ES2130352T3 - Procedimiento fcc que usa una zona de desprendimiento del tubo elevador del reactor con zona de separacion del catalizador suspendido. - Google Patents
Procedimiento fcc que usa una zona de desprendimiento del tubo elevador del reactor con zona de separacion del catalizador suspendido.Info
- Publication number
- ES2130352T3 ES2130352T3 ES94301210T ES94301210T ES2130352T3 ES 2130352 T3 ES2130352 T3 ES 2130352T3 ES 94301210 T ES94301210 T ES 94301210T ES 94301210 T ES94301210 T ES 94301210T ES 2130352 T3 ES2130352 T3 ES 2130352T3
- Authority
- ES
- Spain
- Prior art keywords
- riser
- catalyst
- zone
- suspended
- 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
- 239000003054 catalyst Substances 0.000 title abstract 7
- 238000000034 method Methods 0.000 title abstract 3
- 238000000926 separation method Methods 0.000 title abstract 2
- 238000013022 venting Methods 0.000 abstract 1
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
- B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
- B01J8/005—Separating solid material from the gas/liquid stream
- B01J8/0055—Separating solid material from the gas/liquid stream using cyclones
-
- 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
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Engineering & Computer Science (AREA)
- General Chemical & Material Sciences (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
- Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)
- Cyclones (AREA)
Abstract
LA OPERACION DE UN PROCESO FCC SE PERFECCIONA MEDIANTE EL USO DE UNA NUEVA CONFIGURACION DE DESACOPLADOR DEL ELEVADOR DE REACTOR NUCLEAR, QUE RESULTA EN CATALIZADOR ESTANDO SUSPENDIDO EN UNA ZONA DE DESACOPLAMIENTO EN UNA SECCION 29 DEL ELEVADOR, PROXIMA O POR ENCIMA DE LAS ENTRADAS 34 DE CICLON DEL ELEVADOR, COMO UNA CONSECUENCIA DE VAPORES, Y CATALIZADOR QUE SALE DEL ELEVADOR A TRAVES DE LAS ENTRADAS DE CICLON, PARA OBTENER UNA DENSIDAD CATALIZADORA SUSPENDIDA, QUE ES SUPERIOR A LA DENSIDAD CATALIZADORA FLUYENTE MAS ABAJO EN EL ELEVADOR. EL CATALIZADOR SUSPENDIDO PROPORCIONA UNA ZONA DE DESACOPLAMIENTO QUE REFUERZA LA SEPARACION DEL CATALIZADOR DE LOS VAPORES DEL PRODUCTO. EL ELEVADOR 22, 26, 29 OPERA EN CONDICIONES QUE EVITAN TODA DESCARGA IMPORTANTE DEL VAPOR DEL PRODUCTO PROCEDENTE DE SU EXTREMO 40 SUPERIOR. LA DISPOSICION PROPORCIONA ADEMAS UN METODO CONVENIENTE PARA AIREAR VAPORES DE DESPRENDIMIENTO, INTRODUCIDOS EN 26, Y QUE SALEN POR EL SISTEMA DE CICLON DEL REACTOR 34, 36, 42, 44.
Applications Claiming Priority (7)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US07/790,924 US5290430A (en) | 1991-11-13 | 1991-11-13 | Riser disengager with suspended catalyst separation zone |
| AU55283/94A AU5528394A (en) | 1991-11-13 | 1994-02-21 | FCC process using reactor riser disengager with suspended catalyst separation zone |
| EP94301210A EP0668341B1 (en) | 1991-11-13 | 1994-02-21 | FCC process using reactor riser disengager with suspended catalyst separation zone |
| CA002116163A CA2116163A1 (en) | 1991-11-13 | 1994-02-22 | Fcc process using reactor riser disengager with suspended catalyst separation zone |
| ZA941208A ZA941208B (en) | 1991-11-13 | 1994-02-22 | FCC process using reactor riser disengager with suspended catalyst separation zone |
| RU9494006801A RU2079541C1 (ru) | 1991-11-13 | 1994-02-28 | Способ проведения каталитического крекинга сырья в псевдоожиженном слое и устройство для его осуществления |
| CN94102538A CN1062890C (zh) | 1991-11-13 | 1994-02-28 | 一种新的流化催化裂化的方法及装置 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| ES2130352T3 true ES2130352T3 (es) | 1999-07-01 |
Family
ID=36950120
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| ES94301210T Expired - Lifetime ES2130352T3 (es) | 1991-11-13 | 1994-02-21 | Procedimiento fcc que usa una zona de desprendimiento del tubo elevador del reactor con zona de separacion del catalizador suspendido. |
Country Status (11)
| Country | Link |
|---|---|
| US (2) | US5290430A (es) |
| EP (1) | EP0668341B1 (es) |
