CN101691971B - Heat exchanger - Google Patents

Heat exchanger Download PDF

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Publication number
CN101691971B
CN101691971B CN200910168195XA CN200910168195A CN101691971B CN 101691971 B CN101691971 B CN 101691971B CN 200910168195X A CN200910168195X A CN 200910168195XA CN 200910168195 A CN200910168195 A CN 200910168195A CN 101691971 B CN101691971 B CN 101691971B
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CN
China
Prior art keywords
heat exchanger
outlet
collecting pipe
outlet header
header
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.)
Active
Application number
CN200910168195XA
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Chinese (zh)
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CN101691971A (en
Inventor
蒋建龙
黄宁杰
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.)
Sanhua Hangzhou Micro Channel Heat Exchanger Co Ltd
Danfoss AS
Original Assignee
Danfoss Sanhua Hangzhou Micro Channel Heat Exchanger Co Ltd
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 Danfoss Sanhua Hangzhou Micro Channel Heat Exchanger Co Ltd filed Critical Danfoss Sanhua Hangzhou Micro Channel Heat Exchanger Co Ltd
Priority to CN200910168195XA priority Critical patent/CN101691971B/en
Publication of CN101691971A publication Critical patent/CN101691971A/en
Application granted granted Critical
Publication of CN101691971B publication Critical patent/CN101691971B/en
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    • 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
    • F28F9/027Header boxes; End plates with static flow control means, e.g. with means for uniformly distributing heat exchange media into conduits in the form of distribution pipes

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  • Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)

Abstract

The invention provides a heat exchanger. The heat exchanger comprises an outlet current collecting pipe and an outlet collecting pipe, wherein the outlet collecting pipe is connected with the outlet current collecting pipe, and the outlet collecting pipe is inserted into the outlet current collecting pipe in predetermined depth from the end of the outlet current collecting pipe. By extending the outlet collecting pipe into the outlet current collecting pipe, a refrigerant in the outlet current collecting pipe does not need to flow to a near end from a far end so as to balance the resistance of the refrigerant between a flat pipe at the far end and a flat pipe at the near end and improve the distribution of the refrigerant in the flat pipe at the far end and the flat pipe at the near end.

