MY163298A - Reactor for carrying out autothermal gas-phase dehydrogenation - Google Patents
Reactor for carrying out autothermal gas-phase dehydrogenationInfo
- 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
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.
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)
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 |
DE202014011409U1 (en) * | 2013-02-14 | 2020-04-21 | Jochen Gauer | Reactor for carrying out heterogeneously catalyzed gas phase reactions with monoliths |
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 |
CA2992255A1 (en) * | 2018-01-18 | 2019-07-18 | Nova Chemicals Corporation | Odh complex with on-line mixer unit and feed line cleaning |
AU2019210970B2 (en) | 2018-01-26 | 2023-02-16 | Basf Se | Solids-packed apparatus for performance of endothermic reactions with direct electrical heating |
Family Cites Families (12)
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 |
KR20000068068A (en) | 1997-06-06 | 2000-11-25 | 요트.게.아. 롤페즈 | 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 |
US8017085B2 (en) * | 2007-08-31 | 2011-09-13 | Unifrax I Llc | Substrate mounting system |
US7989511B2 (en) * | 2008-05-21 | 2011-08-02 | Texaco Inc. | Process and apparatus for synthesis gas and hydrocarbon production |
EP2506963B1 (en) * | 2009-12-01 | 2014-11-05 | Basf Se | Reactor for carrying out autothermal gas phase dehydrogenation |
KR20130130791A (en) * | 2010-12-21 | 2013-12-02 | 바스프 에스이 | Reactor for carrying out autothermal gas phase dehydration |
-
2012
- 2012-08-01 EP EP12740994.4A patent/EP2739388B1/en not_active Not-in-force
- 2012-08-01 WO PCT/EP2012/064988 patent/WO2013017609A1/en active Application Filing
- 2012-08-01 JP JP2014523310A patent/JP2014527463A/en active Pending
- 2012-08-01 EA EA201490315A patent/EA025292B1/en not_active IP Right Cessation
- 2012-08-01 CN CN201280036097.0A patent/CN103702753B/en not_active Expired - Fee Related
- 2012-08-01 MY MYPI2014000125A patent/MY163298A/en unknown
- 2012-08-01 KR KR1020147005009A patent/KR20140058579A/en not_active Application Discontinuation
Also Published As
Publication number | Publication date |
---|---|
JP2014527463A (en) | 2014-10-16 |
CN103702753A (en) | 2014-04-02 |
EA201490315A1 (en) | 2014-09-30 |
EA025292B1 (en) | 2016-12-30 |
WO2013017609A1 (en) | 2013-02-07 |
EP2739388A1 (en) | 2014-06-11 |
EP2739388B1 (en) | 2015-06-17 |
KR20140058579A (en) | 2014-05-14 |
CN103702753B (en) | 2015-07-08 |
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