US4654047A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Hybrid membrane/cryogenic process for hydrogen purification
Assignee: Air Products and Chemicals Inc
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Filing: 1985-08-23
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Granted: 1987-03-31
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Expires: 2005-08-23
Abstract
Abstract The present invention involves a process for recovering hydrogen from a feed gas mixture comprising hydrogen and at least one other component. The feed gas mixture is initially separated in a membrane separation unit to produce a hydrogen-rich stream and a hydrogen-lean stream. The hydrogen-lean stream is subsequently treated in a cryogenic separation unit to remove a portion of the non-hydrogen components and produce a hydrogen-enriched stream. The hydrogen-enriched stream from the cryogenic separation unit is recycled and combined with the feed gas mixture to the membrane separation unit.
Inventors
- 👤 Jeffrey A. Hopkins
- 👤 Stephen P. DiMartino
- 👤 David M. Nicholas
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-31 10:50
CPC Classifications
F; F25; F25J; F25J3/00; F25J3/02; F25J3/0204; F25J3/0219; B; B01; B01D; B01D53/00; B01D53/22; B01D53/229; C; C01; C01B; C01B3/00; C01B3/50; C01B3/501; C01B3/506; F25J3/0228; F25J3/0233; F25J3/0252; C01B2203/00; C01B2203/04; C01B2203/046; C01B2203/0465; C01B2203/047; C01B2203/048; C01B2203/0495; F25J2205/00; F25J2205/40; F25J2205/80; F25J2205/82; F25J2210/00; F25J2210/04; F25J2210/12; F25J2245/00; F25J2245/02; Y; Y10; Y10S; Y10S62/00; Y10S62/931
Claims Analysis
Total Claims: 14
Claim 1
Independent Claim
122 words
A process for recovering a purified hydrogen product from a feed gas mixture comprising hydrogen and at least one other component, said process comprising: a. passing said feed gas stream to a membrane separation unit to produce a hydrogen-rich stream and a hydrogen-lean stream; b. passing said hydrogen-lean stream to an auto-refrigerated cryogenic separation unit for treatment and separation to produce a hydrogen deficient stream and a hydrogen-enriched stream having a hydrogen concentration between 80-95 mole %; c. combining the hydrogen-enriched stream with the feed gas stream entering the membrane separation unit; d. recovering the hydrogen-deficient stream; and e. recovering the hydrogen-rich stream from the membrane separation unit as purified hydrogen product having a hydrogen concentration of at least 97 mole %.
Claim 2
Dependent Claim
122 words
A process for recovering a purified hydrogen product from a feed gas mixture comprising hydrogen and at least one other component, said process comprising: a. passing said feed gas stream to a membrane separation unit to produce a hydrogen-rich stream and a hydrogen-lean stream; b. passing said hydrogen-lean stream to an auto-refrigerated cryogenic separation unit for treatment and separation to produce a hydrogen deficient stream and a hydrogen-enriched stream having a hydrogen concentration between 80-95 mole %; c. combining the hydrogen-enriched stream with the feed gas stream entering the membrane separation unit; d. recovering the hydrogen-deficient stream; and e. recovering the hydrogen-rich stream from the membrane separation unit as purified hydrogen product having a hydrogen concentration of at least 97 mole %.
Claim 3
Dependent Claim
29 words
The process in accordance with claim 1 wherein the hydrogen-rich stream produced by the membrane separation unit is the permeate stream and the hydrogen-lean stream is the reject stream.
Claim 4
Dependent Claim
28 words
The process in accordance with claim 2 wherein the feed gas stream is pressurized to at least 200 psi prior to being passed through the membrane separation unit.
Claim 5
Dependent Claim
43 words
The process in accordance with claim 3 wherein the pressure of the hydrogen-enriched stream from the cryogenic separation unit is adjusted to be about equal to the pressure of the feed gas stream entering the membrane separation unit prior to combining said streams.
Claim 6
Dependent Claim
21 words
The process in accordance with claim 4 wherein the feed gas mixture comprises hydrogen at a concentration of at least 70%.
Claim 7
Dependent Claim
24 words
The process in accordance with claim 5 wherein at least 98% of the hydrogen present in the feed is recovered as purified hydrogen product.
Claim 8
Dependent Claim
22 words
The process in accordance with claim 6 wherein the hydrogen-deficient stream recovered from the cryogenic separation unit comprises a medium Btu fuel.
Claim 9
Dependent Claim
31 words
The process in accordance with claim 7 wherein the membrane separation unit comprises a membrane having a higher permeability to H 2 than the other components in the feed gas mixture.
Claim 10
Dependent Claim
32 words
The process in accordance with claim 8 wherein the membrane separation unit contains a membrane selected from the group consisting of cellulose acetate type, polysulfone hollow filter type and polyimide type membranes.
Claim 11
Dependent Claim
37 words
The process in accordance with claim 9 wherein the feed gas mixture is passed through a drying unit to remove H 2 O and/or CO 2 prior to passing said feed gas through the membrane separation unit.
Claim 12
Dependent Claim
41 words
The process in accordance with claim 9 wherein the hydrogen-lean reject stream from the membrane separation unit is passed through a drying unit to remove H 2 O and/or CO 2 prior to passing said stream to the cryogenic separation unit.
Claim 13
Dependent Claim
29 words
The process in accordance with claim 9 wherein the hydrogen-rich stream from the membrane separation unit is treated in a methanation reactor prior to being recovered as hydrogen product.
Claim 14
Dependent Claim
34 words
The process in accordance with claim 12 wherein the hydrogen-rich stream treated in the methanation reactor is subsequently passed to a chiller and separator to remove water prior to being recovered as hydrogen product.
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USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1990-03-30 | 1990-09-29 | 1991-03-31 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1994-03-30 | 1994-09-29 | 1995-03-31 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1998-03-30 | 1998-09-29 | 1999-03-31 | $7700.00 | Window Closed / Lapsed |