Process for the production of oxygen by adsorption with transatmospheric pressure variation

Claim 2

A process for the production of oxygen from air by adsorption, in at least one unit comprising two adsorbers, where there is carried out in each adsorber a cycle comprising the following successive steps: a1) countercurrent repressurization to an intermediate pressure with at least one gas coming directly from the other adsorber subject to a first co-current depressurization; a2) co-current repressurization by air, terminating by a sub-step of production at an upper pressure of the cycle during which product gas is withdrawn from the adsorber and sent to a non-segregated product gas capacity; b) a first co-current decompression step with simultaneous counter-current and co-current withdrawal of gas from the adsorber, the gas withdrawn co-currently being sent directly to the other adsorber in the course of step a1); c) a countercurrent purge step to a low pressure of the cycle; and d) a purge/elution step in which production gas is introduced countercurrently into the adsorber which is subjected simultaneously to countercurrent evacuation.

Claim 3

The process of claim 1 , wherein during step b) counter-current gas withdrawal is achieved by pumping.

Claim 4

The process of claim 1 , wherein during step a1) product gas is also introduced countercurrently into the adsorber.

Claim 5

The process of claim 3 , wherein during step a1) the two gases are introduced simultaneously during all the duration of step a1).

Claim 6

The process of claim 3 , wherein during an initial portion of the production sub-step, the product gas is sent to an auxiliary tank.

Claim 7

The process of claim 1 , wherein during all the production sub-step, product gas is sent to at least one tank (C 1 ; C 1 , C 2 ).

Claim 8

The process of claim 1 , wherein during step b) the gas withdrawn countercurrently is vented to the atmosphere.

Claim 9

A process for the production of oxygen product from air by adsorption with transatmospheric pressure variation, in at least one unit comprising two adsorbers, where there is carried out in each adsorber a cycle comprising, successively and cyclically: a repressurization phase to a high pressure of the cycle, comprising the following successive steps: a1) repressurization with countercurrent introduction of gas from the other adsorber subject to depressurization and of oxygen product; a2) co-current repressurization by air, terminating by a sub-step of production during which product gas is withdrawn from the adsorber and sent to at least one non-segregated product gas capacity; and an immediately subsequent regeneration phase comprising the following successive steps: b) a first co-current decompression step with simultaneous counter-current and co-current withdrawal of gas from the adsorber, the gas withdrawn co-currently being sent directly to the other adsorber in the course of step a1); c) a countercurrent purge step to a low pressure of the cycle; and d) a purge/elution step with countercurrent introduction of oxygen product.

Claim 10

A process for the production of oxygen product from air by adsorption with transatmospheric pressure variation, in at least one unit comprising two adsorbers, where there is carried out in each adsorber a cycle comprising, successively and cyclically: a repressurization phase to a high pressure of the cycle, comprising the following successive steps: a1) repressurization with countercurrent introduction of gas from the other adsorber subject to depressurization and of oxygen product; a2) co-current repressurization by air, terminating by a sub-step of production during which product gas is withdrawn from the adsorber and sent to at least one non-segregated product gas capacity; and an immediately subsequent regeneration phase comprising the following successive steps: b) a first co-current decompression step with simultaneous counter-current and co-current withdrawal of gas from the adsorber, the gas withdrawn co-currently being sent directly to the other adsorber in the course of step a1); c) a countercurrent purge step to a low pressure of the cycle; and d) a purge/elution step with countercurrent introduction of oxygen product.

Claim 11

Process according to claim 8 , wherein the duration of the cycle does not exceed 120 seconds.

Claim 12

Process according to claim 9 , wherein the duration of the cycle does not exceed 80 seconds.

Claim 13

The process of claim 8 , wherein during step a1) the two gases are introduced simultaneously during all the duration of step a1).

Claim 14

The process of claim 8 , wherein during all the production sub-step, the oxygen product is sent to at least one tank. introduction of oxygen product.

Claim 15

The process of claim 8 , wherein during an initial portion of the production sub-step, the oxygen product is sent to an auxiliary tank.

Claim 16

The process of claim 8 , wherein during at least part of step b) the gas withdrawn countercurrent is vented to the atmosphere.

Claim 17

A process for the production of a product gas separated from a feed mixture by adsorption with transatmospheric pressure variation, in a unit comprising at least one pair of adsorbers, where there is carried out in each adsorber of the pair a cycle comprising the following successive steps: a1) countercurrent repressurization with gas from a first co-current depressurization in the other adsorber of the pair, and product gas from a non-segregated product gas tank; a2) co-current repressurization by the feed mixture, terminating by a sub-step of production in which product gas is withdrawn from the adsorber and sent to the non-segregated product gas tank; b) a first co-current decompression step with simultaneous counter-current and co-current withdrawal of gas from the adsorber, the gas withdrawn co-currently being sent directly to the other adsorber of the pair in the course cf step a1); c) a countercurrent purge step comprising a pumping to a low pressure of the cycle; and d) a purge/elution step with countercurrent introduction of product gas and simultaneous countercurrent pumping.

Claim 18

A process for the production of a product gas separated from a feed mixture by adsorption with transatmospheric pressure variation, in a unit comprising at least one pair of adsorbers, where there is carried out in each adsorber of the pair a cycle comprising the following successive steps: a1) countercurrent repressurization with gas from a first co-current depressurization in the other adsorber of the pair, and product gas from a non-segregated product gas tank; a2) co-current repressurization by the feed mixture, terminating by a sub-step of production in which product gas is withdrawn from the adsorber and sent to the non-segregated product gas tank; b) a first co-current decompression step with simultaneous counter-current and co-current withdrawal of gas from the adsorber, the gas withdrawn co-currently being sent directly to the other adsorber of the pair in the course cf step a1); c) a countercurrent purge step comprising a pumping to a low pressure of the cycle; and d) a purge/elution step with countercurrent introduction of product gas and simultaneous countercurrent pumping.