[go: up one dir, main page]

GB2051096A - Macromonomers - Google Patents

Macromonomers Download PDF

Info

Publication number
GB2051096A
GB2051096A GB7940085A GB7940085A GB2051096A GB 2051096 A GB2051096 A GB 2051096A GB 7940085 A GB7940085 A GB 7940085A GB 7940085 A GB7940085 A GB 7940085A GB 2051096 A GB2051096 A GB 2051096A
Authority
GB
United Kingdom
Prior art keywords
macromonomer
anhydride
polymer
oligomer
hydroxyl group
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.)
Granted
Application number
GB7940085A
Other versions
GB2051096B (en
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.)
Dulux Australia Ltd
Imperial Chemical Industries Ltd
Original Assignee
Dulux Australia Ltd
Imperial Chemical Industries Ltd
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 Dulux Australia Ltd, Imperial Chemical Industries Ltd filed Critical Dulux Australia Ltd
Priority to GB7940085A priority Critical patent/GB2051096B/en
Priority to MX18023279A priority patent/MX152451A/en
Priority to BR7907965A priority patent/BR7907965A/en
Priority to AR27918979A priority patent/AR225299A1/en
Publication of GB2051096A publication Critical patent/GB2051096A/en
Application granted granted Critical
Publication of GB2051096B publication Critical patent/GB2051096B/en
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
    • C08G85/00General processes for preparing compounds provided for in this subclass
    • C08G85/004Modification of polymers by chemical after-treatment
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08FMACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F290/00Macromolecular compounds obtained by polymerising monomers on to polymers modified by introduction of aliphatic unsaturated end or side groups
    • C08F290/02Macromolecular compounds obtained by polymerising monomers on to polymers modified by introduction of aliphatic unsaturated end or side groups on to polymers modified by introduction of unsaturated end groups
    • C08F290/06Polymers provided for in subclass C08G
    • C08F290/062Polyethers
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08FMACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F8/00Chemical modification by after-treatment
    • C08F8/14Esterification
    • 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
    • C08G65/00Macromolecular compounds obtained by reactions forming an ether link in the main chain of the macromolecule
    • C08G65/02Macromolecular compounds obtained by reactions forming an ether link in the main chain of the macromolecule from cyclic ethers by opening of the heterocyclic ring
    • C08G65/32Polymers modified by chemical after-treatment
    • C08G65/329Polymers modified by chemical after-treatment with organic compounds
    • C08G65/331Polymers modified by chemical after-treatment with organic compounds containing oxygen
    • 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
    • C08G65/00Macromolecular compounds obtained by reactions forming an ether link in the main chain of the macromolecule
    • C08G65/02Macromolecular compounds obtained by reactions forming an ether link in the main chain of the macromolecule from cyclic ethers by opening of the heterocyclic ring
    • C08G65/32Polymers modified by chemical after-treatment
    • C08G65/329Polymers modified by chemical after-treatment with organic compounds
    • C08G65/331Polymers modified by chemical after-treatment with organic compounds containing oxygen
    • C08G65/332Polymers modified by chemical after-treatment with organic compounds containing oxygen containing carboxyl groups, or halides, or esters thereof
    • C08G65/3324Polymers modified by chemical after-treatment with organic compounds containing oxygen containing carboxyl groups, or halides, or esters thereof cyclic

Landscapes

  • Chemical & Material Sciences (AREA)
  • Health & Medical Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Organic Chemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Macromonomer-Based Addition Polymer (AREA)

Abstract

Macromonomers are obtained by successively reacting an oligomer or polymer containing at least one hydroxyl group with a carboxylic cyclic anhydride in an amount of at least one mole of the anhydride per hydroxyl group, and reacting the product with a compound containing a single epoxide group and a single polymerizable double bond, in such proportions as to esterify all carboxyl groups in that product. Graft copolymers which are useful as steric stabilisers for dispersions of polymer particles can be made by copolymerising the macromonomers with other polymerisable monomers. Examples relate to reaction with polyoxyethylenes and ethers thereof, e.g. with succinic anhydride and subsequently with glycidyl methacrylate.

