ES2074837T3 - Procedimiento y dispositivo para la conversion de un compuesto oxigenado en hidrocarburos olefinicos. - Google Patents

Procedimiento y dispositivo para la conversion de un compuesto oxigenado en hidrocarburos olefinicos.

Info

Publication number
ES2074837T3
ES2074837T3 ES92400521T ES92400521T ES2074837T3 ES 2074837 T3 ES2074837 T3 ES 2074837T3 ES 92400521 T ES92400521 T ES 92400521T ES 92400521 T ES92400521 T ES 92400521T ES 2074837 T3 ES2074837 T3 ES 2074837T3
Authority
ES
Spain
Prior art keywords
duct
conversion
phase
separator
reactor
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Lifetime
Application number
ES92400521T
Other languages
English (en)
Inventor
Francois Hugues
Jean-Pierre Burzynski
Daniel Vuillemot
Pierre Galtier
Thierry Gauthier
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
IFP Energies Nouvelles IFPEN
Original Assignee
IFP Energies Nouvelles IFPEN
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 IFP Energies Nouvelles IFPEN filed Critical IFP Energies Nouvelles IFPEN
Application granted granted Critical
Publication of ES2074837T3 publication Critical patent/ES2074837T3/es
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Classifications

    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B04—CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
    • B04C—APPARATUS USING FREE VORTEX FLOW, e.g. CYCLONES
    • B04C7/00—Apparatus not provided for in group B04C1/00, B04C3/00, or B04C5/00; Multiple arrangements not provided for in one of the groups B04C1/00, B04C3/00, or B04C5/00; Combinations of apparatus covered by two or more of the groups B04C1/00, B04C3/00, or B04C5/00
    • 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
    • B01J19/24—Stationary reactors without moving elements inside
    • B01J19/2405—Stationary reactors without moving elements inside provoking a turbulent flow of the reactants, such as in cyclones, or having a high Reynolds-number
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B04—CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
    • B04C—APPARATUS USING FREE VORTEX FLOW, e.g. CYCLONES
    • B04C3/00—Apparatus in which the axial direction of the vortex flow following a screw-thread type line remains unchanged ; Devices in which one of the two discharge ducts returns centrally through the vortex chamber, a reverse-flow vortex being prevented by bulkheads in the central discharge duct
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B04—CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
    • B04C—APPARATUS USING FREE VORTEX FLOW, e.g. CYCLONES
    • B04C3/00—Apparatus in which the axial direction of the vortex flow following a screw-thread type line remains unchanged ; Devices in which one of the two discharge ducts returns centrally through the vortex chamber, a reverse-flow vortex being prevented by bulkheads in the central discharge duct
    • B04C3/06—Construction of inlets or outlets to the vortex chamber
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C1/00—Preparation of hydrocarbons from one or more compounds, none of them being a hydrocarbon
    • C07C1/20—Preparation of hydrocarbons from one or more compounds, none of them being a hydrocarbon starting from organic compounds containing only oxygen atoms as heteroatoms
    • 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
    • B01J2208/00—Processes carried out in the presence of solid particles; Reactors therefor
    • B01J2208/00008—Controlling the process
    • B01J2208/00548—Flow
    • B01J2208/00557—Flow controlling the residence time inside the reactor vessel
    • 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
    • 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
    • Y02P30/40—Ethylene production
    • 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

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Hydrogen, Water And Hydrids (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
  • Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)
  • Cyclones (AREA)

Abstract

LA CONVERSION DE UNA CARGA QUE COMPRENDE AL MENOS UN COMPUESTO OXIGENADO SE EFECTUA EN UN REACTOR (C) EN EL QUE LA CARGA SE INTRODUCE POR EL CONDUCTO (11), FORMANDO LAS PARTICULAS SOLIDAS CATALITICAS LAS FASE DENSA D1 POR EL CONDUCTO (14) Y EL GAS DE ARRASTRE DEL SOLIDO POR EL CONDUCTO (12). EL REACTOR ESTA CONECTADO POR UN CONDUCTO (1) A UN MEZCLADOR-SEPARADOR (MS) CICLONICO DE COCORRIENTE QUE PERMITE SEPARAR UNA FASE SOLIDA DE UNA FASE GASEOSA QUE CONTIENE LOS PRODUCTOS DE LA CONVERSION RECUPERADA POR EL CONDUCTO (4'') A LA VEZ QUE EFECTUA UN TEMPLE DE ESTA FASE GASEOSA POR UN PRODUCTO M2 INTRODUCIDO POR EL CONDUCTO (3). LA FASE D1 ES ENVIADA POR EL CONDUCTO 7 A UN REGENERADOR R ANTES DE SER REENVIADA, POR EL CONDUCTO (13) EN EL REACTOR (C). LA MEZCLA DE LA FASE GASEOSA Y DEL PRODUCTO M2 SE SEPARA EN UN SEPARADOR Y EL PRODUCTO M2, EVENTUALMENTE TRAS EL ENFRIAMENTO, ES RECICLADO EN EL MEZCLADOR-SEPARADOR (MS).
ES92400521T 1991-03-07 1992-02-27 Procedimiento y dispositivo para la conversion de un compuesto oxigenado en hidrocarburos olefinicos. Expired - Lifetime ES2074837T3 (es)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
FR9102892A FR2673623B1 (fr) 1991-03-07 1991-03-07 Procede et dispositif de conversion catalytique d'une charge contenant un compose oxygene comportant la trempe et la separation simultanee des produits formes et du catalyseur.

