ES2155677T3 - Sistema convertidor catalitico y procedimiento correspondiente. - Google Patents

Sistema convertidor catalitico y procedimiento correspondiente.

Info

Publication number
ES2155677T3
ES2155677T3 ES97912221T ES97912221T ES2155677T3 ES 2155677 T3 ES2155677 T3 ES 2155677T3 ES 97912221 T ES97912221 T ES 97912221T ES 97912221 T ES97912221 T ES 97912221T ES 2155677 T3 ES2155677 T3 ES 2155677T3
Authority
ES
Spain
Prior art keywords
reactor
liquid
reaction
series
zones
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
ES97912221T
Other languages
English (en)
Inventor
John Jubin Jr
Wayne Wentzheimer
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.)
Lyondell Chemical Technology LP
Original Assignee
Arco Chemical Technology LP
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 Arco Chemical Technology LP filed Critical Arco Chemical Technology LP
Application granted granted Critical
Publication of ES2155677T3 publication Critical patent/ES2155677T3/es
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Classifications

    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07D—HETEROCYCLIC COMPOUNDS
    • C07D301/00—Preparation of oxiranes
    • C07D301/02—Synthesis of the oxirane ring
    • C07D301/03—Synthesis of the oxirane ring by oxidation of unsaturated compounds, or of mixtures of unsaturated and saturated compounds
    • C07D301/19—Synthesis of the oxirane ring by oxidation of unsaturated compounds, or of mixtures of unsaturated and saturated compounds with organic hydroperoxides
    • 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
    • B01J8/02—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds
    • 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
    • B01J8/02—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds
    • B01J8/0285—Heating or cooling the reactor
    • 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
    • B01J8/02—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds
    • B01J8/04—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds the fluid passing successively through two or more beds
    • B01J8/0446—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds the fluid passing successively through two or more beds the flow within the beds being predominantly vertical
    • B01J8/0449—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds the fluid passing successively through two or more beds the flow within the beds being predominantly vertical in two or more cylindrical beds
    • B01J8/0453—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds the fluid passing successively through two or more beds the flow within the beds being predominantly vertical in two or more cylindrical beds the beds being superimposed one above the other
    • 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
    • B01J8/02—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds
    • B01J8/04—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds the fluid passing successively through two or more beds
    • B01J8/0496—Heating or cooling the reactor
    • 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
    • B01J2208/00017—Controlling the temperature
    • B01J2208/00106—Controlling the temperature by indirect heat exchange
    • B01J2208/00265—Part of all of the reactants being heated or cooled outside the reactor while recycling
    • B01J2208/00283—Part of all of the reactants being heated or cooled outside the reactor while recycling involving reactant liquids
    • 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
    • B01J2208/00017—Controlling the temperature
    • B01J2208/00327—Controlling the temperature by direct heat exchange
    • 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
    • B01J2208/00017—Controlling the temperature
    • B01J2208/00327—Controlling the temperature by direct heat exchange
    • B01J2208/00336—Controlling the temperature by direct heat exchange adding a temperature modifying medium to the reactants
    • B01J2208/00353—Non-cryogenic fluids
    • B01J2208/00362—Liquid
    • 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
    • B01J2219/00049—Controlling or regulating processes
    • B01J2219/00051—Controlling the temperature
    • B01J2219/00074—Controlling the temperature by indirect heating or cooling employing heat exchange fluids
    • B01J2219/00087—Controlling the temperature by indirect heating or cooling employing heat exchange fluids with heat exchange elements outside the reactor
    • B01J2219/00103—Controlling the temperature by indirect heating or cooling employing heat exchange fluids with heat exchange elements outside the reactor in a heat exchanger separate from the reactor
    • 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
    • Y02P20/00—Technologies relating to chemical industry
    • Y02P20/50—Improvements relating to the production of bulk chemicals

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Epoxy Compounds (AREA)
  • Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)

