MX2010008947A - Reactor para la preparacion de metanol. - Google Patents
Reactor para la preparacion de metanol.Info
- Publication number
- MX2010008947A MX2010008947A MX2010008947A MX2010008947A MX2010008947A MX 2010008947 A MX2010008947 A MX 2010008947A MX 2010008947 A MX2010008947 A MX 2010008947A MX 2010008947 A MX2010008947 A MX 2010008947A MX 2010008947 A MX2010008947 A MX 2010008947A
- Authority
- MX
- Mexico
- Prior art keywords
- methanol
- reactor
- catalyst bed
- gaseous phase
- cooling surface
- Prior art date
Links
Classifications
-
- 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
- B01J8/0285—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
- 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
- B01J8/06—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 in tube reactors; the solid particles being arranged in 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
- 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
- B01J8/009—Membranes, e.g. feeding or removing reactants or products to or from the catalyst bed through a membrane
-
- 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
- B01J8/0207—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 flow within the bed being predominantly horizontal
- B01J8/0214—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 flow within the bed being predominantly horizontal in a cylindrical annular shaped bed
-
- 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
- B01J8/0292—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 with stationary packing material in the bed, e.g. bricks, wire rings, baffles
-
- 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
- B01J8/06—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 in tube reactors; the solid particles being arranged in tubes
- B01J8/065—Feeding reactive fluids
-
- 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
- B01J8/06—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 in tube reactors; the solid particles being arranged in tubes
- B01J8/067—Heating or cooling the reactor
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C29/00—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring
- C07C29/15—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring by reduction of oxides of carbon exclusively
- C07C29/151—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring by reduction of oxides of carbon exclusively with hydrogen or hydrogen-containing gases
- C07C29/152—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring by reduction of oxides of carbon exclusively with hydrogen or hydrogen-containing gases characterised by the reactor used
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C31/00—Saturated compounds having hydroxy or O-metal groups bound to acyclic carbon atoms
- C07C31/02—Monohydroxylic acyclic alcohols
- C07C31/04—Methanol
-
- 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
- B01J2208/00115—Controlling the temperature by indirect heat exchange with heat exchange elements inside the bed of solid particles
-
- 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
- B01J2208/00115—Controlling the temperature by indirect heat exchange with heat exchange elements inside the bed of solid particles
- B01J2208/00123—Fingers
-
- 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
- B01J2208/00115—Controlling the temperature by indirect heat exchange with heat exchange elements inside the bed of solid particles
- B01J2208/00132—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
- B01J2208/00106—Controlling the temperature by indirect heat exchange
- B01J2208/00115—Controlling the temperature by indirect heat exchange with heat exchange elements inside the bed of solid particles
- B01J2208/0015—Plates; Cylinders
-
- 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
- B01J2208/00212—Plates; Jackets; Cylinders
-
- 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
- B01J2219/00761—Details of the reactor
- B01J2219/00763—Baffles
- B01J2219/00765—Baffles attached to the reactor wall
- B01J2219/0077—Baffles attached to the reactor wall inclined
- B01J2219/00772—Baffles attached to the reactor wall inclined in a helix
-
- 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)
- 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)
- Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
- Catalysts (AREA)
Abstract
Un diseño mejorado de un reactor catalítico para la producción de metanol en condiciones de equilibrio, con lo cual el metanol a medida que se forma es separado de la fase gaseosa en la fase líquida dentro del reactor, sin reducir la actividad catalítica del catalizador de metanol. Esto se logra al ajustar el punto de ebullición de un agente de enfriamiento líquido que está en contacto indirecto con las partículas de catalizador y al proporcionar una relación específica del volumen del lecho de catalizador con respecto al área de la superficie de enfriamiento. Por esa razón, la condensación de metanol a medida que se forma en la fase gaseosa toma lugar en la superficie de enfriamiento dispuesta que está distribuida uniformemente dentro del reactor y dentro de una región muy limitada del lecho de catalizador. La figura más representativa de la invención es la número 1a.
