CN201811640U - Distributing device of dry evaporator - Google Patents
Distributing device of dry evaporator Download PDFInfo
- Publication number
- CN201811640U CN201811640U CN2010202795937U CN201020279593U CN201811640U CN 201811640 U CN201811640 U CN 201811640U CN 2010202795937 U CN2010202795937 U CN 2010202795937U CN 201020279593 U CN201020279593 U CN 201020279593U CN 201811640 U CN201811640 U CN 201811640U
- Authority
- CN
- China
- Prior art keywords
- swirling flow
- pipe
- distributing pipe
- curved surface
- distributing
- 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.)
- Expired - Fee Related
Links
- 239000007788 liquid Substances 0.000 claims abstract description 22
- 230000007246 mechanism Effects 0.000 claims abstract description 4
- 230000008676 import Effects 0.000 claims description 12
- 244000309464 bull Species 0.000 claims description 3
- 238000009826 distribution Methods 0.000 abstract description 5
- 238000009828 non-uniform distribution Methods 0.000 abstract 1
- 239000003507 refrigerant Substances 0.000 description 10
- 230000000694 effects Effects 0.000 description 5
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 5
- 238000004378 air conditioning Methods 0.000 description 4
- 238000000926 separation method Methods 0.000 description 4
- 239000012530 fluid Substances 0.000 description 3
- 230000009471 action Effects 0.000 description 2
- 239000012141 concentrate Substances 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 230000008569 process Effects 0.000 description 2
- 238000009827 uniform distribution Methods 0.000 description 2
- 230000008901 benefit Effects 0.000 description 1
- 230000005540 biological transmission Effects 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
Images
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- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
Abstract
The utility model discloses a distributing device of a dry evaporator, which mainly comprises a swirling flow distributing pipe, a pipe box and a curved liquid distributing plate, wherein the inner side of the swirling flow distributing pipe has a multi-head elliptical spiral structure, the inlet of the swirling flow distributing pipe is connected with the outlet of a throttling mechanism, the outlet of the swirling flow distributing pipe is connected with the inlet of the pipe box, the curved liquid distributing plate has a three-dimensional curved surface to meet the requirement for the distribution of the pipe box and a heat-exchange pipe, the curved surface is a part of a parabolic surface fitting well with the shape of the pipe box, the focus of the parabolic surface is positioned on the extended line of the axis of the swirling flow distributing pipe, a certain number of distributing holes are formed in the curved surface as required, and the curved liquid distributing plate is arranged on the pipe box. The distributing device solves the problem of the dry evaporator in the prior art that the cold energy is reduced due to non-uniform distribution of the feed liquid, resulting in low energy efficiency.
Description
Technical field
The utility model relates to a kind of central air-conditioning heat transfer technology, relates in particular to the liquid distributing device of a kind of central air-conditioning cold water (heat pump) unit with dry evaporator.
Background technology
Central air-conditioning cold water source pump is as the central air conditioner system nucleus equipment, and its efficiency has directly determined the efficiency of central air conditioner system.Improve central air-conditioning cold water (heat pump) unit efficiency, reduce building energy consumption, be the importance of energy-saving and emission-reduction always.Dry evaporator is as one of core part of cold water (heat pump) unit, and the efficiency and the refrigerating capacity of unit had conclusive effect, also is simultaneously cold water source pump the most frequently used heat transmission equipment at present.
Because the special construction of dry evaporator, and the refrigerant fluid under the duty is the gas-liquid two-phase attitude, thus in the quality of dry evaporator import department along the import distribution of radially outward successively decreasing, promptly the cold-producing medium flow velocity of import center is greater than the flow velocity of inlet ambient.And the heat exchanger tube distribution cross section of heat exchanger is greater than inlet-duct area.Therefore be far longer than heat exchange tube inner refrigerant mass flow in heat exchange tube inner refrigerant mass flow away from import over against import, and therefore cause the state of heat exchanger tube inner refrigerant to differ, finally cause the exchange capability of heat of heat exchanger to descend, the evaporating temperature of unit descends, the unit cold descends, and efficiency reduces.
