US5004592A
Expired / Lapsed
US
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Steam reforming process
Assignee: Imperial Chemical Industries Ltd
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Filing: 1988-05-23
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Granted: 1991-04-02
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Expires: 2008-05-23
Abstract
Abstract The endothermic reaction of a hydrocarbon feedstock with steam and/or carbon dioxide is carried out using a double-tube reactor. In one preferred form of the reactor the catalyst is present as a coating on the outside of the inner tube. In another form inner tubes are mounted in one tube-plate and the outer tubes in a second tube plate and the tube plates are disposed across a cylindrical shell so as to define a heat exchange zone (provided with a heat source) a reactants feed zone and a products offtake zone. The heat source is preferably a burner, to be fed with the product of the endothermic reaction, followed by a secondary reforming catalyst. The apparatus makes possible processes for making raw hydrogen-containing gases with advantageous internal heat recovery.
Inventors
- 👤 Alwyn Pinto
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-03 12:08
CPC Classifications
B; B01; B01J; B01J19/00; B01J19/24; B01J19/2415; B01J19/2425; B01J12/00; B01J12/005; B01J8/00; B01J8/02; B01J8/06; B01J8/062; C; C01; C01B; C01B3/00; C01B3/02; C01B3/025; B01J2208/00; B01J2208/00008; B01J2208/00017; B01J2208/00106; B01J2208/00168; B01J2208/00185; B01J2208/00212; B01J2208/00796; B01J2208/00823; B01J2208/00831; B01J2208/00849; B01J2219/00; B01J2219/00049; B01J2219/00051; B01J2219/00074; B01J2219/00076; B01J2219/00078; B01J2219/00085; B01J2219/00087; B01J2219/00094
Claims Analysis
Total Claims: 4
Claim 1
Independent Claim
235 words
In a process for producing raw ammonia synthesis gas by the steps of: (a) primary reforming a hydrocarbon feedstock with seam to give a gas containing carbon oxides, hydrogen, methane and unreacted steam by passing a mixture of the feedstock and steam over a heated catalyst; (b) reacting the product of step (a) catalytically with an oxygen/nitrogen mixture to decease the content of methane and introduce nitrogen; and (c) obtaining the endothermic heat required for step (a), part from the hot effluent of step (b) and part from an external heat supply means, by carrying out step (a) in a first stage giving a partially primary reformed gas which is then subjected to further primary reforming in a second stage, with one of the stages being heated from an external heat supply means and the other stage heated by the hot effluent of step (b); the improvement comprising effecting the first stage of step (a) by passing a mixture of the hydrocarbon feedstock and steam over a catalyst, heating the catalyst by indirect heat exchange with both the hot effluent of step (b) and the partially primary reformed gas produced in the first stage, thereby cooling both the hot effluent from stage (b) and the partially reformed gas, and then passing the resusltant cooled partially primary reformed gas to the second stage of step (a), heating the second stage using the external heat supply means.
Claim 2
Dependent Claim
235 words
In a process for producing raw ammonia synthesis gas by the steps of: (a) primary reforming a hydrocarbon feedstock with seam to give a gas containing carbon oxides, hydrogen, methane and unreacted steam by passing a mixture of the feedstock and steam over a heated catalyst; (b) reacting the product of step (a) catalytically with an oxygen/nitrogen mixture to decease the content of methane and introduce nitrogen; and (c) obtaining the endothermic heat required for step (a), part from the hot effluent of step (b) and part from an external heat supply means, by carrying out step (a) in a first stage giving a partially primary reformed gas which is then subjected to further primary reforming in a second stage, with one of the stages being heated from an external heat supply means and the other stage heated by the hot effluent of step (b); the improvement comprising effecting the first stage of step (a) by passing a mixture of the hydrocarbon feedstock and steam over a catalyst, heating the catalyst by indirect heat exchange with both the hot effluent of step (b) and the partially primary reformed gas produced in the first stage, thereby cooling both the hot effluent from stage (b) and the partially reformed gas, and then passing the resusltant cooled partially primary reformed gas to the second stage of step (a), heating the second stage using the external heat supply means.
Claim 3
Dependent Claim
63 words
In a process according to claim 1, the further improvement comprising, before passing the cooled partially reformed gas to the second stage of step (a), further cooling the cooled partially primary reformed gas from the first stage of step (a) by indirect heat exchange with the mixture of feedstock and steam before the latter is fed to the first stage of step (a).
Claim 4
Dependent Claim
53 words
In a process according to claim 1, the further improvement comprising preheating the cooled partially reformed gas from the first stage of step (a) by indirect heat exchange with the reformed gas from the second stage of step (a) before that partially reformed gas is fed to the second stage of step (a).
References Cited (Backward Citations)
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1994-04-01 | 1994-10-01 | 1995-04-02 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1998-04-01 | 1998-10-01 | 1999-04-02 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 2002-04-01 | 2002-10-01 | 2003-04-02 | $7700.00 | Window Closed / Lapsed |