| CN (1) | CN1062890C (es) |
| AT (1) | ATE179205T1 (es) |
| AU (1) | AU5528394A (es) |
| CA (1) | CA2116163A1 (es) |
| DE (1) | DE69418024T2 (es) |
| ES (1) | ES2130352T3 (es) |
| GR (1) | GR3030140T3 (es) |
| RU (1) | RU2079541C1 (es) |
| ZA (1) | ZA941208B (es) |
Families Citing this family (25)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5614083A (en) * | 1991-11-13 | 1997-03-25 | Uop | Riser disengager with suspended catalyst separation zone |
| US5593643A (en) * | 1994-12-28 | 1997-01-14 | Uop | FCC arrangement with externally suspended catalyst separation zone |
| CN1095392C (zh) * | 1998-12-25 | 2002-12-04 | 中国石油化工集团公司 | 一种用于流化催化转化的提升管反应器 |
| RU2228349C2 (ru) * | 2000-05-18 | 2004-05-10 | Юоп Ллк | Способ и устройство для контактирования исходной реакционной смеси с немедленным отделением катализатора |
| CN1114479C (zh) * | 2000-06-02 | 2003-07-16 | 清华大学 | 分隔式分布板双射流管射流流化床 |
| US7008527B2 (en) * | 2002-10-23 | 2006-03-07 | Institut Francais Du Petrole | Process for catalytic cracking two integrated cracking zones of different degrees of severity followed by a cooling zone |
| US6902593B2 (en) * | 2003-02-26 | 2005-06-07 | Kellogg Brown And Root, Inc. | Separation device to remove fine particles |
| CN100473463C (zh) * | 2003-06-04 | 2009-04-01 | 国际壳牌研究有限公司 | 分离装置 |
| NO20040615L (no) * | 2004-02-11 | 2005-08-12 | Ellycrack As | Lav temperatur katalytisk krakking og omdannelsesprosess for oppgradering av tung raolje |
| RU2262527C1 (ru) * | 2004-05-18 | 2005-10-20 | Открытое акционерное общество "Славнефть-Ярославнефтеоргсинтез" | Способ каталитического крекинга тяжелых нефтяных фракций |
| US7682501B2 (en) * | 2004-12-23 | 2010-03-23 | Abb Lummus Global, Inc. | Processing of different feeds in a fluid catalytic cracking unit |
| US7390339B1 (en) | 2005-05-05 | 2008-06-24 | Hach Ultra Analytics, Inc. | Vortex separator in particle detection systems |
| CN101045881B (zh) * | 2006-03-31 | 2010-06-23 | 中国石油化工股份有限公司 | 一种催化转化装置 |
| JP2010500435A (ja) * | 2006-08-08 | 2010-01-07 | シエル・インターナシヨネイル・リサーチ・マーチヤツピイ・ベー・ウイ | 接触分解ライザー反応器 |
| US7758817B2 (en) * | 2006-08-09 | 2010-07-20 | Uop Llc | Device for contacting high contaminated feedstocks with catalyst in an FCC unit |
| US20080081006A1 (en) * | 2006-09-29 | 2008-04-03 | Myers Daniel N | Advanced elevated feed distribution system for very large diameter RCC reactor risers |
| CN101191070B (zh) * | 2006-11-30 | 2011-02-09 | 中国石油化工股份有限公司石油化工科学研究院 | 一种生产低碳烯烃的方法 |
| US20090277514A1 (en) * | 2008-05-09 | 2009-11-12 | D-Cok, Llc | System and method to control catalyst migration |
| FR2966161B1 (fr) * | 2010-10-15 | 2013-12-20 | Total Raffinage Marketing | Procede de reaction et de stripage etage dans une unite de fcc pour maximisation de la production d'olefines |
| EP3062922B1 (en) * | 2013-10-29 | 2018-12-19 | Dow Global Technologies LLC | Cyclonic separation assembly having a low residence time plenum arranged in a fluidized bed reactor vessel |
| US20160168050A1 (en) * | 2014-12-12 | 2016-06-16 | Uop Llc | Process and apparatus with catalyst heating in a riser |
| US20160168051A1 (en) * | 2014-12-12 | 2016-06-16 | Uop Llc | Process and apparatus for heating catalyst in a regenerator |
| US9707533B2 (en) * | 2015-12-01 | 2017-07-18 | Dow Global Technologies Llc | Fluidized catalyst stripping unit for displacing entrained gas from catalyst particles |
| FR3073153B1 (fr) * | 2017-11-08 | 2019-11-22 | IFP Energies Nouvelles | Nouveau separateur gaz solide pour les unites de craquage catalytique possedant un riser externe |
| CN108893142B (zh) * | 2018-08-17 | 2020-09-01 | 中石化(洛阳)科技有限公司 | 一种重油裂化装置及重油裂化方法 |
Family Cites Families (19)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3817872A (en) * | 1972-02-07 | 1974-06-18 | Standard Oil Co | Cyclone separation method and apparatus |
| AR207247A1 (es) * | 1975-01-16 | 1976-09-22 | Pullman Inc | Colector de camara de sobrepresion externa para regenerador de aparato de termodesintegracion catalitica de fluido |
