BR9804750A - Método para modernização, no local, de um reator de sìntese heterogênea exotérmica. - Google Patents
Método para modernização, no local, de um reator de sìntese heterogênea exotérmica.Info
- Publication number
- BR9804750A BR9804750A BR9804750A BR9804750A BR9804750A BR 9804750 A BR9804750 A BR 9804750A BR 9804750 A BR9804750 A BR 9804750A BR 9804750 A BR9804750 A BR 9804750A BR 9804750 A BR9804750 A BR 9804750A
- Authority
- BR
- Brazil
- Prior art keywords
- reactor
- modernization
- site
- synthesis reactor
- heterogeneous exothermic
- 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
- B01J8/008—Details of the reactor or of the particulate material; Processes to increase or to retard the rate of reaction
-
- 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
- B01J8/0446—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 flow within the beds being predominantly vertical
- B01J8/0449—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 flow within the beds being predominantly vertical in two or more cylindrical beds
- B01J8/0453—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 flow within the beds being predominantly vertical in two or more cylindrical 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
- B01J8/0446—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 flow within the beds being predominantly vertical
- B01J8/0461—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 flow within the beds being predominantly vertical in two or more cylindrical annular shaped beds
- B01J8/0469—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 flow within the beds being predominantly vertical in 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
-
- 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
- B01J21/00—Catalysts comprising the elements, oxides, or hydroxides of magnesium, boron, aluminium, carbon, silicon, titanium, zirconium, or hafnium
- B01J21/18—Carbon
-
- 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
- B01J2208/00—Processes carried out in the presence of solid particles; Reactors therefor
- B01J2208/00008—Controlling the process
- B01J2208/00017—Controlling the temperature
- B01J2208/00106—Controlling the temperature by indirect heat exchange
- B01J2208/00168—Controlling the temperature by indirect heat exchange with heat exchange elements outside the bed of solid particles
- B01J2208/00194—Tubes
-
- 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
- B01J2208/00—Processes carried out in the presence of solid particles; Reactors therefor
- B01J2208/00008—Controlling the process
- B01J2208/00017—Controlling the temperature
- B01J2208/0053—Controlling multiple zones along the direction of flow, e.g. pre-heating and after-cooling
-
- 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
- B01J2208/00—Processes carried out in the presence of solid particles; Reactors therefor
- B01J2208/02—Processes carried out in the presence of solid particles; Reactors therefor with stationary particles
- B01J2208/023—Details
- B01J2208/024—Particulate material
- B01J2208/025—Two or more types of 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
- B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J2219/00002—Chemical plants
- B01J2219/00018—Construction aspects
- B01J2219/00024—Revamping, retrofitting or modernisation of existing plants
-
- 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)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)
- Physical Or Chemical Processes And Apparatus (AREA)
- Catalysts (AREA)
Abstract
OR DE SìNTESE HETEROGêNEA EXOTéRMICA"<D>. Método para modernização, in-situ (no local), de um reator de síntese heterogênea exotérmica, compreendendo a porção inferior (2b) respectivamente a uma porção superior (2a) do reator, fornecer adicionalmente um leito catalítico mais baixo (14) na porção inferior (2b) do reator, tendo um volume de reação menor que o volume de reação do segundo leito catalíxo (14) com um catalisador que apresenta uma atividade maior que a atividade do catalisador carregado nos outros leitos (12, 13). Graças às etapas acima, o presente método permite obter um reator com alto rendimento de conversão.
