HRP20050811A2 - Auto thermal cracking reactor - Google Patents
Auto thermal cracking reactor Download PDFInfo
- Publication number
- HRP20050811A2 HRP20050811A2 HR20050811A HRP20050811A HRP20050811A2 HR P20050811 A2 HRP20050811 A2 HR P20050811A2 HR 20050811 A HR20050811 A HR 20050811A HR P20050811 A HRP20050811 A HR P20050811A HR P20050811 A2 HRP20050811 A2 HR P20050811A2
- Authority
- HR
- Croatia
- Prior art keywords
- gaseous
- chamber
- gas
- exits
- zone
- Prior art date
Links
- 238000004227 thermal cracking Methods 0.000 title 1
- 239000007789 gas Substances 0.000 claims description 117
- 238000002347 injection Methods 0.000 claims description 110
- 239000007924 injection Substances 0.000 claims description 110
- 239000000376 reactant Substances 0.000 claims description 87
- 238000006243 chemical reaction Methods 0.000 claims description 58
- 229930195733 hydrocarbon Natural products 0.000 claims description 39
- 150000002430 hydrocarbons Chemical class 0.000 claims description 39
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims description 38
- 239000001301 oxygen Substances 0.000 claims description 38
- 229910052760 oxygen Inorganic materials 0.000 claims description 38
- 239000004215 Carbon black (E152) Substances 0.000 claims description 34
- 238000000034 method Methods 0.000 claims description 31
- 239000003054 catalyst Substances 0.000 claims description 27
- 239000000203 mixture Substances 0.000 claims description 24
- 238000001816 cooling Methods 0.000 claims description 17
- 238000002485 combustion reaction Methods 0.000 claims description 16
- 239000012530 fluid Substances 0.000 claims description 15
- 150000005673 monoalkenes Chemical class 0.000 claims description 14
- 239000008246 gaseous mixture Substances 0.000 claims description 13
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 claims description 10
- 238000004891 communication Methods 0.000 claims description 10
- 238000004519 manufacturing process Methods 0.000 claims description 10
- 239000000463 material Substances 0.000 claims description 10
- 238000009826 distribution Methods 0.000 claims description 8
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 claims description 8
- 238000011144 upstream manufacturing Methods 0.000 claims description 8
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims description 6
- 230000015572 biosynthetic process Effects 0.000 claims description 5
- 229910002092 carbon dioxide Inorganic materials 0.000 claims description 5
- 239000001569 carbon dioxide Substances 0.000 claims description 5
- 238000009792 diffusion process Methods 0.000 claims description 5
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 5
- OTMSDBZUPAUEDD-UHFFFAOYSA-N Ethane Chemical compound CC OTMSDBZUPAUEDD-UHFFFAOYSA-N 0.000 claims description 4
- ATUOYWHBWRKTHZ-UHFFFAOYSA-N Propane Chemical compound CCC ATUOYWHBWRKTHZ-UHFFFAOYSA-N 0.000 claims description 4
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 claims description 3
- 229910002091 carbon monoxide Inorganic materials 0.000 claims description 3
- 239000001257 hydrogen Substances 0.000 claims description 3
- 229910052739 hydrogen Inorganic materials 0.000 claims description 3
- 229910052757 nitrogen Inorganic materials 0.000 claims description 3
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 claims description 2
- 239000001273 butane Substances 0.000 claims description 2
- 238000001704 evaporation Methods 0.000 claims description 2
- 230000008020 evaporation Effects 0.000 claims description 2
- VUZPPFZMUPKLLV-UHFFFAOYSA-N methane;hydrate Chemical compound C.O VUZPPFZMUPKLLV-UHFFFAOYSA-N 0.000 claims description 2
- IJDNQMDRQITEOD-UHFFFAOYSA-N n-butane Chemical compound CCCC IJDNQMDRQITEOD-UHFFFAOYSA-N 0.000 claims description 2
- OFBQJSOFQDEBGM-UHFFFAOYSA-N n-pentane Natural products CCCCC OFBQJSOFQDEBGM-UHFFFAOYSA-N 0.000 claims description 2
