CO4920187A1 - Intercambiador de calor y metodo para utilizarlo - Google Patents

Intercambiador de calor y metodo para utilizarlo

Info

Publication number
CO4920187A1
CO4920187A1 CO98038304A CO98038304A CO4920187A1 CO 4920187 A1 CO4920187 A1 CO 4920187A1 CO 98038304 A CO98038304 A CO 98038304A CO 98038304 A CO98038304 A CO 98038304A CO 4920187 A1 CO4920187 A1 CO 4920187A1
Authority
CO
Colombia
Prior art keywords
chamber
heat exchanger
zone
container
dividing plates
Prior art date
Application number
CO98038304A
Other languages
English (en)
Inventor
John Wilson Kippax
Geoffrey Gerald Weedon
William Terence Woodfin
Original Assignee
Bp Exploration Operating
Kvaerner Process Tech Ltd
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 Bp Exploration Operating, Kvaerner Process Tech Ltd filed Critical Bp Exploration Operating
Publication of CO4920187A1 publication Critical patent/CO4920187A1/es

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
    • B01J19/0006—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
    • 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
    • B01J19/2425—Tubular reactors in parallel
    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B3/00—Hydrogen; Gaseous mixtures containing hydrogen; Separation of hydrogen from mixtures containing it; Purification of hydrogen
    • C01B3/02—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen
    • C01B3/32—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air
    • C01B3/34—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air by reaction of hydrocarbons with gasifying agents
    • C01B3/38—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air by reaction of hydrocarbons with gasifying agents using catalysts
    • C01B3/384—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air by reaction of hydrocarbons with gasifying agents using catalysts the catalyst being continuously externally heated
    • 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
    • F28D7/16—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 in parallel spaced relation
    • F28D7/163—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 in parallel spaced relation with conduit assemblies having a particular shape, e.g. square or annular; with assemblies of conduits having different geometrical features; with multiple groups of conduits connected in series or parallel and arranged inside common casing
    • F28D7/1653—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 in parallel spaced relation with conduit assemblies having a particular shape, e.g. square or annular; with assemblies of conduits having different geometrical features; with multiple groups of conduits connected in series or parallel and arranged inside common casing the conduit assemblies having a square or rectangular shape
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28—HEAT EXCHANGE IN GENERAL
    • F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F9/00—Casings; Header boxes; Auxiliary supports for elements; Auxiliary members within casings
    • F28F9/02—Header boxes; End plates
    • F28F9/0236—Header boxes; End plates floating elements
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28—HEAT EXCHANGE IN GENERAL
    • F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F9/00—Casings; Header boxes; Auxiliary supports for elements; Auxiliary members within casings
    • F28F9/22—Arrangements for directing heat-exchange media into successive compartments, e.g. arrangements of guide 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
    • 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
    • B01J2219/00761—Details of the reactor
    • B01J2219/00763—Baffles
    • B01J2219/00765—Baffles attached to the reactor wall
    • B01J2219/00777—Baffles attached to the reactor wall horizontal
    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B2203/00—Integrated processes for the production of hydrogen or synthesis gas
    • C01B2203/08—Methods of heating or cooling
    • C01B2203/0805—Methods of heating the process for making hydrogen or synthesis gas
    • C01B2203/0811—Methods of heating the process for making hydrogen or synthesis gas by combustion of fuel
    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B2203/00—Integrated processes for the production of hydrogen or synthesis gas
    • C01B2203/08—Methods of heating or cooling
    • C01B2203/0805—Methods of heating the process for making hydrogen or synthesis gas
    • C01B2203/0811—Methods of heating the process for making hydrogen or synthesis gas by combustion of fuel
    • C01B2203/0822—Methods of heating the process for making hydrogen or synthesis gas by combustion of fuel the fuel containing hydrogen
    • 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
    • Y02P20/10—Process efficiency

Abstract

Un intercambiador de calor comprende una pluralidad deprimeros tubos de intercambio térmico que se extiende a través del intercambiador, y a través de una pluralidad de cámaras del intercambiador de calor que se extiende lateralmente, teniendo cada cámara al menos una entrada de una primera cámara y al menos una salida a una segunda cámara adyacente axialmente, y teniendo cada cámara una pluralidad de zonas de interconexión transversales, cada una de las cuales está definida al menos por dos de dichos tubos, y al menos una primera zona tiene una entrada a dicha primera cámara y al menos una segunda zona, diferente de dicha primera zona, tiene una salida a dicha segunda cámara. También se incluyó un recipiente para el mezclado o distribución de los flujos de un primer fluido que pasa axialmente desde un emplazamiento situado aguas arriba hasta un emplazamiento situado aguas abajo, que comprende chapas divisorias transversales a través de dicho recipiente al menos en dos filas sucesivas, cuyas filas de chapas divisorias definen una cámara transversal abierta, teniendo las chapas divisorias en filas sucesivas una distribución espacial a través del recipiente. Con preferencia, el aparato tiene el intercambiador de calor con el distribuidor situado aguas abajo del mismo y todo el aparato es un reformador compacto.
CO98038304A 1997-07-08 1998-07-07 Intercambiador de calor y metodo para utilizarlo CO4920187A1 (es)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US5189897P 1997-07-08 1997-07-08

