CN204730526U - A kind of micro-channel heat exchanger with liquid separation structure - Google Patents

Abstract

The utility model discloses a microchannel heat exchanger with a liquid separation structure, which comprises an upper collecting pipe, a lower collecting pipe, and a microchannel flat pipe. The lower collecting pipe or the lower collecting pipe mainly consists of an upper cover plate and a lower The cover plate clamps the distribution pipe and buckles it. The upper cover plate is provided with a number of flat tube slots connecting the microchannel flat tube along the length direction. There is a gap between the upper cover plate, the lower cover plate and the distribution pipe. The upper cover plate A partition plate is arranged parallel to the inner side of the plate and the lower cover plate along the length direction, and an inner rib plate is arranged along the axial direction in the inner cavity of the distribution pipe. One end of the distribution pipe is sealed, and several groups of distribution areas and flow chambers are arranged on the pipe wall A one-to-one correspondence with the set of connected split holes. The utility model evenly distributes the refrigerant into each circulation cavity through the distribution pipe; the pressure of the refrigerant flowing into each sector of the distribution pipe increases, and is sprayed into each circulation chamber through the distribution hole on the pipe, so that the gas-liquid two-phase refrigerant is mixed more After being uniform, it is distributed into the flat tube, thus increasing the uniformity of refrigerant distribution in the flat tube and improving the heat exchange efficiency of the heat exchanger.

Description

A Microchannel Heat Exchanger with Liquid Separation Structure

technical field

The utility model relates to a microchannel heat exchanger, in particular to a microchannel heat exchanger with a liquid separation structure.

Background technique

Due to its advantages of high heat transfer efficiency, small size, and light weight, microchannel heat exchangers are gradually applied to automotive air conditioners, household air conditioners, and other fields. The existing parallel microchannel heat exchanger generally consists of two headers, flat tubes connecting the two headers and windowed fins. Ideally, the distribution of refrigerant in each flat tube is uniform, and at this time the overall heat exchange efficiency of the heat exchanger is the best. But in reality, because the flat tube is long and thin, one input channel often corresponds to hundreds of fine channels, so when the refrigerant flows into the flat tube, it will be affected by gravity and resistance along the way, and the refrigerant distribution will be very uneven. Phenomenon.

At present, there are few applications of microchannel heat exchangers in occasions with large cooling and heating capacity, such as passenger car air conditioners. The main reason is that the existing design schemes with more than 3 processes are mostly used for large-area micro-channel heat exchangers, but the design of multiple processes will bring problems such as excessive pressure drop and increased power consumption of the compressor. Therefore, it is generally recommended to adopt a single-flow or less-flow design for the design of microchannel heat exchangers. On the other hand, if a single-flow design is adopted, the number of distribution flat tubes corresponding to a single inlet of a microchannel heat exchanger with a large heat transfer area often reaches tens or hundreds, and the problem of poor refrigerant distribution uniformity is difficult to solve solve. Therefore, how to improve the refrigerant distribution and drainage performance of parallel-flow microchannel heat exchangers with large heat exchange area and large aspect ratio, so as to improve the energy efficiency of the entire system, is an urgent problem to be solved by those skilled in the art.

Utility model content

The utility model aims to provide a micro-channel heat exchanger with a new split flow structure, so as to improve the distribution uniformity of the inlet of the micro-channel heat exchanger and the drainage performance of the fins with a large number of inserted flat tubes.

For the problems of the technologies described above, the technical solution provided by the utility model is:

A microchannel heat exchanger with a liquid separation structure, comprising an upper header and a lower header, and a microchannel flat tube connected between the upper header and the lower header, the lower header Or the upper header is mainly composed of the upper cover plate and the lower cover plate clamping the distribution pipe, and the upper cover plate is provided with a number of flat tube slots connecting the microchannel flat tubes along the length direction. The upper cover plate, There is a gap between the lower cover plate and the distribution pipe, and the inside of the upper cover plate and the lower cover plate are arranged in parallel along the length direction with a number of partition plates that divide the gap into at least two independent flow chambers. The distribution pipe A number of internal ribs are arranged in the inner cavity along the axial direction to divide the inner cavity into at least two independent distribution areas. The cavities correspond to the connected flow hole sets one by one, and the numbers of the flow cavity, the distribution area and the flow hole sets are consistent.

