MY163298A - Reactor for carrying out autothermal gas-phase dehydrogenation - Google Patents

Reactor for carrying out autothermal gas-phase dehydrogenation

Info

Publication number
MY163298A
MY163298A MYPI2014000125A MYPI2014000125A MY163298A MY 163298 A MY163298 A MY 163298A MY PI2014000125 A MYPI2014000125 A MY PI2014000125A MY PI2014000125 A MYPI2014000125 A MY PI2014000125A MY 163298 A MY163298 A MY 163298A
Authority
MY
Malaysia
Prior art keywords
reactor
inner region
carrying
catalytically active
gas
Prior art date
Application number
MYPI2014000125A
Inventor
Gerhard Olbert
Ulrike Wegerle
Grigorios Kolios
Herranz Carlos Tellaeche
Reinhold Höchst
Andrea Gienger
Roland Bauer
Original Assignee
Basf Se
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 Basf Se filed Critical Basf Se
Publication of MY163298A publication Critical patent/MY163298A/en

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
    • B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J19/24—Stationary reactors without moving elements inside
    • B01J19/248—Reactors comprising multiple separated flow channels
    • B01J19/2485—Monolithic 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
    • C07C5/32—Preparation of hydrocarbons from hydrocarbons containing the same number of carbon atoms by dehydrogenation with formation of free hydrogen
    • 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
    • B01J2219/00049—Controlling or regulating processes
    • B01J2219/00051—Controlling the temperature
    • B01J2219/0015—Controlling the temperature by thermal insulation means
    • B01J2219/00155—Controlling the temperature by thermal insulation means using insulating materials or refractories
    • 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
    • B01J2219/24—Stationary reactors without moving elements inside
    • B01J2219/2401—Reactors comprising multiple separate flow channels
    • B01J2219/2402—Monolithic-type reactors
    • B01J2219/2409—Heat exchange aspects
    • B01J2219/2411—The reactant being in indirect heat exchange with a non reacting heat exchange medium
    • 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
    • B01J2219/24—Stationary reactors without moving elements inside
    • B01J2219/2401—Reactors comprising multiple separate flow channels
    • B01J2219/2402—Monolithic-type reactors
    • B01J2219/2409—Heat exchange aspects
    • B01J2219/2416—Additional heat exchange means, e.g. electric resistance heater, coils
    • 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
    • B01J2219/24—Stationary reactors without moving elements inside
    • B01J2219/2401—Reactors comprising multiple separate flow channels
    • B01J2219/2402—Monolithic-type reactors
    • B01J2219/2418—Feeding means
    • B01J2219/2419—Feeding means for the reactants
    • 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
    • B01J2219/24—Stationary reactors without moving elements inside
    • B01J2219/2401—Reactors comprising multiple separate flow channels
    • B01J2219/2402—Monolithic-type reactors
    • B01J2219/2422—Mixing means, e.g. fins or baffles attached to the monolith or placed in the channel
    • 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
    • B01J2219/24—Stationary reactors without moving elements inside
    • B01J2219/2401—Reactors comprising multiple separate flow channels
    • B01J2219/2402—Monolithic-type reactors
    • B01J2219/2441—Other constructional details
    • B01J2219/2443—Assembling means of monolith modules
    • 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)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
  • Physical Or Chemical Processes And Apparatus (AREA)
  • Hydrogen, Water And Hydrids (AREA)
  • Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)
  • Catalysts (AREA)

Abstract

THE INVENTION RELATES TO A REACTOR (1) IN THE FORM OF A CYLINDER OR PRISM FOR CARRYING OUT AUTOTHERMAL GASAPHASE DEHYDROGENATION OF A GAS FLOW (2) CONTAINING HYDROCARBONS BY MEANS OF A GAS FLOW (3) CONTAINING OXYGEN SO AS TO OBTAIN A REACTION GAS MIXTURE, ON A HETEROGENEOUS CATALYST, WHICH IS DESIGNED AS A MONOLITH (4), THE INTERIOR OF THE REACTOR (1) BEING DIVIDED BY A CIRCULAR CYLINDRICAL OR PRISMATIC GAS-TIGHT HOUSING (G) ARRANGED IN THE LONGITUDINAL DIRECTION OF THE REACTOR (1) INTO AN INNER REGION (A) HAVING ONE OR MORE CATALYTICALLY ACTIVE ZONES (5), IN EACH OF WHICH A RESPECTIVE PACKING OF MONOLITHS (4) STACKED ONE ON THE OTHER, ONE NEXT TO THE OTHER, AND ONE BEHIND THE OTHER AND, BEFORE EACH CATALYTICALLY ACTIVE ZONE (5), A RESPECTIVE MIXING ZONE (6) HAVING FIXED INSTALLATIONS ARE PROVIDED, AND AN OUTER REGION (B) ARRANGED COAXIAL WITH THE INNER REGION (A), SAID REACTOR BEING CHARACTERIZED IN THAT THE INNER REGION (A) IS INSULATED FROM THE OUTER REGION (B) OF THE REACTOR BY MEANS OF A MICROPOROUS HIGH-PERFORMANCE INSULATING MATERIAL (15) HAVING A THERMAL CONDUCTIVITY VALUE () LESS THAN 0.05 W/M*K AT TEMPERATURES UP TO 700 °C.
MYPI2014000125A 2011-08-02 2012-08-01 Reactor for carrying out autothermal gas-phase dehydrogenation MY163298A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
EP11176343 2011-08-02

