ATE395395T1 - Reaktor mit mehreren steigrohren und mit konsolidiertem transport - Google Patents
Reaktor mit mehreren steigrohren und mit konsolidiertem transportInfo
- 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
Links
Classifications
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- 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
- C10G2/00—Production of liquid hydrocarbon mixtures of undefined composition from oxides of carbon
- C10G2/30—Production of liquid hydrocarbon mixtures of undefined composition from oxides of carbon from carbon monoxide with hydrogen
- C10G2/32—Production of liquid hydrocarbon mixtures of undefined composition from oxides of carbon from carbon monoxide with hydrogen with the use of catalysts
- C10G2/34—Apparatus, reactors
- C10G2/342—Apparatus, reactors with moving solid catalysts
- C10G2/344—Apparatus, reactors with moving solid catalysts according to the "fluidised-bed" technique
-
- 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
- B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J19/26—Nozzle-type reactors, i.e. the distribution of the initial reactants within the reactor is effected by their introduction or injection through nozzles
-
- 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
-
- 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
- B01J8/24—Chemical 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
- B01J8/26—Chemical 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
-
- 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
- B01J8/24—Chemical 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
- B01J8/38—Chemical 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
- B01J8/384—Chemical 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
- B01J8/388—Chemical 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
-
- 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
- C10G3/00—Production of liquid hydrocarbon mixtures from oxygen-containing organic materials, e.g. fatty oils, fatty acids
- C10G3/42—Catalytic treatment
- C10G3/44—Catalytic treatment characterised by the catalyst used
- C10G3/48—Catalytic treatment characterised by the catalyst used further characterised by the catalyst support
- C10G3/49—Catalytic treatment characterised by the catalyst used further characterised by the catalyst support containing crystalline aluminosilicates, e.g. molecular sieves
-
- 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
- C10G3/00—Production of liquid hydrocarbon mixtures from oxygen-containing organic materials, e.g. fatty oils, fatty acids
- C10G3/54—Production of liquid hydrocarbon mixtures from oxygen-containing organic materials, e.g. fatty oils, fatty acids characterised by the catalytic bed
- C10G3/55—Production 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
- C10G3/57—Production 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
-
- 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
- C10G3/00—Production of liquid hydrocarbon mixtures from oxygen-containing organic materials, e.g. fatty oils, fatty acids
- C10G3/62—Catalyst 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
- B01J2219/00027—Process aspects
- B01J2219/00038—Processes in parallel
-
- 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
- C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
- C10G2300/40—Characteristics of the process deviating from typical ways of processing
- C10G2300/4093—Catalyst stripping
-
- 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
- C10G2400/00—Products obtained by processes covered by groups C10G9/00 - C10G69/14
- C10G2400/20—C2-C4 olefins
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P30/00—Technologies relating to oil refining and petrochemical industry
- Y02P30/20—Technologies 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)
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)
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)
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 |
-
2002
- 2002-09-24 US US10/253,106 patent/US7122160B2/en not_active Expired - Lifetime
-
2003
- 2003-05-30 ES ES03798661T patent/ES2305562T3/es not_active Expired - Lifetime
- 2003-05-30 EA EA200501080A patent/EA008696B1/ru not_active IP Right Cessation
- 2003-05-30 WO PCT/US2003/017121 patent/WO2004029178A1/en not_active Application Discontinuation
- 2003-05-30 EP EP03798661A patent/EP1565541B1/de not_active Expired - Lifetime
- 2003-05-30 DE DE60321036T patent/DE60321036D1/de not_active Expired - Fee Related
- 2003-05-30 AU AU2003232464A patent/AU2003232464A1/en not_active Abandoned
- 2003-05-30 AT AT03798661T patent/ATE395395T1/de not_active IP Right Cessation
Also Published As
Publication number | Publication date |
---|---|
EP1565541A1 (de) | 2005-08-24 |
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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