EA017645B1 - Способ проведения эндотермической реакции - Google Patents
Способ проведения эндотермической реакции Download PDFInfo
- Publication number
- EA017645B1 EA017645B1 EA201000156A EA201000156A EA017645B1 EA 017645 B1 EA017645 B1 EA 017645B1 EA 201000156 A EA201000156 A EA 201000156A EA 201000156 A EA201000156 A EA 201000156A EA 017645 B1 EA017645 B1 EA 017645B1
- Authority
- EA
- Eurasian Patent Office
- Prior art keywords
- catalyst
- reactor
- pipes
- heating medium
- section
- Prior art date
Links
- 238000006243 chemical reaction Methods 0.000 title claims abstract description 85
- 238000000034 method Methods 0.000 title claims abstract description 40
- 230000008569 process Effects 0.000 title abstract description 8
- 238000010438 heat treatment Methods 0.000 claims abstract description 113
- 239000003054 catalyst Substances 0.000 claims abstract description 111
- 239000002994 raw material Substances 0.000 claims description 24
- 238000006356 dehydrogenation reaction Methods 0.000 claims description 12
- 239000003546 flue gas Substances 0.000 claims description 12
- 230000005855 radiation Effects 0.000 claims description 11
- YNQLUTRBYVCPMQ-UHFFFAOYSA-N Ethylbenzene Chemical compound CCC1=CC=CC=C1 YNQLUTRBYVCPMQ-UHFFFAOYSA-N 0.000 claims description 8
- 150000001335 aliphatic alkanes Chemical class 0.000 claims description 6
- 150000001336 alkenes Chemical class 0.000 claims description 5
- 239000004215 Carbon black (E152) Substances 0.000 claims description 2
- 229930195733 hydrocarbon Natural products 0.000 claims description 2
- 150000002430 hydrocarbons Chemical class 0.000 claims description 2
- 230000002829 reductive effect Effects 0.000 claims description 2
- 235000010469 Glycine max Nutrition 0.000 claims 1
- 244000068988 Glycine max Species 0.000 claims 1
- JRZJOMJEPLMPRA-UHFFFAOYSA-N olefin Natural products CCCCCCCC=C JRZJOMJEPLMPRA-UHFFFAOYSA-N 0.000 claims 1
- 238000002156 mixing Methods 0.000 abstract description 5
- 230000001737 promoting effect Effects 0.000 abstract 1
- 239000002609 medium Substances 0.000 description 68
- 239000000047 product Substances 0.000 description 27
- ATUOYWHBWRKTHZ-UHFFFAOYSA-N Propane Chemical compound CCC ATUOYWHBWRKTHZ-UHFFFAOYSA-N 0.000 description 18
- 238000012546 transfer Methods 0.000 description 15
- 239000010410 layer Substances 0.000 description 11
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 10
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 10
- 239000001294 propane Substances 0.000 description 9
- 238000004519 manufacturing process Methods 0.000 description 8
- 238000007086 side reaction Methods 0.000 description 8
- 230000015572 biosynthetic process Effects 0.000 description 7
- 230000008901 benefit Effects 0.000 description 6
- 239000000463 material Substances 0.000 description 6
- 239000000571 coke Substances 0.000 description 5
- 239000000203 mixture Substances 0.000 description 5
- 238000002485 combustion reaction Methods 0.000 description 4
- 230000000694 effects Effects 0.000 description 4
- 239000011261 inert gas Substances 0.000 description 4
- QQONPFPTGQHPMA-UHFFFAOYSA-N propylene Natural products CC=C QQONPFPTGQHPMA-UHFFFAOYSA-N 0.000 description 4
- 125000004805 propylene group Chemical group [H]C([H])([H])C([H])([*:1])C([H])([H])[*:2] 0.000 description 4
- WSFSSNUMVMOOMR-UHFFFAOYSA-N Formaldehyde Chemical compound O=C WSFSSNUMVMOOMR-UHFFFAOYSA-N 0.000 description 3
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 3
- 230000003197 catalytic effect Effects 0.000 description 3
- 238000000354 decomposition reaction Methods 0.000 description 3
- 238000013461 design Methods 0.000 description 3
- 239000007789 gas Substances 0.000 description 3
- 230000020169 heat generation Effects 0.000 description 3
- VLKZOEOYAKHREP-UHFFFAOYSA-N n-Hexane Chemical compound CCCCCC VLKZOEOYAKHREP-UHFFFAOYSA-N 0.000 description 3
- 230000035882 stress Effects 0.000 description 3
- IKHGUXGNUITLKF-UHFFFAOYSA-N Acetaldehyde Chemical compound CC=O IKHGUXGNUITLKF-UHFFFAOYSA-N 0.000 description 2
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- KAKZBPTYRLMSJV-UHFFFAOYSA-N Butadiene Chemical compound C=CC=C KAKZBPTYRLMSJV-UHFFFAOYSA-N 0.000 description 2
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 2
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 2