Abstract

SE DESCRIBEN UN REACTOR (1) Y UN PROCEDIMIENTO PARA LA PRODUCCION DE COMPUESTOS DE OXIDANO POR REACCION DE UNA OLECINA, COMO EL PROPILENO, CON UN HIDROPEROXIDO ORGANICO QUE UTILIZA UN CATALIZADOR SOLIDO POR CONTACTO, CARACTERIZADO POR LOS ASPECTOS SIGUIENTES: (1) EL REACTOR (1) ESTA DIVIDIDO EN UNA SERIE DE ZONAS SEPARADAS (8, 17, 24, 30, 36), CONTENIENDO CADA ZONA UN LECHO (2, 3, 4, 5, 6) DE CATALIZADOR SOLIDO DE EPOXIDACION; (2) SE MANTIENEN CONDICIONES A FIN DE PROPORCIONAR LA FASE LIQUIDA SIN FORMACION SUSTANCIAL DE VAPOR A TRAVES DE TODO EL REACTOR; (3) SE PROPORCIONA UNA ALIMENTACION (7) DEL REACTOR EN FRIO, QUE SE CALIENTA PREVIAMENTE A LA TEMPERATURA DE REACCION POR TERMOINTERCAMBIO INDIRECTO SEPARADO CON EL LIQUIDO DE REACCION DE VARIAS DE LAS ZONAS SEPARADAS DEL REACTOR; (4)EL LIQUIDO DE REACCION (38) DE LA ULTIMA DE LAS SERIES DE ZONAS DE REACCION SE REDUCE EN CUANTO A SU PRESION, PARA FORMAR UNA MEZCLA GAS-LIQUIDO A TEMPERATURA MENOR, Y ESTA MEZCLA DE GAS-LIQUIDO SE CALIENTA PORINTERCAMBIO TERMICO INDIRECTO DENTRO DEL LIQUIDO DE REACCION DESDE AL MENOS UNA DE LAS ZONAS SEPARADAS DEL REACTOR.
ES97912221T 1996-10-29 1997-10-27 Sistema convertidor catalitico y procedimiento correspondiente. Expired - Lifetime ES2155677T3 (es)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US08/740,461 US5840933A (en) 1996-10-29 1996-10-29 Catalytic converter system and progress

Publications (1)

Publication Number Publication Date
ES2155677T3 true ES2155677T3 (es) 2001-05-16

Family

ID=24976627

Family Applications (1)

Application Number Title Priority Date Filing Date
ES97912221T Expired - Lifetime ES2155677T3 (es) 1996-10-29 1997-10-27 Sistema convertidor catalitico y procedimiento correspondiente.

Country Status (12)

Country Link
US (2) US5840933A (es)
EP (1) EP0938370B1 (es)
JP (1) JP4121154B2 (es)
KR (1) KR100469038B1 (es)
CN (1) CN1106878C (es)
AU (1) AU4949497A (es)
BR (1) BR9712395A (es)
CA (1) CA2268961C (es)
DE (1) DE69704566T2 (es)
ES (1) ES2155677T3 (es)
RU (1) RU2181071C2 (es)
WO (1) WO1998018547A1 (es)