Applications Claiming Priority (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DKPA200800260 | 2008-02-25 | ||
DKPA200800261 | 2008-02-25 | ||
PCT/EP2009/000972 WO2009106231A1 (en) | 2008-02-25 | 2009-02-12 | Reactor for the preparation of methanol |
Publications (1)
Publication Number | Publication Date |
---|---|
MX2010008947A true MX2010008947A (es) | 2010-09-07 |
Family
ID=40586790
Family Applications (2)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
MX2010008947A MX2010008947A (es) | 2008-02-25 | 2009-02-12 | Reactor para la preparacion de metanol. |
MX2010007376A MX2010007376A (es) | 2008-02-25 | 2009-02-12 | Metodo y reactor para la preparacion de metanol. |
Family Applications After (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
MX2010007376A MX2010007376A (es) | 2008-02-25 | 2009-02-12 | Metodo y reactor para la preparacion de metanol. |
Country Status (17)
Country | Link |
---|---|
US (3) | US8202915B2 (es) |
EP (3) | EP2374533B8 (es) |
JP (2) | JP2011515333A (es) |
KR (2) | KR20100122898A (es) |
CN (2) | CN101959586B (es) |
AT (2) | ATE521407T1 (es) |
AU (2) | AU2009218828B2 (es) |
BR (2) | BRPI0907815B1 (es) |
CA (2) | CA2730916C (es) |
EA (2) | EA019311B1 (es) |
ES (3) | ES2372670T3 (es) |
MX (2) | MX2010008947A (es) |
NZ (2) | NZ586789A (es) |
PL (3) | PL2374533T3 (es) |
RU (1) | RU2481151C2 (es) |
WO (2) | WO2009106231A1 (es) |
ZA (2) | ZA201004473B (es) |
Families Citing this family (30)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CA2799460C (en) * | 2010-05-20 | 2015-08-11 | Haldor Topsoe A/S | Method and apparatus for the separation of a liquid from a gas feed stream in a catalytic reactor |
CN102985398B (zh) | 2010-06-24 | 2015-04-15 | 赫多特普索化工设备公司 | 甲醇和氨的共同生产 |
US20130153188A1 (en) * | 2011-12-16 | 2013-06-20 | L'air Liquide Societe Anonyme Pour L'etude Et L'exploitation Des Procedes Georges Claude | Advanced smr reactor design featuring high thermal efficiency |
EP3034161A1 (en) * | 2014-12-18 | 2016-06-22 | Haldor Topsøe A/S | Method and reactor design for the production of methanol |
DE102015202680A1 (de) | 2015-02-13 | 2016-08-18 | Friedrich-Alexander-Universität Erlangen-Nürnberg | Verfahren zur Durchführung einer chemischen Synthese und Synthesereaktor |
RU2716797C2 (ru) * | 2015-07-15 | 2020-03-16 | Хальдор Топсёэ А/С | Каталитический реактор |
CA2993958A1 (en) * | 2015-07-29 | 2017-02-02 | Primus Green Energy Inc. | Two-stage reactor for exothermal and reversible reactions and methods thereof |
EP3400098B1 (en) | 2016-01-07 | 2019-12-04 | Total Raffinage Chimie | Supported indium oxide catalyst and process for methanol synthesis using the same |
WO2017118573A1 (en) | 2016-01-07 | 2017-07-13 | Total Research & Technology Feluy | Process for methanol synthesis using an indium oxide based catalyst |
CN105797653A (zh) * | 2016-03-19 | 2016-07-27 | 江苏怡达化学股份有限公司 | 直接氧化法制备环氧丙烷的绿色合成反应装置及工艺 |
DE102016204718A1 (de) | 2016-03-22 | 2017-09-28 | Siemens Aktiengesellschaft | Reaktor |
DE102016204717A1 (de) | 2016-03-22 | 2017-09-28 | Siemens Aktiengesellschaft | Reaktor zur Durchführung von gleichgewichtslimitierten Reaktionen |
