CN101589278A - Multi-channel heat exchanger with multi-stage expansion device - Google Patents

Multi-channel heat exchanger with multi-stage expansion device Download PDF

Info

Publication number
CN101589278A
CN101589278A CNA200680056541XA CN200680056541A CN101589278A CN 101589278 A CN101589278 A CN 101589278A CN A200680056541X A CNA200680056541X A CN A200680056541XA CN 200680056541 A CN200680056541 A CN 200680056541A CN 101589278 A CN101589278 A CN 101589278A
Authority
CN
China
Prior art keywords
expansion
round nose
cold
openend
producing medium
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
CNA200680056541XA
Other languages
Chinese (zh)
Other versions
CN101589278B (en
Inventor
M·B·戈尔布诺夫
Y·姜
J·J·桑焦文尼
H·比默
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.)
Carrier Corp
Original Assignee
Carrier Corp
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 Carrier Corp filed Critical Carrier Corp
Publication of CN101589278A publication Critical patent/CN101589278A/en
Application granted granted Critical
Publication of CN101589278B publication Critical patent/CN101589278B/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Images

Classifications

    • 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
    • F28F9/0246Arrangements for connecting header boxes with flow lines
    • 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
    • F28D2021/0019Other heat exchangers for particular applications; Heat exchange systems not otherwise provided for
    • F28D2021/0068Other heat exchangers for particular applications; Heat exchange systems not otherwise provided for for refrigerant cycles
    • F28D2021/0071Evaporators
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F2260/00Heat exchangers or heat exchange elements having special size, e.g. microstructures
    • F28F2260/02Heat exchangers or heat exchange elements having special size, e.g. microstructures having microchannels

Landscapes

  • Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Mechanical Engineering (AREA)
  • Thermal Sciences (AREA)
  • General Engineering & Computer Science (AREA)
  • Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)

Abstract

An expansion device for a heat exchanger having a manifold and a plurality of mini-and or micro-channels. The expansion device has an outer element having a plurality of orifices therethrough that is received in the manifold, and an inner element telescopically received in the outer element having at least one orifice therethrough and being in fluid communication with the plurality of orifices. Fluid passing through the at least one orifice and through the plurality of orifices is expanded and reduced in pressure prior to entering the manifold.

