WO2004106833A1 - Echangeur de chaleur cryogene/eau et application a la fourniture de gaz a un groupe de puissance embarque dans un vehicule - Google Patents
Echangeur de chaleur cryogene/eau et application a la fourniture de gaz a un groupe de puissance embarque dans un vehicule Download PDFInfo
- Publication number
- WO2004106833A1 WO2004106833A1 PCT/FR2004/001226 FR2004001226W WO2004106833A1 WO 2004106833 A1 WO2004106833 A1 WO 2004106833A1 FR 2004001226 W FR2004001226 W FR 2004001226W WO 2004106833 A1 WO2004106833 A1 WO 2004106833A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- exchanger according
- plates
- cryogen
- water
- exchange
- Prior art date
Links
Classifications
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M8/00—Fuel cells; Manufacture thereof
- H01M8/04—Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids
- H01M8/04007—Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids related to heat exchange
- H01M8/04067—Heat exchange or temperature measuring elements, thermal insulation, e.g. heat pipes, heat pumps, fins
- H01M8/04074—Heat exchange unit structures specially adapted for fuel cell
-
- 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
- C01B3/0005—Reversible uptake of hydrogen by an appropriate medium, i.e. based on physical or chemical sorption phenomena or on reversible chemical reactions, e.g. for hydrogen storage purposes ; Reversible gettering of hydrogen; Reversible uptake of hydrogen by electrodes
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
- F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
- F17C11/00—Use of gas-solvents or gas-sorbents in vessels
- F17C11/005—Use of gas-solvents or gas-sorbents in vessels for hydrogen
-
- 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
- F28D9/00—Heat-exchange apparatus having stationary plate-like or laminated conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
- F28D9/0062—Heat-exchange apparatus having stationary plate-like or laminated conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits for one heat-exchange medium being formed by spaced plates with inserted 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
- 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
- F28F13/08—Arrangements for modifying heat-transfer, e.g. increasing, decreasing by affecting the pattern of flow of the heat-exchange media by varying the cross-section of the flow channels
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F19/00—Preventing the formation of deposits or corrosion, e.g. by using filters or scrapers
- F28F19/006—Preventing deposits of ice
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M8/00—Fuel cells; Manufacture thereof
- H01M8/04—Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids
- H01M8/04007—Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids related to heat exchange
- H01M8/04029—Heat exchange using liquids
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
- F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
- F17C2221/00—Handled fluid, in particular type of fluid
- F17C2221/01—Pure fluids
- F17C2221/012—Hydrogen
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
- F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
- F17C2223/00—Handled fluid before transfer, i.e. state of fluid when stored in the vessel or before transfer from the vessel
- F17C2223/01—Handled fluid before transfer, i.e. state of fluid when stored in the vessel or before transfer from the vessel characterised by the phase
- F17C2223/0146—Two-phase
- F17C2223/0153—Liquefied gas, e.g. LPG, GPL
- F17C2223/0161—Liquefied gas, e.g. LPG, GPL cryogenic, e.g. LNG, GNL, PLNG
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
- F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
- F17C2223/00—Handled fluid before transfer, i.e. state of fluid when stored in the vessel or before transfer from the vessel
- F17C2223/03—Handled fluid before transfer, i.e. state of fluid when stored in the vessel or before transfer from the vessel characterised by the pressure level
- F17C2223/033—Small pressure, e.g. for liquefied gas
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
- F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
- F17C2223/00—Handled fluid before transfer, i.e. state of fluid when stored in the vessel or before transfer from the vessel
- F17C2223/04—Handled fluid before transfer, i.e. state of fluid when stored in the vessel or before transfer from the vessel characterised by other properties of handled fluid before transfer
- F17C2223/042—Localisation of the removal point
- F17C2223/046—Localisation of the removal point in the liquid
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
- F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
- F17C2225/00—Handled fluid after transfer, i.e. state of fluid after transfer from the vessel
- F17C2225/01—Handled fluid after transfer, i.e. state of fluid after transfer from the vessel characterised by the phase
- F17C2225/0107—Single phase
- F17C2225/0123—Single phase gaseous, e.g. CNG, GNC
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
- F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
- F17C2225/00—Handled fluid after transfer, i.e. state of fluid after transfer from the vessel