Present dry evaporator import is adopted simple porous plate separatory usually or is not adopted any liquid distributing device.Such way has directly influenced the uniformity coefficient of separatory, makes the exchange capability of heat of evaporimeter descend.
The utility model content
The purpose of this utility model is to provide a kind of dry evaporator distributor, solves prior art dry evaporator feed liquor and distributes the uneven cold that causes to descend the problem that efficiency reduces.
In order to achieve the above object, the utility model adopts following technical scheme: described dry evaporator distributor is mainly by the swirling flow distributing pipe, bobbin carriage and curved surface liquid separatnig plate constitute, the ellipse spiral curve of bull is processed in swirling flow distributing pipe inboard, the import of swirling flow distributing pipe links to each other with the outlet of throttle mechanism, the outlet of swirling flow distributing pipe links to each other with the import of bobbin carriage, distribution according to bobbin carriage and heat exchanger tube, the curved surface liquid separatnig plate is made into three-dimension curved surface, curved surface is the paraboloidal part according to the shape intercepting of bobbin carriage, paraboloidal focus is positioned on the axis extended line of swirling flow distributing pipe, and make the dispensing orifice of some as required, be installed on the bobbin carriage.
Compare with prior art, the utlity model has following advantage:
When cold-producing medium enters the swirling flow distributing pipe because the characteristic of fluid, refrigerant air-liquid can carry out primary separation, because centrifugal action, the liquid that density is big can separate to the tube wall direction, the gas that density is little then concentrates on the middle part of distributing pipe, the refrigerant mixture of process primary separation leaves distributing pipe and enters bobbin carriage, and it is axial and radially two components synthetic that the refrigerant velocities of this moment can be regarded as.Because the effect of curved surface liquid separatnig plate, the axial velocity component of cold-producing medium further reduces, and under the acting in conjunction that the guiding of curved surface convection cell and the perforate on the liquid separatnig plate distribute, it is enough makes cold-producing medium reach the position of bobbin carriage away from the distributing pipe axle center for the radial velocity component of cold-producing medium, its axial component is at each position basically identical along the bobbin carriage cross section, and therefore one's duty is equipped with the effect of having played uniform distribution of putting.
Through software simulation and test, this device has improved the heat exchange property of evaporimeter.
Description of drawings
Figure 1 shows that structural representation of the present utility model.
Among the figure
1 swirling flow distributing pipe, 2 bobbin carriages, 3 curved surface liquid separatnig plates
The specific embodiment
Below in conjunction with accompanying drawing, specify the utility model.
The dry evaporator distributor that the utility model relates to is mainly by swirling flow distributing pipe 1, bobbin carriage 2 and curved surface liquid separatnig plate 3 constitute, the ellipse spiral curve of bull is processed in swirling flow distributing pipe 1 inboard, the import of swirling flow distributing pipe 1 links to each other with the outlet of throttle mechanism, the outlet of swirling flow distributing pipe 1 links to each other with the import of bobbin carriage 2, distribution according to bobbin carriage 2 and heat exchanger tube, curved surface liquid separatnig plate 3 is made into three-dimension curved surface, curved surface is the paraboloidal part according to the shape intercepting of bobbin carriage 2, paraboloidal focus is positioned on the axis extended line of swirling flow distributing pipe 1, and make the dispensing orifice of some as required, be installed on the bobbin carriage 2.
