ES2356824T3 - Procedimiento y dispositivo para la inyección de oxígeno en un reactor de síntesis. - Google Patents
Procedimiento y dispositivo para la inyección de oxígeno en un reactor de síntesis. Download PDFInfo
- Publication number
- ES2356824T3 ES2356824T3 ES04801221T ES04801221T ES2356824T3 ES 2356824 T3 ES2356824 T3 ES 2356824T3 ES 04801221 T ES04801221 T ES 04801221T ES 04801221 T ES04801221 T ES 04801221T ES 2356824 T3 ES2356824 T3 ES 2356824T3
- Authority
- ES
- Spain
- Prior art keywords
- oxygen
- catalyst
- annular
- catalyst bed
- synthesis reactor
- 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.)
- Expired - Lifetime
Links
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 title claims abstract description 38
- 239000001301 oxygen Substances 0.000 title claims abstract description 38
- 229910052760 oxygen Inorganic materials 0.000 title claims abstract description 38
- 238000000034 method Methods 0.000 title claims abstract description 15
- 230000015572 biosynthetic process Effects 0.000 title claims abstract description 12
- 238000003786 synthesis reaction Methods 0.000 title claims abstract description 12
- 238000002347 injection Methods 0.000 title claims description 14
- 239000007924 injection Substances 0.000 title claims description 14
- 239000003054 catalyst Substances 0.000 claims abstract description 38
- 239000007789 gas Substances 0.000 claims abstract description 23
- 239000000203 mixture Substances 0.000 claims abstract description 6
- 239000011261 inert gas Substances 0.000 claims abstract description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 4
- 238000006297 dehydration reaction Methods 0.000 abstract 2
- 238000010276 construction Methods 0.000 description 3
- ATUOYWHBWRKTHZ-UHFFFAOYSA-N Propane Chemical compound CCC ATUOYWHBWRKTHZ-UHFFFAOYSA-N 0.000 description 2
- 230000001419 dependent effect Effects 0.000 description 2
- 239000011872 intimate mixture Substances 0.000 description 2
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 150000001336 alkenes Chemical class 0.000 description 1
- 239000001273 butane Substances 0.000 description 1
- 230000003197 catalytic effect Effects 0.000 description 1
- 238000006555 catalytic reaction Methods 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 230000001788 irregular Effects 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
- 239000007800 oxidant agent Substances 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 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
- 230000035484 reaction time Effects 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
- 239000004071 soot Substances 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F25/00—Flow mixers; Mixers for falling materials, e.g. solid particles
- B01F25/30—Injector mixers
- B01F25/31—Injector mixers in conduits or tubes through which the main component flows
- B01F25/313—Injector mixers in conduits or tubes through which the main component flows wherein additional components are introduced in the centre of the conduit
- B01F25/3132—Injector mixers in conduits or tubes through which the main component flows wherein additional components are introduced in the centre of the conduit by using two or more injector devices
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F25/00—Flow mixers; Mixers for falling materials, e.g. solid particles
- B01F25/30—Injector mixers
- B01F25/31—Injector mixers in conduits or tubes through which the main component flows
- B01F25/313—Injector mixers in conduits or tubes through which the main component flows wherein additional components are introduced in the centre of the conduit
- B01F25/3133—Injector mixers in conduits or tubes through which the main component flows wherein additional components are introduced in the centre of the conduit characterised by the specific design of the injector
- B01F25/31332—Ring, torus, toroidal or coiled configurations
-
- 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
- B01J8/0278—Feeding reactive fluids
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B3/00—Hydrogen; Gaseous mixtures containing hydrogen; Separation of hydrogen from mixtures containing it; Purification of hydrogen
- C01B3/02—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen
- C01B3/32—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air
- C01B3/34—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air by reaction of hydrocarbons with gasifying agents
- C01B3/38—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air by reaction of hydrocarbons with gasifying agents using catalysts
