GB2205561A - Method of producing ammonia - Google Patents
Method of producing ammoniaInfo
- Publication number
- GB2205561A GB2205561A GB08811619A GB8811619A GB2205561A GB 2205561 A GB2205561 A GB 2205561A GB 08811619 A GB08811619 A GB 08811619A GB 8811619 A GB8811619 A GB 8811619A GB 2205561 A GB2205561 A GB 2205561A
- Authority
- GB
- United Kingdom
- Prior art keywords
- catalyst
- gas mixture
- nitrogen
- initial gas
- temperature
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01C—AMMONIA; CYANOGEN; COMPOUNDS THEREOF
- C01C1/00—Ammonia; Compounds thereof
- C01C1/02—Preparation, purification or separation of ammonia
- C01C1/04—Preparation of ammonia by synthesis in the gas phase
- C01C1/0405—Preparation of ammonia by synthesis in the gas phase from N2 and H2 in presence of a catalyst
- C01C1/0411—Preparation of ammonia by synthesis in the gas phase from N2 and H2 in presence of a catalyst characterised by the catalyst
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
- B01J8/02—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds
- B01J8/04—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds the fluid passing successively through two or more beds
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01C—AMMONIA; CYANOGEN; COMPOUNDS THEREOF
- C01C1/00—Ammonia; Compounds thereof
- C01C1/02—Preparation, purification or separation of ammonia
- C01C1/04—Preparation of ammonia by synthesis in the gas phase
- C01C1/0405—Preparation of ammonia by synthesis in the gas phase from N2 and H2 in presence of a catalyst
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/50—Improvements relating to the production of bulk chemicals
- Y02P20/52—Improvements relating to the production of bulk chemicals using catalysts, e.g. selective catalysts
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Analytical Chemistry (AREA)
- Inorganic Chemistry (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Catalysts (AREA)
Abstract
A method of producing ammonia provides for introducing a nitrogen-hydrogen mixture into a catalyst layer divided into at least two parts by a plane which is perpendicular to the initial gas mixture flow direction. The temperature of the initial gas mixture introduced is 20-250 DEG C, its pressure 10-100 MPa and the temperature of the catalyst before introduction of the inital gas mixture is 420-590 DEG C. The direction of the initial gas mixture introduced into the catalyst is periodically changed to the opposite one. The nitrogen-hydrogen mixture is mixed between the catalyst layers formed during the division of the latter in a ratio of (0.5-1):1 until its temperature gradient between the preceding and subsequent layers of the catalyst does not exceed 20 DEG C. The ammonia generated and the non-reacted part of the nitrogen-hydrogen mixture are extracted from the catalyst layer. The method of producing ammonia enables an end product with a yield of 14-30 % to be obtained.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
SU864131458A SU1696387A1 (en) | 1986-10-17 | 1986-10-17 | Method of ammonia synthesis |
PCT/SU1987/000106 WO1988002737A1 (en) | 1986-10-17 | 1987-09-23 | Method of producing ammonia |
Publications (3)
Publication Number | Publication Date |
---|---|
GB8811619D0 GB8811619D0 (en) | 1988-07-13 |
GB2205561A true GB2205561A (en) | 1988-12-14 |
GB2205561B GB2205561B (en) | 1990-12-19 |
Family
ID=21261751
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB8811619A Expired - Lifetime GB2205561B (en) | 1986-10-17 | 1987-09-23 | Process for producing ammonia. |
Country Status (8)
Country | Link |
---|---|
JP (1) | JPH01501141A (en) |
DE (1) | DE3790631T1 (en) |
FR (1) | FR2605305B1 (en) |
GB (1) | GB2205561B (en) |
HU (1) | HUT46594A (en) |
PL (1) | PL268264A1 (en) |
SU (1) | SU1696387A1 (en) |
WO (1) | WO1988002737A1 (en) |
Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4423022A (en) * | 1979-05-22 | 1983-12-27 | The Lummus Company | Processes for carrying out catalytic exothermic and endothermic high-pressure gas reactions |
US4510123A (en) * | 1982-11-26 | 1985-04-09 | C F Braun & Co. | Temperature controlled ammonia synthesis process |
-
1986
- 1986-10-17 SU SU864131458A patent/SU1696387A1/en active
-
1987
- 1987-09-23 JP JP62506696A patent/JPH01501141A/en active Pending
- 1987-09-23 HU HU875776A patent/HUT46594A/en unknown
- 1987-09-23 WO PCT/SU1987/000106 patent/WO1988002737A1/en active Application Filing
- 1987-09-23 GB GB8811619A patent/GB2205561B/en not_active Expired - Lifetime
- 1987-09-23 DE DE19873790631 patent/DE3790631T1/de not_active Withdrawn
- 1987-10-16 PL PL1987268264A patent/PL268264A1/en unknown
- 1987-10-16 FR FR878714279A patent/FR2605305B1/en not_active Expired - Lifetime
Patent Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4423022A (en) * | 1979-05-22 | 1983-12-27 | The Lummus Company | Processes for carrying out catalytic exothermic and endothermic high-pressure gas reactions |
US4510123A (en) * | 1982-11-26 | 1985-04-09 | C F Braun & Co. | Temperature controlled ammonia synthesis process |
Non-Patent Citations (1)
Title |
---|
A.G. KASATKIN }OSUOVNYE PROTSESSY I APPARATY KHIMICHESKOI TEKHNOLOGII}, 1973, KHIMIA MOSCOW, SEE PAGE 246 * |
Also Published As
Publication number | Publication date |
---|---|
WO1988002737A1 (en) | 1988-04-21 |
GB8811619D0 (en) | 1988-07-13 |
DE3790631T1 (en) | 1988-10-06 |
FR2605305A1 (en) | 1988-04-22 |
FR2605305B1 (en) | 1990-07-20 |
SU1696387A1 (en) | 1991-12-07 |
JPH01501141A (en) | 1989-04-20 |
HUT46594A (en) | 1988-11-28 |
GB2205561B (en) | 1990-12-19 |
PL268264A1 (en) | 1988-08-18 |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
PCNP | Patent ceased through non-payment of renewal fee |