Enhanced gas separation by selective adsorption

Claim 2

An improved pressure swing adsorption process for separating a more readily adsorbable gas component(s) from less readily adsorbable gas component(s) of a gas mixture comprising: (a) introducing said gas mixture to an adsorption column, containing an adsorbent capable of selectively adsorbing the more readily adsorbable gas component(s) of said gas mixture, at a point between the opposite ends of the column; (b) imposing cyclic gas flow and pressure variations on the gas mixture in said column from a first end thereof by a first, larger, cyclic volume displacement means; (c) imposing cyclic gas flow and pressure variations on the gas mixture in said column at the same time from the second end thereof by a second, smaller, cyclic volume displacement means, the ratio of the volume displacement produced by said second means to that of said first means being from about 0.15 to about 0.65, the second means imposing said cyclic flow and pressure variations relative to the flow and pressure variations of said first means at a phase angle within the range of from about 30° lag to about 90° lead; (d) withdrawing a gas stream enriched in one said gas component from the first end of the column; and (e) withdrawing a gas stream enriched in the other said gas component(s) from the second end of the column, whereby the gas mixture passes rapidly back-and-forth within said column, achieving an enhanced separation of the gas mixture and production of the desired product.

Claim 3

The process of claim 1 in which said phase angle for the second displacement means is from about 15° lag to about 75° lead.

Claim 4

The process of claim 2 in which said phase angle is from about 30° lead to about 45° lead.

Claim 5

The process of claim 1 in which said volume displacement ratio of second means/first means is from about 0.25 to about 0.50.

Claim 6

The process of claim 4 in which said phase angle for the second displacement means is from about 15° lag to about 75° lead.

Claim 7

The process of claim 5 in which said phase angle is from about 30° lead to about 45° lead.

Claim 8

The process of claim 6 in which said volume displacement ratio of second means/first means is from about 0.25 to about 0.50.

Claim 9

The process of claim 7 in which said gas mixture comprises air.

Claim 10

The process of claim 1 in which said cyclic gas flow and pressure variations are imposed by driving pistons in fluid communication with each end of the column.

Claim 11

The process of claim 1 in which said cyclic gas flow and pressure variations are imposed by movable diaphragms in fluid communication with each end of the column.

Claim 12

The process of claim 1 in which said gas mixture comprises air, said more readily adsorbable component being nitrogen and said less readily adsorbable component being oxygen.

Claim 13

The process of claim 1 in which said gas mixture comprises a mixture of hydrogen and methane, said more readily adsorbable component being methane and said less readily adsorbable component being hydrogen.

Claim 14

An improved apparatus for the pressure swing adsorption separation of a more readily adsorbable gas component(s) from a less readily adsorbable gas component(s) of a gas mixture comprising: (a) an adsorption column containing an adsorbent capable of selectively adsorbing the more readily adsorbable gas components from less readily adsorbable gas components of a gas mixture; (b) inlet means for introducing said gas mixture to the adsorption column at an injection point intermediate between the opposite ends of the column; (c) a first, larger, cyclic volume displacement means adapted to impose cyclic gas flow and pressure variations on the gas mixture in said column from a first end portion thereof; (d) a second, smaller, cyclic volume displacement means adapted to impose cyclic gas flow and pressure variations on the gas mixture in said column from the second, opposite end portion thereof, the ratio of the volume displacement produced by said second means to that of said first means being from about 0.15 to about 0.65, said second means being adapted for cyclic operation at a phase angle within the range of from about 30° lag to about 90° lead relative to the cyclic flow and pressure variations of said first means; (e) discharge means for withdrawing a gas stream enriched in one said gas component(s) from the first end of the column; and (f) discharge means for withdrawing a gas stream enriched in the other said gas component(s) from the second end of the column, whereby the cyclic volume displacement means having the indicated relative volume displacements and phase angles cause a gas mixture introduced to the column to pass rapidly back-and-forth within said column, achieving an enhanced separation of the gas mixture and production of the desired product.

Claim 15

An improved apparatus for the pressure swing adsorption separation of a more readily adsorbable gas component(s) from a less readily adsorbable gas component(s) of a gas mixture comprising: (a) an adsorption column containing an adsorbent capable of selectively adsorbing the more readily adsorbable gas components from less readily adsorbable gas components of a gas mixture; (b) inlet means for introducing said gas mixture to the adsorption column at an injection point intermediate between the opposite ends of the column; (c) a first, larger, cyclic volume displacement means adapted to impose cyclic gas flow and pressure variations on the gas mixture in said column from a first end portion thereof; (d) a second, smaller, cyclic volume displacement means adapted to impose cyclic gas flow and pressure variations on the gas mixture in said column from the second, opposite end portion thereof, the ratio of the volume displacement produced by said second means to that of said first means being from about 0.15 to about 0.65, said second means being adapted for cyclic operation at a phase angle within the range of from about 30° lag to about 90° lead relative to the cyclic flow and pressure variations of said first means; (e) discharge means for withdrawing a gas stream enriched in one said gas component(s) from the first end of the column; and (f) discharge means for withdrawing a gas stream enriched in the other said gas component(s) from the second end of the column, whereby the cyclic volume displacement means having the indicated relative volume displacements and phase angles cause a gas mixture introduced to the column to pass rapidly back-and-forth within said column, achieving an enhanced separation of the gas mixture and production of the desired product.

Claim 16

The apparatus of claim 13 in which said volume displacement ratio of said second means to that of said first means is from about 0.25 to about 0.50.

Claim 17

The apparatus of claim 13 in which said second means is adapted for cyclic operation at a phase angle of from about 15° lag to about 75° lead relative to said first means.

Claim 18

The apparatus of claim 15 in which said second means is adapted for cyclic operation at a phase angle of about 30° to about 45° lead.

Claim 19

The apparatus of claim 16 in which said volume displacement ratio of said second means to that of said first means is from about 0.25 to about 0.50.

Claim 20

The apparatus of claim 13 in which said first and second cyclic volume displacement means comprise piston means in fluid communication with each end of the column.

Claim 21

The apparatus of claim 13 in which said first and second cyclic volume displacement means comprise movable diaphragms in fluid communication with each end of the column.