Further, the cross section of the distribution pipe is circular, elliptical, semicircular, rectangular, rhombus, triangular, or other shapes that can be evenly divided into N equal parts.

Further, each group of orifice sets includes 4-8 equidistant small holes arranged in a line.

Further, windowed fins are arranged between adjacent flat tubes of the microchannel.

Compared with the existing technology, the microchannel heat exchanger with liquid separation structure of the utility model divides the refrigerant evenly into N equal parts at the inlet of the refrigerant by using N equally divided distribution pipes, and then passes through different split flows The hole set sends the refrigerant into the corresponding independent circulation cavity. Moreover, the pressure of the refrigerant in the distribution pipe will increase, and the injection effect of the distribution hole set will make the gas-liquid mixed refrigerant evenly mixed, and then distribute into each microchannel flat tube. The use of this type of distribution pipe greatly improves The liquid distribution uniformity of the refrigerant in dozens or hundreds of microchannel flat tubes improves its heat exchange efficiency.

Description of drawings

Fig. 1 is a schematic diagram of the overall structure of an embodiment of the utility model.

Fig. 2 is a schematic exploded view of the lower header of the embodiment of the present invention.

Fig. 3 is a schematic structural view of the liquid pipe of the embodiment of the present invention.

FIG. 4 is an enlarged schematic diagram of point A in FIG. 3 .

5-10 are schematic cross-sectional views of other embodiments of the liquid pipe of the present invention.

Shown in the figure: 1-exit header; 2-upper header; 3-lower header; 31-lower cover; 32-upper cover; 321-flat tube slot; -separation plate; 4-window fin; 5-microchannel flat tube; 6-distribution pipe; 61-distribution hole set; 611~616-sub-distribution hole set; Rib; 64-distribution pipe end cover.

Detailed ways

The purpose of the utility model will be further described in detail below in conjunction with the accompanying drawings and specific embodiments, and the embodiments cannot be repeated here one by one, but the implementation of the utility model is not therefore limited to the following examples.

As shown in Figures 1 to 4, a microchannel heat exchanger with a liquid separation structure includes an upper header 2 and a lower header 3, and is arranged in communication between the upper header 2 and the lower header 3 Between the microchannel flat tubes 5, window fins 4 are arranged between the adjacent microchannel flat tubes 5, one end of the upper header 2 is sealed, and the other end is connected to the outlet header 1, and the lower header 2 is sealed. The flow pipe 3 is mainly formed by clamping the distribution pipe 6 with the upper cover 32 and the lower cover 31. The cross section of the distribution pipe 6 is circular, and the upper cover 32 is provided with a number of connecting microchannels along the length direction. The flat tube slot 321 of the flat tube 5, there is a gap between the upper cover plate 32, the lower cover plate 31 and the distributing pipe 6, and the inside of the upper cover plate 32 and the lower cover plate 31 are arranged in parallel along the length direction. The partition plate 34 that divides the gap into six independent circulation chambers 33, and the inner chamber connected to the distribution pipe 6 is provided with six along the axial direction to divide the inner chamber into six independent fan-shaped distribution areas 621 ~626 inner ribs 63, one end of the distribution pipe 6 is sealed by the distribution pipe end cover plate 64, and the pipe wall is provided with six fan-shaped distribution areas 621~626 and six independent cylindrical flow chambers 33- One correspondingly connected flow hole set 61, the flow hole set 61 includes six sub flow hole sets 611~616, each sub flow hole set 611~616 includes six equidistant small holes arranged in a line, each sub flow hole set 611~616 present an angle of 30 degrees to each other along the axial direction. In this embodiment, each flow chamber 33 corresponds to 5~20 microchannel flat tubes 5, and each flow chamber corresponds to only one distribution hole set 61, such as fan-shaped distribution The area 621 communicates with the sub-distribution hole set 611 , the fan-shaped distribution area 622 communicates with the sub-distribution hole set 612 . . . and so on.

As shown in Figures 5-10, as a modification, the cross section of the distribution pipe 6 can be divided into oval, semicircle, square, rectangle, rhombus and triangle in addition to the circle in this embodiment. The shape of the structure, the cross-sectional shape of the inner rib plate 63 is cross-shaped, fork-shaped, Y-shaped or fan-shaped, etc.

