CN203629390U - Separating type heat pipe and heat exchanging device using same - Google Patents
Separating type heat pipe and heat exchanging device using same Download PDFInfo
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- CN203629390U CN203629390U CN201320799549.2U CN201320799549U CN203629390U CN 203629390 U CN203629390 U CN 203629390U CN 201320799549 U CN201320799549 U CN 201320799549U CN 203629390 U CN203629390 U CN 203629390U
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- heat
- pipe
- hot fluid
- outlet
- cold fluid
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- 239000012530 fluid Substances 0.000 claims abstract description 75
- 238000010438 heat treatment Methods 0.000 claims abstract description 40
- 230000000694 effects Effects 0.000 claims abstract description 4
- 230000005494 condensation Effects 0.000 claims description 23
- 238000009833 condensation Methods 0.000 claims description 23
- 238000001816 cooling Methods 0.000 claims description 14
- 230000008676 import Effects 0.000 claims description 9
- 238000001704 evaporation Methods 0.000 abstract description 5
- 239000007788 liquid Substances 0.000 abstract 2
- 230000000630 rising effect Effects 0.000 abstract 2
- 230000008901 benefit Effects 0.000 description 3
- 238000009434 installation Methods 0.000 description 3
- 238000000034 method Methods 0.000 description 3
- 230000004048 modification Effects 0.000 description 3
- 238000012986 modification Methods 0.000 description 3
- 239000008280 blood Substances 0.000 description 2
- 210000004369 blood Anatomy 0.000 description 2
- 230000008859 change Effects 0.000 description 2
- 230000006378 damage Effects 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000005540 biological transmission Effects 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 239000002360 explosive Substances 0.000 description 1
- 238000007689 inspection Methods 0.000 description 1
- 230000008569 process Effects 0.000 description 1
- 230000002441 reversible effect Effects 0.000 description 1
- 238000005096 rolling process Methods 0.000 description 1
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Abstract
The utility model discloses a separating type heat pipe including an evaporating section and a condensing section, and further including a pipe plate, the pipe plate is hollow and rectangular in shape, the evaporating section includes a plurality of heating pipes, the plurality of heating pipes are connected with the two ends inside the lower part of the pipe plate, the condensing section includes a plurality of condensing pipes, the plurality of condensing pipes are connected with the two ends inside the upper part of the pipe plate, the condensing section is further provided with a cold source inlet and a cold source outlet, the evaporating section is further provided with a hot source inlet and a hot source outlet, and the separating type heat pipe further includes a condensing liquid falling pipe and a steam rising pipe, the condensing liquid falling pipe and the steam rising pipe are respectively arranged at the left section and the right section of the pipe plate, thereby taking the effects that the heating pipes are immersed in a heat pipe medium, hot fluid flows through the heating pipes to heat the heat pipe medium to generate steam, and meanwhile, the hot fluid cools down, cold fluid flows through the condensing pipes to condense the steam of the heat pipe medium generated from the evaporating section, and meanwhile, the cold fluid heats up.
Description
Technical field
The utility model relates to a kind of heat transmission equipment in thermal energy exchange field, relates in particular to a kind of separate heat pipe and applies the heat-exchanger rig of this separate heat pipe.
Background technology
Heat pipe, as a kind of heat transfer element with high heat conductivility, plays an important role in the various fields of fluid heat transferring.As compared with the various heat-pipe heat exchangers of heat transfer element and the heat exchanger of general conventional version, have that heat transfer efficiency is high, fluid flow resistance is little, movement-less part, thermostatic characteristics are good, dismounting and change and the advantage such as rolling inspection is convenient by heat pipe.The separate type heat pipe exchanger of commercial Application is except having the superiority of integral heat-tube heat exchanger, also have that cold and hot fluid is separated completely, site layout project flexibly, be easy to carry out heat exchange to thering is the fluid that inflammable and explosive abrasiveness is large, do not have the advantage such as constraint of carrying heat transport limitation, be subject to people's attention gradually.
Conventional heat pipe, hot fluid and cold fluid flow through respectively evaporator section and condensation segment, respectively by heating and cooling outside wall surface, thereby distinguish the working media of heating evaporation section and cooling condensation intersegmental part.Such version, tends to increase the flow resistance of hot fluid and cold fluid, is unfavorable for increasing heat exchange area, and poor in the applications effect of some special fluids.
