EA201400463A1 - Система катализаторного слоя для процесса эндотермического каталитического дегидрирования и способ эндотермического дегидрирования - Google Patents
Система катализаторного слоя для процесса эндотермического каталитического дегидрирования и способ эндотермического дегидрированияInfo
- Publication number
- EA201400463A1 EA201400463A1 EA201400463A EA201400463A EA201400463A1 EA 201400463 A1 EA201400463 A1 EA 201400463A1 EA 201400463 A EA201400463 A EA 201400463A EA 201400463 A EA201400463 A EA 201400463A EA 201400463 A1 EA201400463 A1 EA 201400463A1
- Authority
- EA
- Eurasian Patent Office
- Prior art keywords
- endothermal
- catalyst layer
- layer system
- dehydration
- dehydrogenation process
- Prior art date
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
- C07C5/3332—Catalytic processes with metal oxides or metal sulfides
-
- 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
- B01J8/0242—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 flow within the bed being predominantly vertical
- B01J8/025—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 flow within the bed being predominantly vertical in a cylindrical shaped bed
-
- 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
- B01J8/0285—Heating or cooling the reactor
-
- 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
- B01J8/0292—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 with stationary packing material in the bed, e.g. bricks, wire rings, baffles
-
- 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
- B01J8/0403—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 fluid flow within the beds being predominantly horizontal
- B01J8/0407—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 fluid flow within the beds being predominantly horizontal through two or more cylindrical annular shaped beds
- B01J8/0419—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 fluid flow within the beds being predominantly horizontal through two or more cylindrical annular shaped beds the beds being placed in separate reactors
-
- 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
- B01J8/0496—Heating or cooling the reactor
-
- 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
- C07C5/3335—Catalytic processes with metals
-
- 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
- B01J2208/00—Processes carried out in the presence of solid particles; Reactors therefor
- B01J2208/00008—Controlling the process
- B01J2208/00017—Controlling the temperature
- B01J2208/00522—Controlling the temperature using inert heat absorbing solids outside the bed
-
- 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
- B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
- B01J23/16—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
- B01J23/24—Chromium, molybdenum or tungsten
- B01J23/26—Chromium
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C2521/00—Catalysts comprising the elements, oxides or hydroxides of magnesium, boron, aluminium, carbon, silicon, titanium, zirconium or hafnium
- C07C2521/02—Boron or aluminium; Oxides or hydroxides thereof
- C07C2521/04—Alumina
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C2523/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00
- C07C2523/16—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00 of arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
- C07C2523/24—Chromium, molybdenum or tungsten
- C07C2523/26—Chromium
-
- 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)
- Physics & Mathematics (AREA)
- Fluid Mechanics (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
- Catalysts (AREA)
- Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)
Abstract
Изобретение относится к системе катализаторного слоя, включающей горизонтальный слой катализатора, включающий смесь по крайней мере одного катализатора и по крайней мере одного первого инертного материала, предварительно определенный объем по крайней мере одного второго инертного материала, расположенного выше по потоку от катализаторного слоя, где объем реактора над системой катализаторного слоя не заполнен каким-либо твердым материалом (свободное пространство). Система катализаторного слоя характеризуется тем, что соотношение объема второго инертного материала и объема реактора над вторым инертным материалом (свободное пространство) находится между 0,04 и 0,73, предпочтительно между 0,06 и 0,3, наиболее предпочтительно между 0,09 и 0,2. Изобретение относится также к способу дегидрирования, использующему данную систему катализаторного слоя.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
