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US3984218A Expired / Lapsed US ⏱️ 0.0 years remaining

Process for the removal of vinyl chloride from gas streams

Assignee: Occidental Chemical Corp
•
Filing: 1976-03-05
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Granted: 1976-10-05
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Expires: 1996-03-05
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Abstract

Abstract Vinyl chloride is removed from gas streams that contain from 10 ppm to 100 mole percent of vinyl chloride by passing the gas stream through a bed of coconut shell-derived or petroleum-derived activated carbon. The exit gas stream contains less than 5 ppm of vinyl chloride.

Inventors

  • 👤 Piyush J. Patel
  • 👤 Clay G. Thompson
  • 👤 Edward J. Hourihan
  • 👤 Carl S. Stutts

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-30 11:06
CPC Classifications
B; B01; B01D; B01D53/00; B01D53/34; B01D53/46; B01D53/72; B01D53/68; B01D53/70; Y; Y10; Y10S; Y10S95/00; Y10S95/90; Y10S95/901

Claims Analysis

Total Claims: 9
Claim 1
Independent Claim 253 words
In the process for the removal of vinyl chloride from gas streams wherein the gas streams are contacted with activated carbon until the surface of the carbon is saturated with vinyl chloride, vinyl chloride is desorbed from the carbon, and the carbon is regenerated and recycled, the improvements that consist essentially of the steps of a. passing a gas stream that contains from 10 ppm to 100 mole percent of vinyl chloride through a bed of activated carbon, said carbon being selected from the group consisting of coconut shell-derived activated carbon and petroleum-derived activated carbon and having an iodine number of at least 1100 milligrams per gram and a total surface area of at least 1150 square meters per gram, until the gas stream leaving the bed of vinyl chloride-saturated carbon contains more than 10 ppm of vinyl chloride; b. passing steam at 100°C. to 150°C. through the bed of vinyl chloride-saturated activated carbon until at least 99% by weight of the vinyl chloride has been desorbed from the carbon and the carbon is saturated with water; c. directing the steam leaving the carbon bed to a vinyl chloride recovery system; d. passing a stream of inert gas at 90° to 150°C. through the bed of water-saturated activated carbon until the hot carbon contains less than 1% of water; e. passing a stream of inert gas at a temperature below 30°C. through the hot carbon until the carbon has been cooled to a temperature below 30°C.; and f. repeating Steps (a) to (e).
Claim 2
Dependent Claim 253 words
In the process for the removal of vinyl chloride from gas streams wherein the gas streams are contacted with activated carbon until the surface of the carbon is saturated with vinyl chloride, vinyl chloride is desorbed from the carbon, and the carbon is regenerated and recycled, the improvements that consist essentially of the steps of a. passing a gas stream that contains from 10 ppm to 100 mole percent of vinyl chloride through a bed of activated carbon, said carbon being selected from the group consisting of coconut shell-derived activated carbon and petroleum-derived activated carbon and having an iodine number of at least 1100 milligrams per gram and a total surface area of at least 1150 square meters per gram, until the gas stream leaving the bed of vinyl chloride-saturated carbon contains more than 10 ppm of vinyl chloride; b. passing steam at 100°C. to 150°C. through the bed of vinyl chloride-saturated activated carbon until at least 99% by weight of the vinyl chloride has been desorbed from the carbon and the carbon is saturated with water; c. directing the steam leaving the carbon bed to a vinyl chloride recovery system; d. passing a stream of inert gas at 90° to 150°C. through the bed of water-saturated activated carbon until the hot carbon contains less than 1% of water; e. passing a stream of inert gas at a temperature below 30°C. through the hot carbon until the carbon has been cooled to a temperature below 30°C.; and f. repeating Steps (a) to (e).
Claim 3
Dependent Claim 31 words
The process of claim 1 wherein the activated carbon that is used in Step (a) is a coconut shell-derived activated carbon that has an iodine number of at least 1200 mg./g.
Claim 4
Dependent Claim 20 words
The process of claim 1 wherein the activated carbon that is used in Step (a) is a petroleum-derived activated carbon.
Claim 5
Dependent Claim 22 words
The process of claim 1 wherein the Step (b) steam at 115°-130°C. is passed through the bed of vinyl chloride-saturated activated carbon.
Claim 6
Dependent Claim 15 words
The process of claim 1 wherein the inert gas used in Step (d) is nitrogen.
Claim 7
Dependent Claim 23 words
The process of claim 1 wherein in Step (d) nitrogen at 120° to 140°C. is passed through the bed of water-saturated activated carbon.
Claim 8
Dependent Claim 15 words
The process of claim 1 wherein the inert gas used in Step (e) is nitrogen.
Claim 9
Dependent Claim 22 words
The process of claim 1 wherein in Step (e) nitrogen at a temperature below 20°C. is used to cool the hot carbon.

References Cited (Backward Citations)

CA487833A Cited
US1619326A Cited
US1619327A Cited
US1616073A Cited
US2933454A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1979-10-05 1980-04-05 1980-10-05 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1983-10-05 1984-04-05 1984-10-05 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1987-10-05 1988-04-05 1988-10-05 $7700.00 Window Closed / Lapsed

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