Summary of the invention
The defect existing for technique scheme, in order to solve the problem of above existence, has designed a kind of separate heat pipe, and the heating tube of this heat pipe is placed in evaporator section inside, and is immersed in heat-pipe working medium; Condenser pipe is also as for condensation segment inside.Heating tube or condenser pipe are all connected with the tube sheet at two ends, can make fluid when by tube sheet, produce flow-disturbing phenomenon, and breakable layer laminar sublayer impels the even of fluid temperature (F.T.), can reduce flow resistance simultaneously, makes heat transfer process more smooth and easy, and significantly improves heat exchange efficiency; Can change as required caliber and the quantity of heating tube (cooling tube), thereby adjust the heat exchange area of heating tube (cooling tube), can realize in the situation that increasing more heat exchange area, but keep the constant of evaporator section appearance and size.
The invention provides a kind of separate heat pipe, comprise evaporator section, condensation segment, vapor uptake and condensate descending, wherein, comprising: evaporator section, condensation segment and tube sheet, described tube sheet is middle hollow out rectangle, wherein, described evaporator section comprises many heating tubes, and described many heating tubes are connected with the two ends in described tube sheet bottom, condensation segment comprises many condenser pipes, and described many condenser pipes are connected with the two ends in described tube sheet top; Described condensation segment is also provided with low-temperature receiver import and low-temperature receiver outlet, and described evaporator section is also provided with thermal source import and thermal source outlet; And, also comprise condensate descending and vapor uptake, in the left and right of described tube sheet two sections respectively of described condensate descending and vapor uptakes, be immersed in heat-pipe medium thereby play heating tube, hot fluid flows through from heating tube, and heating heat-pipe medium produces steam, hot fluid cooling simultaneously, cold fluid flows through from condenser pipe, the heat-pipe medium steam that condensation produces from evaporator section, the effect that cold fluid heats up simultaneously.
Above-mentioned separate heat pipe, wherein: described heating tube and condenser pipe can be one or more the combination in light pipe, gilled tube or other shape tubes.
Above-mentioned separate heat pipe, wherein: the cross section of described evaporator section and condensation segment is the one in square, rectangle, triangle, trapezoidal, circular, ellipse or regular polygon.
The heat-exchanger rig of above-mentioned separate heat pipe, wherein, comprising: multiple series-parallel separate heat pipes, hot fluid entrance, hot fluid outlet, cold fluid entrance and cold fluid outlet; The hot fluid entrance of described heat-exchanger rig is connected with heat source side, after heating tube, is flowed out by the outlet of heat-exchanger rig hot fluid; The cold fluid entrance of described heat-exchanger rig is connected with low-temperature receiver end, after condenser pipe, is flowed out by the outlet of heat-exchanger rig cold fluid.
Above-mentioned separate heat pipe, wherein, described hot fluid and cold fluid counter-flow arrangement or following current are arranged.
Compared with prior art, the invention has following significant beneficial effect: 1, tube sheet can strengthen the disturbance of the hot fluid (cold fluid) passing through effectively,, thus the laminar sublayer of destruction fluid impels the even of fluid temperature (F.T.), has improved heat exchange efficiency; 2, heating tube (cooling tube) adopts straight tube design, can effectively reduce the flow resistance of fluid; 3, can, by adjusting caliber and the quantity of heating tube (cooling tube), in the situation that evaporator section (condensation segment) appearance and size is constant, adjust heating (cooling) area.There is requirement for appearance and size, but the larger occasion of required heat-transfer surface; The occasion of 4, carrying out heat exchange for some special fluid, the present invention also can normally use; 5, modular structure design, serial or parallel connection use flexibly according to actual needs, is convenient to installation and transportation.
Accompanying drawing explanation
Fig. 1 is the separate heat pipe structural representation that the utility model provides.
Fig. 2 is the heat-exchanger rig scheme of installation of the separate heat pipe described in the application that provides of the utility model.
Description of reference numerals:
1 thermal source import;
2 thermal source outlets;
3 tube sheets;
4 low-temperature receivers enter (going out) mouthful;
5 low-temperature receivers go out (entering) mouthful;
6 condensate descending;
7 vapor uptakes;
8 heating tubes;
9 condenser pipes;
10 evaporator sections;
11 condensation segments;
12 separate heat pipes;
13 hot fluid entrances;
14 hot fluid outlets;
15 cold fluid entrances;
16 cold fluid outlets.
