CN1611897A - Refrigerant branching structure for superfine pipeline heat exchanger - Google Patents
Refrigerant branching structure for superfine pipeline heat exchanger Download PDFInfo
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- CN1611897A CN1611897A CN 200310106835 CN200310106835A CN1611897A CN 1611897 A CN1611897 A CN 1611897A CN 200310106835 CN200310106835 CN 200310106835 CN 200310106835 A CN200310106835 A CN 200310106835A CN 1611897 A CN1611897 A CN 1611897A
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Abstract
This invention provides a kind of refrigerant shunt structure with superfine heat exchanger. It can adjust partition spacing along the flow direction of the refrigerant, and adjusts the refrigerant distribution with different methods according to the sectional area of the refrigerant tube bank. The heat exchanger of this invention includes level header, several vertical refrigerant tube banks. The level header is hollow, so the refrigerant can flow through it. The several tube banks insert in the level header, so it can distribute the refrigerant that flow in the level header. Partitions are set between the vertical refrigerant tubes in the level header; they can change the flow direction of the refrigerant. The vertical refrigerant tube banks are set along the flow direction of the refrigerant. The sectional areas of the refrigerant tube banks are different, so the refrigerant can flow uniformly in the heat exchanger, and can most raise the efficiency of the heat exchanger.
Description
Technical field
The present invention relates to heat exchanger, relate in particular to a kind of by regulating the interval that cuts off along the flow direction of cold-producing medium and being designed to the refrigerant flow dividing structure that method inequality regulates and distributes the ultra-fine pipeline thermal interchanger of cold-producing medium with the refrigerant pipe group cross-section is long-pending.
Background technology
General heat exchanger is to be applied in indoor temperature rising or the air regulators such as air conditioner that reduces or warm-air drier.Fig. 1 is existing heat exchanger outward appearance schematic side view, and each forms structure annexation decomposing schematic representation to Fig. 2 for existing heat exchanger, and Fig. 3 is an arm schematic cross-section shown in Figure 2.
Can learn that with reference to above-mentioned accompanying drawing existing heat exchanger promptly is positioned at the upper header 2 corresponding to lower header 1 top by constituting with the lower part; Several arms 3 between upper header 2 and lower header 1; Be installed in the pin 6 between each arm 3.Above-mentioned lower header 1 cylindrical shape, its inside is hollow form, and its outer peripheral portion one side forms several and is used to insert and the fixing header aperture 4 of arm 3, and these header aperture 4 are provided with identical distance along the length direction of lower header 1.And upper header 2 that be positioned at its top corresponding with lower header 1 has the shape identical with lower header 1.Each arm 3 is separately fixed in each header aperture 4 along the two ends of its length direction, thereby each arm 3 is arranged side by side along the length direction of collector 1,2.
Because moving air is to keep the mode at certain angle of inclination to flow towards the face that the axis on the length direction of two collectors 1,2 is coupled together in using, thereby, can flow through the gap of each arm 3 and two collectors 1,2.Arm 3 has certain length, thickness and width, wherein, length is meant that it is fixed on distance between the two ends on two collectors 1,2, thickness be meant it with the flow direction of moving air keep distance on the vertical direction, width be meant it with the flow direction keeping parallelism direction of moving air on distance.Arm 3 is at right angles tetragonal tabular, and it has the width and the very thin thickness that can be inserted in two collectors 1,2, and its inside forms the pipeline (channel) 5 of several hollows.
In addition, each arm 3 is being fixed on two collectors 1,2 with the mode of the flow direction keeping parallelism of moving air on the width with each arm 3.On the direction vertical, have small sectional area at several pipelines 5 that form on each arm 3, and have certain length, and they are arranged in proper order along the flow direction of moving air along arm 3 length directions with arm 3 length directions.Because having the both-side ends of the arm 3 of said structure is fixed on two collectors 1,2, thereby, arm 3 is connected with the hollow spaces that form in collector 1,2 inside, and, gap at each arm 3, can to make the space that moving air flows through and needle body 6 is installed respectively in order to form, promptly above-mentioned each needle body 6 is owing to be and have the tabular of very thin thickness, therefore can be bent into several " it " word shapes and is installed between each arm 3.Though above-mentioned needle body 6 can be installed with multiple fixed in shape,, in general preferably select to make its formed space can make the flow impedance of moving air reach minimum shape.
Fig. 4 is the cross-sectional schematic of partition of the prior art with the same intervals installment state, and Fig. 5 is the simple schematic diagram of the long-pending cold-producing medium nest of tubes of same cross-sectional in the prior art.