Description

The multi-channel heat exchanger that has multi-stage expansion device
Technical field
The present invention relates to a kind of expansion gear that is used for heat exchanger.More specifically, the present invention relates to a kind of expansion gear that is used for passage aisle or micro-channel heat exchanger (MCHX), it provides pressure drop and mixing by a plurality of throttle orifices, thereby improves heat exchanger efficiency.
Background technology
Refrigeration system is to be well known in the modern times, and is ubiquitous in as these industry such as food service industry, chemistry and auto industrys.Heat exchanger obtains the widespread demand of office building and domestic use.These systems worry to lose efficacy or efficient deficiency more commonly very much.
Traditional kind of refrigeration cycle or air-conditioning comprise compressor, condenser, expansion valve, evaporimeter and cold-producing medium, and the evaporation of cold-producing medium produces chilling temperature.In some refrigeration systems, evaporimeter is the small diameter pipeline of series of parallel.When refrigerant fluid when condenser flows through evaporimeter, pressure drop and temperature drop will appear, obtain colder temperature thus.
Cooling system can use the single-phase or dual phase coolant that runs through the loop.When cold-producing medium is single-phase cooling fluid (for example water in the automobile radiators), just do not worry that fluid can be between the phase of expansion and become two-phase afterwards.Yet, in many refrigerant vapor compression systems, when fluid when condenser flows to evaporimeter, the part of fluid will expand into steam.As a result, a part that enters the fluid of evaporimeter is a steam, and it causes low heat exchanger efficiency.This steam problem is known as maldistribution and is to use the common issue with of the heat exchanger of parallel refrigerant stream.The gravity of vapour phase and liquid phase and density contrast have caused this problem.
In passage aisle or micro-channel heat exchanger (MCHX), this worry even can be bigger, because cold-producing medium stream is divided into many small pipelines, here each pipeline and passage aisle all should receive the little and impartial share of total cold-producing medium stream.But because this maldistribution, some pipeline receives more liquid and remaining pipes receives more steaminess.The whole bag of tricks (for example expand and distribute the cold-producing medium that enters in or several mini) can be used to stop maldistribution and obtains pressure drop.
Therefore, need a kind of multi-stage expansion device that is used for minichannel heat exchanger, its a plurality of big throttle orifices generation pressure drops that can use series connection during expansion phase are avoided the above-mentioned mentioned problem that causes the heat exchanger poor efficiency with mixed refrigerant fluid suitably.
Summary of the invention
The objective of the invention is to reduce the maldistribution of the cold-producing medium of the heat exchanger in passage aisle or the micro-channel heat exchanger, increase single channel and multi-channel heat exchanger efficient thus.
Another object of the present invention is by promoting the pressure drop in the exchanger header to reduce the maldistribution of the two-phase flow in passage aisle or the micro-channel heat exchanger.
Another purpose of the present invention provides a kind of hookup that inserts in the exchanger header, and it uses a plurality of big throttle orifices to replace a little throttle orifice to obtain pressure drop.
Another purpose of the present invention provides a pair of supporting connecting tube, and they are joined together provides a kind of repeatedly expansion gear, and this device inserts in the collector to minimize the maldistribution of cold-producing medium.
Another purpose of the present invention provides the repeatedly expansion gear with big throttle orifice, and it can obtain the mixing of very big pressure drop and cold-producing medium and cold-producing medium is supplied to passage aisle or micro-channel evaporator.
Another purpose of the present invention provides has exchanger header moulding and perforation, and it takes at least one expansion gear to improve its pressure drop and mixing before the passage aisle that enters heat exchanger at cold-producing medium or the microchannel tubing further.
Another purpose of the present invention provides a kind of collector with a plurality of openings, and expansion gear inserts in these openings or is incorporated in wherein.
Provide these and other objects and advantage by a kind of expansion gear that is used to have the heat exchanger of collector and a plurality of passage aisle and/or microchannel.This expansion gear has external member, this external member has a plurality of throttle orifices that run through it, and be incorporated in the collector, and telescopically is accommodated in the inner member in the external member, this inner member has at least one throttle orifice of running through it and is communicated with these a plurality of throttle orifice fluids.Fluid flow through this at least one throttle orifice and flows through these a plurality of throttle orifices and obtains expanding and step-down before entering collector.
Description of drawings
By below in conjunction with the accompanying drawing detailed description of the present invention, will find out these and other purpose of the present invention more significantly, wherein:
