Adsorption process with mixed repressurization and purge/equalization

Claim 2

A process for selectively separating a more strongly adsorbable component from a less strongly adsorbable component of a feed gas mixture in a plurality of adsorption beds containing an adsorbent selective for the more strongly adsorbable component, comprising the steps of: (a) introducing a feed gas mixture at high pressure containing said more strongly adsorbable component and said less strongly adsorbable component into an inlet of a first adsorption bed containing said adsorbent selectivel for the more strongly adsorbable component and adsorbing the more strongly adsorbable component on the adsorbent while the less strongly adsorbable component passes through said first bed unadsorbed until the adsorption front of the more strongly adsorbable component approaches an outlet of said first bed and terminating the introduction of the feed gas mixture; (b) following the termination of the introduction of the feed gas mixture into said first bed and without any intervening steps, cocurrently depressurizing said first bed to a lower pressure to remove said gas mixture from said first bed and passing said gas mixture to an outlet of a second bed of said plurality of adsorption beds at lower pressure to countercurrently purge said more strongly adsorbable component from said second bed; (c) countercurrently evacuating said first bed under vacuum conditions to further remove said more strongly adsorbable component at the lowest pressure; (d) countercurrently purging said first bed with cocurrently depressurizing gas mixture from a bed of said plurality of adsorption beds undergoing step (b) to remove additional more strongly adsorbable component from said first bed; (e) repressurizing said first bed with less strongly adsorbable component from a bed of said plurality of adsorption beds currently undergoing step (a) and with feed gas mixture; and (f) performing steps (a) through (e) in each of said plurality of adsorption beds in a phased sequence.

Claim 3

The process of claim 1 wherein a bed undergoing step (e) is repressurized initially with feed gas mixture and then with said less strongly adsorbable component.

Claim 4

The process of claim 1 wherein a bed undergoing step (e) is repressurized with ambient pressure feed gas mixture and high pressure feed gas mixture.

Claim 5

The process of claim 3 wherein a bed undergoing step (e) is repressurized initially with ambient pressure feed gas mixture, then with high pressure feed gas mixture and finally with said less strongly adsorbable component.

Claim 6

The process of claim 1 wherein a bed undergoing step (e) is repressurized initially with ambient pressure feed gas mixture and then with said less strongly adsorbable component.

Claim 7

The process of claim 1 wherein a bed undergoing step (e) is repressurized initially with said less strongly adsorbable component and then with feed gas mixture.

Claim 8

The process of claim 1 wherein a bed undergoing step (e) is repressurized initially with said less strongly adsorbable component then with ambient pressure feed gas mixture.

Claim 9

The process of claim 1 wherein a bed undergoing step (e) is repressurized initially with said less strongly adsorbable component then with ambient pressure feed gas mixture and then with high pressure feed gas mixture.

Claim 10

The process of claim 1 wherein a bed undergoing step (e) is repressurized with said less strongly adsorbable component and said feed gas mixture simultaneously.

Claim 11

The process of claim 9 wherein a bed undergoing step (e) is repressurized with said less strongly adsorbable component and ambient pressure feed gas mixture simultaneously.

Claim 12

The process of claim 9 wherein a bed undergoing step (e) is repressurized with said less strongly adsorbable component and high pressure feed gas mixture simultaneously.

Claim 13

The process of claim 1 wherein said feed gas mixture is air, said more strongly adsorbable component is nitrogen and said less strongly adsorbable component is oxygen.

Claim 14

The process of claim 1 wherein a bed finishing cocurrent depressurization is then further cocurrent depressurized to pressure equalize with a bed of said plurality of adsorption beds finishing countercurrent purge.

Claim 15

The process of claim 1 wherein the process is carried out in two beds.

Claim 16

The process of claim 1 wherein the process is carried out in at least four beds and at least two beds are simultaneously in a portion of step (a).

Claim 17

A process for selectively separating a more strongly adsorbable component from a less strongly adsorbable component of a feed gas mixture in a plurality of adsorption beds containing an adsorbent selective for the more strongly adsorbable component, comprising the steps of: (a) introducing a feed gas mixture at high pressure containing said more strongly adsorbable component and said less strongly adsorbable component into an inlet of a first adsorption bed containing said adsorbent selective for the more strongly adsorbable component and adsorbing the more strongly adsorbable component on the adsorbent while the less strongly adsorbable component passes through said first bed unadsorbed until the adsorption front of the more strongly adsorbable component approaches an outlet of said first bed and terminating the introduction of the feed gas mixture; (b) following the termination of the introduction of the feed gas mixture into said first bed and without any intervening steps, cocurrently depressurizing said first bed to a lower pressure to remove said gas mixture from said first bed and passing said gas mixture to an outlet of a second bed of said plurality of adsorption beds at lower pressure to countercurrently purge said more strongly adsorbable component from said second bed; (c) cocurrently depressurizing said first bed to further remove said gas mixture from said first bed and to pressure equalize said first bed with a bed of said plurality of adsorption beds finishing countercurrent purge of step (e); (d) countercurrently evacuating said first bed under vacuum conditions to further remove said more strongly adsorbable component at a lowest pressure; (e) countercurrently purging said first bed with cocurrently depressurizing gas mixture from a bed of said plurality of adsorption beds undergoing step (b) to remove additional more strongly adsorbable component from said first bed; (f) countercurrently pressure equalizing said first bed with a bed of said plurality of adsorption beds at higher pressure undergoing said cocurrent depressurization of step (c); (g) repressurizing said first bed with less strongly adsorbable component from a bed of said plurality of adsorption beds currently undergoing step (a) and with feed gas mixture; and (h) performing steps (a) through (g) in each of said plurality of adsorption beds in a phased sequence.