- 239000001294 propane Substances 0.000 claims description 2
- 239000000446 fuel Substances 0.000 claims 1
- 239000000047 product Substances 0.000 description 30
- 238000002156 mixing Methods 0.000 description 12
- 239000011148 porous material Substances 0.000 description 10
- 150000001336 alkenes Chemical class 0.000 description 8
- 229910052751 metal Inorganic materials 0.000 description 7
- 239000002184 metal Substances 0.000 description 7
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 5
- 230000035699 permeability Effects 0.000 description 5
- BASFCYQUMIYNBI-UHFFFAOYSA-N platinum Chemical group [Pt] BASFCYQUMIYNBI-UHFFFAOYSA-N 0.000 description 5
- KDLHZDBZIXYQEI-UHFFFAOYSA-N Palladium Chemical compound [Pd] KDLHZDBZIXYQEI-UHFFFAOYSA-N 0.000 description 4
- 239000000919 ceramic Substances 0.000 description 4
- 238000005336 cracking Methods 0.000 description 4
- 230000007423 decrease Effects 0.000 description 4
- 230000035939 shock Effects 0.000 description 4
- 239000002826 coolant Substances 0.000 description 3
- 238000011084 recovery Methods 0.000 description 3
- 229910000990 Ni alloy Inorganic materials 0.000 description 2
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 description 2
- MCMNRKCIXSYSNV-UHFFFAOYSA-N Zirconium dioxide Chemical compound O=[Zr]=O MCMNRKCIXSYSNV-UHFFFAOYSA-N 0.000 description 2
- 229910045601 alloy Inorganic materials 0.000 description 2
- 239000000956 alloy Substances 0.000 description 2
- 239000012876 carrier material Substances 0.000 description 2
- 238000005266 casting Methods 0.000 description 2
- 229910010293 ceramic material Inorganic materials 0.000 description 2
- 238000010276 construction Methods 0.000 description 2
- 239000006260 foam Substances 0.000 description 2
- 239000011261 inert gas Substances 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- -1 lithium-aluminum silicates Chemical class 0.000 description 2
- JRZJOMJEPLMPRA-UHFFFAOYSA-N olefin Natural products CCCCCCCC=C JRZJOMJEPLMPRA-UHFFFAOYSA-N 0.000 description 2
- 229910052763 palladium Inorganic materials 0.000 description 2
- 239000012188 paraffin wax Substances 0.000 description 2
- 229910052697 platinum Inorganic materials 0.000 description 2
- 238000007789 sealing Methods 0.000 description 2
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 1
- 229910000881 Cu alloy Inorganic materials 0.000 description 1
- MYMOFIZGZYHOMD-UHFFFAOYSA-N Dioxygen Chemical compound O=O MYMOFIZGZYHOMD-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
- 229910000831 Steel Inorganic materials 0.000 description 1
- ATJFFYVFTNAWJD-UHFFFAOYSA-N Tin Chemical compound [Sn] ATJFFYVFTNAWJD-UHFFFAOYSA-N 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
- 238000009530 blood pressure measurement Methods 0.000 description 1
- MXCNPGJZHAUBMR-UHFFFAOYSA-H calcium zirconium(4+) diphosphate Chemical compound [Ca++].[Zr+4].[O-]P([O-])([O-])=O.[O-]P([O-])([O-])=O MXCNPGJZHAUBMR-UHFFFAOYSA-H 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 239000007795 chemical reaction product Substances 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 229910052802 copper Inorganic materials 0.000 description 1
- 239000010949 copper Substances 0.000 description 1
- 238000006356 dehydrogenation reaction Methods 0.000 description 1
- 239000006185 dispersion Substances 0.000 description 1
- 238000005242 forging Methods 0.000 description 1
- 239000008187 granular material Substances 0.000 description 1
- 229910000856 hastalloy Inorganic materials 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 150000002431 hydrogen Chemical class 0.000 description 1
- 229910001026 inconel Inorganic materials 0.000 description 1
- 238000009413 insulation Methods 0.000 description 1
- 239000011490 mineral wool Substances 0.000 description 1