Fig. 1 shows the heat exchanger according to the first embodiment of the present invention, and it has a plurality of mini and is combined with expansion gear;
Fig. 2 shows the expansion gear according to first embodiment of the invention, and it is inserted in the exchanger header of Fig. 1;
Fig. 3 shows the side view of second structure of expansion gear of the present invention, and it is inserted in and is used for step-down further in the moulding collector; And
Fig. 4 shows the upward view of the punching collector of Fig. 3, and it has the opening of the expansion gear that is used for Fig. 2.
The specific embodiment
Fig. 1 shows a kind of minichannel heat exchanger, represents with Reference numeral 10 generally.Heat exchanger 10 has inlet header 15 and discharges collector 20. Connecting collector 15 and 20 is a series of or a plurality of passage aisles or microchannel tubing 25, and they form the main body of heat exchanger 10.Each passage aisle or microchannel tubing 25 all are small diameter pipelines very, and it forms the main body of heat exchanger 10 and refrigerant conveying 30 during evaporating with other pipeline.
Inlet header 15 receives the cold-producing medium 30 that flows through passage aisle or microchannel tubing 25, and it can single-phase or biphasic cryogen.Inlet header is taken in repeatedly expansion gear 40 of the present invention.Thereby can being inserted in the collector 15, at least one or a plurality of repeatedly expansion gear 40 of the present invention guarantee to mini 25 uniform distribution cold-producing mediums with the pressure drop that improves cold-producing medium 30.Although Fig. 1 illustrates the heat exchanger of single channel structure, also can use multi-channel heat exchanger.
With reference to Fig. 2, show the detail drawing of expansion gear 40.Expansion gear 40 has feed pipe 45, and it receives cold-producing medium 30 from loop before.What be mounted to feed pipe 45 is that first hookup, 50, the first hookups 50 have throttle orifice 55 at its peak or summit.What link to each other with first hookup 50 is second hookup 60.Hookup 60 has a series of or a plurality of throttle orifices 65 at place, its summit around its top, and these a series of or a plurality of throttle orifices 65 are on the point around the summit of coupling 60 or become the position of an angle of 90 degrees with its summit.
When cold-producing medium 30 when feed pipe flows to expansion gear 40, it is incorporated in first hookup 50.When cold-producing medium 30 flows through throttle orifice 55, its experience pressure drop and expansion, and in space 70, mix.When cold-producing medium 30 was discharged by throttle orifice 65, the pressure of cold-producing medium 30 further reduced and is inflated once more.When flowing through second throttle orifice 65 of second hookup 60 once more before cold-producing medium is entering the mini 25 of heat exchanger 10, the pressure of cold-producing medium 30 further reduces, and cold-producing medium 30 expands and redistributes in collector 15.
Be not inserted at expansion gear 40 under the situation of collector, the cold-producing medium that enters collector and enter passage aisle from feed pipe can become and single-phase opposite two phase fluid.Further, by flowing through the big throttle orifice 65 of a plurality of series connection, just can obtain required overall presure drop.Use two expansion gears 40 although Fig. 1 shows, can use more expansion gear according to system requirements.Further, Fig. 2 shows two hookups 50 and 60 that have throttle orifice 55 and 65 (series connection) respectively, but other throttle orifice or hookup structure also can be used for obtaining the double expansion of cold-producing medium 30.
With reference to Fig. 3 and 4, show second structure of inserting the expansion system in the moulding collector, represent with Reference numeral 70 generally.In this structure, the expansion gear 40 of first embodiment inserts in the moulding collector 85 at a plurality of openings 90 and 95 places.Moulding collector 85 has the circular section, and it is separated thing 102 and is divided into two chambeies, reception cavity 100 and output cavity 105.Reception cavity 100 is taken in the expansion gear 40 that is arranged in each opening 90 and 95.Separator 102 has a series of eyelets 110, though its permission cold-producing medium 30 in expansion gear 40, expanded and step-down also have extra dilation after twice.
Although collector 85 is shown to have the circular section, other cross section also can be used for the step-down that provides identical and the help of expanding.And more eyelet 90 can be located at bigger expansion and the mixing that is used for cold-producing medium in the collector 85.
Although described the present invention, it will be appreciated by those skilled in the art that and to make various changes, and can do equal replacement to parts in the situation that does not deviate from its scope with reference to one or more exemplary embodiments.In addition, can under the situation that does not deviate from its scope, make a lot of remodeling according to instruction of the present invention to adapt to particular condition or material.Therefore, this means that the present invention is not subjected to the restriction of the specific embodiment (a plurality of embodiment) of disclosed enforcement best form of implementation of the present invention, but comprise all within the scope of the appended claims embodiment of falling.

