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 |
|---|---|---|---|
| GB0004934.6 | 2000-03-01 | ||
| GB0004934A GB2359764A (en) | 2000-03-01 | 2000-03-01 | An endothermic tube reactor |
| 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 (https=) | 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 (https=) |
| EP (1) | EP1259314A1 (https=) |
| JP (1) | JP4955885B2 (https=) |
| AU (1) | AU2001235811A1 (https=) |
| GB (1) | GB2359764A (https=) |
| WO (1) | WO2001064327A1 (https=) |
Families Citing this family (36)
| 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 |
| WO2006046846A1 (es) * | 2004-10-28 | 2006-05-04 | Francisco Alvarado Barrientos | Calentador de líquidos y caldera de vapor |
| AU2006223449A1 (en) | 2005-03-10 | 2006-09-21 | Shell Internationale Research Maatschappij B.V. | Method of starting up a direct heating system for the flameless combustion of fuel and direct heating of a process fluid |
| RU2384791C2 (ru) * | 2005-03-10 | 2010-03-20 | Шелл Интернэшнл Рисерч Маатсхаппий Б.В. | Многотрубная система переноса тепла для сжигания топлива и нагревания технологической текучей среды и ее использование |
| RU2007137495A (ru) * | 2005-03-10 | 2009-04-20 | Шелл Интернэшнл Рисерч Маатсхаппий Б.В. (NL) | Система теплопередачи для сгорания топлива и нагревания технологической текучей среды и способ ее использования |
| 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 |
| CN101687162B (zh) * | 2007-07-05 | 2013-01-02 | 沙特基础工业公司 | 用于执行吸热反应的方法 |
| US20090093555A1 (en) * | 2007-07-09 | 2009-04-09 | Range Fuels, Inc. | Methods and apparatus for producing syngas |
| US9227895B2 (en) * | 2007-07-09 | 2016-01-05 | Albemarle Corporation | Methods and apparatus for producing alcohols from syngas |
| US8142530B2 (en) * | 2007-07-09 | 2012-03-27 | 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 |
| US8153027B2 (en) * | 2007-07-09 | 2012-04-10 | Range Fuels, Inc. | Methods for producing syngas |
| US20090014689A1 (en) * | 2007-07-09 | 2009-01-15 | Range Fuels, Inc. | Methods and apparatus for producing syngas and alcohols |
| AR067577A1 (es) * | 2007-07-20 | 2009-10-14 | Shell Int Research | Un calentador de combustion no inflamable y metodo para proporcionar calor a un conducto del proceso |
| 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. |
| 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 |
| 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 |
| US20100175386A1 (en) * | 2009-01-09 | 2010-07-15 | General Electric Company | Premixed partial oxidation syngas generation and gas turbine system |
| 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. |
| WO2013188671A2 (en) * | 2012-06-14 | 2013-12-19 | Nuvera Fuel Cells, Inc. | Steam reformers, modules, and methods of use |
| 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 |
| CA3004298C (en) * | 2015-11-04 | 2020-04-28 | Exxonmobil Chemical Patents Inc. | Fired tube conversion system and process |
| CA3001494C (en) * | 2015-11-04 | 2020-08-25 | Exxonmobil Chemical Patents Inc. | Integrated gas turbine and conversion system process |
| US9914678B2 (en) | 2015-11-04 | 2018-03-13 | Exxonmobil Chemical Patents Inc. | Fired tube conversion system and 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 |
| EP4436914A1 (en) * | 2021-11-26 | 2024-10-02 | Topsoe A/S | Improving the energy efficiency of a process and plant for producing hydrogen |
| 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 |
| EP0349011A1 (en) * | 1985-06-27 | 1990-01-03 | Stone & Webster Engineering Corporation | A convective reforming device for production of synthesis gas |
| 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 US US10/220,500 patent/US7279019B2/en not_active Expired - Fee Related
- 2001-02-28 WO PCT/GB2001/000870 patent/WO2001064327A1/en not_active Ceased
- 2001-02-28 JP JP2001563218A patent/JP4955885B2/ja not_active Expired - Fee Related
- 2001-02-28 EP EP01907945A patent/EP1259314A1/en not_active Withdrawn
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