In this embodiment, the distribution pipe 6 is placed in the lower header 3. In actual implementation, the distribution pipe 6 can be placed in the upper header 2, left and right headers, or double or multiple rows of headers. In this embodiment, the microchannel flat tubes 5 are placed vertically, and the discharge of condensed water on the fins is used to improve its drainage and anti-frost performance. It is preferably used as a single cooling system evaporator. When the gas-liquid two-phase flow enters the distribution pipe 6, it is divided into 6 streams by each fan-shaped distribution area, and sprayed into the flow chambers 33 of the lower header through the distribution holes at different angles. Then it is redistributed into the microchannel flat tubes 4 corresponding to each flow chamber for evaporation and heat exchange, and finally the gaseous refrigerant is gathered through the upper header 2 and flows out from the outlet header 1 . In addition, this embodiment can also be used in a heat pump system. When the system is heating, the gaseous refrigerant enters through a header. Since the distribution of the gaseous refrigerant is very good, it is quickly and evenly distributed into each flat tube, and in each flat tube Condensate into a liquid state, and finally flow out in the distribution pipe 6.

In the technical solution of the utility model, by setting the distribution pipe 6 with an equal structure, the refrigerant is divided into 6 equal parts at the inlet of the refrigerant, and then flows into each independent circulation cavity through the corresponding distribution holes. First, the refrigerant is evenly distributed into each flow chamber, and second, the pressure of the refrigerant entering the distribution pipe sector rises, and it is sprayed into the flow chamber through each distribution hole set, and the kinetic energy increases, making the gas-liquid two-phase refrigerant mix It is more evenly distributed into each microchannel flat tube. At the same time, the number of refrigerant distribution flat tubes corresponding to a single flow chamber is reduced, which is very suitable for micro-channel heat exchangers with a large length, a large aspect ratio, and a large number of inserted flat tubes. In addition, the vertical placement of the microchannel heat exchanger is also conducive to the drainage of the windowed fins.

When this embodiment is used for cooling in a heat pump system, the gas-liquid two-phase flow enters from the lower header, enters each flow chamber through distribution pipes, and then evaporates into a gaseous state in the microchannel flat tube, then converges on the upper header and flows out. . When used for heating in heat pump systems, the microchannel heat exchanger is used as a condenser, and the gaseous refrigerant flows in from the upper header. Since the gaseous refrigerant has a good distribution, it is evenly distributed to each flat tube and condensed into Liquid refrigerant converges and flows out from the lower header.

The above-mentioned embodiments of the present utility model are only examples for clearly illustrating the present utility model, and are not intended to limit the implementation of the present utility model. For those of ordinary skill in the art, other changes or changes in different forms can be made on the basis of the above description. It is not necessary and impossible to exhaustively list all the implementation manners here. All modifications, equivalent replacements and improvements made within the spirit and principles of the utility model shall be included in the protection scope of the claims of the utility model.

Claims (4)

1. the micro-channel heat exchanger with liquid separation structure, comprises header and lower header, connection and is arranged at micro-channel flat between header and lower header, it is characterized in that:

Described lower header or upper header fasten primarily of upper cover plate and lower cover clamping distributing pipe and form, upper cover plate is provided with along its length the flat tube slot of some connection micro-channel flat, described upper cover plate, gap is left between lower cover and distributing pipe, described upper cover plate be arranged with some demarcation strips described separated being become at least two independent flowing lumens inside lower cover along its length in parallel, be provided with in the axial direction in the inner chamber of described distributing pipe and some described inner chamber be divided into the inner rib plate that at least two are independently distributed district, the sealing of described distributing pipe one end, its tube wall is provided with the some groups of tap hole collection that distribution district is communicated with flowing lumen one_to_one corresponding, described flowing lumen, the quantity of distributing district and tap hole collection is consistent.

2. a kind of micro-channel heat exchanger with liquid separation structure according to claim 1, is characterized in that: the cross section of described distributing pipe is circle, ellipse, semicircle, rectangle, rhombus, triangle.

3. a kind of micro-channel heat exchanger with liquid separation structure according to claim 1, is characterized in that: every component discharge orifice collection comprises the equidistant aperture of 4-8 word order.

4. a kind of micro-channel heat exchanger with liquid separation structure according to claim 1, is characterized in that: be provided with louvered fin between adjacent described micro-channel flat.