MXPA03009299A - Recuperacion del catalizador con un pozo central. - Google Patents
Recuperacion del catalizador con un pozo central.Info
- Publication number
- MXPA03009299A MXPA03009299A MXPA03009299A MXPA03009299A MXPA03009299A MX PA03009299 A MXPA03009299 A MX PA03009299A MX PA03009299 A MXPA03009299 A MX PA03009299A MX PA03009299 A MXPA03009299 A MX PA03009299A MX PA03009299 A MXPA03009299 A MX PA03009299A
- Authority
- MX
- Mexico
- Prior art keywords
- catalyst
- centerwell
- annulus
- introduces
- regenerator
- 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
- 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
- B01J8/1827—Feeding of the fluidising gas the fluidising gas being a reactant
-
- 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
-
- 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
- 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
- B01J2219/00002—Chemical plants
- B01J2219/00018—Construction aspects
- B01J2219/00024—Revamping, retrofitting or modernisation of existing plants
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Engineering & Computer Science (AREA)
- Combustion & Propulsion (AREA)
- Oil, Petroleum & Natural Gas (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)
Abstract
Un regenerador de catalizador para regenerar un catalizador de FCC ligero gastado y calentar el catalizador para suministrar calor a un reactor de FCC. El regenerador tiene salidas de descarga para catalizar y el gas libre y una valvula para introducir el catalizador gastado a traves de una porcion de trre hidraulica central. El regenerador aloja un lecho catalizador de fase densa. Un pozo central recibe un extremo inferior de la porcion de torre hidraulica y define una zona anular entre los mismos. El catalizador gastado se introduce a traves de la porcion de torre hidraulica dentro de la zona anular. Un distribuidor de combustible introduce el combustible dentro del pozo central para mezclarse con el catalizador en la zona anular. Un distribuidor de fluidizacion introduce gas de fluidizacion dentro del pozo central para fluidizar el catalizador en la zona anular. Una ranura radial en el pozo central. introduce el catalizador y la mezcla de combustible desde la zona anular por debajo de la superficie superior del lecho de fase densa. Un distribuidor de aire localizado por debajo de la ranura radial introduce el aire de combustion dentro del lecho de fase densa.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US10/065,376 US7153479B2 (en) | 2002-10-10 | 2002-10-10 | Catalyst regenerator with a centerwell |
Publications (1)
Publication Number | Publication Date |
---|---|
MXPA03009299A true MXPA03009299A (es) | 2004-04-28 |
Family
ID=32028530
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
MXPA03009299A MXPA03009299A (es) | 2002-10-10 | 2003-10-10 | Recuperacion del catalizador con un pozo central. |
Country Status (10)
Country | Link |
---|---|
US (2) | US7153479B2 (es) |
EP (1) | EP1408100B1 (es) |
JP (1) | JP4284146B2 (es) |
CN (1) | CN100509715C (es) |
CA (1) | CA2437649C (es) |
DE (1) | DE60326911D1 (es) |
ES (1) | ES2321077T3 (es) |
MX (1) | MXPA03009299A (es) |
RU (1) | RU2326930C2 (es) |
SG (1) | SG128445A1 (es) |
Families Citing this family (59)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
TW200734055A (en) * | 2005-12-20 | 2007-09-16 | Shell Int Research | A process and apparatus for the regeneration of spent FCC catalyst |
US7491315B2 (en) * | 2006-08-11 | 2009-02-17 | Kellogg Brown & Root Llc | Dual riser FCC reactor process with light and mixed light/heavy feeds |
