EA201000156A1 - Способ проведения эндотермической реакции - Google Patents

Способ проведения эндотермической реакции

Info

Publication number
EA201000156A1
EA201000156A1 EA201000156A EA201000156A EA201000156A1 EA 201000156 A1 EA201000156 A1 EA 201000156A1 EA 201000156 A EA201000156 A EA 201000156A EA 201000156 A EA201000156 A EA 201000156A EA 201000156 A1 EA201000156 A1 EA 201000156A1
Authority
EA
Eurasian Patent Office
Prior art keywords
carrying
catalyst
endothermic reaction
heating medium
flow
Prior art date
Application number
EA201000156A
Other languages
English (en)
Other versions
EA017645B1 (ru
Inventor
Петер Хубертус Кёстерс
Original Assignee
Сауди Бейсик Индастриз Корпорейшн
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 Сауди Бейсик Индастриз Корпорейшн filed Critical Сауди Бейсик Индастриз Корпорейшн
Publication of EA201000156A1 publication Critical patent/EA201000156A1/ru
Publication of EA017645B1 publication Critical patent/EA017645B1/ru

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
    • B01J8/062Chemical 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 being installed in a furnace
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J19/00Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J19/0053Details of the reactor
    • B01J19/006Baffles
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J19/00Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J19/24Stationary reactors without moving elements inside
    • B01J19/2415Tubular reactors
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J19/00Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J19/24Stationary reactors without moving elements inside
    • B01J19/2415Tubular reactors
    • B01J19/2425Tubular reactors in parallel
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C5/00Preparation of hydrocarbons from hydrocarbons containing the same number of carbon atoms
    • C07C5/32Preparation of hydrocarbons from hydrocarbons containing the same number of carbon atoms by dehydrogenation with formation of free hydrogen
    • C07C5/327Formation of non-aromatic carbon-to-carbon double bonds only
    • C07C5/333Catalytic processes
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C5/00Preparation of hydrocarbons from hydrocarbons containing the same number of carbon atoms
    • C07C5/32Preparation of hydrocarbons from hydrocarbons containing the same number of carbon atoms by dehydrogenation with formation of free hydrogen
    • C07C5/327Formation of non-aromatic carbon-to-carbon double bonds only
    • C07C5/333Catalytic processes
    • C07C5/3335Catalytic processes with metals
    • C07C5/3337Catalytic processes with metals of the platinum group
    • 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
    • B01J2208/00504Controlling the temperature by means of a burner
    • 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
    • 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
    • B01J2219/24Stationary reactors without moving elements inside
    • B01J2219/2401Reactors comprising multiple separate flow channels
    • B01J2219/2402Monolithic-type reactors
    • B01J2219/2409Heat exchange aspects
    • B01J2219/2411The reactant being in indirect heat exchange with a non reacting heat exchange medium
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C2521/00Catalysts comprising the elements, oxides or hydroxides of magnesium, boron, aluminium, carbon, silicon, titanium, zirconium or hafnium
    • C07C2521/02Boron or aluminium; Oxides or hydroxides thereof
    • C07C2521/04Alumina
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C2523/00Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00
    • C07C2523/38Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00 of noble metals
    • C07C2523/54Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00 of noble metals combined with metals, oxides or hydroxides provided for in groups C07C2523/02 - C07C2523/36
    • C07C2523/56Platinum group metals
    • C07C2523/62Platinum group metals with gallium, indium, thallium, germanium, tin or lead
    • 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
    • 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
    • Y02P20/584Recycling of catalysts

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)
  • Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
  • Catalysts (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Abstract

Способ проведения эндотермической реакции в реакторе с находящимися в нём катализаторными трубами, содержащими катализатор, ускоряющий эндотермическую реакцию, включающий стадии: а) контактирование содержащегося в катализаторных трубах катализатора с сырьевым потоком, проходящим через каналы от входного конца к выходному концу; b) контактирование внешней поверхности катализаторных труб с потоком нагревающей среды, имеющей некоторую начальную температуру нагрева и протекающей прямоточно с потоком сырья, с целью конвекционного нагрева поверхности; с) смешение по крайней мере части нагревающей среды после её контактирования с катализаторными трубами с потоком свежей нагревающей среды, имеющей исходную температуру более высокую, чем начальная температура нагрева, в результате чего образуется прямоточная нагревающая среда, имеющая начальную температуру нагрева, и реактор для проведения процесса.
EA201000156A 2007-07-05 2008-06-25 Способ проведения эндотермической реакции EA017645B1 (ru)

