Claims Analysis
Total Claims: 15
Claim 1
Independent Claim
233 words
A process for producing a powdered copolymer of an ethylenically unsaturated compound having a terminal double bond and maleic anhydride or an ester derivative thereof, which comprises polymerizing a polymerizable reactant mixture comprising an ethylenically unsaturated compound having a terminal double bond and being represented by the general formula: ##STR3## wherein R 1 is hydrogen, an alkyl group having 1 to 15 carbon atoms, an aryl group, --OR 3 , ##STR4## and R 2 and R 3 are independently hydrogen or an alkyl group having 1 to 10 carbon atoms, and maleic anhydride or an ester derivative thereof in a kneading machine with continuous kneading of the reactant mixture in the presence or absence of a poor solvent for the copolymer to form a highly viscous resin phase containing the copolymer produced and remaining polymerizable reactant mixture at least one reactant of which is capable of dissolving the copolymer, further kneading the highly viscous resin phase, effecting further polymerization of the resin phase while kneading is continued with tearing of the resin phase to produce solid resin aggregates containing said copolymer, and continuing the kneading to effect powdering of the solid resin aggregates to produce a powdered copolymer; the internal free volume of the kneading machine being about twice or more of the volume of the reactant mixture or the total volume of the reactant mixture and the poor solvent for the copolymer.
Claim 2
Dependent Claim
233 words
A process for producing a powdered copolymer of an ethylenically unsaturated compound having a terminal double bond and maleic anhydride or an ester derivative thereof, which comprises polymerizing a polymerizable reactant mixture comprising an ethylenically unsaturated compound having a terminal double bond and being represented by the general formula: ##STR3## wherein R 1 is hydrogen, an alkyl group having 1 to 15 carbon atoms, an aryl group, --OR 3 , ##STR4## and R 2 and R 3 are independently hydrogen or an alkyl group having 1 to 10 carbon atoms, and maleic anhydride or an ester derivative thereof in a kneading machine with continuous kneading of the reactant mixture in the presence or absence of a poor solvent for the copolymer to form a highly viscous resin phase containing the copolymer produced and remaining polymerizable reactant mixture at least one reactant of which is capable of dissolving the copolymer, further kneading the highly viscous resin phase, effecting further polymerization of the resin phase while kneading is continued with tearing of the resin phase to produce solid resin aggregates containing said copolymer, and continuing the kneading to effect powdering of the solid resin aggregates to produce a powdered copolymer; the internal free volume of the kneading machine being about twice or more of the volume of the reactant mixture or the total volume of the reactant mixture and the poor solvent for the copolymer.
Claim 3
Dependent Claim
17 words
A process according to claim 1, wherein the kneading machine is a kneader-mixer or an internal mixer.
Claim 4
Dependent Claim
65 words
A process according to claim 1 or 2, wherein the polymerization is carried out in the presence of an excess amount, based on the amount of maleic anhydride or an ester derivative thereof, of the reactant ethylenically unsaturated compound component which is a poor solvent for the copolymer to be formed or in the presence of a poor solvent for the copolymer to be formed.
Claim 5
Dependent Claim
55 words
A process according to claim 3, wherein the excess amount of the reactant ethylenically unsaturated compound component which is a poor solvent for the copolymer to be formed or the amount of the poor solvent for the copolymer to be formed is 20% by weight or more based on the expected amount of the copolymer.
Claim 6
Dependent Claim
56 words
A process according to claim 1, wherein copolymerization of ethylenically unsaturated compound having a terminal double bond and maleic anhydride or an ester derivative thereof which are not miscible is carried out in the presence of 30% by weight, based on the expected amount of the copolymer, or less of a solvent miscible with both reactants.
Claim 7
Dependent Claim
17 words
A process according to claim 2, wherein the kneading machine has a reflux condenser at the top.
Claim 8
Dependent Claim
20 words
A process according to claim 1, wherein the ethylenically unsaturated compound is an alkene having 6 to 12 carbon atoms.
Claim 9
Dependent Claim
27 words
A process according to claim 1, wherein the ethylenically unsaturated compound is at least one member selected from the group consisting of styrene, styrene derivatives and 2,4,4-trimethylpentene-1.
Claim 10
Dependent Claim
26 words
A process according to claim 1 wherein the ester derivative of maleic anhydride is obtained from a monohydric alcohol containing from 1 to 8 carbon atoms.
Claim 11
Dependent Claim
29 words
A process according to claim 1 wherein the molar ratio of the ethylenically unsaturated compound to the maleic anhydride or an ester derivative thereof is from 1.0:1.0 to 10:1.0.
Claim 12
Dependent Claim
35 words
A process according to claim 1 wherein polymerization of the polymerizable reactant mixture as well as the highly viscous resin phase is effected at a temperature ranging from 70° to 120° C. with a catalyst.
Claim 13
Dependent Claim
36 words
A process according to claim 11 wherein powdering of the solid resin aggregates is effected at a temperature that is lower than the softening point, melting point or decomposition point of the copolymer by 10°-50° C.
Claim 14
Dependent Claim
31 words
A process according to claim 1 wherein kneading of the polymerization reaction mixture, the highly viscous reaction phase and the solid resin aggregates is effected within a single batch-type kneading machine.
Claim 15
Dependent Claim
32 words
A process according to claim 1 wherein kneading of the polymerization reactant mixture, the highly viscous resin phase and the solid resin aggregates is effected, successively, in a series of kneading machines.