to claim 'I or claim 2, wherein the at least one polyhydroXylated polymer is a polyol.
4- A composition according to any one of clairrs 1 to 3, wherein the content of polyhydroxylated polymer expressed in mass percent is at least equal to
18. 5. A composition according to claim 4, wherein the content of polyhydroxylated polymer expressed in mass percent is equal to 16. 6. A composition according to any one of claims I to 5, wherein the said polyisocyanate(s), masked or otherwise, has(hav6) the polydispersity index defined as is at most equal to 2. OT~d 9V'ON£ES8eF9 zo 1-3 )BNGAS [1Sa 60:9T 00/v'0/90 [SGgg ON XH/X1J 90OLT MU 00, i'0/90 16- 7T A composition according to claim 6, wherein the said polyisocyanate(s), masked or otherwise, has(have) the polydisperSity index defined as (d 90 -d 10 )/d 50 that is equal to I. 8. A comnpositionl according to any one of claims I to 7, wherein the said polyhydroxylated polymer(s) has(have) the polyclispersity index (defined as I (doo- d 1 o)/dso) at most equal to 2. 9. A composition according to claim 8, whereirtl the said polyhydroxylated polymer(s) has(have) the polydispersity index (defined as I 9 1 )/d 5 o) equal to I A composition according to any one of claimrs 1 to 9, wherein it additionally comprises at least one catalyst of release of the wasked isocyanates, latent or otherwise. 11. A composition according to claim 10, wherein the at least one catalyst is a tin based catalyst. 12. A composition according to any one of claims I toll1, wherein the water content of the said compositions is at least equal to one third of the mass of thc composition. C. 13. A composition ac~cording to claim 12, wherein the water content of the said composition is at least 215. 14- A composition according to any one of clairns 1Ito 13, wherein the said polyisocyaflate has(have) one or more isocyanuric rings and/or at least one of the fanctionalities is biuret or dimer type. A composition according to any one of claims 1 to 14, wherein the said polyisocyaflate is chosen from those in which the nitrogen of at least one of the isocyaflate functional groups is attached to a carbon with sp 3 hybridisation. T TT08 9TV'ON tT~d 9W0N GGE9 EO -i9 )3NGAS flSEl 60:9T 00/VO/90 [SSZR ON XMI/X1L] 9O LT aUH 00, 170/90 16. A composition according to claimi 15, wherein the carbon with sp 3 hybridisation carries one hydrogen atom. 17. A compositionl according to claim 15, wherein the carbon with sp 3 hybridisation carries two hydrogen atoms. 18. A compositionl according to any one Of claims I to 17, wherein the said polyisocyanate is chosen from those which gre, mfasked especiallY by masking agents a which are themselves known, such as phenols, ketone oximfes and especially Methyl a ethy ketone oxime, and the vaious pyrazoles.
19. A composition according to any one of claims I to 18, wherein the said polyol is a 0 nanolatex. A coating obtainable by crosslinkinfg from, the compositions according to any one of claims I to 18,
21. A composition comnprising at least one masked or unmasked polyisocyanate in the a* form of an aqu1eous emulsion and at least one polyhydroxylated polymer, substantially as 15herein described with reference to one or more of the Examples excluding any control or comparative compositions.
22. A coating obtained by crosslinkuig at least one masked or unmasked polyisocyaflate and at least one polyhydroxylated polymer, substantially as herein described with reference to one or more of the Examples excluding any control or conparative coating. DATED this 6th day of April 2000 RHONE-POULEN~C CHIMIE Attorney: IVAN A- RAJKOVIC Fellow Institute of Patent Attorneys of Australia 2 5 of BALDWIN SHELSTON WATERS T~d 9Tt'ON E: 9 SB 9 F T9 AkNCAS Msg 60:9 1 00/V70/90
AU44414/96A 1995-02-21 1996-02-07 Composition, for use in coatings, based on a mixture of emulsion(s) and of dispersion(s) of polyol polymer and coating(s) produced therefrom Ceased AU720369B2 (en)

Applications Claiming Priority (2)

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FR9502001 1995-02-21
FR9502001A FR2730738B1 (en) 1995-02-21 1995-02-21 COMPOSITION USEFUL FOR COATINGS, BASED ON MIXTURE OF POLYOL POLYMER EMULSION (S) AND DISPERSION (S) AND COATINGS THEREOF

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AU4441496A AU4441496A (en) 1996-08-29
AU720369B2 true AU720369B2 (en) 2000-06-01

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EP (1) EP0728786B1 (en)
JP (1) JP2975304B2 (en)
KR (1) KR100397651B1 (en)
CN (1) CN1078901C (en)
AT (1) ATE207504T1 (en)
AU (1) AU720369B2 (en)
BR (1) BR9600770A (en)
CA (1) CA2169897C (en)
DE (1) DE69616110T2 (en)
DK (1) DK0728786T3 (en)
ES (1) ES2166430T3 (en)
FR (1) FR2730738B1 (en)
HU (1) HU218014B (en)
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FR2730737B1 (en) * 1995-02-21 1997-06-06 Rhone Poulenc Chimie COMPOSITION USEFUL FOR PAINT BASED ON MIXTURE OF EMULSION (S) AND DISPERSION (S) OF POLYOL POLYMER AND COATING (S) THEREOF
FR2775482A1 (en) * 1998-03-02 1999-09-03 Rhodia Chimie Sa COATING WITH TWO POLYOLS, COMPOSITION USEFUL FOR THESE COATINGS AND PROCESS FOR OBTAINING THESE COATINGS
CN100363449C (en) * 2001-12-31 2008-01-23 熊永强 Double component aluminum plate imitating surface paint

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US5322865A (en) * 1992-01-29 1994-06-21 Kansai Paint Co., Ltd. Aqueous color paint compositions and coating method using same
US5508337A (en) * 1992-02-11 1996-04-16 Bayer Aktiengesellschaft Powder coating compositions, a process for their preparation, and their use for the coating of heat resistant substrates

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DE69616110T2 (en) 2002-06-20
ES2166430T3 (en) 2002-04-16
CA2169897C (en) 2001-04-17
JP2975304B2 (en) 1999-11-10
DK0728786T3 (en) 2002-02-11
HUP9600388A1 (en) 1997-10-28
DE69616110D1 (en) 2001-11-29
EP0728786A1 (en) 1996-08-28
ATE207504T1 (en) 2001-11-15
HU9600388D0 (en) 1996-04-29
KR960031540A (en) 1996-09-17
FR2730738B1 (en) 1997-06-06
BR9600770A (en) 1997-12-23
PT728786E (en) 2002-04-29
FR2730738A1 (en) 1996-08-23
KR100397651B1 (en) 2004-04-17
CN1078901C (en) 2002-02-06
ZA961202B (en) 1996-07-30
CA2169897A1 (en) 1996-08-22
HU218014B (en) 2000-05-28
MX9600668A (en) 1997-02-28
AU4441496A (en) 1996-08-29
CN1134438A (en) 1996-10-30
EP0728786B1 (en) 2001-10-24
JPH08259653A (en) 1996-10-08

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