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
EP07013192 2007-07-05
EP07022847 2007-11-26
PCT/EP2008/005265 WO2009003647A1 (en) 2007-07-05 2008-06-25 Process for performing an endothermic reaction

Publications (2)

Publication Number Publication Date
EA201000156A1 true EA201000156A1 (ru) 2010-06-30
EA017645B1 EA017645B1 (ru) 2013-02-28

Family

ID=39717824

Family Applications (1)

Application Number Title Priority Date Filing Date
EA201000156A EA017645B1 (ru) 2007-07-05 2008-06-25 Способ проведения эндотермической реакции

Country Status (11)

Country Link
US (2) US8916737B2 (ru)
EP (1) EP2173469B1 (ru)
JP (3) JP6009732B2 (ru)
CN (1) CN101687162B (ru)
BR (1) BRPI0814196A2 (ru)
CA (1) CA2691566C (ru)
EA (1) EA017645B1 (ru)
ES (1) ES2496171T3 (ru)
IL (1) IL202831A (ru)
MX (1) MX2009014078A (ru)
WO (1) WO2009003647A1 (ru)

Families Citing this family (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US8608696B1 (en) 2009-02-24 2013-12-17 North Carolina State University Rapid fluid cooling devices and methods for cooling fluids
DE102009012663B3 (de) * 2009-03-13 2010-09-16 Uhde Gmbh Verfahren und Vorrichtung zur gleichmäßigen Dampferzeugung aus der Abwärme einer Alkandehydrierung
EP2671634B1 (en) * 2012-06-08 2017-08-09 L'air Liquide, Societe Anonyme Pour L'etude Et L'exploitation Des Procedes Georges Claude Method to homogenize the tube temperatures between tubes during processes involving heating of gas flowing in the tubes
WO2016038557A1 (en) 2014-09-12 2016-03-17 Sabic Global Technologies B.V. Embedded alkane dehydrogenation systems and processes
TWI613007B (zh) 2015-06-08 2018-02-01 Ihi股份有限公司 反應器
US10987646B2 (en) * 2015-10-28 2021-04-27 Haldor Topsøe A/S Dehydrogenation of alkanes
WO2017134225A1 (en) * 2016-02-04 2017-08-10 Technip France Method for reducing temperature spread in reformer
US10518236B2 (en) 2016-06-09 2019-12-31 Sabic Global Technologies B.V. Systems for heating multi-tubular reactors
JP2018084308A (ja) 2016-11-25 2018-05-31 株式会社Ihi 圧力容器
US10544371B2 (en) * 2018-05-11 2020-01-28 Intramicron, Inc. Channel reactors
US11920078B2 (en) 2019-11-20 2024-03-05 Lummus Technology Llc Heat storage in chemical reactors
JP7467192B2 (ja) 2020-03-25 2024-04-15 三菱重工業株式会社 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

