AR004100A1 - Distribuidor de catalizador agotado auto-aireante - Google Patents
Distribuidor de catalizador agotado auto-aireanteInfo
- Publication number
- AR004100A1 AR004100A1 ARP960104900A ARP960104900A AR004100A1 AR 004100 A1 AR004100 A1 AR 004100A1 AR P960104900 A ARP960104900 A AR P960104900A AR P960104900 A ARP960104900 A AR P960104900A AR 004100 A1 AR004100 A1 AR 004100A1
- Authority
- AR
- Argentina
- Prior art keywords
- spent catalyst
- aeration
- fluid
- distributor
- catalyst distributor
- Prior art date
Links
Classifications
-
- 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
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G11/00—Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils
- C10G11/14—Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils with preheated moving solid catalysts
- C10G11/18—Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils with preheated moving solid catalysts according to the "fluidised-bed" technique
- C10G11/182—Regeneration
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F35/00—Accessories for mixers; Auxiliary operations or auxiliary devices; Parts or details of general application
- B01F35/71—Feed mechanisms
- B01F35/717—Feed mechanisms characterised by the means for feeding the components to the mixer
- B01F35/7182—Feed mechanisms characterised by the means for feeding the components to the mixer with means for feeding the material with a fractal or tree-type distribution in a surface
-
- 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
- B01J8/0015—Feeding of the particles in the reactor; Evacuation of the particles out of the reactor
- B01J8/003—Feeding of the particles in the reactor; Evacuation of the particles out of the reactor in a downward flow
-
- 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
- B01J8/18—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles
- B01J8/1818—Feeding of the fluidising gas
-
- 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
- B01J8/18—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles
- B01J8/1872—Details of the fluidised bed reactor
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G11/00—Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils
- C10G11/14—Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils with preheated moving solid catalysts
- C10G11/18—Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils with preheated moving solid catalysts according to the "fluidised-bed" technique
-
- 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
- B01F25/40—Static mixers
- B01F25/41—Mixers of the fractal type
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Organic Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Combustion & Propulsion (AREA)
- General Chemical & Material Sciences (AREA)
- Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
- Feeding, Discharge, Calcimining, Fusing, And Gas-Generation Devices (AREA)
- Catalysts (AREA)
Abstract
Un distribuidor de catalizador agotado en un regenerador de fluido de una unidad de craqueo catalítica se auto-airea adhiriendo en el lado inferior decada brazo con canaletas un reborde contiguo que captura el fluido de aireación en elevación utiliza el fluido de aireación para airear elcatalizador agotado que fluye a través de los brazos con canaletas del distribuidor de catalizador agotado. Los orificios que se encuentran en laplaca inferior de cada brazo con canaletas hacen pasar al fluido de aireación capturado hacia el catalizador agotado que fluye dentro del brazo concanaletas. El fluido de aireación brinda aireación y fluidización del catalizador agotado para facilitar el flujo del catalizador agotado a travésde los brazos con canaletas del distribuidor de catalizador agotado.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US08/557,780 US5635140A (en) | 1995-11-13 | 1995-11-13 | Self-aerating spent catalyst distributor |
Publications (1)
Publication Number | Publication Date |
---|---|
AR004100A1 true AR004100A1 (es) | 1998-09-30 |
Family
ID=24226847
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
ARP960104900A AR004100A1 (es) | 1995-11-13 | 1996-10-24 | Distribuidor de catalizador agotado auto-aireante |
Country Status (10)
Country | Link |
---|---|
US (1) | US5635140A (es) |
EP (1) | EP0773275B1 (es) |
JP (1) | JP4043541B2 (es) |
KR (1) | KR100426829B1 (es) |
AR (1) | AR004100A1 (es) |
BR (1) | BR9605533A (es) |
DE (1) | DE69612817T2 (es) |
MX (1) | MX9605294A (es) |
NO (1) | NO314688B1 (es) |
