US5230877A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Method for removal of ammonia from a gas mixture
Assignee: Norsk Hydro ASA
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Filing: 1990-02-02
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Granted: 1993-07-27
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Expires: 2010-02-02
Abstract
Abstract The present invention relates to a method of catalytic production of ammonia, where a gas mixture consisting mainly of unconverted synthesis gas, some ammonia, inert gases and possibly also water is recirculated to the synthesis reactor being first freed from the main part of the ammonia and possibly also water by absorption. The gas mixture is brought in contact with a hygroscopic abosrption agent having two or more OH-groups for absorption of ammonia and possibly also water. The absorption is carried out at a pressure being substantially the same as the ammonia synthesis pressure, and ammonia being desorbed from the absorption agent at a lower pressure and higher temperature than at the absorption. At least part of the possibly present water is removed from the absorption agent before it is supplied to the absorption column. Preferably it si applied ethylene glycol, diethylene glycol or triethylene glycol alone or in mixture as absorption agent. Possible water can be removed form the absorption agent by inert stripping gas before it is returned to the absorption column.
Inventors
- 👤 Dag A. Eimer
- 👤 Lars E. Oi
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-29 06:56
CPC Classifications
C; C01; C01C; C01C1/00; C01C1/02; C01C1/04; C01C1/0405; C01C1/0458; C01C1/0464; Y; Y02; Y02P; Y02P20/00; Y02P20/50; Y02P20/52
Claims Analysis
Total Claims: 9
Claim 1
Independent Claim
172 words
In a method for removal of ammonia from a gas mixture formed in an ammonia synthesis process by catalytic production of ammonia, wherein the gas mixture comprises unconverted synthesis gas, ammonia, and inert gases, and wherein the gas mixture is freed from ammonia by absorption with an organic absorption agent having two or more OH-groups, the ammonia is subsequently desorbed from the absorption agent, and the resultant gas mixture is then returned to the ammonia synthesis process, the improvement comprising: carrying out the absorption at a pressure which is substantially the same as the pressure of the ammonia synthesis process; and carrying out the desorption of the ammonia from the absorption agent in at least two stages, including a first desorption stage in which a major portion of the ammonia is desorbed at a pressure of 7-20 bare and condensed by cooling water at a temperature of 5°-35° C., and a second desorption stage in which further amounts of ammonia are desorbed from the absorption agent at a pressure of 1-3 bar.
Claim 2
Dependent Claim
172 words
In a method for removal of ammonia from a gas mixture formed in an ammonia synthesis process by catalytic production of ammonia, wherein the gas mixture comprises unconverted synthesis gas, ammonia, and inert gases, and wherein the gas mixture is freed from ammonia by absorption with an organic absorption agent having two or more OH-groups, the ammonia is subsequently desorbed from the absorption agent, and the resultant gas mixture is then returned to the ammonia synthesis process, the improvement comprising: carrying out the absorption at a pressure which is substantially the same as the pressure of the ammonia synthesis process; and carrying out the desorption of the ammonia from the absorption agent in at least two stages, including a first desorption stage in which a major portion of the ammonia is desorbed at a pressure of 7-20 bare and condensed by cooling water at a temperature of 5°-35° C., and a second desorption stage in which further amounts of ammonia are desorbed from the absorption agent at a pressure of 1-3 bar.
Claim 3
Dependent Claim
23 words
A method according to claim 1, wherein the desorption is carried out during heating by process heat at a temperature of 100°-150 C.
Claim 4
Dependent Claim
23 words
A method according to claim 1, wherein ammonia desorbed in the second desorption stage is compressed and returned to the first desorption stage.
Claim 5
Dependent Claim
25 words
A method according to claim 1, wherein the ammonia desorbed in the second desorption stage is reabsorbed and pumped back to the first desorption stage.
Claim 6
Dependent Claim
50 words
A method according to claim 1, wherein the ammonia desorbed in the second desorption stage is first brought in contact with volatilized ammonia formed after expansion of condensed ammonia removed in the first desorption stage, and then the combined ammonia streams are compressed and returned to the first desorption stage.
Claim 7
Dependent Claim
19 words
A method according to claim 1, wherein the absorption agent used in carrying out the absorption comprises ethylene glycol.
Claim 8
Dependent Claim
39 words
A method according to claim 1, wherein said at least two stages of said desorption further include a third desorption stage in which additional amounts of ammonia are desorbed from the desorption agent at a pressure of 3-15 bar.
Claim 9
Dependent Claim
34 words
A method according to claim 1, wherein cooling water used for desorption in the first desorption stage is subsequently used a the cooling water for condensing the ammonia desorbed in the first desorption stage.
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) | 1996-07-26 | 1997-01-25 | 1997-07-27 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 2000-07-26 | 2001-01-25 | 2001-07-27 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 2004-07-26 | 2005-01-25 | 2005-07-27 | $7700.00 | Window Closed / Lapsed |