Adsorption process to recover hydrogen from low pressure feeds

Claim 2

A process for selectively separating at least one more strongly adsorbable component(s) 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(s), comprising the steps of: (a) introducing a feed gas mixture at elevated pressure containing said more strongly adsorbable component(s) and said less strongly adsorbable component into an inlet of a first adsorption bed containing said adsorbent selective for the more strongly adsorbable component(s) and adsorbing the more strongly adsorbable component(s) 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(s) approaches an outlet of said first bed and terminating the introduction of the feed gas mixture; (b) 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 another bed of said plurality of adsorption beds at lower pressure to countercurrently purge said more strongly adsorbable component(s) from the other bed under the influence of a vacuum, while simultaneously countercurrently venting said first bed; (c) countercurrently evacuating said first bed under vacuum conditions to further remove said more strongly adsorbable component(s) at the lowest pressure; (d) countercurrently purging said first bed with cocurrently depressurizing gas mixture from another bed of said plurality of adsorption beds undergoing step (b) to remove additional more strongly adsorbable component(s) from said first bed under the influence of vacuum; (e) repressurizing said first bed; 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 said first adsorption bed is repressurized with feed gas mixture.

Claim 4

The process of claim 1 wherein said first adsorption bed is repressurized with less strongly adsorbable component.

Claim 5

The process of claim 1 wherein said first adsorption bed is repressurized with pressure feed gas mixture and with said less strongly adsorbable component.

Claim 6

The process of claim 1 wherein after the step (a) adsorption step the first bed is cocurrently depressurized to pressure equalize with another bed at a lower pressure.

Claim 7

The process of claim 5 wherein the first bed is simultaneously countercurrently depressurized to pressure equalize with another bed at a lower pressure while the first bed is cocurrently depressurized.

Claim 8

The process of claim 1 wherein after the step (d) purging, the first bed is at least partially repressurized by pressure equalization with another bed.

Claim 9

The process of claim 7 wherein after the step (a) adsorption, the first bed is cocurrently depressurized to supply pressure equalization gas for another bed.

Claim 10

The process of claim 1 wherein during the step (a) adsorption, less strongly adsorbable component is produced for a product and for repressurizing another bed.

Claim 11

The process of claim 9 wherein during step (a) adsorption, less strongly adsorbable component is produced for a product during a portion of the step (a) adsorption and less strongly adsorbable component is produced for a product and for repressurizing another bed simultaneously in another portion of the step (a) adsorption.

Claim 12

The process of claim 1 wherein between three and six parallel beds are utilized for said plurality of adsorption beds.

Claim 13

The process of claim 1 wherein said feed gas mixture is a hydrogen containing gas mixture, said more strongly adsorbable component(s) is selected from the group consisting of nitrogen, methane, carbon monoxide, carbon dioxide and mixtures thereof and said less strongly adsorbable component is hydrogen.

Claim 14

The process of claim 1 wherein multiple beds of said plurality of adsorption beds are performing step (a) adsorption at a given time during the process.

Claim 15

The process of claim 1 wherein multiple beds of said plurality of adsorption beds are performing step (c) evacuation at a given time during the process.

Claim 16

A process for selectively separating at least one more strongly adsorbable component(s) selected from the group consisting of nitrogen, methane, carbon monoxide, carbon dioxide and mixtures thereof from hydrogen in a hydrogen-containing feed gas mixture in a plurality of adsorption beds containing an adsorbent selective for the more strongly adsorbable component(s), comprising the steps of: (a) introducing a hydrogen-containing feed gas mixture at elevated pressure containing said at least one more strongly adsorbable component(s) and said hydrogen into an inlet of a first adsorption bed containing said adsorbent selective for said at least one more strongly adsorbable component(s) and adsorbing a more strongly adsorbable component(s) on the adsorbent while the hydrogen passes through said first bed unadsorbed until the adsorption front of the more strongly adsorbable component(s) approaches an outlet of said first bed and terminating the introduction of said hydrogen-containing feed gas mixture; (b) cocurrently depressurizing said first bed to a lower pressure to remove gas from said first bed and passing said gas to an outlet of another bed of said plurality of adsorption beds at lower pressure to countercurrently purge said more strongly adsorbable component(s) from the other bed under the influence of a vacuum, while simultaneously countercurrently venting said first bed; (c) countercurrently evacuating said first bed under vacuum conditions to further remove said more strongly adsorbable component(s) at a lowest pressure; (d) countercurrently purging said first bed with cocurrently depressurizing gas from another bed of said plurality of adsorption beds undergoing step (b) to remove additional more strongly adsorbable component from said first bed under the influence of a vacuum; (e) repressurizing said first bed; and (f) performing steps (a) through (e) in each of said plurality of adsorption beds in a phased sequence.

