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US 4,376,640 AGranted
Repressurization of pressure swing adsorption system
AssigneeCalgon Corporation
InventorToan P. Vo
Life of this patent
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Abstract
Gaseous mixtures are separated on a two adsorption zone carbon molecular sieve pressure swing adsorption system each zone consisting of either one or two adsorption columns. This process includes the pressurization of an adsorption zone with lean gas in the range of 70 to 120 percent of the adsorption pressure.
Claims5
An adsorption process for producing an enriched gas stream of a predetermined purity which comprises the sequential steps of:
- (a) passing a gaseous mixture, at an adsorption pressure selected from the range of from 3.0 to 8.0 bars through a first adsorption zone comprising one column of carbon molecular sieves to yield enriched gas passing said enriched gas to a product reservoir;
- (b) when said enriched gas declines in purity by from 1 to 10 percent below said predetermined purity, thereby becoming lean gas, passing said lean gas from the outlet end of said first adsorption zone into the inlet end of a second adsorption zone comprising one column of carbon molecular sieves, to pressurize said second adsorption zone in the range of about 70 to 120% of said adsorption pressure, thereafter halting said lean gas flow and isolating said first adsorption zone;
- (c) allowing said second adsorption zone to decrease in pressure via a time delay process while concomitantly venting said isolated first adsorption zone to the atmosphere through its inlet end;
- (d) thereafter passing said gaseous mixture through said pressurized second adsorption zone at the adsorption pressure to yield enriched gas while regenerating said isolated and vented first adsorption zone by application of vacuum to the inlet end of said first zone in the range of from 70 to 250 torr;
- (e) repeating the cycle, treating said second zone as said first zone when the enriched gas quality declines in purity by from 1 to 10 percent below said predetermined purity.
2 more elements
An adsorption process for producing an enriched gas stream of a predetermined purity which comprises the sequential steps of:
- (a) passing a gaseous mixture, at an adsorption pressure selected from the range of from 3.0 to 8.0 bars through a first adsorption zone comprising a first and a last column of carbon molecular sieves arranged in series to yield said enriched gas;
- (b) when the enriched gas declines in purity by from 1 to 10 percent below said predetermined purity, passing the gaseous mixture solely through the last column of said first adsorption zone, thereby producing lean gas and passing said lean gas from the outlet end of said first adsorption zone into the inlet end of a second adsorption zone comprising a first and a last column of carbon molecular sieves arranged in series, to pressurize said second adsorption zone in the range of about 70 to 120% of said adsorption pressure, halting said lean gas flow and thereafter isolating said first adsorption column of said first adsorption zone;
- (c) allowing said second adsorption zone to decrease in pressure via a time delay process while concomitantly venting said first column of said first adsorption zone to atmospheric pressure through its inlet end, and countercurrently venting said last column of said first adsorption zone and using said vented gas to countercurrently purge the previously vented and isolated first column in said first adsorption zone;
- (d) thereafter passing said gaseous mixture through said second adsorption zone at the adsorption pressure to yield enriched gas while regenerating said first adsorption zone by application of vacuum to the inlet end of said first zone in the range of 70 to 250 torr;
- (e) repeating the cycle, treating said second zone as said first zone when the enriched gas purity declines by from 1 to 10 percent below said predetermined purity.
2 more elements
Dependencies are inferred from the claim text.