AR028922A1 - UN APARATO Y UN PROCESO PARA LA CONVERSIoN DE HIDROCARBUROS - Google Patents

UN APARATO Y UN PROCESO PARA LA CONVERSIoN DE HIDROCARBUROS

Info

Publication number
AR028922A1
AR028922A1 ARP010102050A ARP010102050A AR028922A1 AR 028922 A1 AR028922 A1 AR 028922A1 AR P010102050 A ARP010102050 A AR P010102050A AR P010102050 A ARP010102050 A AR P010102050A AR 028922 A1 AR028922 A1 AR 028922A1
Authority
AR
Argentina
Prior art keywords
catalyst
upright
reactors
separation zone
reactor
Prior art date
Application number
ARP010102050A
Other languages
English (en)
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
Publication of AR028922A1 publication Critical patent/AR028922A1/es

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
    • B01J8/24—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
    • 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
    • C10G11/16—Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils with preheated moving solid catalysts according to the "moving bed" method
    • 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
    • B01J8/1845—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles with particles moving upwards while fluidised
    • 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
    • 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
    • C10G3/62—Catalyst regeneration
    • 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
    • Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10S585/00—Chemistry of hydrocarbon compounds
    • Y10S585/919—Apparatus considerations
    • Y10S585/921—Apparatus considerations using recited apparatus structure
    • 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
    • Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10S585/00—Chemistry of hydrocarbon compounds
    • Y10S585/919—Apparatus considerations
    • Y10S585/921—Apparatus considerations using recited apparatus structure
    • Y10S585/922—Reactor fluid manipulating device
    • 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
    • Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10S585/00—Chemistry of hydrocarbon compounds
    • Y10S585/919—Apparatus considerations
    • Y10S585/921—Apparatus considerations using recited apparatus structure
    • Y10S585/922—Reactor fluid manipulating device
    • Y10S585/923—At reactor inlet
    • 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
    • Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10S585/00—Chemistry of hydrocarbon compounds
    • Y10S585/919—Apparatus considerations
    • Y10S585/921—Apparatus considerations using recited apparatus structure
    • Y10S585/924—Reactor shape or disposition
    • Y10S585/926—Plurality or verticality

Abstract

Un aparato y un proceso para la conversion de hidrocarburos. El aparato comprende: una pluralidad de reactores de montante, teniendo cada uno de los reactores de montante un primer extremo en el cual puede introducirse un catalizador, y un segundo extremo a través del cual el catalizador puede salir del reactor del montante; una zona de separacion en la cual se extienden los segundos extremos de los reactores de montante, estando dicha zona de separacion provista para separar el catalizador de los productos de una reaccion llevada a cabo en el aparato para la conversion de hidrocarburos; y por lo menos un retorno de catalizador en comunicacion fluida con la zona de separacion y los primeros extremos de los reactores de montante, estando el retorno del catalizador provisto para transferir el catalizador desde la zona de separacion a los primeros extremos de los reactores de montante. Mediante la provision de una pluralidad de reactores de tipo montante, el ancho o diámetro del reactor convertidor de la materia prima puede ser reducido, con lo cual es posible mantener una deseada relacion de aspecto junto con su concomitante relacion, más cercana, a un régimen de flujo complejamente desarrollado, deseable, mediante un reactor controlable, de altura reducida. El aparato provee una adecuada relacion de aspecto para un reactor de montante dado sin necesidad de multiples sistemas reactores independientes. El proceso comprende: (a) poner en contacto un catalizador fluidizable, con un fluido fluidizante para fluidizar dicho catalizador fluidizable; (b) introducir dicho catalizador y una materia prima en una pluralidad de reactores de montante, siendo dicha pluralidad de reactores de montante parte de un unico aparato para la conversion de hidrocarburos; (c) hacer reaccionar dicha materia prima con dicho catalizador en dicha pluralidad de reactores de montante, obteniéndose un producto como resultado de dicha reaccion de dicha materia prima con dicho catalizador; (d) separar dicho catalizador de dicho producto en una zona de separacion, estando dicha zona de separacion en comunicacion fluida con dicha pluralidad de reactores de montante; (e) hacer volver dicho catalizador desde dicha zona de separacion a dicha pluralidad de reactores de montante; y (f) repetir los pasos (a) a (e).
ARP010102050A 2000-05-04 2001-04-30 UN APARATO Y UN PROCESO PARA LA CONVERSIoN DE HIDROCARBUROS AR028922A1 (es)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US09/564,613 US7102050B1 (en) 2000-05-04 2000-05-04 Multiple riser reactor