- C01B3/386—Catalytic partial combustion
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B2203/00—Integrated processes for the production of hydrogen or synthesis gas
- C01B2203/02—Processes for making hydrogen or synthesis gas
- C01B2203/025—Processes for making hydrogen or synthesis gas containing a partial oxidation step
- C01B2203/0261—Processes for making hydrogen or synthesis gas containing a partial oxidation step containing a catalytic partial oxidation step [CPO]
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Organic Chemistry (AREA)
- Combustion & Propulsion (AREA)
- Engineering & Computer Science (AREA)
- Fluid Mechanics (AREA)
- Physics & Mathematics (AREA)
- Health & Medical Sciences (AREA)
- General Health & Medical Sciences (AREA)
- Inorganic Chemistry (AREA)
- Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Feeding, Discharge, Calcimining, Fusing, And Gas-Generation Devices (AREA)
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| DE10359744 | 2003-12-19 | ||
| DE10359744A DE10359744A1 (de) | 2003-12-19 | 2003-12-19 | Verfahren und Vorrichtung zum Eindüsen von Sauerstoff in einen Synthesereaktor |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| ES2356824T3 true ES2356824T3 (es) | 2011-04-13 |
Family
ID=34672921
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| ES04801221T Expired - Lifetime ES2356824T3 (es) | 2003-12-19 | 2004-12-10 | Procedimiento y dispositivo para la inyección de oxígeno en un reactor de síntesis. |
Country Status (12)
| Country | Link |
|---|---|
| US (1) | US8043577B2 (enExample) |
| EP (1) | EP1694430B1 (enExample) |
| JP (1) | JP5132938B2 (enExample) |
| AT (1) | ATE489163T1 (enExample) |
| DE (2) | DE10359744A1 (enExample) |
| DK (1) | DK1694430T3 (enExample) |
| EA (1) | EA009402B1 (enExample) |
| EG (1) | EG25659A (enExample) |
| ES (1) | ES2356824T3 (enExample) |
| NO (1) | NO20063258L (enExample) |
| PL (1) | PL1694430T3 (enExample) |
| WO (1) | WO2005063373A1 (enExample) |
Families Citing this family (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE102006054415A1 (de) * | 2006-11-16 | 2008-05-21 | Uhde Gmbh | Verfahren und Vorrichtung zum Eindüsen von Sauerstoff in ein einen Synthesereaktor durchströmendes Reaktionsgas |
| DE102006060507A1 (de) * | 2006-12-19 | 2008-06-26 | Basf Se | Reaktor zur Durchführung einer Reaktion zwischen zwei fluiden Edukten an einem Katalysatorbett mit Vorvermischen der fluiden Edukte in einer Einmischvorrichtung |
| DE102007027881B4 (de) * | 2007-06-13 | 2012-02-16 | Outotec Oyj | Verfahren und Vorrichtung zur Mischung von Gasen |
| DE102008010422A1 (de) * | 2008-02-21 | 2009-09-03 | Uhde Gmbh | Fixiervorrichtung für Katalysatorpartikel |
| AR075787A1 (es) | 2009-03-05 | 2011-04-27 | Uhde Gmbh | Procedimiento y dispositivo para retener el catalizador en forma de particulas arrastradas ingresantes |
| DE102009011375A1 (de) | 2009-03-05 | 2010-09-23 | Uhde Gmbh | Verfahren zur Niederhaltung von angeströmten Katalysatorpartikeln |
| DE102015209874A1 (de) | 2015-05-29 | 2016-12-01 | Thyssenkrupp Ag | System zur Eindüsung einer reaktiven gashaltigen Komponente in einen Synthesereaktor |
| US10933395B1 (en) * | 2019-08-26 | 2021-03-02 | Uop Llc | Apparatus for catalytic reforming hydrocarbons having flow distributor and process for reforming hydrocarbons |
Family Cites Families (33)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US262692A (en) * | 1882-08-15 | Elevator | ||
| US2361623A (en) * | 1943-04-16 | 1944-10-31 | Phillips Petroleum Co | Catalyst chamber |
| US2518583A (en) * | 1945-06-27 | 1950-08-15 | Universal Oil Prod Co | Catalytic reactor |
| US2584391A (en) * | 1947-03-29 | 1952-02-05 | Universal Oil Prod Co | Apparatus for effecting fluidized contact between solid particles and fluid mediums |
| US2632692A (en) * | 1949-01-18 | 1953-03-24 | Hydrocarbon Research Inc | Multiple bed catalyst apparatus |
| US2809981A (en) * | 1953-02-27 | 1957-10-15 | Exxon Research Engineering Co | Method of carrying out homogeneous vapor phase reactions |
| US2954281A (en) * | 1954-09-27 | 1960-09-27 | Stone & Webster Eng Corp | Method and apparatus for the fluidized catalytic treatment of fluid reactants |
| US3208833A (en) * | 1963-05-01 | 1965-09-28 | Universal Oil Prod Co | Fluid distributing means for packed chambers |
| US3685971A (en) * | 1970-07-06 | 1972-08-22 | Universal Oil Prod Co | Flow distributing apparatus |
| BE789153A (fr) * | 1971-09-23 | 1973-03-22 | Aquitaine Petrole | Perfectionnement a la fabrication du styrene |
| GB1449205A (en) * | 1973-11-06 | 1976-09-15 | Exxon Research Engineering Co | Distribut-ng a gas-liquid mixture in a reactor vessel |