Claim 18

A process for selectively separating a more strongly adsorbable component from a less strongly adsorbable component of a feed gas mixture in a plurality of adsorption beds containing an adsorbent selective for the more strongly adsorbable component, comprising the steps of: (a) introducing a feed gas mixture at high pressure containing said more strongly adsorbable component and said less strongly adsorbable component into an inlet of a first adsorption bed containing said adsorbent selective for the more strongly adsorbable component and adsorbing the more strongly adsorbable component on the adsorbent while the less strongly adsorbable component passes through said first bed unadsorbed until the adsorption front of the more strongly adsorbable component approaches an outlet of said first bed and terminating the introduction of the feed gas mixture; (b) following the termination of the introduction of the feed gas mixture into said first bed and without any intervening steps, cocurrently depressurizing said first bed to a lower pressure to remove said gas mixture from said first bed and passing said gas mixture to an outlet of a second bed of said plurality of adsorption beds at lower pressure to countercurrently purge said more strongly adsorbable component from said second bed; (c) cocurrently depressurizing said first bed to further remove said gas mixture from said first bed and to pressure equalize said first bed with a bed of said plurality of adsorption beds finishing countercurrent purge of step (e); (d) countercurrently evacuating said first bed under vacuum conditions to further remove said more strongly adsorbable component at a lowest pressure; (e) countercurrently purging said first bed with cocurrently depressurizing gas mixture from a bed of said plurality of adsorption beds undergoing step (b) to remove additional more strongly adsorbable component from said first bed; (f) countercurrently pressure equalizing said first bed with a bed of said plurality of adsorption beds at higher pressure undergoing said cocurrent depressurization of step (c); (g) repressurizing said first bed with less strongly adsorbable component from a bed of said plurality of adsorption beds currently undergoing step (a) and with feed gas mixture; and (h) performing steps (a) through (g) in each of said plurality of adsorption beds in a phased sequence.

Claim 19

The process of claim 16 wherein a bed undergoing step (g) is repressurized initially with feed gas mixture and then with said less strongly adsorbable component.

Claim 20

The process of claim 16 wherein a bed undergoing step (g) is repressurized with ambient pressure feed gas mixture and high pressure feed gas mixture.

Claim 21

The process of claim 16 wherein a bed undergoing step (g) is repressurized initially with ambient pressure feed gas mixture and then with said less strongly adsorbable component.

Claim 22

The process of claim 16 wherein a bed undergoing step (g) is repressurized initially with ambient pressure feed gas mixture, then with high pressure feed gas mixture and finally with said less strongly adsorbable component.

Claim 23

The process of claim 16 wherein a bed undergoing step (g) is repressurized initially with said less strongly adsorbable component and then with feed gas mixture.

Claim 24

The process of claim 16 wherein a bed undergoing step (g) is repressurized initially with said less strongly adsorbable component then with ambient pressure feed gas mixture.

Claim 25

The process of claim 16 wherein a bed undergoing step (g) is repressurized initially with said less strongly adsorbable component then with ambient pressure feed gas mixture and then with high pressure feed gas mixture.

Claim 26

The process of claim 16 wherein a bed undergoing step (g) is repressurized with said less strongly adsorbable component and said feed gas mixture simultaneously.

Claim 27

The process of claim 16 wherein said feed gas mixture is air, said more strongly adsorbable component is nitrogen and said less strongly adsorbable component is oxygen.

Claim 28

The process of claim 16 wherein during step (c) cocurrent depressurization to pressure equalize with a bed undergoing step (f), simultaneously initiating countercurrent evacuation of said first bed.

Claim 29

The process of claim 16 wherein the process is carried out in two beds.

Claim 30

The process of claim 16 wherein the process is carried out in at least four beds and at least two beds are simultaneously in a portion of step (a).