TW (1) | TW411283B (es) |
Families Citing this family (15)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US6224833B1 (en) * | 1998-12-15 | 2001-05-01 | Koch-Glitsch, Inc. | Apparatus for contacting of gases and solids in fluidized beds |
US6503460B1 (en) | 1999-03-17 | 2003-01-07 | Kellogg Brown & Root, Inc. | Staged catalyst regeneration in a baffled fluidized bed |
US6809054B1 (en) | 2000-11-21 | 2004-10-26 | Uop Llc | FCC spent catalyst distributor |
US6797239B1 (en) | 2000-11-22 | 2004-09-28 | Shell Oil Company | Spent catalyst distributor |
US7452838B2 (en) * | 2004-12-22 | 2008-11-18 | Exxonmobil Chemical Patents Inc. | Controlling temperature in catalyst regenerators |
US7745365B2 (en) * | 2007-03-09 | 2010-06-29 | Stone & Webster Process Technology, Inc. | Bathtub-type spent catalyst distributor for effective counter-current regeneration in fluid catalytic cracking units |
US8618012B2 (en) | 2010-04-09 | 2013-12-31 | Kellogg Brown & Root Llc | Systems and methods for regenerating a spent catalyst |
US8618011B2 (en) | 2010-04-09 | 2013-12-31 | Kellogg Brown & Root Llc | Systems and methods for regenerating a spent catalyst |
US8728302B2 (en) | 2010-06-25 | 2014-05-20 | Exxonmobil Research And Engineering Company | Spent catalyst riser distributor |
CN102350275B (zh) * | 2011-07-19 | 2013-08-07 | 浙江大学 | 一种流化床反应器气体预分布器 |
CN102504861B (zh) * | 2011-11-01 | 2013-10-09 | 中国石油大学(北京) | 流化催化裂化装置待生催化剂分配器及分配方法 |
US9555389B2 (en) * | 2013-03-13 | 2017-01-31 | Kellogg Brown & Root Llc | Gas distributor nozzles |
FR3065886B1 (fr) * | 2017-05-05 | 2021-12-31 | Ifp Energies Now | Nouveau dispositif de distribution de melange polyphasique dans une enceinte comportant un milieu fluidise |
ZA201801627B (en) | 2017-06-03 | 2019-05-29 | Indian Oil Corp Ltd | An apparatus for distribution of catalyst in fluidized catalytic cracking unit |
CN107628986B (zh) * | 2017-10-20 | 2021-07-13 | 山东明化新材料有限公司 | 一种吡啶生产用的催化剂均布器 |
Family Cites Families (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE2707478A1 (de) * | 1976-03-01 | 1977-09-08 | Pullman Inc | Verfahren und vorrichtung zur regenerierung von crack-katalysatoren |
US4051069A (en) * | 1976-05-07 | 1977-09-27 | Texaco Inc. | Fluidized catalytic cracking regeneration process |
US4721603A (en) * | 1983-06-13 | 1988-01-26 | Chevron Research Company | Separation of reacted hydrocarbons and catalyst in fluidized catalytic cracking |
US4615992A (en) * | 1985-04-02 | 1986-10-07 | Air Products And Chemicals, Inc. | Catalyst regeneration process with improved catalyst distribution in a fluidized bed |
US4927606A (en) * | 1986-05-29 | 1990-05-22 | Uop | FCC Stripping apparatus |
EP0289991A3 (en) * | 1987-05-07 | 1990-01-17 | Air Products And Chemicals, Inc. | Fluid catalytic cracking unit catalyst transfer and distribution system and process |
US4888156A (en) * | 1988-04-29 | 1989-12-19 | Houdry Process Corporation | Fluid catalytic cracking unit regeneration having internal cooling means |
US5156817A (en) * | 1990-05-15 | 1992-10-20 | Exxon Research And Engineering Company | Fccu regenerator catalyst distribution system |
-
1995
- 1995-11-13 US US08/557,780 patent/US5635140A/en not_active Expired - Lifetime
-
1996
- 1996-10-24 AR ARP960104900A patent/AR004100A1/es unknown
- 1996-11-01 MX MX9605294A patent/MX9605294A/es unknown
- 1996-11-05 EP EP96117692A patent/EP0773275B1/en not_active Expired - Lifetime
- 1996-11-05 DE DE69612817T patent/DE69612817T2/de not_active Expired - Lifetime
- 1996-11-11 BR BR9605533A patent/BR9605533A/pt not_active IP Right Cessation
- 1996-11-12 KR KR1019960053534A patent/KR100426829B1/ko not_active IP Right Cessation
- 1996-11-12 JP JP30058096A patent/JP4043541B2/ja not_active Expired - Lifetime
- 1996-11-12 NO NO19964800A patent/NO314688B1/no not_active IP Right Cessation
- 1996-11-14 TW TW085113946A patent/TW411283B/zh not_active IP Right Cessation
Also Published As
Publication number | Publication date |
---|---|
KR100426829B1 (ko) | 2004-06-18 |
NO964800L (no) | 1997-05-14 |
EP0773275A1 (en) | 1997-05-14 |
JP4043541B2 (ja) | 2008-02-06 |
MX9605294A (es) | 1997-05-31 |
DE69612817D1 (de) | 2001-06-21 |
DE69612817T2 (de) | 2001-08-30 |
JPH09173820A (ja) | 1997-07-08 |
US5635140A (en) | 1997-06-03 |
EP0773275B1 (en) | 2001-05-16 |
BR9605533A (pt) | 1998-08-11 |
NO314688B1 (no) | 2003-05-05 |
NO964800D0 (no) | 1996-11-12 |
TW411283B (en) | 2000-11-11 |
KR970025687A (ko) | 1997-06-24 |
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