NO20070322L - Fremgangsmate og innretning for a produsere 1,2-dickloretan ved hjelp av direkte klorinering - Google Patents

Fremgangsmate og innretning for a produsere 1,2-dickloretan ved hjelp av direkte klorinering

Info

Publication number
NO20070322L
NO20070322L NO20070322A NO20070322A NO20070322L NO 20070322 L NO20070322 L NO 20070322L NO 20070322 A NO20070322 A NO 20070322A NO 20070322 A NO20070322 A NO 20070322A NO 20070322 L NO20070322 L NO 20070322L
Authority
NO
Norway
Prior art keywords
dichloroethane
dissolved
gaseous
loop
feed point
Prior art date
Application number
NO20070322A
Other languages
English (en)
Other versions
NO340146B1 (no
Inventor
Harald Hafenscher
Michael Benje
Original Assignee
Vinnolit Gmbh & 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 Gmbh & Co Kg filed Critical Vinnolit Gmbh & Co Kg
Publication of NO20070322L publication Critical patent/NO20070322L/no
Publication of NO340146B1 publication Critical patent/NO340146B1/no

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F23/00Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
    • B01F23/20Mixing gases with liquids
    • B01F23/23Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids
    • B01F23/232Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids using flow-mixing means for introducing the gases, e.g. baffles
    • B01F23/2323Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids using flow-mixing means for introducing the gases, e.g. baffles by circulating the flow in guiding constructions or conduits
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J19/00Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J19/24Stationary reactors without moving elements inside
    • B01J19/2415Tubular reactors
    • B01J19/2435Loop-type reactors
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J8/00Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/18Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles
    • B01J8/20Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles with liquid as a fluidising medium
    • B01J8/22Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles with liquid as a fluidising medium gas being introduced into the liquid
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C17/00Preparation of halogenated hydrocarbons
    • C07C17/013Preparation of halogenated hydrocarbons by addition of halogens
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C17/00Preparation of halogenated hydrocarbons
    • C07C17/013Preparation of halogenated hydrocarbons by addition of halogens
    • C07C17/02Preparation of halogenated hydrocarbons by addition of halogens to unsaturated hydrocarbons
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F25/00Flow mixers; Mixers for falling materials, e.g. solid particles
    • B01F25/40Static mixers
    • B01F25/42Static mixers in which the mixing is affected by moving the components jointly in changing directions, e.g. in tubes provided with baffles or obstructions
    • B01F25/43Mixing tubes, e.g. wherein the material is moved in a radial or partly reversed direction
    • B01F25/431Straight mixing tubes with baffles or obstructions that do not cause substantial pressure drop; Baffles therefor
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2208/00Processes carried out in the presence of solid particles; Reactors therefor
    • B01J2208/00796Details of the reactor or of the particulate material
    • B01J2208/00823Mixing elements
    • B01J2208/00831Stationary elements
    • B01J2208/0084Stationary elements inside the bed, e.g. baffles

Landscapes

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

Abstract

Det beskrives en fremgangsmåte for fremstilling av høyren 1,2-dikloretan fra oppløst klor og oppløst etylen, som bringes i kontakt med hverandre i et sirkulerende flytende reaksjonsfluid som i det vesentlige består av 1,2-dikloretan og en katalysator og som strømmer gjennom minst et vertikalt anordnet løkketype reaksjonsavsnitt. I den angitte anordning er begge ben av løkken forbundet med en topp avgassingsbeholder hvorfra reaksjonsproduktet trekkes av enten i gassformig eller i flytende tilstand eller i både gassformig og flytende tilstand, og tallrike blandeavsnitt er anordnet i det ben av løkken der væsken stiger, og hvert av disse blandeavsnitt har et oppstrøms fødepunkt for oppløst eller gassformig etylen og et nedstrøms fødepunkt for oppløst klor og, hvis nødvendig, har blandeavsnittede statiske blandere.
NO20070322A 2004-06-17 2007-01-17 Fremgangsmåte og innretning for å fremstilling av 1,2-dikloretan ved direkte klorinering NO340146B1 (no)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
DE102004029147A DE102004029147B4 (de) 2004-06-17 2004-06-17 Verfahren und Vorrichtung zur Herstellung von 1,2-Dichlorethan mittels Direktchlorierung
PCT/EP2005/006437 WO2005123635A1 (de) 2004-06-17 2005-06-15 Verfahren und vorrichtung zur herstellung von 1,2-dichlorethan mittels direktchlorierung