Publications (1)

Publication Number Publication Date
AR028922A1 true AR028922A1 (es) 2003-05-28

Family

ID=24255202

Family Applications (1)

Application Number Title Priority Date Filing Date
ARP010102050A AR028922A1 (es) 2000-05-04 2001-04-30 UN APARATO Y UN PROCESO PARA LA CONVERSIoN DE HIDROCARBUROS

Country Status (18)

Country Link
US (2) US7102050B1 (es)
EP (1) EP1299504B1 (es)
JP (1) JP2003532782A (es)
KR (1) KR100793496B1 (es)
CN (1) CN1307288C (es)
AR (1) AR028922A1 (es)
AT (1) ATE395396T1 (es)
AU (2) AU5924301A (es)
BR (1) BR0110469A (es)
CA (1) CA2404977A1 (es)
DE (1) DE60134020D1 (es)
ES (1) ES2306712T3 (es)
MX (1) MXPA02010825A (es)
MY (1) MY138835A (es)
NO (1) NO20025176D0 (es)
TW (1) TW587095B (es)
WO (1) WO2001085872A2 (es)
ZA (1) ZA200208905B (es)

Families Citing this family (58)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6869521B2 (en) * 2002-04-18 2005-03-22 Uop Llc Process and apparatus for upgrading FCC product with additional reactor with thorough mixing
US7169293B2 (en) 1999-08-20 2007-01-30 Uop Llc Controllable space velocity reactor and process
DK1255719T3 (da) 2000-02-02 2004-08-30 Dow Global Technologies Inc Integreret fremgangsmåde til fremstilling af en alkenylsubstitueret aromatisk forbindelse
US7102050B1 (en) * 2000-05-04 2006-09-05 Exxonmobil Chemical Patents Inc. Multiple riser reactor
US6642281B1 (en) * 2000-09-01 2003-11-04 Exxonmobil Research And Engineering Company Fischer-tropsch process
PL222211B1 (pl) 2001-06-26 2016-07-29 Amgen Fremont Inc Przeciwciało przeciwko OPGL, kompozycja je zawierająca, jego zastosowanie i sposób jego wytwarzania, sposób wykrywania poziomu OPGL, kompozycja obejmująca polinukleotydy i komórka gosodarza
DE10150481B4 (de) * 2001-10-16 2020-09-10 Exxonmobil Chemical Patents Inc. Verfahren zur Herstellung von Olefinen aus Methanol
US7122160B2 (en) * 2002-09-24 2006-10-17 Exxonmobil Chemical Patents Inc. Reactor with multiple risers and consolidated transport
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
CN100363463C (zh) * 2002-10-18 2008-01-23 埃克森美孚化学专利公司 带有中央催化剂回路的多级提升管反应器
US6791002B1 (en) 2002-12-11 2004-09-14 Uop Llc Riser reactor system for hydrocarbon cracking
FI119179B (fi) * 2003-10-21 2008-08-29 Einco Oy Kiertomassareaktori
US20080194891A1 (en) 2004-02-09 2008-08-14 Pretz Matthew T Process for the Preparation of Hydrogenated Hydrocarbon Compounds
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
WO2006020547A1 (en) * 2004-08-10 2006-02-23 Shell Internationale Research Maatschappij B.V. Method and apparatus for making a middle distillate product and lower olefins from a hydrocarbon feedstock
US7622625B2 (en) * 2004-11-01 2009-11-24 Uop Llc Purge gas streams to stagnant zones within oxygenate-to-olefin reactor
FR2877671B1 (fr) * 2004-11-09 2008-10-17 Inst Francais Du Petrole Dispositif et procede pour le craquage catalytique de deux charges distinctes d'hydrocarbures
AR056806A1 (es) 2005-11-14 2007-10-24 Amgen Inc Moleculas quimericas de anticuerpo rankl- pth/ pthrp
EP1955989B1 (en) * 2005-11-14 2017-01-25 JGC Corporation Method for production of lower olefin
US7763765B2 (en) 2006-03-31 2010-07-27 Exxonmobil Chemical Patents Inc. Method of high pressure and high capacity oxygenate conversion with catalyst exposure cycle
CN101448765A (zh) 2006-05-19 2009-06-03 国际壳牌研究有限公司 环烯烃的烷基化方法
US8049054B2 (en) 2006-05-19 2011-11-01 Shell Oil Company Process for the preparation of C5 and/or C6 olefin
US7470825B2 (en) * 2006-06-26 2008-12-30 Exxonmobil Chemical Patents Inc. Reactor and process for producing methanol
BRPI0810190A2 (pt) * 2007-04-13 2014-12-30 Shell Int Research Sistema, e, método.
