ES2115388T3 - Reactor ciclonico. - Google Patents

Reactor ciclonico.

Info

Publication number
ES2115388T3
ES2115388T3 ES95924302T ES95924302T ES2115388T3 ES 2115388 T3 ES2115388 T3 ES 2115388T3 ES 95924302 T ES95924302 T ES 95924302T ES 95924302 T ES95924302 T ES 95924302T ES 2115388 T3 ES2115388 T3 ES 2115388T3
Authority
ES
Spain
Prior art keywords
reactor
sprayers
reagents
reaction area
mixing
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
ES95924302T
Other languages
English (en)
Inventor
Paul Marie Ayoub
Jean Charles Ginestra
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.)
SHELL INT RESEARCH
Shell Internationale Research Maatschappij BV
Original Assignee
SHELL INT RESEARCH
Shell Internationale Research Maatschappij BV
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 SHELL INT RESEARCH, Shell Internationale Research Maatschappij BV filed Critical SHELL INT RESEARCH
Application granted granted Critical
Publication of ES2115388T3 publication Critical patent/ES2115388T3/es
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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
    • 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
    • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F25/00—Flow mixers; Mixers for falling materials, e.g. solid particles
    • B01F25/10—Mixing by creating a vortex flow, e.g. by tangential introduction of flow components
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F25/00—Flow mixers; Mixers for falling materials, e.g. solid particles
    • B01F25/20—Jet mixers, i.e. mixers using high-speed fluid streams
    • B01F25/23—Mixing by intersecting jets
    • 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
    • B01J12/00—Chemical processes in general for reacting gaseous media with gaseous media; Apparatus specially adapted therefor
    • 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
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J4/00—Feed or outlet devices; Feed or outlet control devices
    • B01J4/001—Feed or outlet devices as such, e.g. feeding tubes
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C17/00—Preparation of halogenated hydrocarbons
    • C07C17/093—Preparation of halogenated hydrocarbons by replacement by halogens
    • C07C17/10—Preparation of halogenated hydrocarbons by replacement by halogens of hydrogen atoms
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F23/00—Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
    • B01F23/10—Mixing gases with gases
    • 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
    • B01J2219/00162—Controlling or regulating processes controlling the 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
    • B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/00049—Controlling or regulating processes
    • B01J2219/00164—Controlling or regulating processes controlling the flow
    • B01J2219/00166—Controlling or regulating processes controlling the 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
    • Y02P20/00—Technologies relating to chemical industry
    • Y02P20/50—Improvements relating to the production of bulk chemicals
    • Y02P20/582—Recycling of unreacted starting or intermediate materials

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Physical Or Chemical Processes And Apparatus (AREA)
  • Feeding, Discharge, Calcimining, Fusing, And Gas-Generation Devices (AREA)

Abstract

SE PRESENTA UN REACTOR (1) QUE TIENE UNA O MAS ENTRADAS DE REACTIVOS (2A) EN LAS QUE SE FIJAN UNOS ROCIADORES (3) Y UNA O MAS ENTRADAS DE REACTIVOS (2B) QUE TIENEN CADA UNA BOQUILLA DE INYECCION (5). LOS REACTIVOS SON INTRODUCIDOS EN UN REACTOR (1) A TRAVES DE LOS ROCIADORES (3) Y LAS BOQUILLAS (5) EN UNAS CONDICIONES EN LAS QUE SE CREA UN CARACTER CICLONICO TRIDIMENSIONAL EN UNA ZONA DE REACCION BIEN MEZCLADA (6). ESTO, JUNTO CON LA ENERGIA CON LA QUE LOS REACTIVOS SON INTRODUCIDOS EN LA ZONA DE REACCION (6), FACILITA LAS OPERACIONES DE MICROMEZCLADO Y MACROMEZCLADO. EL REACTOR (1) ES PARTICULARMENTE UTIL PARA REACTIVAR CLORO Y PROPILENO PARA OBTENER CLORURO ALILICO.
ES95924302T 1994-06-25 1995-06-20 Reactor ciclonico. Expired - Lifetime ES2115388T3 (es)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US08/264,825 US5518700A (en) 1994-06-25 1994-06-25 Cyclonic reactor

Publications (1)

Publication Number Publication Date
ES2115388T3 true ES2115388T3 (es) 1998-06-16

Family

ID=23007770

Family Applications (1)

Application Number Title Priority Date Filing Date
ES95924302T Expired - Lifetime ES2115388T3 (es) 1994-06-25 1995-06-20 Reactor ciclonico.

