ATE395395T1 - Reaktor mit mehreren steigrohren und mit konsolidiertem transport - Google Patents

Reaktor mit mehreren steigrohren und mit konsolidiertem transport

Info

Publication number
ATE395395T1
ATE395395T1 AT03798661T AT03798661T ATE395395T1 AT E395395 T1 ATE395395 T1 AT E395395T1 AT 03798661 T AT03798661 T AT 03798661T AT 03798661 T AT03798661 T AT 03798661T AT E395395 T1 ATE395395 T1 AT E395395T1
Authority
AT
Austria
Prior art keywords
catalyst
separation zone
riser reactors
reactor
riser
Prior art date
Application number
AT03798661T
Other languages
English (en)
Inventor
Walter Brookhart
Original Assignee
Exxonmobil Chem Patents Inc
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Exxonmobil Chem Patents Inc filed Critical Exxonmobil Chem Patents Inc
Application granted granted Critical
Publication of ATE395395T1 publication Critical patent/ATE395395T1/de

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10GCRACKING 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
    • C10G2/00Production of liquid hydrocarbon mixtures of undefined composition from oxides of carbon
    • C10G2/30Production of liquid hydrocarbon mixtures of undefined composition from oxides of carbon from carbon monoxide with hydrogen
    • C10G2/32Production of liquid hydrocarbon mixtures of undefined composition from oxides of carbon from carbon monoxide with hydrogen with the use of catalysts
    • C10G2/34Apparatus, reactors
    • C10G2/342Apparatus, reactors with moving solid catalysts
    • C10G2/344Apparatus, reactors with moving solid catalysts according to the "fluidised-bed" technique
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J19/00Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J19/26Nozzle-type reactors, i.e. the distribution of the initial reactants within the reactor is effected by their introduction or injection through nozzles
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J8/00Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/005Separating solid material from the gas/liquid stream
    • B01J8/0055Separating solid material from the gas/liquid stream using cyclones
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J8/00Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/18Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles
    • B01J8/24Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles according to "fluidised-bed" technique
    • B01J8/26Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles according to "fluidised-bed" technique with two or more fluidised beds, e.g. reactor and regeneration installations
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J8/00Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/18Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles
    • B01J8/24Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles according to "fluidised-bed" technique
    • B01J8/38Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles according to "fluidised-bed" technique with fluidised bed containing a rotatable device or being subject to rotation or to a circulatory movement, i.e. leaving a vessel and subsequently re-entering it
    • B01J8/384Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles according to "fluidised-bed" technique with fluidised bed containing a rotatable device or being subject to rotation or to a circulatory movement, i.e. leaving a vessel and subsequently re-entering it being subject to a circulatory movement only
    • B01J8/388Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles according to "fluidised-bed" technique with fluidised bed containing a rotatable device or being subject to rotation or to a circulatory movement, i.e. leaving a vessel and subsequently re-entering it being subject to a circulatory movement only externally, i.e. the particles leaving the vessel and subsequently re-entering it
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10GCRACKING 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
    • C10G3/00Production of liquid hydrocarbon mixtures from oxygen-containing organic materials, e.g. fatty oils, fatty acids
    • C10G3/42Catalytic treatment
    • C10G3/44Catalytic treatment characterised by the catalyst used
    • C10G3/48Catalytic treatment characterised by the catalyst used further characterised by the catalyst support
    • C10G3/49Catalytic treatment characterised by the catalyst used further characterised by the catalyst support containing crystalline aluminosilicates, e.g. molecular sieves
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10GCRACKING 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
    • C10G3/00Production of liquid hydrocarbon mixtures from oxygen-containing organic materials, e.g. fatty oils, fatty acids
    • C10G3/54Production of liquid hydrocarbon mixtures from oxygen-containing organic materials, e.g. fatty oils, fatty acids characterised by the catalytic bed
    • C10G3/55Production of liquid hydrocarbon mixtures from oxygen-containing organic materials, e.g. fatty oils, fatty acids characterised by the catalytic bed with moving solid particles, e.g. moving beds
    • C10G3/57Production of liquid hydrocarbon mixtures from oxygen-containing organic materials, e.g. fatty oils, fatty acids characterised by the catalytic bed with moving solid particles, e.g. moving beds according to the fluidised bed technique
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10GCRACKING 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
    • C10G3/00Production of liquid hydrocarbon mixtures from oxygen-containing organic materials, e.g. fatty oils, fatty acids
    • C10G3/62Catalyst regeneration
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2219/00Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/00002Chemical plants
    • B01J2219/00027Process aspects
    • B01J2219/00038Processes in parallel
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10GCRACKING 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
    • C10G2300/00Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
    • C10G2300/40Characteristics of the process deviating from typical ways of processing
    • C10G2300/4093Catalyst stripping
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10GCRACKING 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
    • C10G2400/00Products obtained by processes covered by groups C10G9/00 - C10G69/14
    • C10G2400/20C2-C4 olefins
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P30/00Technologies relating to oil refining and petrochemical industry
    • Y02P30/20Technologies relating to oil refining and petrochemical industry using bio-feedstock

