CN2623313Y - A dry-type evaporator intermediate - Google Patents
A dry-type evaporator intermediate Download PDFInfo
- Publication number
- CN2623313Y CN2623313Y CN 03216926 CN03216926U CN2623313Y CN 2623313 Y CN2623313 Y CN 2623313Y CN 03216926 CN03216926 CN 03216926 CN 03216926 U CN03216926 U CN 03216926U CN 2623313 Y CN2623313 Y CN 2623313Y
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- CN
- China
- Prior art keywords
- plate
- dry evaporator
- liquid separatnig
- utility
- model
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- 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.)
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- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
The utility model discloses a dry-type evaporator intermediate, comprising an intermediate board (1) which is provided inside with a liquid feeding cavity (2) and an air return cavity (3). The utility model is characterized in that the feeding cavity (2) is provided inside with a liquid separating board (4) which is connected with the wall of the liquid feeding cavity, the liquid separating board (4) is provided with a liquid separating hole (5). The utility model has a simple structure, makes the dry-type evaporator supply liquid evenly and improves the efficiency of heat change.
Description
(1) technical field: the utility model relates to a kind of intermediate, relates in particular to a kind of dry evaporator intermediate.
(2) background technology: present existing dry evaporator, liquid directly enters admission chamber, and it is inhomogeneous that feed flow advances the liquid of each evaporation tube like this, makes the feed flow of dry evaporator inhomogeneous, reduces the heat exchange efficiency of evaporimeter so greatly.
(3) summary of the invention: the purpose of this utility model is to overcome the deficiency of above-mentioned prior art and provides a kind of simple in structure, can make the dry evaporator feed flow even, the dry evaporator intermediate that heat exchange efficiency improves.
The purpose of this utility model can reach by following measure: a kind of dry evaporator intermediate, it comprises intermediate plate 1, be provided with admission chamber 2, return-air chamber 3 in the intermediate plate 1, it is characterized in that being provided with in the admission chamber 2 liquid separatnig plate 4, liquid separatnig plate 4 joins with the admission chamber wall, and liquid separatnig plate 4 is provided with separatory hole 5.
In order to further specify the purpose of this utility model, the 5 regular arrangements of described separatory hole, the type of array in every adjacent three separatory holes 5 is an equilateral triangle.
In order to further specify the purpose of this utility model, the diameter in described separatory hole 5 is 2-6mm, and pitch of holes is 16mm-21mm.
In order to further specify the purpose of this utility model, the diameter in described separatory hole 5 is 5mm, and pitch of holes is 20mm.
In order to further specify the purpose of this utility model, the thickness of described liquid separatnig plate 4 is 2mm-4mm.
In order to further specify the purpose of this utility model, described liquid separatnig plate 4 thickness are 2mm.
In order to further specify the purpose of this utility model, the thickness of described intermediate plate 1 is 18mm-22mm.
In order to further specify the purpose of this utility model, the distance L that the fluid of described liquid separatnig plate 4 and intermediate plate 1 goes out end is 2mm-3mm.
The utility model can produce following good effect compared with the prior art: the utility model is provided with liquid separatnig plate in admission chamber, utilize the separatory hole on the liquid separatnig plate to carry out second diffluence, reach the purpose that even feed flow advances each evaporation tube, can make the dry evaporator feed flow even like this, heat exchange efficiency improves.
(4) description of drawings:
Fig. 1 is a structural representation of the present utility model;
Fig. 2 is the side view of Fig. 1.
(5) specific embodiment: preferred forms of the present utility model is elaborated below in conjunction with accompanying drawing:
Embodiment: a kind of dry evaporator intermediate (referring to Fig. 1, Fig. 2), it comprises intermediate plate 1, be provided with admission chamber 2, return-air chamber 3 in the intermediate plate 1, be provided with liquid separatnig plate 4 in the admission chamber 2, liquid separatnig plate 4 and admission chamber wall close proximity, liquid separatnig plate 4 is provided with separatory hole 5, the 5 regular arrangements of separatory hole, the type of array in three whenever adjacent separatory holes 5 is an equilateral triangle, the diameter in separatory hole 5 is 4mm, and pitch of holes is 20mm, and the thickness of liquid separatnig plate 4 is 2mm, the thickness of intermediate plate 1 is 20mm, and the distance L that the fluid of liquid separatnig plate 4 and intermediate plate 1 goes out end is 2mm.
Claims (8)
1, a kind of dry evaporator intermediate, it comprises intermediate plate (1), is provided with admission chamber (2), return-air chamber (3) in the intermediate plate (1), it is characterized in that being provided with in the admission chamber (2) liquid separatnig plate (4), liquid separatnig plate (4) joins with the admission chamber wall, and liquid separatnig plate (4) is provided with separatory hole (5).
2, a kind of dry evaporator intermediate according to claim 1 is characterized in that the regular arrangement in described separatory hole (5). the type of array in whenever adjacent three separatory holes (5) is an equilateral triangle.
3, a kind of dry evaporator intermediate according to claim 1 and 2, the diameter that it is characterized in that described separatory hole (5) is 2-6mm, pitch of holes is 16mm-21mm.
4, a kind of dry evaporator intermediate according to claim 3, the diameter that it is characterized in that described separatory hole (5) is 5mm, pitch of holes is 20mm.
5, a kind of dry evaporator intermediate according to claim 1, the thickness that it is characterized in that described liquid separatnig plate (4) is 2mm-4mm.
6, a kind of dry evaporator intermediate according to claim 5 is characterized in that described liquid separatnig plate (4) thickness is 2mm.
7, a kind of dry evaporator intermediate according to claim 1, the thickness that it is characterized in that described intermediate plate (1) is 18mm-22mm.
8, according to claim 1 or 5 or 6 or 7 described a kind of dry evaporator intermediates, the distance L that the fluid that it is characterized in that described liquid separatnig plate (4) and intermediate plate (1) goes out end is 2mm-3mm.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN 03216926 CN2623313Y (en) | 2003-04-30 | 2003-04-30 | A dry-type evaporator intermediate |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN 03216926 CN2623313Y (en) | 2003-04-30 | 2003-04-30 | A dry-type evaporator intermediate |
Publications (1)
Publication Number | Publication Date |
---|---|
CN2623313Y true CN2623313Y (en) | 2004-07-07 |
Family
ID=34243220
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN 03216926 Expired - Fee Related CN2623313Y (en) | 2003-04-30 | 2003-04-30 | A dry-type evaporator intermediate |
Country Status (1)
Country | Link |
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CN (1) | CN2623313Y (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102563978A (en) * | 2011-01-04 | 2012-07-11 | 珠海格力电器股份有限公司 | Shell-tube heat exchanger |
CN103277944A (en) * | 2013-05-08 | 2013-09-04 | 杭州赛富特设备有限公司 | Dry-type evaporator |
-
2003
- 2003-04-30 CN CN 03216926 patent/CN2623313Y/en not_active Expired - Fee Related
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102563978A (en) * | 2011-01-04 | 2012-07-11 | 珠海格力电器股份有限公司 | Shell-tube heat exchanger |
CN103277944A (en) * | 2013-05-08 | 2013-09-04 | 杭州赛富特设备有限公司 | Dry-type evaporator |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
C17 | Cessation of patent right | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20040707 |