PE20060805A1 - DEVICE FOR MIXING LIGHT HYDROCARBON, STEAM AND A GAS STREAM CONTAINING OXYGEN, AND PROCESS TO OPTIMIZE THE SIZE AND ORIENTATION OF THE INNER TUBE AND TUBE OPENINGS OF THE DEVICE - Google Patents
DEVICE FOR MIXING LIGHT HYDROCARBON, STEAM AND A GAS STREAM CONTAINING OXYGEN, AND PROCESS TO OPTIMIZE THE SIZE AND ORIENTATION OF THE INNER TUBE AND TUBE OPENINGS OF THE DEVICEInfo
- Publication number
- PE20060805A1 PE20060805A1 PE2005001455A PE2005001455A PE20060805A1 PE 20060805 A1 PE20060805 A1 PE 20060805A1 PE 2005001455 A PE2005001455 A PE 2005001455A PE 2005001455 A PE2005001455 A PE 2005001455A PE 20060805 A1 PE20060805 A1 PE 20060805A1
- Authority
- PE
- Peru
- Prior art keywords
- gas
- light hydrocarbon
- openings
- orientation
- tube
- Prior art date
Links
Classifications
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- 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
- B01J4/00—Feed or outlet devices; Feed or outlet control devices
- B01J4/001—Feed or outlet devices as such, e.g. feeding tubes
- B01J4/002—Nozzle-type elements
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- 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
-
- 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
- B01F25/31331—Perforated, multi-opening, with a plurality of holes
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- 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
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- 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
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- 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
- C01B3/382—Multi-step processes
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- 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
- C01B2203/0205—Processes for making hydrogen or synthesis gas containing a reforming step
- C01B2203/0227—Processes for making hydrogen or synthesis gas containing a reforming step containing a catalytic reforming step
- C01B2203/0244—Processes for making hydrogen or synthesis gas containing a reforming step containing a catalytic reforming step the reforming step being an autothermal reforming step, e.g. secondary reforming processes
-
- 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
- C01B2203/12—Feeding the process for making hydrogen or synthesis gas
- C01B2203/1276—Mixing of different feed components
- C01B2203/1282—Mixing of different feed components using static mixers
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Organic Chemistry (AREA)
- Health & Medical Sciences (AREA)
- General Health & Medical Sciences (AREA)
- Engineering & Computer Science (AREA)
- Combustion & Propulsion (AREA)
- Inorganic Chemistry (AREA)
- Hydrogen, Water And Hydrids (AREA)
- Accessories For Mixers (AREA)
Abstract
DONDE EL DISPOSITIVO COMPRENDE: a) UN TUBO INTERIOR QUE TIENE UNA PLURALIDAD DE ABERTURAS A TRAVES DE SUS PAREDES; b) UN TUBO CASCO QUE RODEA A (a), CREANDO UN ESPACIO ANULAR ENTRE AMBOS TUBOS, Y TIENE UNA PLURALIDAD DE ABERTURAS EN SUS PAREDES; Y, c) UNA CAMISA QUE RODEA TODO O PARTE DE (b); DONDE EL GAS CONTENIENDO OXIGENO ES ALIMENTADO DENTRO DE (a) Y (c), O DENTRO DE (b), Y EL HIDROCARBURO LIGERO Y EL VAPOR SON ALIMENTADOS DENTRO DE (b), O DENTRO DE (a). (a) Y (b) SON CALIBRADOS PARA OBTENER UNA VELOCIDAD DE GAS EN EL ESPACIO ANULAR ENTRE 30 Y 900 pies/s. UNA ZONA DE EXPANSION ESTA CORRIENTE ABAJO DE (a) Y (b); Y UN MATERIAL INERTE PREVIENE LA TRANSFERENCIA DE CALOR RADIANTE ENTRE DICHA ZONA Y UN CATALIZADOR REFORMADOR/OXIDACION PARCIAL ACTIVO. EL DISPOSITIVO OPERA BAJO UNA PRESION ENTRE 50 Y 600 psig, Y UNA TEMPERATURA ENTRE 600 Y 1200°F. EL HIDROCARBURO LIGERO ES GAS NATURAL. EL PROCESO INCLUYE UTILIZAR LA DINAMICA DE FLUJO COMPUTACIONAL A FIN DE EVALUAR LOS COMPONENTES DE LA VELOCIDAD DEL GAS DE LA MEZCLA DEL GAS DE VAPOR, GAS NATURAL Y EL GAS QUE CONTIENE OXIGENO DENTRO DEL DISPOSITIVO PARA OBTENER UNA PLURALIDAD DE TAMANOS U ORIENTACIONES DE LAS ABERTURAS. SE PREVIENE EL AUTOENCEDIDO DE LA MEZCLA DE ALIMENTACION ANTES QUE SE CONVIERTA EN GAS DE SINTESIS POR CONTACTO CON DICHO CATALIZADORWHERE THE DEVICE INCLUDES: a) AN INTERIOR TUBE THAT HAS A PLURALITY OF OPENINGS THROUGH ITS WALLS; b) A HULL TUBE THAT SURROUNDS (a), CREATING AN ANNULAR SPACE BETWEEN BOTH TUBES, AND HAS A PLURALITY OF OPENINGS IN ITS WALLS; AND, c) A SHIRT THAT SURROUNDS ALL OR PART OF (b); WHERE