DK647587D0 - CONTROL DEVICE SPECIAL FOR AN AMMONIA CONVERTER - Google Patents
CONTROL DEVICE SPECIAL FOR AN AMMONIA CONVERTERInfo
- Publication number
- DK647587D0 DK647587D0 DK647587A DK647587A DK647587D0 DK 647587 D0 DK647587 D0 DK 647587D0 DK 647587 A DK647587 A DK 647587A DK 647587 A DK647587 A DK 647587A DK 647587 D0 DK647587 D0 DK 647587D0
- Authority
- DK
- Denmark
- Prior art keywords
- heat exchanger
- gas
- catalyst bed
- process gas
- control
- Prior art date
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
- C01C1/0417—Preparation of ammonia by synthesis in the gas phase from N2 and H2 in presence of a catalyst characterised by the synthesis reactor, e.g. arrangement of catalyst beds and heat exchangers in the reactor
- C01C1/0423—Cold wall reactors
-
- 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
- B01J8/0403—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 the fluid flow within the beds being predominantly horizontal
- B01J8/0407—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 the fluid flow within the beds being predominantly horizontal through two or more cylindrical annular shaped beds
- B01J8/0415—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 the fluid flow within the beds being predominantly horizontal through two or more cylindrical annular shaped beds the beds being superimposed one above the other
-
- 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
- B01J8/0496—Heating or cooling the reactor
-
- 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)
- Chemical Kinetics & Catalysis (AREA)
- Organic Chemistry (AREA)
- Analytical Chemistry (AREA)
- Inorganic Chemistry (AREA)
- Physics & Mathematics (AREA)
- Fluid Mechanics (AREA)
- Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)
- Control Of Non-Electrical Variables (AREA)
- Dc-Dc Converters (AREA)
- Sampling And Sample Adjustment (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Fats And Perfumes (AREA)
- Exhaust Gas After Treatment (AREA)
- Networks Using Active Elements (AREA)
- Incineration Of Waste (AREA)
- Investigating Or Analysing Materials By Optical Means (AREA)
Abstract
In the converter having a process gas inlet and outlet, at least one heat exchanger and at least one catalyst bed as well as a further gas feed and having a central pipe and a process gas feed to the heat exchanger and/or catalyst bed, the heat exchanger and the first catalyst bed around the latter being arranged rotationally symmetrically to the central pipe, control gas, quench gas, a part of the process gas at a different temperature and/or under other conditions at a point of a reactor is to be added to the particular gas streams in such a way that the mixing-in and/or the by-pass line are designed for complete isolation, partial loading and/or complete opening. For this purpose, the central pipe (14) for temperature control as a control gas feedpipe completely penetrates the heat exchanger (4 and/or 5 and/or 6) and is provided at its lower end with controllable outlets (18) for at least partial mixing of the control gas with the process gas stream, before the latter flows through the catalyst bed (4), and/or for mixing the control gas stream with the process gas stream after the latter has passed through the catalyst bed (4) and the heat exchanger (7). <IMAGE>
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE19863643856 DE3643856A1 (en) | 1986-12-22 | 1986-12-22 | DEVICE FOR REGULATING, IN PARTICULAR, AN AMMONIA CONVERTER |
DE3643856 | 1986-12-22 |
Publications (3)
Publication Number | Publication Date |
