JP2003525115A5 - - Google Patents
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- Publication number
- JP2003525115A5 JP2003525115A5 JP2001563218A JP2001563218A JP2003525115A5 JP 2003525115 A5 JP2003525115 A5 JP 2003525115A5 JP 2001563218 A JP2001563218 A JP 2001563218A JP 2001563218 A JP2001563218 A JP 2001563218A JP 2003525115 A5 JP2003525115 A5 JP 2003525115A5
- Authority
- JP
- Japan
- Prior art keywords
- tube
- combustion
- heat
- fuel
- gas
- Prior art date
- Legal status (The legal status 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 status listed.)
- Granted
Links
- 238000000034 method Methods 0.000 description 166
- 238000006243 chemical reaction Methods 0.000 description 105
- 238000002485 combustion reaction Methods 0.000 description 94
- 230000008569 process Effects 0.000 description 85
- 239000007789 gas Substances 0.000 description 84
- 239000000567 combustion gas Substances 0.000 description 81
- 238000011084 recovery Methods 0.000 description 77
- 239000000446 fuel Substances 0.000 description 73
- 238000012546 transfer Methods 0.000 description 35
- 239000000463 material Substances 0.000 description 28
- 239000000047 product Substances 0.000 description 28
- 239000012530 fluid Substances 0.000 description 25
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 21
- 238000004519 manufacturing process Methods 0.000 description 15
- 239000003054 catalyst Substances 0.000 description 14
- 239000001257 hydrogen Substances 0.000 description 13
- 229910052739 hydrogen Inorganic materials 0.000 description 13
- 230000015572 biosynthetic process Effects 0.000 description 12
- 238000003786 synthesis reaction Methods 0.000 description 11
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 10
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 9
- 229910002092 carbon dioxide Inorganic materials 0.000 description 9
- 238000004891 communication Methods 0.000 description 9
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 9
- 238000013461 design Methods 0.000 description 8
- 239000002737 fuel gas Substances 0.000 description 8
- 239000003345 natural gas Substances 0.000 description 8
- 230000005855 radiation Effects 0.000 description 8
- 230000000694 effects Effects 0.000 description 7
- 229910052751 metal Inorganic materials 0.000 description 7
- 239000002184 metal Substances 0.000 description 7
- 238000011069 regeneration method Methods 0.000 description 7
- 230000008901 benefit Effects 0.000 description 6
- 239000007795 chemical reaction product Substances 0.000 description 6
- 238000000746 purification Methods 0.000 description 6
- 230000008929 regeneration Effects 0.000 description 6
- 238000010586 diagram Methods 0.000 description 5
- 238000010438 heat treatment Methods 0.000 description 5
- 239000011159 matrix material Substances 0.000 description 5
- 238000011144 upstream manufacturing Methods 0.000 description 5
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 4
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 4
- 238000009826 distribution Methods 0.000 description 4
- 238000002156 mixing Methods 0.000 description 4
- 239000000203 mixture Substances 0.000 description 4
- QTBSBXVTEAMEQO-UHFFFAOYSA-N Acetic acid Chemical compound CC(O)=O QTBSBXVTEAMEQO-UHFFFAOYSA-N 0.000 description 3
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 3
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 3
- 239000011248 coating agent Substances 0.000 description 3
- 238000000576 coating method Methods 0.000 description 3
- 238000010276 construction Methods 0.000 description 3
- 238000007796 conventional method Methods 0.000 description 3
- 238000001816 cooling Methods 0.000 description 3