US7585470B2 (en) * | 2006-12-21 | 2009-09-08 | Uop Llc | Apparatus for mixing in fluidized beds |
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 |
US8608942B2 (en) | 2007-03-15 | 2013-12-17 | Kellogg Brown & Root Llc | Systems and methods for residue upgrading |
US7883618B2 (en) * | 2008-02-28 | 2011-02-08 | Kellogg Brown & Root Llc | Recycle of olefinic naphthas by removing aromatics |
WO2011079355A1 (pt) | 2009-12-28 | 2011-07-07 | Petróleo Brasileiro S.A.- Petrobras | Combustor de alta eficiência e processo de craqueamento catalítico fluidizado orientado para a produção de olefinas leves |
CN102188939B (zh) * | 2010-03-18 | 2013-09-04 | 中国石油化工股份有限公司 | 一种低炭催化剂的流化床再生设备及其再生方法 |
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 |
US8383052B2 (en) * | 2010-04-16 | 2013-02-26 | Kellogg Brown & Root Llc | System for a heat balanced FCC forlight hydrocarbon feeds |
US8415264B2 (en) * | 2010-04-30 | 2013-04-09 | Uop Llc | Process for regenerating catalyst in a fluid catalytic cracking unit |
US8506795B2 (en) * | 2010-06-04 | 2013-08-13 | Uop Llc | Process for fluid catalytic cracking |
US8728302B2 (en) | 2010-06-25 | 2014-05-20 | Exxonmobil Research And Engineering Company | Spent catalyst riser distributor |
US8563455B2 (en) | 2010-09-30 | 2013-10-22 | Uop Llc | Process for regenerating catalyst |
US8535610B2 (en) | 2010-09-30 | 2013-09-17 | Uop Llc | Apparatus for regenerating catalyst |
US8889942B2 (en) | 2010-12-23 | 2014-11-18 | Kellogg Brown & Root Llc | Integrated light olefin separation/cracking process |
US8815082B2 (en) | 2011-12-12 | 2014-08-26 | Uop Llc | Process and apparatus for mixing two streams of catalyst |
US8747759B2 (en) | 2011-12-12 | 2014-06-10 | Uop Llc | Process and apparatus for mixing two streams of catalyst |
US8747758B2 (en) | 2011-12-12 | 2014-06-10 | Uop Llc | Process and apparatus for mixing two streams of catalyst |
US8747657B2 (en) | 2011-12-12 | 2014-06-10 | Uop Llc | Process and apparatus for mixing two streams of catalyst |
US9238600B2 (en) * | 2011-12-14 | 2016-01-19 | Uop Llc | Dual riser catalytic cracker for increased light olefin yield |
US8932452B2 (en) | 2012-01-11 | 2015-01-13 | Cameron International Corporation | Method for separating entrained catalyst and catalyst fines from slurry oil |
US9446364B2 (en) | 2012-02-23 | 2016-09-20 | Kellogg Brown & Root Llc | Surge drum mixing system |
US8815166B2 (en) | 2012-03-20 | 2014-08-26 | Uop Llc | Process and apparatus for mixing two streams of catalyst |
US8916099B2 (en) | 2012-03-20 | 2014-12-23 | Uop Llc | Process and apparatus for mixing two streams of catalyst |
US9375695B2 (en) | 2012-03-20 | 2016-06-28 | Uop Llc | Process and apparatus for mixing two streams of catalyst |
US8936758B2 (en) | 2012-03-20 | 2015-01-20 | Uop Llc | Process and apparatus for mixing two streams of catalyst |
US9023286B2 (en) * | 2012-03-23 | 2015-05-05 | Uop Llc | MTO regenerator multi-pass grids |
CN103571530B (zh) * | 2012-08-02 | 2015-11-18 | 中国石油天然气股份有限公司 | 蜡油催化裂解制备低碳烯烃的方法 |
US9745519B2 (en) | 2012-08-22 | 2017-08-29 | Kellogg Brown & Root Llc | FCC process using a modified catalyst |
US9134064B2 (en) * | 2013-10-04 | 2015-09-15 | Aggreko, Llc | Process vessel cooldown apparatus and method |
US9205394B2 (en) | 2014-03-31 | 2015-12-08 | Uop Llc | Process and apparatus for distributing fluidizing gas to an FCC riser |
US9376633B2 (en) | 2014-03-31 | 2016-06-28 | Uop Llc | Process and apparatus for distributing fluidizing gas to an FCC riser |
CN105521833B (zh) * | 2014-09-30 | 2017-12-22 | 中国石油化工股份有限公司 | 一种催化裂化催化剂再生方法和设备 |
