Adsorptive process for selective separation of gases

Claim 2

In a pressure swing process for fractionating at least one component from a gaseous mixture by selective adsorption in each of at least two adsorption zones by sequentially passing the gaseous mixture from a feed stream through a first adsorption zone until low purity product gas is obtained while simultaneously purging and then pressurizing a second adsorption zone and then through the second adsorption zone until low purity product gas is obtained while simultaneously purging and then pressurizing the first adsorption zone, the improvement comprising selectively collecting product quality gas and low purity gas which is not of product quality in a segregated storage adsorption zone; selectively passing the product quality gas collected in the segregated storage adsorption zone from one end of the segregated storage adsorption zone as countercurrent purge gas to at least contribute to the purge gas used to remove components adsorbed in the beds of the adsorption zones; and selectively diverting the low purity gas collected in the segregated storage adsorption zone from the other end of the segregated storage adsorption zone as repressurizing gas to an adsorption zone after said adsorption zone has been purged with a countercurrent flow of purge gas at least part of which was contributed by gas from the segregated storage adsorption zone to at least contribute to the repressurization of that particular adsorption zone, said segregated storage adsorption zone never being exposed directly to the feed gas stream during the fractionation cycles.

Claim 3

The process of claim 1 further comprising selectively passing the product quality gas collected in the segregated storage adsorption zone as product gas to contribute to a continuous flow of product gas when the adsorption zones do not provide product gas.

Claim 4

The pressure swing process of claim 1 further comprising passing the gaseous mixture through a plurality of first adsorption zones.

Claim 5

The pressure swing process of claim 1 further comprising passing the gaseous mixture through a plurality of second adsorption zones.

Claim 6

The pressure swing process of claim 1 further comprising collecting product gas in a plurality of segregated storage adsorption zones.

Claim 7

A process for continuously fractionating at least one component from a gaseous mixture by selective adsorption in each of at least two adsorption zones in a high pressure product cycle comprising the steps of: a. providing a first adsorption bed having a gas inlet and a gas outlet, at least one additional adsorption bed having a gas inlet and a gas outlet, the gas inlets of said first and at least one additional adsorption beds being connected to a feed gas stream, at least one segregated storage adsorption bed having two inlet-outlet pipes the at least one segregated storage adsorption bed being isolated from direct communication with the feed gas stream, the first inlet-outlet communicating with the gas inlets and gas outlets of said first and at least one additional adsorption beds and the second inlet-outlet communicating with the gas outlet of said first and at least one additional adsorption beds and a product outlet, the product outlet also communicating with the outlet of the first and at least one additional beds, a waste outlet communicating with the inlet of said first and at least one additional adsorption beds, and associated valves to isolate each of said adsorption beds; b. simultaneously introducing the gaseous mixture into the gas inlet of the first adsorption bed from the feed gas stream, allowing the gaseous mixture to pass through the first adsorption bed, releasing product gas from the outlet of the first adsorption bed, and discharging the product gas from the product outlet; c. simultaneously with step (b) collecting product gas in the segregated storage adsorption bed through one of the inlet-outlet pipes thereof while partially depressurizing the at least one additional adsorption bed from the outlet thereof into the other inlet-outlet pipe of the segregated storage adsorption bed, until the gas flowing from the at least one additional adsorption bed into the segregated storage adsorption bed is depleted of any product value; d. terminating the depressurizing of step (c) from the outlet end of the at least one additional adsorption bed and then continuing depressurizing thereof from the inlet end thereof to the waste outlet while continuing adsorption of the feed gas mixture in the first adsorption bed, discharging the product gas from the product outlet and collecting product gas in the segregated storage adsorption bed; e. continuing to discharge product gas from the product outlet and diverting product gas from the outlet of the first adsorption bed and from the product gas collected in the segregated storage adsorption bed to the outlet end of the at least one additional adsorption bed, passing said diverted product gas through the adsorption bed thereof to purge waste gas from the bed to the waste outlet; f. continuing to discharge product gas from the product outlet, terminating the flow of diverted product gas to the at least one additional adsorption bed, terminating the discharge of purge gas from the waste outlet, and equalizing the pressures of the segregated storage adsorption bed and the at least one additional adsorption bed by passing gas collected in the segregated storage adsorption bed in step (c) by the partial depressurizing of the at least on additional adsorption bed from the one inlet-outlet pipe of the segregated storage adsorption bed to the gas inlet of the at least one additional adsorption bed while passing product gas into the other inlet-outlet pipe of the segregated storage adsorption bed, thereby initiating repressurization of the at least one additional adsorption bed with a gas of greater product quality than the feed gaseous mixture; g. terminating the initial repressurization of step (f), isolating the segregated storage adsorption bed, and completely repressurizing the at least one additional adsorption bed with product gas diverted from the outlet of the first adsorption bed whereby the at least one additional adsorption bed is prepared for the fractionation of at least one component from a gaseous mixture by selective adsorption, while continuing to discharge product gas from the product outlet; and h. thereafter consecutively repeating steps (b) through (g) reversing the functions of the first adsorption bed and the at least one additional bed, wherein the gaseous mixture to be fractionated is introduced into and product gas is discharged from the at least one additional adsorption bed and the first adsorption bed is depressurized, purged and pressurized for repeating steps (a) through (h).