Description

SPECIFICATION Macromonomers This invention relates to macromonomers, that is to say to oligomeric or polymeric molecules which contain one or more polymerisable double bonds by virtue of which they are capable of copolymerising with other, low molecular weight monomers to form polymers of greater complexity.
A number of procedures have previously been described for preparing macromonomers, but these suffer from the disadvantage that various byproducts are also formed which can interfere with the subsequent copolymerisation of the macromonomer with other monomers and which therefore have to be removed beforehand. For example, an oligomer or polymer having a reactive hydroxyl group may be subjected to ester interchange with an acrylic or methacrylic ester of a lower alcohol, such as methyl methacrylate, but it is generally necessary to use a large excess of the ester most or all of which may have to be separated later together with the lower alcohol released as by-product.
Alternatively, a hydroxylic oligomer or polymer may be reacted with an acid chloride derived from a polymerisable acid, such as acrylic acid or methacrylic acid, but the reaction requires the presence of a base in order to neutralise the hydrogen chloride by-product and there is then a problem of separating the base hydrochloride from the macromonomer formed.
Yet again, the hydroxylic oligomer or polymer may be esterified with a polymerisable acid itself, or with its an hydride, but here also there may be a problem of removing excess reagent and in addition it will be necessary to remove the catalyst, such as sulphuric acid or methane sulphonic acid, which is conventionally used in such a reaction.
A procedure has now been found whereby a hydroxyl group-containing oligomer or polymer can be easily converted into a derivative having one or more polymerisable double bonds by reactions which do not require the use of catalysts, and/or do not lead to the formation of any by-products, which could interfere with the subsequent copolymerisation of the derivative with another monomer.
According to the present invention, there is provided a macromonomer which is obtained by (i) reacting an oligomer or polymer containing at least one hydroxyl group with a cyclic carboxylic anhydride in an amount of at least one mole of the anhydride per hydroxyl group present in the oligomer or polymer, and (ii) reacting the product so obtained with a compound containing in the molecule a single epoxide group and a single polymerisable double bond in such proportions that all carboxyl groups in the said product are thereby esterified. Suitable oligomers of polymers containing at least one hydroxyl group may be of various types.They may, for example, be derived from unsaturated monomers, such as one or more acrylic or vinyl monomers; terminal hydroxyl groups may be introduced into the oligomer or polymer by polymerising the monomer(s) from which it is derived in the presence of a hydroxyl group-containing initiator and of a hydroxyl group-containing chain transfer agent, according to the method described in British Patent Specification No. 1,096,912. Suitable monomers of use in this method include the esters, amides and nitriles of acrylic acid and methacrylic acid, styrene and alkyl styrenes, vinyl esters of organic and inorganic acids such as vinyl acetate and vinyl chloride, and vinyl heterocyclic compounds such as 2-vinyl-pyrrolidone.Alternatively the oligomers or polymers may be of the type derived from cyclic monomers, such as those obtained by the polymerisation of alkylene oxides using a hydroxylic initiator such as water or a lower alcohol. Thus suitable oligomers or polymers of this type are the polyethylene glycols, the polypropylene glycols and the poly-(ethylene oxide) - poiy(propylene oxide) block copolymers all of which contain two terminal hydroxyl groups in the molecule, or the corresponding monoalkyl ethers which contain a single terminal hydroxyl group. Yet other suitable oligomers and polymers include hydroxyl group-containing polyesters and hydroxyl group-containing polymers derived from epoxy resins.The location of the hydroxyl group or groups in the oligomer or polymer molecule is not critical, the important point being simply that it should be sufficiently reactive with the cyclic carboxylic anhydride; however, with steric considerations in mind, it is preferred that the hydroxyl group or groups should be terminal with regard to the oligomer of polymer chain. Similarly, the molecular weight of the oligomer or polymer is not critical to the performance of the invention, except for the possibility that as higher molecular weights are approached the reactivity of the hydroxyl group may fall to an inconveniently low level.
Suitable cyclic carboxylic anhydrides include both aliphatic and aromatic types, for example succinic anhydride, glutaric anhydride, 3:3 - dimethylglutaric anhydride, adipic anhydride, maieic anhydride, itaconic anhydride and phthalic anhydride.
Suitable compounds containing in the molecule a single epoxide group and a single polymerisable double bond include glycidyl acrylate, glycidyl methacrylate, allyl glycidyl ether and methallyl glycidyl ether.
Step (i) of the process whereby the macromonomers of the invention are obtained may be carried out in the presence of a suitable inert solvent, for example a hydrocarbon. such as toluene, by heating the reactants to a temperature sufficient to bring about the desired reaction, resulting in the production of the half-ester of the carboxylic acid with the hydroxylic oligomer or polymer. A suitable temperature will normally be in the range 1200 to 1500C. The progress of the reaction may be followed by infra-red analysis or by measurement of acid value of the reaction mixture. In the event that the reaction proceeds sluggishly in the later stages, the solvent may be stripped off so as to allow a higher operating temperature.
