ID18080A - Alat untuk melaksanakan reaksi kimia dengan kontinyu - Google Patents

Alat untuk melaksanakan reaksi kimia dengan kontinyu

Info

Publication number
ID18080A
ID18080A IDP972961A ID972961A ID18080A ID 18080 A ID18080 A ID 18080A ID P972961 A IDP972961 A ID P972961A ID 972961 A ID972961 A ID 972961A ID 18080 A ID18080 A ID 18080A
Authority
ID
Indonesia
Prior art keywords
tools
continuous
chemical reactions
implementing chemical
implementing
Prior art date
Application number
IDP972961A
Other languages
English (en)
Indonesian (id)
Inventor
Christof Herrmann
Wolfgang Hubinger
Jens Kremeskotter
Jurgen Schmidt-Thummes
Original Assignee
Basf Ag
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 Basf Ag filed Critical Basf Ag
Publication of ID18080A publication Critical patent/ID18080A/id

Links

Classifications

    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28—HEAT EXCHANGE IN GENERAL
    • F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
    • F28D7/00—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
    • F28D7/08—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits being otherwise bent, e.g. in a serpentine or zig-zag
    • 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
    • B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J19/24—Stationary reactors without moving elements inside
    • B01J19/2415—Tubular reactors
    • B01J19/243—Tubular reactors spirally, concentrically or zigzag wound
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F10/00—Homopolymers and copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28—HEAT EXCHANGE IN GENERAL
    • F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
    • F28D7/00—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
    • F28D7/08—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits being otherwise bent, e.g. in a serpentine or zig-zag
    • F28D7/082—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits being otherwise bent, e.g. in a serpentine or zig-zag with serpentine or zig-zag configuration
    • 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
    • B01J2219/00076—Controlling the temperature by indirect heating or cooling employing heat exchange fluids with heat exchange elements inside the reactor
    • B01J2219/00083—Coils

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Health & Medical Sciences (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Physical Or Chemical Processes And Apparatus (AREA)
IDP972961A 1996-08-26 1997-08-25 Alat untuk melaksanakan reaksi kimia dengan kontinyu ID18080A (id)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
DE19634450A DE19634450A1 (de) 1996-08-26 1996-08-26 Vorrichtung zur kontinuierlichen Durchführung chemischer Reaktionen

Publications (1)

Publication Number Publication Date
ID18080A true ID18080A (id) 1998-02-26

Family

ID=7803718

Family Applications (1)

Application Number Title Priority Date Filing Date
IDP972961A ID18080A (id) 1996-08-26 1997-08-25 Alat untuk melaksanakan reaksi kimia dengan kontinyu

Country Status (9)

Country Link
US (1) US6399031B1 (enExample)
EP (1) EP0944431B1 (enExample)
JP (1) JP2000516851A (enExample)
CN (1) CN1228717A (enExample)
AU (1) AU4207597A (enExample)
BR (1) BR9711230A (enExample)
DE (2) DE19634450A1 (enExample)
ID (1) ID18080A (enExample)
WO (1) WO1998008602A1 (enExample)