- 238000005260 corrosion Methods 0.000 description 3
- 230000007797 corrosion Effects 0.000 description 3
- 238000009413 insulation Methods 0.000 description 3
- 239000012212 insulator Substances 0.000 description 3
- 230000007246 mechanism Effects 0.000 description 3
- MWUXSHHQAYIFBG-UHFFFAOYSA-N nitrogen oxide Inorganic materials O=[N] MWUXSHHQAYIFBG-UHFFFAOYSA-N 0.000 description 3
- 239000001301 oxygen Substances 0.000 description 3
- 229910052760 oxygen Inorganic materials 0.000 description 3
- 238000012545 processing Methods 0.000 description 3
- 239000002994 raw material Substances 0.000 description 3
- 238000002407 reforming Methods 0.000 description 3
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 2
- ATUOYWHBWRKTHZ-UHFFFAOYSA-N Propane Chemical compound CCC ATUOYWHBWRKTHZ-UHFFFAOYSA-N 0.000 description 2
- 230000004913 activation Effects 0.000 description 2
- 229910021529 ammonia Inorganic materials 0.000 description 2
- 238000003491 array Methods 0.000 description 2
- 239000000356 contaminant Substances 0.000 description 2
- 230000007423 decrease Effects 0.000 description 2
- 238000009792 diffusion process Methods 0.000 description 2
- 230000007613 environmental effect Effects 0.000 description 2
- 238000000605 extraction Methods 0.000 description 2
- 230000004907 flux Effects 0.000 description 2
- 150000002431 hydrogen Chemical class 0.000 description 2
- 230000000977 initiatory effect Effects 0.000 description 2
- 238000002347 injection Methods 0.000 description 2
- 239000007924 injection Substances 0.000 description 2
- 239000011810 insulating material Substances 0.000 description 2
- 238000011068 loading method Methods 0.000 description 2
- 230000002028 premature Effects 0.000 description 2
- 238000002360 preparation method Methods 0.000 description 2
- 239000000376 reactant Substances 0.000 description 2
- 230000009467 reduction Effects 0.000 description 2
- 230000000452 restraining effect Effects 0.000 description 2
- 125000006850 spacer group Chemical group 0.000 description 2
- 239000002918 waste heat Substances 0.000 description 2
- PQVHMOLNSYFXIJ-UHFFFAOYSA-N 4-[2-(2,3-dihydro-1H-inden-2-ylamino)pyrimidin-5-yl]-1-[2-oxo-2-(2,4,6,7-tetrahydrotriazolo[4,5-c]pyridin-5-yl)ethyl]pyrazole-3-carboxylic acid Chemical compound C1C(CC2=CC=CC=C12)NC1=NC=C(C=N1)C=1C(=NN(C=1)CC(N1CC2=C(CC1)NN=N2)=O)C(=O)O PQVHMOLNSYFXIJ-UHFFFAOYSA-N 0.000 description 1
- IKHGUXGNUITLKF-UHFFFAOYSA-N Acetaldehyde Natural products CC=O IKHGUXGNUITLKF-UHFFFAOYSA-N 0.000 description 1
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- OTMSDBZUPAUEDD-UHFFFAOYSA-N Ethane Chemical compound CC OTMSDBZUPAUEDD-UHFFFAOYSA-N 0.000 description 1
- VGGSQFUCUMXWEO-UHFFFAOYSA-N Ethene Chemical compound C=C VGGSQFUCUMXWEO-UHFFFAOYSA-N 0.000 description 1
- 239000005977 Ethylene Substances 0.000 description 1
- 230000004308 accommodation Effects 0.000 description 1
- 230000009471 action Effects 0.000 description 1
- 150000001336 alkenes Chemical class 0.000 description 1
- 229910052782 aluminium Inorganic materials 0.000 description 1
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 1
- 239000001273 butane Substances 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 239000001569 carbon dioxide Substances 0.000 description 1
- 229910002090 carbon oxide Inorganic materials 0.000 description 1
- 239000003575 carbonaceous material Substances 0.000 description 1
- 238000003763 carbonization Methods 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 239000007809 chemical reaction catalyst Substances 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 230000006835 compression Effects 0.000 description 1