RU2463335C2 (ru) * 2007-04-30 2012-10-10 Шелл Интернэшнл Рисерч Маатсхаппий Б.В. Установка и способ получения средних дистиллятов и низших олефинов из углеводородного сырья
FR2918070B1 (fr) * 2007-06-27 2012-10-19 Inst Francais Du Petrole Zone reactionnelle comportant deux risers en parallele et une zone de separation gaz solide commune en vue de la production de propylene
WO2009048920A1 (en) * 2007-10-10 2009-04-16 Shell Oil Company Systems and methods for making a middle distillate product and lower olefins from a hydrocarbon feedstock
JP2011504466A (ja) 2007-11-19 2011-02-10 シエル・インターナシヨナル・リサーチ・マートスハツペイ・ベー・ヴエー オレフィン生成物の調製方法
WO2009065851A1 (en) 2007-11-19 2009-05-28 Shell Internationale Research Maatschappij B.V. Process for the preparation of an olefin
BRPI0704443B1 (pt) * 2007-11-30 2018-09-11 Petroleo Brasileiro S/A Petrobras sistema e processo de separação de suspensões de catalisadores gastos e hidrocarbonetos formadas em unidade de craqueamento catalítico fluido com múltiplos tubos de fluxo ascendente de reação
WO2010062611A2 (en) * 2008-10-27 2010-06-03 Kior, Inc. Biomass conversion process
EP2342169A4 (en) * 2008-11-04 2012-04-11 Kior Inc METHOD FOR CONVERTING BIOMASS
EP2373602B1 (en) 2008-12-22 2013-08-21 Shell Internationale Research Maatschappij B.V. Process to prepare methanol and/or dimethylether
CN102355947A (zh) * 2009-03-19 2012-02-15 陶氏环球技术有限责任公司 脱氢方法和催化剂
US9126174B2 (en) * 2010-03-31 2015-09-08 Uop Llc Hydroprocessing method, or an apparatus relating thereto
CN102464532B (zh) * 2010-11-17 2014-07-02 中国石油化工股份有限公司 低碳烯烃的制备方法
US8689709B2 (en) * 2011-05-04 2014-04-08 Southern Company Oxycombustion in transport oxy-combustor
CN102875279B (zh) * 2011-07-12 2015-01-07 中国石油化工股份有限公司 甲醇和石脑油制备低碳烯烃的反应装置
CN102875304B (zh) * 2011-07-12 2015-02-11 中国石油化工股份有限公司 甲醇和石脑油制备低碳烯烃的方法
JP2013116431A (ja) * 2011-12-01 2013-06-13 Sumitomo Chemical Co Ltd 反応装置
JP2013116434A (ja) * 2011-12-01 2013-06-13 Sumitomo Chemical Co Ltd 反応装置
US10189763B2 (en) 2016-07-01 2019-01-29 Res Usa, Llc Reduction of greenhouse gas emission
US9981896B2 (en) 2016-07-01 2018-05-29 Res Usa, Llc Conversion of methane to dimethyl ether
WO2018004994A1 (en) 2016-07-01 2018-01-04 Res Usa, Llc Fluidized bed membrane reactor
KR101982786B1 (ko) * 2017-12-01 2019-05-28 한국에너지기술연구원 유동층 반응기
CN115210201A (zh) 2020-03-06 2022-10-18 埃克森美孚化学专利公司 烷烃和烷基芳族烃的提质方法
US11760703B2 (en) 2020-03-06 2023-09-19 Exxonmobil Chemical Patents Inc. Processes for upgrading alkanes and alkyl aromatic hydrocarbons
US11859136B2 (en) 2020-03-06 2024-01-02 Exxonmobil Chemical Patents Inc. Processes for upgrading alkanes and alkyl aromatic hydrocarbons
JP2023516098A (ja) 2020-03-06 2023-04-17 エクソンモービル ケミカル パテンツ インコーポレイテッド アルカン及びアルキル芳香族炭化水素のアップグレードプロセス
JP2023524562A (ja) 2020-05-08 2023-06-12 エクソンモービル ケミカル パテンツ インコーポレイテッド アルカン及びアルキル芳香族炭化水素を改質するための方法及びシステム
CA3220944A1 (en) 2021-06-02 2022-12-08 Xiaoying Bao Processes for regenerating catalysts and for upgrading alkanes and/or alkyl aromatic hydrocarbons
BR112023026786A2 (pt) 2021-07-28 2024-03-12 Exxonmobil Chemical Patents Inc Composições de catalisador e processos para a sua preparação e uso
CA3228400A1 (en) 2021-08-11 2023-02-16 Exxonmobil Chemical Patents Inc. Processes for regenerating catalysts and for upgrading alkanes and/or alkyl aromatic hydrocarbons
WO2023018527A1 (en) 2021-08-11 2023-02-16 Exxonmobil Chemical Patents Inc. Processes for dehydrogenating alkanes and alkyl aromatic hydrocarbons
WO2023018536A1 (en) 2021-08-13 2023-02-16 Exxonmobil Chemical Patents Inc. Processes for dehydrogenating alkanes and alkyl aromatic hydrocarbons
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
WO2023107797A1 (en) 2021-12-06 2023-06-15 Exxonmobil Chemical Patents Inc. Catalyst compositions and processes for making and using same

