US4432774A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Adsorption-desorption process for the recovery of hydrogen
Assignee: Bergwerksverband GmbH
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Filing: 1979-11-09
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Granted: 1984-02-21
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Expires: 1999-11-09
Abstract
Abstract An adsorption-desorption process for the recovery of hydrogen from a feed gas containing trace pollutants adapted to be strongly adsorbed, in concentrations generally below 1% by volume and containing components adapted for only light adsorption, in concentrations above 1% by volume is operated through a preliminary first adsorption stage for the strongly adsorbable trace pollutants and a second main adsorption stage for the light adsorbable components and for the discharge of hydrogen. Contrary to the prior art where the adsorption-desorption was effected by alternating high pressure and low pressure cycles in the main adsorption stage only, the pressure cycles in the present case are carried out both in the preliminary first adsorption stage and in the second main adsorption stage, preferably by arranging the two adsorption states in series. The process substantially extends the service time of the adsorber used in the first adsorption stage.
Inventors
- 👤 Harald Juntgen
- 👤 Karl Knoblauch
- 👤 Jurgen Reichenberger
- 👤 Hans-Jurgen Schroter
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-04 12:21
CPC Classifications
C; C01; C01B; C01B3/00; C01B3/50; C01B3/56; C01B2203/00; C01B2203/04; C01B2203/042; C01B2203/043; C01B2203/0465; C01B2203/047; C01B2203/0475; C01B2203/048
Claims Analysis
Total Claims: 9
Claim 1
Independent Claim
225 words
In a process for the recovery of a purified gas from a feed gas mixture comprising passing the feed gas through successive interconnected adsorbent containing adsorbers and operating the adsorbers for successive adsorption and desorption, the feed gas containing, in addition to the desired gas, trace pollutants strongly adsorbed in concentrations generally below 1% by volume and components lightly adsorbed in concentrations above 1% by volume, said process employing a preliminary first adsorber for the strongly adsorbable trace pollutants and a main adsorber for the lightly adsorbable components, recovering the purified gas from the main adsorber, effecting the desorption by closing the outlet for the purified gas from the main adsorber and passing the gas through reversal of pressure by pressure reduction or evacuation from the main adsorber to the preliminary adsorber and causing the reversal of pressure jointly in said two adsorbers in the same cycle and subjecting said two adsorbers for the same periods of time to the same adsorption and desorption steps, the desorption gas being discharged exclusively from said preliminary adsorber, and shutting off said first adsorber from said main adsorber only after a number of several adsorption/desorption cycles, namely when the first adsorber has reached substantially complete contamination by said strongly adsorbable trace pollutants, whereupon said first adsorber is then subjected to a separate regeneration or replacement of the adsorbent.
Claim 2
Dependent Claim
225 words
In a process for the recovery of a purified gas from a feed gas mixture comprising passing the feed gas through successive interconnected adsorbent containing adsorbers and operating the adsorbers for successive adsorption and desorption, the feed gas containing, in addition to the desired gas, trace pollutants strongly adsorbed in concentrations generally below 1% by volume and components lightly adsorbed in concentrations above 1% by volume, said process employing a preliminary first adsorber for the strongly adsorbable trace pollutants and a main adsorber for the lightly adsorbable components, recovering the purified gas from the main adsorber, effecting the desorption by closing the outlet for the purified gas from the main adsorber and passing the gas through reversal of pressure by pressure reduction or evacuation from the main adsorber to the preliminary adsorber and causing the reversal of pressure jointly in said two adsorbers in the same cycle and subjecting said two adsorbers for the same periods of time to the same adsorption and desorption steps, the desorption gas being discharged exclusively from said preliminary adsorber, and shutting off said first adsorber from said main adsorber only after a number of several adsorption/desorption cycles, namely when the first adsorber has reached substantially complete contamination by said strongly adsorbable trace pollutants, whereupon said first adsorber is then subjected to a separate regeneration or replacement of the adsorbent.
Claim 3
Dependent Claim
23 words
The process of claim 1 wherein the size ratio of the preliminary adsorber to the main adsorber is between about 1:3 and 1:20.
Claim 4
Dependent Claim
46 words
The process of claim 1 wherein at least two groups of adsorption-desorption units are employed, each consisting of a preliminary adsorber and a main adsorber, the two groups being used alternately for adsorption and desorption and the units in each group being operated jointly as defined.
Claim 5
Dependent Claim
22 words
The process of claim 1 wherein the two adsorbers are directly connected by the shortest possible route for both adsorption and desorption.
Claim 6
Dependent Claim
28 words
The process of claim 1 wherein the adsorption is effected at pressures equal to or above 1 bar and the desorption is effected at a substantially lower pressure.
Claim 7
Dependent Claim
31 words
The process of claim 5 wherein the adsorption is effected at a pressure between 5 and 70 bar and the desorption is effected at a pressure between 1 and 0.01 bar.
Claim 8
Dependent Claim
33 words
The process of claim 1 wherein an adsorbent of relatively wide pore size is employed in the preliminary adsorber and an adsorbent with relatively narrow pore size is employed in the main adsorber.
Claim 9
Dependent Claim
42 words
The process of claim 7 wherein the adsorbent employed in the preliminary adsorber has a mean adsorption pore diameter of 0.6 to 2.0 nm and the adsorbent employed in the main adsorber has a mean adsorption pore size of below 0.6 nm.
References Cited (Backward Citations)
US2340398A
Cited
US2918140A
Cited
US3150942A
Cited
US3221476A
Cited
US3237379A
Cited
US3252268A
Cited
US3225516A
Cited
US3720042A
Cited
US3719025A
Cited
US3923477A
Cited
US3957463A
Cited
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1987-02-20 | 1987-08-22 | 1988-02-21 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1991-02-20 | 1991-08-22 | 1992-02-21 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1995-02-20 | 1995-08-22 | 1996-02-21 | $7700.00 | Window Closed / Lapsed |