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Organic Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • General Chemical & Material Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Crystallography & Structural Chemistry (AREA)
  • Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
  • Catalysts (AREA)
AT03798661T 2002-09-24 2003-05-30 Reaktor mit mehreren steigrohren und mit konsolidiertem transport ATE395395T1 (de)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US10/253,106 US7122160B2 (en) 2002-09-24 2002-09-24 Reactor with multiple risers and consolidated transport

Publications (1)

Publication Number Publication Date
ATE395395T1 true ATE395395T1 (de) 2008-05-15

Family

ID=31993096

Family Applications (1)

Application Number Title Priority Date Filing Date
AT03798661T ATE395395T1 (de) 2002-09-24 2003-05-30 Reaktor mit mehreren steigrohren und mit konsolidiertem transport

Country Status (8)

Country Link
US (1) US7122160B2 (de)
EP (1) EP1565541B1 (de)
AT (1) ATE395395T1 (de)
AU (1) AU2003232464A1 (de)
DE (1) DE60321036D1 (de)
EA (1) EA008696B1 (de)
ES (1) ES2305562T3 (de)
WO (1) WO2004029178A1 (de)

Families Citing this family (31)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US7169293B2 (en) * 1999-08-20 2007-01-30 Uop Llc Controllable space velocity reactor and process
US6869521B2 (en) * 2002-04-18 2005-03-22 Uop Llc Process and apparatus for upgrading FCC product with additional reactor with thorough mixing
ES2220713T3 (es) 2000-02-02 2004-12-16 Dow Global Technologies Inc. Procedimiento integrado para producir un compuesto aromatico sustituido con alquenilo.
US20040064007A1 (en) * 2002-09-30 2004-04-01 Beech James H. Method and system for regenerating catalyst from a plurality of hydrocarbon conversion apparatuses
US7083762B2 (en) * 2002-10-18 2006-08-01 Exxonmobil Chemical Patents Inc. Multiple riser reactor with centralized catalyst return
RU2508282C2 (ru) 2004-02-09 2014-02-27 Дзе Дау Кемикал Компани Способ получения дегидрированных углеводородных соединений
US7582203B2 (en) 2004-08-10 2009-09-01 Shell Oil Company Hydrocarbon cracking process for converting gas oil preferentially to middle distillate and lower olefins
JP2008510032A (ja) 2004-08-10 2008-04-03 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 炭化水素供給原料から中間留分生成物及び低級オレフィンを製造する方法及び装置
US7439414B2 (en) * 2005-10-13 2008-10-21 Uop Llc Oxygenate conversion catalyst processing
CN101679880B (zh) * 2007-04-13 2013-05-22 国际壳牌研究有限公司 用于由烃原料生产中间馏分油产物和低级烯烃的系统和方法
EP2142619A1 (de) * 2007-04-30 2010-01-13 Shell Internationale Research Maatschappij B.V. Systeme und verfahren zur herstellung eines mitteldestillatprodukts und niederen olefinen aus einem kohlenwasserstoffeinsatzstoff
CN101952394B (zh) * 2007-10-10 2013-09-11 国际壳牌研究有限公司 由烃原料制备中间馏分产物和低级烯烃的系统和方法
DK2340295T3 (en) * 2008-10-27 2017-05-15 Kior Inc METHOD OF BIOMASS CONVERSION
US8137632B2 (en) * 2008-11-04 2012-03-20 Kior, Inc. Biomass conversion process
US8747767B2 (en) 2008-12-22 2014-06-10 Shell Oil Company Catalyst return apparatus, and process for reacting a feedstock
EP2408558B1 (de) * 2009-03-19 2017-06-28 Dow Global Technologies LLC Dehydrierungsverfahren und dessen katalysator
WO2015081494A1 (zh) * 2013-12-03 2015-06-11 中国科学院大连化学物理研究所 一种用于甲醇和/或二甲醚制低碳烯烃的反应装置
WO2017218187A1 (en) * 2016-06-17 2017-12-21 Dow Global Technologies Llc System components of fluid catalytic reactor systems
AR111124A1 (es) * 2017-03-13 2019-06-05 Dow Global Technologies Llc Métodos para fabricar olefinas ligeras a partir de corrientes de alimentación diferentes
BR112022017379A2 (pt) 2020-03-06 2022-10-18 Exxonmobil Chemical Patents Inc Processos para melhorar alcanos e hidrocarbonetos aromáticos de alquila
US11760703B2 (en) 2020-03-06 2023-09-19 Exxonmobil Chemical Patents Inc. Processes for upgrading alkanes and alkyl aromatic hydrocarbons
BR112022017782A2 (pt) 2020-03-06 2022-10-25 Exxonmobil Chemical Patents Inc Processos para melhoria de qualidade de alcanos e hidrocarbonetos aromáticos de alquila
US11859136B2 (en) 2020-03-06 2024-01-02 Exxonmobil Chemical Patents Inc. Processes for upgrading alkanes and alkyl aromatic hydrocarbons
KR20220164584A (ko) 2020-05-08 2022-12-13 엑손모빌 케미칼 패턴츠 인코포레이티드 알칸 및 알킬 방향족 탄화수소의 업그레이드 방법 및 시스템
EP4347117A1 (de) 2021-06-02 2024-04-10 ExxonMobil Chemical Patents Inc. Verfahren zur regenerierung von katalysatoren und zur aufwertung von alkanen und/oder alkylaromatischen kohlenwasserstoffen
US20240269653A1 (en) 2021-07-28 2024-08-15 Exxonmobil Chemical Patents Inc. Catalyst Compositions and Processes for Making and Using Same
WO2023018527A1 (en) 2021-08-11 2023-02-16 Exxonmobil Chemical Patents Inc. Processes for dehydrogenating alkanes and alkyl aromatic hydrocarbons
CN117813160A (zh) 2021-08-11 2024-04-02 埃克森美孚化学专利公司 再生催化剂和提质烷烃和/或烷基芳族烃的方法
KR20240034227A (ko) 2021-08-13 2024-03-13 엑손모빌 케미칼 패턴츠 인코포레이티드 알칸 및 알킬 방향족 탄화수소를 탈수소화하는 방법
CN113750911B (zh) * 2021-09-10 2022-10-04 中国科学院过程工程研究所 一种多通道提升管反应装置及其应用
KR20240096780A (ko) 2021-12-06 2024-06-26 엑손모빌 케미칼 패턴츠 인코포레이티드 촉매 조성물 및 이의 제조 및 사용 방법

