CA2141712A1 - Dispositif pour la mise en oeuvre de reactions chimiques necessitant au moins au demarrage un apport de calories - Google Patents

Dispositif pour la mise en oeuvre de reactions chimiques necessitant au moins au demarrage un apport de calories

Info

Publication number
CA2141712A1
CA2141712A1 CA002141712A CA2141712A CA2141712A1 CA 2141712 A1 CA2141712 A1 CA 2141712A1 CA 002141712 A CA002141712 A CA 002141712A CA 2141712 A CA2141712 A CA 2141712A CA 2141712 A1 CA2141712 A1 CA 2141712A1
Authority
CA
Canada
Prior art keywords
heat exchange
reactor
reagent
axis
effluents
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.)
Granted
Application number
CA002141712A
Other languages
English (en)
Other versions
CA2141712C (fr
Inventor
Christian Busson
Henri Delhomme
Laure Gollion
Jean P. Cassagne
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.)
IFP Energies Nouvelles IFPEN
Engie SA
Original Assignee
Individual
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 Individual filed Critical Individual
Publication of CA2141712A1 publication Critical patent/CA2141712A1/fr
Application granted granted Critical
Publication of CA2141712C publication Critical patent/CA2141712C/fr
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Classifications

    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28—HEAT EXCHANGE IN GENERAL
    • F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F21/00—Constructions of heat-exchange apparatus characterised by the selection of particular materials
    • F28F21/04—Constructions of heat-exchange apparatus characterised by the selection of particular materials of ceramic; of concrete; of natural stone
    • 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
    • B01J12/007—Chemical processes in general for reacting gaseous media with gaseous media; Apparatus specially adapted therefor in the presence of catalytically active bodies, e.g. porous plates
    • 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
    • B01J19/0006—Controlling or regulating processes
    • B01J19/0013—Controlling the temperature of the process
    • 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
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C2/00—Preparation of hydrocarbons from hydrocarbons containing a smaller number of carbon atoms
    • C07C2/76—Preparation of hydrocarbons from hydrocarbons containing a smaller number of carbon atoms by condensation of hydrocarbons with partial elimination of hydrogen
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C4/00—Preparation of hydrocarbons from hydrocarbons containing a larger number of carbon atoms
    • C07C4/02—Preparation of hydrocarbons from hydrocarbons containing a larger number of carbon atoms by cracking a single hydrocarbon or a mixture of individually defined hydrocarbons or a normally gaseous hydrocarbon fraction
    • C07C4/04—Thermal processes
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23C—METHODS OR APPARATUS FOR COMBUSTION USING FLUID FUEL OR SOLID FUEL SUSPENDED IN  A CARRIER GAS OR AIR 
    • F23C3/00—Combustion apparatus characterised by the shape of the combustion chamber
    • F23C3/002—Combustion apparatus characterised by the shape of the combustion chamber the chamber having an elongated tubular form, e.g. for a radiant tube
    • 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
    • F28D7/10—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 arranged one within the other, e.g. concentrically
    • F28D7/12—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 arranged one within the other, e.g. concentrically the surrounding tube being closed at one end, e.g. return type
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28—HEAT EXCHANGE IN GENERAL
    • F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F13/00—Arrangements for modifying heat-transfer, e.g. increasing, decreasing
    • F28F13/06—Arrangements for modifying heat-transfer, e.g. increasing, decreasing by affecting the pattern of flow of the heat-exchange media
    • 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
    • B01J2219/00054—Controlling or regulating the heat exchange system
    • B01J2219/00056—Controlling or regulating the heat exchange system involving measured parameters
    • B01J2219/00058—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
    • 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
    • B01J2219/00081—Tubes
    • 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
    • B01J2219/0015—Controlling the temperature by thermal insulation means
    • B01J2219/00155—Controlling the temperature by thermal insulation means using insulating materials or refractories
    • 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
    • B01J2219/00157—Controlling the temperature by means of a burner