Claim 8

A process for continuously fractionating at least one component from a gaseous mixture by selective adsorption in each of at least two adsorption zones in a high pressure product cycle comprising the steps of: a. providing a first adsorption bed having a gas inlet and a gas outlet, at least one additional adsorption bed having a gas inlet and a gas outlet, the gas inlets of said first and at least one additional adsorption beds being connected to a feed gas stream, at least one segregated storage adsorption bed having two inlet-outlet pipes the at least one segregated storage adsorption bed being isolated from direct communication with the feed gas stream, the first inlet-outlet communicating with the gas inlets and gas outlets of said first and at least one additional adsorption beds and the second inlet-outlet communicating with the gas outlet of said first and at least one additional adsorption beds and a product outlet, the product outlet also communicating with the outlet of the first and at least one additional beds, a waste outlet communicating with the inlet of said first and at least one additional adsorption beds, and associated valves to isolate each of said adsorption beds; b. simultaneously introducing the gaseous mixture into the gas inlet of the first adsorption bed from the feed gas stream, allowing the gaseous mixture to pass through the first adsorption bed, releasing product gas from the outlet of the first adsorption bed, and discharging the product gas from the product outlet; c. simultaneously with step (b) collecting product gas in the segregated storage adsorption bed through one of the inlet-outlet pipes thereof while partially depressurizing the at least one additional adsorption bed from the outlet thereof into the other inlet-outlet pipe of the segregated storage adsorption bed, until the gas flowing from the at least one additional adsorption bed into the segregated storage adsorption bed is depleted of any product value; d. terminating the depressurizing of step (c) from the outlet end of the at least one additional adsorption bed and then continuing depressurizing thereof from the inlet end thereof to the waste outlet while continuing adsorption of the feed gas mixture in the first adsorption bed, discharging the product gas from the product outlet and collecting product gas in the segregated storage adsorption bed; e. continuing to discharge product gas from the product outlet and diverting product gas from the outlet of the first adsorption bed and from the product gas collected in the segregated storage adsorption bed to the outlet end of the at least one additional adsorption bed, passing said diverted product gas through the adsorption bed thereof to purge waste gas from the bed to the waste outlet; f. continuing to discharge product gas from the product outlet, terminating the flow of diverted product gas to the at least one additional adsorption bed, terminating the discharge of purge gas from the waste outlet, and equalizing the pressures of the segregated storage adsorption bed and the at least one additional adsorption bed by passing gas collected in the segregated storage adsorption bed in step (c) by the partial depressurizing of the at least on additional adsorption bed from the one inlet-outlet pipe of the segregated storage adsorption bed to the gas inlet of the at least one additional adsorption bed while passing product gas into the other inlet-outlet pipe of the segregated storage adsorption bed, thereby initiating repressurization of the at least one additional adsorption bed with a gas of greater product quality than the feed gaseous mixture; g. terminating the initial repressurization of step (f), isolating the segregated storage adsorption bed, and completely repressurizing the at least one additional adsorption bed with product gas diverted from the outlet of the first adsorption bed whereby the at least one additional adsorption bed is prepared for the fractionation of at least one component from a gaseous mixture by selective adsorption, while continuing to discharge product gas from the product outlet; and h. thereafter consecutively repeating steps (b) through (g) reversing the functions of the first adsorption bed and the at least one additional bed, wherein the gaseous mixture to be fractionated is introduced into and product gas is discharged from the at least one additional adsorption bed and the first adsorption bed is depressurized, purged and pressurized for repeating steps (a) through (h).

Claim 9

The process of claim 6 wherein the gaseous mixture is air, the adsorbent beds comprise a zeolite, the component fractionated from the gaseous mixture is nitrogen, and the product gas is enriched in oxygen.