Claim 17

A process for selectively separating at least one more strongly adsorbable component(s) selected from the group consisting of nitrogen, methane, carbon monoxide, carbon dioxide and mixtures thereof from hydrogen in a hydrogen-containing feed gas mixture in a plurality of adsorption beds containing an adsorbent selective for the more strongly adsorbable component(s), comprising the steps of: (a) introducing a hydrogen-containing feed gas mixture at elevated pressure containing said at least one more strongly adsorbable component(s) and said hydrogen into an inlet of a first adsorption bed containing said adsorbent selective for said at least one more strongly adsorbable component(s) and adsorbing a more strongly adsorbable component(s) on the adsorbent while the hydrogen passes through said first bed unadsorbed until the adsorption front of the more strongly adsorbable component(s) approaches an outlet of said first bed and terminating the introduction of said hydrogen-containing feed gas mixture; (b) cocurrently depressurizing said first bed to a lower pressure to remove gas from said first bed and passing said gas to an outlet of another bed of said plurality of adsorption beds at lower pressure to countercurrently purge said more strongly adsorbable component(s) from the other bed under the influence of a vacuum, while simultaneously countercurrently venting said first bed; (c) countercurrently evacuating said first bed under vacuum conditions to further remove said more strongly adsorbable component(s) at a lowest pressure; (d) countercurrently purging said first bed with cocurrently depressurizing gas from another bed of said plurality of adsorption beds undergoing step (b) to remove additional more strongly adsorbable component from said first bed under the influence of a vacuum; (e) repressurizing said first bed; and (f) performing steps (a) through (e) in each of said plurality of adsorption beds in a phased sequence.

Claim 18

The process of claim 15 wherein said hydrogen-containing feed gas mixture contains less than 60% hydrogen.

Claim 19

The process of claim 15 wherein said hydrogen-containing feed gas mixture is at a pressure less than 125 psig.

Claim 20

The process of claim 15 wherein said hydrogen-containing feed gas mixture contains more than 1% carbon monoxide or carbon dioxide.

Claim 21

The process of claim 15 wherein said adsorbent is selected from the group consisting of 13X-zeolite, 5A-zeolite, CaA-zeolite, activated carbon and mixtures thereof.

Claim 22

The process of claim 19 wherein the adsorbent is layered in the plurality of adsorbent beds with a layer of activated carbon near a feed end of each bed, a layer of 13X-zeolite, a layer of 5A-zeolite and a layer of CaA-zeolite.

Claim 23

The process of claim 15 wherein the hydrogen recovered from the process has a recovery of at least 80%.

Claim 24

The process of claim 15 wherein the hydrogen recovered from the process has a purity of at least 95%.

Claim 25

The process of claim 15 wherein the hydrogen-containing feed gas mixture is a refinery off gas.

