Process for preparing diene-containing rubbers having improved green strength

Claim 2

A process for preparing a diene-containing synthetic rubber, via emulsion polymerization, having improved green strength wherein the improvement comprises: forming a copolymer of a conjugated diene monomer, having from about four to about 20 carbon atoms, and a vinyl monomer selected from the group consisting of monovinyl aromatic compounds having from eight to about 20 carbon atoms and acrylic compounds having from three to about five carbon atoms, in the presence of an N-(alkoxymethyl)acrylamide monomer having the formula ##STR2## where R is selected from the group consisting of straight and branched alkyl chains having from 1 to about 20 carbon atoms, said monomers being polymerized at a temperature of from about 0° C. to about 30° C., to form a synthetic rubber wherein from about 0.5 to about 10 percent by weight thereof is derived from said N-(alkoxymethyl)acrylamide; from about 10 to about 90 percent by weight thereof is derived from said conjugated diene monomer and from about 1 to about 10 percent by weight thereof is derived from said monomer containing a vinyl group.

Claim 3

A process, as set forth in claim 1, wherein the polymerization of said conjugated diene, vinyl and N-(alkoxymethyl)acrylamide monomers is conducted for a period of time of from about 12 to about 16 hours.

Claim 4

A process, as set forth in claim 2, wherein said N-(alkoxymethol)acrylamide monomer is N-(isobutoxymethyl)acrylamide; said diene monomer is butadiene; and said vinyl monomer is styrene.

Claim 5

An emulsion polymerization process for preparing a diene-containing synthetic rubber having improved green strength comprising the steps of: charging a reaction vessel with water, an emulsifier, an initiator, an N-(alkoxymethyl)acrylamide monomer and a monomer containing a vinyl group; purging said vessel with an inert gas; charging a conjugated diene monomer and an activator to said vessel; polymerizing said monomers at a temperature of from about 0° C. to about 30° C. to form a copolymer wherein from about 0.5 to about 10 percent by weight thereof is derived from said N-(alkoxymethyl)acrylamide monomer, from about 10 to about 90 percent by weight thereof is derived from said diene monomer and from about 1 to about 90 percent by weight thereof is derived from said monomer containing a vinyl group; and, thereafter extracting said copolymer from said vessel and any unreacted monomers; wherein said N-(alkoxymethyl)acrylamide monomer has the formula ##STR3## where R is selected from the group consisting of straight and branched alkyl chains having from 1 to about 20 carbon atoms; said conjugated diene monomer has from about four to about 20 carbon atoms; said monomer containing a vinyl group is selected from the group consisting of monovinyl aromatic compounds having from eight to about 20 carbon atoms and acrylic compounds having from three to about five carbon atoms; said emulsifier is selected from the group consisting of sodium lauryl sulfate, long chain metal sulfonates and rosin acid salts; said initiator is selected from the group consisting of free radical peroxides and peroxydicarbonates; and, said activator is selected from the group consisting of tetraethylenepentamine, ferrous sulfate heptahydrate, alkyl amines having primary and secondary amines and sodium formaldehyde sulfoxylate.

Claim 6

An emulsion polymerization process for preparing a diene-containing synthetic rubber having improved green strength comprising the steps of: charging a reaction vessel with water, an emulsifier, an initiator, an N-(alkoxymethyl)acrylamide monomer and a monomer containing a vinyl group; purging said vessel with an inert gas; charging a conjugated diene monomer and an activator to said vessel; polymerizing said monomers at a temperature of from about 0° C. to about 30° C. to form a copolymer wherein from about 0.5 to about 10 percent by weight thereof is derived from said N-(alkoxymethyl)acrylamide monomer, from about 10 to about 90 percent by weight thereof is derived from said diene monomer and from about 1 to about 90 percent by weight thereof is derived from said monomer containing a vinyl group; and, thereafter extracting said copolymer from said vessel and any unreacted monomers; wherein said N-(alkoxymethyl)acrylamide monomer has the formula ##STR3## where R is selected from the group consisting of straight and branched alkyl chains having from 1 to about 20 carbon atoms; said conjugated diene monomer has from about four to about 20 carbon atoms; said monomer containing a vinyl group is selected from the group consisting of monovinyl aromatic compounds having from eight to about 20 carbon atoms and acrylic compounds having from three to about five carbon atoms; said emulsifier is selected from the group consisting of sodium lauryl sulfate, long chain metal sulfonates and rosin acid salts; said initiator is selected from the group consisting of free radical peroxides and peroxydicarbonates; and, said activator is selected from the group consisting of tetraethylenepentamine, ferrous sulfate heptahydrate, alkyl amines having primary and secondary amines and sodium formaldehyde sulfoxylate.

Claim 7

A process, as set forth in claim 1, wherein said emulsifier comprises sodium lauryl sulfate; said initiator comprises diisopropylbenzene hydroperoxide and said activator comprises tetraethylenepentamine.

Claim 8

A process, as set forth in claim 4, wherein said step of polymerizing is conducted for a period of time of from about 12 to about 16 hours.

Claim 9

A process, as set forth in claim 4, wherein said N-(alkoxymethyl)acrylamide monomer is N-(isobutoxymethyl)acrylamide; said diene monomer is butadiene; and said monomer containing a vinyl group is styrene.