ATE190302T1 - Apparatur zur katalytischen dehydrogenierung von kohlenwasserstoffen mit selektiver oxidation von wasserstoff - Google Patents

Apparatur zur katalytischen dehydrogenierung von kohlenwasserstoffen mit selektiver oxidation von wasserstoff

Info

Publication number
ATE190302T1
ATE190302T1 AT95942322T AT95942322T ATE190302T1 AT E190302 T1 ATE190302 T1 AT E190302T1 AT 95942322 T AT95942322 T AT 95942322T AT 95942322 T AT95942322 T AT 95942322T AT E190302 T1 ATE190302 T1 AT E190302T1
Authority
AT
Austria
Prior art keywords
oxygen
hydrocarbon
zone
containing stream
pct
Prior art date
Application number
AT95942322T
Other languages
English (en)
Inventor
Rune Lodeng
Pal Soraker
Original Assignee
Norske Stats Oljeselskap
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 Norske Stats Oljeselskap filed Critical Norske Stats Oljeselskap
Application granted granted Critical
Publication of ATE190302T1 publication Critical patent/ATE190302T1/de

Links

Classifications

    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C5/00—Preparation of hydrocarbons from hydrocarbons containing the same number of carbon atoms
    • C07C5/32—Preparation of hydrocarbons from hydrocarbons containing the same number of carbon atoms by dehydrogenation with formation of free hydrogen
    • C07C5/327—Formation of non-aromatic carbon-to-carbon double bonds only
    • C07C5/333—Catalytic processes
    • 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
    • B01J8/0492—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
    • B01J8/04—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
    • 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
    • B01J8/0457—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 placed in separate reactors
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C5/00—Preparation of hydrocarbons from hydrocarbons containing the same number of carbon atoms
    • C07C5/42—Preparation of hydrocarbons from hydrocarbons containing the same number of carbon atoms by dehydrogenation with a hydrogen acceptor
    • C07C5/48—Preparation of hydrocarbons from hydrocarbons containing the same number of carbon atoms by dehydrogenation with a hydrogen acceptor with oxygen as an acceptor

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Catalysts (AREA)
  • Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
  • Hydrogen, Water And Hydrids (AREA)
  • Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)
AT95942322T 1994-12-22 1995-12-18 Apparatur zur katalytischen dehydrogenierung von kohlenwasserstoffen mit selektiver oxidation von wasserstoff ATE190302T1 (de)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
NO944982A NO300117B1 (no) 1994-12-22 1994-12-22 Reaktor for dehydrogenering av hydrokarboner med selektiv oksidasjon av hydrogen
PCT/NO1995/000236 WO1996019424A1 (en) 1994-12-22 1995-12-18 A reactor for catalytic dehydrogenation of hydrocarbons with selective oxidation of hydrogen

Publications (1)

Publication Number Publication Date
ATE190302T1 true ATE190302T1 (de) 2000-03-15

Family

ID=19897780

Family Applications (1)

Application Number Title Priority Date Filing Date
AT95942322T ATE190302T1 (de) 1994-12-22 1995-12-18 Apparatur zur katalytischen dehydrogenierung von kohlenwasserstoffen mit selektiver oxidation von wasserstoff

Country Status (12)

Country Link
US (1) US5997826A (de)
EP (1) EP0799169B1 (de)
KR (1) KR100258656B1 (de)
CN (1) CN1070832C (de)
AT (1) ATE190302T1 (de)
AU (1) AU691715B2 (de)
BR (1) BR9510515A (de)
CA (1) CA2207038C (de)
DE (1) DE69515511D1 (de)
NO (1) NO300117B1 (de)
RU (1) RU2140895C1 (de)
WO (1) WO1996019424A1 (de)