As shown in Figure 4, several arms 3 can be divided into several nest of tubes, are base unit with above-mentioned each nest of tubes then, make each nest of tubes front and back replace the partition that is equiped with the flow direction that is used to change the cold-producing medium that flows to lower header 1 and upper header 2.Promptly the rearmost end place is equiped with the 1st partition below the 1st nest of tubes, and the rearmost end place is equiped with the 2nd partition above the 2nd nest of tubes, and the rearmost end place is equiped with the 3rd partition below the 3rd nest of tubes, and the 4th partition is equipped with at the rearmost end place above the 4th nest of tubes.In this heat exchanger that possesses partition-type structures, the cold-producing medium that at first flows into lower header 1 can rise by the 1st nest of tubes, cold-producing medium after the rising can move horizontally along upper header 2, be subjected to the 2nd interference effect that cuts off afterwards, thereby descend downwards along the 2nd nest of tubes, afterwards, rise and descend along Zhi Guanqun repeatedly in aforesaid mode, and in the process that moves along arm 3 by this way, heat can conduct to the needle body 6 that is fixed on the arm 3, realizes effective heat exchange by the surface and the moving air of needle body 6 at last.
Because, the cold-producing medium of the two states that mixes for gaseous state and liquid two states, when cold-producing medium divides timing from collector to refrigerant pipe, along with the flow direction of cold-producing medium (down → go up or on → down) its partition characteristic can dissimilate.But, in existing heat exchanger, because the interval between cutting off is identical, and the refrigerant pipe between cutting off is also irrelevant with the flow direction of cold-producing medium, and have identical sectional area, so gas-liquid can not get uniform distribution, thus the problem that causes evaporator effectiveness to reduce.
Summary of the invention
Main purpose of the present invention is to overcome the above-mentioned shortcoming that existing product exists, and provide a kind of refrigerant flow dividing structure (Micro Channel Heater Exchanger) of ultra-fine pipeline thermal interchanger, its flow direction along cold-producing medium is provided with the cold-producing medium nest of tubes, by regulating the interval that cuts off along the flow direction of cold-producing medium and being designed to method inequality and regulating and distributing cold-producing medium the refrigerant pipe group cross-section is long-pending, reach the effect that cold-producing medium flows equably in heat exchanger inside, to improve the purpose of effectiveness of heat exchanger to greatest extent.
The objective of the invention is to realize by following technical scheme.
The refrigerant flow dividing structure of a kind of ultra-fine pipeline thermal interchanger of the present invention, it is characterized in that: heat exchanger comprises: level header, it is a hollow form, thereby cold-producing medium is flow through; Several vertical cold-producing medium nest of tubes, they are inserted in the above-mentioned level header, can be distributed in the cold-producing medium that flows in the level header; Cut off, it is arranged between the vertical refrigerant pipe of level header inside, can change the flow direction of cold-producing medium; This vertical cold-producing medium nest of tubes is along the flow direction setting of cold-producing medium, and the sectional area of cold-producing medium nest of tubes is inequality separately.
The refrigerant flow dividing structure of aforesaid ultra-fine pipeline thermal interchanger, wherein heat exchanger application is in evaporimeter, and the sectional area of cold-producing medium nest of tubes is to make the sectional area ratio of the cold-producing medium nest of tubes that the internal refrigeration storage agent rises make the sectional area of the cold-producing medium nest of tubes that the internal refrigeration storage agent descends big.
The refrigerant flow dividing structure of aforesaid ultra-fine pipeline thermal interchanger, wherein heat exchanger application is in condenser, and the sectional area of cold-producing medium nest of tubes is to make the sectional area ratio of the cold-producing medium nest of tubes that the internal refrigeration storage agent descends make the sectional area of the cold-producing medium nest of tubes that the internal refrigeration storage agent rises big.
Description of drawings
Fig. 1 is the outward appearance schematic side view of existing heat exchanger.
Each forms the decomposing schematic representation of structure annexation to Fig. 2 for existing heat exchanger.
Fig. 3 is an arm schematic cross-section shown in Figure 2.
Fig. 4 is the cross-sectional schematic of cutting off in the prior art with the same intervals installment state.
Fig. 5 is the simple schematic diagram of the long-pending cold-producing medium nest of tubes of same cross-sectional in the prior art.
Fig. 6 a is the long-pending simple schematic diagram that is designed to evaporimeter inequality in refrigerant pipe of the present invention group cross-section.