Family Cites Families (75)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1421640A (en) 1919-07-11 1922-07-04 Us Ind Alcohol Co Process of producing ethylene
US2378236A (en) 1944-05-02 1945-06-12 Air Reduction Production of ethylene
US2472377A (en) 1945-01-31 1949-06-07 Hydrocarbon Research Inc Process for hydrocarbon synthesis
US2768127A (en) 1951-05-17 1956-10-23 Exxon Research Engineering Co Improved residual oil conversion process for the production of chemicals
US2847364A (en) 1952-09-12 1958-08-12 Gulf Research Development Co Process for conversion of hydrocarbons and for transport of solid particles
US4076698A (en) 1956-03-01 1978-02-28 E. I. Du Pont De Nemours And Company Hydrocarbon interpolymer compositions
IT609922A (de) 1959-06-06
US3305538A (en) 1961-11-22 1967-02-21 Montedison Spa Polymerization process
US3205275A (en) 1962-02-26 1965-09-07 Phillips Petroleum Co Solid catalyst contacting process and apparatus therefor
US3364190A (en) 1964-04-27 1968-01-16 Standard Oil Co Process for polymerizing propylene to syndiotactic polypropylene
CA849081A (en) 1967-03-02 1970-08-11 Du Pont Of Canada Limited PRODUCTION OF ETHYLENE/.alpha.-OLEFIN COPOLYMERS OF IMPROVED PHYSICAL PROPERTIES
GB1255886A (en) 1969-04-23 1971-12-01 Mitsui Shipbuilding Eng Process and apparatus for preparing lower olefins
US3959117A (en) 1973-03-26 1976-05-25 Texaco Inc. Fluid catalytic cracking of hydrocarbons
US4138440A (en) 1974-08-14 1979-02-06 Mobil Oil Corporation Conversion of liquid alcohols and ethers with a fluid mass of ZSM-5 type catalyst
DE2524540C2 (de) 1975-06-03 1986-04-24 Metallgesellschaft Ag, 6000 Frankfurt Verfahren zur Durchführung endothermer Prozesse
US4134926A (en) 1977-04-18 1979-01-16 The Lummus Company Production of ethylene from ethanol
US4302565A (en) 1978-03-31 1981-11-24 Union Carbide Corporation Impregnated polymerization catalyst, process for preparing, and use for ethylene copolymerization
US4229608A (en) 1978-12-18 1980-10-21 Mobil Oil Corporation Heat balanced cyclic process for manufacture of light olefins
US4243691A (en) 1979-05-18 1981-01-06 The Procter & Gamble Company Sodium-free salt substitute
US4379123A (en) 1979-10-30 1983-04-05 Mobil Oil Corporation Fluid catalyst conversion of alcohols and oxygenates to hydrocarbons
DE3377139D1 (en) 1982-06-15 1988-07-28 Mobil Oil Corp Process for the conversion of alcohols into petrochemicals
US4440871A (en) 1982-07-26 1984-04-03 Union Carbide Corporation Crystalline silicoaluminophosphates
US4677242A (en) 1982-10-04 1987-06-30 Union Carbide Corporation Production of light olefins
US4499327A (en) 1982-10-04 1985-02-12 Union Carbide Corporation Production of light olefins
US4677243A (en) 1982-10-04 1987-06-30 Union Carbide Corporation Production of light olefins from aliphatic hetero compounds
JPS6088222A (ja) 1983-10-21 1985-05-18 Daido Metal Kogyo Kk 複合摺動体
CA1223895A (en) 1984-03-05 1987-07-07 Hugo I. De Lasa Pseudodiabatic reactor for exothermal catalytic conversions
GB2159431B (en) 1984-05-29 1988-04-27 Shell Int Research Reactor for non-isothermic reactions and process for the preparation of hydrocarbons using such a reactor
US4590320A (en) 1984-08-31 1986-05-20 Mobil Oil Corporation Conversion of methanol to olefins in a tubular reactor with light olefin co-feeding