Claim 26

A process for selectively separating at least one more strongly adsorbable component(s) selected from the group consisting of nitrogen, methane, carbon monoxide, carbon dioxide and mixtures thereof from hydrogen in a hydrogen-containing feed gas mixture in six parallel connected adsorption beds containing an adsorbent(s) selective for the more strongly adsorbable component(s), comprising the steps of: (a) introducing a hydrogen-containing feed gas mixture at elevated pressure in the range of 5 to 125 psig containing said at least one more strongly adsorbable component(s) and said hydrogen into an inlet of a first adsorption bed containing said adsorbent(s) selective for said at least one more strongly adsorbable component(s) and adsorbing a more strongly adsorbable component(s) on the adsorbent while the hydrogen passes through said first bed unadsorbed as a product of at least 95% purity until the adsorption front of the more strongly adsorbable component(s) approaches an outlet of said first bed and terminating the introduction of said hydrogen-containing feed gas mixture; (b) initially cocurrently depressurizing said first bed to a lower pressure to remove gas from said first bed and passing said gas to an outlet of another bed of said six adsorption beds at lower pressure to equalize the pressure in the two adsorption beds; (c) further cocurrently depressurizing said first bed to a lower pressure to remove gas from said first bed and passing said gas directly to an outlet of a third bed of said six adsorption beds at a lowest pressure to countercurrently purge said more strongly adsorbable component(s) from said third bed under the influence of a vacuum, while simultaneously countercurrently venting said first bed; (d) countercurrently evacuating said first bed under vacuum conditions to further remove said more strongly adsorbable component(s) to a lowest pressure in the range of 500 to 80 Torr absolute; (e) countercurrently purging said first bed with cocurrently depressurizing gas from another bed of said plurality of adsorption beds undergoing step (c) to remove additional more strongly adsorbable component(s) from said first bed under the influence of a vacuum; (f) initially repressurizing said first bed by passing gas from a bed undergoing step (b) initial cocurrent depressurization to pressure equalize the two beds; (g) repressurizing said first bed with hydrogen-containing feed gas mixture; and (h) performing steps (a) through (g) in each of said six adsorption beds in a phased sequence.

Claim 27

A process for selectively separating at least one more strongly adsorbable component(s) selected from the group consisting of nitrogen, methane, carbon monoxide, carbon dioxide and mixtures thereof from hydrogen in a hydrogen-containing feed gas mixture in six parallel connected adsorption beds containing an adsorbent(s) selective for the more strongly adsorbable component(s), comprising the steps of: (a) introducing a hydrogen-containing feed gas mixture at elevated pressure in the range of 5 to 125 psig containing said at least one more strongly adsorbable component(s) and said hydrogen into an inlet of a first adsorption bed containing said adsorbent(s) selective for said at least one more strongly adsorbable component(s) and adsorbing a more strongly adsorbable component(s) on the adsorbent while the hydrogen passes through said first bed unadsorbed as a product of at least 95% purity until the adsorption front of the more strongly adsorbable component(s) approaches an outlet of said first bed and terminating the introduction of said hydrogen-containing feed gas mixture; (b) initially cocurrently depressurizing said first bed to a lower pressure to remove gas from said first bed and passing said gas to an outlet of another bed of said six adsorption beds at lower pressure to equalize the pressure in the two adsorption beds; (c) further cocurrently depressurizing said first bed to a lower pressure to remove gas from said first bed and passing said gas directly to an outlet of a third bed of said six adsorption beds at a lowest pressure to countercurrently purge said more strongly adsorbable component(s) from said third bed under the influence of a vacuum, while simultaneously countercurrently venting said first bed; (d) countercurrently evacuating said first bed under vacuum conditions to further remove said more strongly adsorbable component(s) to a lowest pressure in the range of 500 to 80 Torr absolute; (e) countercurrently purging said first bed with cocurrently depressurizing gas from another bed of said plurality of adsorption beds undergoing step (c) to remove additional more strongly adsorbable component(s) from said first bed under the influence of a vacuum; (f) initially repressurizing said first bed by passing gas from a bed undergoing step (b) initial cocurrent depressurization to pressure equalize the two beds; (g) repressurizing said first bed with hydrogen-containing feed gas mixture; and (h) performing steps (a) through (g) in each of said six adsorption beds in a phased sequence.

Claim 28

The process of claim 24 wherein step (g) repressurization is performed with product hydrogen and hydrogen-containing feed gas mixture.

Claim 29

The process of claim 24 wherein step (b) pressure equalization is performed between the two beds by connecting their respective outlets and their respective inlets.

Claim 30

The process of claim 24 wherein each bed has an idle period between step (f) pressure equalization and step (g) repressurization.