- 239000003345 natural gas Substances 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 238000003825 pressing Methods 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 230000002250 progressing effect Effects 0.000 description 1
- 229910052594 sapphire Inorganic materials 0.000 description 1
- 239000003566 sealing material Substances 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 238000010583 slow cooling Methods 0.000 description 1
- 230000003068 static effect Effects 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
- 238000007514 turning Methods 0.000 description 1
- 210000002268 wool Anatomy 0.000 description 1
- 229910052727 yttrium Inorganic materials 0.000 description 1
- VWQVUPCCIRVNHF-UHFFFAOYSA-N yttrium atom Chemical compound [Y] VWQVUPCCIRVNHF-UHFFFAOYSA-N 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07B—GENERAL METHODS OF ORGANIC CHEMISTRY; APPARATUS THEREFOR
- C07B35/00—Reactions without formation or introduction of functional groups containing hetero atoms, involving a change in the type of bonding between two carbon atoms already directly linked
- C07B35/04—Dehydrogenation
-
- 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
- B01J8/0446—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 flow within the beds being predominantly vertical
- B01J8/0449—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 flow within the beds being predominantly vertical in two or more cylindrical beds
- B01J8/0453—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 flow within the beds being predominantly vertical in two or more cylindrical beds the beds being superimposed one above the other
-
- 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
- B01J8/0492—Feeding reactive fluids
-
- 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
- C07C4/00—Preparation of hydrocarbons from hydrocarbons containing a larger number of carbon atoms
- C07C4/08—Preparation of hydrocarbons from hydrocarbons containing a larger number of carbon atoms by splitting-off an aliphatic or cycloaliphatic part from the molecule
- C07C4/10—Preparation of hydrocarbons from hydrocarbons containing a larger number of carbon atoms by splitting-off an aliphatic or cycloaliphatic part from the molecule from acyclic hydrocarbons
-
- 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
- C07C5/42—Preparation of hydrocarbons from hydrocarbons containing the same number of carbon atoms by dehydrogenation with a hydrogen acceptor
- C07C5/48—Preparation of hydrocarbons from hydrocarbons containing the same number of carbon atoms by dehydrogenation with a hydrogen acceptor with oxygen as an acceptor
-
- 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
- B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J2219/00049—Controlling or regulating processes
- B01J2219/00051—Controlling the temperature
- B01J2219/00074—Controlling the temperature by indirect heating or cooling employing heat exchange fluids
- B01J2219/00087—Controlling the temperature by indirect heating or cooling employing heat exchange fluids with heat exchange elements outside the reactor
- B01J2219/00094—Jackets
-
- 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
- B01J2219/00245—Avoiding undesirable reactions or side-effects
- B01J2219/00259—Preventing runaway of the chemical reaction
- B01J2219/00265—Preventing flame propagation
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Engineering & Computer Science (AREA)
- General Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)
- Physical Or Chemical Processes And Apparatus (AREA)
- Fire-Extinguishing Compositions (AREA)
- Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
Applications Claiming Priority (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB0303723A GB0303723D0 (en) | 2003-02-18 | 2003-02-18 | Auto thermal cracking reactor |