| US4166834A (en) * | 1977-09-27 | 1979-09-04 | John Zink Company | Air injector nozzle for secondary reformer |
| US4223843A (en) * | 1978-03-16 | 1980-09-23 | Texaco Inc. | Air distribution apparatus |
| US4372920A (en) * | 1979-07-13 | 1983-02-08 | Ammonia Casale S.A. | Axial-radial reactor for heterogeneous synthesis |
| JPS5852692B2 (ja) * | 1979-11-08 | 1983-11-24 | 日揮株式会社 | 接触反応器 |
| GB2065492B (en) | 1979-12-21 | 1983-10-19 | Uop Inc | Fluid distributor for fixed-bed catalytic reaction zones |
| JPS5876134A (ja) | 1981-11-02 | 1983-05-09 | Toyo Eng Corp | 複数の円筒状反応室を有する球形反応器とその使用法 |
| US4443551A (en) * | 1982-01-11 | 1984-04-17 | Texaco Inc. | Method and new distributor for delivering high velocity gas from a gas distributor through a nozzle with decreased erosion in the nozzle |
| US4994239A (en) * | 1984-02-03 | 1991-02-19 | Phillips Petroleum Company | Catalyst regeneration |
| US4595145A (en) * | 1984-10-01 | 1986-06-17 | Texaco Inc. | Air distribution apparatus for a fluid catalytic cracking catalyst regenerator |
| US4705621A (en) * | 1985-03-22 | 1987-11-10 | Mobil Oil Corporation | Catalytic reactor system with crosscurrent liquid and gasflow |
| DE3532413A1 (de) * | 1985-09-11 | 1987-03-12 | Uhde Gmbh | Vorrichtung zur erzeugung von synthesegas |
| DK155979C (da) * | 1987-05-20 | 1989-10-30 | Haldor Topsoe As | Fordelingselement til fordeling af gas til en reaktor |
| US4865820A (en) * | 1987-08-14 | 1989-09-12 | Davy Mckee Corporation | Gas mixer and distributor for reactor |
| DE3829215A1 (de) | 1988-08-29 | 1990-03-08 | Uhde Gmbh | Reaktor zur durchfuehrung katalytischer gasreaktionen mit einem druckfesten mantel und je einem kugelboden am stirnseitigen aussenrand |
| DE3829214A1 (de) | 1988-08-29 | 1990-03-08 | Uhde Gmbh | Reaktor zur durchfuehrung katalytischer gasreaktionen mit einer mehrzahl von kaltgaszufuehrungen |
| US5043500A (en) * | 1989-12-20 | 1991-08-27 | Uop | Use of steam eductor to supply oxygen for oxidative reheating in dehydrogenation of C3 + hydrocarbons |
| DE4027410A1 (de) | 1990-08-30 | 1992-03-05 | Uhde Gmbh | Reformer, insbesondere autothermer sekundaerreformer |
| US5439859A (en) * | 1992-04-27 | 1995-08-08 | Sun Company, Inc. (R&M) | Process and catalyst for dehydrogenation of organic compounds |
| IT1255710B (it) | 1992-10-01 | 1995-11-10 | Snam Progetti | Procedimento integrato per produrre olefine da miscele gassose contenenti metano |
| US5935489A (en) * | 1997-04-25 | 1999-08-10 | Exxon Research And Engineering Co. | Distributed injection process and apparatus for producing synthesis gas |
| AU2001251334A1 (en) * | 2000-04-05 | 2001-10-23 | Hydrogen Burner Technology, Inc. | Pulsed flow, fuel-processing system |
| US20020098136A1 (en) * | 2001-01-23 | 2002-07-25 | Nicholas Vanderborgh | Device for staged addition of heat to a reactor |
-
2003
- 2003-12-19 DE DE10359744A patent/DE10359744A1/de not_active Withdrawn
-
2004
- 2004-12-10 WO PCT/EP2004/014050 patent/WO2005063373A1/de not_active Ceased
- 2004-12-10 JP JP2006544287A patent/JP5132938B2/ja not_active Expired - Fee Related
- 2004-12-10 US US10/583,572 patent/US8043577B2/en not_active Expired - Fee Related
- 2004-12-10 EP EP04801221A patent/EP1694430B1/de not_active Expired - Lifetime
- 2004-12-10 ES ES04801221T patent/ES2356824T3/es not_active Expired - Lifetime
- 2004-12-10 EA EA200601115A patent/EA009402B1/ru not_active IP Right Cessation
- 2004-12-10 DK DK04801221.5T patent/DK1694430T3/da active
- 2004-12-10 PL PL04801221T patent/PL1694430T3/pl unknown
- 2004-12-10 AT AT04801221T patent/ATE489163T1/de not_active IP Right Cessation
- 2004-12-10 DE DE502004011937T patent/DE502004011937D1/de not_active Expired - Lifetime
-
2006
- 2006-06-11 EG EGNA2006000544 patent/EG25659A/xx active
- 2006-07-13 NO NO20063258A patent/NO20063258L/no not_active Application Discontinuation
Also Published As
| Publication number | Publication date |
|---|---|
| JP5132938B2 (ja) | 2013-01-30 |
| US20070100191A1 (en) | 2007-05-03 |
| NO20063258L (no) | 2006-09-19 |
| EP1694430B1 (de) | 2010-11-24 |
| DE502004011937D1 (de) | 2011-01-05 |
| EG25659A (en) | 2012-05-08 |
| WO2005063373A1 (de) | 2005-07-14 |
| DE10359744A1 (de) | 2005-07-14 |
| ATE489163T1 (de) | 2010-12-15 |
| EA009402B1 (ru) | 2007-12-28 |
| US8043577B2 (en) | 2011-10-25 |
| EP1694430A1 (de) | 2006-08-30 |
| PL1694430T3 (pl) | 2011-05-31 |
| DK1694430T3 (da) | 2011-02-28 |
| JP2007516074A (ja) | 2007-06-21 |
| EA200601115A1 (ru) | 2006-12-29 |
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