US4215099A
Expired / Lapsed
US
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Ammonia synthesis process
Assignee: Imperial Chemical Industries Ltd
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Filing: 1977-11-07
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Granted: 1980-07-29
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Expires: 1997-11-07
Abstract
Abstract An exothermic gas phase reaction, especially synthesis of ammonia or methanol, is carried out by passing the reactant gas over a catalyst in a first zone in heat exchange with a coolant and then in a second, adiabatic zone and then passing reacted gas directly to a heat recovery zone. Such a sequence of zones affords a higher output of product and better heat recovery than in many previously used sequences, especially when the heat available from the cooled zone is used to pre-heat reactant gas and the heat removed from the gas leaving the adiabatic zone is used in high-grade recoveries such as high pressure steam generation.
Inventors
- 👤 Alwyn Pinto
- 👤 Stanley A. Ward
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-28 12:59
CPC Classifications
C; C01; C01C; C01C1/00; C01C1/02; C01C1/04; C01C1/0405; C01C1/0417; C01C1/0423; B; B01; B01J; B01J8/00; B01J8/0005; B01J8/02; B01J8/0285; B01J2208/00; B01J2208/00008; B01J2208/00017; B01J2208/00026; B01J2208/00035; B01J2208/00088; B01J2208/00106; B01J2208/00168; B01J2208/00194; B01J2208/00212; B01J2208/00221; B01J2208/00265; B01J2208/00274; B01J2208/00477; B01J2208/00495; B01J2208/0053; B01J2219/00; B01J2219/00002; B01J2219/00004; B01J2219/00006; Y; Y02; Y02P; Y02P20/00; Y02P20/50; Y02P20/52
Claims Analysis
Total Claims: 8
Claim 1
Independent Claim
261 words
A process for carrying out the gas phase catalytic synthesis of ammonia utilizing a reactor having a first catalyst zone within a plurality of tubes around which there is a coolant circulation space, and having immediately downstream of that first catalyst zone an adiabatic catalyst zone; said process comprising the step of: (a) disposing an ammonia synthesis catalyst in the reactor first catalyst zone; (b) passing a gas mixture containing nitrogen and hydrogen and residual ammonia through the reactor coolant circulation space so as to heat the gas to a temperature in the range 350°-430° C.; (c) passing the thus heated gas through the first zone, reacting it therein to produce ammonia, and controlling the rate of feed of the gas mixture containing nitrogen and hydrogen through the space so that the temperature in the first zone (i) rises to a temperature which is 540°-580° C. when the residual ammonia content is 3% v/v, 400°-450° C. when the residual ammonia content is 20% and at corresponding interpolated levels between these residual ammonia contents and (ii) falls as that the reacted gas leaves the said first zone at under 400° C.; (d) passing the effluent of the first catalyst zone into the adiabatic catalyst zone and reacting it therein so as to produce further ammonia and increase the temperature to 420°-480° C.; and (e) passing the effluent of the said adiabatic zone, without any further catalytic ammonia synthesis or heat exchange, through a high grade heat recovery zone affording an external heat recovery of steam at a pressure over 30 atm. abs.
Claim 2
Dependent Claim
261 words
A process for carrying out the gas phase catalytic synthesis of ammonia utilizing a reactor having a first catalyst zone within a plurality of tubes around which there is a coolant circulation space, and having immediately downstream of that first catalyst zone an adiabatic catalyst zone; said process comprising the step of: (a) disposing an ammonia synthesis catalyst in the reactor first catalyst zone; (b) passing a gas mixture containing nitrogen and hydrogen and residual ammonia through the reactor coolant circulation space so as to heat the gas to a temperature in the range 350°-430° C.; (c) passing the thus heated gas through the first zone, reacting it therein to produce ammonia, and controlling the rate of feed of the gas mixture containing nitrogen and hydrogen through the space so that the temperature in the first zone (i) rises to a temperature which is 540°-580° C. when the residual ammonia content is 3% v/v, 400°-450° C. when the residual ammonia content is 20% and at corresponding interpolated levels between these residual ammonia contents and (ii) falls as that the reacted gas leaves the said first zone at under 400° C.; (d) passing the effluent of the first catalyst zone into the adiabatic catalyst zone and reacting it therein so as to produce further ammonia and increase the temperature to 420°-480° C.; and (e) passing the effluent of the said adiabatic zone, without any further catalytic ammonia synthesis or heat exchange, through a high grade heat recovery zone affording an external heat recovery of steam at a pressure over 30 atm. abs.