Families Citing this family (56)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1127449C (zh) * 1998-07-08 2003-11-12 丰田自动车株式会社 燃料重整装置
DE19840018A1 (de) * 1998-09-02 2000-03-09 Fraunhofer Ges Forschung Verfahren und Vorrichtung zur Herstellung von Distickstoffpentoxid
NO310807B1 (no) * 1999-05-28 2001-09-03 Norske Stats Oljeselskap Forbehandling av katalysator
US6969506B2 (en) * 1999-08-17 2005-11-29 Battelle Memorial Institute Methods of conducting simultaneous exothermic and endothermic reactions
NO316512B1 (no) * 2000-01-25 2004-02-02 Statoil Asa Fremgangsmate og reaktor for autoterm dehydrogenering av hydrokarboner
EP1166864A1 (de) * 2000-06-30 2002-01-02 Casale Chemicals SA Verfahren zur Produktion von Formaldehyd
FR2813023B1 (fr) * 2000-08-17 2003-10-24 Inst Francais Du Petrole Dispositif de distribution permettant de realiser un melange polyphasique et reacteur associe
FR2813024B1 (fr) * 2000-08-17 2004-02-13 Inst Francais Du Petrole Dispositif d'injection d'un fluide place entre deux lits successifs permettant de realiser et de distribuer simultanement un melange polyphasique
WO2003078052A1 (en) * 2002-03-11 2003-09-25 Battelle Memorial Institute Microchannel reactors with temperature control
US8206666B2 (en) * 2002-05-21 2012-06-26 Battelle Memorial Institute Reactors having varying cross-section, methods of making same, and methods of conducting reactions with varying local contact time
US7402719B2 (en) * 2002-06-13 2008-07-22 Velocys Catalytic oxidative dehydrogenation, and microchannel reactors for catalytic oxidative dehydrogenation
US7195742B2 (en) * 2002-07-26 2007-03-27 Utc Fuel Cells, Llc Preferential oxidation reactor and process
US7250151B2 (en) 2002-08-15 2007-07-31 Velocys Methods of conducting simultaneous endothermic and exothermic reactions
US9192929B2 (en) 2002-08-15 2015-11-24 Velocys, Inc. Integrated combustion reactor and methods of conducting simultaneous endothermic and exothermic reactions
DE10251135B4 (de) * 2002-10-31 2006-07-27 Uhde Gmbh Verfahren zur katalytischen Dehydrierung von leichten Paraffinen zu Olefinen
DE10251262A1 (de) * 2002-11-04 2004-05-13 Basf Ag Verfahren zur Herstellung von Aldehyden aus Alkanen
US6989134B2 (en) * 2002-11-27 2006-01-24 Velocys Inc. Microchannel apparatus, methods of making microchannel apparatus, and processes of conducting unit operations
TW200422289A (en) 2003-02-18 2004-11-01 Bp Chem Int Ltd Auto thermal cracking reactor
US7405338B2 (en) * 2003-04-07 2008-07-29 Velocys Dehydrogenation reactions in narrow reaction chambers and integrated reactors
US7294734B2 (en) * 2003-05-02 2007-11-13 Velocys, Inc. Process for converting a hydrocarbon to an oxygenate or a nitrile
US7470408B2 (en) * 2003-12-18 2008-12-30 Velocys In situ mixing in microchannels
US8378163B2 (en) * 2004-03-23 2013-02-19 Velocys Corp. Catalysts having catalytic material applied directly to thermally-grown alumina and catalytic methods using same, improved methods of oxidative dehydrogenation
US7304198B2 (en) * 2004-05-14 2007-12-04 Battelle Memorial Institute Staged alkylation in microchannels
WO2006020709A1 (en) 2004-08-12 2006-02-23 Velocys Inc. Process for converting ethylene to ethylene oxide using microchannel process technology
US7622509B2 (en) 2004-10-01 2009-11-24 Velocys, Inc. Multiphase mixing process using microchannel process technology
US7468455B2 (en) * 2004-11-03 2008-12-23 Velocys, Inc. Process and apparatus for improved methods for making vinyl acetate monomer (VAM)
FR2877589B1 (fr) * 2004-11-09 2007-01-12 Inst Francais Du Petrole Reacteur a plusieurs zones en lit fixe ou mobile avec echangeur thermique integre
DE102004054657A1 (de) 2004-11-11 2006-05-18 Uhde Gmbh Verfahren zur katalytischen Dehydrierung von Propan zu Propylen
CA2586971C (en) 2004-11-12 2013-07-23 Velocys Inc. Process using microchannel technology for conducting alkylation or acylation reaction
CN102258968A (zh) 2004-11-16 2011-11-30 万罗赛斯公司 使用微通道技术的多相反应方法
US7507274B2 (en) 2005-03-02 2009-03-24 Velocys, Inc. Separation process using microchannel technology
WO2006127889A2 (en) 2005-05-25 2006-11-30 Velocys Inc. Support for use in microchannel processing
US20070004810A1 (en) * 2005-06-30 2007-01-04 Yong Wang Novel catalyst and fischer-tropsch synthesis process using same
JP5551871B2 (ja) 2005-07-08 2014-07-16 ヴェロシス，インク． マイクロチャネル技術を用いる触媒反応プロセス
KR101004487B1 (ko) 2005-09-08 2010-12-31 가시오게산키 가부시키가이샤 이동형 전자 장치의 전원공급용 개질기
KR101278795B1 (ko) 2005-11-03 2013-06-25 바스프 에스이 프로판으로부터 아크롤레인 또는 아크릴산 또는 그의혼합물을 수득하기 위한 안정한 연속 제조 방법
DE102005052923A1 (de) * 2005-11-03 2007-05-10 Basf Ag Verfahren zum stabilen Betreiben eines kontinuierlich ausgeübten Herstellprozesses zur Erzeugung von Acrolein, oder Acrylsäure oder deren Gemisch aus Propan
DE102005061626A1 (de) * 2005-12-21 2007-06-28 Basf Ag Verfahren der kontinuierlichen heterogen katalysierten partiellen Dehydrierung wenigstens eines zu dehydrierenden Kohlenwasserstoffs
RU2448080C2 (ru) * 2006-03-30 2012-04-20 Басф Се Способ гетерогенного каталитического парциального дегидрирования по меньшей мере одного подлежащего дегидрированию углеводорода
US7842846B2 (en) 2006-03-30 2010-11-30 Basf Aktiengesellschaft Process for heterogeneously catalyzed partial dehydrogenation of at least one hydrocarbon to be dehydrogenated
CN101460433B (zh) * 2006-03-30 2013-11-27 巴斯夫欧洲公司 至少一种待脱氢烃的多相催化部分脱氢方法
DE102006029790A1 (de) * 2006-06-27 2008-01-03 Basf Ag Verfahren der kontinuierlichen heterogen katalysierten partiellen Dehydrierung wenigstens eines zu dehydrierenden Kohlenwasserstoffs
US7999144B2 (en) 2006-09-01 2011-08-16 Velocys Microchannel apparatus and methods of conducting catalyzed oxidative dehydrogenation
DE102007006647A1 (de) 2007-02-06 2008-08-07 Basf Se Verfahren zur Regenerierung eines im Rahmen einer heterogen katalysierten partiellen Dehydrierung eines Kohlenwasserstoffs deaktivierten Katalysatorbetts
US8262755B2 (en) 2007-06-05 2012-09-11 Air Products And Chemicals, Inc. Staged membrane oxidation reactor system
US7745667B2 (en) * 2008-04-07 2010-06-29 Velocys Microchannel apparatus comprising structured walls, chemical processes, methods of making formaldehyde
MX2011009207A (es) * 2009-03-05 2011-12-14 Uop Llc Proceso para la deshidrogenacion de hidrocarburos.
CN103805234B (zh) * 2012-11-07 2015-09-02 中国石油化工股份有限公司 一种径流式渣油加氢处理反应器
US20140371503A1 (en) * 2013-06-18 2014-12-18 Uop Llc Single stage reactor system with oxidative preheat for dehydrogenation of hydrocarbons
CA2833822C (en) * 2013-11-21 2020-08-04 Nova Chemicals Corporation Inherently safe odh operation
WO2018037315A1 (en) * 2016-08-22 2018-03-01 Sabic Global Technologies B.V. Integrated method and system for hydrogen and ethylene production
CN111433182B (zh) * 2017-07-28 2023-04-04 罗门哈斯公司 通过使用非均相催化剂进行氧化酯化来生产甲基丙烯酸甲酯的方法
EP3476471A1 (de) * 2017-10-25 2019-05-01 Linde Aktiengesellschaft Verfahren und reaktor zur bildung und zur katalytischen umsetzung eines eduktgemischs
EP3848113A1 (de) 2020-01-07 2021-07-14 SABIC Global Technologies B.V. Systeme, vorrichtungen und verfahren eines reaktorspeisungsverteilungssystems
EP4172133B1 (de) * 2020-06-30 2023-10-04 Shell Internationale Research Maatschappij B.V. Verfahren zur oxidativen dehydrierung von ethan
CN113380431A (zh) * 2021-06-03 2021-09-10 哈尔滨工程大学 一种氢气复合器催化单元

