MX351529B - Sistema de intercambio de calor. - Google Patents

Sistema de intercambio de calor.

Info

Publication number
MX351529B
MX351529B MX2013013051A MX2013013051A MX351529B MX 351529 B MX351529 B MX 351529B MX 2013013051 A MX2013013051 A MX 2013013051A MX 2013013051 A MX2013013051 A MX 2013013051A MX 351529 B MX351529 B MX 351529B
Authority
MX
Mexico
Prior art keywords
heat exchange
interspace
fluid bath
exchange system
situated
Prior art date
Application number
MX2013013051A
Other languages
English (en)
Other versions
MX2013013051A (es
Inventor
Eugenio Basini Luca
Joachim Wilhelm Alfred
Original Assignee
Eni Spa
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 Eni Spa filed Critical Eni Spa
Publication of MX2013013051A publication Critical patent/MX2013013051A/es
Publication of MX351529B publication Critical patent/MX351529B/es

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
    • F28D15/00—Heat-exchange apparatus with the intermediate heat-transfer medium in closed tubes passing into or through the conduit walls ; Heat-exchange apparatus employing intermediate heat-transfer medium or bodies
    • 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
    • C01B3/386—Catalytic partial combustion
    • 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
    • C01B3/48—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 followed by reaction of water vapour with carbon monoxide
    • 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
    • F28D21/00—Heat-exchange apparatus not covered by any of the groups F28D1/00 - F28D20/00
    • F28D21/0017—Flooded core heat exchangers
    • 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
    • C01B2203/04—Integrated processes for the production of hydrogen or synthesis gas containing a purification step for the hydrogen or the synthesis gas
    • 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
    • C01B2203/0872—Methods of cooling
    • C01B2203/0883—Methods of cooling by indirect heat exchange
    • 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
    • C01B2203/0872—Methods of cooling
    • C01B2203/0888—Methods of cooling by evaporation of a fluid
    • C01B2203/0894—Generation of steam
    • 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
    • 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
    • Y02P20/129—Energy recovery, e.g. by cogeneration, H2recovery or pressure recovery turbines

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Organic Chemistry (AREA)
  • Combustion & Propulsion (AREA)
  • General Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Health & Medical Sciences (AREA)
  • General Health & Medical Sciences (AREA)
  • Inorganic Chemistry (AREA)
  • Physical Or Chemical Processes And Apparatus (AREA)
  • Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)

Abstract

La presente invención se refiere a un sistema de intercambio de calor que comprende: - un único aparato (N) que tiene un zona sumergida en un baño (N2) de fluido y un espacio (N1) libre en el cabezal en el que se acumula una fase vapor, - al menos un espacio (P) intermedio abierto en ambos extremos, situado en el interior de dicho aparato y sumergido completamente en el baño de fluido, - una o más superficies (6, 7, 8, 9, 10, 11) de intercambio de calor, estando dicho sistema caracterizado por que contiene todas las superficies de intercambio de calor en un único aparato y dichas superficies están sumergidas completamente en el baño de fluido y están conectadas de manera fluida a las fuentes de calor y de frío, externas a dicho sistema, a través de los flujos de materia. Al menos una de las superficies (6, 7, 8) de intercambio de calor está situada en el interior del espacio intermedio, y al menos otra superficie (9, 10, 11) está situada en el espacio entre dicho espacio intermedio y las paredes del aparato.
MX2013013051A 2011-05-11 2012-04-17 Sistema de intercambio de calor. MX351529B (es)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
IT000817A ITMI20110817A1 (it) 2011-05-11 2011-05-11 "sistema di scambio termico"
PCT/EP2012/056998 WO2012152548A1 (en) 2011-05-11 2012-04-17 Heat exchange system

Publications (2)

Publication Number Publication Date
MX2013013051A MX2013013051A (es) 2014-05-21
MX351529B true MX351529B (es) 2017-10-18

Family

ID=44554469

Family Applications (1)

Application Number Title Priority Date Filing Date
MX2013013051A MX351529B (es) 2011-05-11 2012-04-17 Sistema de intercambio de calor.