Family Cites Families (30)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2945077A (en) * 1955-12-01 1960-07-12 Phillips Petroleum Co Process and apparatus for pressure and temperature control system
US3453087A (en) * 1964-06-25 1969-07-01 Girdler Corp Modular reformer furnace
GB1367453A (en) 1970-09-25 1974-09-18 Topsoe H F A Furnace design
US3958951A (en) * 1974-04-09 1976-05-25 Stone & Webster Engineering Corporation Convective power reformer equipment and system
NL187622C (nl) * 1975-04-14 1991-12-02 Stone & Webster Eng Corp Reformeeroven met convectieverhitting van de procesbuizen.
JPS5863783A (ja) 1981-10-13 1983-04-15 Babcock Hitachi Kk 改質装置
JPS5930705A (ja) * 1982-08-12 1984-02-18 Mitsubishi Heavy Ind Ltd 燃料改質装置
NL8401064A (nl) * 1984-04-04 1985-11-01 Dow Chemical Nederland Werkwijze voor de dehydrogenering van een koolwaterstof, een apparaat voor het uitvoeren van chemische reacties en een methode voor het daarin uitvoeren van die reacties.
US4769506A (en) 1985-03-21 1988-09-06 The Dow Chemical Company Method for dehydrogenating a hydrocarbon, an apparatus and method for conducting chemical reactions therein
JPS6339629A (ja) 1986-08-01 1988-02-20 Yamaha Motor Co Ltd 燃料電池用改質装置
GB2201903B (en) 1987-03-03 1990-11-28 Shell Int Research Apparatus and process suitable for producing hydrogen
FR2634396B1 (fr) * 1988-07-22 1990-09-14 Inst Francais Du Petrole Procede et appareillage de reformage basse pression des essences avec chauffage par des gaz de fumees
JPH07483B2 (ja) * 1988-10-27 1995-01-11 株式会社富士電機総合研究所 熱媒加熱式改質装置
JP3096302B2 (ja) 1989-12-11 2000-10-10 ゲブリユーダー ズルツアー アクチエンゲゼルシヤフト 不均一反応型の反応器及び反応器用触媒
FR2657273B1 (fr) * 1990-01-19 1992-05-15 Inst Francais Du Petrole Enceinte reactionnelle comprenant un reacteur calandre et des moyens de stratification du courant d'un fluide caloporteur.
JPH04190843A (ja) 1990-11-22 1992-07-09 Toshiba Corp ガス反応装置
DE69203938T2 (de) 1991-05-06 1996-02-08 Inst Francais Du Petrole Verfahren und Vorrichtung zur Dehydrierung von aliphatischen Kohlenwasserstoffen zu olefinischen Kohlenwasserstoffen.
US5247907A (en) 1992-05-05 1993-09-28 The M. W. Kellogg Company Process furnace with a split flue convection section
JP3202441B2 (ja) * 1993-10-08 2001-08-27 東京瓦斯株式会社 水素製造装置
JP3283958B2 (ja) 1993-04-13 2002-05-20 株式会社日立製作所 反応器およびその製造方法
US5935531A (en) 1993-10-29 1999-08-10 Mannesmann Aktiengesellschaft Catalytic reactor for endothermic reactions
US5562857A (en) 1995-12-22 1996-10-08 Bayer Corporation Azeotrope-like compositions of 1,1,1,3,3-pentafluoropropane and 2-methyl butane
JP4041567B2 (ja) 1997-12-25 2008-01-30 千代田化工建設株式会社 触媒改質型反応炉
GB2359764A (en) * 2000-03-01 2001-09-05 Geoffrey Gerald Weedon An endothermic tube reactor
DE10042746A1 (de) 2000-08-31 2002-03-28 Degussa Verfahren und Vorrichtung zum Durchführen von Reaktionen in einem Reaktor mit spaltförmigen Reaktionsräumen
US6781024B2 (en) * 2000-11-22 2004-08-24 Fina Technology, Inc. Dehydrogenation process
DE10229661A1 (de) 2001-10-09 2003-04-10 Linde Ag Verfahren zur Dehydrierung von Alkanen
JP3993023B2 (ja) * 2002-05-22 2007-10-17 東邦瓦斯株式会社 熱風循環装置
JP4401644B2 (ja) 2002-11-22 2010-01-20 三菱化学エンジニアリング株式会社 プレート型触媒反応装置及び(メタ)アクリル酸等の製造方法
JP2006097526A (ja) 2004-09-29 2006-04-13 Mitsubishi Heavy Ind Ltd 車両積載型水素製造システムのための昇温装置

Also Published As

Publication number Publication date
CA2691566A1 (en) 2009-01-08
US9492803B2 (en) 2016-11-15
EP2173469B1 (en) 2014-06-18
EA017645B1 (ru) 2013-02-28
ES2496171T3 (es) 2014-09-18
US8916737B2 (en) 2014-12-23
IL202831A0 (en) 2010-06-30
JP2010532707A (ja) 2010-10-14
CA2691566C (en) 2018-06-12
BRPI0814196A2 (pt) 2015-01-27
MX2009014078A (es) 2010-03-01
CN101687162A (zh) 2010-03-31
JP2015061726A (ja) 2015-04-02
EP2173469A1 (en) 2010-04-14
IL202831A (en) 2015-03-31
WO2009003647A1 (en) 2009-01-08
CN101687162B (zh) 2013-01-02
JP2016155120A (ja) 2016-09-01
US20100160705A1 (en) 2010-06-24
JP6009732B2 (ja) 2016-10-19
US20150064078A1 (en) 2015-03-05

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