KR102286147B1 (ko) * | 2016-03-30 | 2021-08-09 | 할도르 토프쉐 에이/에스 | 대량 생산 용량을 위한 메탄올 합성 공정 레이아웃 |
EP3401300B1 (de) * | 2017-05-12 | 2021-06-23 | L'air Liquide, Société Anonyme Pour L'Étude Et L'exploitation Des Procédés Georges Claude | Verfahren zur herstellung von methanol |
WO2018210826A1 (en) | 2017-05-17 | 2018-11-22 | Total Research & Technology Feluy | Process for ethylene aromatisation from diluted stream |
EP3404005A1 (en) | 2017-05-17 | 2018-11-21 | Total Research & Technology Feluy | Process for ethylene oligomerisation from diluted stream |
WO2018210827A1 (en) | 2017-05-17 | 2018-11-22 | Total Research & Technology Feluy | Mto-ocp upgrading process to maximize the selectivity to propylene |
AR113649A1 (es) | 2017-12-20 | 2020-05-27 | Haldor Topsoe As | Convertidor de flujo axial enfriado |
EP3593900A1 (en) | 2018-07-10 | 2020-01-15 | Total Raffinage Chimie | Copper-iron-based catalytic composition for the conversion of syngas to higher alcohols and process using such catalyst composition |
EP3599075A1 (de) | 2018-07-27 | 2020-01-29 | Siemens Aktiengesellschaft | Reaktor zur durchführung einer chemischen gleichgewichtsreaktion |
WO2020049081A1 (en) | 2018-09-06 | 2020-03-12 | Total S.A. | Noble metal promoted supported indium oxide catalyst for the hydrogenation of co2 to methanol and process using said catalyst |
EP3917669B1 (en) | 2019-02-01 | 2023-08-16 | TotalEnergies OneTech | Copper-iron-based catalytic composition comprising zeolites, method for producing such catalytic composition and process using such catalytic composition for the conversion of syngas to higher alcohols |
WO2020157049A1 (en) | 2019-02-01 | 2020-08-06 | Total S.A. | Process using catalytic composition for the conversion of syngas to higher alcohols |
EP4021631A1 (en) * | 2019-08-27 | 2022-07-06 | SABIC Global Technologies, B.V. | Mass transfer swirler including distribution member |
EP4031274B1 (en) * | 2019-09-20 | 2023-05-24 | SABIC Global Technologies, B.V. | Reactor tube assembly |
CN114423515A (zh) * | 2019-09-27 | 2022-04-29 | 住友化学株式会社 | 化学反应方法及化学反应装置 |
AU2021332773A1 (en) * | 2020-08-31 | 2023-04-13 | Sumitomo Chemical Company, Limited | Chemical reaction method, chemical reaction apparatus and production method |
AU2021382100A1 (en) | 2020-11-17 | 2023-06-01 | Totalenergies Onetech | Process for methanol synthesis from co2-rich syngas |
ES2914350B2 (es) * | 2020-12-09 | 2023-01-30 | Blueplasma Power S L | Dispositivo y proceso para producir carbonato de dimetilo |
CN114148553B (zh) * | 2021-11-12 | 2024-06-25 | 中国运载火箭技术研究院 | 一种类失重流体分布形态构建系统及控制系统 |
Family Cites Families (37)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US1894768A (en) * | 1929-04-03 | 1933-01-17 | Chemical Construction Corp | Catalytic apparatus |
US2028326A (en) * | 1931-01-23 | 1936-01-21 | Standard Oil Dev Co | Apparatus for the production of hydrogen |
US2185928A (en) * | 1937-09-01 | 1940-01-02 | Socony Vacuum Oil Co Inc | Apparatus for catalytic conversions and other contact mass operations |
