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MX2010007376A - Metodo y reactor para la preparacion de metanol. - Google Patents

Metodo y reactor para la preparacion de metanol.

Info

Publication number
MX2010007376A
MX2010007376A MX2010007376A MX2010007376A MX2010007376A MX 2010007376 A MX2010007376 A MX 2010007376A MX 2010007376 A MX2010007376 A MX 2010007376A MX 2010007376 A MX2010007376 A MX 2010007376A MX 2010007376 A MX2010007376 A MX 2010007376A
Authority
MX
Mexico
Prior art keywords
methanol
reactor
catalyst
gaseous phase
cooling surface
Prior art date
Application number
MX2010007376A
Other languages
English (en)
Inventor
Max Thorhauge
Original Assignee
Haldor Topsoe As
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Haldor Topsoe As filed Critical Haldor Topsoe As
Publication of MX2010007376A publication Critical patent/MX2010007376A/es

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J8/00Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/02Chemical 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
    • B01J8/06Chemical 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
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J8/00Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/02Chemical 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
    • B01J8/0285Heating or cooling the reactor
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J8/00Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/008Details of the reactor or of the particulate material; Processes to increase or to retard the rate of reaction
    • B01J8/009Membranes, e.g. feeding or removing reactants or products to or from the catalyst bed through a membrane
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J8/00Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/02Chemical 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
    • B01J8/0207Chemical 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
    • B01J8/0214Chemical 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
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J8/00Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/02Chemical 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
    • B01J8/0292Chemical 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
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J8/00Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/02Chemical 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
    • B01J8/06Chemical 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
    • B01J8/065Feeding reactive fluids
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J8/00Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/02Chemical 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
    • B01J8/06Chemical 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
    • B01J8/067Heating or cooling the reactor
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C29/00Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring
    • C07C29/15Preparation 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
    • C07C29/151Preparation 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
    • C07C29/152Preparation 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
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C31/00Saturated compounds having hydroxy or O-metal groups bound to acyclic carbon atoms
    • C07C31/02Monohydroxylic acyclic alcohols
    • C07C31/04Methanol
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2208/00Processes carried out in the presence of solid particles; Reactors therefor
    • B01J2208/00008Controlling the process
    • B01J2208/00017Controlling the temperature
    • B01J2208/00106Controlling the temperature by indirect heat exchange
    • B01J2208/00115Controlling the temperature by indirect heat exchange with heat exchange elements inside the bed of solid particles
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2208/00Processes carried out in the presence of solid particles; Reactors therefor
    • B01J2208/00008Controlling the process
    • B01J2208/00017Controlling the temperature
    • B01J2208/00106Controlling the temperature by indirect heat exchange
    • B01J2208/00115Controlling the temperature by indirect heat exchange with heat exchange elements inside the bed of solid particles
    • B01J2208/00123Fingers
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2208/00Processes carried out in the presence of solid particles; Reactors therefor
    • B01J2208/00008Controlling the process
    • B01J2208/00017Controlling the temperature
    • B01J2208/00106Controlling the temperature by indirect heat exchange
    • B01J2208/00115Controlling the temperature by indirect heat exchange with heat exchange elements inside the bed of solid particles
    • B01J2208/00132Tubes
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2208/00Processes carried out in the presence of solid particles; Reactors therefor
    • B01J2208/00008Controlling the process
    • B01J2208/00017Controlling the temperature
    • B01J2208/00106Controlling the temperature by indirect heat exchange
    • B01J2208/00115Controlling the temperature by indirect heat exchange with heat exchange elements inside the bed of solid particles
    • B01J2208/0015Plates; Cylinders
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2208/00Processes carried out in the presence of solid particles; Reactors therefor
    • B01J2208/00008Controlling the process
    • B01J2208/00017Controlling the temperature
    • B01J2208/00106Controlling the temperature by indirect heat exchange
    • B01J2208/00168Controlling the temperature by indirect heat exchange with heat exchange elements outside the bed of solid particles
    • B01J2208/00212Plates; Jackets; Cylinders
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2219/00Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/00761Details of the reactor
    • B01J2219/00763Baffles
    • B01J2219/00765Baffles attached to the reactor wall
    • B01J2219/0077Baffles attached to the reactor wall inclined
    • B01J2219/00772Baffles attached to the reactor wall inclined in a helix
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00Technologies relating to chemical industry
    • Y02P20/50Improvements relating to the production of bulk chemicals
    • Y02P20/52Improvements 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 método y 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 o la temperatura de un agente de enfriamiento líquido que está en contacto indirecto con las partículas de catalizador y al proporcionar una relación específica del volumen de lecho de catalizador con respecto al área de superficie de enfriamiento. Por esa razón, la condensación de metanol a medida que se forma en la fase gaseosa toma lugar para la mayoría en la superficie de enfriamiento dispuesta que está distribuida uniformemente dentro del reactor y si acaso dentro de una región muy limitada del lecho de catalizador. La figura más representativa de la invención es la número 1a.
MX2010007376A 2008-02-25 2009-02-12 Metodo y reactor para la preparacion de metanol. MX2010007376A (es)