In order to ensure that, in step (i), all the hydroxyl groups in the oligomer of polymer are converted to half-ester with the carboxylic anhydride, a stoichiometric excess of the anhydride may if desired be used. After completion of step (i), unreacted anhydride may then be converted to half-ester prior to the carrying out of step (ii) by reacting it with a lower alcohol, such as n-butanol or dimethylaminoethanol.
Step (ii) of the process is also carried out at an elevated temperature, for example at from 1200 to 1 500C, and here again the progress of the reaction may be followed by acid value measurement; preferably the reaction is continued until the acid value is substantially zero.
The proportion of epoxy compound taken may be stoichiometric with respect to the free carboxyl groups present in the half-ester resulting from step (i) (including any half-ester derived from excess carboxylic anhydride, as described in the preceding paragraph), but, in the interests of facilitating the reaction, it will usually be desirable to employ a stoichiometric excess of the epoxy compound.
Where the oligomer or polymer contains only a single terminal hydroxyl group, as in the case of the monoethyl ether of a polyethylene glycol, the macromonomer finally obtained will contain a single terminal polumerisable double bond. If a polyethylene glycol itself is employed, then the macromonomer may correspondingly contain two terminal polymerisable double bonds; however it is possible in this case to employ less than the amounts of the carboxylic anhydride and of the epoxy compounds which are theoretically required to achieve this in which event the final product will be a statistical mixture consisting of a species containing two double bonds, a species containing one double bond and one of the original hydroxyl groups of the oligomer or polymer, and unreacted oligomer or polymer, respectively.
The macromonomers of the invention are readily copolymerisable with other monomers containing polymerisable double bonds to form graft copolymers. Thus, for example, the macromonomer derived from the monomethyl ether of poiy-ethylene glycol molecular weight 2000, reacted with succinic anhydride followed by reaction with glycidyl methacrylate, may be copolymerised in a weight ratio of 1:1 with methyl methacrylate, or with a mixture of methyl methacrylate and butyl acrylate, to give a graft copolymer consisting of an acrylic polymer backbone carrying a plurality of pendant chains derived from the polyethylene glycol.The copolymerisation may be carried out under the conditions well known in the art for the polymerisation of acrylic monomers, that is to say by heating the monomers at a suitably elevated temperature, preferably in the presence of a catalyst or initiator such as an organic azo or peroxy compound, and if desired in solution in a suitable inert liquid which is a solvent both for the macromonomer and the co-monomer(s), and for the copolymer which is produced.
Selected copolymers made in this way, as in the illustration given above, can be arranged to consist of two major molecular components of sharply differing polarity. Thus, where the chain of the oligomer or polymer from which the macromonomer is derived is of a relatively polar nature, the macromonomer may be copolymerised with one or more monomers which give rise to a polymer chain of relatively low polarity. Conversely, a macromonomer containing a non-polar chain may be copolymerised with monomers of a nature such as to yield a second chain which is relatively highly polar. Such amphipathic graft copolymers are very useful as steric stabilisers in the production of dispersions of particles, especially polymer particles, in liquids in which the particles are insoluble.For this purpose, the stabilising copolymer requires to contain in the molecule one component which is solvatable by the liquid of the dispersion and which therefore in practice is of a similar degree of polarity to that liquid; this component forms a steric barrier of solvated chains surrounding each particle. The copolymer at the same time requires to contain a second molecular component which is not solvatable by the dispersion liquid, and hence is of a different polarity to that liquid and also to the first component of the copolymer; this non-solvated component becomes associated with the particles, thus serving to anchor the steric barrier to their surfaces. By means of this barrier the particles are enabled to resist the attraction forces which nornally tend to cause them to flocculate or aggregate.
For the production of amphipathic graft copolymers to be used as steric stabilisers in nonaqueous media of low polarity such as aliphatic hydrocarbons, macromonomers according to the invention which are derived from non-polar oligomers or polymers are useful, for example an oligomer or polymer of a long-chain alkyl ester of acrylic or methacrylic acid, such as lauryl methacrylate. Such a macromonomer is copolymerised with rather more polar monomers such as methyl methacrylate, and the resulting copolymer can be used to stabilise particles of polymethyl methacrylatein an aliphatic hydrocarbon.
Conversely, in order to produce an amphipathic graft copolymer suitable as a steric stabiliser in an aqueous medium, a macromonomer according to the invention will be used which is derived from a polar, hydrophilic oligomer or polymer.