US2521538A (en) * | 1945-06-20 | 1950-09-05 | Texaco Development Corp | Process for synthesis of hydrocarbons and the like |
US3174084A (en) * | 1962-12-28 | 1965-03-16 | Gen Electric | Electron beam delection system |
US3518055A (en) * | 1968-03-06 | 1970-06-30 | Japan Gasoline | Hydrocarbon reforming process |
DE2153437B2 (de) * | 1971-10-27 | 1974-11-21 | Metallgesellschaft Ag, 6000 Frankfurt | Reaktor zur Herstellung von Methanol |
US3970435A (en) * | 1975-03-27 | 1976-07-20 | Midland-Ross Corporation | Apparatus and method for methanation |
GB1565824A (en) | 1976-11-15 | 1980-04-23 | Ici Ltd | Exothermic process and apparatus therefor |
US4134908A (en) * | 1977-04-28 | 1979-01-16 | Foster Wheeler Energy Corporation | Methanation process |
DE3062221D1 (en) * | 1979-10-15 | 1983-04-07 | Ici Plc | Catalytic process and apparatus therefor |
DE3266054D1 (en) * | 1981-11-19 | 1985-10-10 | Ici Plc | Synthesis process and reactor |
AU4695985A (en) * | 1984-09-04 | 1986-03-13 | Mitsubishi Jukogyo Kabushiki Kaisha | Process for reforming methanol |
DE3605792A1 (de) * | 1985-09-27 | 1987-04-02 | Gutehoffnungshuette Man | Stehender reaktor fuer katalytische exotherme und endotherme reaktionen, insbesondere zur herstellung von methanol, ammoniak, synthesegas und hoeheren alkoholen |
GB8524025D0 (en) | 1985-09-30 | 1985-11-06 | Shell Int Research | Chemical equilibrium reaction |
JPS62106834A (ja) * | 1985-11-01 | 1987-05-18 | Hitachi Ltd | リフオ−マの反応管 |
DK167242B1 (da) * | 1989-02-16 | 1993-09-27 | Topsoe Haldor As | Apparat og fremgangsmaade til exoterme reaktioner |
DE3913387A1 (de) * | 1989-04-24 | 1990-10-25 | Henkel Kgaa | Verfahren zur katalytischen hydrierung von fluessigen fettsaeure-methylestern |
US5262443A (en) | 1990-03-19 | 1993-11-16 | Haldor Topsoe A/S | Method of preparing methanol |
DK163578C (da) * | 1990-03-19 | 1992-08-03 | Haldor Topsoe As | Fremgangsmaade til fremstilling af metanol |
US5861353A (en) * | 1992-10-06 | 1999-01-19 | Montecatini Tecnologie S.R.L. | Catalyst in granular form for 1,2-dichloroethane synthesis |
ATE206069T1 (de) | 1993-07-05 | 2001-10-15 | Packinox Sa | Verfahren und vorrichtung zur regulierung von reaktionstemperaturen |
CA2173809C (en) | 1995-04-10 | 1999-10-26 | Shankar Nataraj | Process for operating equilibrium-controlled reactions |
EP0914200A1 (en) * | 1996-07-25 | 1999-05-12 | Syntroleum Corporation | Fixed-bed, catalytic reactor and method for manufacturing same |
JP3559456B2 (ja) * | 1998-09-18 | 2004-09-02 | 株式会社日本触媒 | 接触気相酸化方法及び多管式反応器 |
DE69905543T3 (de) * | 1998-12-07 | 2006-10-19 | Mitsubishi Heavy Industries, Ltd. | Verfahren zur Herstellung von Methanol |
JP4427131B2 (ja) * | 1999-06-28 | 2010-03-03 | 三菱重工業株式会社 | メタノール合成用触媒装置 |
EP1080780B1 (en) * | 1999-08-31 | 2007-08-01 | Nippon Shokubai Co., Ltd. | Reactor for catalytic gas phase oxidation |
AU2002215906A1 (en) * | 2000-09-26 | 2002-04-08 | Shell Internationale Research Maatschappij B.V. | Rod-shaped inserts in reactor tubes |
US20030068260A1 (en) | 2001-03-05 | 2003-04-10 | Wellington Scott Lee | Integrated flameless distributed combustion/membrane steam reforming reactor and zero emissions hybrid power system |