Description

Heat exchanger
Technical field
The present invention relates to a kind of heat exchanger.
Background technology
Existing heat exchanger such as parallel-flow heat exchanger, micro-channel heat exchanger or minichannel heat exchanger as shown in Fig. 1 to 2, heat exchanger 100 ' the comprise inlet header 13 and the outlet header 33 that are separately positioned on both sides (for example upside and downside).The flow direction of cold-producing medium in inlet header 13 and outlet header 33 is respectively by Reference numeral 15 and 35 ' indication.Heat exchanger 100 ' also comprise inlet tube 11 and outlet 31 ', and flat tube 20.Inlet tube 11 and outlet 31 ' be directly welded in respectively on inlet header 13 and the outlet header 33.Flat tube near outlet 31 ' one sides is called the near-end flat tube, and is called the far-end flat tube away from the flat tube of outlet 31 ' one sides.Be provided with fin 23 between the flat tube.
Because outlet header 33 inside have flat tube 20 to stretch into, as shown in Figure 2, cold-producing medium 50 flows in outlet header 33 and is subjected to stretching into the interference of flat tube 20, whirlpool occurs along journey, and flow resistance is very big.Thereby make the cold-producing medium circulation of far-end flat tube be far smaller than the circulation of near-end flat tube, cause the skewness of cold-producing medium in each flat tube, influence the heat transfer property of heat exchanger.Simultaneously, heat exchanger internal refrigeration storage agent resistance greatly also influences the performance of refrigeration system.
Summary of the invention
The purpose of this invention is to provide a kind of heat exchanger, this heat exchanger can improve the cold-producing medium assignment problem of far-end flat tube and near-end flat tube.
According to an aspect of the present invention, the invention provides a kind of heat exchanger, this heat exchanger comprises: the outlet header; With the outlet collecting pipe that the outlet header is connected, its middle outlet collecting pipe inserts outlet header desired depth from the end of outlet header.
According to a further aspect in the invention, described desired depth is about 1/3 to 1 of an outlet header length.
According to a further aspect in the invention, have one or more openings in the sidewall of the part in the insertion of the described outlet collecting pipe outlet header.
The ratio of the cross-sectional area of the internal fluid channels of the part in the cross-sectional area sum of the cross-sectional area of a described opening or described a plurality of openings and the insertion of the described outlet collecting pipe outlet header is 0.5~2.
According to a further aspect in the invention, the hydraulic radius of the part in the insertion of the described outlet collecting pipe outlet header is 0.25~0.69 with the ratio of the water conservancy radius of outlet header.
According to a further aspect in the invention, described heat exchanger is parallel-flow heat exchanger, micro-channel heat exchanger or minichannel heat exchanger.
Among the present invention, extend into outlet header inside by exporting collecting pipe, the cold-producing medium of outlet in the header need not flow to near-end from far-end, thus can balance far-end flat tube with the near-end flat tube between the cold-producing medium resistance, thereby can improve the cold-producing medium distribution of far-end flat tube and near-end flat tube.
Description of drawings
Fig. 1 is the schematic diagram of the heat exchanger of prior art.
Fig. 2 is the local enlarged diagram of the heat exchanger of prior art.
Fig. 3 is the schematic diagram of heat exchanger according to an embodiment of the invention.
The specific embodiment
The present invention will be further described below in conjunction with the drawings and the specific embodiments.
As shown in Figure 3, the heat exchanger 100 according to embodiments of the invention 1 comprises inlet header 13 and the outlet header 33 that is separately positioned on both sides (for example upside and downside).The flow direction of cold-producing medium in inlet header 13 and outlet header 33 is respectively by Reference numeral 15 and 35 indications.Heat exchanger 100 also comprises inlet tube 11 and outlet collecting pipe 31, and flat tube 20.Inlet tube 11 and outlet collecting pipe 31 are connected to inlet header 13 and outlet header 33.Be provided with fin 23 between the flat tube.Outlet collecting pipe 31 inserts outlet header 33 desired depths from the end of outlet header 33.
The degree of depth that outlet collecting pipe 31 inserts outlet headers 33 mainly is subjected to the position influence of inlet tube 11, and insertion depth can be about 1/3 to 1 of the length of outlet header 33.
Because the insertion portion of outlet collecting pipe 31 has influenced near-end flat tube cold-producing medium fluid, open one or more openings thereby can insert on the part that exports header 33 at outlet collecting pipe 31.For example, can open vertical slot, translot, hole or any other shaped aperture.The ratio of the cross-sectional area of the internal fluid channels of the part in the cross-sectional area sum of the cross-sectional area of a described opening or described a plurality of openings and the insertion of the described outlet collecting pipe 31 outlet header 33 (i.e. the inner cross-sectional area of pipe) can be 0.5~2.
The hydraulic radius of the insertion portion of outlet collecting pipe 31 can be 0.25~0.69 with the ratio of the water conservancy radius of outlet header 33.
Heat exchanger 100 can be parallel-flow heat exchanger, micro-channel heat exchanger or minichannel heat exchanger, perhaps the heat exchanger of other type.
To export collecting pipe 31 and extend into outlet header 33 inside, cold-producing medium in the outlet header 33 need not flow to near-end from far-end, thereby can balance far-end flat tube and the near-end flat tube between the cold-producing medium resistance, thereby the cold-producing medium that can improve far-end flat tube and near-end flat tube distributes.

Claims (6)

1. heat exchanger comprises:
The outlet header;
With the outlet collecting pipe that the outlet header is connected, its middle outlet collecting pipe inserts outlet header desired depth from the end of outlet header.
2. heat exchanger according to claim 1, wherein
Described desired depth is about 1/3 to 1 of an outlet header length.
3. heat exchanger according to claim 1, wherein
Have one or more openings in the sidewall of the part in the insertion outlet header of described outlet collecting pipe.
4. heat exchanger according to claim 3, wherein
The ratio of the cross-sectional area of the internal fluid channels of the part in the cross-sectional area sum of the cross-sectional area of a described opening or described a plurality of openings and the insertion of the described outlet collecting pipe outlet header is 0.5~2.
5. heat exchanger according to claim 1, wherein
The hydraulic radius of the part in the insertion outlet header of described outlet collecting pipe is 0.25~0.69 with the ratio of the water conservancy radius of outlet header.
6. heat exchanger according to claim 5, wherein
Described heat exchanger is parallel-flow heat exchanger, micro-channel heat exchanger or minichannel heat exchanger.
CN200910168195XA 2009-09-03 2009-09-03 Heat exchanger Active CN101691971B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN200910168195XA CN101691971B (en) 2009-09-03 2009-09-03 Heat exchanger

