Selective adsorption process
AssigneeUnion Carbide Corporation
InventorsAndrija Fuderer, Ernst Rudelstorfer
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Abstract
In an adiabatic pressure swing process for separation of feed gas mixtures such as H.sub.2 containing CO.sub.2 and N.sub.2 impurities, at least seven adsorbent beds are employed of which at least two are receiving feed gas during the entire cycle, and with at least three pressure equalization stages.
Claims5
In an adiabatic pressure swing process for separation of gas mixtures by selectively adsorbing at least one gas component in each of multiple adsorbent beds by the cycle of introducing feed gas mixture to the bed inlet end at first highest superatmospheric pressure, discharging unadsorbed product effluent from the bed discharge end, releasing initial void space gas from the bed discharge end and introducing the so-released initial gas to the discharge end of another adsorbent bed previously purged of said one component and initially at lower pressure until the two beds are pressure equalized at higher intermediate pressure, releasing gas from the bed inlet end for countercurrent blowdown to lowest pressure, introducing one-component depleted gas from another adsorbent bed to the bed discharge end for desorption of said one component and purging through the bed inlet end, repressurizing the purged bed to said first highest superatmospheric pressure and thereafter repeating the cycle, the improvement comprising at least seven adsorbent beds;
- simultaneously introducing feed gas mixture to the inlet ends of at least two adsorbent beds in overlapping identical cycles sequentially from the first to the highest numbered bed and thereafter continuously repeating the sequence such that during the initial period of a bed adsorption step the immediately preceding lower numbered bed is also on its adsorption step and during the last period the immediately following higher numbered bed is also on its adsorption step;
- performing the initial void space gas releasing-pressure equalization in at least three separate phases comprising first pressure equalizing the adsorbent bed having completed its one component adsorption step, with a different previously purged and at least third higher numbered bed initially at lower intermediate pressure so that the two beds are finally at a first equalization pressure;
- second pressure equalizing the one component-containing adsorbent bed initially at said first equalization pressure with a still different previously purged and at least fourth higher numbered bed initially at still lower intermediate pressure so that the two beds are finally at a second equalization pressure;
- third pressure equalizing the one component-containing adsorbent bed initially at said second equalization pressure with another previously purged and at least fifth higher numbered bed initially at lowest pressure so that the two beds are finally at a third equalization pressure.
In an adiabatic pressure swing process for separation hydrogen-rich mixtures by selectively adsorbing at least one component other than hydrogen in each of multiple adsorbent beds by the cycle of introducing feed gas mixture to the bed inlet end at first highest superatmospheric pressure, discharging unadsorbed hydrogen product effluent from the bed discharge end, releasing initial void space gas from the bed discharge end and introducing the so-released initial gas to the discharge end of another adsorbent bed previously purged of said one component and initially at lower pressure until the two beds are pressure equalized at higher intermediate pressure, releasing further void space gas from the bed discharge end for cocurrent depressurization thereof to lower intermediate pressure, releasing gas from the bed inlet end for countercurrent blowdown to lowest pressure, introducing one-component depleted gas from another adsorbent bed to the bed discharge end for desorption of said one component and purging through the bed inlet end, repressurizing the purged bed to said first highest superatmospheric pressure and thereafter repeating the cycle:
- the improvement comprising providing at least nine adsorbent beds;
- simultaneously introducing hydrogen-rich feed gas mixture to the inlet ends of three adsorbent beds in overlapping identical cycles sequentially from the first to the highest numbered bed and thereafter continuously repeating the sequence such that during the initial period of a bed adsorption step the two immediately preceding lower numbered beds are also on their adsorption steps, during the middle period of a bed adsorption step the immediately preceding lower numbered and immediately following higher numbered beds are also on their adsorption steps, and during the last period of a bed adsorption step the two immediately following higher numbered beds are also on their adsorption steps;
- performing the initial void space gas releasing pressure equalization in three separate phases comprising first pressure equalizing an adsorbent bed having completed its one component adsorption step with the fourth higher numbered adsorbent bed initially at a second equalization pressure so that the two beds are finally at a first equalization pressure, second pressure equalizing said adsorbent bed with the fifth higher numbered adsorbent bed initially at a third equalization pressure so that the two beds are finally at said second equalization pressure, and third pressure equalizing said adsorbent bed with the sixth higher numbered adsorbent bed initially at said lowest pressure so that the two beds are finally at said third equalization pressure;
- further void space gas from said adsorbent bed initially at said third equalization pressure and introducing at least part of said gas to the discharge end of the eighth higher numbered adsorbent for desorption of said one component and purging at said lowest pressure;
- and thereafter conducting said countercurrent blowdown and purging steps in said adsorbent bed;
- said steps being performed such that the absolute pressure ratio (PR) of the first highest superatmospheric pressure of the adsorption step to said lowest pressure of the process is at least 7, and the product of PR times the molar ratio (S) of the non-adsorbates in the adsorbent bed at the end of the adsorption step to the total feed gas introduced during the adsorption step is at least 6.
Dependencies are inferred from the claim text.