- RRHGJUQNOFWUDK-UHFFFAOYSA-N Isoprene Chemical compound CC(=C)C=C RRHGJUQNOFWUDK-UHFFFAOYSA-N 0.000 description 2
- IMNFDUFMRHMDMM-UHFFFAOYSA-N N-Heptane Chemical compound CCCCCCC IMNFDUFMRHMDMM-UHFFFAOYSA-N 0.000 description 2
- PPBRXRYQALVLMV-UHFFFAOYSA-N Styrene Chemical compound C=CC1=CC=CC=C1 PPBRXRYQALVLMV-UHFFFAOYSA-N 0.000 description 2
- 150000001875 compounds Chemical class 0.000 description 2
- 230000001419 dependent effect Effects 0.000 description 2
- 238000010790 dilution Methods 0.000 description 2
- 239000012895 dilution Substances 0.000 description 2
- 230000002349 favourable effect Effects 0.000 description 2
- 239000012530 fluid Substances 0.000 description 2
- 239000002737 fuel gas Substances 0.000 description 2
- NNPPMTNAJDCUHE-UHFFFAOYSA-N isobutane Chemical compound CC(C)C NNPPMTNAJDCUHE-UHFFFAOYSA-N 0.000 description 2
- 238000002955 isolation Methods 0.000 description 2
- QWTDNUCVQCZILF-UHFFFAOYSA-N isopentane Chemical compound CCC(C)C QWTDNUCVQCZILF-UHFFFAOYSA-N 0.000 description 2
- 230000000670 limiting effect Effects 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 238000005192 partition Methods 0.000 description 2
- 238000003825 pressing Methods 0.000 description 2
- 238000011084 recovery Methods 0.000 description 2
- 230000008439 repair process Effects 0.000 description 2
- 208000005156 Dehydration Diseases 0.000 description 1
- OTMSDBZUPAUEDD-UHFFFAOYSA-N Ethane Chemical compound CC OTMSDBZUPAUEDD-UHFFFAOYSA-N 0.000 description 1
- VQTUBCCKSQIDNK-UHFFFAOYSA-N Isobutene Chemical group CC(C)=C VQTUBCCKSQIDNK-UHFFFAOYSA-N 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 238000009825 accumulation Methods 0.000 description 1
- 150000001298 alcohols Chemical class 0.000 description 1
- 150000001299 aldehydes Chemical class 0.000 description 1
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 1
- 150000008064 anhydrides Chemical class 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 238000005452 bending Methods 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 239000001569 carbon dioxide Substances 0.000 description 1
- 229910002092 carbon dioxide Inorganic materials 0.000 description 1
- 150000001735 carboxylic acids Chemical class 0.000 description 1
- 238000004523 catalytic cracking Methods 0.000 description 1
- 229910010293 ceramic material Inorganic materials 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 230000006835 compression Effects 0.000 description 1
- 238000007906 compression Methods 0.000 description 1
- 239000000470 constituent Substances 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 230000008602 contraction Effects 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 230000018044 dehydration Effects 0.000 description 1
- 238000006297 dehydration reaction Methods 0.000 description 1
- 230000006866 deterioration Effects 0.000 description 1
- 150000001993 dienes Chemical class 0.000 description 1
- AFABGHUZZDYHJO-UHFFFAOYSA-N dimethyl butane Natural products CCCC(C)C AFABGHUZZDYHJO-UHFFFAOYSA-N 0.000 description 1
- -1 ethylene, propylene Chemical group 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- 238000011049 filling Methods 0.000 description 1
- 239000012737 fresh medium Substances 0.000 description 1
- 239000013505 freshwater Substances 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 238000007731 hot pressing Methods 0.000 description 1
- 239000012774 insulation material Substances 0.000 description 1
- 230000002427 irreversible effect Effects 0.000 description 1
- 239000001282 iso-butane Substances 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 229910001092 metal group alloy Inorganic materials 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- TVMXDCGIABBOFY-UHFFFAOYSA-N octane Chemical compound CCCCCCCC TVMXDCGIABBOFY-UHFFFAOYSA-N 0.000 description 1
- 230000003287 optical effect Effects 0.000 description 1
- 238000005839 oxidative dehydrogenation reaction Methods 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 238000004806 packaging method and process Methods 0.000 description 1
- 230000036961 partial effect Effects 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 239000011253 protective coating Substances 0.000 description 1
- 239000000376 reactant Substances 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 238000002407 reforming Methods 0.000 description 1