US4547616A (en) 1984-12-28 1985-10-15 Mobil Oil Corporation Conversion of oxygenates to lower olefins in a turbulent fluidized catalyst bed
US4659685A (en) 1986-03-17 1987-04-21 The Dow Chemical Company Heterogeneous organometallic catalysts containing a supported titanium compound and at least one other supported organometallic compound
US4752651A (en) 1986-06-16 1988-06-21 Union Carbide Corporation Production of light olefins
US4873390A (en) 1987-07-07 1989-10-10 Uop Chemical conversion process
US4973792A (en) 1987-07-07 1990-11-27 Uop Chemical conversion process
US4814541A (en) 1987-07-07 1989-03-21 Uop Chemical conversion process
US4861938A (en) 1987-07-07 1989-08-29 Uop Chemical conversion process
US5271905A (en) 1990-04-27 1993-12-21 Mobil Oil Corporation Apparatus for multi-stage fast fluidized bed regeneration of catalyst
US5157193A (en) 1991-01-15 1992-10-20 Energia Andina Ltd. Preparing lower alkenes from methanol
US5095163A (en) 1991-02-28 1992-03-10 Uop Methanol conversion process using SAPO catalysts
US5126308A (en) 1991-11-13 1992-06-30 Uop Metal aluminophosphate catalyst for converting methanol to light olefins
US5191141A (en) 1991-11-13 1993-03-02 Uop Process for converting methanol to olefins using an improved metal aluminophosphate catalyst
AU667114B2 (en) 1992-05-27 1996-03-07 Exxon Chemical Patents Inc. Use of acid extracted molecular sieve catalysts in oxygenate conversion
US5278345A (en) 1992-05-27 1994-01-11 Exxon Chemical Patents Inc. Use of ECR-1, mazmorite and ECR-18 in the conversion of oxygenates to hydrocarbons
US5343830A (en) 1993-03-25 1994-09-06 The Babcock & Wilcox Company Circulating fluidized bed reactor with internal primary particle separation and return
US5714662A (en) 1995-08-10 1998-02-03 Uop Process for producing light olefins from crude methanol
US5962762A (en) 1995-12-13 1999-10-05 Sun; Hsian-Ning Use of transition metal containing small pore molecular sieve catalysts in oxygenate conversion
US5714663A (en) 1996-02-23 1998-02-03 Exxon Research And Engineering Company Process for obtaining significant olefin yields from residua feedstocks
US6040264A (en) 1996-04-04 2000-03-21 Exxon Chemical Patents Inc. Use of alkaline earth metal containing small pore non-zeolitic molecular sieve catalysts in oxygenate conversion
US5972203A (en) 1996-05-29 1999-10-26 Exxon Chemical Patents Inc. Hydrocarbon conversion catalyst and its use
US5811621A (en) 1996-08-09 1998-09-22 Van Dijk; Christiaan P. Process for recovering ethylene from an olefin stream produced by a methanol to olefin reaction
FI101156B (fi) 1996-08-30 1998-04-30 Fortum Oil Oy Kiertomassareaktoriin perustuva menetelmä ja laite hiilivetyjen konver toimiseksi
US5723094A (en) 1996-10-29 1998-03-03 Arco Chemical Technology, L.P. Reactor for chemical reactions
AT405648B (de) 1996-11-22 1999-10-25 Oemv Ag Vorrichtung zum katalytischen umsetzen von organischen stubstanzen mit einem fliessbettreaktor
US5904880A (en) 1996-12-31 1999-05-18 Exxon Chemical Patents Inc. One step conversion of methanol to hydrogen and carbon dioxide
US5925800A (en) 1996-12-31 1999-07-20 Exxon Chemical Patents Inc. Conversion of oxygenates to hydrocarbons with monolith supported non-zeolitic molecular sieve catalysts
