BR9806981A - Conversor catalìtico e processo para reações altamente exotérmicas. - Google Patents

Conversor catalìtico e processo para reações altamente exotérmicas.

Info

Publication number
BR9806981A
BR9806981A BR9806981-0A BR9806981A BR9806981A BR 9806981 A BR9806981 A BR 9806981A BR 9806981 A BR9806981 A BR 9806981A BR 9806981 A BR9806981 A BR 9806981A
Authority
BR
Brazil
Prior art keywords
reactor
catalytic converter
reaction
exothermic reactions
highly exothermic
Prior art date
Application number
BR9806981-0A
Other languages
English (en)
Inventor
Jeffrey B Danner
John C Jubin
Richard J Wolff
Original Assignee
Arco Chem Tech
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 Chem Tech filed Critical Arco Chem Tech
Publication of BR9806981A publication Critical patent/BR9806981A/pt

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
    • B01J8/0005—Catalytic processes under superatmospheric pressure
    • 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
    • B01J8/0446—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
    • B01J8/0457—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 placed in separate reactors
    • 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
    • B01J2208/00026—Controlling or regulating the heat exchange system
    • B01J2208/00035—Controlling or regulating the heat exchange system involving measured parameters
    • B01J2208/00044—Temperature measurement
    • 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
    • B01J2208/00026—Controlling or regulating the heat exchange system
    • B01J2208/00035—Controlling or regulating the heat exchange system involving measured parameters
    • B01J2208/0007—Pressure measurement
    • 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
    • B01J2208/00026—Controlling or regulating the heat exchange system
    • B01J2208/00035—Controlling or regulating the heat exchange system involving measured parameters
    • B01J2208/00088—Flow rate measurement
    • 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
    • B01J2208/00274—Part of all of the reactants being heated or cooled outside the reactor while recycling involving reactant vapours
    • 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
    • B01J2208/00796—Details of the reactor or of the particulate material
    • B01J2208/00823—Mixing elements
    • B01J2208/00831—Stationary elements
    • B01J2208/00849—Stationary elements outside the bed, e.g. baffles

Landscapes

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

Abstract

Patente de Invenção: <B>"CONVERSOR CATALìTICO E PROCESSO PARA REAçõES ALTAMENTE EXOTéRMICAS"<D>. Um reator (5, 15, 301) e um processo para a produção de compostos de oxirano, por reação de uma olefina, tal como propileno, com um hidroperóxido orgânico, usando um catalisador de contato sólido, caracterizados pelas seguintes características: (1) o reator é dividido em uma série de zonas separadas (8, 10, 16, 19, 304, 311), cada zona (8, 10, 16, 19, 304, 311) contendo um leito de catalisador sólido de epoxidação; (2) cerca de 25 - 75% do calor da reação são removidos por preaquecimento da alimentação do reator fria por contato direto com uma corrente de reciclo aquecida do reator, e (3) cerca de 25 - 75% do calor da reação são responsáveis por um aumento da temperatura da mistura reacional de -7 para 38°C (20 - 100°F) e por vaporização de 15 - 40% do produto do reator resultante.
BR9806981-0A 1997-01-29 1998-01-26 Conversor catalìtico e processo para reações altamente exotérmicas. BR9806981A (pt)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US08/791,796 US5760253A (en) 1997-01-29 1997-01-29 Catalytic converter and method for highly exothermic reactions
PCT/EP1998/000410 WO1998032530A1 (en) 1997-01-29 1998-01-26 Catalytic converter and method for highly exothermic reactions

Publications (1)

Publication Number Publication Date
BR9806981A true BR9806981A (pt) 2000-03-14

Family

ID=25154809

Family Applications (1)

Application Number Title Priority Date Filing Date
BR9806981-0A BR9806981A (pt) 1997-01-29 1998-01-26 Conversor catalìtico e processo para reações altamente exotérmicas.

Country Status (11)

Country Link
US (1) US5760253A (pt)
EP (1) EP1017487B1 (pt)
JP (1) JP4287910B2 (pt)
KR (1) KR100471930B1 (pt)
CN (1) CN1110359C (pt)
AU (1) AU6616298A (pt)
BR (1) BR9806981A (pt)
CA (1) CA2278666C (pt)
DE (1) DE69803082T2 (pt)
ES (1) ES2165148T3 (pt)
WO (1) WO1998032530A1 (pt)

Families Citing this family (32)

