US4229569A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Process for the removal of vinyl chloride from aqueous slurries of vinyl chloride polymers
Assignee: Occidental Chemical Corp
•
Filing: 1979-02-05
•
Granted: 1980-10-21
•
Expires: 1999-02-05
Abstract
Abstract 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 DEG 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.
Inventors
- 👤 Martin L. Feldman
- 👤 Donald Goodman
- 👤 Marvin Koral
- 👤 Robert S. Miller
- 👤 Robert J. Stanaback
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-30 02:33
CPC Classifications
C; C08; C08F; C08F6/00; C08F6/001; C08F6/003
Claims Analysis
Total Claims: 6
Claim 1
Independent Claim
163 words
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° 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.
Claim 2
Dependent Claim
163 words
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° 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.
Claim 3
Dependent Claim
64 words
The process of claim 1 wherein the aqueous slurry is heated at a temperature between 80° C. and 100° C. at a pressure in the range of 400 mm Hg absolute to atmospheric pressure while the vinyl chloride vapor that is evolved is removed until the slurry contains less than 0.1 ppm of vinyl chloride, based on the weight of polymer in the slurry.
Claim 4
Dependent Claim
179 words
The process for the production of vinyl chloride polymers that contain less than 0.1 ppm of vinyl chloride that comprises the steps of (a) heating 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 ppm to 15,000 ppm of vinyl chloride, and not more than 0.1% by weight of surfactant, at a temperature between 70° 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, and (b) recovering from said aqueous slurry a vinyl chloride polymer that contains less than 0.1 ppm of vinyl chloride.
Claim 5
Dependent Claim
179 words
The process for the production of vinyl chloride polymers that contain less than 0.1 ppm of vinyl chloride that comprises the steps of (a) heating 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 ppm to 15,000 ppm of vinyl chloride, and not more than 0.1% by weight of surfactant, at a temperature between 70° 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, and (b) recovering from said aqueous slurry a vinyl chloride polymer that contains less than 0.1 ppm of vinyl chloride.
Claim 6
Dependent Claim
37 words
The process of claim 3 wherein in Step (a) the aqueous slurry is heated at a temperature between 80° C. and 100° C. at a pressure in the range of 400 mm Hg absolute to atmospheric pressure.
References Cited (Backward Citations)
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1983-10-21 | 1984-04-21 | 1984-10-21 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1987-10-21 | 1988-04-21 | 1988-10-21 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1991-10-21 | 1992-04-21 | 1992-10-21 | $7700.00 | Window Closed / Lapsed |