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| EP97203724A EP0931586B1 (en) | 1997-11-28 | 1997-11-28 | Method for in-situ modernization of a heterogeneous exothermic synthesis reactor |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| BR9804750A true BR9804750A (pt) | 2000-03-21 |
Family
ID=8228986
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| BR9804750A BR9804750A (pt) | 1997-11-28 | 1998-11-27 | Método para modernização, no local, de um reator de sìntese heterogênea exotérmica. |
Country Status (9)
| Country | Link |
|---|---|
| US (1) | US6299849B1 (pt) |
| EP (1) | EP0931586B1 (pt) |
| CN (1) | CN1166446C (pt) |
| BR (1) | BR9804750A (pt) |
| CA (1) | CA2254694C (pt) |
| DE (1) | DE69732781T2 (pt) |
| ID (1) | ID21407A (pt) |
| RU (1) | RU2217230C2 (pt) |
| UA (1) | UA73466C2 (pt) |
Families Citing this family (22)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE69909788T2 (de) * | 1999-08-31 | 2004-06-03 | Ammonia Casale S.A. | Verfahren zur in-situ Modernisierung eines heterogenen Synthesereaktors |
| ATE279374T1 (de) | 2000-02-10 | 2004-10-15 | Haldor Topsoe As | Verfahren und vorrichtung zur herstellung von ammoniak |
| EP1153653A1 (en) * | 2000-05-11 | 2001-11-14 | Methanol Casale S.A. | Reactor for exothermic or endothermic heterogeneous reactions |
| ITMI20012565A1 (it) | 2001-12-05 | 2003-06-05 | Univ Degli Studi Milano | Catalizzatori per la sintesi dell'ammoniaca |
| DE60236589D1 (de) * | 2002-08-27 | 2010-07-15 | Methanol Casale Sa | Verfahren zur Durchführung von chemischen Reaktionen unter pseudo-isothermischen Bedingungen |
| WO2009082930A1 (en) * | 2007-12-17 | 2009-07-09 | Accelergy Shanghai R & D Center Co., Ltd. | Methods and apparatus for exothermic catalystic process |
| US7867465B2 (en) * | 2008-05-29 | 2011-01-11 | Kellogg Brown & Root Llc | Cold wall horizontal ammonia converter |
| EP2354092A1 (en) * | 2010-01-29 | 2011-08-10 | Ammonia Casale S.A. | A method for modernizing the synthesis loop of an ammonia plant |
| EP2759338A1 (en) * | 2013-01-29 | 2014-07-30 | Ammonia Casale S.A. | Adiabatic multi-bed catalytic converter with inter-bed cooling |
| GB201308428D0 (en) * | 2013-05-10 | 2013-06-19 | Johnson Matthey Plc | Reactor |
| CN103980090B (zh) * | 2014-05-28 | 2016-03-16 | 灯塔北方化工有限公司 | 天然脂肪醇的生产方法 |
| DE102015114201A1 (de) * | 2015-08-26 | 2017-03-02 | Thyssenkrupp Ag | Reaktor und Verfahren zur katalytischen Umsetzung eines Gasgemisches |
| US10329159B2 (en) * | 2016-06-21 | 2019-06-25 | Haldor Topsoe A/S | Axial-radial flow converter |
| DE102017001520A1 (de) * | 2017-02-15 | 2018-08-16 | Clariant International Ltd | Reaktor und Verfahren zur Maximierung der Methanolausbeute durch Einsatz von Katalysatorschichten |
| CN107055570B (zh) * | 2017-03-21 | 2023-07-25 | 武汉金中石化工程有限公司 | 低压合成氨设备及低压合成氨方法 |
| WO2018226917A2 (en) * | 2017-06-08 | 2018-12-13 | Industrial Heat, Llc | Low cost plate reactor for exothermic reactions |
| AR113649A1 (es) | 2017-12-20 | 2020-05-27 | Haldor Topsoe As | Convertidor de flujo axial enfriado |
| US10994860B2 (en) | 2017-12-20 | 2021-05-04 | Hamilton Sunstrand Corporation | Catalytic fuel tank inerting system |
| US10569896B2 (en) | 2017-12-20 | 2020-02-25 | Hamilton Sundstrand Corporation | Catalytic fuel tank inerting system |
| UA127973C2 (uk) * | 2017-12-21 | 2024-02-28 | Касале Са | Багатошаровий каталітичний реактор |
| CN113856566A (zh) * | 2021-10-31 | 2021-12-31 | 中国船舶重工集团公司第七一八研究所 | 一种便于拆卸的多层组合催化床 |
| US20250297174A1 (en) * | 2024-03-22 | 2025-09-25 | Uop Llc | Optimized reactor centerpipe |