KR101652598B1 (ko) * | 2014-12-22 | 2016-08-31 | 주식회사 효성 | 촉매 재생 장치 |
US20160312127A1 (en) * | 2015-04-22 | 2016-10-27 | Uop Llc | Processes for minimizing catalyst fines in a regenerator flue gas stream |
KR101771163B1 (ko) * | 2016-02-01 | 2017-08-24 | 한국기계연구원 | 촉매 재생기와 그 재생 방법 |
CN108698007B (zh) * | 2016-02-29 | 2022-02-08 | 环球油品公司 | 流化废催化剂的方法 |
WO2018125366A1 (en) * | 2016-12-27 | 2018-07-05 | Uop Llc | Fcc counter-current regenerator with a regenerator riser |
CN110234434A (zh) * | 2016-12-27 | 2019-09-13 | 环球油品有限责任公司 | 具有再生器提升管的fcc逆流再生器 |
US10870802B2 (en) | 2017-05-31 | 2020-12-22 | Saudi Arabian Oil Company | High-severity fluidized catalytic cracking systems and processes having partial catalyst recycle |
US10889768B2 (en) | 2018-01-25 | 2021-01-12 | Saudi Arabian Oil Company | High severity fluidized catalytic cracking systems and processes for producing olefins from petroleum feeds |
US11279885B2 (en) | 2018-05-10 | 2022-03-22 | Korea Institute Of Machinery & Materials | Catalyst regenerator |
KR102088413B1 (ko) * | 2018-05-10 | 2020-03-12 | 한국기계연구원 | 촉매 재생기 |
KR102232804B1 (ko) * | 2018-12-21 | 2021-03-26 | 한국기계연구원 | 유동층 촉매 재생기 |
RU185080U1 (ru) * | 2018-07-03 | 2018-11-21 | Общество с ограниченной ответственностью "Институт по проектированию предприятий нефтеперерабатывающей и нефтехимической промышленности" (ООО "Ленгипронефтехим") | Установка для регенерации катализатора риформинга |
CN109647544B (zh) * | 2019-01-03 | 2021-06-11 | 飞潮(无锡)过滤技术有限公司 | 一种干湿法复合再生回收废旧铜铋催化剂的工艺 |
CN111715306B (zh) * | 2019-03-18 | 2023-03-21 | 江苏博颂化工科技有限公司 | 一种烷烃脱氢催化剂再生装置 |
US10947458B1 (en) * | 2020-03-18 | 2021-03-16 | Chevron U.S.A. Inc. | Upgrading of renewable feedstocks with spent equilibrium catalyst |
US11242493B1 (en) | 2020-09-01 | 2022-02-08 | Saudi Arabian Oil Company | Methods for processing crude oils to form light olefins |
US11434432B2 (en) | 2020-09-01 | 2022-09-06 | Saudi Arabian Oil Company | Processes for producing petrochemical products that utilize fluid catalytic cracking of a greater boiling point fraction with steam |
US11505754B2 (en) | 2020-09-01 | 2022-11-22 | Saudi Arabian Oil Company | Processes for producing petrochemical products from atmospheric residues |
US11352575B2 (en) | 2020-09-01 | 2022-06-07 | Saudi Arabian Oil Company | Processes for producing petrochemical products that utilize hydrotreating of cycle oil |
US11332680B2 (en) | 2020-09-01 | 2022-05-17 | Saudi Arabian Oil Company | Processes for producing petrochemical products that utilize fluid catalytic cracking of lesser and greater boiling point fractions with steam |
US11230672B1 (en) | 2020-09-01 | 2022-01-25 | Saudi Arabian Oil Company | Processes for producing petrochemical products that utilize fluid catalytic cracking |
US11230673B1 (en) | 2020-09-01 | 2022-01-25 | Saudi Arabian Oil Company | Processes for producing petrochemical products that utilize fluid catalytic cracking of a lesser boiling point fraction with steam |
KR102573887B1 (ko) | 2021-09-10 | 2023-09-04 | 한국화학연구원 | 전기 가열로를 활용한 순환 유동층 반응기 |
CN116297066B (zh) * | 2023-03-22 | 2024-04-05 | 新疆新伊碳能环保科技股份有限公司 | 一种带有烟气过滤功能的锅炉烟气检测装置 |
Family Cites Families (19)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3661800A (en) * | 1970-06-17 | 1972-05-09 | Pullman Inc | Staged fluidized solids contacting process in oxidation regeneration of catalysts |
DE2707478A1 (de) * | 1976-03-01 | 1977-09-08 | Pullman Inc | Verfahren und vorrichtung zur regenerierung von crack-katalysatoren |
US4062759A (en) * | 1976-05-07 | 1977-12-13 | Texaco Inc. | Fluidized catalytic cracking regeneration process |
