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CN106152619A - Rectangle split-flow baffles formula parallel-flow evaporator - Google Patents

Rectangle split-flow baffles formula parallel-flow evaporator Download PDF

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Publication number
CN106152619A
CN106152619A CN201610570482.3A CN201610570482A CN106152619A CN 106152619 A CN106152619 A CN 106152619A CN 201610570482 A CN201610570482 A CN 201610570482A CN 106152619 A CN106152619 A CN 106152619A
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CN
China
Prior art keywords
flow
split
pipe
rectangle
flow baffles
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.)
Pending
Application number
CN201610570482.3A
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Chinese (zh)
Inventor
施骏业
陈江平
俞登佳
吕鸿斌
蔡博伟
柳慈翀
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Shanghai Jiao Tong University
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Shanghai Jiao Tong University
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Filing date
Publication date
Application filed by Shanghai Jiao Tong University filed Critical Shanghai Jiao Tong University
Priority to CN201610570482.3A priority Critical patent/CN106152619A/en
Publication of CN106152619A publication Critical patent/CN106152619A/en
Pending legal-status Critical Current

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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

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  • Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Mechanical Engineering (AREA)
  • Thermal Sciences (AREA)
  • General Engineering & Computer Science (AREA)
  • Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)

Abstract

A kind of rectangle split-flow baffles formula parallel-flow evaporator, including: rectangular split-flow baffles and include influent stream distribution pipe and go out the header of flow point pipe arrangement, wherein: split-flow baffles surface is provided with bar shaped link slot, the two ends of this link slot are distributed to manage and go out flow point pipe arrangement by porous flat pipe and influent stream respectively and are connected, compared with prior art, the present invention achieves the direct transfer from a upper flat tube to next flat tube for the cold-producing medium by rectangle split-flow baffles, avoid cold-producing medium distribution inequality, improve the heat exchange efficiency of evaporimeter.

Description

矩形分流隔板式平行流蒸发器Rectangular divider type parallel flow evaporator

技术领域technical field

本发明涉及的是一种换热器领域的技术,具体是一种矩形分流隔板式平行流蒸发器。The invention relates to a technology in the field of heat exchangers, in particular to a parallel-flow evaporator of rectangular splitter plate type.

背景技术Background technique

微通道矩形分流隔板式平行流蒸发器由扁管、翅片等组成,具有优良的换热性能。但通常的矩形分流隔板式平行流蒸发器内部的制冷剂为两相流,两相流不稳定,容易引起制冷剂的分配不均,导致整个蒸发器的性能下降。The micro-channel rectangular divider baffle type parallel flow evaporator is composed of flat tubes, fins, etc., and has excellent heat transfer performance. However, the refrigerant inside the common rectangular divider baffle type parallel flow evaporator is a two-phase flow, and the two-phase flow is unstable, which easily causes uneven distribution of the refrigerant, resulting in a decrease in the performance of the entire evaporator.

发明内容Contents of the invention

本发明针对现有技术由于集流管结构引发的制冷剂的分配不均,从而导致蒸发器换热性能下降等问题,提出一种矩形分流隔板式平行流蒸发器,通过矩形分流隔板实现了制冷剂从上一扁管到下一扁管的直接转移,避免了制冷剂分配不均,提升了蒸发器的换热效率。The present invention aims at problems such as the uneven distribution of refrigerant caused by the header structure in the prior art, which leads to the decrease of the heat transfer performance of the evaporator, etc., and proposes a parallel flow evaporator with a rectangular splitter plate, which is realized by a rectangular splitter plate. The direct transfer of the refrigerant from the upper flat tube to the next flat tube is avoided, the uneven distribution of the refrigerant is avoided, and the heat exchange efficiency of the evaporator is improved.

本发明是通过以下技术方案实现的:The present invention is achieved through the following technical solutions:

本发明包括:呈矩形的分流隔板以及包括进流分配管和出流分配管的集流管,其中:分流隔板表面设有条形连接槽,该连接槽的两端分别通过多孔扁管与进流分配管和出流分配管相连。The present invention includes: a rectangular splitter and a header including an inlet distribution pipe and an outlet distribution pipe, wherein: the surface of the splitter is provided with a strip-shaped connecting groove, and the two ends of the connecting groove respectively pass through the porous flat tube It is connected with the inlet distribution pipe and the outlet distribution pipe.

所述的连接槽沿分流隔板的长度方向相互平行等间距设置。The connecting grooves are arranged in parallel with each other and at equal intervals along the length direction of the flow divider.

所述的分流隔板的与多孔扁管的相连面连有用于密封连接槽的固定板,多孔扁管穿过固定板与分流隔板相连。A fixed plate for sealing the connection groove is connected to the connecting surface of the splitter partition and the porous flat tube, and the porous flat tube passes through the fixed plate to connect with the splitter partition.

所述的进流分配管的一端和出流分配管的一端分别连有进口管和出口管。One end of the inlet distribution pipe and one end of the outlet distribution pipe are respectively connected with an inlet pipe and an outlet pipe.

所述的多孔扁管之间设有翅片。Fins are arranged between the porous flat tubes.