Publications (2)

Publication Number Publication Date
NO20070322L true NO20070322L (no) 2007-01-17
NO340146B1 NO340146B1 (no) 2017-03-13

Family

ID=35115974

Family Applications (1)

Application Number Title Priority Date Filing Date
NO20070322A NO340146B1 (no) 2004-06-17 2007-01-17 Fremgangsmåte og innretning for å fremstilling av 1,2-dikloretan ved direkte klorinering

Country Status (13)

Country Link
US (1) US7579509B2 (no)
EP (1) EP1756026B1 (no)
JP (1) JP5419350B2 (no)
KR (1) KR101225389B1 (no)
CN (2) CN101555189A (no)
AT (1) ATE425944T1 (no)
DE (2) DE102004029147B4 (no)
NO (1) NO340146B1 (no)
PL (1) PL1756026T3 (no)
RU (1) RU2384556C2 (no)
TW (1) TWI491440B (no)
UA (1) UA88906C2 (no)
WO (1) WO2005123635A1 (no)

Families Citing this family (25)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE102004063090A1 (de) * 2004-12-22 2006-07-06 Uhde Gmbh Verfahren zur Herstellung von 1,2-Dichlorethan mittels Direktchlorierung
SE530767C2 (sv) 2006-10-03 2008-09-09 Alfa Laval Corp Ab Värmeväxlarreaktor med blandningszoner och användning av värmeväxlarreaktorn
DE102008020386B4 (de) 2008-04-23 2012-01-26 Uhde Gmbh Vorrichtung und Verfahren zur Herstellung eines chlorierten Alkans
US9133079B2 (en) 2012-01-13 2015-09-15 Siluria Technologies, Inc. Process for separating hydrocarbon compounds
CA2874526C (en) 2012-05-24 2022-01-18 Siluria Technologies, Inc. Oxidative coupling of methane systems and methods
US9969660B2 (en) 2012-07-09 2018-05-15 Siluria Technologies, Inc. Natural gas processing and systems
US9598328B2 (en) 2012-12-07 2017-03-21 Siluria Technologies, Inc. Integrated processes and systems for conversion of methane to multiple higher hydrocarbon products
EP3074119B1 (en) 2013-11-27 2019-01-09 Siluria Technologies, Inc. Reactors and systems for oxidative coupling of methane
CA3123783A1 (en) 2014-01-08 2015-07-16 Lummus Technology Llc Ethylene-to-liquids systems and methods
US10377682B2 (en) 2014-01-09 2019-08-13 Siluria Technologies, Inc. Reactors and systems for oxidative coupling of methane
EP3097068A4 (en) 2014-01-09 2017-08-16 Siluria Technologies, Inc. Oxidative coupling of methane implementations for olefin production
DE102014214872A1 (de) * 2014-07-29 2016-02-04 Thyssenkrupp Ag Verfahren und eine Vorrichtung zur Synthese von 1,2-Dichlorethan
CN104262077B (zh) * 2014-09-29 2016-08-24 中国海洋石油总公司 并联环管型直接氯化生产1,2-二氯乙烷的装置
US10793490B2 (en) 2015-03-17 2020-10-06 Lummus Technology Llc Oxidative coupling of methane methods and systems
US9334204B1 (en) 2015-03-17 2016-05-10 Siluria Technologies, Inc. Efficient oxidative coupling of methane processes and systems
US20160289143A1 (en) 2015-04-01 2016-10-06 Siluria Technologies, Inc. Advanced oxidative coupling of methane
WO2016205411A2 (en) 2015-06-16 2016-12-22 Siluria Technologies, Inc. Ethylene-to-liquids systems and methods
US9328297B1 (en) 2015-06-16 2016-05-03 Siluria Technologies, Inc. Ethylene-to-liquids systems and methods
US20170107162A1 (en) 2015-10-16 2017-04-20 Siluria Technologies, Inc. Separation methods and systems for oxidative coupling of methane
CA3019396A1 (en) 2016-04-13 2017-10-19 Siluria Technologies, Inc. Oxidative coupling of methane for olefin production
CA3029840C (en) * 2016-07-05 2023-09-26 Ineos Americas, Llc Method and apparatus for recovering absorbing agents in acid gas treatment
WO2018118105A1 (en) 2016-12-19 2018-06-28 Siluria Technologies, Inc. Methods and systems for performing chemical separations
ES2960342T3 (es) 2017-05-23 2024-03-04 Lummus Technology Inc Integración de procedimientos de acoplamiento oxidativo del metano
WO2019010498A1 (en) 2017-07-07 2019-01-10 Siluria Technologies, Inc. SYSTEMS AND METHODS FOR OXIDIZING METHANE COUPLING
KR102025186B1 (ko) * 2017-09-27 2019-09-25 한화케미칼 주식회사 1,1,2-트리클로로에탄의 제조 방법

