EP2671032A2 - Échangeur de chaleur - Google Patents

Échangeur de chaleur

Info

Publication number
EP2671032A2
EP2671032A2 EP12703096.3A EP12703096A EP2671032A2 EP 2671032 A2 EP2671032 A2 EP 2671032A2 EP 12703096 A EP12703096 A EP 12703096A EP 2671032 A2 EP2671032 A2 EP 2671032A2
Authority
EP
European Patent Office
Prior art keywords
unit
heat exchanger
evaporator
distribution
distribution unit
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
EP12703096.3A
Other languages
German (de)
English (en)
Other versions
EP2671032B1 (fr
Inventor
Andreas Freund
Wolfgang Seewald
Michael Sickelmann
Bernd Schäfer
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.)
Mahle Behr GmbH and Co KG
Original Assignee
Behr GmbH and Co KG
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
Family has litigation
First worldwide family litigation filed litigation Critical https://patents.darts-ip.com/?family=45569651&utm_source=google_patent&utm_medium=platform_link&utm_campaign=public_patent_search&patent=EP2671032(A2) "Global patent litigation dataset” by Darts-ip is licensed under a Creative Commons Attribution 4.0 International License.
Application filed by Behr GmbH and Co KG filed Critical Behr GmbH and Co KG
Publication of EP2671032A2 publication Critical patent/EP2671032A2/fr
Application granted granted Critical
Publication of EP2671032B1 publication Critical patent/EP2671032B1/fr
Revoked legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F1/00Tubular elements; Assemblies of tubular elements
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B39/00Evaporators; Condensers
    • F25B39/02Evaporators
    • F25B39/028Evaporators having distributing means
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B41/00Fluid-circulation arrangements
    • F25B41/30Expansion means; Dispositions thereof
    • F25B41/39Dispositions with two or more expansion means arranged in series, i.e. multi-stage expansion, on a refrigerant line leading to the same evaporator
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F9/00Casings; Header boxes; Auxiliary supports for elements; Auxiliary members within casings
    • F28F9/02Header boxes; End plates
    • F28F9/026Header boxes; End plates with static flow control means, e.g. with means for uniformly distributing heat exchange media into conduits