所述的进流分配管和出流分配管的横截面都为矩形。The cross-sections of the inlet distribution pipe and the outlet distribution pipe are both rectangular.

附图说明Description of drawings

图1为本发明整体结构示意图;Fig. 1 is a schematic diagram of the overall structure of the present invention;

图2为集流管结构示意图;Fig. 2 is a schematic diagram of the structure of the collector;

图3为固定板结构示意图;Fig. 3 is a schematic diagram of the fixed plate structure;

图4为进流分配管结构示意图;Fig. 4 is a schematic diagram of the structure of the inlet distribution pipe;

图5为分流隔板结构示意图;Figure 5 is a schematic diagram of the structure of the splitter;

图6为多孔扁管与分流隔板连接示意图;Figure 6 is a schematic diagram of the connection between the porous flat tube and the splitter;

图7固定板与分流隔板安装结构示意图;Figure 7 is a schematic diagram of the installation structure of the fixed plate and the splitter partition;

图中:1进口管;2出口管;3集流管;4多孔扁管;5分流隔板;6固定板;7翅片;301进流分配管;302出流分配管;501连接槽。In the figure: 1 inlet pipe; 2 outlet pipe; 3 collecting pipe; 4 porous flat pipe;

具体实施方式detailed description

下面对本发明的实施例作详细说明,本实施例在以本发明技术方案为前提下进行实施,给出了详细的实施方式和具体的操作过程,但本发明的保护范围不限于下述的实施例。The embodiments of the present invention are described in detail below. This embodiment is implemented on the premise of the technical solution of the present invention, and detailed implementation methods and specific operating procedures are provided, but the protection scope of the present invention is not limited to the following implementation example.

实施例1Example 1

如图1所示,本实施例包括:呈矩形的分流隔板5和由进流分配管301和出流分配管302组成的集流管3,其中:分流隔板5表面设有条形连接槽501,该连接槽501的两端分别通过多孔扁管4与进流分配管301和出流分配管302相连。As shown in Figure 1, this embodiment includes: a rectangular divider 5 and a header 3 composed of an inlet distribution pipe 301 and an outlet distribution pipe 302, wherein: the surface of the divider 5 is provided with a strip connection Groove 501, the two ends of the connecting groove 501 are respectively connected with the inlet distribution pipe 301 and the outlet distribution pipe 302 through the porous flat pipe 4.

如图2所示,所述的集流管3包括进流分配管301和出流分配管302。进流分配管301和出流分配管302的横截面都为矩形,其上部表面开有多个与多孔扁管4横截面相同的槽孔。进流分配管301和出流分配管302上的槽孔一一对应。As shown in FIG. 2 , the manifold 3 includes an inlet distribution pipe 301 and an outlet distribution pipe 302 . The cross sections of the inlet distribution pipe 301 and the outlet distribution pipe 302 are both rectangular, and a plurality of slots with the same cross section as the porous flat pipe 4 are opened on the upper surface thereof. The slots on the inlet distribution pipe 301 and the outlet distribution pipe 302 correspond one to one.

如图3所示,所述的分流隔板5的与多孔扁管4的相连表面设有用于密封连接槽501的固定板6,多孔扁管4穿过固定板6与分流隔板5相连。固定板6上依次均布设有两排开孔。该开孔形状与多孔扁管4横截面形状相同,套设于多孔扁管4外部。As shown in FIG. 3 , a fixing plate 6 for sealing the connecting groove 501 is provided on the connecting surface of the splitter baffle 5 and the porous flat tube 4 , and the porous flat tube 4 passes through the fixing plate 6 to connect with the splitter baffle 5 . Two rows of openings are evenly distributed in turn on the fixing plate 6 . The opening shape is the same as the cross-sectional shape of the porous flat tube 4 , and is sheathed outside the porous flat tube 4 .

如图4所示,所述的进流分配管301上的槽孔依次均匀分布。同样的,出流分配管302上的槽孔也依次均匀分布。所述的进流分配管301的一端和出流分配管302的一端分别连有进口管1和出口管2。As shown in FIG. 4 , the slots on the inflow distribution pipe 301 are evenly distributed sequentially. Similarly, the slots on the outflow distribution pipe 302 are also uniformly distributed sequentially. One end of the inlet distribution pipe 301 and one end of the outlet distribution pipe 302 are respectively connected with an inlet pipe 1 and an outlet pipe 2 .

如图5所示,所述的分流隔板5呈矩形,其下表面均布有条形的连接槽501。连接槽501的两端分别通过多孔扁管4与出流分配管302和进流分配管301上的槽孔相连。As shown in FIG. 5 , the flow divider 5 is rectangular, and strip-shaped connecting grooves 501 are evenly distributed on its lower surface. The two ends of the connection groove 501 are respectively connected with the slots on the outflow distribution pipe 302 and the inflow distribution pipe 301 through the porous flat pipe 4 .