Fig. 6 b is the long-pending simple cross-sectional schematic that is designed to condenser inequality in refrigerant pipe of the present invention group cross-section.
The number in the figure explanation: 1 lower header (header), 2 upper header, 3 arms (tube), 4 header aperture, 5 pipelines (channel), 6 needle bodies (pin), 7 cut off.
The specific embodiment
The feature of the refrigerant flow dividing structure of the ultra-fine pipeline thermal interchanger of the present invention is: at first be its heat exchanger by constituting with lower member: level header, it is a hollow form, thereby cold-producing medium is flow through; Several vertical cold-producing medium nest of tubes, they are inserted in the level header, can be distributed in the cold-producing medium that flows in the level header; Cut off, they are arranged between the vertical refrigerant pipe of level header inside, can change the flow direction of cold-producing medium.In such heat exchanger, vertical cold-producing medium nest of tubes is along the flow direction setting of cold-producing medium, and the sectional area of its cold-producing medium nest of tubes is designed to sectional area inequality.
Desirable embodiment to the ultra-fine pipeline thermal interchanger of the present invention refrigerant flow dividing structure describes in detail with reference to the accompanying drawings.
Fig. 6 a is the long-pending simple schematic diagram that is designed to the evaporimeter of sectional area inequality in refrigerant pipe of the present invention group cross-section.Can learn with reference to Fig. 6 a, this be one the embodiment of heat exchanger application of the present invention in evaporimeter, can shunt rising by the first cold-producing medium nest of tubes A by the cold-producing medium that lower header flows into, thereby the cold-producing medium that arrives upper header can descend again by the second cold-producing medium nest of tubes B, and above-mentioned cold-producing medium can rise and descend by this way repeatedly.Here, the sectional area of the sectional area ratio second cold-producing medium nest of tubes B of the first cold-producing medium nest of tubes A is big, and the sectional area of the sectional area ratio second cold-producing medium nest of tubes B of the 3rd cold-producing medium nest of tubes C is big.Along the flow direction of cold-producing medium the sectional area of cold-producing medium nest of tubes is designed to the mode of sectional area inequality like this respectively, promptly inside is had that refrigerant pipe group cross-section that cold-producing medium rises is long-pending to be designed greatlyyer than inner sectional area with cold-producing medium nest of tubes that cold-producing medium descends, cold-producing medium is flowed in heat exchanger equably.Preferably inside is had the ratio that cold-producing medium nest of tubes that cold-producing medium rises and inside has a sectional area of the cold-producing medium nest of tubes that cold-producing medium descends here, and be designed to 10～60%.
Fig. 6 b is designed to the refrigerant pipe sectional area for the present invention the simple schematic diagram of condenser inequality.Can learn with reference to Fig. 6 b, this be one the embodiment of heat exchanger application of the present invention in condenser, can shunt decline by the first cold-producing medium nest of tubes A by the cold-producing medium that upper header flows into, can rise again by the second cold-producing medium nest of tubes B thereby arrive the lower header cold-producing medium, and above-mentioned cold-producing medium can descend and rise by this way repeatedly.Here, the sectional area of the sectional area ratio second cold-producing medium nest of tubes B of the first cold-producing medium nest of tubes C is big, and the sectional area of the sectional area ratio second cold-producing medium nest of tubes B of the 3rd cold-producing medium nest of tubes A is big.Flow direction along cold-producing medium is designed to mode inequality to the sectional area of cold-producing medium nest of tubes respectively like this, promptly the sectional area that inside is had a cold-producing medium nest of tubes that cold-producing medium descends designs greatlyyer than inner sectional area with cold-producing medium nest of tubes that cold-producing medium rises, and cold-producing medium is flowed in heat exchanger equably.Preferably inside is had the ratio that cold-producing medium nest of tubes that cold-producing medium rises and inside has a sectional area of the cold-producing medium nest of tubes that cold-producing medium descends here, and make 10～60%.
The refrigerant flow dividing structure of the ultra-fine pipeline thermal interchanger of the present invention can reach following effect, promptly can by will be along the refrigerant pipe group cross-section of the flow direction setting of cold-producing medium long-pending design the method that has nothing in common with each other, can make cold-producing medium inner evenly mobile, and can improve the efficient of heat exchanger to greatest extent at heat exchanger.