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
DKPA200800260 2008-02-25
DKPA200800261 2008-02-25
PCT/EP2009/000974 WO2009106232A1 (en) 2008-02-25 2009-02-12 Method and reactor for the preparation of methanol

Publications (1)

Publication Number Publication Date
MX2010007376A true MX2010007376A (es) 2010-08-11

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 Before (1)

Application Number Title Priority Date Filing Date
MX2010008947A MX2010008947A (es) 2008-02-25 2009-02-12 Reactor para la preparacion de metanol.

Country Status (17)

Country Link
US (3) US8513314B2 (es)
EP (3) EP2249958B1 (es)
JP (2) JP2011515334A (es)
KR (2) KR20100122898A (es)
CN (2) CN101959586B (es)
AT (2) ATE521407T1 (es)
AU (2) AU2009218828B2 (es)
BR (2) BRPI0906447B1 (es)
CA (2) CA2730916C (es)
EA (2) EA019311B1 (es)
ES (3) ES2372670T3 (es)
MX (2) MX2010008947A (es)
NZ (2) NZ586789A (es)
PL (3) PL2257366T3 (es)
RU (1) RU2481151C2 (es)
WO (2) WO2009106231A1 (es)
ZA (2) ZA201004473B (es)

Families Citing this family (34)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
BR112012029429B1 (pt) 2010-05-20 2018-07-17 Haldor Topsoe A/S método e aparelho para a separação de líquido de um fluxo de alimentação de gás em um reator catalítico.
KR101717121B1 (ko) 2010-06-24 2017-03-16 할도르 토프쉐 에이/에스 메탄올 및 암모니아의 공동 제조
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
CN107835713B (zh) * 2015-07-15 2021-07-13 托普索公司 催化反应器
CA2993958A1 (en) * 2015-07-29 2017-02-02 Primus Green Energy Inc. Two-stage reactor for exothermal and reversible reactions and methods thereof
US10676416B2 (en) 2016-01-07 2020-06-09 Total Raffinage Chimie Process for methanol synthesis using an indium oxide based catalyst
WO2017118572A1 (en) 2016-01-07 2017-07-13 Total Research & Technology Feluy Supported indium oxide catalyst and process for methanol synthesis using the same
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
DE102016204717A1 (de) * 2016-03-22 2017-09-28 Siemens Aktiengesellschaft Reaktor zur Durchführung von gleichgewichtslimitierten Reaktionen
DE102016204718A1 (de) 2016-03-22 2017-09-28 Siemens Aktiengesellschaft Reaktor
US10478798B2 (en) * 2016-03-30 2019-11-19 Haldor Topsoe A/S Methanol synthesis process layout for large production capacity
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
WO2018210827A1 (en) 2017-05-17 2018-11-22 Total Research & Technology Feluy Mto-ocp upgrading process to maximize the selectivity to propylene
EP3404005A1 (en) 2017-05-17 2018-11-21 Total Research & Technology Feluy Process for ethylene oligomerisation from diluted stream
WO2018210826A1 (en) 2017-05-17 2018-11-22 Total Research & Technology Feluy Process for ethylene aromatisation from diluted stream
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
EP3846936A1 (en) 2018-09-06 2021-07-14 Total Se 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