Family Cites Families (16)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2475855A (en) * | 1947-10-13 | 1949-07-12 | Sun Oil Co | Catalytic reaction apparatus |
| US2646391A (en) * | 1947-10-25 | 1953-07-21 | Houdry Process Corp | Method of and apparatus for converting hydrocarbons |
| US3010807A (en) * | 1958-09-10 | 1961-11-28 | Chemical Construction Corp | Multi-stage catalytic conversion |
| GB1565074A (en) * | 1976-11-03 | 1980-04-16 | British Petroleum Co | Process for the production of ammonia |
| US4271136A (en) * | 1978-10-12 | 1981-06-02 | The British Petroleum Company Limited | Process for the production of ammonia |
| SU1095980A1 (ru) * | 1982-08-05 | 1984-06-07 | Предприятие П/Я В-2262 | Контактный аппарат |
| US4518574A (en) * | 1983-03-07 | 1985-05-21 | Exxon Research & Engineering Co. | Catalytic gas synthesis process |
| US4568532A (en) * | 1984-10-16 | 1986-02-04 | The M. W. Kellogg Company | Supplemental ammonia synthesis |
| SU1308377A1 (ru) * | 1985-03-14 | 1987-05-07 | Предприятие П/Я В-8783 | Реактор со стационарным слоем катализатора |
| IN165082B (pt) * | 1985-05-15 | 1989-08-12 | Ammonia Casale Sa | |
| DE68906006T2 (de) * | 1988-12-21 | 1993-08-12 | Ammonia Casale Sa | Reaktoren fuer heterogene synthesen. |
| CH678286A5 (pt) * | 1989-03-09 | 1991-08-30 | Ammonia Casale Sa | |
| FR2684313B1 (fr) * | 1991-12-03 | 1994-01-28 | Institut Francais Petrole | Procede et dispositif pour la fabrication de gaz de synthese et application. |
| RU2035989C1 (ru) * | 1992-04-24 | 1995-05-27 | Научно-производственное объединение "Ярсинтез" | Аппарат для противоточного контактирования жидкости и газа |
| JP2526404B2 (ja) * | 1993-10-15 | 1996-08-21 | 工業技術院長 | 触媒反応方法 |
| DE4446359A1 (de) * | 1993-12-29 | 1995-07-06 | Ammonia Casale Sa | Verfahren zur in-situ-Modernisierung eines heterogenen exothermen Synthesereaktors, insbesondere eines sogenannten Kellog-Reaktors |
-
1997
- 1997-11-28 DE DE69732781T patent/DE69732781T2/de not_active Expired - Lifetime
- 1997-11-28 EP EP97203724A patent/EP0931586B1/en not_active Expired - Lifetime
-
1998
- 1998-03-19 US US09/044,240 patent/US6299849B1/en not_active Expired - Lifetime
- 1998-11-25 RU RU98121322/12A patent/RU2217230C2/ru active
- 1998-11-25 CA CA002254694A patent/CA2254694C/en not_active Expired - Lifetime
- 1998-11-27 CN CNB981233929A patent/CN1166446C/zh not_active Expired - Lifetime
- 1998-11-27 UA UA98116297A patent/UA73466C2/uk unknown
- 1998-11-27 BR BR9804750A patent/BR9804750A/pt not_active Application Discontinuation
- 1998-11-30 ID IDP981557A patent/ID21407A/id unknown
Also Published As
| Publication number | Publication date |
|---|---|
| UA73466C2 (uk) | 2005-08-15 |
| CA2254694C (en) | 2005-04-12 |
| ID21407A (id) | 1999-06-03 |
| CN1166446C (zh) | 2004-09-15 |
| RU2217230C2 (ru) | 2003-11-27 |
| EP0931586B1 (en) | 2005-03-16 |
| US6299849B1 (en) | 2001-10-09 |
| CA2254694A1 (en) | 1999-05-28 |
| DE69732781T2 (de) | 2006-02-02 |
| CN1223169A (zh) | 1999-07-21 |
| DE69732781D1 (de) | 2005-04-21 |
| EP0931586A1 (en) | 1999-07-28 |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| B07A | Application suspended after technical examination (opinion) [chapter 7.1 patent gazette] | ||
| B09B | Patent application refused [chapter 9.2 patent gazette] |
Free format text: INDEFIRO O PRESENTE PEDIDO, UMA VEZ QUE NAO ATENDE AO REQUISITO DE ATIVIDADE INVENTIVA ART. 8O E 13 DA LPI |
|
| B12B | Appeal against refusal [chapter 12.2 patent gazette] |