US4224299A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Combination chemical plant and Brayton-cycle power plant
Assignee: Texaco Inc
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Filing: 1978-11-02
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Granted: 1980-09-23
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Expires: 1998-11-02
Abstract
Abstract A chemical plant, wherein gaseous reactants are converted in an exothermic chemical reaction to a reaction product, is combined with a semi-closed Brayton-cycle power plant to utilize the heat of reaction to generate power. Specifically, in one embodiment, an ammonia synthesis plant, wherein gaseous nitrogen and hydrogen are catalytically converted to ammonia, is combined with a semi-closed Brayton-cycle power plant to utilize the heat of reaction of the ammonia synthesis reaction to generate power.
Inventors
- 👤 Everett M. Barber
- 👤 James R. Muenger
- 👤 David L. Alexander
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-27 05:41
CPC Classifications
F; F02; F02C; F02C6/00; F02C6/04; F02C6/10; C; C01; C01C; C01C1/00; C01C1/02; C01C1/04; C01C1/0405; C01C1/0488; F02C1/00; F02C1/04; F02C1/08; Y; Y02; Y02P; Y02P20/00; Y02P20/50; Y02P20/52
Claims Analysis
Total Claims: 6
Claim 1
Independent Claim
196 words
In a process wherein gaseous hydrogen and nitrogen are supplied to and reacted with one another in a reaction zone, wherein they undergo exothermic reaction to produce ammonia at an elevated temperature and pressure, the resulting ammonia is separated and recovered from unconverted gaseous hydrogen and nitrogen at substantially reaction pressure and at reduced temperature in a separation zone and unconverted gaseous hydrogen and nitrogen are recycled to the reaction zone and fresh feed gaseous hydrogen and nitrogen are supplied to said reaction zone, the improvement which comprises passing said gaseous reaction product ammonia admixed with unconverted gaseous reactants directly from said reaction zone at said elevated temperature and pressure into indirect heat exchange with relatively cooler unconverted gaseous reactants from said separation zone in a first heat exchange zone, thereby heating said unconverted gaseous reactants, further heating resulting unconverted gaseous reactants to a temperature higher than said reaction zone temperature by indirect heat exchange with a heating medium in a second heat exchange zone, thereafter expanding resulting heated unconverted reactants in a heat engine with the production of power therefrom, cooling and recompressing said reactants and supplying said recompressed unconverted reactants to said reaction zone.
Claim 2
Dependent Claim
196 words
In a process wherein gaseous hydrogen and nitrogen are supplied to and reacted with one another in a reaction zone, wherein they undergo exothermic reaction to produce ammonia at an elevated temperature and pressure, the resulting ammonia is separated and recovered from unconverted gaseous hydrogen and nitrogen at substantially reaction pressure and at reduced temperature in a separation zone and unconverted gaseous hydrogen and nitrogen are recycled to the reaction zone and fresh feed gaseous hydrogen and nitrogen are supplied to said reaction zone, the improvement which comprises passing said gaseous reaction product ammonia admixed with unconverted gaseous reactants directly from said reaction zone at said elevated temperature and pressure into indirect heat exchange with relatively cooler unconverted gaseous reactants from said separation zone in a first heat exchange zone, thereby heating said unconverted gaseous reactants, further heating resulting unconverted gaseous reactants to a temperature higher than said reaction zone temperature by indirect heat exchange with a heating medium in a second heat exchange zone, thereafter expanding resulting heated unconverted reactants in a heat engine with the production of power therefrom, cooling and recompressing said reactants and supplying said recompressed unconverted reactants to said reaction zone.
Claim 3
Dependent Claim
220 words
In a process wherein gaseous hydrogen and nitrogen are supplied to and reacted with one another in a reaction zone, wherein they undergo exothermic reaction to produce ammonia at an elevated temperature and pressure, the resulting ammonia is separated and recovered from unconverted gaseous hydrogen and nitrogen at substantially reaction pressure and at reduced temperature in a separation zone and unconverted gaseous hydrogen and nitrogen are recycled to the reaction zone and fresh feed gaseous hydrogen and nitrogen are supplied to said reaction zone, the improvement which comprises passing said gaseous reaction product ammonia admixed with unconverted gaseous reactants directly from said reaction zone at said elevated temperature and pressure into indirect heat exchange with relatively cooler unconverted gaseous reactants from said separation zone in a first heat exchange zone, thereby heating said unconverted gaseous reactants, further heating resulting unconverted gaseous reactants to a temperature higher than said reaction zone temperature by indirect heat exchange with a heating medium in a second heat exchange zone, thereafter expanding resulting heated unconverted reactants in a heat engine with the production of power therefrom, cooling and recompressing said reactants and supplying said recompressed unconverted reactants to said reaction zone, a portion of the unconverted gaseous reactants from the separation step being recycled directly to said reaction zone, thus by-passing the heat exchange zones.