Country Status (12)

Country Link
US (1) US5518700A (es)
EP (1) EP0767704B1 (es)
JP (1) JPH10502014A (es)
KR (1) KR100383023B1 (es)
CN (1) CN1086309C (es)
AU (1) AU2886495A (es)
CA (1) CA2193835C (es)
DE (1) DE69502284T2 (es)
ES (1) ES2115388T3 (es)
PL (1) PL179364B1 (es)
TW (1) TW284703B (es)
WO (1) WO1996000126A1 (es)

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US7582793B2 (en) 2004-09-02 2009-09-01 Eastman Chemical Company Optimized liquid-phase oxidation
US7608732B2 (en) 2005-03-08 2009-10-27 Eastman Chemical Company Optimized liquid-phase oxidation
US7572936B2 (en) 2004-09-02 2009-08-11 Eastman Chemical Company Optimized liquid-phase oxidation
US7568361B2 (en) * 2004-09-02 2009-08-04 Eastman Chemical Company Optimized liquid-phase oxidation
US7495125B2 (en) 2004-09-02 2009-02-24 Eastman Chemical Company Optimized liquid-phase oxidation
US7692036B2 (en) 2004-11-29 2010-04-06 Eastman Chemical Company Optimized liquid-phase oxidation
US7608733B2 (en) 2004-09-02 2009-10-27 Eastman Chemical Company Optimized liquid-phase oxidation
US7381836B2 (en) * 2004-09-02 2008-06-03 Eastman Chemical Company Optimized liquid-phase oxidation
US7507857B2 (en) 2004-09-02 2009-03-24 Eastman Chemical Company Optimized liquid-phase oxidation
US7910769B2 (en) 2004-09-02 2011-03-22 Eastman Chemical Company Optimized liquid-phase oxidation
US7399882B2 (en) * 2004-09-02 2008-07-15 Eastman Chemical Company Optimized liquid-phase oxidation
US7683210B2 (en) * 2004-09-02 2010-03-23 Eastman Chemical Company Optimized liquid-phase oxidation
US7504535B2 (en) 2004-09-02 2009-03-17 Eastman Chemical Company Optimized liquid-phase oxidation
US20060047153A1 (en) * 2004-09-02 2006-03-02 Wonders Alan G Optimized liquid-phase oxidation
US7482482B2 (en) 2004-09-02 2009-01-27 Eastman Chemical Company Optimized liquid-phase oxidation
US7741515B2 (en) 2004-09-02 2010-06-22 Eastman Chemical Company Optimized liquid-phase oxidation
US7572932B2 (en) 2004-09-02 2009-08-11 Eastman Chemical Company Optimized liquid-phase oxidation
US7589231B2 (en) * 2004-09-02 2009-09-15 Eastman Chemical Company Optimized liquid-phase oxidation
US7692037B2 (en) 2004-09-02 2010-04-06 Eastman Chemical Company Optimized liquid-phase oxidation
JP2006297173A (ja) * 2005-04-15 2006-11-02 Hsp:Kk 液体混合装置
US7884232B2 (en) 2005-06-16 2011-02-08 Eastman Chemical Company Optimized liquid-phase oxidation
US8240908B2 (en) * 2005-09-01 2012-08-14 The Procter & Gamble Company Control system for and method of combining materials
US7355068B2 (en) 2006-01-04 2008-04-08 Eastman Chemical Company Oxidation system with internal secondary reactor
