초록 ▼

An adsorptive separation process of the present invention relates to a process for separating hydrogen and/or helium by a pressure swing adsorption process using four or more adsorbent beds. Each adsorbent bed manipulates the individual steps of adsorption, equal depressurization, cocurrent depressu

An adsorptive separation process of the present invention relates to a process for separating hydrogen and/or helium by a pressure swing adsorption process using four or more adsorbent beds. Each adsorbent bed manipulates the individual steps of adsorption, equal depressurization, cocurrent depressurization, countercurrent depressurization, purging, equal pressurization, product pressurization and raw gas pressurization while sequentially switching them and carries out the raw gas pressurization step for applying pressure with raw gas as the final step for pressuring the adsorbent bed to the adsorbent pressure. Accordingly, a variation in pressure and flow rate can be suppressed, product can be attained stably, and the amount of product can be increased.

대표청구항 ▼

An adsorptive separation process for separating hydrogen and/or helium as product by a pressure swing adsorption process, characterized in that four or more adsorbent beds have a raw gas inlet end and a product gas discharge end and have an interior filled with an adsorbent; and that said process se

An adsorptive separation process for separating hydrogen and/or helium as product by a pressure swing adsorption process, characterized in that four or more adsorbent beds have a raw gas inlet end and a product gas discharge end and have an interior filled with an adsorbent; and that said process sequentially executes: (a) an adsorption step for permitting raw gas to flow in the first adsorbent bed from said inlet end thereof under a constant highest pressure, causing said adsorbent to hold an easy adsorptive component, extracting an unadsorbed component as product gas from said product gas discharge end and completing flow of said raw gas when an adsorption front is at a middle of said first adsorbent bed; (b) an equal depressurization step for discharging part of gas in said first adsorbent bed under said highest pressure from said product gas discharge end of said first adsorbent bed in a direction cocurrent to flow of said raw gas, and permitting said discharged gas to flow through said product gas discharge end of the second adsorbent bed which has been purified so as to eliminate an easy adsorptive component and is under a lowest pressure or low pressure set in advance by pressure equalization to cause said first and second adsorbent beds to have intermediate pressure; (c) a cocurrent depressurization step for further discharging gas in said first adsorbent bed, which substantially consists of an unadsorbed component, from said product gas discharge end of said first adsorbent bed in a direction cocurrent to flow of said raw gas, further throttling pressure of said discharged gas to a lowest pressure for depressurization, permitting said cocurrent depressurized gas to flow through said product gas discharge end of the third adsorbent bed holding an easy adsorptive component and continuing said discharging until pressure of said first adsorbent bed becomes lower intermediate pressure lower than said intermediate pressure and when said easy adsorptive component of said third adsorbent bed is purged or is at least partially removed; (d) a countercurrent depressurization step for discharging gas present in said first adsorbent bed under said low pressure formed by pressure equalization executed with respect to said third adsorbent bed already purged to be under said lowest pressure, from said raw gas inlet end in a direction countercurrent to flow of said raw gas to thereby countercurrently desorb said easy adsorptive component held by said adsorbent of said first adsorbent bed, and continuing said discharging until said first adsorbent bed has said lowest pressure; (e) a purging step for throttling cocurrent depressurized gas from the fourth adsorbent bed to have said lowest pressure, introducing said gas to said product gas discharge end of said first adsorbent bed and permitting said gas to flow within said first adsorbent bed in a direction countercurrent to flow of said raw gas to thereby desorb at least part of said easy adsorptive component held by said adsorbent of said first adsorbent bed, and discharging said at least part of said easy adsorptive component in accompaniment with said cocurrent depressurized gas from said fourth adsorbent bed from said raw gas inlet end of said first adsorbent bed for purgation; (f) an equal pressurization step for introducing gas present under said highest pressure in said second adsorbent bed which has undergone said adsorption step, to said product gas discharge end of said first adsorbent bed purged to be under said lowest pressure immediately or after pressure is increased to low pressure by pressure equalization executed with respect to said fourth adsorbent bed which have already undergone cocurrent depressurization to be under said lower intermediate pressure, and increasing pressure of said first adsorbent bed until said first and second adsorbent beds are equalized to have said intermediate pressure; (g) a product pressurization step for introducing part of product gas under said highest pressure flowing from said third adsorbent bed or another adsorbent bed to said product gas discharge end of said first adsorbent bed during or upon completion of said equal pressurization step to thereby increase pressure of said first adsorbent bed to higher intermediate pressure greater than said intermediate pressure but lower than said highest pressure; and (h) a raw gas pressurization step for introducing said raw gas to said raw gas inlet end of said first adsorbent bed whose pressure has been increased to said higher intermediate pressure, to thereby increase pressure of said first adsorbent bed to said highest pressure, while said third adsorbent bed or another adsorbent bed is executing said adsorption step; so that said raw gas is permitted to flow in said repressurized first adsorbent bed, and after returning to said adsorption step to extract hydrogen and/or helium as product gas from said discharge end, by pressure substantially equal to that of raw gas, and the variation of product gas flow rate is within a range of ±5%, said individual steps are thereafter continuously repeated, and a process of said individual steps is sequentially executed for said second adsorbent bed, third adsorbent bed and fourth adsorbent bed, and other adsorbent beds if there are more adsorbent beds.