OXYGEN-CONTAINING GAS IS FEED INTO (a) AND (c), OR INTO (b), AND THE LIGHT HYDROCARBON AND VAPOR ARE FEED INTO (b), OR INTO (a). (a) AND (b) ARE CALIBRATED TO OBTAIN A GAS VELOCITY IN THE ANNULAR SPACE BETWEEN 30 AND 900 ft / s. AN EXPANSION ZONE IS Downstream OF (a) AND (b); AND AN INERT MATERIAL PREVENTS RADIANT HEAT TRANSFER BETWEEN SUCH AREA AND AN ACTIVE PARTIAL OXIDATION / REFORMING CATALYST. THE DEVICE OPERATES UNDER A PRESSURE BETWEEN 50 AND 600 psig, AND A TEMPERATURE BETWEEN 600 AND 1200 ° F. LIGHT HYDROCARBON IS NATURAL GAS. THE PROCESS INCLUDES USING THE COMPUTATIONAL FLOW DYNAMICS IN ORDER TO EVALUATE THE GAS VELOCITY COMPONENTS OF THE MIXTURE OF THE STEAM GAS, NATURAL GAS AND THE GAS CONTAINING OXYGEN WITHIN THE DEVICE FOR ORIENTATION ORTENERATIONS. . THE SELF-IGNITION OF THE FEED MIXTURE IS PREVENTED BEFORE IT BECOMES A SYNTHESIS GAS BY CONTACT WITH SUCH CATALYST
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US63579204P | 2004-12-14 | 2004-12-14 |
Publications (1)
Publication Number | Publication Date |
---|---|
PE20060805A1 true PE20060805A1 (en) | 2006-08-30 |
Family
ID=36588450
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PE2005001455A PE20060805A1 (en) | 2004-12-14 | 2005-12-14 | DEVICE FOR MIXING LIGHT HYDROCARBON, STEAM AND A GAS STREAM CONTAINING OXYGEN, AND PROCESS TO OPTIMIZE THE SIZE AND ORIENTATION OF THE INNER TUBE AND TUBE OPENINGS OF THE DEVICE |
Country Status (6)
Country | Link |
---|---|
EP (1) | EP1835988A2 (en) |
CN (1) | CN101111304A (en) |
AU (1) | AU2005316638A1 (en) |
MY (1) | MY139265A (en) |
PE (1) | PE20060805A1 (en) |
WO (1) | WO2006065766A2 (en) |
Families Citing this family (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP5006413B2 (en) | 2007-03-15 | 2012-08-22 | ダウ グローバル テクノロジーズ エルエルシー | Mixer for continuous flow reactor |
WO2011080754A2 (en) * | 2009-12-29 | 2011-07-07 | Indian Oil Corporation Ltd. | A feed nozzle assembly |
WO2012005644A1 (en) * | 2010-07-09 | 2012-01-12 | Reformtech Sweden Ab | Method for providing a homogeneous mixture of liquid fuels and oxidants for use in a catalytic reactor |
CN110740805B (en) * | 2017-04-21 | 2022-03-11 | 联邦科学与工业研究组织 | Flow distribution system |
EP3441360B1 (en) | 2017-08-10 | 2020-07-29 | Sener Ingenieria Y Sistemas, S.A. | System for alcohol reforming and hydrogen production, units of the system and method thereof |
DE102018110293A1 (en) * | 2018-04-27 | 2019-10-31 | Linde Aktiengesellschaft | Process and apparatus for treating a waste liquor |
EP3693338B1 (en) | 2019-02-07 | 2021-09-01 | Sener Ingenieria Y Sistemas, S.A. | High-pressure auto-thermal system for reforming alcohol and producing hydrogen, and method therefor |
Family Cites Families (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4166834A (en) * | 1977-09-27 | 1979-09-04 | John Zink Company | Air injector nozzle for secondary reformer |
DE3532413A1 (en) * | 1985-09-11 | 1987-03-12 | Uhde Gmbh | DEVICE FOR GENERATING SYNTHESIS GAS |
US4865820A (en) * | 1987-08-14 | 1989-09-12 | Davy Mckee Corporation | Gas mixer and distributor for reactor |
US5292246A (en) * | 1988-05-02 | 1994-03-08 | Institut Francais Du Petrole | Burner for the manufacture of synthetic gas comprising a solid element with holes |
US5980596A (en) * | 1997-04-25 | 1999-11-09 | Exxon Research And Engineering Co. | Multi-injector autothermal reforming process and apparatus for producing synthesis gas (law 565). |
US6620389B1 (en) * | 2000-06-21 | 2003-09-16 | Utc Fuel Cells, Llc | Fuel gas reformer assemblage |
-
2005
- 2005-12-12 AU AU2005316638A patent/AU2005316638A1/en not_active Abandoned
- 2005-12-12 CN CNA2005800471935A patent/CN101111304A/en active Pending
- 2005-12-12 WO PCT/US2005/044968 patent/WO2006065766A2/en active Application Filing
- 2005-12-12 EP EP05853797A patent/EP1835988A2/en not_active Withdrawn
- 2005-12-13 MY MYPI20055849A patent/MY139265A/en unknown
- 2005-12-14 PE PE2005001455A patent/PE20060805A1/en active IP Right Grant
Also Published As
Publication number | Publication date |
---|---|
WO2006065766A2 (en) | 2006-06-22 |
EP1835988A2 (en) | 2007-09-26 |
CN101111304A (en) | 2008-01-23 |
MY139265A (en) | 2009-09-30 |
AU2005316638A1 (en) | 2006-06-22 |
WO2006065766A3 (en) | 2006-12-07 |
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Legal Events
Date | Code | Title | Description |
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FG | Grant, registration |