Tenneco Chemicals, Inc.

Basf Corporation

Robert J Stanaback

Donald Goodman

Robert S Miller

Marvin Koral

Martin L Feldman

Byron G Hays

Michael J Reale

Improved diarylide yellow pigment compositions having high color strength. The compositions are manufactured by modifying tetrazotized 3,3'-dichlorobenzidine with a solution of about 3 to about 5 mole percent of a first acetoacetarylide, followed by coupling into a second acetoacetarylide such as acetoacetanilide.

High color strength diarylide yellow pigment compositions

Vinyl chloride is removed from aqueous slurries prepared by the suspension polymerization of a monomer component that comprises vinyl chloride by heating the slurries at a temperature between 70.degree. C. and the boiling point of water at a pressure in the range of 30 mm Hg absolute to 3 atmospheres and removing the evolved vinyl chloride until the aqueous slurry contains less than 50 ppm and preferably less than 0.1 ppm of vinyl chloride, based on the weight of polymer in the slurry. The polymers that are recovered from the purified aqueous slurries contain less than 10 ppm, and in most cases less than 0.1 ppm of vinyl chloride.

Process for the removal of vinyl chloride from aqueous slurries of vinyl

Vinyl chloride is removed from polyvinyl chloride dispersions, latexes, and slurries by sparging them with an inorganic gas, such as air or ammonia, while they are maintained at subatmospheric pressure.

Process for the removal of vinyl chloride from polyvinyl chloride

Vinyl chloride is removed from polyvinyl chloride dispersions and latexes by adding to them from 2% to 8% by weight of a polar water-soluble organic compound that has a boiling point between about 50.degree. C. and 150.degree. C. and sparging the resulting mixtures with a gas, such as nitrogen, while they are maintained at subatmospheric pressure.

Vinyl chloride is removed from polyvinyl chloride dispersions, latexes, and slurries by sparging them with a gaseous organic compound, such as methane, while they are maintained at subatmospheric pressure.

Vinyl halide polymers of relatively low molecular weight result when a monomer component that comprises a vinyl halide is polymerized in the presence of a free radical generating polymerization initiator and a molecular weight regulating agent that is an alkylene bis-(mercaptoalkanoate), such as ethylene bis-(mercaptoacetate).

Process for the polymerization of vinyl halides in the presence of an

Vinyl halide polymers of relatively low molecular weight are obtained when a monomer component comprising a vinyl halide is polymerized in the presence of a free radical generating polymerization initiator and a molecular weight regulating agent that is a polybromobutene, such as 1,1,2,4-tetrabromobutene-2. The products have low melt viscosity and excellent fusion characteristics that make them valuable in molding, extrusion, and coating applications.

Process for the production of vinyl halide polymers

Flame-retardant resinous compositions comprise an organic polymer and a phosphate that has the structural formula ##STR1## wherein each X represents bromine or chlorine; R represents haloalkyl having 2 to 4 carbon atoms and 1 to 5 bromine and/or chlorine atoms, phenyl, or trihaloneopentyl; and R' represents haloalkyl having 2 to 4 carbon atoms and 1 to 5 bromine and/or chlorine atoms.

Flame-retardant resinous compositions containing trihaloneopentyl

Vinyl chloride is removed from wet cakes that comprise a vinyl chloride polymer, vinyl chloride, and water by contacting the wet cakes with steam, preferably at atmospheric pressure and at a temperature in the range of 100.degree. to 125.degree.C.

Growing community of inventors

Gladstone, NJ, United States of America

Robert J Stanaback