- 238000007906 compression Methods 0.000 description 1
- 238000011109 contamination Methods 0.000 description 1
- 125000004122 cyclic group Chemical group 0.000 description 1
- 238000006356 dehydrogenation reaction Methods 0.000 description 1
- 238000006477 desulfuration reaction Methods 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 230000018109 developmental process Effects 0.000 description 1
- 238000011143 downstream manufacturing Methods 0.000 description 1
- 238000005553 drilling Methods 0.000 description 1
- 238000005538 encapsulation Methods 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 230000003628 erosive effect Effects 0.000 description 1
- 125000002485 formyl group Chemical class [H]C(*)=O 0.000 description 1
- -1 hydrogen Chemical class 0.000 description 1
- 238000007689 inspection Methods 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- JEIPFZHSYJVQDO-UHFFFAOYSA-N iron(III) oxide Inorganic materials O=[Fe]O[Fe]=O JEIPFZHSYJVQDO-UHFFFAOYSA-N 0.000 description 1
- 238000003754 machining Methods 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 238000005272 metallurgy Methods 0.000 description 1
- IJDNQMDRQITEOD-UHFFFAOYSA-N n-butane Chemical compound CCCC IJDNQMDRQITEOD-UHFFFAOYSA-N 0.000 description 1
- OFBQJSOFQDEBGM-UHFFFAOYSA-N n-pentane Natural products CCCCC OFBQJSOFQDEBGM-UHFFFAOYSA-N 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- JCXJVPUVTGWSNB-UHFFFAOYSA-N nitrogen dioxide Inorganic materials O=[N]=O JCXJVPUVTGWSNB-UHFFFAOYSA-N 0.000 description 1
- 238000005457 optimization Methods 0.000 description 1
- 150000002894 organic compounds Chemical class 0.000 description 1
- 239000011148 porous material Substances 0.000 description 1
- 239000001294 propane Substances 0.000 description 1
- QQONPFPTGQHPMA-UHFFFAOYSA-N propylene Natural products CC=C QQONPFPTGQHPMA-UHFFFAOYSA-N 0.000 description 1
- 125000004805 propylene group Chemical group [H]C([H])([H])C([H])([*:1])C([H])([H])[*:2] 0.000 description 1
- 238000010791 quenching Methods 0.000 description 1
- 230000000171 quenching effect Effects 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 239000004071 soot Substances 0.000 description 1
- 238000001179 sorption measurement Methods 0.000 description 1
- 239000007858 starting material Substances 0.000 description 1
- 238000000629 steam reforming Methods 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
- 238000005728 strengthening Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 239000000758 substrate Substances 0.000 description 1
- 125000000383 tetramethylene group Chemical group [H]C([H])([*:1])C([H])([H])C([H])([H])C([H])([H])[*:2] 0.000 description 1
- 238000006276 transfer reaction Methods 0.000 description 1
- 239000001993 wax Substances 0.000 description 1
Applications Claiming Priority (3)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| GB0004934A GB2359764A (en) | 2000-03-01 | 2000-03-01 | An endothermic tube reactor |
| GB0004934.6 | 2000-03-01 | ||
| PCT/GB2001/000870 WO2001064327A1 (en) | 2000-03-01 | 2001-02-28 | Endothermic reaction process and an apparatus therefor |
Publications (3)
| Publication Number | Publication Date |
|---|---|
| JP2003525115A JP2003525115A (ja) | 2003-08-26 |
| JP2003525115A5 true JP2003525115A5 (enExample) | 2012-03-29 |
| JP4955885B2 JP4955885B2 (ja) | 2012-06-20 |
Family
ID=9886738
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP2001563218A Expired - Fee Related JP4955885B2 (ja) | 2000-03-01 | 2001-02-28 | 吸熱反応の実施方法およびその装置 |
Country Status (6)
| Country | Link |
|---|---|
| US (1) | US7279019B2 (enExample) |
| EP (1) | EP1259314A1 (enExample) |
| JP (1) | JP4955885B2 (enExample) |
