Extended vacuum swing adsorption process

Claim 2

A process for selectively separating a more strongly adsorbable component from a less strongly absorbable 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 absorbable 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 undergoing step (d); (c) countercurrently evacuating said first bed under vacuum conditions to further remove said more strongly absorbable 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 wherein at least two adsorption beds are countercurrently evacuated simultaneously in overlapping countercurrent evacuation steps in said plurality of adsorption beds.

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 while the former bed is simultaneously countercurrently evacuated.

Claim 15

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 wherein at least two adsorption beds are countercurrently evacuated simultaneously in overlapping countercurrent evacuation steps in the plurality of adsorption beds.

Claim 16

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 wherein at least two adsorption beds are countercurrently evacuated simultaneously in overlapping countercurrent evacuation steps in the plurality of adsorption beds.

Claim 17

The process of claim 14 wherein said feed gas mixture is air, said more strongly adsorbable component is nitrogen and said less strongly adsorbable component is oxygen.

Claim 18

A process for selectively separating nitrogen from oxygen in air in four 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 oxygen from said first bed and passing said void space gas and oxygen to an outlet of a second bed of said four 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 oxygen from said first bed and to pressure equalize said first bed with a bed of said four 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 from the process; (e) countercurrently purging said first bed with cocurrently depressurizing void space gas and nitrogen from a bed of said four 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 four adsorption beds at higher pressure undergoing said cocurrent depressurization of step (c); (g) repressurizing said first bed with oxygen from a bed of said four adsorption beds currently undergoing step (a) and with feed air; and (h) performing steps (a) through (g) in each of said four adsorption beds in a phased sequence wherein at least two adsorption beds are countercurrently evacuated simultaneously in overlapping countercurrent evacuation steps in the plurality of adsorption beds.

Claim 19

A process for selectively separating nitrogen from oxygen in air in four 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 oxygen from said first bed and passing said void space gas and oxygen to an outlet of a second bed of said four 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 oxygen from said first bed and to pressure equalize said first bed with a bed of said four 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 from the process; (e) countercurrently purging said first bed with cocurrently depressurizing void space gas and nitrogen from a bed of said four 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 four adsorption beds at higher pressure undergoing said cocurrent depressurization of step (c); (g) repressurizing said first bed with oxygen from a bed of said four adsorption beds currently undergoing step (a) and with feed air; and (h) performing steps (a) through (g) in each of said four adsorption beds in a phased sequence wherein at least two adsorption beds are countercurrently evacuated simultaneously in overlapping countercurrent evacuation steps in the plurality of adsorption beds.

Claim 20

The process of claim 16 wherein said feed air is at a pressure in the range of approximately 14-30 psia.

Claim 21

The process of claim 16 wherein said feed air is at a pressure in the range of approximately 14-24 psia.

Claim 22

The process of claim 16 wherein at the end of evacuation the bed undergoing step (d) is at a pressure in the range of approximately 1-10 psia.

Claim 23

The process of claim 16 wherein a bed undergoing step (g) is repressurized with oxygen and ambient pressure feed air simultaneously.

Claim 24

The process of claim 16 wherein a bed undergoing step (g) is repressurized with oxygen and high pressure feed air simultaneously.

Claim 25

The process of claim 16 wherein a bed finishing cocurrent depressurization is then further cocurrent depressurized to pressure equalize with a bed of said four adsorption beds finishing countercurrent purge while the former bed is simultaneously countercurrently evacuated.