Claims (19)

1. expansion gear that is used to have the heat exchanger of collector and a plurality of passages comprises:
External member, it has a plurality of throttle orifices that run through it, and described external member is incorporated in the collector; With
Inner member, it is accommodated in the described external member by telescopically, and described inner member has at least one throttle orifice of running through it and is communicated with described a plurality of throttle orifice fluids,
Wherein, the fluid that flows through described at least one throttle orifice and flow through described a plurality of throttle orifices obtained expanding and step-down before entering described collector.
2. expansion gear according to claim 1, wherein: described external member is a tubular element.
3. expansion gear according to claim 1, wherein: described inner member is a tubular element.
4. expansion gear according to claim 1, wherein: described external member have round nose and with described round nose opposing open end, described a plurality of throttle orifices pass described round nose, described inner member is incorporated in the described openend.
5. expansion gear according to claim 1, wherein: described inner member has openend and the round nose relative with described openend, take in the feed pipe of carrying described cold-producing medium in described openend, described at least one throttle orifice passes described round nose.
6. expansion gear according to claim 1, wherein: described fluid is to be accommodated into cold-producing medium in the described inner member by feed pipe.
7. expansion gear according to claim 1, wherein: the described fluid that flows through described at least one throttle orifice and flow through described a plurality of throttle orifices has carried out at least twice expansion and step-down.
8. expansion gear that is used for heat exchanger, this heat exchanger has collector and a plurality of passage aisles or the microchannel that are connected described collector, and this expansion gear comprises:
Outer expansion tube with a plurality of throttle orifices; With
Be accommodated in the interior expansion tube in the described outer expansion tube,
Flow out described in expansion tube and the cold-producing medium that enters collector that flows out described outer expansion tube carried out at least twice expansion and step-down, the therefore described cold-producing medium of mixing before cold-producing medium enters described a plurality of little and/or microdilatancy passage.
9. expansion gear according to claim 8, wherein: described outer expansion tube have round nose and with described round nose opposing open end, described a plurality of throttle orifices pass described round nose, described in expansion tube be incorporated in the described openend.
10. expansion gear according to claim 8, wherein: expansion tube has openend and round nose in described, described openend is relative with described round nose, takes in the feed pipe of carrying described cold-producing medium in described openend, and described at least one throttle orifice passes described round nose.
11. one kind be used to have a plurality of little-expansion system of the heat exchanger of microdilatancy passage, be used for expanding, it comprises:
Collector, it has two chambeies and is in separator between described two chambeies, and described separator has a series of eyelets that run through it; Described a plurality of little and microdilatancy passage can be taken in one of described two chambeies;
At least one external member, it is incorporated in another of described two chambeies, and described at least one external member has a plurality of throttle orifices that run through it;
Inner member, it is incorporated in described at least one external member, and described inner member has at least one throttle orifice that runs through it,
Therefore the cold-producing medium that enters described inner member and expand by described at least one throttle orifice, described a plurality of throttle orifices and described serial eyelet mixed before entering described a plurality of inflation channel by step-down and expansion.
12. expansion system according to claim 11, wherein: described at least one external member is a plurality of external members.
13. expansion system according to claim 11, wherein: described at least one external member is a tubular element.
14. expansion system according to claim 11, wherein: described inner member is a tubular element.
15. expansion system according to claim 11, wherein: described at least one external member have round nose and with described round nose opposing open end, described a plurality of throttle orifice extends through described round nose, and described inner member is incorporated in the described openend of described at least one external member.
16. expansion system according to claim 11, wherein: described inner member has openend and the round nose relative with described openend, take in the feed pipe of carrying described cold-producing medium in described openend, described at least one throttle orifice extends through described round nose.
17. expansion system according to claim 11, wherein: described fluid is to be accommodated in cold-producing medium in the described inner member by feed pipe.
18. expansion system according to claim 11, wherein: the described fluid that flows through described at least one throttle orifice, flows through described a plurality of throttle orifice and flow through described a plurality of eyelets is inflated for three times and step-down at least.
19. one kind as the front with reference to arbitrary described device among Fig. 1,2,3 and 4, it is used in the agent of collector swell refrigeration and improves heat exchanger efficiency.
CN200680056541XA 2006-10-13 2006-12-19 Multi-channel heat exchanger with multi-stage expansion device Expired - Fee Related CN101589278B (en)

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
US85138206P 2006-10-13 2006-10-13
US60/851,382 2006-10-13
PCT/US2006/048347 WO2008045111A1 (en) 2006-10-13 2006-12-19 Multi-channel heat exchanger with multi-stage expansion device