Family Cites Families (96)

* 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
BE591537A (es) 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
US3607730A (en) * 1968-04-05 1971-09-21 Pullman Inc Apparatus and method for conversion of hydrocarbons
US3764634A (en) 1969-04-23 1973-10-09 Mitsui Shipbuilding Eng Process and apparatus for preparing lower olefins
US3617496A (en) * 1969-06-25 1971-11-02 Gulf Research Development Co Fluid catalytic cracking process with a segregated feed charged to separate reactors
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
US3969426A (en) * 1974-10-17 1976-07-13 Mobil Oil Corporation Conversion of methanol to products comprising gasoline boiling components
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
US4517616A (en) * 1982-04-12 1985-05-14 Memorex Corporation Thin film magnetic recording transducer having embedded pole piece design
NZ204419A (en) 1982-06-15 1985-04-30 Mobil Oil Corp Catalytic conversion of oxygenated compounds to liquid hydrocarbons
US4440871A (en) 1982-07-26 1984-04-03 Union Carbide Corporation Crystalline silicoaluminophosphates
US4404414A (en) * 1982-09-28 1983-09-13 Mobil Oil Corporation Conversion of methanol to gasoline
US4677243A (en) 1982-10-04 1987-06-30 Union Carbide Corporation Production of light olefins from aliphatic hetero compounds
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
JPS6088222A (ja) 1983-10-21 1985-05-18 Daido Metal Kogyo Kk 複合摺動体
US4623443A (en) * 1984-02-07 1986-11-18 Phillips Petroleum Company Hydrocarbon conversion
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
US4659585A (en) * 1985-06-24 1987-04-21 International Business Machines Corporation Planarized ceramic substrates
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
US4853105A (en) * 1986-09-03 1989-08-01 Mobil Oil Corporation Multiple riser fluidized catalytic cracking process utilizing hydrogen and carbon-hydrogen contributing fragments
US4717466A (en) * 1986-09-03 1988-01-05 Mobil Oil Corporation Multiple riser fluidized catalytic cracking process utilizing hydrogen and carbon-hydrogen contributing fragments
US4778600A (en) * 1987-06-17 1988-10-18 Dow Corning Corporation Liquid chromatography dual zone packing materials
US4873390A (en) 1987-07-07 1989-10-10 Uop Chemical conversion process
US4973792A (en) 1987-07-07 1990-11-27 Uop Chemical conversion process
US4861938A (en) 1987-07-07 1989-08-29 Uop Chemical conversion process
US4814541A (en) 1987-07-07 1989-03-21 Uop Chemical conversion process
US5114682A (en) * 1988-11-18 1992-05-19 Stone & Webster Engineering Corporation Apparatus for recovering heat energy from catalyst regenerator flue gases
US5271905A (en) 1990-04-27 1993-12-21 Mobil Oil Corporation Apparatus for multi-stage fast fluidized bed regeneration of catalyst
US5157181A (en) 1990-12-03 1992-10-20 Uop Moving bed hydrocarbon conversion process
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