GB0116894D0 (en) * | 2001-07-11 | 2001-09-05 | Accentus Plc | Catalytic reactor |
KR100440479B1 (ko) * | 2002-04-23 | 2004-07-14 | 주식회사 엘지화학 | 탄화수소의 열분해 공정 |
GB0301323D0 (en) * | 2003-01-21 | 2003-02-19 | Johnson Matthey Plc | Methanol synthesis |
US7161044B2 (en) * | 2003-10-22 | 2007-01-09 | Nippon Shokubai Co., Ltd. | Catalytic gas phase oxidation reaction |
JP4487103B2 (ja) * | 2004-04-13 | 2010-06-23 | 財団法人北九州産業学術推進機構 | メタノールの高効率合成法及びそのための装置 |
EP1600208A1 (en) * | 2004-05-24 | 2005-11-30 | Methanol Casale S.A. | Plate-type heat-exchanger |
JP4967517B2 (ja) * | 2006-08-10 | 2012-07-04 | 株式会社Ihi | メタノール合成方法 |
-
2009
- 2009-02-12 BR BRPI0907815-0A patent/BRPI0907815B1/pt active IP Right Grant
- 2009-02-12 RU RU2010139275/05A patent/RU2481151C2/ru active
- 2009-02-12 BR BRPI0906447-8A patent/BRPI0906447B1/pt active IP Right Grant
- 2009-02-12 CA CA2730916A patent/CA2730916C/en active Active
- 2009-02-12 CN CN2009801064012A patent/CN101959586B/zh active Active
- 2009-02-12 MX MX2010008947A patent/MX2010008947A/es active IP Right Grant
- 2009-02-12 AT AT09714360T patent/ATE521407T1/de not_active IP Right Cessation
- 2009-02-12 WO PCT/EP2009/000972 patent/WO2009106231A1/en active Application Filing
- 2009-02-12 EA EA201001351A patent/EA019311B1/ru unknown
- 2009-02-12 JP JP2010547085A patent/JP2011515333A/ja active Pending
- 2009-02-12 KR KR1020107014940A patent/KR20100122898A/ko not_active Application Discontinuation
- 2009-02-12 AU AU2009218828A patent/AU2009218828B2/en active Active
- 2009-02-12 PL PL11005512T patent/PL2374533T3/pl unknown
- 2009-02-12 ES ES09714360T patent/ES2372670T3/es active Active
- 2009-02-12 PL PL09715912T patent/PL2257366T3/pl unknown
- 2009-02-12 JP JP2010547086A patent/JP2011515334A/ja active Pending
- 2009-02-12 EA EA201001350A patent/EA201001350A1/ru unknown
- 2009-02-12 ES ES09715912T patent/ES2368027T3/es active Active
- 2009-02-12 US US12/812,480 patent/US8202915B2/en active Active
- 2009-02-12 WO PCT/EP2009/000974 patent/WO2009106232A1/en active Application Filing
- 2009-02-12 EP EP11005512.6A patent/EP2374533B8/en active Active
- 2009-02-12 AU AU2009218827A patent/AU2009218827B2/en active Active
- 2009-02-12 NZ NZ586789A patent/NZ586789A/en unknown
- 2009-02-12 NZ NZ587453A patent/NZ587453A/en unknown
- 2009-02-12 AT AT09715912T patent/ATE516876T1/de not_active IP Right Cessation
- 2009-02-12 MX MX2010007376A patent/MX2010007376A/es active IP Right Grant
- 2009-02-12 CN CN2009801063965A patent/CN101959585B/zh active Active
- 2009-02-12 EP EP09715912A patent/EP2257366B1/en active Active
- 2009-02-12 ES ES11005512T patent/ES2409714T3/es active Active
- 2009-02-12 CA CA2713874A patent/CA2713874C/en active Active
- 2009-02-12 KR KR1020107018226A patent/KR20100138884A/ko not_active Application Discontinuation
- 2009-02-12 PL PL09714360T patent/PL2249958T3/pl unknown
- 2009-02-12 EP EP09714360A patent/EP2249958B1/en active Active
- 2009-02-12 US US12/863,011 patent/US8513314B2/en active Active
-
2010
- 2010-06-24 ZA ZA2010/04473A patent/ZA201004473B/en unknown