US20070248510A1 (en) * 2006-04-25 2007-10-25 Dean Anne M Dual gas-liquid spargers for catalytic processing units
US20070263483A1 (en) * 2006-05-10 2007-11-15 Kenrick Venett Introduction of additives into bulk polymer
US7726870B1 (en) * 2007-04-19 2010-06-01 Vortex Systems (International) Ci Method for mixing fluids with an eductor
CN101468300B (zh) * 2007-12-28 2013-04-17 亚泰半导体设备股份有限公司 桶槽漩流混合装置及方法
JP5604038B2 (ja) 2008-08-25 2014-10-08 株式会社日立製作所 反応装置及び反応プラント
CA2754888A1 (en) * 2009-03-13 2010-09-16 University Of Utah Research Foundation Fluid-sparged helical channel reactor and associated methods
CN101839395B (zh) * 2009-10-27 2012-10-24 梁法春 一种气液两相流均匀分配装置
CN102533311B (zh) * 2010-12-30 2014-08-06 中国石油天然气集团公司 一种轴流式超短接触旋流反应器
US20130037492A1 (en) 2011-08-09 2013-02-14 Severn Trent De Nora, Llc System and Method for Optimizing the Mixing of Hypochlorite with Ballast Water
CN103865570B (zh) * 2012-12-11 2016-05-11 中国石油化工集团公司 一种烷基化反应器及方法
EP2874029A1 (de) * 2013-11-15 2015-05-20 Bayer Technology Services GmbH Verfahren zum Betreiben einer zur Durchführung von wenigstens einer chemischen Reaktion eingerichteten Anlage
CN104941521A (zh) * 2014-03-31 2015-09-30 英尼奥斯欧洲股份公司 用于氨氧化反应器的进料分布器设计
CN106157770B (zh) * 2016-09-22 2022-03-04 陕西师范大学 甲烷和氯气取代反应装置及方法
CN106390708B (zh) * 2016-11-24 2019-03-29 东南大学 一种焦炉烟气脱硝的花瓣形喷氨装置
CN108176264B (zh) * 2018-01-04 2021-03-09 中国石油集团海洋工程有限公司 多相体系钻井液混合器
CN108816067B (zh) * 2018-08-06 2024-05-10 北京京诚科林环保科技有限公司 一种高温烟气快混装置
CN110681275B (zh) * 2019-10-15 2020-11-20 中国矿业大学 一种旋流搅拌混合装置及方法
CN113457572A (zh) * 2020-03-30 2021-10-01 中石油吉林化工工程有限公司 一种丙酮氰醇低温反应器
CN111760482B (zh) * 2020-07-14 2022-05-27 珠海格力智能装备有限公司 混合装置
CN114425286B (zh) * 2020-10-29 2023-10-10 中国石油化工股份有限公司 一种烯烃水合反应系统和烯烃水合方法
KR102630752B1 (ko) * 2021-01-25 2024-01-29 한화솔루션 주식회사 방향족 화합물의 염소화 반응 방법
CN115106023B (zh) * 2021-03-17 2024-04-02 中国石油化工股份有限公司 气液两相反应器及其应用和烃油加氢方法
CN113041871A (zh) * 2021-04-22 2021-06-29 昆明有色冶金设计研究院股份公司 一种免搅拌多相混合分配装置
AU2022256206B2 (en) * 2021-12-10 2024-02-22 Ekona Power Inc. Methods and systems for mixing fluids

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Also Published As

Publication number Publication date
CA2193835C (en) 2004-11-23
EP0767704A1 (en) 1997-04-16
AU2886495A (en) 1996-01-19
TW284703B (es) 1996-09-01
CA2193835A1 (en) 1996-01-04
PL317935A1 (en) 1997-04-28
WO1996000126A1 (en) 1996-01-04
CN1151126A (zh) 1997-06-04
KR100383023B1 (ko) 2003-07-22
DE69502284T2 (de) 1998-08-20
KR970703809A (ko) 1997-08-09
PL179364B1 (pl) 2000-08-31
DE69502284D1 (de) 1998-06-04
EP0767704B1 (en) 1998-04-29
CN1086309C (zh) 2002-06-19
US5518700A (en) 1996-05-21
JPH10502014A (ja) 1998-02-24

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