Publications (1)

Publication Number Publication Date
CO4920187A1 true CO4920187A1 (es) 2000-05-29

Family

ID=21974043

Family Applications (1)

Application Number Title Priority Date Filing Date
CO98038304A CO4920187A1 (es) 1997-07-08 1998-07-07 Intercambiador de calor y metodo para utilizarlo

Country Status (23)

Country Link
US (2) US6536513B1 (es)
EP (1) EP0927075B1 (es)
JP (1) JP4085290B2 (es)
KR (1) KR100431367B1 (es)
CN (1) CN1106216C (es)
AR (1) AR013189A1 (es)
AT (1) ATE272442T1 (es)
AU (1) AU8120898A (es)
BR (1) BR9806021B1 (es)
CA (1) CA2264837C (es)
CO (1) CO4920187A1 (es)
DE (1) DE69825408T2 (es)
DK (1) DK0927075T3 (es)
DZ (1) DZ2555A1 (es)
EA (1) EA001900B1 (es)
GE (1) GEP20022836B (es)
ID (1) ID21490A (es)
MY (1) MY122089A (es)
NO (1) NO323705B1 (es)
NZ (1) NZ334500A (es)
UA (1) UA61929C2 (es)
WO (1) WO1999002254A1 (es)
ZA (1) ZA985942B (es)

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EP2070896A1 (en) 2007-12-12 2009-06-17 BP p.l.c. A process for the conversion of n-butanol to di-isobutene and propene
EP2072489A1 (en) 2007-12-17 2009-06-24 BP p.l.c. Process for the conversion of hydrocarbons into ethanol
EP2072492A1 (en) 2007-12-17 2009-06-24 BP p.l.c. Process for the conversion of hydrocarbons to ethanol
EP2072490A1 (en) 2007-12-17 2009-06-24 BP p.l.c. Process for the conversion of hydrocarbons to alcohols
EP2072487A1 (en) 2007-12-17 2009-06-24 BP p.l.c. Process for the conversion of hydrocarbons to ethanol
EP2072486A1 (en) 2007-12-17 2009-06-24 BP p.l.c. Process for the conversion of hydrocarbons to ethanol
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CN102348953B (zh) * 2009-03-13 2014-08-27 开利公司 用于向热交换器分配流体的歧管组件
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Also Published As

Publication number Publication date
EA199900254A1 (ru) 1999-10-28
ID21490A (id) 1999-06-17
JP4085290B2 (ja) 2008-05-14
WO1999002254A1 (en) 1999-01-21
AR013189A1 (es) 2000-12-13
DK0927075T3 (da) 2004-12-06
MY122089A (en) 2006-03-31
DZ2555A1 (fr) 2003-02-15
BR9806021B1 (pt) 2010-06-29
DE69825408T2 (de) 2005-04-07
ZA985942B (en) 2000-01-10
US6536513B1 (en) 2003-03-25
GEP20022836B (en) 2002-11-25
DE69825408D1 (de) 2004-09-09
NZ334500A (en) 1999-10-28
CA2264837A1 (en) 1999-01-21
EP0927075B1 (en) 2004-08-04
BR9806021A (pt) 2006-02-14
US6609562B2 (en) 2003-08-26
JP2001500245A (ja) 2001-01-09
ATE272442T1 (de) 2004-08-15
CN1239443A (zh) 1999-12-22
KR100431367B1 (ko) 2004-05-14
CN1106216C (zh) 2003-04-23
AU8120898A (en) 1999-02-08
NO991041D0 (no) 1999-03-03
EP0927075A1 (en) 1999-07-07
NO323705B1 (no) 2007-06-25
UA61929C2 (en) 2003-12-15
KR20010029486A (ko) 2001-04-06
NO991041L (no) 1999-03-03
CA2264837C (en) 2006-08-15
EA001900B1 (ru) 2001-10-22
US20020038702A1 (en) 2002-04-04

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