- 2010-07-27 ZA ZA2010/05343A patent/ZA201005343B/en unknown
-
2012
- 2012-06-15 US US13/524,910 patent/US8557192B2/en active Active
Also Published As
Similar Documents
Publication | Publication Date | Title |
---|---|---|
MX2010008947A (es) | Reactor para la preparacion de metanol. | |
MX339773B (es) | Catalizador de carburo de tungsteno soportado sobre carbon mesoporoso, preparacion y aplicacion del mismo. | |
Yang et al. | Enhanced hydrogen production by steam reforming of acetic acid over a Ni catalyst supported on mesoporous MgO | |
Yu et al. | A remarkable enhancement of catalytic activity for KBH4 treating the carbothermal reduced Ni/AC catalyst in glycerol hydrogenolysis | |
Chen et al. | Direct conversion of syngas to ethanol over Rh/Mn-supported on modified SBA-15 molecular sieves: Effect of supports | |
WO2009135227A3 (en) | Catalysts, preparation of such catalysts, methods of using such catalysts, products obtained in such methods and uses of products obtained | |
Liu et al. | Catalytic performance of novel Ni catalysts supported on SiC monolithic foam in carbon dioxide reforming of methane to synthesis gas | |
WO2011032703A3 (en) | Hollow particulate support | |
Shejale et al. | Ni–Cu and Ni–Co supported on La–Mg based metal oxides prepared by coprecipitation and impregnation for superior hydrogen production via steam reforming of glycerol | |
MX2009008182A (es) | Reactores de lecho fluidizado y metodos asociados. | |
Zhang et al. | CO2 reforming of CH4 over efficient bimetallic Co–Zr/AC catalyst for H2 production | |
EP3566770A3 (en) | A process for catalytic gasification of carbonaceous feedstock | |
WO2012131385A3 (en) | High pressure gas to liquid process | |
Dieuzeide et al. | Glycerol steam reforming over Ni/mg/γ-Al2O3 catalysts effect of Ni (II) content | |
Liao et al. | Mediatory role of K, Cu and Mo over Ru/SiO2 catalysts for glycerol hydrogenolysis | |
WO2010016027A3 (en) | Autothermic catalytic reactor with flat temperature profile | |
Onyestyák | Outstanding efficiency of indium in bimetallic catalysts for hydroconversion of bioacids to bioalcohols | |
WO2009019395A3 (fr) | Utilisation de filtres a particules pour limiter la desactivation de catalyseurs | |
Pudi et al. | Conversion of Glycerol into value-added products over Cu–Ni catalyst supported on γ-Al2O3 and activated carbon | |
MY155825A (en) | A process for hydrocracking and hydro-isomerisation of a paraffinic feedstock | |
WO2013041516A3 (en) | Cooled reactor for the production of dimethyl ether from methanol | |
WO2008095629A8 (de) | Kohlenstoff-geträgerter goldkatalysator, verfahren zu seiner herstellung und verwendung zur oxidation von organischen verbindungen | |
Chiang et al. | Synthesis of alcohols and alkanes over potassium and vanadium promoted molybdenum carbides | |
Wang et al. | Effect of Pd loading and precursor on the catalytic performance of Pd/WO3–ZrO2 catalysts for selective oxidation of ethylene | |
CN105032421A (zh) | 凹凸棒石负载铜锆催化剂的制备方法及在甲醇水蒸气重整制氢反应中的应用 |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
FG | Grant or registration |