ES2073240T3 (es) * 1991-09-09 1995-08-01 Stone & Webster Eng Corp Procedimiento y aparato para separar catalizadores de craqueo fluidizados de hidrocarburos vaporizados.
US5191141A (en) 1991-11-13 1993-03-02 Uop Process for converting methanol to olefins using an improved metal aluminophosphate catalyst
US5126308A (en) 1991-11-13 1992-06-30 Uop Metal aluminophosphate catalyst for converting methanol to light olefins
US5338517A (en) * 1992-05-18 1994-08-16 Chemical Research & Licensing Company Catalytic distillation column reactor and tray
EP0644866B1 (en) 1992-05-27 1996-08-14 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
US5221301A (en) * 1992-10-28 1993-06-22 Emtrol Corporation Multi-stage cyclone separator system with intermediate manifold
US5343830A (en) 1993-03-25 1994-09-06 The Babcock & Wilcox Company Circulating fluidized bed reactor with internal primary particle separation and return
US5565090A (en) * 1994-11-25 1996-10-15 Uop Modified riser-reactor reforming process
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
US5952539A (en) * 1996-02-23 1999-09-14 Exxon Chemical Patents Inc. Dual process for obtaining olefins
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
KR20000016111A (ko) 1996-05-29 2000-03-25 엑손 케미칼 패턴츠 인코포레이티드 탄화수소 전환 촉매 및 그의 용도
US5851380A (en) * 1996-08-01 1998-12-22 Phillips Petroleum Company Process and apparatus for fluidized catalytic cracking of a hydrocarbon feed
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
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
US5960643A (en) 1996-12-31 1999-10-05 Exxon Chemical Patents Inc. Production of ethylene using high temperature demethanization
US5952538A (en) 1996-12-31 1999-09-14 Exxon Chemical Patents Inc. Use of short contact time in oxygenate conversion
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
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
US5904880A (en) 1996-12-31 1999-05-18 Exxon Chemical Patents Inc. One step conversion of methanol to hydrogen and carbon dioxide
US6051746A (en) 1997-06-18 2000-04-18 Exxon Chemical Patents Inc. Oxygenate conversions using modified small pore molecular sieve catalysts
US6552240B1 (en) * 1997-07-03 2003-04-22 Exxonmobil Chemical Patents Inc. Method for converting oxygenates to 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
ID24324A (id) * 1997-07-15 2000-07-13 I E I Du Pont De Nemours And C Oksidasi fasa map propilen menjadi akrolein yang diperbaiki
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
US6036845A (en) * 1998-05-04 2000-03-14 Uop Llc Modified riser-reactor reforming process with prereactor
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
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
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
US6791002B1 (en) * 2002-12-11 2004-09-14 Uop Llc Riser reactor system for hydrocarbon cracking
US7448481B2 (en) * 2004-07-27 2008-11-11 Ford Global Technologies, Llc Ratcheting one-way clutch having rockers actuated by centrifugal force
JP4873139B2 (ja) * 2006-06-23 2012-02-08 Ｎｏｋ株式会社 ガスケットの製造方法