Family Cites Families (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3502737A (en) * 1968-06-07 1970-03-24 Badger Co Ethylbenzene dehydrogenation
BE789153A (fr) * 1971-09-23 1973-03-22 Aquitaine Petrole Perfectionnement a la fabrication du styrene
SU1257069A1 (ru) * 1984-01-02 1986-09-15 Предприятие П/Я В-8296 Способ управлени процессом дегидрировани углеводородов
US4739124A (en) * 1985-09-16 1988-04-19 Uop Inc. Method for oxygen addition to oxidative reheat zone of ethane dehydrogenation process
US4891464A (en) * 1985-12-26 1990-01-02 Uop Control method for oxygen addition to oxidative reheat zone of hydrocarbon conversion process
US4731924A (en) * 1986-08-04 1988-03-22 American Telephone And Telegraph Company Method and apparatus for inserting multi-leaded articles into a substrate
US4806624A (en) * 1987-06-17 1989-02-21 Uop Inc. Dehydrogenation of dehydrogenatable hydrocarbons
US4778941A (en) * 1988-01-19 1988-10-18 Uop Inc. Eduction of intermediate effluent in dehydrogenation process having oxidative reheat
GB8807732D0 (en) * 1988-03-31 1988-05-05 Bp Chem Int Ltd Hydrocarbon dehydrogenation reactions
US4827066A (en) * 1988-05-23 1989-05-02 Uop Inc. Dehydrogenation of dehydrogenatable hydrocarbons
US4914249A (en) * 1988-12-29 1990-04-03 Uop Dehydrogenation of dehydrogenatable hydrocarbons
US5043500A (en) * 1989-12-20 1991-08-27 Uop Use of steam eductor to supply oxygen for oxidative reheating in dehydrogenation of C3 + hydrocarbons