| AU (1) | AU2001235811A1 (enExample) |
| GB (1) | GB2359764A (enExample) |
| WO (1) | WO2001064327A1 (enExample) |
Families Citing this family (35)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US6796369B1 (en) * | 2003-04-04 | 2004-09-28 | Air Products And Chemicals, Inc. | Method and apparatus to prevent metal dusting |
| US20090000571A1 (en) * | 2004-10-28 | 2009-01-01 | Francisco Alvarado Barrientos | Liquid Heater and Steam Boiler |
| BRPI0608336B1 (pt) * | 2005-03-10 | 2018-09-11 | Shell Int Research | sistema de processamento, sistema de aquecimento direto de quatro tubos para queima de um combustível e aquecimento direto de um fluido de processamento e método |
| MX2007010987A (es) | 2005-03-10 | 2007-09-25 | Shell Int Research | Metodo para iniciar un sistema de calentamiento directo para la combustion sin flama de combustible, y el calentamiento directo de un fluido de proceso. |
| CN101163918A (zh) * | 2005-03-10 | 2008-04-16 | 国际壳牌研究有限公司 | 一种用于燃料燃烧和加热工艺流体的传热系统以及使用该系统的工艺 |
| DE102005020943A1 (de) * | 2005-05-04 | 2006-11-09 | Linde Ag | Verfahren und Reaktor zur Durchführung endothermer katalytischer Reaktionen |
| FR2914395B1 (fr) * | 2007-03-30 | 2009-11-20 | Inst Francais Du Petrole | Nouveau reacteur echangeur compact utilisant un bruleur poreux |
| ES2496171T3 (es) | 2007-07-05 | 2014-09-18 | Saudi Basic Industries Corporation | Proceso para realizar una reacción endotérmica |
| US20090093555A1 (en) * | 2007-07-09 | 2009-04-09 | Range Fuels, Inc. | Methods and apparatus for producing syngas |
| US8153027B2 (en) * | 2007-07-09 | 2012-04-10 | Range Fuels, Inc. | Methods for producing syngas |
| US8142530B2 (en) * | 2007-07-09 | 2012-03-27 | Range Fuels, Inc. | Methods and apparatus for producing syngas and alcohols |
| US9227895B2 (en) * | 2007-07-09 | 2016-01-05 | Albemarle Corporation | Methods and apparatus for producing alcohols from syngas |
| US20090014689A1 (en) * | 2007-07-09 | 2009-01-15 | Range Fuels, Inc. | Methods and apparatus for producing syngas and alcohols |
| US20090018371A1 (en) * | 2007-07-09 | 2009-01-15 | Range Fuels, Inc. | Methods and apparatus for producing alcohols from syngas |
| FR2918904B1 (fr) * | 2007-07-20 | 2011-07-15 | Inst Francais Du Petrole | Reacteur echangeur a tube baionnette permettant de fonctionner avec des differences de pression de l'ordre de 100 bars entre le cote tube et le cote calandre. |
| WO2009014979A2 (en) * | 2007-07-20 | 2009-01-29 | Shell Oil Company | A flameless combustion heater |
| US20090242841A1 (en) * | 2008-03-26 | 2009-10-01 | Air Liquide Process And Construction Inc. | Combustion Air Preheat Optimization System In An SMR |
| FR2936724B1 (fr) | 2008-10-07 | 2011-09-16 | Inst Francais Du Petrole | Enceinte reactionnelle favorisant l'echange de chaleur entre les reactifs et les gaz produits |
| FR2936723B1 (fr) * | 2008-10-07 | 2011-09-16 | Inst Francais Du Petrole | Enceinte reactionnelle favorisant l'echange de chaleur entre les reacteurs et les gaz produits |
| US20100175386A1 (en) * | 2009-01-09 | 2010-07-15 | General Electric Company | Premixed partial oxidation syngas generation and gas turbine system |
| US20100175379A1 (en) * | 2009-01-09 | 2010-07-15 | General Electric Company | Pre-mix catalytic partial oxidation fuel reformer for staged and reheat gas turbine systems |
| DE102009012663B3 (de) * | 2009-03-13 | 2010-09-16 | Uhde Gmbh | Verfahren und Vorrichtung zur gleichmäßigen Dampferzeugung aus der Abwärme einer Alkandehydrierung |
| ES2345759B8 (es) * | 2010-06-01 | 2012-01-26 | Universidad Politécnica de Madrid | Receptor para central solar con espejos longitudinales. |