EP11186322.1A EP2586524A1 (en) | 2011-10-24 | 2011-10-24 | A catalyst bed system for an endothermic catalytic dehydrogenation process and an endothermic dehydrogenation process |
PCT/EP2012/070860 WO2013060640A1 (en) | 2011-10-24 | 2012-10-22 | A catalyst bed system for an endothermic catalytic dehydrogenation process and an endothermic dehydrogenation process |
Publications (2)
Publication Number | Publication Date |
---|---|
EA201400463A1 true EA201400463A1 (ru) | 2014-08-29 |
EA025815B1 EA025815B1 (ru) | 2017-01-30 |
Family
ID=47221311
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EA201400463A EA025815B1 (ru) | 2011-10-24 | 2012-10-22 | Система катализаторного слоя для процесса эндотермического каталитического дегидрирования и способ эндотермического дегидрирования |
Country Status (13)
Country | Link |
---|---|
US (1) | US9926241B2 (ru) |
EP (2) | EP2586524A1 (ru) |
KR (1) | KR101941616B1 (ru) |
CN (1) | CN103889567B (ru) |
BR (1) | BR112014009591B1 (ru) |
CA (1) | CA2851427C (ru) |
EA (1) | EA025815B1 (ru) |
IN (1) | IN2014KN01094A (ru) |
MX (1) | MX364478B (ru) |
MY (1) | MY171930A (ru) |
UA (1) | UA114610C2 (ru) |
WO (1) | WO2013060640A1 (ru) |
ZA (1) | ZA201402604B (ru) |
Families Citing this family (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US9873647B2 (en) | 2015-11-04 | 2018-01-23 | Exxonmobil Chemical Patents Inc. | Processes and systems for converting hydrocarbons to cyclopentadiene |
CN108349841B (zh) * | 2015-11-04 | 2021-04-20 | 埃克森美孚化学专利公司 | 集成的燃气涡轮和转化系统方法 |
WO2019025967A1 (en) * | 2017-07-31 | 2019-02-07 | Sabic Global Technologies B.V. | SYSTEM AND METHOD FOR DEHYDROGENATION OF ISOBUTANE ISOBUTYLENE |
US10836690B1 (en) | 2019-07-26 | 2020-11-17 | Tpc Group Llc | Dehydrogenation process and system with reactor re-sequencing |
Family Cites Families (14)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2419997A (en) | 1943-03-05 | 1947-05-06 | Houdry Process Corp | Catalytic dehydrogenation of aliphatic hydrocarbons |
NL301296A (ru) * | 1962-12-03 | 1900-01-01 | ||
US4560824A (en) | 1985-05-07 | 1985-12-24 | Air Products And Chemicals, Inc. | Heat balance control in catalytic dehydrogenation of isobutane |
US5510557A (en) * | 1994-02-28 | 1996-04-23 | Abb Lummus Crest Inc. | Endothermic catalytic dehydrogenation process |
NO316512B1 (no) * | 2000-01-25 | 2004-02-02 | Statoil Asa | Fremgangsmate og reaktor for autoterm dehydrogenering av hydrokarboner |
US6392113B1 (en) | 2000-10-03 | 2002-05-21 | Abb Lummus Global Inc. | Catalytic hydrocarbon dehydrogenation system with prereaction |
US8063261B2 (en) | 2002-01-14 | 2011-11-22 | Sud-Chemie Inc. | Multi-layered dehydrogenation catalyst system and process of use |
DE10237514A1 (de) | 2002-08-16 | 2004-02-26 | Basf Ag | Isothermes Verfahren zur Dehydrierung von Alkanen |
US7566429B2 (en) * | 2005-06-14 | 2009-07-28 | Sandia Corporation | Catalytic reactive separation system for energy-efficient production of cumene |
US7491860B2 (en) | 2005-08-03 | 2009-02-17 | Süd-Chemie Inc. | Dehydrogenation process |
US7973207B2 (en) | 2005-09-02 | 2011-07-05 | Sud-Chemie Inc. | Endothermic hydrocarbon conversion process |
US7622623B2 (en) | 2005-09-02 | 2009-11-24 | Sud-Chemie Inc. | Catalytically inactive heat generator and improved dehydrogenation process |
DE102006035718A1 (de) * | 2006-07-28 | 2008-01-31 | Basf Ag | Verfahren zum Langzeitbetrieb einer kontinuierlich betriebenen heterogen katalysierten partiellen Dehydrierung eines zu dehydrierenden Kohlenwasserstoffs |
CN101734987B (zh) | 2008-11-07 | 2012-11-21 | 中国石油化工股份有限公司 | 一种由c4烃制备乙烯、丙烯的方法 |
-
2011
- 2011-10-24 EP EP11186322.1A patent/EP2586524A1/en not_active Withdrawn
-
2012