Claim 3
Dependent Claim
38 words
A process as recited in claims 1 comprising the further step of passing the gas, after the high grade external heat recovery, in heat exchanging relationship with gas to be used as coolant for the first catalyst zone.
Claim 4
Dependent Claim
69 words
A process as recited in claims 1 wherein the reactor contains an adiabatic pre-zone before the first catalyst zone, and comprising the further step of, prior to step (b), feeding the nitrogen-hydrogen gas mixture at the lowest temperature at which the catalyst is active to the adiabatic pre-zone so as to produce a substantial rise in temperature just before passing the gas mixture into the reactor first catalyst zone.
Claim 5
Dependent Claim
258 words
A process for carrying out the gas phase catalytic synthesis of ammonia utilizing a reactor having a first catalyst zone within a plurality of tubes around which there is a coolant circulation space, and having immediately downstream of that first catalyst zone an adiabatic catalyst zone; said process comprising the step of: (a) disposing an ammonia synthesis catalyst in the reactor first catalyst zone; (b) passing a gas mixture containing nitrogen and hydrogen and residual ammonia through the reactor coolant circulation space so as to heat the gas to a temperature in the range 350°-430° C.; (c) passing the thus heated gas through the first zone, reacting it therein to produce ammonia, and controlling the rate of feed of the gas mixture containing nitrogen and hydrogen through the space so that the temperature in the first zone (i) rises to a temperature which is 540°-580° C. when the residual ammonia content is 3% v/v, 400°-450° C. when the residual ammonia content is 20% and at corresponding interpolated levels between these residual ammonia contents and (ii) falls as that the reacted gas leaves the said first zone at under 400° C.; (d) passing the effluent of the first catalyst zone into the adiabatic catalyst zone and reacting it therein so as to produce further ammonia and increase the temperature to 420°-480° C.; and (e) passing the effluent of the said adiabatic zone, without any further catalytic ammonia synthesis or heat exchange, through a high grade heat recovery zone affording an external heat recovery of hot pressurized boiler feed water.
Claim 6
Dependent Claim
258 words
A process for carrying out the gas phase catalytic synthesis of ammonia utilizing a reactor having a first catalyst zone within a plurality of tubes around which there is a coolant circulation space, and having immediately downstream of that first catalyst zone an adiabatic catalyst zone; said process comprising the step of: (a) disposing an ammonia synthesis catalyst in the reactor first catalyst zone; (b) passing a gas mixture containing nitrogen and hydrogen and residual ammonia through the reactor coolant circulation space so as to heat the gas to a temperature in the range 350°-430° C.; (c) passing the thus heated gas through the first zone, reacting it therein to produce ammonia, and controlling the rate of feed of the gas mixture containing nitrogen and hydrogen through the space so that the temperature in the first zone (i) rises to a temperature which is 540°-580° C. when the residual ammonia content is 3% v/v, 400°-450° C. when the residual ammonia content is 20% and at corresponding interpolated levels between these residual ammonia contents and (ii) falls as that the reacted gas leaves the said first zone at under 400° C.; (d) passing the effluent of the first catalyst zone into the adiabatic catalyst zone and reacting it therein so as to produce further ammonia and increase the temperature to 420°-480° C.; and (e) passing the effluent of the said adiabatic zone, without any further catalytic ammonia synthesis or heat exchange, through a high grade heat recovery zone affording an external heat recovery of hot pressurized boiler feed water.
Claim 7
Dependent Claim
38 words
A process as recited in claim 4 comprising the further step of passing the gas, after the high grade external heat recovery, in heat exchanging relationship with gas to be used as coolant for the first catalyst zone.
Claim 8
Dependent Claim
68 words
A process as recited in claim 4 wherein the reactor contains an adiabatic pre-zone before the first catalyst zone, and comprising the further step of, prior to step (b), feeding the nitrogen-hydrogen gas mixture at the lowest temperature which the catalyst is active to the adiabatic pre-zone so as to produce a substantial rise in temperature just before passing the gas mixture into the reactor first catalyst zone.
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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) | 1983-07-29 | 1984-01-28 | 1984-07-29 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1987-07-29 | 1988-01-28 | 1988-07-29 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1991-07-29 | 1992-01-28 | 1992-07-29 | $7700.00 | Window Closed / Lapsed |