GB0329710A GB0329710D0 (en) | 2003-12-22 | 2003-12-22 | Autothermal cracking process |
PCT/GB2004/000488 WO2004074222A1 (en) | 2003-02-18 | 2004-02-06 | Auto thermal cracking reactor |
Publications (1)
Publication Number | Publication Date |
---|---|
HRP20050811A2 true HRP20050811A2 (en) | 2005-10-31 |
Family
ID=32910463
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
HR20050811A HRP20050811A2 (en) | 2003-02-18 | 2005-09-15 | Auto thermal cracking reactor |
Country Status (17)
Country | Link |
---|---|
US (1) | US7807860B2 (zh) |
EP (1) | EP1594823B1 (zh) |
JP (1) | JP5054375B2 (zh) |
KR (1) | KR20050111327A (zh) |
AR (1) | AR043192A1 (zh) |
AU (1) | AU2004213211A1 (zh) |
BR (1) | BRPI0407575A (zh) |
CA (1) | CA2516247C (zh) |
EA (1) | EA007370B1 (zh) |
HR (1) | HRP20050811A2 (zh) |
MX (1) | MXPA05008772A (zh) |
MY (1) | MY133424A (zh) |
NO (1) | NO20054297L (zh) |
PL (1) | PL377262A1 (zh) |
RS (1) | RS20050632A (zh) |
TW (1) | TW200422289A (zh) |
WO (1) | WO2004074222A1 (zh) |
Families Citing this family (15)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US7901662B2 (en) * | 2005-11-01 | 2011-03-08 | Celanese International Corporation | Steam generation apparatus and method |
WO2007071925A1 (en) * | 2005-12-20 | 2007-06-28 | Ineos Europe Limited | Catalyst holder, apparatus containing it and process for the reaction of an hydrocarbon with oxygen |
RU2448080C2 (ru) * | 2006-03-30 | 2012-04-20 | Басф Се | Способ гетерогенного каталитического парциального дегидрирования по меньшей мере одного подлежащего дегидрированию углеводорода |
US7842846B2 (en) | 2006-03-30 | 2010-11-30 | Basf Aktiengesellschaft | Process for heterogeneously catalyzed partial dehydrogenation of at least one hydrocarbon to be dehydrogenated |
WO2007113162A1 (de) | 2006-03-30 | 2007-10-11 | Basf Se | Verfahren einer heterogen katalysierten partiellen dehydrierung wenigstens eines zu dehydrierenden kohlenwasserstoffs |
GB0613676D0 (en) | 2006-07-10 | 2006-08-16 | Ineos Europe Ltd | Process |
DE102006054415A1 (de) * | 2006-11-16 | 2008-05-21 | Uhde Gmbh | Verfahren und Vorrichtung zum Eindüsen von Sauerstoff in ein einen Synthesereaktor durchströmendes Reaktionsgas |
US8262755B2 (en) * | 2007-06-05 | 2012-09-11 | Air Products And Chemicals, Inc. | Staged membrane oxidation reactor system |
EP2045002A1 (en) | 2007-10-02 | 2009-04-08 | Ineos Europe Limited | Mixing apparatus |
EP2572781A1 (en) | 2011-09-21 | 2013-03-27 | Evonik Degussa GmbH | Device and method for making a dilute aqueous solution of peroxomonosulphuric acid |
EP2572776A1 (en) * | 2011-09-21 | 2013-03-27 | Evonik Degussa GmbH | Device for mixing and cooling two reactive liquids and method of making peroxomonosulphuric acid with the device |
CN102600787A (zh) * | 2012-03-30 | 2012-07-25 | 凯莱英医药集团(天津)股份有限公司 | 臭氧化连续反应装置及其工作方法 |
RU2534991C1 (ru) * | 2013-04-22 | 2014-12-10 | Юрий Николаевич Филимонов | Устройство для получения непредельных углеводородов, преимущественно этилена |
CN111689861B (zh) * | 2019-03-11 | 2022-04-12 | 北京诺维新材科技有限公司 | 一种提高反应收率的方法 |
CN113522192B (zh) * | 2020-04-20 | 2022-10-21 | 中国石油化工股份有限公司 | 制备聚α-烯烃的装置和方法 |
Family Cites Families (18)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3320331A (en) * | 1966-01-27 | 1967-05-16 | Exxon Research Engineering Co | Oxidative dehydrogenation of aliphatic hydrocarbons over aluminum phosphate supported molybdenum and vanadium |
SU255912A1 (ru) | 1968-07-11 | 1983-05-15 | Институт газа АН УССР | Реактор термоокислительного пиролиза углеводородов |
SU435633A1 (ru) | 1970-08-10 | 1982-06-15 | В. Ф. Попов | Газораспределительное устройство |
US3881701A (en) * | 1973-09-17 | 1975-05-06 | Aerojet General Co | Fluid mixer reactor |
US4865820A (en) * | 1987-08-14 | 1989-09-12 | Davy Mckee Corporation | Gas mixer and distributor for reactor |
GB8805447D0 (en) | 1988-03-08 | 1988-04-07 | British Petroleum Co Plc | Chemical process |
