Vacuum swing adsorption process for production of 95+% n2 from ambient air

Claim 3

The method of claim 1 wherein the method is conducted in a continuous manner whereby the repressurized adsorption zone of step (d) is sequentially operated using steps (a) through (d).

Claim 4

The method of claim 1 wherein there are a plurality of parallel-connected adsorption zones.

Claim 5

The method of claim 1 wherein there are three parallel-connected adsorption zones.

Claim 6

The method of claim 1 wherein when one adsorption zone is undergoing the adsorption stage, step (a); a second adsorption zone is undergoing a portion of the further evacuation stage, step (c) and then the repressurization stage, step (d); while a third adsorption zone is undergoing the first desorption and evacuation stage, step (b) and then a portion of the further evacuation stage, step (c).

Claim 7

The method of claim 1 wherein the adsorption stage of step (a) is conducted with said feed air stream and the recycled nitrogen containing gas of step (b) during a first portion of the adsorption stage of step (a) and with only said feed air stream during a second portion of the adsorption stage of step (a).

Claim 8

The method of claim 1 wherein said first portion of the adsorption stage is conducted for a time period co-extensive with the desorption and evacuation stage of step (b).

Claim 9

The method of claim 1 wherein the adsorption zone contains a first layer of adsorbent selective for water and carbon dioxide and a second layer of adsorbent selective for nitrogen.

Claim 10

The method of claim 8 wherein adsorbent selective for water and carbon dioxide is selected from the group consisting of zeolites, alumina, silica gel, activated carbon and mixtures thereof.

Claim 11

The method of claim 8 wherein the adsorbent selective for nitrogen is selected from the group consisting of A-zeolite, X-zeolite, Y-zeolite, mordenite, such adsorbents with a single or binary exchanged cation from Group I and II metals, and mixtures thereof.

Claim 12

The continuous method for recovering nitrogen-enriched gas from air using three parallel-connected adsorption zones operated in a vacuum swing sequence of stages comprising: (a) passing a feed air stream and optimally a recycle nitrogen-containing gas of step (c) at an above-ambient pressure level of approximately 0-10 psig through a first adsorption zone containing an adsorbent selective to retain nitrogen, adsorbing said nitrogen on said adsorbent and allowing oxygen-enriched gas to pass through the zone essentially unadsorbed; (b) continuing to pass only the feed air stream at elevated pressure through said adsorption zone to further adsorb nitrogen on said adsorbent and allow oxygen to pass essentially unadsorbed through the zone; (c) without any intervening rinse step, desorbing and evacuating nitrogen-containing gas counter-currently of the feed air stream of steps (a) and (b) from said adsorption zone to an intermediate sub-ambient pressure level dependent on the desired nitrogen product purity by a reduction of the pressure in said zone and recycling the resulting nitrogen-containing gas to the feed air stream of step (a); (d) further evacuating nitrogen from said adsorption zone counter-currently of the feed air stream of steps (a) and (b) by further reduction of the pressure in said zone to a lower sub-ambient pressure level of approximately 50 to 200 torr and recovering this nitrogen as a nitrogen product having a nitrogen purity of approximately 95 to 99.5%; (e) repressuring the adsorption zone from the lower sub-ambient pressure level of step (d) to approximately the elevated pressure level of the feed air stream of step (a) by introducing oxygen-enriched gas of step (b) counter-currently of the feed air stream of steps (a) and (b) into the adsorption zone; and (f) repeatedly performing the sequence of steps (a) through (e) on each of the three beds in appropriate timed sequence.

Claim 13

The continuous method for recovering nitrogen-enriched gas from air using three parallel-connected adsorption zones operated in a vacuum swing sequence of stages comprising: (a) passing a feed air stream and optimally a recycle nitrogen-containing gas of step (c) at an above-ambient pressure level of approximately 0-10 psig through a first adsorption zone containing an adsorbent selective to retain nitrogen, adsorbing said nitrogen on said adsorbent and allowing oxygen-enriched gas to pass through the zone essentially unadsorbed; (b) continuing to pass only the feed air stream at elevated pressure through said adsorption zone to further adsorb nitrogen on said adsorbent and allow oxygen to pass essentially unadsorbed through the zone; (c) without any intervening rinse step, desorbing and evacuating nitrogen-containing gas counter-currently of the feed air stream of steps (a) and (b) from said adsorption zone to an intermediate sub-ambient pressure level dependent on the desired nitrogen product purity by a reduction of the pressure in said zone and recycling the resulting nitrogen-containing gas to the feed air stream of step (a); (d) further evacuating nitrogen from said adsorption zone counter-currently of the feed air stream of steps (a) and (b) by further reduction of the pressure in said zone to a lower sub-ambient pressure level of approximately 50 to 200 torr and recovering this nitrogen as a nitrogen product having a nitrogen purity of approximately 95 to 99.5%; (e) repressuring the adsorption zone from the lower sub-ambient pressure level of step (d) to approximately the elevated pressure level of the feed air stream of step (a) by introducing oxygen-enriched gas of step (b) counter-currently of the feed air stream of steps (a) and (b) into the adsorption zone; and (f) repeatedly performing the sequence of steps (a) through (e) on each of the three beds in appropriate timed sequence.