CN202041106U - Parallel flow heat exchanger - Google Patents

Parallel flow heat exchanger Download PDF

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Publication number
CN202041106U
CN202041106U CN2011200744687U CN201120074468U CN202041106U CN 202041106 U CN202041106 U CN 202041106U CN 2011200744687 U CN2011200744687 U CN 2011200744687U CN 201120074468 U CN201120074468 U CN 201120074468U CN 202041106 U CN202041106 U CN 202041106U
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CN
China
Prior art keywords
heat exchanger
parallel
header
flow heat
flat tube
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Expired - Fee Related
Application number
CN2011200744687U
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Chinese (zh)
Inventor
招伟
李惠燕
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TCL Air Conditioner Zhongshan Co Ltd
Original Assignee
TCL Air Conditioner Zhongshan Co Ltd
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Priority to CN2011200744687U priority Critical patent/CN202041106U/en
Application granted granted Critical
Publication of CN202041106U publication Critical patent/CN202041106U/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Abstract

A parallel flow heat exchanger comprises a left header pipe, a right header pipe and a heat exchange unit arranged between the left header pipe and the right header pipe, wherein the heat exchange unit comprises flat pipes and fins, one ends of the flat pipes are connected with the left header pipe, the other ends of the flat pipes are connected with the right header pipe, the flat pipes are composed of left lateral pipes and right lateral pipes, the left lateral pipes incline downward to be inserted into the left header pipe at an angle of A, and the right lateral pipes incline downward to be inserted into the right header pipe at an angle of B. The parallel flow heat exchanger realizes the self-drainage function, resolves the problem of freezing and frosting of parallel flow fins due to the self-drainage difficulty, and improves the parallel flow heat conversion rate.