Abstract

Dispositif comprenant un réacteur (1) de forme allongée selon un axe, de préférence à section carrée ou rectangulaire, comportant à une première extrémité au moins unmoyen d'alimentation en au moins un réactif, à l'extrémité opposée au moins un moyen d'évacuation des effluents produits ledit réacteur comprenant dans une première zone (côté première extrémité) une pluralité de moyens d'échange de chaleur (3),lesdits moyens d'échange de chaleur (3), sensiblement parallèles entre eux, étant disposés en nappes sensiblement parallèles, perpendiculaires à l'axe du réacteur de façon à définir entre lesdits moyens et/ou les nappes formées par ces moyens desespaces ou passages pour la circulation du ou des réactifs et/ou des effluents, lesdits moyens d'échange de chaleur (3) étant adaptés à échanger de la chaleur dans lesdits passages par sections transversales successives, indépendantes et sensiblement perpendiculaires à l'axe du réacteur, ledit dispositif étant tel que certains au moins des moyens d'échange de chaleur (3) comprennent un tube, formé d'au moins une enveloppe, alimenté en gaz ou mélange de gaz d'échange de chaleur et comportant au moins un moyen d'évacuation dudit gaz ou mélange de gaz ayant échangé de la chaleur avec le ou les réactifs et/ou effluents circulant à l'extérieur dudit moyen d'échange de chaleur (3).
CA002141712A 1994-02-02 1995-02-02 Dispositif pour la mise en oeuvre de reactions chimiques necessitant au moins au demarrage un apport de calories Expired - Fee Related CA2141712C (fr)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
FR9401243 1994-02-02
FR9401243A FR2715583B1 (fr) 1994-02-02 1994-02-02 Dispositif pour la mise en Óoeuvre de réactions chimiques nécessitant au moins au démarrage un apport de calories.

Publications (2)

Publication Number Publication Date
CA2141712A1 true CA2141712A1 (fr) 1995-08-03
CA2141712C CA2141712C (fr) 2005-01-18

Family

ID=9459761

Family Applications (1)

Application Number Title Priority Date Filing Date
CA002141712A Expired - Fee Related CA2141712C (fr) 1994-02-02 1995-02-02 Dispositif pour la mise en oeuvre de reactions chimiques necessitant au moins au demarrage un apport de calories

Country Status (11)

Country Link
US (1) US5554347A (fr)
EP (1) EP0666104B1 (fr)
JP (1) JP3697558B2 (fr)
KR (1) KR100364384B1 (fr)
AU (1) AU696504B2 (fr)
CA (1) CA2141712C (fr)
DE (1) DE69505857T2 (fr)
FR (1) FR2715583B1 (fr)
MY (1) MY129215A (fr)
NO (1) NO306658B1 (fr)
RU (1) RU2137539C1 (fr)

