US3699218A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Hydrogen manufacture
Assignee: Chevron USA Inc
•
Filing: 1970-06-12
•
Granted: 1972-10-17
•
Expires: 1990-06-12
Abstract
Abstract Process for obtaining high purity, high pressure hydrogen wherein hydrogen-rich gas containing carbon dioxide and carbon monoxide is centrifugally compressed to high pressure, the carbon dioxide is then removed from the high pressure hydrogen-rich gas by absorption at low temperature to obtain a high pressure, low temperature hydrogen-rich gas containing carbon monoxide and then the carbon monoxide is removed from the hydrogen-rich gas by adsorption at low temperature and high pressure.
Inventors
- 👤 Calvin S Smith
- 👤 William J Mcleod
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-03 19:31
CPC Classifications
C; C01; C01B; C01B3/00; C01B3/50; C01B3/52; C01B3/02; C01B3/32; C01B3/34; C01B3/36; C01B3/48; C01B3/506; C01B2203/00; C01B2203/02; C01B2203/0205; C01B2203/0227; C01B2203/0233; C01B2203/025; C01B2203/0283; C01B2203/04; C01B2203/0415; C01B2203/042; C01B2203/0435; C01B2203/045; C01B2203/0465; C01B2203/047; C01B2203/0475; C01B2203/0485; C01B2203/08; C01B2203/0872; C01B2203/0883; C01B2203/12; C01B2203/1205; C01B2203/1211; C01B2203/1235; C01B2203/1241; C01B2203/14; C01B2203/146
Claims Analysis
Total Claims: 4
Claim 1
Independent Claim
60 words
A process as in claim 1 wherein the low temperature, hydrogen-rich, carbon dioxide-lean gas is cooled to a temperature between minus 200* F. and minus 100* F. prior to removing carbon monoxide by adsorption and wherein the adsorbent used to adsorb carbon monoxide is selected from the group consisting of charcoal, sodium zeolite X, sodium zeolite A, or silica gel.
Claim 2
Dependent Claim
21 words
A process as in claim 1 wherein the raw, hydrogen-rich gas is compressed to a pressure between 1,200 and 2,000 psig.
Claim 3
Dependent Claim
177 words
A process for obtaining high pressure, high purity hydrogen which comprises: a. generating a hydrogen-rich gas comprising hydrogen, carbon dioxide and carbon monoxide and containing sufficient carbon dioxide so that the molecular weight of the hydrogen-rich gas is at least four, b. centrifugally compressing the hydrogen-rich gas to a pressure above 900 psig to obtain high pressure hydrogen-rich gas, c. removing carbon dioxide from the high pressure hydrogen-rich gas by low temperature absorption of carbon dioxide into a methanol absorbent chilled to between 0* F. and minus 120* F. to obtain low-temperature hydrogen-rich carbon dioxide-lean gas at a temperature between minus 100* F. and 32* F., and containing between 0.5 and 4.0 volume percent carbon monoxide, and d. removing carbon monoxide from the low temperature hydrogen-rich gas at a temperature between minus 100* F. and minus 200* F. by carbon monoxide adsorption using a carbon monoxide adsorbent selected from the group consisting of charcoal, sodium zeolite X, sodium zeolite A, or silica gel, to obtain high purity hydrogen gas containing less than 0.01 volume percent carbon monoxide.
Claim 4
Dependent Claim
35 words
A process as in claim 4 wherein sufficient carbon monoxide is removed from the hydrogen-rich gas by carbon monoxide adsorption to obtain a high purity hydrogen gas containing less than 0.005 volume percent carbon monoxide.
References Cited (Backward Citations)
US2882244A
Cited
US2882243A
Cited
US3011589A
Cited
US3271110A
Cited
US3251652A
Cited
US3266219A
Cited
US3361534A
Cited
US3377138A
Cited
US3401111A
Cited
US3463603A
Cited
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1975-10-17 | 1976-04-17 | 1976-10-17 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1979-10-17 | 1980-04-17 | 1980-10-17 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1983-10-17 | 1984-04-17 | 1984-10-17 | $7700.00 | Window Closed / Lapsed |