Also Published As

Publication number Publication date
CN1307288C (zh) 2007-03-28
KR100793496B1 (ko) 2008-01-14
NO20025176L (no) 2002-10-28
DE60134020D1 (de) 2008-06-26
CA2404977A1 (en) 2001-11-15
MY138835A (en) 2009-07-31
EP1299504B1 (en) 2008-05-14
AU2001259243B2 (en) 2005-02-17
TW587095B (en) 2004-05-11
WO2001085872A2 (en) 2001-11-15
WO2001085872A3 (en) 2002-02-28
ZA200208905B (en) 2003-10-15
AU5924301A (en) 2001-11-20
NO20025176D0 (no) 2002-10-28
MXPA02010825A (es) 2004-10-15
US7102050B1 (en) 2006-09-05
US20050152814A1 (en) 2005-07-14
EP1299504A2 (en) 2003-04-09
US7195741B2 (en) 2007-03-27
KR20020093115A (ko) 2002-12-12
BR0110469A (pt) 2003-04-08
ATE395396T1 (de) 2008-05-15
CN1633493A (zh) 2005-06-29
ES2306712T3 (es) 2008-11-16
JP2003532782A (ja) 2003-11-05

Similar Documents

Publication Publication Date Title
AR028922A1 (es) UN APARATO Y UN PROCESO PARA LA CONVERSIoN DE HIDROCARBUROS
ATE395395T1 (de) Reaktor mit mehreren steigrohren und mit konsolidiertem transport
ATE374806T1 (de) Mehrfachsteigrohrreaktor mit centraler katalysatorrückführung
AR015944A1 (es) Metodo para incrementar el rendimiento de olefinas ligeras por conversion de una fraccion hidrocarburo pesado de un producto a olefinas ligeras.
AR025793A1 (es) Metodo para convertir una carga de alimentacion que contiene compuesto oxigenado en un producto de olefina
AR060564A1 (es) Proceso para la conversion de metano
MY197470A (en) Fluid catalytic cracking process and apparatus for maximizing light olefin yield and other applications
RU2008101553A (ru) Способ каталитического крекинга с применением быстрой флюидизации для получения легких олефинов из углеводородного исходного сырья
EP3225678A3 (en) Am fcc process with two reaction zones
CN102099314B (zh) Oto方法与直接dme合成的联合
AR119395A1 (es) Procedimiento y aparato de craqueo catalítico fluido para maximizar el rendimiento de olefinas ligeras y otras aplicaciones
CN101270019B (zh) 由甲醇或二甲醚制备乙烯和丙烯的方法
US20180134966A1 (en) Systems and methods related to syngas to olefin process
MXPA02011071A (es) Metodo para convertir oxigenados en olefinas.
US8747767B2 (en) Catalyst return apparatus, and process for reacting a feedstock
US11447704B2 (en) Oxygenate separation using a metal salt
WO2010072730A1 (en) A riser reactor system and a process for the preparation of an olefinic product
TWI838559B (zh) 流體催化裂解方法以及用於使輕質烯烴產率最大化及其他應用之裝置
CN201186919Y (zh) 可用于石油烃类原料催化转化的沉降器
RU2010121906A (ru) Установки и способы для получения среднедистиллятного продукта и низших олефинов из углеводородного исходного сырья
CN101279874A (zh) 由甲醇或二甲醚生产低碳烯烃的方法
RU2010117231A (ru) Системы и способы получения средних дистиллятов и низких олефинов из углеводородного сырья
TH67858A (th) การนำ c6 กลับมาใช้ใหม่ สำหรับก่อกำเนิดโพรพิลีน ในหน่วยการแตกตัวแบบเร่งปฏิกิริยาของไหล
MY129123A (en) Optimized process for the preparation of olefins by direct conversion of multiple hydrocarbons
RU2020109211A (ru) Способ и установка для производства олефинов из оксигенатов

Legal Events

Date Code Title Description
FG Grant, registration