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AssigneeTenneco Chemicals, Inc.
InventorsMartin L. Feldman, Donald Goodman, Marvin Koral, Robert S. Miller, Robert J. Stanaback
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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.
The process for removal of vinyl chloride from an aqueous slurry prepared by the suspension polymerization of a monomer component selected from the group consisting of vinyl chloride and mixtures of vinyl chloride with up to 35% by weight of at least one monomer copolymerizable therewith, said slurry containing from 5% to 50% by weight of vinyl chloride polymer particles ranging in size from about 25 microns to 500 microns, from 1000 parts to 15,000 parts by weight of vinyl chloride per million parts by weight of polymer in the slurry, and not more than 0.1% by weight of surfactant, that comprises the steps of heating said aqueous slurry at a temperature between 70.degree. C. and the boiling point of water at a pressure in the range of 300 mm Hg absolute to 3 atmospheres and removing the vinyl chloride that is evolved until the slurry contains less than 0.1 ppm of vinyl chloride, based on the weight of polymer in the slurry.
The process for the production of vinyl chloride polymers that contain less than 0.1 ppm of vinyl chloride that comprises the steps of
Dependencies are inferred from the claim text.