Polymerization of ethylenically unsaturated monomer with dialkyl pyrocarbonate and hydrogen peroxide

Claim 2

In the process for polymerizing ethylenically unsaturated material susceptible to polymerization with free-radical type initiator, the improvement which comprises conducting said polymerization in the presence of an initiator system comprising, in combination alkaline reagent, hydrogen peroxide, and dialkyl pyrocarbonate representable by the general formula, ##EQU1## wherein R 1 and R 2 are each selected from the group consisting of C 1 - C 20 alkyl and alkenyl, C 6 - C 12 cycloalkyl, C 7 - C 10 aralkyl having a single aromatic ring, and C 6 - C 8 aryl, said pyrocarbonate and hydrogen peroxide being present in the polymerization medium in amounts sufficient to generate an initiating amount of initiator and thereby polymerize the ethylenically unsaturated material.

Claim 3

The process of claim 1 wherein R 1 and R 2 are the same.

Claim 4

The process of claim 2 wherein R 1 and R 2 are each selected from the group consisting of C 1 - C 12 alkyl, C 6 - C 10 cycloalkyl, phenyl and benzyl.

Claim 5

The process of claim 1 wherein R 1 and R 2 are each C 1 - C 8 alkyl.

Claim 6

The process of claim 1 wherein from about 0.001 to about 3 weight percent of dialkyl pyrocarbonate, based on ethylenically unsaturated material, is used and the mole ratio of hydrogen peroxide to dialkyl pyrocarbonate, is from about 0.1:1 to about 10.0:1.

Claim 7

The process of claim 1 wherein the ethylenically unsaturated material is vinyl chloride.

Claim 8

The process of claim 1 wherein the dialkyl pyrocarbonate is diethyl pyrocarbonate.

Claim 9

The process of claim 1 wherein the alkaline reagent is selected from the group consisting of alkali metal and alkaline earth metal carbonates and bicarbonates, and quaternary ammonium hydroxides.

Claim 10

The process of claim 1 wherein the polymerization is conducted in an aqueous medium.

Claim 11

The process of claim 1 wherein the polymerization temperature is from 0°C. to 95°C.

Claim 12

In the process for polymerizing ethylenically unsaturated material susceptible to polymerizatin with free-radical type initiator in an aqueous or bulk polymerization medium, the improvement which comprises conducting said polymerization at between about 20°C. and about 70°C. in the presence of an initiator system comprising, in combination, alkaline reagent, hydrogen peroxide, and dialkyl pyrocarbonate representable by the general formula, ##STR9## wherein R 1 and R 2 are each selected from the group consisting of C 1 - C 12 alkyl, C 6 - C 10 cycloalkyl, phenyl and benzyl, said pyrocarbonate and hydrogen peroxide being present in the polymerization medium in amounts sufficient to generate an initiating amount of initiator and thereby polymerize the ethylenically unsaturated material.

Claim 13

In the process for polymerizing ethylenically unsaturated material susceptible to polymerizatin with free-radical type initiator in an aqueous or bulk polymerization medium, the improvement which comprises conducting said polymerization at between about 20°C. and about 70°C. in the presence of an initiator system comprising, in combination, alkaline reagent, hydrogen peroxide, and dialkyl pyrocarbonate representable by the general formula, ##STR9## wherein R 1 and R 2 are each selected from the group consisting of C 1 - C 12 alkyl, C 6 - C 10 cycloalkyl, phenyl and benzyl, said pyrocarbonate and hydrogen peroxide being present in the polymerization medium in amounts sufficient to generate an initiating amount of initiator and thereby polymerize the ethylenically unsaturated material.

Claim 14

The process of claim 11 wherein from about 0.01 to about 1 weight percent of dialkyl pyrocarbonate, based on ethylenically unsaturated material, is used and the mole ratio of hydrogen peroxide to dialkyl pyrocarbonate is from about 0.1:1 to about 10.0:1.

Claim 15

The process of claim 12 wherein the alkaline reagent is selected from the group consisting of alkali metal and alkaline earth metal carbonates and bicarbonates and quaternary ammonium hydroxides and the amount of alkaline reagent is between about 0.01 and about 10 weight percent, based on the ethylenically unsaturated material.

Claim 16

The process of claim 12 wherein the ethylenically unsaturated material is vinyl chloride.

Claim 17

The process of claim 12 wherein R 1 and R 2 are the same and are methyl, ethyl, n-propyl, isopropyl or butyl radicals.

Claim 18

The process of claim 14 wherein the polymerization is conducted in an aqueous medium.

Claim 19

The process of claim 16 wherein R 1 and R 2 are each C 1 - C 8 alkyl.

Claim 20

The process of claim 17 wherein R 1 and R 2 are the same and are methyl, ethyl, n-propyl, isopropyl or butyl radicals and the alkaline reagent is sodium bicarbonate or quaternary ammonium hydroxide.

Claim 21

The process of claim 1 wherein the polymerization is conducted in an aqueous or bulk polymerization medium.