- F17C2225/03—Handled fluid after transfer, i.e. state of fluid after transfer from the vessel characterised by the pressure level
- F17C2225/033—Small pressure, e.g. for liquefied gas
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
- F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
- F17C2227/00—Transfer of fluids, i.e. method or means for transferring the fluid; Heat exchange with the fluid
- F17C2227/03—Heat exchange with the fluid
- F17C2227/0302—Heat exchange with the fluid by heating
- F17C2227/0309—Heat exchange with the fluid by heating using another fluid
- F17C2227/0316—Water heating
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
- F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
- F17C2227/00—Transfer of fluids, i.e. method or means for transferring the fluid; Heat exchange with the fluid
- F17C2227/03—Heat exchange with the fluid
- F17C2227/0367—Localisation of heat exchange
- F17C2227/0388—Localisation of heat exchange separate
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
- F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
- F17C2227/00—Transfer of fluids, i.e. method or means for transferring the fluid; Heat exchange with the fluid
- F17C2227/03—Heat exchange with the fluid
- F17C2227/0367—Localisation of heat exchange
- F17C2227/0388—Localisation of heat exchange separate
- F17C2227/0393—Localisation of heat exchange separate using a vaporiser
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
- F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
- F17C2270/00—Applications
- F17C2270/01—Applications for fluid transport or storage
- F17C2270/0165—Applications for fluid transport or storage on the road
- F17C2270/0168—Applications for fluid transport or storage on the road by vehicles
- F17C2270/0178—Cars
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F2250/00—Arrangements for modifying the flow of the heat exchange media, e.g. flow guiding means; Particular flow patterns
- F28F2250/10—Particular pattern of flow of the heat exchange media
- F28F2250/104—Particular pattern of flow of the heat exchange media with parallel flow
-
- 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
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/30—Hydrogen technology
- Y02E60/32—Hydrogen storage
-
- 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
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/30—Hydrogen technology
- Y02E60/50—Fuel cells
Definitions
- the present invention relates to cryogenic / water heat exchangers, intended for heating and / or vaporizing a cryogenic fluid at very low temperature with water, of the type comprising a water circuit having an inlet and an outlet and a circuit for cryogen having an inlet and an outlet, the circuits comprising parallel exchange portions separated by partitions.
- the object of the present invention is to provide an efficient, compact heat exchanger structure which does not present any risk of malfunction due to freezing or the formation of ice cubes in the water circuit.
- each exchange portion of the cryogen circuit has an inlet passage of reduced section opening into an area of enlarged section, the exchange portion of the water circuit having a substantially constant section corresponding to said enlarged section of the exchange portion of the cryogen circuit.
- the inlet passage has at least one downstream part with a flared profile.
- the inlet passage is substantially centered on the longitudinal axis of the exchange portion.
- the ratio between the minimum section of the inlet passage and the enlarged section of the exchange portion of the cryogen circuit is between 10 and 50%, typically between 20 and 30%.
- the exchange portions are delimited by adjoining plates, made of thin stainless steel, typically less than 2.50. mm, advantageously less than 2 mm.
- the inlet passages open into a cryogen distribution pipe extending into a water distribution box closing this side of the exchanger.
- the present invention also relates to an application of this exchanger for the supply of gaseous hydrogen to a power generator of a motor vehicle, for example a heat engine and / or a fuel cell with a proton exchange membrane.
- FIG. 1 is a schematic longitudinal sectional view of a heat exchanger according to the invention.
- FIG. 2 is an exploded perspective view of the plates of the exchanger of Figure 1 showing the configurations of the exchange portions of the cryogen and water circuits;
- Figure 3 is a cross-sectional view along the cutting plane 3/3 of Figure 1.
- the heat exchanger comprises an exchange block, generally designated by the reference 1, constituted by an assembly of adjoining plates, as will be seen below, defining portions of parallel co-current exchange circuits between a cryogen distributor 2 and a heated cryogen outlet manifold 3, on the one hand, and a heater water distributor 4 and a water outlet manifold 5 .
- each portion of the exchange circuit is defined between two solid plates 6 by perforated plates or half-plates 7c for the cryogen circuit and 7th for the water circuit.
- the plates 7e of the water circuit define a passage of substantially constant width £ while the plates 7c define passages 9 with an evolving profile, with an inlet passage 9a of reduced section flaring in a main passage of width I identical to that of the water passages 8.