Claim 10

The process of claim 6 wherein the product gas is available at about adsorption bed pressure.

Claim 11

The process of claim 8 wherein adsorption bed pressure is about 40 p.s.i.g.

Claim 12

A process for continuously fractionating at least one component from a gaseous mixture by selective adsorption in each of at least two adsorption zones in a low pressure delivery product gas cycle comprising the steps of: a. providing a first adsorption bed having a gas inlet and a gas outlet, at least one additional adsorption bed having a gas inlet and a gas outlet, the gas inlets of said first and at least one additional adsorption beds being connected to a feed gas stream, at least one segregated storage adsorption bed having two inlet-outlet pipes the at least one segregated storage adsorption bed being isolated from direct communication with the feed gas stream, the first inlet-outlet communicating with the gas inlets and gas outlets of said first and at least one additional adsorption beds and the second inlet-outlet communicating with the gas outlets of said first and at least one additional adsorption beds and a product outlet, the product outlet also communicating with the outlet of the first and at least one additional beds, a waste outlet communicating with the inlet and outlet of said first and at least one additional adsorption beds, and associated valves to isolate each of said adsorption beds; b. simultaneously introducing the gaseous mixture into the gas inlet of the first adsorption bed from the feed gas stream of repressurize the first adsorption bed, releasing product gas from the second inlet-outlet of the segregated storage adsorption bed after the segregated storage adsorption bed has product gas adsorbed therein, to depressurize the segregated storage adsorption bed and discharging part of the product gas from the product outlet while passing product gas into the gas outlet end of the at least one additional adsorption bed to reverse purge said bed, the purged gas from said bed being removed at the waste outlet; c. terminating the reverse purge and the removal of purged waste gas from the at least one additional adsorption bed of step (b), continuing to introduce the gaseous mixture into the inlet of the first adsorption bed, allowing the gaseous mixture to pass through the first adsorption bed, releasing product gas from the outlet of the first adsorption bed and discharging product gas from the product outlet; d. simultaneously with step (c) diverting product gas from the outlet of the first adsorption bed to the second inlet-outlet of the segregated storage adsorption bed whereby the segregated storage adsorption bed is reverse purged with product gas, the gas purged from the segregated storage adsorption bed passing to the at least one additional adsorption bed through the gas inlet thereof to partially repressurize the at least one additional adsorption bed; e. terminating the delivery of product gas from the first adsorption bed while continuing to introduce the gaseous mixture into the first adsorption bed to repressurize said bed to the desired pressure, isolating the at least one additional adsorption bed and delivering product gas from the segregated storage adsorption bed at low pressure to the product outlet whereby the depressurization of the segregated storage adsorption bed continues and product gas continues to be discharged; f. continuing to deliver product gas from the segregated storage adsorption bed at low pressure to the product outlet and further reducing the pressure of the segregated storage adsorption bed, and continuing to introduce the gaseous mixture into the first adsorption bed, passing gas from the gas outlet of the first adsorption bed to the gas outlet of the at least one additional adsorption bed whereby the at least one additional adsorption bed is repressurized while the pressure of the first adsorption bed is reduced; g. discontinuing the introduction of gaseous mixture into the first adsorption bed, terminating the flow of gas from the first adsorption bed to the at least one additional adsorption bed, introducing the gaseous mixture into the gas inlet of the at least one additional adsorption bed to continue the pressurization of the bed, passing gas from the gas outlet of the first adsorption bed to the first inlet-outlet pipe of the segregated storage adsorption bed and into said bed whereby the first adsorption bed is partially depressurized and the segregated adsorption bed is repressurized, releasing product gas from the second inlet-outlet end of the segregated storage adsorption bed and discharging the product gas from the product outlet; h. terminating the flow of gas from the first adsorption bed to the segregated storage adsorption bed, continuing introducing gaseous mixture into the at least one additional adsorption bed to continue pressurization of the bed, continuing releasing product gas from the second inlet-outlet of the segregated storage adsorption bed whereby the segregated storage adsorption bed begins depressurization, and discharging product gas from the product outlet; and i. thereafter consecutively repeating steps (b) through (h) reversing the functions of the first adsorption bed and the at least one additional bed, wherein the gaseous mixture to be fractionated is introduced into and product gas is discharged from the at least one additional adsorption bed while the first adsorption bed is purged, isolated and repressurized, and the segregated storage adsorption bed provides a reservoir for the continuous discharge of product gas from the product outlet.