- 230000008929 regeneration Effects 0.000 description 1
- 238000011069 regeneration method Methods 0.000 description 1
- 230000000284 resting effect Effects 0.000 description 1
- 229930195734 saturated hydrocarbon Natural products 0.000 description 1
- 239000011949 solid catalyst Substances 0.000 description 1
- 239000010935 stainless steel Substances 0.000 description 1
- 229910001220 stainless steel Inorganic materials 0.000 description 1
- 239000007858 starting material Substances 0.000 description 1
- 230000004936 stimulating effect Effects 0.000 description 1
- 230000008646 thermal stress Effects 0.000 description 1
- 230000009466 transformation Effects 0.000 description 1
- 238000011144 upstream manufacturing Methods 0.000 description 1
- 238000003466 welding Methods 0.000 description 1
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
- 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
- B01J8/06—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 in tube reactors; the solid particles being arranged in tubes
- B01J8/062—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 in tube reactors; the solid particles being arranged in tubes being installed in a furnace
-
- 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
- B01J19/0053—Details of the reactor
- B01J19/006—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
- B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J19/24—Stationary reactors without moving elements inside
- B01J19/2415—Tubular 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
- B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J19/24—Stationary reactors without moving elements inside
- B01J19/2415—Tubular reactors
- B01J19/2425—Tubular reactors in parallel
-
- 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
-
- 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
- C07C5/3337—Catalytic processes with metals of the platinum group
-
- 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
- B01J2208/00504—Controlling the temperature by means of a burner
-
- 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
- B01J2219/00761—Details of the reactor
- B01J2219/00763—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
- 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
-
- 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
- C07C2523/38—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00 of noble metals
- C07C2523/54—Catalysts 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
- C07C2523/56—Platinum group metals
- C07C2523/62—Platinum group metals with gallium, indium, thallium, germanium, tin or lead
-
- 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
-
- 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
- Y02P20/584—Recycling 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)
- Catalysts (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
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 EA201000156A1 (ru) | 2010-06-30 |
| EA017645B1 true 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 (cg-RX-API-DMAC7.html) |
| EP (1) | EP2173469B1 (cg-RX-API-DMAC7.html) |
| JP (3) | JP6009732B2 (cg-RX-API-DMAC7.html) |
| CN (1) | CN101687162B (cg-RX-API-DMAC7.html) |
| BR (1) | BRPI0814196A2 (cg-RX-API-DMAC7.html) |
| CA (1) | CA2691566C (cg-RX-API-DMAC7.html) |
| EA (1) | EA017645B1 (cg-RX-API-DMAC7.html) |
| ES (1) | ES2496171T3 (cg-RX-API-DMAC7.html) |
| IL (1) | IL202831A (cg-RX-API-DMAC7.html) |
| MX (1) | MX2009014078A (cg-RX-API-DMAC7.html) |
| WO (1) | WO2009003647A1 (cg-RX-API-DMAC7.html) |
Families Citing this family (17)
| 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 |
| US10246386B2 (en) * | 2014-09-12 | 2019-04-02 | Sabic Global Technologies B.V. | Embedded alkane dehydrogenation systems and processes |
| CA2987457C (en) | 2015-06-08 | 2020-04-07 | Ihi Corporation | Multilayer reactor utilizing heat exchange |
| WO2017072057A1 (en) * | 2015-10-28 | 2017-05-04 | Haldor Topsøe A/S | Dehydrogenation of alkanes |
| CN108778988B (zh) * | 2016-02-04 | 2022-08-19 | 法国德西尼布 | 降低重整器中温度扩散的方法 |
| WO2017212341A1 (en) | 2016-06-09 | 2017-12-14 | 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 |
| CN114728251B (zh) * | 2019-11-20 | 2025-03-21 | 鲁姆斯科技有限责任公司 | 化学反应器中的热存储 |