Definitions

  • the invention relates to a heat exchanger according to the patent claim 1.
  • Evaporators are known in which the two-phase refrigerant is distributed from an inflow channel to a flow-through device, preferably tubes, in particular flat tubes. After flowing through the flat tubes, the vaporous refrigerant exits the evaporator via an outflow channel.
  • the uniform distribution of the liquid refrigerant in the entire length of the inflow channel presents difficulties.
  • the reason for this is, inter alia, the formation of different flow forms as a function of the operating state.
  • the segregation of the homogeneous two-phase refrigerant mixture at the entry of the evaporator also plays a special role over the length of the inflow channel. Individual pipes are thus supplied exclusively with refrigerant vapor, whereby the evaporator performance deteriorates.
  • the refrigerant is only distributed to a small proportion (typically 1/3, 1/4 or 1/8) of the flat tubes and further deflected in several blocks and thus passed through the evaporator.
  • the refrigerant in the individual collectors is intermixed by internals such as partitions, diaphragms, so that higher pressure losses occur are to be expected in the evaporator unit.
  • the ratio of the pressure differences in the distribution unit (injection pipe + distribution unit for the 1st block) and the entire block (flat tubes + deflections between the blocks) is in the range of less than 3.
  • the invention has for its object to provide an improved heat exchanger, which in particular in the heat-transmitting part of the evaporator - the evaporation section or, evaporator unit - realized low refrigerant side pressure losses, This object is achieved by a heat exchanger with the features of claim 1.
  • the heat exchanger in particular for a heating or air conditioning in a motor vehicle, with a via a distribution unit with a refrigerant medium fed and flowed through by this and after only one deflection (two-block design) formed in the depth in a deflection unit around evaporator unit, wherein the distribution unit is designed in the sense of a uniform distribution of the refrigerant medium over the entire evaporator width. Due to the additional internals in the distribution unit, the two-phase refrigerant is thus distributed evenly over the entire evaporator width on the flat tubes and deflected only once.
  • a design of the distribution unit in terms of a ratio V of the pressure difference between the pressure difference in the distribution unit on the one hand and the pressure difference in the evaporator unit on the other hand, which is greater than 3.
  • An increase in the ratio of the pressure differences is necessary for a homogeneous distribution of the refrigerant in the distribution unit and thus leads to an increase in the specific cooling capacity due to a better temperature profile.
  • a design of the distribution unit in the sense of a ratio of the pressure difference between the pressure difference in the distribution unit on the one hand and the pressure difference in the evaporator unit on the other hand be provided in the range between 3 and 70.
  • a design of the distribution unit in the sense of a ratio of the pressure difference between the pressure difference in the Distribution unit on the one hand and the pressure difference in the evaporator unit on the other hand be provided, which in a range of 3 to 30 at a refrigerant edium mass flow of 30 kg / h on the one hand and 30-70 at a refrigerant medium mass flow of 250 kg / h lies.
  • FIG. 2 and 3 also show a pressure-enthalpy diagram schematically illustrated a refrigerant circuit of an air conditioner, wherein essential points of the refrigerant circuit were provided with digits, which were shown according to the pressure-enthalpy diagram.
  • An embodiment of the invention provides in particular for a deflection unit free of any intermediate mixing means.
  • a further embodiment provides a pressure distribution element in the distribution unit in the sense of a distribution of the refrigerant medium in parallel to all through-flow or flow around tubes, in particular flat tubes, the evaporator unit.
  • a pressure distribution element for example, the installation of an additional pressure loss element at the evaporator inlet (before evaporation) for the distribution of the refrigerant can be applied in parallel to all flat tubes via the Velvet width of the evaporator may be provided so that all flat tubes are supplied evenly with liquid and gaseous refrigerant (this pressure loss element has no effect on the cooling capacity). This results in a large ratio of pressure loss in the refrigerant distribution at the evaporator inlet to the pressure loss in the evaporator network (evaporator section).

Landscapes

  • Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
  • Air-Conditioning For Vehicles (AREA)
EP12703096.3A 2011-02-04 2012-02-06 Échangeur de chaleur Revoked EP2671032B1 (fr)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
DE102011003649A DE102011003649A1 (de) 2011-02-04 2011-02-04 Wärmeübertrager
PCT/EP2012/051984 WO2012104438A2 (fr) 2011-02-04 2012-02-06 Échangeur de chaleur

Publications (2)

Publication Number Publication Date
EP2671032A2 true EP2671032A2 (fr) 2013-12-11
EP2671032B1 EP2671032B1 (fr) 2018-05-09

Family

ID=45569651

Family Applications (1)

Application Number Title Priority Date Filing Date
EP12703096.3A Revoked EP2671032B1 (fr) 2011-02-04 2012-02-06 Échangeur de chaleur

Country Status (4)

Country Link
US (1) US9599409B2 (fr)
EP (1) EP2671032B1 (fr)
DE (1) DE102011003649A1 (fr)
WO (1) WO2012104438A2 (fr)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE102014206043B4 (de) 2014-03-31 2021-08-12 Mtu Friedrichshafen Gmbh Verfahren zum Betreiben eines Systems für einen thermodynamischen Kreisprozess mit einem mehrflutigen Verdampfer, Steuereinrichtung für ein System, System für einen thermodynamischen Kreisprozess mit einem mehrflutigen Verdampfer, und Anordnung einer Brennkraftmaschine und eines Systems