The specific embodiment
Below in conjunction with the drawings and specific embodiments, the invention will be further described, but not as limiting to the invention.Be described further below in conjunction with embodiment and accompanying drawing.
The utility model provides a kind of separate heat pipe, as shown in Figure 1, includes evaporator section 10 and condensation segment 11, and wherein, described evaporator section 10 comprises thermal source import 1, thermal source outlet 2, heating tube 8 and tube sheet 3; Described condensation segment 11 comprises that low-temperature receiver enters (going out) mouth 4, low-temperature receiver goes out (entering) mouth 5, condenser pipe 9 and tube sheet 3; Between evaporator section 10 and condensation segment 11, there are condensate descending 6, vapor uptake 7.Wherein, heating tube 8(condenser pipe 9 on tube sheet) be " mouth " font distribute.This distribution form, can make thermal source (low-temperature receiver) enter heating tube 8(condenser pipe 9 from import) time, produce flow-disturbing phenomenon, thereby destroy the laminar sublayer of fluid, impel the even of fluid temperature (F.T.), improve the coefficient of heat transfer; Simultaneously also can be according to actual conditions, select the form (as one or more the combination in light pipe, gilled tube or other different in nature pipes) of heating tube (condenser pipe), thereby aggravate disturbance and increase heat exchange area.Heating tube 8 is immersed in heat-pipe medium, and hot fluid enters from thermal source import 1, from heating tube, flows through, and flows out from thermal source outlet 2, and heating heat-pipe medium produces steam, hot fluid cooling simultaneously; Cold fluid is from low-temperature receiver import 4(5) enter, from condenser pipe 9, flow through, from low-temperature receiver outlet 5(4) enter, the heat-pipe medium steam that condensation produces from evaporator section, cold fluid heats up simultaneously.Thereby realize the heat exchange between Cooling and Heat Source
The cross section of described evaporator section 10 and condensation segment 11 is the one in square, rectangle, triangle, trapezoidal, circular, ellipse or polygon.
Described heating tube 8 and condenser pipe 9 can be one or more the combinations in light pipe, gilled tube or other different in nature pipes.The present embodiment take circular light pipe as representative for example.
A kind of heat-exchanger rig of applying described separate heat pipe of the present utility model, as shown in Figure 2, comprises multiple series-parallel separate heat pipes 12, hot fluid entrance 13, hot fluid outlet 14, cold fluid entrance 15 and cold fluid outlet 16 etc.The hot fluid entrance 13 of described heat-exchanger rig is connected with heat source side, after heating tube, is flowed out by heat-exchanger rig hot fluid outlet 14; The cold fluid entrance 15 of described heat-exchanger rig is connected with low-temperature receiver end, after condenser pipe, is flowed out by heat-exchanger rig cold fluid outlet 16.Hot fluid and cold fluid reversible flow are arranged, also can following current arrange.
In sum, compared with prior art, the invention has the following advantages: 1, tube sheet can strengthen the disturbance of the hot fluid (cold fluid) passing through effectively,, thus the laminar sublayer of destruction fluid impels the even of fluid temperature (F.T.), has improved heat exchange efficiency; 2, heating tube (cooling tube) adopts straight tube design, can effectively reduce the flow resistance of fluid; 3, can, by adjusting caliber and the quantity of heating tube (cooling tube), in the situation that evaporator section (condensation segment) appearance and size is constant, adjust heating (cooling) area.There is requirement for appearance and size, but the larger occasion of required heat-transfer surface; The occasion of 4, carrying out heat exchange for some special fluid, the present invention also can normally use; 5, modular structure design, serial or parallel connection use flexibly according to actual needs, is convenient to installation and transportation.
It should be appreciated by those skilled in the art that those skilled in the art can realize described variation example in conjunction with prior art and above-described embodiment, do not repeat them here.Such variation example does not affect flesh and blood of the present invention, does not repeat them here.
Above preferred embodiment of the present invention is described.It will be appreciated that, the present invention is not limited to above-mentioned specific implementations, the equipment of wherein not describing in detail to the greatest extent and structure are construed as and give any those of ordinary skill in the art of reality with the common mode in this area, do not departing from technical solution of the present invention scope situation, all can utilize method and the technology contents of above-mentioned announcement to make many possible variations and modification to technical solution of the present invention, or being revised as the equivalent embodiment of equivalent variations, this does not affect flesh and blood of the present invention.Therefore, every content that does not depart from technical solution of the present invention,, all still belongs in the scope of technical solution of the present invention protection any simple modification made for any of the above embodiments, equivalent variations and modification according to technical spirit of the present invention.