- the inlet passage 9a is centered on the longitudinal axis of the passage 9 (the longitudinal axes of the passages 8 and 9 being advantageously coplanar).
- the extremely cold zone of the portion of the cryogen exchange circuit constituted by the inlet passage zone 9a, has a reduced width, typically less than 50% of the nominal width I, advantageously greater than 10% of the latter, preferably between 20 and 30% of the latter, so that the water arriving cocurrently in the inlet portion of the passage 8 absorbs the maximum of frigories in a central portion itself centered on the inlet passage 9a but projecting slightly laterally from the latter due to the large temperature gradients on either side of this zone provided by the area of the plates.
- a small block of ice 10 occupying only a central part of the width of the passage 8 and never preventing circulation, on both sides.
- Another of the water flow as shown by the two arrows in Figure 2, causing only a small pressure drop in the water circuit.
- the plates 6 and 7 are typically produced by stamping 316 L or 304 L stainless steel sheets of a thickness less than 2 mm for the water circuit and not more than 1 mm for the cryogen circuit .
- the H2L cryogen arrives in the distributor 2 at a temperature of the order of -250 ° C, typically under a pressure between 1 to 10 bar absolute, with a flow rate of less than 5 g per second.
- the plates 7c have a thickness of approximately 0.5 mm
- the plates 7e a thickness of approximately 2 mm
- the plates 6 a thickness of approximately 0.6 mm.
- the exchange block 1 is produced by joining a plurality of plates 6,7c and 7e against each other and by assembling them by welding of their external lateral edges.
- the water coming from the radiator of the vehicle's thermal engine, enters the inlet distributor 4 at a temperature below 110 ° C., typically between 60 and 80 ° C., and exits at a slightly lower temperature of the collector 5, the gaseous hydrogen leaving the collector 3 at a temperature slightly lower than that of the water, of the order of 50 to 60 ° C.
- an electric heater 11 is advantageously provided in the collector 3.
- the cryogen supply distributor 2 here consists of a gutter welded to the lower edges of the plates 6 and 7. Similarly, the gaseous cryogen is recovered, at the outlet of the passage 9, in a gutter 12 welded to the edges upper plates and welded along an upper generator to the outlet manifold 3 with which it communicates by facing openings 13 formed in the contacting areas.
- a box 15 forming the water distributor 4 closes the bottom side of the exchange block 1, while a box 16 forming the water outlet manifold 5 closes the top side of the exchange block.
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- General Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Sustainable Energy (AREA)
- General Chemical & Material Sciences (AREA)
- Electrochemistry (AREA)
- Life Sciences & Earth Sciences (AREA)
- Sustainable Development (AREA)
- Manufacturing & Machinery (AREA)
- Organic Chemistry (AREA)
- Combustion & Propulsion (AREA)
- Inorganic Chemistry (AREA)
- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
Abstract
Description
Claims
Priority Applications (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
EP04742771A EP1631783A1 (fr) | 2003-05-27 | 2004-05-18 | Echangeur de chaleur cryogene/eau et application a la fourniture de gaz a un groupe de puissance embarque dans un vehicule |
JP2006530364A JP2007501376A (ja) | 2003-05-27 | 2004-05-18 | 寒剤/水熱交換器および車上の動力装置にガスを供給する寒剤/水熱交換器の使用 |
US10/557,587 US7299642B2 (en) | 2003-05-27 | 2004-05-18 | Cryogen/water heat exchanger and the application thereof to the supply of gas to an on-board power unit in a vehicle |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