US4615992A (en) * | 1985-04-02 | 1986-10-07 | Air Products And Chemicals, Inc. | Catalyst regeneration process with improved catalyst distribution in a fluidized bed |
US4859424A (en) | 1987-11-02 | 1989-08-22 | Uop | Conversion of stacked FCC unit |
US5167795A (en) * | 1988-01-28 | 1992-12-01 | Stone & Webster Engineering Corp. | Process for the production of olefins and aromatics |
US5271826A (en) * | 1988-03-03 | 1993-12-21 | Mobil Oil Corporation | Catalytic cracking of coke producing hydrocarbons |
US5043522A (en) * | 1989-04-25 | 1991-08-27 | Arco Chemical Technology, Inc. | Production of olefins from a mixture of Cu+ olefins and paraffins |
US5171921A (en) * | 1991-04-26 | 1992-12-15 | Arco Chemical Technology, L.P. | Production of olefins |
WO1993000674A1 (en) | 1991-06-25 | 1993-01-07 | Mobil Oil Corporation | A process for stripping and regenerating fluidized catalytic cracking catalyst |
US5198397A (en) * | 1991-11-25 | 1993-03-30 | Mobil Oil Corporation | Two-stage fluid bed regeneration of catalyst with shared dilute phase |
US5220093A (en) * | 1992-04-03 | 1993-06-15 | Stone & Webster Engineering Corporation | Process for production of olefins from mixtures of light paraffins |
CN1089641A (zh) * | 1992-08-20 | 1994-07-20 | 史东及韦伯斯特工程公司 | 含高和低康拉逊残炭组分的富石蜡原料的催化裂化方法 |
US5346613A (en) * | 1993-09-24 | 1994-09-13 | Uop | FCC process with total catalyst blending |
US5565089A (en) * | 1994-09-30 | 1996-10-15 | The Boc Group, Inc. | Process for decoking catalysts |
US5965012A (en) * | 1997-12-05 | 1999-10-12 | Uop Llc | FCC process with short primary contacting and controlled secondary contacting |
US6118035A (en) * | 1998-05-05 | 2000-09-12 | Exxon Research And Engineering Co. | Process for selectively producing light olefins in a fluid catalytic cracking process from a naphtha/steam feed |
US6113776A (en) * | 1998-06-08 | 2000-09-05 | Uop Llc | FCC process with high temperature cracking zone |
US6797239B1 (en) * | 2000-11-22 | 2004-09-28 | Shell Oil Company | Spent catalyst distributor |
-
2002
- 2002-10-10 US US10/065,376 patent/US7153479B2/en not_active Expired - Lifetime
-
2003
- 2003-08-20 CA CA2437649A patent/CA2437649C/en not_active Expired - Lifetime
- 2003-08-28 SG SG200304882A patent/SG128445A1/en unknown
- 2003-09-25 EP EP03021731A patent/EP1408100B1/en not_active Expired - Lifetime
- 2003-09-25 ES ES03021731T patent/ES2321077T3/es not_active Expired - Lifetime
- 2003-09-25 DE DE60326911T patent/DE60326911D1/de not_active Expired - Lifetime
- 2003-10-09 JP JP2003350225A patent/JP4284146B2/ja not_active Expired - Lifetime
- 2003-10-09 RU RU2003129990/04A patent/RU2326930C2/ru active
- 2003-10-10 CN CNB2003101006346A patent/CN100509715C/zh not_active Expired - Lifetime
- 2003-10-10 MX MXPA03009299A patent/MXPA03009299A/es active IP Right Grant
-
2006
- 2006-11-15 US US11/599,763 patent/US7435331B2/en not_active Expired - Lifetime
Also Published As
Publication number | Publication date |
---|---|
US7435331B2 (en) | 2008-10-14 |
RU2326930C2 (ru) | 2008-06-20 |
JP4284146B2 (ja) | 2009-06-24 |
US7153479B2 (en) | 2006-12-26 |
JP2004131735A (ja) | 2004-04-30 |
EP1408100B1 (en) | 2009-04-01 |
CN100509715C (zh) | 2009-07-08 |
CA2437649A1 (en) | 2004-04-10 |
SG128445A1 (en) | 2007-01-30 |
CN1496970A (zh) | 2004-05-19 |
US20070051666A1 (en) | 2007-03-08 |
US20040069681A1 (en) | 2004-04-15 |
EP1408100A1 (en) | 2004-04-14 |
ES2321077T3 (es) | 2009-06-02 |
RU2003129990A (ru) | 2005-04-10 |
DE60326911D1 (de) | 2009-05-14 |
CA2437649C (en) | 2011-07-26 |
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FG | Grant or registration |