Claims (5)
1. a separate heat pipe, comprise evaporator section, condensation segment, it is characterized in that, also comprise: evaporator section, condensation segment and tube sheet, described tube sheet is middle hollow out rectangle, wherein, described evaporator section comprises many heating tubes, and described many heating tubes are connected with the two ends in described tube sheet bottom, condensation segment comprises many condenser pipes, and described many condenser pipes are connected with the two ends in described tube sheet top; Described condensation segment is also provided with low-temperature receiver import and low-temperature receiver outlet, and described evaporator section is also provided with thermal source import and thermal source outlet; And, also comprise condensate descending and vapor uptake, in the left and right of described tube sheet two sections respectively of described condensate descending and vapor uptakes, be immersed in heat-pipe medium thereby play heating tube, hot fluid flows through from heating tube, and heating heat-pipe medium produces steam, hot fluid cooling simultaneously, cold fluid flows through from condenser pipe, the heat-pipe medium steam that condensation produces from evaporator section, the effect that cold fluid heats up simultaneously.
2. separate heat pipe according to claim 1, is characterized in that: described heating tube and condenser pipe can be one or more the combination in light pipe, gilled tube or other shape tubes.
3. separate heat pipe according to claim 1, is characterized in that: the cross section of described evaporator section and condensation segment is the one in square, rectangle, triangle, trapezoidal, circular, ellipse or regular polygon.
4. application rights requires a heat-exchanger rig for the separate heat pipe described in 1 to 3, it is characterized in that, comprising: multiple series-parallel separate heat pipes, hot fluid entrance, hot fluid outlet, cold fluid entrance and cold fluid outlet; The hot fluid entrance of described heat-exchanger rig is connected with heat source side, after heating tube, is flowed out by the outlet of heat-exchanger rig hot fluid; The cold fluid entrance of described heat-exchanger rig is connected with low-temperature receiver end, after condenser pipe, is flowed out by the outlet of heat-exchanger rig cold fluid.
5. separate heat pipe according to claim 4, is characterized in that: described hot fluid and cold fluid counter-flow arrangement or following current are arranged.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320799549.2U CN203629390U (en) | 2013-12-05 | 2013-12-05 | Separating type heat pipe and heat exchanging device using same |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320799549.2U CN203629390U (en) | 2013-12-05 | 2013-12-05 | Separating type heat pipe and heat exchanging device using same |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203629390U true CN203629390U (en) | 2014-06-04 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201320799549.2U Expired - Lifetime CN203629390U (en) | 2013-12-05 | 2013-12-05 | Separating type heat pipe and heat exchanging device using same |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN203629390U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109708187A (en) * | 2018-12-21 | 2019-05-03 | 上海理工大学 | Heating floor is the same as the personalized heating system for drawing hot device and combining |
| CN112673227A (en) * | 2018-07-11 | 2021-04-16 | 梅克斯公司 | Plume suppression using thermosiphon shell and tube heat exchangers |
-
2013
- 2013-12-05 CN CN201320799549.2U patent/CN203629390U/en not_active Expired - Lifetime
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112673227A (en) * | 2018-07-11 | 2021-04-16 | 梅克斯公司 | Plume suppression using thermosiphon shell and tube heat exchangers |
| CN109708187A (en) * | 2018-12-21 | 2019-05-03 | 上海理工大学 | Heating floor is the same as the personalized heating system for drawing hot device and combining |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C56 | Change in the name or address of the patentee |
Owner name: SHANGHAI SHENGYU TECHNICAL CO., LTD. Free format text: FORMER NAME: SHANGHAI CHENGYU SCIENCE AND TRADE CO., LTD. |
|
| CP01 | Change in the name or title of a patent holder |
Address after: 201100 No. 1188 Guanghua Road, Xhenzhuang Industrial Zone, Shanghai, Minhang District Patentee after: Shanghai Shengyu Technology Co., Ltd. Address before: 201100 No. 1188 Guanghua Road, Xhenzhuang Industrial Zone, Shanghai, Minhang District Patentee before: Shanghai Chengyu Science and Trade Co., Ltd. |