MA35066B1 - Systeme d'echange thermique - Google Patents

Systeme d'echange thermique

Info

Publication number
MA35066B1
MA35066B1 MA36373A MA36373A MA35066B1 MA 35066 B1 MA35066 B1 MA 35066B1 MA 36373 A MA36373 A MA 36373A MA 36373 A MA36373 A MA 36373A MA 35066 B1 MA35066 B1 MA 35066B1
Authority
MA
Morocco
Prior art keywords
heat exchange
fluid bath
space
intermediate space
exchange system
Prior art date
Application number
MA36373A
Other languages
English (en)
Inventor
Luca Eugenio Basini
Alfred Joachim Wilhelm
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 MA35066B1 publication Critical patent/MA35066B1/fr

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28DHEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
    • F28D15/00Heat-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
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01BNON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B3/00Hydrogen; Gaseous mixtures containing hydrogen; Separation of hydrogen from mixtures containing it; Purification of hydrogen
    • C01B3/02Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen
    • C01B3/32Production 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
    • C01B3/34Production 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
    • C01B3/38Production 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
    • C01B3/386Catalytic partial combustion
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01BNON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B3/00Hydrogen; Gaseous mixtures containing hydrogen; Separation of hydrogen from mixtures containing it; Purification of hydrogen
    • C01B3/02Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen
    • C01B3/32Production 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
    • C01B3/34Production 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
    • C01B3/48Production 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
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28DHEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
    • F28D21/00Heat-exchange apparatus not covered by any of the groups F28D1/00 - F28D20/00
    • F28D21/0017Flooded core heat exchangers
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01BNON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B2203/00Integrated processes for the production of hydrogen or synthesis gas
    • C01B2203/04Integrated processes for the production of hydrogen or synthesis gas containing a purification step for the hydrogen or the synthesis gas
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01BNON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B2203/00Integrated processes for the production of hydrogen or synthesis gas
    • C01B2203/08Methods of heating or cooling
    • C01B2203/0872Methods of cooling
    • C01B2203/0883Methods of cooling by indirect heat exchange
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01BNON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B2203/00Integrated processes for the production of hydrogen or synthesis gas
    • C01B2203/08Methods of heating or cooling
    • C01B2203/0872Methods of cooling
    • C01B2203/0888Methods of cooling by evaporation of a fluid
    • C01B2203/0894Generation of steam
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00Technologies relating to chemical industry
    • Y02P20/10Process efficiency
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00Technologies relating to chemical industry
    • Y02P20/10Process efficiency
    • Y02P20/129Energy 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)
  • Thermal Sciences (AREA)
  • General Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • Physics & Mathematics (AREA)
  • General Health & Medical Sciences (AREA)
  • Inorganic Chemistry (AREA)
  • Health & Medical Sciences (AREA)
  • Physical Or Chemical Processes And Apparatus (AREA)
  • Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)

Abstract

La présente invention concerne un système d'échange de chaleur comportant : - un appareil unique (N) comprenant une zone immergée dans un bain de fluide (N2) et un espace libre (N1) au niveau de la partie supérieure dans lequel est accumulée une phase vapeur; - au moins un espace intermédiaire (P) ouvert aux deux extrémités, situé à l'intérieur dudit appareil et entièrement immergé dans le bain de fluide; - une ou plusieurs surfaces (6, 7, 8, 9, 10, 11) d'échange de chaleur, ledit système étant caractérisé en ce qu'il contient toutes les surfaces d'échange de chaleur dans un même appareil et en ce que lesdites surfaces sont entièrement immergées dans le bain de fluide et sont reliées fluidiquement aux sources chaude et froide, extérieures audit système, via des flux de matière. Au moins une des surfaces (6, 7, 8) d'échange de chaleur est située à l'intérieur de l'espace intermédiaire et au moins une autre surface (9, 10, 11) est située dans l'espace compris entre ledit espace intermédiaire et les parois de l'appareil.
MA36373A 2011-05-11 2012-04-17 Systeme d'echange thermique MA35066B1 (fr)

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 (fr) 2011-05-11 2012-04-17 Système d'échange de chaleur

Publications (1)

Publication Number Publication Date
MA35066B1 true MA35066B1 (fr) 2014-04-03

Family

ID=44554469

Family Applications (1)

Application Number Title Priority Date Filing Date
MA36373A MA35066B1 (fr) 2011-05-11 2012-04-17 Systeme d'echange thermique

Country Status (14)

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

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2017058041A1 (fr) * 2015-09-28 2017-04-06 Михаил Александрович НАДТОЧЕЙ Procédé de fonctionnement de chaudière, et chaudière pour sa mise en œuvre (variantes)
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
US4488513A (en) 1983-08-29 1984-12-18 Texaco Development Corp. Gas cooler for production of superheated steam
US4462339A (en) 1983-08-29 1984-07-31 Texaco Development Corporation Gas cooler for production of saturated or superheated steam, or both
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
AP3528A (en) 2016-01-11
CN103649665A (zh) 2014-03-19
CA2834946C (fr) 2019-11-19
MX351529B (es) 2017-10-18
MX2013013051A (es) 2014-05-21
US9568251B2 (en) 2017-02-14
AP2013007170A0 (en) 2013-10-31
ITMI20110817A1 (it) 2012-11-12
PT2710317T (pt) 2017-06-07
RU2013154550A (ru) 2015-06-20
US20140230438A1 (en) 2014-08-21
CN103649665B (zh) 2017-02-15
RS55970B1 (sr) 2017-09-29
EP2710317A1 (fr) 2014-03-26
CA2834946A1 (fr) 2012-11-15
WO2012152548A1 (fr) 2012-11-15
ES2628405T3 (es) 2017-08-02
DK2710317T3 (en) 2017-07-10
RU2583192C2 (ru) 2016-05-10
EP2710317B1 (fr) 2017-03-29

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