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DE10060372A1 (de) * 2000-12-05 2002-06-06 Basell Polyolefine Gmbh Vorrichtung zur Initiatoreinspeisung an Reaktoren
WO2002046266A2 (en) 2000-12-07 2002-06-13 Eastman Chemical Company Low cost polyester process using a pipe reactor
US6906164B2 (en) 2000-12-07 2005-06-14 Eastman Chemical Company Polyester process using a pipe reactor
DE10117275B4 (de) * 2001-04-06 2005-02-24 Hte Ag The High Throughput Experimentation Company Vorrichtung zur Archivierung und Analyse von Materialien
DE10125583A1 (de) * 2001-05-25 2002-11-28 Basf Ag Verfahren zur Herstellung von Homo- und Copolymeren des Isobutens
GB0306179D0 (en) * 2003-03-18 2003-04-23 Imp College Innovations Ltd Piping
US7135541B2 (en) * 2003-06-06 2006-11-14 Eastman Chemical Company Polyester process using a pipe reactor
US7074879B2 (en) * 2003-06-06 2006-07-11 Eastman Chemical Company Polyester process using a pipe reactor
WO2005010055A1 (ja) 2003-07-25 2005-02-03 Idemitsu Kosan Co., Ltd. ラジカル重合体の製造方法及び微細化学反応装置
US7332548B2 (en) 2004-03-04 2008-02-19 Eastman Chemical Company Process for production of a polyester product from alkylene oxide and carboxylic acid
WO2006020787A1 (en) * 2004-08-12 2006-02-23 E.I. Dupont De Nemours And Company Device and method of producing low molecular polymers
EP1632277A1 (en) * 2004-09-03 2006-03-08 Nederlandse Organisatie voor toegepast-natuurwetenschappelijk Onderzoek TNO Process and apparatus for carrying out crystallization
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CN101119512B (zh) * 2006-08-04 2012-07-18 鸿富锦精密工业（深圳）有限公司 使用移动设备进行工作处理的系统及方法
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US7649109B2 (en) * 2006-12-07 2010-01-19 Eastman Chemical Company Polyester production system employing recirculation of hot alcohol to esterification zone
US20080139780A1 (en) * 2006-12-07 2008-06-12 Debruin Bruce Roger Polyester production system employing short residence time esterification
US7943094B2 (en) 2006-12-07 2011-05-17 Grupo Petrotemex, S.A. De C.V. Polyester production system employing horizontally elongated esterification vessel
US7863477B2 (en) * 2007-03-08 2011-01-04 Eastman Chemical Company Polyester production system employing hot paste to esterification zone
JP5006413B2 (ja) * 2007-03-15 2012-08-22 ダウ グローバル テクノロジーズ エルエルシー 連続流反応器用ミキサー
JP5172946B2 (ja) * 2007-04-16 2013-03-27 ザ ジェネラル ホスピタル コーポレーション ドゥーイング ビジネス アズ マサチューセッツ ジェネラル ホスピタル マイクロチャネルにおける粒子集束のためのシステムおよび方法
US7847053B2 (en) 2007-07-12 2010-12-07 Eastman Chemical Company Multi-level tubular reactor with oppositely extending segments
US7829653B2 (en) 2007-07-12 2010-11-09 Eastman Chemical Company Horizontal trayed reactor
US7868129B2 (en) 2007-07-12 2011-01-11 Eastman Chemical Company Sloped tubular reactor with spaced sequential trays
US7872089B2 (en) 2007-07-12 2011-01-18 Eastman Chemical Company Multi-level tubular reactor with internal tray
US7872090B2 (en) 2007-07-12 2011-01-18 Eastman Chemical Company Reactor system with optimized heating and phase separation
US7868130B2 (en) 2007-07-12 2011-01-11 Eastman Chemical Company Multi-level tubular reactor with vertically spaced segments
US7858730B2 (en) * 2007-07-12 2010-12-28 Eastman Chemical Company Multi-level tubular reactor with dual headers
US7842777B2 (en) 2007-07-12 2010-11-30 Eastman Chemical Company Sloped tubular reactor with divided flow