| 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 |
| FR3114590B1 (fr) * | 2020-09-25 | 2022-09-09 | Ifp Energies Now | Procédé de deshydrogenation de l’éthanol en reacteur multitubulaire |
| US20240101418A1 (en) * | 2022-09-23 | 2024-03-28 | Tushar P. Vispute | Method for carbon formation free operation of reformers |
| CN119771278A (zh) * | 2023-10-07 | 2025-04-08 | 北京化工大学 | 一种管壳式换热反应装置及反应方法 |
| KR20250134948A (ko) * | 2024-03-05 | 2025-09-12 | 주식회사 엘지화학 | 전기 가열 반응기 |
| CN119951422B (zh) * | 2025-04-09 | 2025-06-20 | 苏州大学 | 一种多级流化循环反应系统的加热控制方法 |
Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3453087A (en) * | 1964-06-25 | 1969-07-01 | Girdler Corp | Modular reformer furnace |
| GB1549736A (en) * | 1975-04-14 | 1979-08-08 | Stone & Webster Eng Corp | Convective power reformer equipment and system |
| 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 |
| GB2201903A (en) * | 1987-03-03 | 1988-09-14 | Shell Int Research | Apparatus and process suitable for producing hydrogen |
| US6191332B1 (en) * | 1991-05-06 | 2001-02-20 | Institut Francais Du Petrole | Method and apparatus for dehydrogenating aliphatic hydrocarbons to olefinic hydrocarbons |
Family Cites Families (24)
| 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 |
| 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 |
| 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. |
| JPS6339629A (ja) | 1986-08-01 | 1988-02-20 | Yamaha Motor Co Ltd | 燃料電池用改質装置 |
| 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 |
| 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 |
| 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 |
-
2008
- 2008-06-25 EP EP08759353.9A patent/EP2173469B1/en active Active
- 2008-06-25 CA CA2691566A patent/CA2691566C/en active Active
- 2008-06-25 ES ES08759353.9T patent/ES2496171T3/es active Active
- 2008-06-25 US US12/452,362 patent/US8916737B2/en active Active
- 2008-06-25 MX MX2009014078A patent/MX2009014078A/es active IP Right Grant
- 2008-06-25 WO PCT/EP2008/005265 patent/WO2009003647A1/en not_active Ceased
- 2008-06-25 EA EA201000156A patent/EA017645B1/ru active IP Right Revival
- 2008-06-25 BR BRPI0814196-7A2A patent/BRPI0814196A2/pt not_active IP Right Cessation
- 2008-06-25 CN CN2008800235175A patent/CN101687162B/zh not_active Expired - Fee Related
- 2008-06-25 JP JP2010513759A patent/JP6009732B2/ja not_active Expired - Fee Related
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2009
- 2009-12-20 IL IL202831A patent/IL202831A/en active IP Right Grant
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2014
- 2014-09-29 JP JP2014198977A patent/JP2015061726A/ja active Pending
- 2014-11-07 US US14/536,093 patent/US9492803B2/en not_active Expired - Fee Related
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2016
- 2016-02-03 JP JP2016018705A patent/JP2016155120A/ja not_active Abandoned
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3453087A (en) * | 1964-06-25 | 1969-07-01 | Girdler Corp | Modular reformer furnace |
| GB1549736A (en) * | 1975-04-14 | 1979-08-08 | Stone & Webster Eng Corp | Convective power reformer equipment and system |
| 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 |
| GB2201903A (en) * | 1987-03-03 | 1988-09-14 | Shell Int Research | Apparatus and process suitable for producing hydrogen |
| US6191332B1 (en) * | 1991-05-06 | 2001-02-20 | Institut Francais Du Petrole | Method and apparatus for dehydrogenating aliphatic hydrocarbons to olefinic hydrocarbons |
Also Published As
| Publication number | Publication date |
|---|---|
| EA201000156A1 (ru) | 2010-06-30 |
| WO2009003647A1 (en) | 2009-01-08 |
| US8916737B2 (en) | 2014-12-23 |
| EP2173469B1 (en) | 2014-06-18 |
| US20150064078A1 (en) | 2015-03-05 |
| BRPI0814196A2 (pt) | 2015-01-27 |
| IL202831A0 (en) | 2010-06-30 |
| JP6009732B2 (ja) | 2016-10-19 |
| JP2015061726A (ja) | 2015-04-02 |
| CN101687162B (zh) | 2013-01-02 |
| ES2496171T3 (es) | 2014-09-18 |
| JP2010532707A (ja) | 2010-10-14 |
| CA2691566A1 (en) | 2009-01-08 |
| MX2009014078A (es) | 2010-03-01 |
| IL202831A (en) | 2015-03-31 |
| US9492803B2 (en) | 2016-11-15 |
| EP2173469A1 (en) | 2010-04-14 |
| JP2016155120A (ja) | 2016-09-01 |
| US20100160705A1 (en) | 2010-06-24 |
| CA2691566C (en) | 2018-06-12 |
| CN101687162A (zh) | 2010-03-31 |
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