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US 5,450,728 AGranted
Recovery of volatile organic compounds from gas streams
AssigneeAir Products and Chemicals, Inc.
InventorsJayesh P. Vora, James VanOmmeren
Life of this patent
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Abstract
Volatile organic compounds and water vapor are recovered from a low-boiling gas by compressing the gas to an elevated pressure and cooling the gas in stages to condense volatile components and water while avoiding freezing in the system. Operating the system at an elevated pressure increases condensation efficiency, reduces the number of stages required, and minimizes operating problems to avoid freezing.
Claims12
A method for recovering one or more volatile compounds contained in admixture with one or more low-boiling gases which comprises:
- (a) compressing a gaseous mixture comprising said one or more volatile organic compounds and one or more low-boiling gases to a pressure of at least 30 psia;
- and cooling, partially condensing, and separating the resulting compressed mixture at a first temperature to yield a first vapor and a first condensate stream;
- (b) further cooling said first vapor stream to a second temperature to yield a second stream containing mixed vapor and condensate, and separating the mixed stream into a second vapor and a second condensate stream having a first initial freezing point, said second vapor stream comprising said one or more low-boiling gases having a substantially reduced concentration of said volatile organic compounds;
- and
- (c) cooling said second vapor stream to a third temperature by indirect heat exchange with a first cold recirculating liquid which is cooled in turn by indirect heat exchange with a first stream of vaporizing liquid nitrogen to yield a third mixed stream containing vapor and condensate, and separating the third mixed stream into a third vapor and a third condensate stream having a second initial freezing point, said third vapor stream comprising said one or more low-boiling gases substantially free of residual volatile organic compounds;
- wherein said second temperature is controlled at a temperature above said first initial freezing point of said second condensate stream and said third temperature is controlled at a temperature of -40.degree. to -100.degree. F. which is above said second initial freezing point of said third condensate stream, whereby operation of steps (a), (b), and (c) at a pressure of at least 30 psia allows condensation at higher temperatures than those possible at a pressure below 30 psia, thereby reducing refrigeration requirements for said cooling and the probability of freezing in said second and third condensate streams.
3 more elements
Dependencies are inferred from the claim text.