Method of polymerizing rosin

Claim 2

The polymerization of a rosin in the presence of a catalytic proportion of an insoluble catalyst which comprises a polymer having pendant organosulfonic acid groups.

Claim 3

The polymerization of claim 1 wherein the catalyst contains recurring groups selected from those of the formulae: ##STR8## wherein n is 0, 1 or 2; R is selected from the group consisting of fluorine and perfluoroalkyl radicals having from 1 to 10 carbon atoms; and X is selected from the group consisting of: [O(CF 2 ) m ], [OCF 2 CFY] and [OCFYCF 2 ] where m is an integer of from 2 to 10 and Y is selected from the group consisting of fluorine and trifluoromethyl.

Claim 4

The polymerization of claim 1 wherein said catalyst has the general formula: ##STR9## wherein n equals 1 or 2; a is an integer of from 5 to 13.5 and the ratio of a over b varies from about 2 to about 50; and b is such that the polymer has a molecular weight of circa 1000.

Claim 5

The polymerization of claim 1 wherein said catalyst has the general formula: ##STR10## wherein n is 0, 1 or 2; the ratio of a over b varies from about 2 to about 50 and b is such that the polymer has a molecular weight of circa 1000.

Claim 6

The polymerization of claim 1, wherein said catalyst has the general formula: ##STR11##

Claim 7

The polymerization of claim 1 wherein said catalyst has the general formula: ##STR12## wherein n is an integer of at least 1.

Claim 8

The polymerization of claim 1 wherein the catalyst is a sulfonated styrene-divinylbenzene copolymer.

Claim 9

The polymerization of claim 1 wherein the rosin is selected from the group consisting of tall oil rosin, wood rosin and gum rosin.

Claim 10

The polymerization of claim 8 wherein the rosin is tall oil rosin.

Claim 11

The polymerization of claim 8 wherein the rosin is wood rosin.

Claim 12

The polymerization of claim 8 wherein the rosin is gum rosin.

Claim 13

The polymerization of claim 1 wherein the catalytic proportion is from about 0.01 to about 20 percent by weight of the rosin.

Claim 14

The polymerization of claim 12 wherein the proportion is about 20 percent.

Claim 15

The polymerization of claim 1 wherein the polymerization is carried out in an inert solvent.

Claim 16

The polymerization of claim 1 carried out in a cyclic terpene solvent.

Claim 17

The polymerization of claim 1 wherein the catalyst is supported on an inert porous carrier having an average pore diameter of between about 50 Å and about 600 Å in a weight ratio of catalyst to support of between about 0.1:100 and about 20:100.

Claim 18

The polymerization of claim 16 wherein said carrier is selected from the group consisting of alumina, silica, silica-alumina and porous glass.

Claim 19

The polymerization of claim 1 carried out at a temperature of from about 60° C. to about 180° C.

Claim 20

The polymerization of claim 1 wherein the catalyst is present in a continuous reactor zone and the rosin is passed continuously into said zone while product polymer is passed continuously from said zone.