EP3917903A1 (en) 2019-02-01 2021-12-08 Total Se Process using catalytic composition for the conversion of syngas to higher alcohols
EP4021631B1 (en) * 2019-08-27 2025-06-25 SABIC Global Technologies, B.V. Mass transfer swirler including distribution member
US12434213B2 (en) 2019-09-20 2025-10-07 Sabic Global Technologies B.V. Reactor tube assembly
AU2020355652B2 (en) * 2019-09-27 2025-10-23 Sumitomo Chemical Company, Limited Chemical reaction method and chemical reaction device
JP2021154230A (ja) * 2020-03-27 2021-10-07 三菱パワー株式会社 ガス状生成物を得るための装置およびガス状生成物を得るための方法
CN115989081B (zh) * 2020-08-31 2025-04-01 住友化学株式会社 化学反应方法、化学反应装置和制造方法
US20230312444A1 (en) * 2020-08-31 2023-10-05 Sumitomo Chemical Company, Limited Method for producing methanol
US12049438B2 (en) 2020-11-17 2024-07-30 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
CN115597405A (zh) * 2022-10-11 2023-01-13 浙江软控智能科技有限公司(Cn) 浆料高效冷却器
WO2024257435A1 (ja) * 2023-06-14 2024-12-19 本田技研工業株式会社 反応器

Family Cites Families (37)

* Cited by examiner, † Cited by third party
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
CA2166564A1 (en) 1993-07-05 1995-01-19 Christine Jeannine Bernadette Girod Process and apparatus for controlling reaction temperatures
SG59974A1 (en) * 1995-04-10 1999-02-22 Air Prod & Chem Process for operating equilibrium controlled reactions
AU3406297A (en) * 1996-07-25 1998-02-20 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
CA2292178C (en) * 1998-12-07 2003-07-15 Mitsubishi Heavy Industries, Ltd. Method of manufacturing 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
JP5089008B2 (ja) * 2000-09-26 2012-12-05 シエル・インターナシヨナル・リサーチ・マートスハツペイ・ベー・ヴエー 反応管におけるロッド状インサート
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

Also Published As

Publication number Publication date
CA2713874A1 (en) 2009-09-03
EP2249958A1 (en) 2010-11-17
US20100312021A1 (en) 2010-12-09
CN101959585A (zh) 2011-01-26
ZA201004473B (en) 2011-09-28
BRPI0907815B1 (pt) 2021-04-06
EA019311B1 (ru) 2014-02-28
ATE516876T1 (de) 2011-08-15
CA2730916A1 (en) 2009-09-03
BRPI0906447A2 (pt) 2021-02-23
NZ586789A (en) 2011-10-28
AU2009218828A1 (en) 2009-09-03
WO2009106231A1 (en) 2009-09-03
MX2010008947A (es) 2010-09-07
BRPI0907815A2 (pt) 2020-08-18
KR20100138884A (ko) 2010-12-31
KR20100122898A (ko) 2010-11-23
ATE521407T1 (de) 2011-09-15
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RU2481151C2 (ru) 2013-05-10
PL2374533T3 (pl) 2013-09-30
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PL2249958T3 (pl) 2012-01-31
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AU2009218827A1 (en) 2009-09-03
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CN101959586A (zh) 2011-01-26
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EP2374533B8 (en) 2013-08-28

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