Publications (2)

Publication Number Publication Date
CN101589278A true CN101589278A (en) 2009-11-25
CN101589278B CN101589278B (en) 2011-07-06

Family

ID=39283137

Family Applications (1)

Application Number Title Priority Date Filing Date
CN200680056541XA Expired - Fee Related CN101589278B (en) 2006-10-13 2006-12-19 Multi-channel heat exchanger with multi-stage expansion device

Country Status (5)

Country Link
US (1) US20100037652A1 (en)
EP (1) EP2079968A4 (en)
CN (1) CN101589278B (en)
HK (1) HK1138354A1 (en)
WO (1) WO2008045111A1 (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103712376A (en) * 2013-12-30 2014-04-09 杭州三花微通道换热器有限公司 Heat exchanger integrated with throttling device and refrigerating system with heat exchanger
CN111699351A (en) * 2018-03-27 2020-09-22 东芝开利株式会社 Heat exchanger, heat exchange module, and refrigeration cycle device

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2009018150A1 (en) 2007-07-27 2009-02-05 Johnson Controls Technology Company Multichannel heat exchanger
US8943854B2 (en) * 2009-01-06 2015-02-03 Danfoss Qinbao (Hangzhou) Plate Heat Exchanger Company Limited Heat exchanger and air condition system
US11022382B2 (en) 2018-03-08 2021-06-01 Johnson Controls Technology Company System and method for heat exchanger of an HVAC and R system
US11879676B2 (en) 2021-07-30 2024-01-23 Danfoss A/S Thermal expansion valve for a heat exchanger and heat exchanger with a thermal expansion valve