Particularly useful such oligomers or polymers are the polyethylene glycols, the polypropylene glycols and the poly(ethylene oxides) poly(propylene oxide) block copolymers, and their monoalkyl ethers, of molecular weight from 200 to 5000, and the hydroxyl group-terminated polyvinyl pyrrolidones obtained by the method referred to above. Macromonomers derived from these oligomers or polymers are copolymerised with monomers of relatively lower polarity, for example with acrylic or methacrylic acid esters.
The resulting copolymers can be used as steric stabilisers for dispersions in aqueous media of particles of polymer derived from the same or similar acrylic or methacrylic esters.
Where, in any of the sterically stabilised polymer dispersions mentioned above, it is acceptable or desired that the non-solvated or "anchor" component of the stabiliser should be identical in chemical composition to the polymer of the disperse phase, and where the disperse polymer is produced by polymerisation of monomer actually in the liquid which is to form the continuous phase, an appropriate macromonomer according to the present invention may be introduced into the reaction mixture before polymerisation is begun. When polymerisation proceeds, a minor part of the monomer or monomers copolymerised with the macromonomer to form the required amphipathic copolymer in situ; this effects stabilisation of the polymer particles as they are formed from the major part of the monomer.
The invention is illustrated by the following Examples, in which percentages are by weight.
Example 1 To a 6 litre flask fitted with stirrer, thermometer, Dean and Stark separator, reflux condenser and provision for introduction of inert gas there was charged 3000 g (1.5 moles) of the monoethyl ether of polyethylene glycol (mol. wt.
2000) and 600 g of toluene. The charge was heated to reflux temperature (about 1 400C) and any water present was removed by azeotropic distillation via the Dean and Stark separator. The charge was then cooled to about 80"C and 150 g (1.5 moles) of succinic anhydride was added.
Reaction was effected at reflux temperature until measurement of acid value of the mixture showed that all the succinic anhydride had been converted to the half-ester. After cooling the mixture to 900C, 3 g of hydroquinone, 320 g (2.25 moles) of glycidyl methacrylate and 4.6 g of dimethyl coconut amine were added in that order, the mixture heated to 130-1 500C and held at that temperature until the acid value had fallen substantially to zero indicating complete reaction of the half-ester with the glycidyl methacrylate.
The product was a 85% solids solution in toluene of macromonomer containing a chain derived from the polyethylene glycol and a single polymerisable unsaturated grouping.
Example 2 To a 2-litre flask fitted as described in Example 1 was charged 1000 g (0.5 mole) of the monoethyl ether of polyethylene glycol (mol. wt.
2000) and 100 g of toluene. Following the procedure of Example 1 there was added, after azeotropic removal of water, 100 g (1.0 mole) of succinic anhydride and the temperature of the reaction mixture was maintained at about 1 400C until the acid value was 76 mg KOH/g. On cooling to 1000C, there was then added 45 g (0.5 mole) of N,N-dimethylaminoethanol and the temperature was held at 1 400C until the acid value was 49 mg KOH/g. The patch was cooled to 700C and 1 g of hydroquinone was added followed by 160 g (1.1 moles) of glycidyl methacrylate. The mixture was heated carefully up to 1200 C, observing the onset of any exothermic reaction, and was then maintained at that temperature until the acid value was substantially zero.
The product was a 93% solids toluene solution of a macromonomer containing a chain derived from the polyethylene glycol and a single polymerisable unsaturated grouping, accompanied by the glycidyl methacrylate adduct of the half-ester of succinic acid with dimethylaminoethanol.
Example 3 Using the apparatus and procedure described in Example 1,750 g (1.0 mole) of the monoethyl ether of polyethylene glycol (mol wt. 750), 50 g of toluene and 100 g (1.0 mole) of succinic anhydride were heated together to form the halfester, following which there were added 2 g of hydroquinone, 200 g (1.4 moles) of glycidyl methacrylate and 2.5 g of dimethyl coconut amine.
The product was analogous to that obtained in the case of Example 1.
Example 4 Using the apparatus and procedure described in Example 1,4000 g (1.0 mole) of polyethylene glycol (mol. wt. 4000), 800 g of toluene and 1 60 g (1.6 moles) of succinic anhydride were reacted together, followed by 3 g of hydroquinone, 300 g (2.1 moles) of glycidyl methacrylate and 4.5 g of dimethyl coconut amine.
The product was a mixture of species; Poisson distribution calculations indicate that the composition of the mixture was approximately 4% unreacted polyethylene glycol, 32% of the derivative containing one of the original hydroxyl groups of the polyethylene glycol and one polymerisable double bond per molecule, and 64% of the derivative containing two polymerisable double bonds per molecule.
Example 5 The procedure of Example 1 was repeated, using in place of the stated amount of glycidyl methacrylate an equivalent amount of glycidyl acrylate.
An analogous product to that of Example 1 was obtained.
Example 6 The procedure of Example 1 was repeated, using in place of the stated amount of succinic anhydride an equivalent amount of phthalic an hydride.
An analogous product to that of Example 1 was obtained.
Example 7 The procedure of Example 1 was repeated, using in place of the stated amount of succinic anhydride an equivalent amount of glutaric anhydride.
An analogous product to that of Example 1 was obtained.