---|---|
DK647587D0 true DK647587D0 (en) | 1987-12-09 |
DK647587A DK647587A (en) | 1988-06-23 |
DK166772B1 DK166772B1 (en) | 1993-07-12 |
Family
ID=6316843
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
DK647587A DK166772B1 (en) | 1986-12-22 | 1987-12-09 | CONTROL DEVICE SPECIAL FOR AN AMMONIA CONVERTER |
Country Status (12)
Country | Link |
---|---|
EP (1) | EP0273231B1 (en) |
JP (1) | JPS63248431A (en) |
CN (1) | CN1013664B (en) |
AT (1) | ATE72423T1 (en) |
AU (1) | AU602744B2 (en) |
CA (1) | CA1287480C (en) |
DE (2) | DE3643856A1 (en) |
DK (1) | DK166772B1 (en) |
ES (1) | ES2029260T3 (en) |
FI (1) | FI875417A (en) |
NO (1) | NO168020C (en) |
ZA (1) | ZA879320B (en) |
Families Citing this family (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE3710004A1 (en) * | 1987-03-26 | 1988-10-06 | Uhde Gmbh | DEVICE FOR THE CATALYTIC TREATMENT OF NITROGEN AND HYDROGEN |
DE3819451A1 (en) * | 1988-06-08 | 1989-12-14 | Uhde Gmbh | DEVICE FOR CARRYING OUT EXOTHERMAL, CATALYTIC GAS REACTIONS FOR AMMONIA OR METHANOL SYNTHESIS |
DE69111820T2 (en) * | 1990-09-24 | 1995-12-14 | Braun C F Inc | HIGH CONVERSION AMMONIA SYNTHESIS. |
US7081230B2 (en) * | 2002-11-15 | 2006-07-25 | Kellogg Brown & Root Llc | Split-flow, vertical ammonia converter |
EP1442786A1 (en) * | 2003-01-29 | 2004-08-04 | Methanol Casale S.A. | Pseudo isothermal radial reactor |
US7371361B2 (en) * | 2004-11-03 | 2008-05-13 | Kellogg Brown & Root Llc | Maximum reaction rate converter system for exothermic reactions |
US7867465B2 (en) * | 2008-05-29 | 2011-01-11 | Kellogg Brown & Root Llc | Cold wall horizontal ammonia converter |
WO2012172065A1 (en) * | 2011-06-16 | 2012-12-20 | Haldor Topsøe A/S | Method for carrying out exothermic catalytic reactions and a reactor for use in the method |
CN105621454A (en) * | 2016-02-25 | 2016-06-01 | 山东奥能电力科技有限公司 | Integrated liquid ammonia consumption and conversion device |
Family Cites Families (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE1715928U (en) * | 1954-09-18 | 1956-02-02 | Adolf Dipl Ing Schild | HEAT EXCHANGER WITH COOLING WATER VOLUME REGULATOR. |
US3852147A (en) * | 1972-04-24 | 1974-12-03 | W Wilson | Heat exchanger |
GB1574723A (en) * | 1976-03-10 | 1980-09-10 | Haldor Topsoe As | Apparatus for the synthesis of ammonia |
GB1565824A (en) * | 1976-11-15 | 1980-04-23 | Ici Ltd | Exothermic process and apparatus therefor |
CH646618A5 (en) * | 1981-03-26 | 1984-12-14 | Ammonia Casale Sa | REACTOR FOR CATALYTIC HETEROGENEOUS SYNTHESIS. |
FR2539524B1 (en) * | 1983-01-17 | 1986-08-22 | Azote & Prod Chim | METHOD FOR REGULATING THE OPERATING TEMPERATURES OF A SYNTHESIS REACTOR AND INTERNAL IMPLEMENTATION EQUIPMENT |
DE3343114C2 (en) * | 1983-11-29 | 1985-11-07 | Uhde Gmbh, 4600 Dortmund | Device for carrying out exothermic, catalytic gas reactions for ammonia or methanol synthesis |
JPS60225632A (en) * | 1984-04-23 | 1985-11-09 | Mitsubishi Heavy Ind Ltd | Reactor |
-
1986
- 1986-12-22 DE DE19863643856 patent/DE3643856A1/en active Granted
-
1987
- 1987-12-04 ES ES198787117925T patent/ES2029260T3/en not_active Expired - Lifetime
- 1987-12-04 EP EP87117925A patent/EP0273231B1/en not_active Expired - Lifetime
- 1987-12-04 DE DE8787117925T patent/DE3776634D1/en not_active Expired - Fee Related
- 1987-12-04 AT AT87117925T patent/ATE72423T1/en not_active IP Right Cessation
- 1987-12-09 NO NO875137A patent/NO168020C/en unknown
- 1987-12-09 FI FI875417A patent/FI875417A/en not_active Application Discontinuation
- 1987-12-09 DK DK647587A patent/DK166772B1/en not_active IP Right Cessation