Families Citing this family (18)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5849937A (en) * 1997-12-19 1998-12-15 Arco Chemical Technology, L.P. Epoxidation process using serially connected cascade of fixed bed reactors
JP2001270871A (ja) 2000-03-24 2001-10-02 Sumitomo Chem Co Ltd オキシラン化合物の製造方法
JP2001270879A (ja) * 2000-03-24 2001-10-02 Sumitomo Chem Co Ltd オキシラン化合物の製造方法
JP2001270874A (ja) 2000-03-24 2001-10-02 Sumitomo Chem Co Ltd プロピレンオキサイドの製造方法
DE10020632A1 (de) * 2000-04-27 2001-10-31 Merck Patent Gmbh Verfahren zur Expodierung von Olefinen
CA2427174C (en) * 2000-11-11 2009-04-07 Haldor Topsoe A/S Improved hydroprocessing process and method of retrofitting existing hydroprocessing reactors
CN1809546A (zh) * 2001-05-08 2006-07-26 国际壳牌研究有限公司 制备烯化氧(环氧化物、环氧乙烷）的方法
WO2003050100A1 (en) * 2001-12-05 2003-06-19 Dow Global Technologies Inc. Process of preparing an olefin oxide from olefin and organic hydroperoxide
US6562987B1 (en) * 2002-02-28 2003-05-13 Arco Chemical Technology, L.P. Method for highly exothermic epoxidation reactions
US6583300B1 (en) * 2002-10-17 2003-06-24 Arco Chemical Technology, L.P. Epoxidation system with fixed bed reactors
WO2005028405A1 (ja) * 2003-09-18 2005-03-31 Sumitomo Chemical Company, Limited クメンの製造方法
US20080132717A1 (en) * 2006-12-04 2008-06-05 Bernard Cooker Propylene oxide system
ITMI20070932A1 (it) * 2007-05-08 2008-11-09 Basf Ag Procedimento per la preparazione di un ossido olefinico
CA2789688C (en) * 2010-02-13 2014-07-08 Mcalister Technologies, Llc Reactor vessels with pressure and heat transfer features for producing hydrogen-based fuels and structural elements, and associated systems and methods
CN105294605A (zh) * 2014-07-24 2016-02-03 中国石油化工股份有限公司 过氧化氢乙苯与丙烯制环氧丙烷的循环方法
CN105294606B (zh) * 2014-07-24 2017-11-17 中国石油化工股份有限公司 过氧化氢乙苯与丙烯制环氧丙烷的反应方法
CN110787739A (zh) * 2018-08-03 2020-02-14 中国石化工程建设有限公司 一种烷基苯过氧化物与低碳烯烃反应生成环氧烷烃的装置和方法
CN114715847B (zh) * 2022-03-22 2023-06-02 中国矿业大学 一种双燃料供给式可变流量重整器及运行方法

Family Cites Families (15)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2271646A (en) * 1939-05-17 1942-02-03 Universal Oil Prod Co Control of contact catalytic reactions
US3351635A (en) * 1966-03-14 1967-11-07 Halcon International Inc Epoxidation process
DE1904078A1 (de) * 1969-01-28 1970-08-13 Basf Ag Verfahren zur Durchfuehrung exothermer Reaktionen
US4367342A (en) * 1969-04-02 1983-01-04 Shell Oil Company Olefin epoxidation
ZA702171B (en) * 1969-04-02 1971-11-24 Shell Int Research A process for epoxidizing olefins with hydroperoxides
US3829392A (en) * 1970-10-01 1974-08-13 Shell Oil Co Heterogeneous catalysts for olefin epoxidation
US4021454A (en) * 1971-08-19 1977-05-03 Shell Oil Company Olefin epoxidation
US3792981A (en) * 1971-09-15 1974-02-19 Phillips Petroleum Co Catalytic reactor
US3923843A (en) * 1972-03-13 1975-12-02 Shell Oil Co Epoxidation process with improved heterogeneous catalyst
DE2430769A1 (de) * 1974-06-26 1976-01-15 Linde Ag Verfahren zur durchfuehrung einer stark exothermen chemischen reaktion
US4510123A (en) * 1982-11-26 1985-04-09 C F Braun & Co. Temperature controlled ammonia synthesis process
US4867959A (en) * 1986-11-20 1989-09-19 Santa Fe Braun, Inc. Process for synthesizing ammonia
GB8729555D0 (en) * 1987-12-18 1988-02-03 Shell Int Research Alkylation process
US5081267A (en) * 1989-10-05 1992-01-14 Arco Chemical Technology, Inc. Epoxidation process
CA2137310C (en) * 1993-12-20 2004-02-17 John C. Jubin Jr. Catalytic converter and method for highly exothermic reactions

Also Published As

Publication number Publication date
RU2181071C2 (ru) 2002-04-10
DE69704566D1 (de) 2001-05-17
KR20000052927A (ko) 2000-08-25
US6153153A (en) 2000-11-28
JP4121154B2 (ja) 2008-07-23
CN1235560A (zh) 1999-11-17
US5840933A (en) 1998-11-24
EP0938370B1 (en) 2001-04-11
DE69704566T2 (de) 2002-04-11
BR9712395A (pt) 1999-08-31
WO1998018547A1 (en) 1998-05-07
CA2268961C (en) 2005-07-12
KR100469038B1 (ko) 2005-01-29
CA2268961A1 (en) 1998-05-07
AU4949497A (en) 1998-05-22
CN1106878C (zh) 2003-04-30
JP2001506977A (ja) 2001-05-29
EP0938370A1 (en) 1999-09-01

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