- 2012-10-22 US US14/353,619 patent/US9926241B2/en active Active
- 2012-10-22 MX MX2014004909A patent/MX364478B/es active IP Right Grant
- 2012-10-22 CA CA2851427A patent/CA2851427C/en active Active
- 2012-10-22 MY MYPI2014001041A patent/MY171930A/en unknown
- 2012-10-22 KR KR1020147012124A patent/KR101941616B1/ko active IP Right Grant
- 2012-10-22 EP EP12790440.7A patent/EP2771101B1/en active Active
- 2012-10-22 IN IN1094KON2014 patent/IN2014KN01094A/en unknown
- 2012-10-22 WO PCT/EP2012/070860 patent/WO2013060640A1/en active Application Filing
- 2012-10-22 UA UAA201405215A patent/UA114610C2/uk unknown
- 2012-10-22 CN CN201280051896.5A patent/CN103889567B/zh active Active
- 2012-10-22 EA EA201400463A patent/EA025815B1/ru active IP Right Grant
- 2012-10-22 BR BR112014009591-4A patent/BR112014009591B1/pt active IP Right Grant
-
2014
- 2014-04-09 ZA ZA201402604A patent/ZA201402604B/en unknown
Also Published As
Publication number | Publication date |
---|---|
MX364478B (es) | 2019-04-29 |
MX2014004909A (es) | 2014-07-09 |
BR112014009591B1 (pt) | 2019-11-12 |
EP2771101A1 (en) | 2014-09-03 |
CA2851427A1 (en) | 2013-05-02 |
ZA201402604B (en) | 2019-10-30 |
EP2586524A1 (en) | 2013-05-01 |
CN103889567B (zh) | 2017-02-22 |
IN2014KN01094A (ru) | 2015-10-09 |
US9926241B2 (en) | 2018-03-27 |
US20140296606A1 (en) | 2014-10-02 |
MY171930A (en) | 2019-11-07 |
BR112014009591A2 (pt) | 2017-05-09 |
CN103889567A (zh) | 2014-06-25 |
UA114610C2 (uk) | 2017-07-10 |
KR20140084129A (ko) | 2014-07-04 |
KR101941616B1 (ko) | 2019-01-23 |
CA2851427C (en) | 2021-04-27 |
EA025815B1 (ru) | 2017-01-30 |
WO2013060640A1 (en) | 2013-05-02 |
EP2771101B1 (en) | 2019-08-21 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
EA201400487A1 (ru) | Способы получения и формирования нанесенных активных металлических катализаторов и предшественников | |
MX2015006893A (es) | Reactores y metodos para producir materiales de carbono solido. | |
EA201590225A1 (ru) | Способ и реакционная система для получения метанола | |
EA201400463A1 (ru) | Система катализаторного слоя для процесса эндотермического каталитического дегидрирования и способ эндотермического дегидрирования | |
EA201270706A1 (ru) | Способы получения стирола и катализаторы для применения в них | |
IN2015DN03885A (ru) | ||
WO2012030065A3 (en) | Catalyst composition for hydroformylation reaction and a hydroformylation process using the same | |
MX2018002024A (es) | Procedimiento para llevar a cabo reacciones limitadas por el equilibrio. | |
MX2016004485A (es) | Metodo para la produccion de compuestos fluorados. | |
MX2015010460A (es) | Un metodo para mitigar la formacion de hfc-245cb durante hidrofluoracion de hcfo-1233xf a hcfc-244bb. | |
EP3517499A4 (en) | POROUS CARBONACEOUS MATERIAL, PRODUCTION METHOD THEREOF AND SYNTHESIS REACTION CATALYST | |
MY171153A (en) | Supported noble-metal-comprising catalyst for oxidative dehydrogenation or epoxidation | |
MX2015001915A (es) | Un catalizador de deshidrogenacion para hidrocarburos y un metodo para la preparacion del mismo. | |
MX350643B (es) | Procedimiento para la produccion de acetato de vinilo. | |
EA201591496A1 (ru) | Способ установки монолитов в реактор для проведения гетерогенно-каталитических газофазных реакций | |
IN2014KN01659A (ru) | ||
EA201791087A1 (ru) | Синтез фишера-тропша | |
MY188899A (en) | Reactor and method for maximizing methanol yield by using catalyst layers | |
MY170588A (en) | Method for producing internal olefin | |
MY172078A (en) | Multihydric compound dehydration systems, catalyst compositions, and methods | |
IN2014DN07933A (ru) | ||
EA201791650A1 (ru) | Способ синтеза углеводородов | |
EA201591207A1 (ru) | Способ получения метилацетата | |
WO2014101900A3 (zh) | 一种低碳脂加氢制备乙醇的方法 | |
WO2014122421A3 (en) | Reactor and reaction method for reacting carbon monoxide and hydrogen in the presence of a carrier liquid to form a hydrocarbon product |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
MM4A | Lapse of a eurasian patent due to non-payment of renewal fees within the time limit in the following designated state(s) |
Designated state(s): AM AZ BY KG TJ TM |
|
RH4A | Grant of a duplicate of a eurasian patent |