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN200910168195XA CN101691971B (en) 2009-09-03 2009-09-03 Heat exchanger

Publications (2)

Publication Number Publication Date
CN101691971A CN101691971A (en) 2010-04-07
CN101691971B true CN101691971B (en) 2011-07-27

Family

ID=42080681

Family Applications (1)

Application Number Title Priority Date Filing Date
CN200910168195XA Active CN101691971B (en) 2009-09-03 2009-09-03 Heat exchanger

Country Status (1)

Country Link
CN (1) CN101691971B (en)

Families Citing this family (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102297547B (en) * 2011-06-27 2013-04-10 三花控股集团有限公司 Heat exchanger
CN103196310B (en) * 2013-04-02 2015-02-25 虞寿仁 Liquid-cooling heat exchanger with miniature mini-channel metal round tubes
CN104719047A (en) * 2015-03-30 2015-06-24 广东都灵新能源科技有限公司 Microchannel local constant-temperature heat exchange system of greenhouse
CN106482398A (en) * 2015-08-28 2017-03-08 杭州三花家电热管理系统有限公司 Micro-channel heat exchanger
CN108050579A (en) * 2017-12-23 2018-05-18 黑龙江聚拢华玺智能科技有限公司 A kind of low temp heating radiator
CN108050580A (en) * 2017-12-24 2018-05-18 黑龙江聚拢华玺智能科技有限公司 A kind of high-efficiency radiator

Also Published As

Publication number Publication date
CN101691971A (en) 2010-04-07

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C41 Transfer of patent application or patent right or utility model
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Owner name: SANHUA HOLDING GROUP CO., LTD.

Free format text: FORMER NAME: DANFOSS SANHUA (HANGZHOU) MICRO-CHANNEL HEAT EXCHANGER CO., LTD.

CP03 Change of name, title or address

Address after: 312500 Shaoxing City, Zhejiang province Xinchang Qixing street under the Liquan

Co-patentee after: DANFOSS A/S

Patentee after: SANHUA HOLDING GROUP Co.,Ltd.

Address before: 310018 Hangzhou economic and Technological Development Zone, Zhejiang, No. 12 Avenue, No. 289

Patentee before: DANFOSS SANHUA (HANGZHOU) MICRO CHANNEL HEAT EXCHANGER Co.,Ltd.

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Effective date of registration: 20120720

Address after: 310018 Hangzhou economic and Technological Development Zone, Zhejiang, No. 12 Avenue, No. 289

Patentee after: DANFOSS SANHUA (HANGZHOU) MICRO CHANNEL HEAT EXCHANGER Co.,Ltd.

Address before: 310018 Hangzhou economic and Technological Development Zone, Zhejiang, No. 21 Avenue, No. 60

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Address after: 310018 Hangzhou economic and Technological Development Zone, Zhejiang, No. 12 Avenue, No. 289

Patentee after: DANFOSS SANHUA (HANGZHOU) MICRO CHANNEL HEAT EXCHANGER Co.,Ltd.

Address before: 310018 Hangzhou economic and Technological Development Zone, Zhejiang, No. 21 Avenue, No. 60

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Effective date of registration: 20120906

Address after: 312500 Shaoxing City, Zhejiang province Xinchang Qixing street under the Liquan

Patentee after: SANHUA HOLDING GROUP Co.,Ltd.

Patentee after: DANFOSS A/S

Address before: 310018 Hangzhou economic and Technological Development Zone, Zhejiang, No. 12 Avenue, No. 289

Patentee before: DANFOSS SANHUA (HANGZHOU) MICRO CHANNEL HEAT EXCHANGER Co.,Ltd.

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Address after: 310018, No. 289-1, No. 12, Poplar Street, Hangzhou economic and Technological Development Zone, Hangzhou, Zhejiang

Patentee after: SANHUA (HANGZHOU) MICRO CHANNEL HEAT EXCHANGER Co.,Ltd.

Patentee after: DANFOSS A/S

Address before: 312500 Shaoxing City, Zhejiang province Xinchang Qixing street under the Liquan

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Contract record no.: 2015990000010

Denomination of invention: Plate heat exchanger for fluids of different flow

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