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FR2743007B1 (fr) 1995-12-27 1998-01-30 Inst Francais Du Petrole Procede de pyrolyse et de decokage en continu applicable notamment a la production d'acetylene
FR2748273B1 (fr) * 1996-05-06 1998-06-26 Inst Francais Du Petrole Procede et dispositif de conversion thermique d'hydrocarbures en hydrocarbures aliphatiques plus insatures que les produits de depart, combinant une etape de vapocraquage et une etape de pyrolyse
DE29716862U1 (de) * 1997-09-19 1999-01-28 Bleickert Gerhard Einrichtung zum Führen der Brennergase in einem Ofen
DE19741409A1 (de) * 1997-09-19 1999-03-25 Gerhard Bleickert Ofen zur Verschwelung von Feststoffen, bspw. Müll
PL191124B1 (pl) * 1997-10-08 2006-03-31 Shell Int Research Sposób doprowadzania ciepła do procesu z zastosowaniem komory reakcji utleniania bezpłomieniowego podgrzewacza procesowego i bezpłomieniowy podgrzewacz procesowy
US6153150A (en) 1998-01-12 2000-11-28 Advanced Technology Materials, Inc. Apparatus and method for controlled decomposition oxidation of gaseous pollutants
US6100436A (en) * 1998-09-08 2000-08-08 Uop Llc Process and apparatus for controlling reaction temperatures with heating arrangement in series flow
US6602920B2 (en) 1998-11-25 2003-08-05 The Texas A&M University System Method for converting natural gas to liquid hydrocarbons
FR2786779B1 (fr) 1998-12-04 2001-04-20 Inst Francais Du Petrole Procede de pyrolyse thermique d'une charge contenant de l'ethane
FR2791665B1 (fr) * 1999-03-31 2001-05-18 Inst Francais Du Petrole Procede de production de methylacetylene et de propadiene
US6641625B1 (en) 1999-05-03 2003-11-04 Nuvera Fuel Cells, Inc. Integrated hydrocarbon reforming system and controls
FR2802119B1 (fr) 1999-12-08 2002-04-12 Inst Francais Du Petrole Dispositif de liaison entre un tube destine au chauffage et/ ou au refroidissement d'un reacteur sous pression et ledit reacteur
US20020182132A1 (en) * 2000-10-04 2002-12-05 Lesieur Roger R. Fuel gas reformer assemblage
FR2821572B1 (fr) * 2001-03-05 2003-10-31 Inst Francais Du Petrole Dispositif de reacteur comportant une enceinte en materiau refractaire et une enveloppe de confinement, pour la mise en oeuvre de reactions chimiques necessitant un echange de chaleur
FR2828731B1 (fr) * 2001-08-14 2004-10-22 Inst Francais Du Petrole Installation de conversion chimique d'une charge presentant une surface reduite d'echange de chaleur
US6793699B2 (en) * 2001-09-05 2004-09-21 Dennis D. Coleman Continuous tracer generation apparatus
US7223602B2 (en) 2001-09-05 2007-05-29 Coleman Dennis D Continuous tracer generation method
FR2830205B1 (fr) 2001-09-28 2003-12-12 Inst Francais Du Petrole Enceinte reactionnelle comprenant une enveloppe contenant au moins un module relie par des moyens souples a l'enveloppe et contenant des moyens d'echange de chaleur
FR2844349B1 (fr) * 2002-09-06 2005-06-24 Nanotec Solution Detecteur de proximite par capteur capacitif
DE10313529A1 (de) * 2003-03-26 2004-10-14 Basf Ag Reaktor für Hochtemperaturreaktionen und Verwendung
JP2005018510A (ja) * 2003-06-27 2005-01-20 Hitachi Ltd データセンタシステム及びその制御方法
SE527766C2 (sv) * 2004-10-22 2006-05-30 Sandvik Intellectual Property Förfarande för förbränning med brännare för industriugnar, jämte brännare
US7293983B2 (en) * 2005-03-01 2007-11-13 Fina Technology, Inc. Heating hydrocarbon process flow using flameless oxidation burners
JP2008532747A (ja) * 2005-03-10 2008-08-21 シエル・インターナシヨネイル・リサーチ・マーチヤツピイ・ベー・ウイ 燃料の燃焼とプロセス流体の加熱のための伝熱システム及びその使用方法
PL1856443T3 (pl) * 2005-03-10 2016-01-29 Shell Int Research Wielorurowy układ wymiany ciepła do spalania paliwa i ogrzewania płynu technologicznego oraz jego zastosowanie
CN101163919B (zh) * 2005-03-10 2010-10-13 国际壳牌研究有限公司 用于启动燃料的无焰燃烧和处理流体直接加热的直接加热系统的方法
US7675430B2 (en) * 2005-08-02 2010-03-09 Warner Thomas P Device control module and method for controlling devices
CN101970346A (zh) * 2006-12-18 2011-02-09 硅之火股份公司 一种新型级联电厂工艺和在该电厂工艺中提供可逆使用的氢载体的方法
BRPI0814798A2 (pt) * 2007-07-20 2019-09-24 Shell Int Research aquecedor por combustão sem chama
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US9441887B2 (en) 2011-02-22 2016-09-13 Ensyn Renewables, Inc. Heat removal and recovery in biomass pyrolysis
US10041667B2 (en) * 2011-09-22 2018-08-07 Ensyn Renewables, Inc. Apparatuses for controlling heat for rapid thermal processing of carbonaceous material and methods for the same
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Also Published As

Publication number Publication date
NO306658B1 (no) 1999-12-06
KR100364384B1 (ko) 2003-02-05
CA2141712C (fr) 2005-01-18
AU696504B2 (en) 1998-09-10
FR2715583B1 (fr) 1996-04-05
JP3697558B2 (ja) 2005-09-21
AU1149595A (en) 1995-08-10
MY129215A (en) 2007-03-30
EP0666104A1 (fr) 1995-08-09
NO950363D0 (no) 1995-01-31
RU2137539C1 (ru) 1999-09-20
EP0666104B1 (fr) 1998-11-11
NO950363L (no) 1995-08-03
JPH07308571A (ja) 1995-11-28
DE69505857D1 (de) 1998-12-17
DE69505857T2 (de) 1999-04-15
FR2715583A1 (fr) 1995-08-04
US5554347A (en) 1996-09-10
RU95101388A (ru) 1997-01-27

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Legal Events

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Effective date: 20140204