Country Status (14)

Country Link
US (1) US9568251B2 (es)
EP (1) EP2710317B1 (es)
CN (1) CN103649665B (es)
AP (1) AP3528A (es)
CA (1) CA2834946C (es)
DK (1) DK2710317T3 (es)
ES (1) ES2628405T3 (es)
IT (1) ITMI20110817A1 (es)
MA (1) MA35066B1 (es)
MX (1) MX351529B (es)
PT (1) PT2710317T (es)
RS (1) RS55970B1 (es)
RU (1) RU2583192C2 (es)
WO (1) WO2012152548A1 (es)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US10914466B2 (en) * 2015-09-28 2021-02-09 Eduard Petrovich GAYZER Method for operating a heating boiler and heating boiler for carrying out said method (variants)
TWI620872B (zh) * 2016-01-27 2018-04-11 訊凱國際股份有限公司 熱交換模組及其串聯泵
CN106326531B (zh) * 2016-08-09 2021-03-23 杭州汽轮机股份有限公司 一种工业汽轮机排汽***优化方法

Family Cites Families (14)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1279135A (en) * 1915-09-04 1918-09-17 Rudolph Wurlitzer Mfg Co Air and varnish heater.
FR1476550A (fr) * 1965-07-07 1967-04-14 Thomson Houston Comp Francaise Perfectionnements aux échangeurs de chaleur à ébullition de surface
US3716045A (en) * 1969-05-03 1973-02-13 Siegener Ag Heat exchanger
US4462339A (en) 1983-08-29 1984-07-31 Texaco Development Corporation Gas cooler for production of saturated or superheated steam, or both
US4488513A (en) 1983-08-29 1984-12-18 Texaco Development Corp. Gas cooler for production of superheated steam
RU2063071C1 (ru) * 1994-05-30 1996-06-27 Опытное Конструкторское Бюро "Гидропресс" Система аварийного охлаждения активной зоны ядерного реактора при ее разрушении
JP3957558B2 (ja) * 2002-05-21 2007-08-15 株式会社タクマ 満液二重管式の蒸発器及びアンモニア吸収式冷凍機
JP4623297B2 (ja) * 2005-10-28 2011-02-02 Ｓｍｃ株式会社 温調装置
US7871449B2 (en) * 2006-01-31 2011-01-18 Linde Process Plants, Inc. Process and apparatus for synthesis gas heat exchange system
US7890215B2 (en) * 2006-12-22 2011-02-15 Duncan Scot M Optimized control system for cooling systems
US7942018B2 (en) * 2008-02-01 2011-05-17 The Hong Kong Polytechnic University Apparatus for cooling or heating thermal storage using microencapsulated phase change material slurries
CN100567853C (zh) * 2008-04-18 2009-12-09 中国家用电器研究院 一种回热式硫氰酸钠-氨吸收式热泵***
DE102012204404B4 (de) * 2011-03-25 2022-09-08 Denso Corporation Wärmeaustauschsystem und Fahrzeugkältekreislaufsystem
DE102011015433A1 (de) * 2011-03-29 2012-10-04 Linde Ag Wärmetauschersystem

Also Published As

Publication number Publication date
EP2710317A1 (en) 2014-03-26
WO2012152548A1 (en) 2012-11-15
US20140230438A1 (en) 2014-08-21
CA2834946A1 (en) 2012-11-15
DK2710317T3 (en) 2017-07-10
CA2834946C (en) 2019-11-19
US9568251B2 (en) 2017-02-14
AP2013007170A0 (en) 2013-10-31
ITMI20110817A1 (it) 2012-11-12
CN103649665A (zh) 2014-03-19
CN103649665B (zh) 2017-02-15
RU2013154550A (ru) 2015-06-20
RS55970B1 (sr) 2017-09-29
PT2710317T (pt) 2017-06-07
ES2628405T3 (es) 2017-08-02
MA35066B1 (fr) 2014-04-03
AP3528A (en) 2016-01-11
MX2013013051A (es) 2014-05-21
RU2583192C2 (ru) 2016-05-10
EP2710317B1 (en) 2017-03-29

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