Claims (3)
1, a kind of refrigerant flow dividing structure of ultra-fine pipeline thermal interchanger, it is characterized in that: heat exchanger comprises: level header, it is a hollow form, thereby cold-producing medium is flow through; Several vertical cold-producing medium nest of tubes, they are inserted in the above-mentioned level header, can be distributed in the cold-producing medium that flows in the level header; Cut off, it is arranged between the vertical refrigerant pipe of level header inside, can change the flow direction of cold-producing medium; This vertical cold-producing medium nest of tubes is along the flow direction setting of cold-producing medium, and the sectional area of cold-producing medium nest of tubes is inequality separately.
2, the refrigerant flow dividing structure of ultra-fine pipeline thermal interchanger according to claim 1, it is characterized in that: described heat exchanger application is in evaporimeter, and the sectional area of cold-producing medium nest of tubes is to make the sectional area ratio of the cold-producing medium nest of tubes that the internal refrigeration storage agent rises make the sectional area of the cold-producing medium nest of tubes that the internal refrigeration storage agent descends big.
3, the refrigerant flow dividing structure of ultra-fine pipeline thermal interchanger according to claim 1, it is characterized in that: described heat exchanger application is in condenser, and the sectional area of cold-producing medium nest of tubes is to make the sectional area ratio of the cold-producing medium nest of tubes that the internal refrigeration storage agent descends make the sectional area of the cold-producing medium nest of tubes that the internal refrigeration storage agent rises big.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB2003101068357A CN100398968C (en) | 2003-10-30 | 2003-10-30 | Refrigerant branching structure for superfine pipeline heat exchanger |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB2003101068357A CN100398968C (en) | 2003-10-30 | 2003-10-30 | Refrigerant branching structure for superfine pipeline heat exchanger |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN1611897A true CN1611897A (en) | 2005-05-04 |
| CN100398968C CN100398968C (en) | 2008-07-02 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNB2003101068357A Expired - Fee Related CN100398968C (en) | 2003-10-30 | 2003-10-30 | Refrigerant branching structure for superfine pipeline heat exchanger |
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| CN (1) | CN100398968C (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101858672A (en) * | 2010-06-29 | 2010-10-13 | 三花丹佛斯（杭州）微通道换热器有限公司 | Heat exchanger with improved heat exchange property |
| CN102230692A (en) * | 2010-06-29 | 2011-11-02 | 三花丹佛斯（杭州）微通道换热器有限公司 | Heat exchanger with improved heat exchange performance |
| CN104620069A (en) * | 2012-09-04 | 2015-05-13 | 夏普株式会社 | Parallel-flow type heat exchanger and air conditioner equipped with same |
Family Cites Families (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP3661275B2 (en) * | 1996-05-29 | 2005-06-15 | 株式会社デンソー | Stacked evaporator |
| US5826649A (en) * | 1997-01-24 | 1998-10-27 | Modine Manufacturing Co. | Evaporator, condenser for a heat pump |
| JP2000346568A (en) * | 1999-05-31 | 2000-12-15 | Mitsubishi Heavy Ind Ltd | Heat exchanger |
| JP2002071283A (en) * | 2000-08-30 | 2002-03-08 | Zexel Valeo Climate Control Corp | Heat exchanger |
| KR100382523B1 (en) * | 2000-12-01 | 2003-05-09 | 엘지전자 주식회사 | a tube structure of a micro-multi channel heat exchanger |
-
2003
- 2003-10-30 CN CNB2003101068357A patent/CN100398968C/en not_active Expired - Fee Related
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101858672A (en) * | 2010-06-29 | 2010-10-13 | 三花丹佛斯（杭州）微通道换热器有限公司 | Heat exchanger with improved heat exchange property |
| CN102230692A (en) * | 2010-06-29 | 2011-11-02 | 三花丹佛斯（杭州）微通道换热器有限公司 | Heat exchanger with improved heat exchange performance |
| CN102230692B (en) * | 2010-06-29 | 2012-11-14 | 三花控股集团有限公司 | Heat exchanger with improved heat exchange performance |
| CN104620069A (en) * | 2012-09-04 | 2015-05-13 | 夏普株式会社 | Parallel-flow type heat exchanger and air conditioner equipped with same |
| CN104620069B (en) * | 2012-09-04 | 2016-08-31 | 夏普株式会社 | Parallel flow heat exchanger and the air conditioner being provided with this parallel flow heat exchanger |
Also Published As
| Publication number | Publication date |
|---|---|
| CN100398968C (en) | 2008-07-02 |
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Granted publication date: 20080702 Termination date: 20191030 |
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| CF01 | Termination of patent right due to non-payment of annual fee |