| CA2876374C (en) | 2012-06-14 | 2020-09-01 | Nuvera Fuel Cells, Inc. | Steam reformers for the production of hydrogen reformate and uses thereof |
| US9592487B2 (en) * | 2014-06-25 | 2017-03-14 | Zoneflow Reactor Technologies, LLC | Steam methane reformer system and method of performing a steam methane reforming process |
| US10005976B2 (en) * | 2014-10-07 | 2018-06-26 | Pride of the Hills Manufacturing, Inc. | Heat exchanger on a fossil fuel processing assembly |
| JP6707129B2 (ja) * | 2015-11-04 | 2020-06-10 | エクソンモービル ケミカル パテンツ インコーポレイテッド | 加熱管変換システム及び方法 |
| WO2017078891A1 (en) | 2015-11-04 | 2017-05-11 | Exxonmoble Chemical Patents Inc. | Integrated gas turbine and conversion system process |
| US9926242B2 (en) | 2015-11-04 | 2018-03-27 | Exxonmobil Chemical Patents Inc. | Integrated gas turbine and conversion system process |
| US10272385B2 (en) * | 2016-05-17 | 2019-04-30 | Linde Engineering North America, Inc. | Flameless thermal oxidizer for oxidizing gaseous effluent streams containing hydrogen gas |
| MY189567A (en) * | 2017-04-25 | 2022-02-17 | Bin Halim Rasip Amin | Reaction chamber for exothermic and endothermic reactions |
| GB201813431D0 (en) | 2018-08-17 | 2018-10-03 | Weedon Geoffrey Gerald | Process & apparatus for steam reforming |
| DE102019211177A1 (de) | 2019-07-26 | 2021-01-28 | Thyssenkrupp Ag | Vorrichtung und Verfahren zum automatisierbaren Anfahren einer Dampfreformeranordnung in den Normalbetriebszustand sowie Verwendung sowie Steuerungs-/Regelungseinrichtung sowie Computerprogrammprodukt |
| US12111148B2 (en) * | 2021-05-21 | 2024-10-08 | General Electric Company | Component imaging systems, apparatus, and methods |
| US20240217901A1 (en) * | 2022-12-28 | 2024-07-04 | Uop Llc | Process and apparatus for producing ethylene from alcohol |
Family Cites Families (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE1093948B (de) * | 1960-06-02 | 1960-12-01 | Carl Mertens | Katalytische Umformungsanlage zur kontinuierlichen Erzeugung von Gasen aller Art aus Kohlenwasserstoffen |
| US3958951A (en) * | 1974-04-09 | 1976-05-25 | Stone & Webster Engineering Corporation | Convective power reformer equipment and system |
| EP0227807B1 (en) * | 1985-06-27 | 1991-11-21 | Stone & Webster Engineering Corporation | Production of synthesis gas using convective reforming |
| IT1226413B (it) * | 1987-08-27 | 1991-01-15 | Toyo Engineering Corp | Apparecchiatura per reforming con vapore. |
| US5567398A (en) * | 1990-04-03 | 1996-10-22 | The Standard Oil Company | Endothermic reaction apparatus and method |
| AU661877B2 (en) * | 1990-04-03 | 1995-08-10 | Standard Oil Company, The | Endothermic reaction apparatus |
| JPH05147901A (ja) * | 1991-11-29 | 1993-06-15 | Toshiba Corp | 燃料改質器 |
| DE9320711U1 (de) * | 1993-07-21 | 1995-01-19 | Fraunhofer-Gesellschaft zur Förderung der angewandten Forschung e.V., 80636 München | Chemischer Reaktor mit integriertem Brenner |
| EP0849245A1 (en) * | 1996-12-20 | 1998-06-24 | Kvaerner Process Technology Limited | Process and plant for the production of methanol |
| DE10007766A1 (de) * | 2000-02-20 | 2001-08-23 | Gen Motors Corp | Brenneranordnung |
-
2000
- 2000-03-01 GB GB0004934A patent/GB2359764A/en not_active Withdrawn
-
2001
- 2001-02-28 AU AU2001235811A patent/AU2001235811A1/en not_active Abandoned
- 2001-02-28 WO PCT/GB2001/000870 patent/WO2001064327A1/en not_active Ceased
- 2001-02-28 US US10/220,500 patent/US7279019B2/en not_active Expired - Fee Related
- 2001-02-28 EP EP01907945A patent/EP1259314A1/en not_active Withdrawn
- 2001-02-28 JP JP2001563218A patent/JP4955885B2/ja not_active Expired - Fee Related
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