Claim 13

A process for continuously fractionating at least one component from a gaseous mixture by selective adsorption in each of at least two adsorption zones in a low pressure delivery product gas cycle comprising the steps of: a. providing a first adsorption bed having a gas inlet and a gas outlet, at least one additional adsorption bed having a gas inlet and a gas outlet, the gas inlets of said first and at least one additional adsorption beds being connected to a feed gas stream, at least one segregated storage adsorption bed having two inlet-outlet pipes the at least one segregated storage adsorption bed being isolated from direct communication with the feed gas stream, the first inlet-outlet communicating with the gas inlets and gas outlets of said first and at least one additional adsorption beds and the second inlet-outlet communicating with the gas outlets of said first and at least one additional adsorption beds and a product outlet, the product outlet also communicating with the outlet of the first and at least one additional beds, a waste outlet communicating with the inlet and outlet of said first and at least one additional adsorption beds, and associated valves to isolate each of said adsorption beds; b. simultaneously introducing the gaseous mixture into the gas inlet of the first adsorption bed from the feed gas stream of repressurize the first adsorption bed, releasing product gas from the second inlet-outlet of the segregated storage adsorption bed after the segregated storage adsorption bed has product gas adsorbed therein, to depressurize the segregated storage adsorption bed and discharging part of the product gas from the product outlet while passing product gas into the gas outlet end of the at least one additional adsorption bed to reverse purge said bed, the purged gas from said bed being removed at the waste outlet; c. terminating the reverse purge and the removal of purged waste gas from the at least one additional adsorption bed of step (b), continuing to introduce the gaseous mixture into the inlet of the first adsorption bed, allowing the gaseous mixture to pass through the first adsorption bed, releasing product gas from the outlet of the first adsorption bed and discharging product gas from the product outlet; d. simultaneously with step (c) diverting product gas from the outlet of the first adsorption bed to the second inlet-outlet of the segregated storage adsorption bed whereby the segregated storage adsorption bed is reverse purged with product gas, the gas purged from the segregated storage adsorption bed passing to the at least one additional adsorption bed through the gas inlet thereof to partially repressurize the at least one additional adsorption bed; e. terminating the delivery of product gas from the first adsorption bed while continuing to introduce the gaseous mixture into the first adsorption bed to repressurize said bed to the desired pressure, isolating the at least one additional adsorption bed and delivering product gas from the segregated storage adsorption bed at low pressure to the product outlet whereby the depressurization of the segregated storage adsorption bed continues and product gas continues to be discharged; f. continuing to deliver product gas from the segregated storage adsorption bed at low pressure to the product outlet and further reducing the pressure of the segregated storage adsorption bed, and continuing to introduce the gaseous mixture into the first adsorption bed, passing gas from the gas outlet of the first adsorption bed to the gas outlet of the at least one additional adsorption bed whereby the at least one additional adsorption bed is repressurized while the pressure of the first adsorption bed is reduced; g. discontinuing the introduction of gaseous mixture into the first adsorption bed, terminating the flow of gas from the first adsorption bed to the at least one additional adsorption bed, introducing the gaseous mixture into the gas inlet of the at least one additional adsorption bed to continue the pressurization of the bed, passing gas from the gas outlet of the first adsorption bed to the first inlet-outlet pipe of the segregated storage adsorption bed and into said bed whereby the first adsorption bed is partially depressurized and the segregated adsorption bed is repressurized, releasing product gas from the second inlet-outlet end of the segregated storage adsorption bed and discharging the product gas from the product outlet; h. terminating the flow of gas from the first adsorption bed to the segregated storage adsorption bed, continuing introducing gaseous mixture into the at least one additional adsorption bed to continue pressurization of the bed, continuing releasing product gas from the second inlet-outlet of the segregated storage adsorption bed whereby the segregated storage adsorption bed begins depressurization, and discharging product gas from the product outlet; and i. thereafter consecutively repeating steps (b) through (h) reversing the functions of the first adsorption bed and the at least one additional bed, wherein the gaseous mixture to be fractionated is introduced into and product gas is discharged from the at least one additional adsorption bed while the first adsorption bed is purged, isolated and repressurized, and the segregated storage adsorption bed provides a reservoir for the continuous discharge of product gas from the product outlet.

Claim 14

The process of claim 10 wherein the gaseous mixture is air, the adsorbent bed comprise a zeolite, the component fractionated is nitrogen, and the product gas is enriched in oxygen.

Claim 15

The process of claim 10 wherein the product gas is available at a pressure less than about 2 p.s.i.g.