초록 ▼

A method for operating a pressure swing adsorption process at turndown conditions by adding selected steps to the normal design operation of the process. The selected steps include the extension of a make product/no feed step and the addition of idle steps at specific points in the process cycle dur

A method for operating a pressure swing adsorption process at turndown conditions by adding selected steps to the normal design operation of the process. The selected steps include the extension of a make product/no feed step and the addition of idle steps at specific points in the process cycle during depressurization and repressurization. The average volumetric flow ratio of the pressurized feed gas to the final product gas during design operation and during turndown operation may be essentially equal. The average oxygen concentration in the final product gas during design operation and during turndown operation also may be essentially equal.

대표청구항 ▼

A method for operating a pressure swing adsorption process at turndown conditions by adding selected steps to the normal design operation of the process. The selected steps include the extension of a make product/no feed step and the addition of idle steps at specific points in the process cycle dur

A method for operating a pressure swing adsorption process at turndown conditions by adding selected steps to the normal design operation of the process. The selected steps include the extension of a make product/no feed step and the addition of idle steps at specific points in the process cycle during depressurization and repressurization. The average volumetric flow ratio of the pressurized feed gas to the final product gas during design operation and during turndown operation may be essentially equal. The average oxygen concentration in the final product gas during design operation and during turndown operation also may be essentially equal. a second gas stream from the bed until the pressure therein reaches a second intermediate pressure and utilizing at least a portion of the second gas stream to pressurize yet another bed; and (3c) evacuating the bed from the feed end using a vacuum blower until the pressure therein reaches the minimum bed pressure. 6. The process of claim 5 wherein the first idle period follows step (3b). 7. The process of claim 5 which further comprises purging the bed following the evacuation step (3c) by introducing a purge gas into the product end of the bed while continuing to evacuate gas from the feed end of the bed. 8. The process of claim 7 wherein the purge gas is provided to the bed by a first gas stream withdrawn from another bed which is in step (3a). 9. The process of claim 5 which further comprises evacuating the bed from the feed end while withdrawing the second gas stream from the product end of the bed during step (3b). 10. The process of claim 9 wherein the first idle period follows step (3b). 11. The process of claim 5 wherein the repressurizing of the bed in step (4) is accomplished by (4a) introducing repressurizing gas into the adsorber bed wherein a portion of the repressurizing gas is provided by a second gas stream withdrawn from another bed which is in step (3b); and (4b) introducing repressurizing gas into the adsorber bed wherein a portion of the repressurizing gas is provided by pressurized feed gas from a feed gas compressor. 12. The process of claim 11 wherein the second idle period follows step (4a). 13. The process of claim 11 wherein the modified idle period follows step (4a). 14. The process of claim 11 wherein the pressurized feed gas is air, the more strongly adsorbable component is nitrogen, the less strongly adsorbable component is oxygen, and the final product gas is enriched in oxygen. 15. The process of claim 14 wherein a portion of the repressurization gas in step (4a) is provided by allowing atmospheric air to flow into the adsorber bed when the pressure in the bed is initially below atmospheric pressure. 16. The process of claim 14 wherein a portion of the repressurization gas in step (4b) is provided by allowing atmospheric air to flow into the adsorber bed when the pressure in the bed is initially below atmospheric pressure. 17. The process of claim 14 wherein the vacuum blower has an inlet which is in flow communication with atmospheric air during step (4a). 18. The process of claim 17 wherein the feed gas compressor discharges to the atmosphere during step (4a). 19. A pressure swing adsorption process for the separation of a pressurized feed gas containing at least one more strongly adsorbable component and at least one less strongly adsorbable component which comprises (a) during a period of design product gas flow, the steps of (1) introducing the pressurized feed gas into a feed end of an adsorber bed containing one or more solid adsorbents which preferentially adsorbs the more strongly adsorbable component and withdrawing from a product end of the adsorber bed a first adsorber effluent gas enriched in the less strongly adsorbable component, wherein the first adsorber effluent gas is utilized as a final product gas, wherein the adsorber bed is one of a plurality of adsorber beds; (2) terminating the introduction of the pressurized feed gas into the adsorber bed while withdrawing from the product end of the adsorber bed a second adsorber effluent gas enriched in the less strongly adsorbable component, wherein the pressure in the adsorber bed decreases while the second adsorber effluent gas is withdrawn therefrom, and wherein the second adsorber effluent gas is utilized as a final product gas; (3) depressurizing the adsorber bed to a minimum bed pressure by withdrawing additional gas therefrom, wherein the depressurizing of the adsorber bed is accomplished by (3a) withdrawing a first gas stream from the bed until the pressure therein reaches a first intermediate pressure and utilizing at least a portion of the first gas stream to purge another bed; (3b) withdrawing a second gas stream from the bed until the pressure therein reaches a second intermediate pressure and utilizing at least a portion of the second gas stream to pressurize yet another bed; and (3c) evacuating the bed from the feed end until the pressure therein reaches the minimum bed pressure; (4) purging the bed following the evacuation of step (3c) by introducing a purge gas into the product end of the bed while continuing to evacuate gas from the feed end of the bed, wherein the purge gas is provided to the bed by a first gas stream withdrawn from another bed in step (3a); (5) repressurizing the adsorber bed by introducing a second gas stream withdrawn from another bed which is in step (3b); (6) further repressurizing the adsorber bed by introducing pressurized feed gas into the bed; and (7) repeating steps (1) through (6) in a cyclic manner; and (b) during a period of reduced product gas flow, utilizing steps (1) through (5) in modified form wherein the duration of step (2) is extended, a first idle period introduced into step (3), and a second idle period or a modified idle period is inserted into step (4). 20. The process of claim 19 wherein the pressurized feed gas is air, the more strongly adsorbable component is nitrogen, the less strongly adsorbable component is oxygen, and the final product gas is enriched in oxygen. 21. The process of claim 20 which further comprises, following step (5) and prior to step (6), allowing atmospheric air to flow into the adsorber bed when the pressure in the bed is initially below atmospheric pressure. 22. The process of claim 19 which further comprises evacuating the bed from the feed end while withdrawing the second gas stream from the product end of the bed during step (3b). 23. The process of claim 19 wherein the average volumetric flow ratio of the pressurized feed gas to the final product gas during (a) is essentially equal to the average volumetric flow ratio of the pressurized feed gas to the final product gas during (b). 24. The method of claim 19 wherein the more strongly adsorbed component is nitrogen and the less strongly adsorbed component is oxygen, and wherein the average oxygen concentration in the final product gas during (a) is essentially equal to the average oxygen concentration in the final product gas during (b).