Description

A kind of parallel-flow heat exchanger
Technical field
The utility model relates to air-conditioner parts technical field, more particularly, relates to a kind of parallel-flow heat exchanger.
Background technology
Along with improving constantly of living standards of the people, air-conditioner has entered huge numbers of families, and air-conditioning technical just towards energy-conservation, direction develops efficiently.Heat exchanger is as one of vitals in the air-conditioning system, and its heat exchange effect can directly influence the performance of whole system, and its weight and volume size also can influence the compactedness and the volume of complete machine.For the heat exchange efficiency that improves air-condition heat exchanger, reduce its installation footprint, its version is now from fin tube type, the stacked parallel flow type that develops into.Fin-tube heat exchanger is the heat exchanger structure that uses the earliest, and stacked heat exchanger is that a kind of runner is the plate type heat exchanger of U-shaped, its compact conformation, the heat exchange efficiency height, but difficulty of processing is bigger, and owing to be subjected to the restriction of appearance and size, it can not satisfy the condition of big heat exchange amount.Parallel-flow heat exchanger is a kind of novel flat pipe heat exchanger that grows up on the basis of fin tube type, stacked heat exchanger at present, and it has been considered to a kind of regeneration product of the most rising air-condition heat exchanger with efficient, compact characteristics.Referring to Fig. 1, Fig. 2, Fig. 4, the flat tube of existing parallel-flow heat exchanger all adopts horizontally disposed mode, the flat tube level is inserted in left header, the right header, when the air conditioner heat-production mode operation, when the temperature of parallel-flow heat exchanger was lower than environment temperature, the condensed water that airborne moisture content condensation is produced was attached to discharging on the flat tube of parallel-flow heat exchanger.Also may appear at air-conditioner running time frosting or icing phenomenon on the flat tube of concurrent flow when longer, cause the thermal conversion rate of air-conditioning system low, the heat exchange effect further worsens.
The utility model content
The utility model purpose is in order to overcome the deficiency that above-mentioned prior art exists, and a kind of thermal conversion rate height, parallel-flow heat exchanger that heating effect is good are provided.
The technical solution adopted in the utility model is, a kind of parallel-flow heat exchanger, comprise left header, right header, be located at the heat exchange unit between left header and right header, described heat exchange unit is made of flat tube and fin, one end of described flat tube connects left header, and the other end of described flat tube connects right header, and described flat tube is made of left side pipe and right side pipe, described left side pipe is with in the left header of the downward-sloping insertion of angle A, and described right side pipe is with in the right header of the downward-sloping insertion of angle B.
Above-mentioned parallel-flow heat exchanger, angle A equates with angle B numerical value.
Above-mentioned parallel-flow heat exchanger, angle A is in 10~80 degree scopes.
Above-mentioned parallel-flow heat exchanger, arrangement parallel to each other is managed in the left side of described flat tube, and arrangement parallel to each other is managed on the right side of described flat tube.
Above-mentioned parallel-flow heat exchanger, described left side pipe is provided with gutter channel in the end near left header, and described right side pipe is provided with gutter channel in the end near right header.
Above-mentioned parallel-flow heat exchanger is provided with the above coolant channel of twice or twice in the described flat tube.
Compared with prior art, the utlity model has following advantage:
1) because the flat tube of parallel-flow heat exchanger of the present utility model is divided into azimuth by-pass, azimuth by-pass is oblique connection left and right sides header respectively, condensed water on the flat tube is flowed down along the inclined-plane of flat tube, realized the self-drain function of parallel-flow heat exchanger, solved that concurrent flow fin that parallel-flow heat exchanger draining difficulty causes freezes and the problem of frosting, improved the parallel flow heat conversion ratio, when air-conditioning system is moved with heating mode, under the effect of water that parallel-flow heat exchanger produces, flow to both sides, make the parallel-flow heat exchanger heating effect better at gravity.
2) utilize the heat exchange unit of existing parallel-flow heat exchanger and the ripe assembly technology of left and right sides header in the wooden utility model, flat tube has improved production efficiency greatly being assemblied in behind the bending forming on the header of the left and right sides; Flat tube is a loose structure, has a plurality of coolant channels, and the gaseous refrigerant that produces in heat transfer process is in time drained in the header, and the flat tube heat exchange area of whole heat exchange unit is utilized more fully, thereby has further improved heat exchange efficiency.
Description of drawings
Fig. 1 is the structural front view of the parallel-flow heat exchanger of prior art;
Fig. 2 is the structure side view of Fig. 1;
Fig. 3 is the structural representation of parallel-flow heat exchanger of the present utility model;
Fig. 4 is the enlarged drawing of the I portion of Fig. 2;
Fig. 5 is the enlarged drawing of the II portion of Fig. 3;
Fig. 6 is the flat tube inclination angle schematic diagram of parallel-flow heat exchanger of the present utility model;
Fig. 7 is the flat tube configuration schematic diagram of parallel-flow heat exchanger of the present utility model.
The specific embodiment
Below pass through the specific embodiment, and the utility model is described in further detail in conjunction with the accompanying drawings.
Referring to Fig. 3, Fig. 5, Fig. 6, Fig. 7, the utility model provides a kind of parallel-flow heat exchanger, constitute by left header 3, right header 4, flat tube 1 and fin 2, the end of the left side pipe 11 of flat tube 1 connects left header 3, the end of the right side pipe 12 of flat tube 1 connects right header 4, the azimuth by-pass of flat tube 1 tilts to the header of both sides respectively, makes the moisture content on the heat exchanger can flow to both sides.Wherein, left side pipe 11 is with the left header 3 of downward-sloping insertion, and the right side manages 12 with the right header 4 of the downward-sloping insertion of angle B, and as shown in Figure 6, angle A is the angle of left side pipe 11 and horizontal plane, and angle B is the angle of right side pipe 12 and horizontal plane, and A=B.It is 10~80 degree that angle A, angle B have span.All left side pipe 11 arrangements parallel to each other of parallel-flow heat exchanger, all right side pipe 12 arrangements also parallel to each other.In order to make the smooth outflow heat exchanger of water, be provided with gutter channel near the end of left header 3 and right header 4 respectively at left side pipe 11, right side pipe 12.See Fig. 7, the flat tube 1 of parallel-flow heat exchanger of the present utility model is the porous flat pipe structure, is provided with the coolant channel 14 of multiple tracks in the flat tube 1.Make that the heat exchange area of flat tube 1 is utilized more fully, thereby further improve the exchange capability of heat of parallel-flow heat exchanger.
As another kind of embodiment, the fin 2 of strengthening the heat exchange effect can be the wave fin structure, as shown in Figure 7.
The course of work of cold-producing medium in parallel-flow heat exchanger is: under the air conditioner heat-production pattern, cold-producing medium flows in the multiple tracks coolant channel 14 of flat tube 1, and the convection current air is along flat tube 1 flows outside.The cold-producing medium that comes out from the throttling arrangement of air-conditioning system enters from the influent stream chamber of inlet tube through left header 3 (or right header 4), in the multiple tracks coolant channel 14 of flat tube 1, flow, enter right header 4 (or left header 3) then, leave parallel-flow heat exchanger from outlet.Flat tube 1 inner refrigerant is along with being overheated gas by liquid, two-phase state-transition gradually with the carrying out of the outer convection current air heat transfer process of pipe, and last overheated gaseous refrigerant is got back in the compressor of air conditioner.