Family Cites Families (57)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4474232A (en) * 1981-07-02 1984-10-02 Carrier Corporation Heat exchange unit for both vertical and horizontal applications
US4548050A (en) * 1983-05-31 1985-10-22 Carrier Corporation High efficiency fan coil unit
US4620423A (en) * 1985-09-25 1986-11-04 Carrier Corporation Expansion devices for a multizone heat pump system
US5279360A (en) * 1985-10-02 1994-01-18 Modine Manufacturing Co. Evaporator or evaporator/condenser
US4829780A (en) * 1988-01-28 1989-05-16 Modine Manufacturing Company Evaporator with improved condensate collection
US4787210A (en) * 1988-02-05 1988-11-29 Thermo King Corporation Bus air conditioning unit
US4993487A (en) * 1989-03-29 1991-02-19 Sundstrand Corporation Spiral heat exchanger
US4922732A (en) * 1989-11-20 1990-05-08 Dyna-Manufacturing, Ltd. Evaporator system for refrigeration systems
US4972678A (en) * 1989-11-24 1990-11-27 Finlayson Donald F Refrigeration and heat exchange system and process
US5245843A (en) * 1991-01-31 1993-09-21 Nippondenso Co., Ltd. Evaporator
JP3459271B2 (en) * 1992-01-17 2003-10-20 株式会社デンソー Heater core of automotive air conditioner
US5390507A (en) * 1992-09-17 1995-02-21 Nippondenso Co., Ltd. Refrigerant evaporator
JP2917764B2 (en) * 1992-09-17 1999-07-12 株式会社デンソー Evaporator for cooling system
US5326537A (en) * 1993-01-29 1994-07-05 Cleary James M Counterflow catalytic device
DE4422178A1 (en) * 1993-07-03 1995-01-12 Flitsch E Gmbh & Co Device for distributing coolant in an evaporator
KR0136759B1 (en) * 1993-09-15 1998-07-01 김광호 Airconditioner
JPH07284642A (en) * 1994-04-19 1995-10-31 Hisao Kojima Mixing element and production therefor
US5755107A (en) * 1994-09-22 1998-05-26 Denso Corporation Automotive air conditioner
CN1044334C (en) * 1994-12-28 1999-07-28 黄为民 Stirring caldron
US5826649A (en) * 1997-01-24 1998-10-27 Modine Manufacturing Co. Evaporator, condenser for a heat pump
KR19980068338A (en) * 1997-02-18 1998-10-15 김광호 Refrigerant Expansion Device
US5910167A (en) * 1997-10-20 1999-06-08 Modine Manufacturing Co. Inlet for an evaporator
US6032728A (en) * 1998-11-12 2000-03-07 Livernois Research & Development Co. Variable pitch heat exchanger
JP2000346568A (en) * 1999-05-31 2000-12-15 Mitsubishi Heavy Ind Ltd Heat exchanger
US6449979B1 (en) * 1999-07-02 2002-09-17 Denso Corporation Refrigerant evaporator with refrigerant distribution
US6478081B1 (en) * 1999-08-04 2002-11-12 Apv North America Inc. Plate heat exchanger
US6289924B1 (en) * 2000-02-24 2001-09-18 Richard C. Kozinski Variable flow area refrigerant expansion device
KR100365022B1 (en) * 2000-05-04 2002-12-16 한국기계연구원 Loop heat transfer device with high efficiency fin
JP3644358B2 (en) * 2000-07-05 2005-04-27 株式会社デンソー Refrigeration cycle decompression device
US6877550B2 (en) * 2000-07-21 2005-04-12 Denso Corporation Vehicle air conditioner
US6457325B1 (en) * 2000-10-31 2002-10-01 Modine Manufacturing Company Refrigeration system with phase separation
US6460358B1 (en) * 2000-11-13 2002-10-08 Thomas H. Hebert Flash gas and superheat eliminator for evaporators and method therefor
US6964296B2 (en) * 2001-02-07 2005-11-15 Modine Manufacturing Company Heat exchanger
US6557371B1 (en) * 2001-02-08 2003-05-06 York International Corporation Apparatus and method for discharging fluid
CN1526063A (en) * 2001-03-14 2004-09-01 昭和电工株式会社 Layered heat exchanger, layered evaporator for motor vehicle air conditioners and refrigeration system
US6460372B1 (en) * 2001-05-04 2002-10-08 Carrier Corporation Evaporator for medium temperature refrigerated merchandiser
TW552382B (en) * 2001-06-18 2003-09-11 Showa Dendo Kk Evaporator, manufacturing method of the same, header for evaporator and refrigeration system
JP4109444B2 (en) * 2001-11-09 2008-07-02 Gac株式会社 Heat exchanger and manufacturing method thereof
US6725913B2 (en) * 2001-11-30 2004-04-27 Modine Manufacturing Company High pressure header and heat exchanger and method of making the same
US20030116310A1 (en) * 2001-12-21 2003-06-26 Wittmann Joseph E. Flat tube heat exchanger core with internal fluid supply and suction lines
JP3945252B2 (en) * 2002-01-10 2007-07-18 株式会社デンソー Gas-liquid separator for ejector cycle
US6715539B2 (en) * 2002-02-19 2004-04-06 Michael Bianco Heat exchanger and airflow therethrough
CA2476592A1 (en) * 2002-02-28 2003-09-04 Marc A. Paradis Method and apparatus for cooling and dehumidifying air
JP3960233B2 (en) * 2002-04-03 2007-08-15 株式会社デンソー Heat exchanger
CA2381214C (en) * 2002-04-10 2007-06-26 Long Manufacturing Ltd. Heat exchanger inlet tube with flow distributing turbulizer
US6688138B2 (en) * 2002-04-16 2004-02-10 Tecumseh Products Company Heat exchanger having header
US6814136B2 (en) * 2002-08-06 2004-11-09 Visteon Global Technologies, Inc. Perforated tube flow distributor
AU2003262034A1 (en) * 2002-09-10 2004-04-30 Gac Corporation Heat exchanger and method of producing the same
PT1413845E (en) * 2002-10-25 2005-10-31 Denso Thermal Systems Spa CONDENSER FOR VEHICLES
JP4280545B2 (en) * 2003-05-14 2009-06-17 カルソニックカンセイ株式会社 Combined heat exchanger
JP4221244B2 (en) * 2003-05-14 2009-02-12 カルソニックカンセイ株式会社 Combined heat exchanger
JP4222137B2 (en) * 2003-07-22 2009-02-12 株式会社デンソー Radiator
US6912864B2 (en) * 2003-10-10 2005-07-05 Hussmann Corporation Evaporator for refrigerated merchandisers
US6848268B1 (en) * 2003-11-20 2005-02-01 Modine Manufacturing Company CO2 cooling system
EP1548380A3 (en) * 2003-12-22 2006-10-04 Hussmann Corporation Flat-tube evaporator with micro-distributor
CN2745001Y (en) * 2004-12-02 2005-12-07 珠海格力电器股份有限公司 Liquid separator of air conditioner
MX2007009244A (en) * 2005-02-02 2007-09-04 Carrier Corp Heat exchanger with multiple stage fluid expansion in header.