When cold-producing medium enters swirling flow distributing pipe 1 because the characteristic of fluid, refrigerant air-liquid can carry out primary separation, because centrifugal action, the liquid that density is big can separate to the tube wall direction, the gas that density is little then concentrates on the middle part of swirling flow distributing pipe 1, the refrigerant mixture of process primary separation leaves distributing pipe and enters bobbin carriage, and it is axial and radially two components synthetic that the refrigerant velocities of this moment can be regarded as.Because the effect of curved surface liquid separatnig plate 3, the axial velocity component of cold-producing medium further reduces, and under the acting in conjunction that the guiding of curved surface convection cell and the perforate on the liquid separatnig plate distribute, it is enough makes cold-producing medium reach the position of bobbin carriage away from the distributing pipe axle center for the radial velocity component of cold-producing medium, its axial component is at each position basically identical along the bobbin carriage cross section, and therefore one's duty is equipped with the effect of having played uniform distribution of putting.
More than disclosed be the specific embodiment of this patent only, but this patent is not limited thereto, any those skilled in the art can think variation, all should drop in the protection domain of this patent.
Claims (2)
1. dry evaporator distributor, it is characterized in that: mainly constitute by swirling flow distributing pipe (1), bobbin carriage (2) and curved surface liquid separatnig plate (3), the import of swirling flow distributing pipe (1) links to each other with the outlet of throttle mechanism, and the outlet of swirling flow distributing pipe (1) links to each other with the import of bobbin carriage (2).
2. dry evaporator distributor as claimed in claim 1, it is characterized in that: the ellipse spiral curve of bull is processed in described swirling flow distributing pipe (1) inboard, curved surface liquid separatnig plate (3) is made into three-dimension curved surface, curved surface is that paraboloidal focus is positioned on the axis extended line of swirling flow distributing pipe (1) according to the paraboloidal part of the shape intercepting of bobbin carriage (2).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010202795937U CN201811640U (en) | 2010-08-03 | 2010-08-03 | Distributing device of dry evaporator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010202795937U CN201811640U (en) | 2010-08-03 | 2010-08-03 | Distributing device of dry evaporator |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201811640U true CN201811640U (en) | 2011-04-27 |
Family
ID=43894579
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2010202795937U Expired - Fee Related CN201811640U (en) | 2010-08-03 | 2010-08-03 | Distributing device of dry evaporator |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201811640U (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102865696A (en) * | 2012-07-13 | 2013-01-09 | 江门市东联热工设备有限公司 | Refrigeration and evaporation distributor |
| WO2014094304A1 (en) * | 2012-12-21 | 2014-06-26 | Trane International Inc. | Shell and tube evaporator |
| CN106940102A (en) * | 2016-01-04 | 2017-07-11 | 珠海格力电器股份有限公司 | Shell and tube heat exchanger and air conditioning equipment with same |
| CN107328294A (en) * | 2017-07-18 | 2017-11-07 | 甘肃蓝科石化高新装备股份有限公司 | Shell-and-plate heat exchanger liquid distribution mixing arrangement |
-
2010
- 2010-08-03 CN CN2010202795937U patent/CN201811640U/en not_active Expired - Fee Related
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102865696A (en) * | 2012-07-13 | 2013-01-09 | 江门市东联热工设备有限公司 | Refrigeration and evaporation distributor |
| WO2014094304A1 (en) * | 2012-12-21 | 2014-06-26 | Trane International Inc. | Shell and tube evaporator |
| CN104956162B (en) * | 2012-12-21 | 2017-11-21 | 特灵国际有限公司 | Shell-and-tube evaporator |
| CN106940102A (en) * | 2016-01-04 | 2017-07-11 | 珠海格力电器股份有限公司 | Shell and tube heat exchanger and air conditioning equipment with same |
| CN107328294A (en) * | 2017-07-18 | 2017-11-07 | 甘肃蓝科石化高新装备股份有限公司 | Shell-and-plate heat exchanger liquid distribution mixing arrangement |
| CN107328294B (en) * | 2017-07-18 | 2023-09-08 | 甘肃蓝科石化高新装备股份有限公司 | Liquid distribution mixing device for plate-shell heat exchanger |
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Legal Events
| 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: 20110427 Termination date: 20150803 |
|
| EXPY | Termination of patent right or utility model |