Claims (6)

1. parallel-flow heat exchanger, comprise left header (3), right header (4), be located at the heat exchange unit between left header (3) and right header (4), described heat exchange unit is made of flat tube (1) and fin (2), one end of described flat tube (1) connects left header (3), the other end of described flat tube (1) connects right header (4), it is characterized in that: described flat tube (1) is made of left side pipe (11) and right side pipe (12), described left side pipe (11) is with in the left header of the downward-sloping insertion of angle A (3), and described right side pipe (12) is with in the right header of the downward-sloping insertion of angle B (4).
2. parallel-flow heat exchanger according to claim 1 is characterized in that: angle A equates with angle B numerical value.
3. parallel-flow heat exchanger according to claim 2 is characterized in that: angle A is in 10~80 degree scopes.
4. according to claim 2 or 3 described parallel-flow heat exchangers, it is characterized in that: left side pipe (11) arrangement parallel to each other of described flat tube (1), right side pipe (12) arrangement parallel to each other of described flat tube (1).
5. parallel-flow heat exchanger according to claim 4 is characterized in that: described left side pipe (11) is provided with gutter channel in the end near left header (3), and described right side pipe (12) is provided with gutter channel in the end near right header (4).
6. parallel-flow heat exchanger according to claim 5 is characterized in that: be provided with the above coolant channel (14) of twice or twice in the described flat tube (1).
CN2011200744687U 2011-03-21 2011-03-21 Parallel flow heat exchanger Expired - Fee Related CN202041106U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN2011200744687U CN202041106U (en) 2011-03-21 2011-03-21 Parallel flow heat exchanger

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN2011200744687U CN202041106U (en) 2011-03-21 2011-03-21 Parallel flow heat exchanger

Publications (1)

Publication Number Publication Date
CN202041106U true CN202041106U (en) 2011-11-16

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Family Applications (1)

Application Number Title Priority Date Filing Date
CN2011200744687U Expired - Fee Related CN202041106U (en) 2011-03-21 2011-03-21 Parallel flow heat exchanger

Country Status (1)

Country Link
CN (1) CN202041106U (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104061719A (en) * 2013-03-21 2014-09-24 杭州三花微通道换热器有限公司 Bent heat exchanger and manufacturing method thereof
CN105222405A (en) * 2015-10-30 2016-01-06 海信(山东)空调有限公司 Micro-channel heat exchanger and air-conditioner
CN105571349A (en) * 2016-02-18 2016-05-11 珠海格力电器股份有限公司 Heat exchanger

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104061719A (en) * 2013-03-21 2014-09-24 杭州三花微通道换热器有限公司 Bent heat exchanger and manufacturing method thereof
CN105222405A (en) * 2015-10-30 2016-01-06 海信(山东)空调有限公司 Micro-channel heat exchanger and air-conditioner
CN105571349A (en) * 2016-02-18 2016-05-11 珠海格力电器股份有限公司 Heat exchanger

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Date Code Title Description
C14 Grant of patent or utility model
GR01 Patent grant
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20111116

Termination date: 20190321

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