Family Cites Families (14)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2211427B1 (no) 1972-12-27 1976-10-29 Rhone Progil
DE2935884A1 (de) * 1979-09-05 1981-04-02 Wacker-Chemie GmbH, 8000 München Verfahren zur herstellung von 1.2-dichlorethan
DE3340624C1 (de) 1983-11-10 1984-10-11 Dynamit Nobel Ag, 5210 Troisdorf Verfahren zur Herstellung von 1,2-Dichlorethan aus Ethylen und Chlorgas
JPS6128A (ja) * 1984-06-11 1986-01-06 Kanegafuchi Chem Ind Co Ltd 二塩化エタンの製造方法
DE3445896C1 (de) * 1984-12-15 1986-04-10 Dynamit Nobel Ag, 5210 Troisdorf Verfahren zur kontinuierlichen Herstellung von 1.2-Dichlorethan
FR2650678B1 (fr) 1989-08-04 1993-04-16 Aerospatiale Dispositif d'observation aerienne pour un sous-marin
DE4012529A1 (de) * 1990-04-19 1991-10-24 Wacker Chemie Gmbh Katalysatorsystem und verfahren zur herstellung von 1,2-dichlorethan durch chlorierung von ethylen unter einsatz dieses katalysatorsystems
JPH06157365A (ja) 1992-11-27 1994-06-03 Tosoh Corp 二塩化エタンの製造方法
TW442449B (en) 1996-07-04 2001-06-23 Hoechst Ag Process for preparing 1,2-dichloroethane by direct chlorination
DE19910964A1 (de) 1999-03-12 2000-09-21 Krupp Uhde Gmbh Verfahren zur Herstellung von Ethylendichlorid (EDC)
DE19953762C2 (de) * 1999-11-09 2003-07-10 Uhde Gmbh Verfahren zur Nutzung der bei der 1,2-Dichlorethan-Herstellung im Direktchlorierungsreaktor anfallenden Wärme
DE10207217C1 (de) * 2002-02-21 2003-03-27 Vinnolit Technologie Gmbh & Co Verfahren zur Herstellung von 1,2-Dichlorethan mittels Direktchlorierung
AU2002240549A1 (en) 2002-02-28 2003-09-16 Exxonmobile Chemical Patents Inc. _____________________________G Continuous slurry polymerization process in a loop reactor
BRPI0314282C8 (pt) 2002-09-13 2017-05-23 Chevron Phillips Chemical Co Lp aparelho reator de laço e processos de polimerização com múltiplos pontos de alimentação para olefinas e catalisadores

Also Published As

Publication number Publication date
DE102004029147B4 (de) 2008-01-03
KR20070028422A (ko) 2007-03-12
CN101555189A (zh) 2009-10-14
DE502005006880D1 (de) 2009-04-30
UA88906C2 (ru) 2009-12-10
CN1984858A (zh) 2007-06-20
EP1756026A1 (de) 2007-02-28
JP5419350B2 (ja) 2014-02-19
CN1984858B (zh) 2010-06-16
NO340146B1 (no) 2017-03-13
ATE425944T1 (de) 2009-04-15
US20080125613A1 (en) 2008-05-29
TW200610748A (en) 2006-04-01
JP2008502632A (ja) 2008-01-31
WO2005123635A1 (de) 2005-12-29
KR101225389B1 (ko) 2013-01-22
PL1756026T3 (pl) 2009-06-30
RU2384556C2 (ru) 2010-03-20
EP1756026B1 (de) 2009-03-18
US7579509B2 (en) 2009-08-25
DE102004029147A1 (de) 2006-01-12
RU2007101533A (ru) 2008-07-27
TWI491440B (zh) 2015-07-11

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