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ES2126296T3 - Dispositivo para oxicloracion y su utilizacion - Google Patents

Dispositivo para oxicloracion y su utilizacion

Info

Publication number
ES2126296T3
ES2126296T3 ES95924203T ES95924203T ES2126296T3 ES 2126296 T3 ES2126296 T3 ES 2126296T3 ES 95924203 T ES95924203 T ES 95924203T ES 95924203 T ES95924203 T ES 95924203T ES 2126296 T3 ES2126296 T3 ES 2126296T3
Authority
ES
Spain
Prior art keywords
gases
flow
wall
catalyzing
nozzles
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
ES95924203T
Other languages
English (en)
Inventor
Reinhard Krumbock
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.)
Vinnolit Monomer GmbH and Co KG
Original Assignee
Vinnolit Monomer GmbH and Co KG
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 Vinnolit Monomer GmbH and Co KG filed Critical Vinnolit Monomer GmbH and Co KG
Application granted granted Critical
Publication of ES2126296T3 publication Critical patent/ES2126296T3/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
    • 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
    • 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
    • B01J8/1818—Feeding of the fluidising gas
    • B01J8/1827—Feeding of the fluidising gas the fluidising gas being a reactant
    • 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
    • B01J8/1818—Feeding of the fluidising gas
    • 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
    • B01J8/1836—Heating and cooling the reactor
    • 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
    • C07C17/15—Preparation of halogenated hydrocarbons by replacement by halogens with oxygen as auxiliary reagent, e.g. oxychlorination
    • C07C17/152—Preparation of halogenated hydrocarbons by replacement by halogens with oxygen as auxiliary reagent, e.g. oxychlorination of hydrocarbons
    • C07C17/156—Preparation of halogenated hydrocarbons by replacement by halogens with oxygen as auxiliary reagent, e.g. oxychlorination of hydrocarbons of unsaturated hydrocarbons
    • 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
    • B01J2208/00115—Controlling the temperature by indirect heat exchange with heat exchange elements inside the bed of solid particles
    • B01J2208/00141—Coils

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Combustion & Propulsion (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)
  • Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)

Abstract

LA PRODUCCION DE 1,2 ACIDO CLORHIDRICO Y OXIGENO U OTRO GAS QUE CONTENGA OXIGENO (OXICLORACION) SE REALIZA DE FORMA VENTAJOSA EN UN REACTOR CON UNA PARED INFERIOR PARA UN LECHO FLUIDIFICADO CATALIZADOR. POR ENCIMA DE LA PARED Y DENTRO DEL LECHO FLUIDIFICADO CATALIZADOR SE SITUA UNA PRIMERA ENTRADA DE GAS (TUBOS DE DISTRIBUCION)(4) QUE CUENTA CON TOBERAS (5) DISTRIBUIDAS A LO LARGO DE TODA LA SECCION DEL REACTOR. ESTAS TOBERAS (5), A SU VEZ, TERMINAN EN TUBOS (6) QUE CONDUCEN EL FLUJO DE GASES DE SALIDA EN DIRECCION OPUESTA AL FLUJO DE GASES QUE FLUIDIFICA EL CATALIZADOR. ESTE ULTIMO FLUJO DE GASES ES INTRODUCIDO POR UNA SEGUNDA ENTRADA DE GASES (7) SITUADA DEBAJO DE LA PARED.
ES95924203T 1995-02-20 1995-05-17 Dispositivo para oxicloracion y su utilizacion Expired - Lifetime ES2126296T3 (es)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
DE19505664A DE19505664C2 (de) 1995-02-20 1995-02-20 Vorrichtung und ihre Verwendung zur Oxichlorierung

Publications (1)

Publication Number Publication Date
ES2126296T3 true ES2126296T3 (es) 1999-03-16

Family

ID=7754432

Family Applications (1)

Application Number Title Priority Date Filing Date
ES95924203T Expired - Lifetime ES2126296T3 (es) 1995-02-20 1995-05-17 Dispositivo para oxicloracion y su utilizacion

Country Status (21)

Country Link
EP (1) EP0810902B1 (es)
JP (1) JPH11500062A (es)
KR (1) KR100368512B1 (es)
CN (1) CN1089026C (es)
AU (1) AU702305B2 (es)
BG (1) BG62436B1 (es)
BR (1) BR9510383A (es)
CA (1) CA2213446C (es)
CZ (1) CZ289342B6 (es)
DE (2) DE19505664C2 (es)
ES (1) ES2126296T3 (es)
HU (1) HU221883B1 (es)
IN (1) IN188066B (es)
NO (1) NO973714L (es)
PL (1) PL180784B1 (es)
RO (1) RO118119B1 (es)
RU (1) RU2157726C2 (es)
SK (1) SK282850B6 (es)
UA (1) UA42056C2 (es)
WO (1) WO1996026003A1 (es)
ZA (1) ZA961278B (es)