Claims (10)

Claims
1. A macromonomer which is obtained by (i) reacting an oligomer or polymer containing at least one hydroxyl group with a cyclic carboxyl anhydride in an amount of at least one mole of the anhydride per hydroxyl group present in the oligomer or polymer, and (ii) reacting the product so obtained with a compound containing in the molecule a single epoxide group and a single polymerisable double bond in such proportions that all carboxyl groups in the said product are thereby esterified.
2. A macromonomer as claimed in claim 1, wherein the oligomer or polymer containing at least one hydroxyl group is a polyethylene glycol or a monoalkyl ether thereof.
3. A macromonomer as claimed in claim 1 or claim 2, wherein the cyclic carboxylic anhydride is selected from succinic anhydride, glutaric anhydride and phthalic anhydride.
4. A macromonomer as claimed in any one of claims 1 to 3, wherein the compound containing a single epoxide group and a single polymerisable double bond is selected from glycidyl acrylate and glycidyl methacrylate.
5. A macromonomer as claimed in any one of claims 1 to 4, wherein after completion of step (i) of the reaction sequence, unreacted anhydride is converted to half-ester by reacting it with a lower alcohol.
6. A macromonomer as claimed in any one of claims 1 to 5, wherein step (ii) of the reaction sequence is continued until the acid value of the product is substantially zero.
7. A macromonomer according to claim 1 substantially as hereinbefore described, with reference to the foregoing Examples.
8. A graft copolymer obtained by copolymerising a macromonomer as claimed in any one of claims 1 to 7, with other monomers containing polymerisable double bonds.
9. A graft copolymer as claimed in claim 8, wherein the two major molecular components of the copolymer are of sharply differing polarity.
10. Use of a graft copolymer as claimed in claim 9 for the steric stabilisation of polymer particles in a liquid in which the particles are insoluble, one of the major molecular components of the copolymer being solvatable by the liquid and the other major molecular component being non-solvatable by the liquid and associated with the particles.
GB7940085A 1978-12-07 1979-11-20 Macromonomers Expired GB2051096B (en)

Priority Applications (4)

Application Number Priority Date Filing Date Title
GB7940085A GB2051096B (en) 1978-12-07 1979-11-20 Macromonomers
MX18023279A MX152451A (en) 1978-12-07 1979-11-29 PROCEDURE TO PREPARE GRAFT COPOLYMERS
BR7907965A BR7907965A (en) 1978-12-07 1979-12-06 PROCESS OF OBTAINING MACROMONOMERS AND THE RELATIVE GRAFT COPOLIMERS, AS WELL AS THE PROCESS OF STABILIZATION OF THE POLYMER PARTICLES IN A LIQUID
AR27918979A AR225299A1 (en) 1978-12-07 1979-12-07 MACROMONOMERS WITH AT LEAST ONE DOUBLE POLYMERABLE LINK

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
GB7847584 1978-12-07
GB7940085A GB2051096B (en) 1978-12-07 1979-11-20 Macromonomers

Publications (2)

Publication Number Publication Date
GB2051096A true GB2051096A (en) 1981-01-14
GB2051096B GB2051096B (en) 1983-05-18

Family

ID=26269879

Family Applications (1)

Application Number Title Priority Date Filing Date
GB7940085A Expired GB2051096B (en) 1978-12-07 1979-11-20 Macromonomers

Country Status (4)