Also Published As

Publication number Publication date
BR9510515A (pt) 1998-07-07
NO944982L (no) 1996-06-24
NO944982D0 (no) 1994-12-22
WO1996019424A1 (en) 1996-06-27
KR980700943A (ko) 1998-04-30
US5997826A (en) 1999-12-07
AU4357596A (en) 1996-07-10
EP0799169A1 (de) 1997-10-08
CA2207038C (en) 2002-02-12
KR100258656B1 (ko) 2000-06-15
EP0799169B1 (de) 2000-03-08
RU2140895C1 (ru) 1999-11-10
CA2207038A1 (en) 1996-06-27
CN1070832C (zh) 2001-09-12
CN1170397A (zh) 1998-01-14
NO300117B1 (no) 1997-04-14
DE69515511D1 (de) 2000-04-13
AU691715B2 (en) 1998-05-21

Similar Documents

Publication Publication Date Title
ATE190302T1 (de) Apparatur zur katalytischen dehydrogenierung von kohlenwasserstoffen mit selektiver oxidation von wasserstoff
NO944550L (no) Fremgangsmåte for katalytisk, delvis oksidasjon av hydrokarboner
RU97112487A (ru) Реактор для каталитического дегидрирования углеводородов избирательным оксидированием водорода
KR870003037A (ko) 탄화수소 접촉 탈수소화 공정
MXPA04005840A (es) Composicion catalitica para la deshidrogenacion de hidrocarburos alquilaromaticos.
ATE391761T1 (de) Methode zum nachrüsten von hydrobehandlungsreaktoren
AU2591088A (en) Production of olefins
MX9202577A (es) Proceso mejorado para la conversion de gas.
ATE134739T1 (de) Reaktor zur katalytischen behandlung gasförmiger fluide
ATE307790T1 (de) Verfahren und reaktor zur autothermischen dehydrogenierung von kohlenwasserstoffen
DE69526212D1 (de) Verbesserte verfahren und katalytische, struktur, benutzend integralen wärmeaustausch mit wahlweise vorgeschaltetem flammenhalter
AU3176193A (en) A purifying apparatus
KR860003972A (ko) 이산화탄소의 정제방법
CO4410399A1 (es) Procedimiento para la oxidacion parcial catalitica de hidro- carburos
KR870000273A (ko) 탄화수소 원료의 탈수소 방법
RU94017120A (ru) Металлуглеродный катализатор
KR970001288A (ko) 에틸벤젠을 스티렌으로 탈수소화시키는 방법
WO2001080992A3 (en) Rhodium cloth catalyst for partial oxidation of hydrocarbons
SU601041A1 (ru) Катализатор дл ароматизации бензиновой фракции
Moustafa et al. An integrated dehydrogenation-hydrogenation membrane reactor for the simultaneous production of styrene and cyclohexane
ES8505908A1 (es) Un procedimiento para deshidrogenar un hidrocarburo deshidrogenable
TH15378A (th) กรรมวิธีสำหรับออกซิเดชันบางส่วนด้วยตัวเร่งปฏิกิริยาของไฮโดรคาร์บอน
TH17652A (th) กรรมวิธีสำหรับออกซิเดชันแบบบางส่วนของไฮโดรคาร์บอนที่มีตัวเร่งปฏิกิริยา
TH44652A (th) วิธีการสำหรับการเปลี่ยนออกซิจิเนตไปเป็นโอเลฟิน

Legal Events

Date Code Title Description
RER Ceased as to paragraph 5 lit. 3 law introducing patent treaties