Claim 31

A process for selectively separating nitrogen from oxygen in air in three adsorption beds containing an adsorbent selective for nitrogen, comprising the steps of: (a) introducing feed air at high pressure into an inlet of a first adsorption bed containing said adsorbent selective for nitrogen and adsorbing nitrogen on the adsorbent while oxygen passes through said first bed unadsorbed as a product until the adsorption front of nitrogen approaches an outlet of said first bed and terminating the introduction of air into said first bed; (b) following the termination of the introduction of air into said first bed and without any intervening steps, cocurrently depressurizing said first bed to remove void space gas and nitrogen from said first bed and passing said void space gas and nitrogen to an outlet of a second bed of said three adsorption beds at lower pressure to countercurrently purge said nitrogen from said second bed; (c) cocurrently depressurizing said first bed to further remove said void space gas and nitrogen from said first bed and to pressure equalize said first bed with a bed of said three adsorption beds finishing countercurrent purge of step (e); (d) countercurrently evacuating said first bed under vacuum conditions to further remove said void space gas and nitrogen at a lowest pressure; (e) countercurrently purging said first bed with cocurrently depressurizing void space gas and nitrogen from a bed of said three adsorption beds undergoing step (b) to remove additional nitrogen from said first bed; (f) countercurrently pressure equalizing said first bed with a bed of said three adsorption beds at higher pressure undergoing said cocurrent depressurization of step (c); (g) repressurizing said first bed with oxygen from a bed of said three adsorption beds currently undergoing step (a) and with feed air; and (h) performing steps (a) through (g) in each of said three adsorption beds in a phased sequence.

Claim 32

A process for selectively separating nitrogen from oxygen in air in three adsorption beds containing an adsorbent selective for nitrogen, comprising the steps of: (a) introducing feed air at high pressure into an inlet of a first adsorption bed containing said adsorbent selective for nitrogen and adsorbing nitrogen on the adsorbent while oxygen passes through said first bed unadsorbed as a product until the adsorption front of nitrogen approaches an outlet of said first bed and terminating the introduction of air into said first bed; (b) following the termination of the introduction of air into said first bed and without any intervening steps, cocurrently depressurizing said first bed to remove void space gas and nitrogen from said first bed and passing said void space gas and nitrogen to an outlet of a second bed of said three adsorption beds at lower pressure to countercurrently purge said nitrogen from said second bed; (c) cocurrently depressurizing said first bed to further remove said void space gas and nitrogen from said first bed and to pressure equalize said first bed with a bed of said three adsorption beds finishing countercurrent purge of step (e); (d) countercurrently evacuating said first bed under vacuum conditions to further remove said void space gas and nitrogen at a lowest pressure; (e) countercurrently purging said first bed with cocurrently depressurizing void space gas and nitrogen from a bed of said three adsorption beds undergoing step (b) to remove additional nitrogen from said first bed; (f) countercurrently pressure equalizing said first bed with a bed of said three adsorption beds at higher pressure undergoing said cocurrent depressurization of step (c); (g) repressurizing said first bed with oxygen from a bed of said three adsorption beds currently undergoing step (a) and with feed air; and (h) performing steps (a) through (g) in each of said three adsorption beds in a phased sequence.

Claim 33

The process of claim 29 wherein a bed undergoing step (g) is repressurized initially with feed air and then with said less strongly adsorbable component.

Claim 34

The process of claim 29 wherein a bed undergoing step (g) is additionally repressurized with ambient pressure feed air.

Claim 35

The process of claim 29 wherein a bed undergoing step (g) is repressurized initially with ambient pressure feed gas mixture and then with said less strongly adsorbable component.

Claim 36

The process of claim 29 wherein a bed undergoing step (g) is repressurized initially with ambient pressure feed air, then with high pressure feed air and finally with oxygen.

Claim 37

The process of claim 29 wherein a bed undergoing step (g) is repressurized initially with oxygen and then with feed air.

Claim 38

The process of claim 29 wherein a bed undergoing step (g) is repressurized initially with oxygen and then with ambient pressure feed air.

Claim 39

The process of claim 29 wherein a bed undergoing step (g) is repressurized initially with oxygen then with ambient pressure feed air and then with high pressure feed air.

Claim 40

The process of claim 29 wherein a bed undergoing step (g) is repressurized with oxygen and said feed air simultaneously.

Claim 41

The process of claim 29 wherein said feed air is at a pressure in the range of approximately 14-30 psia.

Claim 42

The process of claim 29 wherein said feed air is at a pressure in the range of approximately 14-24 psia.

Claim 43

The process of claim 29 wherein at the end of evacuation a bed undergoing step (d) is at a pressure in the range of approximately 1-10 psia.

Claim 44

The process of claim 29 wherein a bed undergoing step (g) is repressurized with oxygen and ambient pressure feed air simultaneously.

Claim 45

The process of claim 29 wherein a bed undergoing step (g) is repressurized with oxygen and high pressure feed air simultaneously.

Claim 46

The process of claim 29 wherein during step (c) cocurrent depressurization to pressure equalize with a bed undergoing step (f), simultaneously initiating countercurrent evacuation of said first bed.

Claim 47

The process of claim 29 wherein the process is carried out in two beds.

Claim 48

The process of claim 29 wherein the process is carried out in at least four beds and at least two beds are simultaneously in a portion of step (a).