Family Cites Families (24)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE3311579C2 (de) * 1983-03-30 1985-10-03 Süddeutsche Kühlerfabrik Julius Fr. Behr GmbH & Co. KG, 7000 Stuttgart Wärmetauscher
JP2936775B2 (ja) 1991-04-05 1999-08-23 株式会社デンソー 熱交換器
US5241839A (en) 1991-04-24 1993-09-07 Modine Manufacturing Company Evaporator for a refrigerant
JP3305460B2 (ja) 1993-11-24 2002-07-22 昭和電工株式会社 熱交換器
DE19515527A1 (de) 1995-04-27 1996-10-31 Thermal Werke Beteiligungen Gm Verdampfer in Flachrohr- oder Plattenbauweise für den Kältemittelkreislauf einer Kraftfahrzeugklimaanlage
DE19719261C2 (de) * 1997-05-07 2001-06-07 Valeo Klimatech Gmbh & Co Kg Zweiflutiger Flachrohrverdampfer einer Kraftfahrzeugklimaanlage
DE19719257C2 (de) * 1997-05-07 2002-09-19 Valeo Klimatech Gmbh & Co Kg Sammelkasten eines Verdampfers in Flachrohr- oder Plattenbauweise für eine Kraftfahrzeugklimaanlage und Herstellungsverfahren
US6070428A (en) * 1997-05-30 2000-06-06 Showa Aluminum Corporation Stack type evaporator
US6382313B2 (en) * 2000-02-25 2002-05-07 Nippon Shokubai Co., Ltd. Heat exchanger for easily polymerizing substance-containing gas provided with gas distributing plate
DE10015976B4 (de) * 2000-03-30 2019-07-04 Mahle International Gmbh Befüllvorrichtung für Kraftfahrzeugklimaanlagen
ES2198179B1 (es) 2001-03-01 2004-11-16 Valeo Termico, S.A. Intercambiador de calor para gases.
TW552382B (en) * 2001-06-18 2003-09-11 Showa Dendo Kk Evaporator, manufacturing method of the same, header for evaporator and refrigeration system
BRPI0215085A2 (pt) * 2001-12-21 2016-06-28 Behr Gmbh & Co dispositivo para a troca de calor.
JP4124136B2 (ja) * 2003-04-21 2008-07-23 株式会社デンソー 冷媒蒸発器
KR100525424B1 (ko) * 2003-09-18 2005-11-02 엘지전자 주식회사 열교환기용 냉매 분배기와 그 제조방법
DE102004011608A1 (de) * 2004-03-18 2005-10-13 Obrist Engineering Gmbh Wärmetauscher einer Fahrzeugklimaanlage
JP4613645B2 (ja) * 2005-03-09 2011-01-19 株式会社デンソー 熱交換器
US7967060B2 (en) 2005-08-18 2011-06-28 Parker-Hannifin Corporation Evaporating heat exchanger
JP4830918B2 (ja) * 2006-08-02 2011-12-07 株式会社デンソー 熱交換器
JP5002797B2 (ja) * 2007-03-16 2012-08-15 株式会社ケーヒン・サーマル・テクノロジー 熱交換器
CN101680689B (zh) * 2007-05-22 2012-11-14 贝洱两合公司 热交换器
JP5046771B2 (ja) * 2007-07-27 2012-10-10 三菱重工業株式会社 冷媒蒸発器
DE102008028290B4 (de) * 2008-06-16 2019-05-16 Mahle International Gmbh Einrichtung zur Kühlung eines Kühlmittels, Kreislauf zur Aufladung einer Brennkraftmaschine und Verfahren zum Kühlen eines zur Aufladung einer Brennkraftmaschine vorgesehenen im Wesentlichen gasförmigen Ladefluids
JP5381770B2 (ja) * 2010-02-09 2014-01-08 株式会社デンソー 熱交換器

Also Published As

Publication number Publication date
DE102011003649A1 (de) 2012-08-09
US20140027096A1 (en) 2014-01-30
WO2012104438A3 (fr) 2013-03-28
US9599409B2 (en) 2017-03-21
WO2012104438A2 (fr) 2012-08-09
EP2671032B1 (fr) 2018-05-09

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