Methods of treating a gaseous mixture of adsorption

Claim 1

A method of treating a gaseous mixture by adsorption which employs the selective arrest of at least one component of said gaseous mixture, using three adsorbent beds and a buffer container, comprising performing sequentially the following cycle relating to a first bed of said beds: (a) a high pressure phase extending over a first third of said cycle, during which a treated gas is withdrawn which results from passing the said mixture through a first adsorbent bed in a direction termed the production direction at virtually constant high production pressure, (b) a regeneration phase of said first adsorbent bed extending over a second third of said cycle consisting firstly of a de-pressurization phase from the high production pressure to a low regeneration pressure, said de-pressurization phase including two successive balancing operations firstly between said first adsorbent bed and a second adsorbent bed and secondly between said first adsorbent bed and said buffer chamber each of said balancing operations being effected with outfeed in the production direction and infeed in the opposite direction and a continuous removal of gas in the opposite direction from the production direction during the whole duration of said de-pressurization phase on one hand and finally of a cleaning phase at said low regeneration pressure which is performed by passing gas from said buffer chamber through said first adsorbent bed in the opposite direction from the direction of production, (c) a re-pressurization phase extending over a third of said cycle, consisting of a balancing between said first adsorbent bed and a third adsorbent bed which is at the beginning of its regeneration phase, in the opposite direction from the direction of production, and a continuous introducing of treated gas in the direction opposite the direction of production, extending over the whole duration of said re-pressurization phase, repeating said cycle for each of said three adsorbent beds in sequence with a stagger of a third of a cycle, introducing said mixture into said beds in sequence at a constant rate and pressure throughout said cycle, removing said treated gas from said beds in sequence at a substantially constant rate and pressure throughout said cycle, and removing from said beds in sequence, at a rate and pressure that are substantially constant throughout said cycle, gas that has passed through said beds in said opposite direction from the production direction.

Claim 2

A method of treating a gaseous mixture by adsorption which employs the selective arrest of at least one component of said gaseous mixture, using three adsorbent beds and a buffer container, comprising performing sequentially the following cycle relating to a first bed of said beds: (a) a high pressure phase extending over a first third of said cycle, during which a treated gas is withdrawn which results from passing the said mixture through a first adsorbent bed in a direction termed the production direction at virtually constant high production pressure, (b) a regeneration phase of said first adsorbent bed extending over a second third of said cycle consisting firstly of a de-pressurization phase from the high production pressure to a low regeneration pressure, said de-pressurization phase including two successive balancing operations firstly between said first adsorbent bed and a second adsorbent bed and secondly between said first adsorbent bed and said buffer chamber each of said balancing operations being effected with outfeed in the production direction and infeed in the opposite direction and a continuous removal of gas in the opposite direction from the production direction during the whole duration of said de-pressurization phase on one hand and finally of a cleaning phase at said low regeneration pressure which is performed by passing gas from said buffer chamber through said first adsorbent bed in the opposite direction from the direction of production, (c) a re-pressurization phase extending over a third of said cycle, consisting of a balancing between said first adsorbent bed and a third adsorbent bed which is at the beginning of its regeneration phase, in the opposite direction from the direction of production, and a continuous introducing of treated gas in the direction opposite the direction of production, extending over the whole duration of said re-pressurization phase, repeating said cycle for each of said three adsorbent beds in sequence with a stagger of a third of a cycle, introducing said mixture into said beds in sequence at a constant rate and pressure throughout said cycle, removing said treated gas from said beds in sequence at a substantially constant rate and pressure throughout said cycle, and removing from said beds in sequence, at a rate and pressure that are substantially constant throughout said cycle, gas that has passed through said beds in said opposite direction from the production direction.