US5952538A (en) 1996-12-31 1999-09-14 Exxon Chemical Patents Inc. Use of short contact time in oxygenate conversion
US5960643A (en) 1996-12-31 1999-10-05 Exxon Chemical Patents Inc. Production of ethylene using high temperature demethanization
US5907076A (en) 1996-12-31 1999-05-25 Exxon Chemical Patents Inc. Process for selectively separating hydrogen, or both hydrogen and carbon monoxide from olefinic hydrocarbons
US5925586A (en) 1996-12-31 1999-07-20 Exxon Chemical Patents, Inc. Phosphorus modified small pore molecular sieve catalysts, and their use in the production of light olefins
US6023005A (en) 1997-07-03 2000-02-08 Exxon Chemicals Patents Inc. Process for converting oxygenates to olefins using molecular sieve catalysts comprising desirable carbonaceous deposits
US5927063A (en) 1997-08-19 1999-07-27 Exxon Chemical Patents Inc. High efficiency reformed methanol gas turbine power plants
US5932512A (en) 1997-08-19 1999-08-03 Exxon Chemical Patents, Inc. Fluorination of synthesized molecular sieve catalysts for increased selectivity to ethylene during conversion of oxygenates to olefins
US5892079A (en) 1997-10-17 1999-04-06 Sri International Metallocene catalysts and associated methods of preparation and use
US5958222A (en) 1997-11-17 1999-09-28 Uop Llc Standpipe distributor for short time contact of hydrocarbon compounds with particles
US6005155A (en) 1997-12-03 1999-12-21 Exxon Chemicals Patents Inc. Modification of molecular sieve catalyst for reduced methane production during conversion of oxygenates to olefins
US6046373A (en) 1998-04-29 2000-04-04 Exxon Chemical Patents Inc. Catalytic conversion of oxygenates to olefins
US5944982A (en) 1998-10-05 1999-08-31 Uop Llc Method for high severity cracking
US6051745A (en) 1999-03-04 2000-04-18 Phillips Petroleum Company Silicoaluminophosphate material, a method of making such improved material and the use thereof in the conversion of oxygenated hydrocarbons to olefins
CN1078094C (zh) 1999-04-23 2002-01-23 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
US6046371A (en) 1999-05-05 2000-04-04 Phillips Petroleum Company Silicoaluminophosphate material, a method of making such improved material and the use thereof in the conversion of oxygenated hydrocarbons to olefins
FI106242B (fi) 1999-05-20 2000-12-29 Einco Oy Kiertomassareaktori
WO2001004079A1 (en) 1999-07-09 2001-01-18 E.I. Du Pont De Nemours And Company Vapor phase catalytic oxidation of propylene to acrylic acid
US6869521B2 (en) * 2002-04-18 2005-03-22 Uop Llc Process and apparatus for upgrading FCC product with additional reactor with thorough mixing
US6166282A (en) 1999-08-20 2000-12-26 Uop Llc Fast-fluidized bed reactor for MTO process
US7102050B1 (en) * 2000-05-04 2006-09-05 Exxonmobil Chemical Patents Inc. Multiple riser reactor

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DE60321036D1 (de) 2008-06-26
EA008696B1 (ru) 2007-06-29
US7122160B2 (en) 2006-10-17
ES2305562T3 (es) 2008-11-01
US20040059171A1 (en) 2004-03-25
WO2004029178A1 (en) 2004-04-08
EA200501080A1 (ru) 2005-12-29
EP1565541B1 (de) 2008-05-14
AU2003232464A1 (en) 2004-04-19

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