Publications (1)

Publication Number Publication Date
MY163298A true MY163298A (en) 2017-09-15

Family

ID=46598539

Family Applications (1)

Application Number Title Priority Date Filing Date
MYPI2014000125A MY163298A (en) 2011-08-02 2012-08-01 Reactor for carrying out autothermal gas-phase dehydrogenation

Country Status (7)

Country Link
EP (1) EP2739388B1 (en)
JP (1) JP2014527463A (en)
KR (1) KR20140058579A (en)
CN (1) CN103702753B (en)
EA (1) EA025292B1 (en)
MY (1) MY163298A (en)
WO (1) WO2013017609A1 (en)

Families Citing this family (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US9611191B2 (en) 2012-12-12 2017-04-04 Basf Se Reactor for carrying out an autothermal gas-phase dehydrogenation
EP2956236A1 (en) * 2013-02-14 2015-12-23 Basf Se Method for mounting monoliths in a reactor for carrying out heterogeneously catalyzed gas-phase reactions
US9616406B2 (en) 2013-02-14 2017-04-11 Basf Se Installing monoliths in a reactor for conducting heterogeneously catalyzed gas phase reactions
WO2016055453A1 (en) 2014-10-07 2016-04-14 Basf Se Reactor for carrying out gas-phase reactions using a heterogeneous catalytic converter
DE102016114713A1 (en) * 2016-08-09 2018-02-15 Thyssenkrupp Ag Synthesizer and method of making a product
CA2992255C (en) * 2018-01-18 2025-12-09 Nova Chemicals Corporation Odh complex with on-line mixer unit and feed line cleaning
WO2019145279A1 (en) 2018-01-26 2019-08-01 Basf Se Device packed with solid material for performing endothermic reactions with direct electrical heating

Family Cites Families (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE4026566C2 (en) 1990-08-22 1993-10-28 Eberspaecher J Exhaust gas purification device with two exhaust gas treatment bodies in a row
US6726884B1 (en) * 1996-06-18 2004-04-27 3M Innovative Properties Company Free-standing internally insulating liner
WO1998056112A2 (en) 1997-06-06 1998-12-10 Koninklijke Philips Electronics N.V. Oscillator frequency-drift compensation
DE19743667B4 (en) 1997-10-02 2004-07-01 Robert Bosch Gmbh Arrangement for regulating the boost pressure of an internal combustion engine
JP2002003204A (en) * 2000-06-15 2002-01-09 Toshiba Corp Fuel reformer
MY135793A (en) 2002-07-12 2008-06-30 Basf Ag Method for the production of butadiene from n-butane
DE102005061626A1 (en) * 2005-12-21 2007-06-28 Basf Ag Continuous heterogeneous catalyzed partial dehydrogenation of hydrocarbon involves feeding hydrocarbon to reaction chamber enclosed by shell made of specific steel, passing hydrocarbon through catalyst bed and dehydrogenating feed
US7842846B2 (en) 2006-03-30 2010-11-30 Basf Aktiengesellschaft Process for heterogeneously catalyzed partial dehydrogenation of at least one hydrocarbon to be dehydrogenated
JP5662798B2 (en) * 2007-08-31 2015-02-04 ユニフラックス ワン リミテッド ライアビリティ カンパニー Carrier mounting system
US7989511B2 (en) * 2008-05-21 2011-08-02 Texaco Inc. Process and apparatus for synthesis gas and hydrocarbon production
CA2782417A1 (en) * 2009-12-01 2011-06-09 Basf Se Reactor for carrying out autothermal gas-phase dehydrogenations
WO2012084609A1 (en) * 2010-12-21 2012-06-28 Basf Se Reactor for carrying out autothermal gas phase dehydration

Also Published As

Publication number Publication date
CN103702753B (en) 2015-07-08
EP2739388B1 (en) 2015-06-17
EP2739388A1 (en) 2014-06-11
KR20140058579A (en) 2014-05-14
EA025292B1 (en) 2016-12-30
JP2014527463A (en) 2014-10-16
WO2013017609A1 (en) 2013-02-07
CN103702753A (en) 2014-04-02
EA201490315A1 (en) 2014-09-30

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