EP2133141A1 (en) * 2008-06-10 2009-12-16 Nederlandse Organisatie voor Toegepast-Natuuurwetenschappelijk Onderzoek TNO Process for carrying out multi-phase reactions
GB0817219D0 (en) 2008-09-19 2008-10-29 Heliswirl Petrochemicals Ltd Cracking furnace
US8765217B2 (en) 2008-11-04 2014-07-01 Entrotech, Inc. Method for continuous production of (meth)acrylate syrup and adhesives therefrom
EP2357036B1 (en) * 2008-11-21 2017-09-27 LG Chem, Ltd. Method and apparatus for manufacturing polymer particle
EP2403633B1 (de) * 2009-03-06 2013-04-17 Ehrfeld Mikrotechnik BTS GmbH Koaxialer kompaktstatikmischer sowie dessen verwendung
US8329079B2 (en) 2009-04-20 2012-12-11 Entrochem, Inc. Method and apparatus for continuous production of partially polymerized compositions and polymers therefrom
FR2955039B1 (fr) * 2010-01-11 2012-10-19 Commissariat Energie Atomique Dispositif formant reacteur chimique a efficacite amelioree integrant un circuit d'echange thermique
JP5718028B2 (ja) * 2010-11-18 2015-05-13 古河電気工業株式会社 ２重管
SG2014010250A (en) * 2011-08-15 2014-08-28 Abbott Lab Process for manufacturing hmb and salts thereof
DE102012216945A1 (de) * 2012-09-21 2014-05-28 Ehrfeld Mikrotechnik Bts Gmbh Verfahren und Vorrichtung zur Herstellung organischer Peroxide mittels Millireaktionstechnik
EP2719452A1 (en) 2012-10-12 2014-04-16 Nederlandse Organisatie voor toegepast -natuurwetenschappelijk onderzoek TNO Method and apparatus for physical or chemical processes
CN102977279B (zh) * 2012-12-21 2014-12-31 北方华锦化学工业集团有限公司 用于制备连续本体abs树脂的含物料内循环的管式平推流反应器及制备方法
CN103349950B (zh) * 2013-07-02 2015-03-04 滨州裕能化工有限公司 一种用于制备nmp的油浴式反应器
EP2918294A1 (de) 2014-03-11 2015-09-16 Bayer Technology Services GmbH Vorrichtung und Verfahren zur kontinuierlichen Virusinaktivierung
DE102014111779A1 (de) * 2014-08-18 2016-02-18 Iva Industrieöfen Gmbh Verfahren zur Herstellung einer Retorte für einen Nitrierofen sowie Retorte
EP4481401A3 (en) 2015-02-24 2025-04-23 The University of British Columbia Continuous flow microfluidic system and method
JP2018525209A (ja) 2015-04-28 2018-09-06 ザ・ユニバーシティ・オブ・ブリティッシュ・コロンビア 使い捨てマイクロ流体カートリッジ
FR3042793B1 (fr) * 2015-10-26 2019-12-27 Arkema France Synthese de peroxydes organiques a l'aide d'un reacteur agite a ecoulement oscillatoire
EP3797860B1 (en) 2016-01-06 2025-07-30 The University of British Columbia Bifurcating mixers and methods of their use and manufacture
CA3115258A1 (en) 2018-10-08 2020-04-16 Boehringer Ingelheim International Gmbh Continuous flow reactor for viral inactivation
SG11202103443XA (en) * 2018-10-08 2021-05-28 Boehringer Ingelheim Int A novel continuous flow reactor for low ph viral inactivation
CN114478894B (zh) * 2021-12-31 2023-05-02 复旦大学 三氟氯乙烯共聚物的流动化学合成方法
CN114705063B (zh) * 2022-03-29 2024-04-02 张家港氢云新能源研究院有限公司 一种高效换热汽化器
DE102023117789A1 (de) 2023-07-06 2025-01-09 Technische Universität Dresden, Körperschaft des öffentlichen Rechts Verfahren zur kontinuierlichen Synthese von Polyoxazolinen mit einem Wendelrohrreaktor
CN118267946B (zh) * 2024-04-28 2024-11-22 深圳智微通科技有限公司 用于微反应器的反应模块

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Also Published As

Publication number Publication date
WO1998008602A1 (de) 1998-03-05
BR9711230A (pt) 1999-08-17
EP0944431A1 (de) 1999-09-29
DE59702114D1 (de) 2000-09-07
CN1228717A (zh) 1999-09-15
US6399031B1 (en) 2002-06-04
DE19634450A1 (de) 1998-03-05
EP0944431B1 (de) 2000-08-02
JP2000516851A (ja) 2000-12-19
AU4207597A (en) 1998-03-19

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