如图6~7所示,所述的分流隔板5下表面与固定板6相贴合,实现对连接槽501的密封。固定板6还能够对多孔扁管4起到固定的作用。所述的多孔扁管4之间设有用于散热的翅片7。制冷剂从进口管1流进进流分配管301,而后经多孔扁管4流向分流隔板5,再通过连接槽501流向另一多孔扁管4,最后流到出流分配管302,完成循环。As shown in FIGS. 6-7 , the lower surface of the splitter partition 5 is attached to the fixing plate 6 to realize the sealing of the connecting groove 501 . The fixing plate 6 can also fix the porous flat tube 4 . Fins 7 for heat dissipation are arranged between the porous flat tubes 4 . The refrigerant flows from the inlet pipe 1 into the inflow distribution pipe 301, then flows through the porous flat pipe 4 to the distribution partition plate 5, then flows through the connecting groove 501 to another porous flat pipe 4, and finally flows into the outflow distribution pipe 302, completing cycle.

与现有技术相比,本发明通过矩形分流隔板实现了制冷剂从上一扁管到下一扁管的直接转移,避免了制冷剂分配不均,提升了蒸发器的换热效率。Compared with the prior art, the present invention realizes the direct transfer of the refrigerant from the upper flat tube to the next flat tube through the rectangular dividing plate, avoids the uneven distribution of the refrigerant, and improves the heat exchange efficiency of the evaporator.

Claims (6)

1. a rectangle split-flow baffles formula parallel-flow evaporator, it is characterised in that include: rectangular split-flow baffles and including Influent stream distribution pipe and the header going out flow point pipe arrangement, wherein: split-flow baffles surface is provided with bar shaped link slot, the two ends of this link slot Distribute to manage and go out flow point pipe arrangement by porous flat pipe and influent stream respectively and be connected.
2. rectangle split-flow baffles formula parallel-flow evaporator according to claim 1, is characterized in that, described link slot edge point The length direction of stream dividing plate is parallel to each other spaced set.
3. rectangle split-flow baffles formula parallel-flow evaporator according to claim 2, is characterized in that, described split-flow baffles Being connected with the fixed plate for being tightly connected groove with the face that is connected of porous flat pipe, porous flat pipe passes through fixed plate and split-flow baffles phase Even.
4. rectangle split-flow baffles formula parallel-flow evaporator according to claim 1, is characterized in that, described influent stream distribution pipe One end and go out one end of flow point pipe arrangement and be connected with inlet tube and outlet respectively.
5. rectangle split-flow baffles formula parallel-flow evaporator according to claim 1, is characterized in that, described porous flat pipe it Between be provided with fin.
6. rectangle split-flow baffles formula parallel-flow evaporator according to claim 1, is characterized in that, described influent stream distribution pipe It is all rectangle with the cross section going out flow point pipe arrangement.
CN201610570482.3A 2016-07-19 2016-07-19 Rectangle split-flow baffles formula parallel-flow evaporator Pending CN106152619A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201610570482.3A CN106152619A (en) 2016-07-19 2016-07-19 Rectangle split-flow baffles formula parallel-flow evaporator

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201610570482.3A CN106152619A (en) 2016-07-19 2016-07-19 Rectangle split-flow baffles formula parallel-flow evaporator

Publications (1)

Publication Number Publication Date
CN106152619A true CN106152619A (en) 2016-11-23

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Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP4055449B2 (en) * 2002-03-27 2008-03-05 三菱電機株式会社 Heat exchanger and air conditioner using the same
EP2175223A1 (en) * 2007-07-27 2010-04-14 Mitsubishi Heavy Industries, Ltd. Refrigerant evaporator
CN101738128A (en) * 2009-12-25 2010-06-16 三花丹佛斯(杭州)微通道换热器有限公司 Header pipe of heat exchanger with plurality of rows of flat pipes and heat exchanger
CN102207347A (en) * 2010-03-31 2011-10-05 摩丁制造公司 Heat exchanger
CN103438750A (en) * 2013-09-17 2013-12-11 杭州三花研究院有限公司 Heat exchanger and collecting pipe assembly thereof
CN104913548A (en) * 2015-06-26 2015-09-16 上海交通大学 Parallel flow heat exchanger of single header pipe
CN105650946A (en) * 2014-11-11 2016-06-08 杭州三花研究院有限公司 Micro-channel heat exchanger

Patent Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP4055449B2 (en) * 2002-03-27 2008-03-05 三菱電機株式会社 Heat exchanger and air conditioner using the same
EP2175223A1 (en) * 2007-07-27 2010-04-14 Mitsubishi Heavy Industries, Ltd. Refrigerant evaporator
CN101738128A (en) * 2009-12-25 2010-06-16 三花丹佛斯(杭州)微通道换热器有限公司 Header pipe of heat exchanger with plurality of rows of flat pipes and heat exchanger
CN102207347A (en) * 2010-03-31 2011-10-05 摩丁制造公司 Heat exchanger
CN103438750A (en) * 2013-09-17 2013-12-11 杭州三花研究院有限公司 Heat exchanger and collecting pipe assembly thereof
CN105650946A (en) * 2014-11-11 2016-06-08 杭州三花研究院有限公司 Micro-channel heat exchanger
CN104913548A (en) * 2015-06-26 2015-09-16 上海交通大学 Parallel flow heat exchanger of single header pipe

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Application publication date: 20161123