Claim 4
Dependent Claim
220 words
In a process wherein gaseous hydrogen and nitrogen are supplied to and reacted with one another in a reaction zone, wherein they undergo exothermic reaction to produce ammonia at an elevated temperature and pressure, the resulting ammonia is separated and recovered from unconverted gaseous hydrogen and nitrogen at substantially reaction pressure and at reduced temperature in a separation zone and unconverted gaseous hydrogen and nitrogen are recycled to the reaction zone and fresh feed gaseous hydrogen and nitrogen are supplied to said reaction zone, the improvement which comprises passing said gaseous reaction product ammonia admixed with unconverted gaseous reactants directly from said reaction zone at said elevated temperature and pressure into indirect heat exchange with relatively cooler unconverted gaseous reactants from said separation zone in a first heat exchange zone, thereby heating said unconverted gaseous reactants, further heating resulting unconverted gaseous reactants to a temperature higher than said reaction zone temperature by indirect heat exchange with a heating medium in a second heat exchange zone, thereafter expanding resulting heated unconverted reactants in a heat engine with the production of power therefrom, cooling and recompressing said reactants and supplying said recompressed unconverted reactants to said reaction zone, a portion of the unconverted gaseous reactants from the separation step being recycled directly to said reaction zone, thus by-passing the heat exchange zones.
Claim 5
Dependent Claim
251 words
In a process wherein gaseous hydrogen and nitrogen are supplied to and reacted with one another in a reaction zone, wherein they undergo exothermic reaction to produce ammonia at an elevated temperature and pressure, the resulting ammonia is separated and recovered from unconverted gaseous hydrogen and nitrogen at substantially reaction pressure and at reduced temperature in a separation zone and unconverted gaseous hydrogen and nitrogen are recycled to the reaction zone and fresh feed gaseous hydrogen and nitrogen are supplied to said reaction zone, the improvement which comprises passing said gaseous reaction product ammonia admixed with unconverted gaseous reactants directly from said reaction zone at said elevated temperature and pressure into indirect heat exchange with relatively cooler unconverted gaseous reactants from said separation zone in a first heat exchange zone, thereby heating said unconverted gaseous reactants, further heating resulting unconverted gaseous reactants to a temperature higher than said reaction zone temperature by indirect heat exchange with a heating medium in a second heat exchange zone, thereafter expanding resulting heated unconverted reactants in a heat engine with the production of power therefrom, cooling and recompressing said reactants and supplying said recompressed unconverted reactants to said reaction zone, a portion of the recompressed unconverted gaseous reactants being passed directly to said first heat exchange zone into indirect heat exchange with gaseous reaction product and unconverted gaseous reactants from the reaction zone in admixture with unconverted gaseous reactants from said separation zone and thus recycled to said heat engine while by-passing said reaction zone.
Claim 6
Dependent Claim
251 words
In a process wherein gaseous hydrogen and nitrogen are supplied to and reacted with one another in a reaction zone, wherein they undergo exothermic reaction to produce ammonia at an elevated temperature and pressure, the resulting ammonia is separated and recovered from unconverted gaseous hydrogen and nitrogen at substantially reaction pressure and at reduced temperature in a separation zone and unconverted gaseous hydrogen and nitrogen are recycled to the reaction zone and fresh feed gaseous hydrogen and nitrogen are supplied to said reaction zone, the improvement which comprises passing said gaseous reaction product ammonia admixed with unconverted gaseous reactants directly from said reaction zone at said elevated temperature and pressure into indirect heat exchange with relatively cooler unconverted gaseous reactants from said separation zone in a first heat exchange zone, thereby heating said unconverted gaseous reactants, further heating resulting unconverted gaseous reactants to a temperature higher than said reaction zone temperature by indirect heat exchange with a heating medium in a second heat exchange zone, thereafter expanding resulting heated unconverted reactants in a heat engine with the production of power therefrom, cooling and recompressing said reactants and supplying said recompressed unconverted reactants to said reaction zone, a portion of the recompressed unconverted gaseous reactants being passed directly to said first heat exchange zone into indirect heat exchange with gaseous reaction product and unconverted gaseous reactants from the reaction zone in admixture with unconverted gaseous reactants from said separation zone and thus recycled to said heat engine while by-passing said reaction zone.
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) | 1983-09-23 | 1984-03-24 | 1984-09-23 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1987-09-23 | 1988-03-24 | 1988-09-23 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1991-09-23 | 1992-03-24 | 1992-09-23 | $7700.00 | Window Closed / Lapsed |