FR0306438A FR2855600B1 (fr) | 2003-05-27 | 2003-05-27 | Echangeur de chaleur cryogene/eau et application a la fourniture de gaz a un groupe de puissance embarque dans un vehicule |
FR03/06438 | 2003-05-27 |
Publications (1)
Publication Number | Publication Date |
---|---|
WO2004106833A1 true WO2004106833A1 (fr) | 2004-12-09 |
Family
ID=33427484
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/FR2004/001226 WO2004106833A1 (fr) | 2003-05-27 | 2004-05-18 | Echangeur de chaleur cryogene/eau et application a la fourniture de gaz a un groupe de puissance embarque dans un vehicule |
Country Status (6)
Country | Link |
---|---|
US (1) | US7299642B2 (fr) |
EP (1) | EP1631783A1 (fr) |
JP (1) | JP2007501376A (fr) |
CN (1) | CN1795360A (fr) |
FR (1) | FR2855600B1 (fr) |
WO (1) | WO2004106833A1 (fr) |
Families Citing this family (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US8276654B2 (en) | 2005-11-17 | 2012-10-02 | Hamilton Sundstrand Corporation | Core assembly with deformation preventing features |
US7637112B2 (en) * | 2006-12-14 | 2009-12-29 | Uop Llc | Heat exchanger design for natural gas liquefaction |
US8631858B2 (en) * | 2009-06-16 | 2014-01-21 | Uop Llc | Self cooling heat exchanger with channels having an expansion device |
DE102011010840B4 (de) * | 2011-02-10 | 2019-08-14 | Oventrop Gmbh & Co. Kg | Trink- oder Brauchwassersystem |
WO2014038179A1 (fr) * | 2012-09-05 | 2014-03-13 | パナソニック株式会社 | Dispositif de refroidissement, automobile électrique comportant ledit dispositif de refroidissement, et dispositif électronique |
JP6347003B1 (ja) * | 2017-01-25 | 2018-06-20 | デウ シップビルディング アンド マリン エンジニアリング カンパニー リミテッド | Lng船の蒸発ガス再液化方法及びシステム |
Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3282334A (en) * | 1963-04-29 | 1966-11-01 | Trane Co | Heat exchanger |
US5095973A (en) * | 1990-12-20 | 1992-03-17 | Toy William W | Heat exchangers |
FR2807152A1 (fr) * | 2000-03-28 | 2001-10-05 | Cie Ind D Applic Thermiques Ci | Echangeur de chaleur a plaques |
FR2809805A1 (fr) * | 2000-05-31 | 2001-12-07 | Nordon Cryogenie Snc | Procede d'echange de chaleur dans un echangeur de chaleur a plaques brassees et echangeur de chaleur correspondant |
Family Cites Families (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3565201A (en) * | 1969-02-07 | 1971-02-23 | Lng Services | Cryogenic fuel system for land vehicle power plant |
US4590770A (en) * | 1985-06-03 | 1986-05-27 | National Semiconductor Corporation | Cryogenic liquid heat exchanger |
JPH0711325Y2 (ja) * | 1987-12-24 | 1995-03-15 | 住友精密工業株式会社 | プレートフィン型熱交換器 |
GB9104156D0 (en) * | 1991-02-27 | 1991-04-17 | Rolls Royce & Ass | Heat exchanger |
-
2003
- 2003-05-27 FR FR0306438A patent/FR2855600B1/fr not_active Expired - Fee Related
-
2004
- 2004-05-18 JP JP2006530364A patent/JP2007501376A/ja active Pending
- 2004-05-18 EP EP04742771A patent/EP1631783A1/fr not_active Withdrawn
- 2004-05-18 US US10/557,587 patent/US7299642B2/en not_active Expired - Fee Related
- 2004-05-18 WO PCT/FR2004/001226 patent/WO2004106833A1/fr active Application Filing
- 2004-05-18 CN CNA2004800145151A patent/CN1795360A/zh active Pending
Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3282334A (en) * | 1963-04-29 | 1966-11-01 | Trane Co | Heat exchanger |
US5095973A (en) * | 1990-12-20 | 1992-03-17 | Toy William W | Heat exchangers |
FR2807152A1 (fr) * | 2000-03-28 | 2001-10-05 | Cie Ind D Applic Thermiques Ci | Echangeur de chaleur a plaques |
FR2809805A1 (fr) * | 2000-05-31 | 2001-12-07 | Nordon Cryogenie Snc | Procede d'echange de chaleur dans un echangeur de chaleur a plaques brassees et echangeur de chaleur correspondant |
Also Published As
Publication number | Publication date |
---|---|
FR2855600A1 (fr) | 2004-12-03 |
JP2007501376A (ja) | 2007-01-25 |
FR2855600B1 (fr) | 2005-07-08 |
CN1795360A (zh) | 2006-06-28 |
US20070028627A1 (en) | 2007-02-08 |
EP1631783A1 (fr) | 2006-03-08 |
US7299642B2 (en) | 2007-11-27 |
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