US5106590A (en) * | 1990-05-11 | 1992-04-21 | Davy Mckee (London) Limited | Gas mixer and distributor with heat exchange between incoming gases |
US5399307A (en) | 1993-06-18 | 1995-03-21 | Dalton; Robert E. | Methods of compression molding two or more polytetrafluoroethylene resin layers |
NO300117B1 (no) | 1994-12-22 | 1997-04-14 | Norske Stats Oljeselskap | Reaktor for dehydrogenering av hydrokarboner med selektiv oksidasjon av hydrogen |
US5905180A (en) | 1996-01-22 | 1999-05-18 | Regents Of The University Of Minnesota | Catalytic oxidative dehydrogenation process and catalyst |
US6267912B1 (en) | 1997-04-25 | 2001-07-31 | Exxon Research And Engineering Co. | Distributed injection catalytic partial oxidation process and apparatus for producing synthesis gas |
US6183702B1 (en) | 1998-12-21 | 2001-02-06 | Chevron U.S.A. Inc. | Fluid distributor assembly for a multi-bed, downflow catalytic reactor |
EP1206316B1 (en) | 1999-08-17 | 2005-06-29 | Battelle Memorial Institute | Chemical reactor and method for catalytic gas phase reactions |
CN1188374C (zh) | 1999-12-23 | 2005-02-09 | 英国石油化学品有限公司 | 烯烃的生产方法 |
EP1616847A1 (en) | 1999-12-23 | 2006-01-18 | Innovene Europe Limited | Process for the production of olefins in the presence of a catalyst comprising Pt and Pb, Zn, Mo or Cr |
GB0010693D0 (en) * | 2000-05-03 | 2000-06-28 | Bp Chem Int Ltd | Process for the production of olefins |
US20020098136A1 (en) * | 2001-01-23 | 2002-07-25 | Nicholas Vanderborgh | Device for staged addition of heat to a reactor |
US7097787B2 (en) | 2002-07-19 | 2006-08-29 | Conocophillips Company | Utilization of micro-channel gas distributor to distribute unreacted feed gas into reactors |
-
2004
- 2004-02-02 TW TW093102298A patent/TW200422289A/zh unknown
- 2004-02-06 EP EP04708800.0A patent/EP1594823B1/en not_active Expired - Lifetime
- 2004-02-06 JP JP2006502252A patent/JP5054375B2/ja not_active Expired - Fee Related
- 2004-02-06 CA CA2516247A patent/CA2516247C/en not_active Expired - Fee Related
- 2004-02-06 PL PL377262A patent/PL377262A1/pl unknown
- 2004-02-06 AU AU2004213211A patent/AU2004213211A1/en not_active Abandoned
- 2004-02-06 MX MXPA05008772A patent/MXPA05008772A/es unknown
- 2004-02-06 WO PCT/GB2004/000488 patent/WO2004074222A1/en active Application Filing
- 2004-02-06 US US10/543,696 patent/US7807860B2/en not_active Expired - Fee Related
- 2004-02-06 EA EA200501225A patent/EA007370B1/ru not_active IP Right Cessation
- 2004-02-06 RS YUP-2005/0632A patent/RS20050632A/sr unknown
- 2004-02-06 BR BRPI0407575-7A patent/BRPI0407575A/pt not_active IP Right Cessation
- 2004-02-06 KR KR1020057015263A patent/KR20050111327A/ko not_active Application Discontinuation
- 2004-02-16 AR ARP040100474A patent/AR043192A1/es unknown
- 2004-02-16 MY MYPI20040487A patent/MY133424A/en unknown
-
2005
- 2005-09-15 HR HR20050811A patent/HRP20050811A2/hr not_active Application Discontinuation
- 2005-09-16 NO NO20054297A patent/NO20054297L/no not_active Application Discontinuation
Also Published As
Publication number | Publication date |
---|---|
AU2004213211A1 (en) | 2004-09-02 |
AU2004213211A8 (en) | 2004-09-02 |
CA2516247A1 (en) | 2004-09-02 |
WO2004074222A1 (en) | 2004-09-02 |
EP1594823B1 (en) | 2016-08-17 |
JP2006517956A (ja) | 2006-08-03 |
NO20054297L (no) | 2005-09-16 |
PL377262A1 (pl) | 2006-01-23 |
US7807860B2 (en) | 2010-10-05 |
RS20050632A (en) | 2007-12-31 |
MY133424A (en) | 2007-11-30 |
TW200422289A (en) | 2004-11-01 |
EP1594823A1 (en) | 2005-11-16 |
US20060149114A1 (en) | 2006-07-06 |
KR20050111327A (ko) | 2005-11-24 |
CA2516247C (en) | 2013-05-28 |
EA200501225A1 (ru) | 2006-04-28 |
JP5054375B2 (ja) | 2012-10-24 |
EA007370B1 (ru) | 2006-10-27 |
AR043192A1 (es) | 2005-07-20 |
BRPI0407575A (pt) | 2006-02-14 |
MXPA05008772A (es) | 2006-03-21 |
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