Claims Analysis
Total Claims: 12
Claim 1
Independent Claim
177 words
A process for the free-radical polymerization of vinyl monomers, including vinyl aromatic monomers, comprises polymerizing said vinyl monomers in at least two thermally distinct polymerization stages, each between the temperatures of about 70° C. and 150° C. in the presence of at least two free-radical initiators, one of which initiators is particularly effective at the lowest temperature stage and has the formula ##STR3## and where R is an alkylene, alkynylene or alkenylene diradical, R 1 is alkyl, alkenyl, alkynl or alkoxy and R 2 is lower alkyl and R 3 is hydrogen or lower alkyl and a second of which initiators have a 10 hour half-life temperature of at least about 80° C., said temperature being at least about 15° C. above the 10 hour half-life temperature of the compound of Formula (I) wherein the same solvent is used for measuring the half-life of all initiators, wherein the initiator of Formula (I) allows completing the polymerization in a shorter time with the resulting polymer having a higher viscosity-average molecular weight than without the initiator of Formula (I).
Claim 2
Dependent Claim
177 words
A process for the free-radical polymerization of vinyl monomers, including vinyl aromatic monomers, comprises polymerizing said vinyl monomers in at least two thermally distinct polymerization stages, each between the temperatures of about 70° C. and 150° C. in the presence of at least two free-radical initiators, one of which initiators is particularly effective at the lowest temperature stage and has the formula ##STR3## and where R is an alkylene, alkynylene or alkenylene diradical, R 1 is alkyl, alkenyl, alkynl or alkoxy and R 2 is lower alkyl and R 3 is hydrogen or lower alkyl and a second of which initiators have a 10 hour half-life temperature of at least about 80° C., said temperature being at least about 15° C. above the 10 hour half-life temperature of the compound of Formula (I) wherein the same solvent is used for measuring the half-life of all initiators, wherein the initiator of Formula (I) allows completing the polymerization in a shorter time with the resulting polymer having a higher viscosity-average molecular weight than without the initiator of Formula (I).
Claim 3
Dependent Claim
14 words
The process of claim 1 wherein the vinyl monomer is a vinyl aromatic monomer.
Claim 4
Dependent Claim
12 words
The process of claim 2 wherein the vinyl aromatic monomer is styrene.
Claim 5
Dependent Claim
13 words
The process of claim 3 wherein the initiator of formula (I) is 2,5-dimethyl-2,5-bis[2-ethylhexanoylperoxy]hexane.
Claim 6
Dependent Claim
11 words
The process of claim 4 wherein said second initiator is 2,5-dimethyl-2,5-bis[benzoylperoxy]hexane.
Claim 7
Dependent Claim
17 words
The process of claim 4 wherein said second initiator is a mixture of 2,5-dimethyl-2,5-bis[benzoylperoxy]hexane and di-t-butyl diperoxycarbonate.
Claim 8
Dependent Claim
18 words
The process of claim 4 wherein said second initiator is a mixture of 1,1-bis(t-butylperoxy)cyclohexane and tertiary butyl perbenzoate.
Claim 9
Dependent Claim
16 words
The process of claim 4 wherein said second initiator is a mixture of 2,5-dimethyl-2,5-bis[benzoylperoxy]hexane and ethyl(3,3-bis(t-butylperoxy)butyrate.
Claim 10
Dependent Claim
15 words
The process of claim 4 wherein said initiators are used in a bulk polymerization technique.
Claim 11
Dependent Claim
15 words
The process of claim 4 wherein said initiators are used in a suspension polymerization technique.
Claim 12
Dependent Claim
19 words
The process of claim 4 wherein the polymerization stages are between the temperatures of 90° C. and 130° C.