Country Link
AR (1) AR225299A1 (en)
BR (1) BR7907965A (en)
GB (1) GB2051096B (en)
MX (1) MX152451A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0107300A1 (en) * 1982-10-01 1984-05-02 Imperial Chemical Industries Plc Redox-initiated polymerisation process for the production of non-charged, wholly sterically stabilised aqueous polymer dispersions
EP0434446A3 (en) * 1989-12-22 1991-11-21 Nitto Chemical Industry Co., Ltd. Radical-curing polyvinyl alcohol derivative
WO1994018260A1 (en) * 1993-02-09 1994-08-18 Dsm N.V. Water-soluble and air-drying resin
WO2007052122A1 (en) * 2005-11-04 2007-05-10 Coatex S.A.S. Method of producing an impact-resistant thermoplastic resin

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0107300A1 (en) * 1982-10-01 1984-05-02 Imperial Chemical Industries Plc Redox-initiated polymerisation process for the production of non-charged, wholly sterically stabilised aqueous polymer dispersions
EP0434446A3 (en) * 1989-12-22 1991-11-21 Nitto Chemical Industry Co., Ltd. Radical-curing polyvinyl alcohol derivative
US5200464A (en) * 1989-12-22 1993-04-06 Nitto Chemical Industry Co. Ltd. Water-soluble radical-curing polyvinyl alcohol derivative
WO1994018260A1 (en) * 1993-02-09 1994-08-18 Dsm N.V. Water-soluble and air-drying resin
BE1007442A3 (en) * 1993-02-09 1995-07-04 Dsm Nv Water-soluble resin.
WO2007052122A1 (en) * 2005-11-04 2007-05-10 Coatex S.A.S. Method of producing an impact-resistant thermoplastic resin
FR2893031A1 (en) * 2005-11-04 2007-05-11 Coatex Sas PROCESS FOR PRODUCING A THERMOPLASTIC RESIN WITH ENHANCED IMPACT RESISTANCE USING A COMBINED POLYMER WITH AT LEAST ONE POLYALKYLENE OXIDE GRAY FUNCTION AND RESINS OBTAINED
US8536292B2 (en) 2005-11-04 2013-09-17 Omya International Ag Method of producing an impact-resistant thermoplastic resin

Also Published As

Publication number Publication date
AR225299A1 (en) 1982-03-15
MX152451A (en) 1985-07-23
BR7907965A (en) 1980-07-22
GB2051096B (en) 1983-05-18

Similar Documents

Publication Publication Date Title
US4273888A (en) Macromonomers
KR950008509B1 (en) Method of manufacturing polyalkyl methacry late macromoners and of same in the manufacture of comb polymers
JPS58167606A (en) Preparation of graft copolymer by radical copolymerization
CA2147903A1 (en) Polymers from propoxylated allyl alcohol
KR101794383B1 (en) Aziridinyl-containing compounds
US4818804A (en) Polycondensable macromonomer from vinyl monomer and mercapto compound
EP0779305A2 (en) Macromonomers with high acid content and their method of preparation
GB2051096A (en) Macromonomers
EP0703250B1 (en) Polymers of allyl esters with allylic alcohols or propoxylated allylic alcohols
US5480954A (en) Allyl ester copolymers with allylic alcohols or propoxylated allylic alcohols
US3583955A (en) Saturated linear polymers having pendant functionality
US3640931A (en) Cross-linkable derivatives of an addition polymer in a substantially nonpolar organic liquid
EP0564703B1 (en) Macromers of vinylidene fluoride arylate-terminated poly(vinylidene fluoride) and its copolymeric thermoplastic elastomers
US5420216A (en) Process for making allyl polymers and copolymers
JP2697934B2 (en) Method for producing radically polymerizable polyolefin
Xie et al. Copolymerization of polymethyl methacrylate macromers with n-butyl acrylate and mechanical properties of the graft copolymers
JP2002517528A (en) Method for producing allyl / ethylene copolymer
US3607974A (en) Thermosetting resin containing pendant unsaturation and monomer where monomer and pendency have identical functionality
JPH06322042A (en) Bulk polymerization method
JPH10279528A (en) Itaconic acid ester and its polymer
JPH10510314A (en) Functionalized p-alkylstyrene polymers and copolymers
US5254667A (en) Macromers for preparation of graft polymer polyol dispersions
Odeberg et al. Influence of spacer groups on grafting ability, curing ability, and film properties of water‐based radiation curable latexes
US6031066A (en) Process for producing α, β-unsaturated carboxylic acid ester polymer
JP4145173B2 (en) Three-arm star polymer containing polyolefin segment

Legal Events

Date Code Title Description
PCNP Patent ceased through non-payment of renewal fee