* 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
EP1122246A1 (de) 2000-02-07 2001-08-08 Degussa AG Verfahren zur Epoxidierung von Olefinen
EP1122248A1 (de) 2000-02-07 2001-08-08 Degussa AG Verfahren zur Epoxidierung von Olefinen
EP1122247A1 (de) 2000-02-07 2001-08-08 Degussa AG Verfahren zur Epoxidierung von Olefinen
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
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
ATE475654T1 (de) 2001-01-08 2010-08-15 Evonik Degussa Gmbh Verfahren zur epoxidierung von olefinen
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
US6608219B2 (en) 2001-06-13 2003-08-19 Degussa Ag Process for the epoxidation of olefins
US6596881B2 (en) 2001-06-13 2003-07-22 Degussa Ag Process for the epoxidation of olefins
US6600055B2 (en) 2001-06-13 2003-07-29 Degussa Ag Process for the epoxidation of olefins
US6749668B2 (en) * 2001-06-18 2004-06-15 Degussa Ag Process for the recovery of combustible components of a gas stream
US6610865B2 (en) 2001-08-15 2003-08-26 Degussa Ag Process for the epoxidation of olefins
EP1285915A1 (en) * 2001-08-16 2003-02-26 Degussa AG Continuous process to make epoxide from olefins and hydrogen peroxide
EP1420014A4 (en) * 2001-08-22 2004-09-29 Sumitomo Chemical Co PROCESS FOR PRODUCING PROPYLENE OXIDE
US6596883B2 (en) 2001-08-23 2003-07-22 Degussa Ag Process for the epoxidation of olefins
EP1453818B1 (en) * 2001-12-05 2005-11-09 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
US6720436B2 (en) 2002-03-18 2004-04-13 Degussa Ag Process for the epoxidation of olefins
US7141683B2 (en) * 2002-05-02 2006-11-28 Degussa Ag Process for the epoxidation of olefins
US20040000473A1 (en) * 2002-06-20 2004-01-01 Willi Hofen Process of separating 1-methoxy-2-propanol and 2-methoxy-1-propanol from aqueous compositions
US7722847B2 (en) * 2002-09-30 2010-05-25 Evonik Degussa Gmbh Aqueous hydrogen peroxide solutions and method of making same
US6838572B2 (en) * 2002-09-30 2005-01-04 Degussa Ag Process for the epoxidation of olefins
US7169945B2 (en) * 2002-11-26 2007-01-30 Degussa Ag Process for the epoxidation of olefins
ES2319993T3 (es) 2003-08-19 2009-05-18 Shell Internationale Research Maatschappij B.V. Procedimiento de preparacion de oxido de alquileno.
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
MX2009012234A (es) 2007-05-11 2010-03-26 Barry J Billig Activacion de catalizadores de alta selectividad en plantas de oxido de olefina.
TW201332982A (zh) 2011-11-04 2013-08-16 Dow Global Technologies Llc 用於製造環氧化物的方法及系統
CN104107728B (zh) * 2013-04-16 2017-04-19 中国石油化工股份有限公司 固体环氧化催化剂的再生方法
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

Family Cites Families (14)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3010807A (en) * 1958-09-10 1961-11-28 Chemical Construction Corp Multi-stage catalytic conversion
US3109864A (en) * 1961-09-26 1963-11-05 Halcon International Inc Oxidation of hydrocarbons
US3351635A (en) * 1966-03-14 1967-11-07 Halcon International Inc Epoxidation process
JPS5030049B1 (pt) * 1969-04-02 1975-09-29
US4367342A (en) * 1969-04-02 1983-01-04 Shell Oil Company Olefin epoxidation
US3849451A (en) * 1970-06-30 1974-11-19 Halcon International Inc Epoxidation process
US3829392A (en) * 1970-10-01 1974-08-13 Shell Oil Co Heterogeneous catalysts for olefin epoxidation
US3976713A (en) * 1971-06-11 1976-08-24 Sun Oil Company Of Pennsylvania Isoparaffin-olefin alkylation utilizing recycle streams and multiple packed catalyst beds
US4021454A (en) * 1971-08-19 1977-05-03 Shell Oil Company Olefin epoxidation
US3923843A (en) * 1972-03-13 1975-12-02 Shell Oil Co Epoxidation process with improved heterogeneous catalyst
GB8613354D0 (en) * 1986-06-03 1986-07-09 Davy Mckee Ltd Process
GB8729555D0 (en) * 1987-12-18 1988-02-03 Shell Int Research Alkylation process
US5183556A (en) * 1991-03-13 1993-02-02 Abb Lummus Crest Inc. Production of diesel fuel by hydrogenation of a diesel feed
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
CA2278666A1 (en) 1998-07-30
KR100471930B1 (ko) 2005-03-07
AU6616298A (en) 1998-08-18
EP1017487A1 (en) 2000-07-12
KR20000070421A (ko) 2000-11-25
CA2278666C (en) 2005-09-20
CN1110359C (zh) 2003-06-04
DE69803082D1 (de) 2002-01-31
WO1998032530A1 (en) 1998-07-30
DE69803082T2 (de) 2002-08-01
JP2002509530A (ja) 2002-03-26
ES2165148T3 (es) 2002-03-01
US5760253A (en) 1998-06-02
CN1244816A (zh) 2000-02-16
EP1017487B1 (en) 2001-12-19
JP4287910B2 (ja) 2009-07-01

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Legal Events

Date Code Title Description
B08F Application dismissed because of non-payment of annual fees [chapter 8.6 patent gazette]

Free format text: REFERENTE A 7,8A E 9A ANUIDADES.

B08K Patent lapsed as no evidence of payment of the annual fee has been furnished to inpi [chapter 8.11 patent gazette]

Free format text: REFERENTE AO DESPACHO 8.6 PUBLICADO NA RPI 1888 DE 13/03/2007.