Families Citing this family (22)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE19753165B4 (de) 1997-12-01 2006-10-19 Vinnolit Monomer Gmbh & Co. Kg Verfahren zur Herstellung von 1,2-Dichlorethan durch Oxichlorierung
DE19849709C2 (de) * 1998-10-28 2000-09-14 Krupp Uhde Gmbh Verfahren und Wirbelschicht-Reaktor zur Oxichlorierung von Ethylen, Sauerstoff und HCl
DE19903335A1 (de) * 1999-01-28 2000-08-17 Vinnolit Monomer Gmbh & Co Kg Verfahren für die Herstellung von 1,2-Dichlorethan aus der Oxichlorierung
DE19911078A1 (de) * 1999-03-12 2000-09-21 Krupp Uhde Gmbh Verfahren zur Herstellung von VCM
US6991767B1 (en) * 2000-09-18 2006-01-31 Procedyne Corp. Fluidized bed gas distributor system for elevated temperature operation
DE10258180A1 (de) * 2002-12-12 2004-06-24 Basf Ag Verfahren zur Herstellung von Chlor durch Gasphasenoxidation von Chlorwasserstoff
RU2359747C2 (ru) * 2003-05-09 2009-06-27 ИНЕОС ЮЭсЭй ЭлЭлСи Реакторное устройство
US7488601B2 (en) 2003-06-20 2009-02-10 Roche Diagnostic Operations, Inc. System and method for determining an abused sensor during analyte measurement
CA2541295A1 (en) * 2003-10-15 2005-04-28 Basf Aktiengesellschaft Catalytic bulk material having catalytically inactive shaped bodies that are rounded off on the external friction surfaces
MY140160A (en) 2004-01-28 2009-11-30 Shell Int Research Heat exchanger for carrying out an exothermic reaction
AU2005218950B2 (en) * 2004-03-08 2008-09-04 Shell Internationale Research Maatschappij B.V. Gas distributor for a reactor
BRPI0620401A2 (pt) * 2005-12-23 2011-11-16 Siemens Vai Metals Tech Gmbh fundo distribuidor
CN100435928C (zh) * 2006-09-20 2008-11-26 浙江大学 一种气体分布器
DE102006049546A1 (de) * 2006-10-20 2008-04-30 Vinnolit Gmbh & Co.Kg Profitcenter Vintec Vorrichtung und Verfahren zur Oxichlorierung
DE102008048526A1 (de) * 2008-09-23 2010-04-01 Uhde Gmbh Verfahren zur Nutzung der im Herstellungsprozess von 1,2-Dichlorethan aus Ethylen in einem Wirbelschichtreaktor anfallenden Reaktionswärme
US8092755B2 (en) * 2009-04-06 2012-01-10 Lummus Technology Inc. Devices for injection of gaseous streams into a bed of fluidized solids
US20150064089A1 (en) * 2013-08-29 2015-03-05 Honeywell International Inc. Fluidized bed reactors including conical gas distributors and related methods of fluorination
CN104941524B (zh) * 2014-03-31 2020-11-03 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
CN105727846B (zh) * 2016-01-29 2019-02-05 清华大学 导流式喷动床和导流式喷动流化床
JP6373523B1 (ja) * 2017-06-19 2018-08-15 旭化成株式会社 化合物の製造方法
JP7689121B2 (ja) * 2019-11-20 2025-06-05 中国石油化工股▲ふん▼有限公司 ガス分配板、流動層反応器及びアンモ酸化の方法
KR20230076022A (ko) * 2021-11-23 2023-05-31 주식회사 엘지화학 기포탑 반응기

Family Cites Families (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB1265770A (es) * 1969-07-01 1972-03-08
US4436507A (en) * 1981-07-16 1984-03-13 Foster Wheeler Energy Corporation Fluidized bed reactor utilizing zonal fluidization and anti-mounding air distributors
US4801731A (en) * 1987-12-14 1989-01-31 E. I. Du Pont De Nemours And Company Preparation of acrylonitrile
ES2051025T3 (es) * 1989-10-04 1994-06-01 Asahi Chemical Ind Aparato para la fabricacion de nitrilo alfa,beta no saturado.
DE9116161U1 (de) * 1991-12-07 1992-03-26 Hoechst Ag, 65929 Frankfurt Vorrichtung zur Herstellung von 1,2-Dichlorethan durch Oxichlorierung
DE4305001A1 (de) * 1993-02-18 1994-08-25 Hoechst Ag Vorrichtung zur Oxichlorierung

Also Published As

Publication number Publication date
NO973714D0 (no) 1997-08-12
UA42056C2 (uk) 2001-10-15
KR19980702341A (ko) 1998-07-15
EP0810902B1 (de) 1998-10-21
CZ289342B6 (cs) 2002-01-16
CZ265797A3 (cs) 1998-02-18
BG101745A (en) 1998-05-29
DE19505664C2 (de) 1996-12-12
HUT77918A (hu) 1998-10-28
AU2881095A (en) 1996-09-11
CA2213446C (en) 2002-01-29
ZA961278B (en) 1996-08-27
BR9510383A (pt) 1998-06-02
CA2213446A1 (en) 1996-08-29
HU221883B1 (hu) 2003-02-28
SK282850B6 (sk) 2002-12-03
MX9706276A (es) 1997-11-29
RU2157726C2 (ru) 2000-10-20
DE19505664A1 (de) 1996-08-29
WO1996026003A1 (de) 1996-08-29
SK113497A3 (en) 1998-01-14
JPH11500062A (ja) 1999-01-06
EP0810902A1 (de) 1997-12-10
BG62436B1 (bg) 1999-11-30
IN188066B (es) 2002-08-17
PL180784B1 (pl) 2001-04-30
DE59504023D1 (de) 1998-11-26
RO118119B1 (ro) 2003-02-28
CN1089026C (zh) 2002-08-14
CN1175219A (zh) 1998-03-04
NO973714L (no) 1997-08-12
KR100368512B1 (ko) 2003-03-26
PL321830A1 (en) 1997-12-22
AU702305B2 (en) 1999-02-18

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