Claims Analysis
Total Claims: 11
Claim 1
Independent Claim
235 words
In the production of a binary gas mixture of desired fixed proportions of components from a starting feed gas containing such components, the method which comprisees the steps of (a) passing the feed gas at superatmospheric pressure into a bed of solid adsorbent preferentially selective in retention of a first of said components, while discharging from said bed as primary effluent a stream consisting essentially of the unadsorbed or less selectively adsorbed second component; (b) while said bed is at about the aforesaid superatmospheric pressure, discontinuing said feed gas introduction and rinsing the bed, in a direction co-current to that of the feed gas introduction, with a gas stream rich in said preferentially retained first component; (c) withdrawing contained gas from said bed until said bed is depressurized to about a pressure level P and compressing at least a part of the gas so withdrawn to about superatmospheric level for use as rinsing gas in step (b); (d) while at about said pressure level of P, purging the bed with a controlled amount of the gas discharged as primary effluent during step (a), thereby producing a purge effluent as the binary gas mixture of desired fixed proportions of components; and thereafter (e) repressuring the bed to the initial superatmospheric pressure level of step (a) for repetition of the recited sequence of steps, said repressuring being effected with part of the primary effluent from step (a).
Claim 2
Dependent Claim
235 words
In the production of a binary gas mixture of desired fixed proportions of components from a starting feed gas containing such components, the method which comprisees the steps of (a) passing the feed gas at superatmospheric pressure into a bed of solid adsorbent preferentially selective in retention of a first of said components, while discharging from said bed as primary effluent a stream consisting essentially of the unadsorbed or less selectively adsorbed second component; (b) while said bed is at about the aforesaid superatmospheric pressure, discontinuing said feed gas introduction and rinsing the bed, in a direction co-current to that of the feed gas introduction, with a gas stream rich in said preferentially retained first component; (c) withdrawing contained gas from said bed until said bed is depressurized to about a pressure level P and compressing at least a part of the gas so withdrawn to about superatmospheric level for use as rinsing gas in step (b); (d) while at about said pressure level of P, purging the bed with a controlled amount of the gas discharged as primary effluent during step (a), thereby producing a purge effluent as the binary gas mixture of desired fixed proportions of components; and thereafter (e) repressuring the bed to the initial superatmospheric pressure level of step (a) for repetition of the recited sequence of steps, said repressuring being effected with part of the primary effluent from step (a).
Claim 3
Dependent Claim
18 words
The method as defined in claim 1 wherein said starting feed gas contains principally hydrogen and carbon monoxide.
Claim 4
Dependent Claim
25 words
The method as defined in claim 2 wherein said starting feed gas is one consisting essentially of hydrogen and carbon monoxide in substantially equal proportions.
Claim 5
Dependent Claim
30 words
The method as defined in claim 2 wherein said starting feed gas is one derived from a steam methane reforming product, from which product contained carbon dioxide was first removed.
Claim 6
Dependent Claim
28 words
The method as defined in claim 2 wherein said method is practiced in a PSA system comprising a plurality of such beds of solid adsorbent operated in parallel.
Claim 7
Dependent Claim
16 words
The method as defined in claim 2 wherein the pressure level P is between 0-20 psig.
Claim 8
Dependent Claim
54 words
The method as defined in claim 1 wherein said preferentially adsorbed component is carbon monoxide and said unadsorbed second component consists essentially of hydrogen, and the controlled amount of said second component employed in step (d) is that resulting in a purge effluent comprising about 0.5-2.5 moles of hydrogen per mole of carbon monoxide.
Claim 9
Dependent Claim
17 words
The method as defined in claim 1 wherein said starting feed gas contains principally hydrogen and nitrogen.
Claim 10
Dependent Claim
21 words
The method as defined in claim 1 wherein the purge of step (d) is countercurrent to the feed of step (a).
Claim 11
Dependent Claim
17 words
The method as defined in claim 1 wherein the pressure P of step (c) is ambient pressure.