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103712376A (en) * 2013-12-30 2014-04-09 杭州三花微通道换热器有限公司 Heat exchanger integrated with throttling device and refrigerating system with heat exchanger
CN111699351A (en) * 2018-03-27 2020-09-22 东芝开利株式会社 Heat exchanger, heat exchange module, and refrigeration cycle device

Also Published As

Publication number Publication date
WO2008045111A1 (en) 2008-04-17
CN101589278B (en) 2011-07-06
US20100037652A1 (en) 2010-02-18
EP2079968A4 (en) 2013-05-01
HK1138354A1 (en) 2010-08-20
EP2079968A1 (en) 2009-07-22

Similar Documents

Publication Publication Date Title
US10234181B2 (en) Flash gas bypass evaporator
CN100549567C (en) Refrigerant distribution device and method
CN100538249C (en) The mini-channel heat exchanger that has the collector that reduces size
CN101558277B (en) Multi-pass heat exchangers having return manifolds with distributing inserts
KR100908769B1 (en) Co-current heat exchangers and methods to promote uniform refrigerant flow
EP2242963B1 (en) Heat exchanger including multiple tube distributor
KR100830301B1 (en) Heat exchanger with multiple stage fluid expansion in header
CN101589278B (en) Multi-channel heat exchanger with multi-stage expansion device
US6250103B1 (en) Condenser and air conditioning refrigeration system and using same
AU2005326650A1 (en) Liquid-vapor separator for a minichannel heat exchanger
JP2008528941A (en) Small channel heat exchanger header
CN105209846A (en) Heat exchanger
EP4130638A1 (en) Heat exchanger
CN112833589B (en) Condenser and air conditioner comprising same
WO2021070808A1 (en) Cooling device
CN107131687B (en) Heat exchange device suitable for low-pressure refrigerant
KR20150098835A (en) Condenser
WO2013184522A1 (en) Heat exchanger, and method of distributing refrigerant therein
US20190024954A1 (en) Heat Exchange System
CN114198946A (en) Coil pipe micro-channel heat exchanger and air conditioner
WO2019215837A1 (en) Heat exchanger, indoor unit, outdoor unit, air conditioner, method for manufacturing communication pipe, and method for manufacturing heat exchanger
CN105526740A (en) Evaporator and air conditioner comprising same
CN221881770U (en) Heat exchanger, refrigerant circulation system and air conditioner
JP2001208451A (en) Refrigerant distributor
KR20160119378A (en) Double pipe heat-exchanger with one body type connector

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
REG Reference to a national code

Ref country code: HK

Ref legal event code: DE

Ref document number: 1138354

Country of ref document: HK

C14 Grant of patent or utility model
GR01 Patent grant
REG Reference to a national code

Ref country code: HK

Ref legal event code: GR

Ref document number: 1138354

Country of ref document: HK

CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20110706

Termination date: 20161219

CF01 Termination of patent right due to non-payment of annual fee