- 1987-12-11 ZA ZA879320A patent/ZA879320B/en unknown
- 1987-12-15 CA CA000554318A patent/CA1287480C/en not_active Expired - Fee Related
- 1987-12-16 JP JP62316364A patent/JPS63248431A/en active Pending
- 1987-12-17 AU AU82899/87A patent/AU602744B2/en not_active Ceased
- 1987-12-22 CN CN87108165A patent/CN1013664B/en not_active Expired
Also Published As
Publication number | Publication date |
---|---|
ES2029260T3 (en) | 1992-08-01 |
EP0273231A3 (en) | 1988-10-05 |
EP0273231A2 (en) | 1988-07-06 |
AU8289987A (en) | 1988-06-23 |
DK647587A (en) | 1988-06-23 |
JPS63248431A (en) | 1988-10-14 |
AU602744B2 (en) | 1990-10-25 |
NO875137D0 (en) | 1987-12-09 |
NO875137L (en) | 1988-06-23 |
DE3776634D1 (en) | 1992-03-19 |
ZA879320B (en) | 1988-06-15 |
CA1287480C (en) | 1991-08-13 |
CN1013664B (en) | 1991-08-28 |
EP0273231B1 (en) | 1992-02-05 |
NO168020C (en) | 1992-01-08 |
CN87108165A (en) | 1988-08-03 |
DK166772B1 (en) | 1993-07-12 |
DE3643856C2 (en) | 1989-10-12 |
DE3643856A1 (en) | 1988-06-30 |
NO168020B (en) | 1991-09-30 |
ATE72423T1 (en) | 1992-02-15 |
FI875417A (en) | 1988-06-23 |
FI875417A0 (en) | 1987-12-09 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US4393031A (en) | Process for efficiently removing oxides of nitrogen from exhaust gas | |
DK647587A (en) | CONTROL DEVICE SPECIAL FOR AN AMMONIA CONVERTER | |
ES335594A1 (en) | Partial wet air oxidation of sewage sludge | |
DE1926629B2 (en) | Process for removing ammonia separated from coke oven gases and their condensates | |
DE3244252C2 (en) | ||
DE3474158D1 (en) | Catalytic cracking unit and operation | |
DE2512410A1 (en) | PROCEDURE FOR THE REMOVAL OF NITROGEN OXIDES AND INSTALLATION FOR CARRYING OUT THE PROCEDURE | |
GB1202588A (en) | Process for catalytically converting so2-containing gases to so2 and sulphuric acid | |
EP1118083B1 (en) | Device and method for recombining hydrogen and oxygen in a gaseous mixture | |
DE2346247A1 (en) | PROCESS FOR THE RECOVERY OF SULFUR FROM HYDROGEN SULFUR AND SULFUR DIOXIDE AND PLANT FOR CARRYING OUT THE PROCESS | |
US4737345A (en) | System for efficiently removing oxides of nitrogen from exhaust gas | |
JPS55104634A (en) | Improved process for exhaust gas treatment by means of catalyst combustion system | |
JPS63264132A (en) | Treatment to liquid or by said liquid | |
DE3515843A1 (en) | Process and apparatus for NOx removal from an exhaust gas stream | |
DE2438790B2 (en) | PROCESS AND SYSTEM FOR THE REDUCTION OF IRON ORES, IN PARTICULAR IRON ORES PELLETS | |
EP0236343B1 (en) | Process and installation for cleaning exhaust gases from furnace installations | |
US3424553A (en) | Method and apparatus for carrying out exothermic gas reactions | |
DE69901799D1 (en) | METHOD AND DEVICE FOR PRODUCING AMMONIA | |
AT226741B (en) | Process for increasing the waste heat-steam yield in catalytic high-pressure gas syntheses | |
CH445359A (en) | Process for the production of high-quality hemihydrate plasters and device for carrying out this process | |
JPS567634A (en) | Treating method of nh3 and so3 contained in high-concentration so2 gas | |
DE1134790B (en) | Process for the catalytic cracking of gaseous and / or liquid hydrocarbons | |
DE533106C (en) | Process for regulating the reaction temperature in gas reactions | |
DE3618514A1 (en) | Method for operating a catalytic nitrogen oxide reduction stage | |
DE1417707C3 (en) | Device to increase the waste heat-steam yield with catalytic! High pressure syntheses |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
B1 | Patent granted (law 1993) | ||
PBP | Patent lapsed |