Low molecular weight acrylates or methacrylates

Claim 2

A process for preparing low molecular weight, room temperature liquid acrylate or methacrylate resins from monomers about 20 to 100 weight percent of which are selected from acrylate and methacrylate esters having the general formula: ##STR3## wherein R' is hydrogen or methyl and R" is C 1 -C 8 alkyl or mixtures thereof and about 0 to about 80 weight percent of which are selected from ethylenically unsaturated monomers copolymerizable therewith, which comprises: A. heating to above about 150° C. at least 75 percent, by weight, of a reaction solvent containing an -OH group having a boiling point of above about 150° C. in a batch reactor; B. adding at a temperature of above about 150° C. said monomers and the remaining solvent to the reactor over at least about 30 minutes so that the final polymerization solids of the reaction medium is above at least 30 weight percent; C. maintaining the reaction above about 150° C. for a time sufficient to polymerize said monomers to a monomer to polymer conversion percentage of at least about 85 percent, by weight; and D. stripping off substantially all of the reaction solvent.

Claim 3

The process of claim 1 wherein said monomers are added with a polymerization initiator.

Claim 4

The process of claim 1 wherein the reaction temperature is maintained above about 160° C.

Claim 5

The process of claim 1 wherein the reaction temperature is maintained between about 170° and 215° C.

Claim 6

The process of claim 1 wherein the monomers are added over a period of about 2 to 6 hours.

Claim 7

The process of claim 1 wherein the reaction is carried out at a solids level of about 45 to about 60 percent, by weight.

Claim 8

A process for preparing low molecular weight, room temperature liquid acrylate or methacrylate resins from monomers, about 20 to about 100 weight percent of which are selected from acrylate and methacrylate esters having the general formula: ##STR4## wherein R' is hydrogen or methyl and R" is C 1 -C 8 alkyl or mixtures thereof, and about 0 to about 80 percent, by weight, of which are selected from ethylenically unsaturated monomers copolymerizable therewith, which comprises: A. heating at least 75 percent, by weight, of a reaction solvent which contains at least above 25 percent, by weight, benzyl alcohol to about above 150° C. in a reactor, the remainder of said reaction solvent having a boiling point in excess of about 150° C. B. adding at a temperature above about 150° C. said monomers and the remaining solvent to the reactor over at least about 30 minutes, so that the final polymerization solids is above about 30 weight percent; C. maintaining the reaction above about 150° C. for a time sufficient to polymerize said monomers to a monomer to polymer conversion percentage of at least about 85 percent, by weight; and D. stripping off substantially all of the reaction solvent.

Claim 9

A process for preparing low molecular weight, room temperature liquid acrylate or methacrylate resins from monomers, about 20 to about 100 weight percent of which are selected from acrylate and methacrylate esters having the general formula: ##STR4## wherein R' is hydrogen or methyl and R" is C 1 -C 8 alkyl or mixtures thereof, and about 0 to about 80 percent, by weight, of which are selected from ethylenically unsaturated monomers copolymerizable therewith, which comprises: A. heating at least 75 percent, by weight, of a reaction solvent which contains at least above 25 percent, by weight, benzyl alcohol to about above 150° C. in a reactor, the remainder of said reaction solvent having a boiling point in excess of about 150° C. B. adding at a temperature above about 150° C. said monomers and the remaining solvent to the reactor over at least about 30 minutes, so that the final polymerization solids is above about 30 weight percent; C. maintaining the reaction above about 150° C. for a time sufficient to polymerize said monomers to a monomer to polymer conversion percentage of at least about 85 percent, by weight; and D. stripping off substantially all of the reaction solvent.

Claim 10

The process of claim 7 wherein the reaction solvent comprises 100 percent, by weight, benzyl alcohol.

Claim 11

The process of claim 7 wherein the reaction temperature is maintained above about 160° C.

Claim 12

The process of claim 7 wherein the reaction temperature is maintained between about 170° and 215° C.

Claim 13

The process of claim 7 wherein the monomers are added over a period of about 2 to 6 hours.

Claim 14

The process of claim 7 wherein the reaction is carried out at a solids level of between about 45 and about 60 weight percent.