| AT364745B (de) * | 1975-03-24 | 1981-11-10 | Ashland Oil Inc | Verfahren und vorrichtung zum abscheiden feiner feststoffteilchen aus stroemenden gasen |
| US4295961A (en) * | 1979-11-23 | 1981-10-20 | Standard Oil Company (Indiana) | Method and apparatus for improved fluid catalytic riser reactor cracking of hydrocarbon feedstocks |
| US4377470A (en) * | 1981-04-20 | 1983-03-22 | Ashland Oil, Inc. | Immobilization of vanadia deposited on catalytic materials during carbo-metallic oil conversion |
| US4394349A (en) * | 1981-07-06 | 1983-07-19 | Standard Oil Company (Indiana) | Apparatus for the fluidized catalytic cracking of hydrocarbon feedstock |
| US4406776A (en) * | 1982-08-25 | 1983-09-27 | Uop Inc. | Fluidized catalytic cracking process and apparatus |
| US4721603A (en) * | 1983-06-13 | 1988-01-26 | Chevron Research Company | Separation of reacted hydrocarbons and catalyst in fluidized catalytic cracking |
| US4786622A (en) * | 1984-01-09 | 1988-11-22 | Ashland Oil, Inc. | Regeneration of fluid solid particles and separation of solid particles from combustion product flue gases |
| US5055177A (en) * | 1984-05-21 | 1991-10-08 | Mobil Oil Corporation | Closed cyclone FCC catalyst separation method and apparatus |
| US4737346A (en) * | 1984-05-21 | 1988-04-12 | Mobil Oil Corporation | Closed cyclone FCC catalyst separation with stripping gas injection and direct steam injection |
| US4869880A (en) * | 1984-06-08 | 1989-09-26 | Ashland Oil, Inc. | Apparatus for the separation of solid particulates from a gaseous effluent |
| US4792437A (en) * | 1984-06-08 | 1988-12-20 | Ashland Oil, Inc. | Apparatus for the separation of solid particulates from a gaseous effluent |
| US4701307A (en) * | 1984-09-19 | 1987-10-20 | Ashland Oil, Inc. | Vented riser |
| US4572780A (en) * | 1984-10-22 | 1986-02-25 | Mobil Oil Corporation | Multistage stripper for FCC unit with catalyst separation by spinning |
| US4678642A (en) * | 1985-01-10 | 1987-07-07 | Ashland Oil, Inc. | Ballistic separation of particles in a progressive flow reactor |
| US4714541A (en) * | 1985-11-22 | 1987-12-22 | Mobil Oil Corporation | Method and apparatus for improving cyclone efficiency |
| US5141625A (en) * | 1989-12-27 | 1992-08-25 | Uop | Second stage stripping and lift gas supply |
| US5266187A (en) * | 1992-05-19 | 1993-11-30 | Amoco Corporation | Method for catalytic cracking with post-cyclone inertial separator |
-
1991
- 1991-11-13 US US07/790,924 patent/US5290430A/en not_active Expired - Fee Related
-
1994
- 1994-02-21 EP EP94301210A patent/EP0668341B1/en not_active Expired - Lifetime
- 1994-02-21 ES ES94301210T patent/ES2130352T3/es not_active Expired - Lifetime
- 1994-02-21 AT AT94301210T patent/ATE179205T1/de not_active IP Right Cessation
- 1994-02-21 AU AU55283/94A patent/AU5528394A/en not_active Abandoned
- 1994-02-21 DE DE69418024T patent/DE69418024T2/de not_active Expired - Fee Related
- 1994-02-22 CA CA002116163A patent/CA2116163A1/en not_active Abandoned
- 1994-02-22 ZA ZA941208A patent/ZA941208B/xx unknown
- 1994-02-24 US US08/201,495 patent/US5417931A/en not_active Expired - Fee Related
- 1994-02-28 RU RU9494006801A patent/RU2079541C1/ru active
- 1994-02-28 CN CN94102538A patent/CN1062890C/zh not_active Expired - Fee Related
-
1999
- 1999-05-06 GR GR990401224T patent/GR3030140T3/el unknown
Also Published As
| Publication number | Publication date |
|---|---|
| ATE179205T1 (de) | 1999-05-15 |
| DE69418024T2 (de) | 1999-08-12 |
| CN1107502A (zh) | 1995-08-30 |
| DE69418024D1 (de) | 1999-05-27 |
| US5417931A (en) | 1995-05-23 |
| EP0668341B1 (en) | 1999-04-21 |
| US5290430A (en) | 1994-03-01 |
| ZA941208B (en) | 1994-11-30 |
| AU5528394A (en) | 1995-09-21 |
| CA2116163A1 (en) | 1995-08-23 |
| RU2079541C1 (ru) | 1997-05-20 |
| GR3030140T3 (en) | 1999-08-31 |
| CN1062890C (zh) | 2001-03-07 |
| EP0668341A1 (en) | 1995-08-23 |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| FG2A | Definitive protection |
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