Publications (1)

Publication Number Publication Date
ES2074837T3 true ES2074837T3 (es) 1995-09-16

Family

ID=9410573

Family Applications (1)

Application Number Title Priority Date Filing Date
ES92400521T Expired - Lifetime ES2074837T3 (es) 1991-03-07 1992-02-27 Procedimiento y dispositivo para la conversion de un compuesto oxigenado en hidrocarburos olefinicos.

Country Status (10)

Country Link
US (1) US5264645A (es)
EP (1) EP0502767B1 (es)
AU (1) AU653583B2 (es)
CA (1) CA2062471A1 (es)
DE (1) DE69202285T2 (es)
ES (1) ES2074837T3 (es)
FR (1) FR2673623B1 (es)
NO (1) NO179745C (es)
NZ (1) NZ241847A (es)
ZA (1) ZA921695B (es)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
ES2164544A1 (es) * 1999-07-22 2002-02-16 Univ Zaragoza Reactor de membrana zeolitica para la obtencion de metanol y otros alcoholes a partir de gas de sintesis

Families Citing this family (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
AU4996896A (en) * 1996-02-20 1997-09-10 Oleg Vyacheslavovich Kozyuk Method for changing the qualitative and quantitative composition of a mixture of liquid hydrocarbons
US5785933A (en) * 1997-01-21 1998-07-28 Mobil Oil Corporation Sulfuric acid alkylation reactor system with static mixers
US5937906A (en) * 1997-05-06 1999-08-17 Kozyuk; Oleg V. Method and apparatus for conducting sonochemical reactions and processes using hydrodynamic cavitation
US5931771A (en) * 1997-12-24 1999-08-03 Kozyuk; Oleg V. Method and apparatus for producing ultra-thin emulsions and dispersions
US5971601A (en) * 1998-02-06 1999-10-26 Kozyuk; Oleg Vyacheslavovich Method and apparatus of producing liquid disperse systems
US6870072B2 (en) * 2001-10-30 2005-03-22 Exxonmobil Chemical Patents Inc. Heat recovery in an olefin production process
US7141711B2 (en) * 2003-03-24 2006-11-28 Exxonmobil Chemical Patents Inc. Catalyst fines handling process
CN103801242B (zh) * 2012-11-03 2015-12-02 中国石油化工股份有限公司 反应器和利用这种反应器的烷基化反应方法
CN105561896A (zh) * 2016-01-28 2016-05-11 杭州海虹精细化工有限公司 一种高效的气液反应装置
PL3448576T3 (pl) * 2016-04-26 2024-09-16 Newcastle Innovation Limited Urządzenie podające do separatora cząstek stałych, separator cząstek stałych i sposób separacji cząstek
CN110343028A (zh) * 2018-04-02 2019-10-18 中国石化工程建设有限公司 一种降低mto装置催化剂损失量的方法和装置

Family Cites Families (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4229608A (en) * 1978-12-18 1980-10-21 Mobil Oil Corporation Heat balanced cyclic process for manufacture of light olefins
US4197418A (en) * 1979-03-01 1980-04-08 Mobil Oil Corporation Heat disposed in lower alcohols and derivatives conversion to gasoline hydrocarbons in a crystaline zeolite fluidized bed
US4423274A (en) * 1980-10-03 1983-12-27 Mobil Oil Corporation Method for converting alcohols to hydrocarbons
US4686313A (en) * 1984-12-31 1987-08-11 Mobil Oil Corporation Low nitrogen iron-containing Fischer-Tropsch catalyst and conversion of synthesis gas therewith
US4627911A (en) * 1985-08-21 1986-12-09 Mobil Oil Corporation Dispersed catalyst cracking with methanol as a coreactant

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
ES2164544A1 (es) * 1999-07-22 2002-02-16 Univ Zaragoza Reactor de membrana zeolitica para la obtencion de metanol y otros alcoholes a partir de gas de sintesis

Also Published As

Publication number Publication date
NO920880L (no) 1992-09-08
EP0502767A1 (fr) 1992-09-09
ZA921695B (en) 1993-09-06
DE69202285D1 (de) 1995-06-08
NO179745C (no) 1996-12-11
DE69202285T2 (de) 1995-09-07
AU1212992A (en) 1992-09-10
NZ241847A (en) 1995-03-28
NO920880D0 (no) 1992-03-05
AU653583B2 (en) 1994-10-06
FR2673623A1 (fr) 1992-09-11
CA2062471A1 (fr) 1992-09-08
US5264645A (en) 1993-11-23
NO179745B (no) 1996-09-02
EP0502767B1 (fr) 1995-05-03
FR2673623B1 (fr) 1993-06-11

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