CN201926355U - Integral type heat-pipe heat exchanger - Google Patents
Integral type heat-pipe heat exchanger Download PDFInfo
- Publication number
- CN201926355U CN201926355U CN 201120020202 CN201120020202U CN201926355U CN 201926355 U CN201926355 U CN 201926355U CN 201120020202 CN201120020202 CN 201120020202 CN 201120020202 U CN201120020202 U CN 201120020202U CN 201926355 U CN201926355 U CN 201926355U
- Authority
- CN
- China
- Prior art keywords
- heat
- heat exchanger
- integrated thermal
- connecting portion
- mentioned
- 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
- 238000001704 evaporation Methods 0.000 claims abstract description 44
- 238000009833 condensation Methods 0.000 claims description 41
- 230000005494 condensation Effects 0.000 claims description 41
- 230000008020 evaporation Effects 0.000 claims description 41
- 125000006850 spacer group Chemical group 0.000 claims description 35
- 238000009434 installation Methods 0.000 claims description 27
- 239000012530 fluid Substances 0.000 claims description 14
- 230000006872 improvement Effects 0.000 description 9
- 230000000694 effects Effects 0.000 description 5
- 238000009834 vaporization Methods 0.000 description 5
- 230000008016 vaporization Effects 0.000 description 5
- 230000008901 benefit Effects 0.000 description 4
- 238000004519 manufacturing process Methods 0.000 description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 4
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 3
- 230000003247 decreasing effect Effects 0.000 description 3
- 238000005516 engineering process Methods 0.000 description 3
- 230000005855 radiation Effects 0.000 description 3
- CSCPPACGZOOCGX-UHFFFAOYSA-N Acetone Chemical compound CC(C)=O CSCPPACGZOOCGX-UHFFFAOYSA-N 0.000 description 2
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 2
- 230000008859 change Effects 0.000 description 2
- 238000001816 cooling Methods 0.000 description 2
- 230000005484 gravity Effects 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 1
- BQCADISMDOOEFD-UHFFFAOYSA-N Silver Chemical compound [Ag] BQCADISMDOOEFD-UHFFFAOYSA-N 0.000 description 1
- 239000004411 aluminium Substances 0.000 description 1
- 229910052782 aluminium Inorganic materials 0.000 description 1
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 1
- 229910021529 ammonia Inorganic materials 0.000 description 1
- 230000000712 assembly Effects 0.000 description 1
- 238000000429 assembly Methods 0.000 description 1
- 239000011324 bead Substances 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000004891 communication Methods 0.000 description 1
- 235000019628 coolness Nutrition 0.000 description 1
- 239000010949 copper Substances 0.000 description 1
- 229910052802 copper Inorganic materials 0.000 description 1
- SWXVUIWOUIDPGS-UHFFFAOYSA-N diacetone alcohol Natural products CC(=O)CC(C)(C)O SWXVUIWOUIDPGS-UHFFFAOYSA-N 0.000 description 1
- 239000000428 dust Substances 0.000 description 1
- 238000009413 insulation Methods 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 230000007257 malfunction Effects 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 230000000505 pernicious effect Effects 0.000 description 1
- 230000008569 process Effects 0.000 description 1
- 238000010992 reflux Methods 0.000 description 1
- 238000005057 refrigeration Methods 0.000 description 1
- 239000004332 silver Substances 0.000 description 1
- 229910052709 silver Inorganic materials 0.000 description 1
- 238000005476 soldering Methods 0.000 description 1
- 238000007669 thermal treatment Methods 0.000 description 1
- 230000007704 transition Effects 0.000 description 1
Images
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
- F28D15/00—Heat-exchange apparatus with the intermediate heat-transfer medium in closed tubes passing into or through the conduit walls ; Heat-exchange apparatus employing intermediate heat-transfer medium or bodies
- F28D15/02—Heat-exchange apparatus with the intermediate heat-transfer medium in closed tubes passing into or through the conduit walls ; Heat-exchange apparatus employing intermediate heat-transfer medium or bodies in which the medium condenses and evaporates, e.g. heat pipes
- F28D15/0275—Arrangements for coupling heat-pipes together or with other structures, e.g. with base blocks; Heat pipe cores
Landscapes
- Engineering & Computer Science (AREA)
- Life Sciences & Earth Sciences (AREA)
- Sustainable Development (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
Abstract
The utility model relates to an integral type heat-pipe heat exchanger comprising an outer shell, a heat-pipe heat exchanger device contained in the outer shell, and a clapboard fixedly connected with the outer shell. The heat-pipe heat exchanger device comprises an evaporating end and a condensing end. The clapboard and the outer shell jointly divide the integral type heat-pipe heat exchanger into an inner circulation heat exchange systerm and an outer circulation heat exchange systerm. The heat-pipe heat exchanger device is provided with a connecting part which is formed by extending along a certain angle inclined from the horizontal direction. The connecting part connects the condensing end and the evaporating end and is penetrated through by the clapboard so as to be divided into a first connecting part and a second connecting part. The first connecting part and the evaporating end are jointly positioned in the inner circulation heat exchange system; and the second connecting part and the condensing end are jointly positioned in the outer circulation heat exchange system. The integral type heat-pipe heat exchanger has a simple structure, high heat transfer efficiency, less flow resistance loss and large power-heat rate.
Description
Technical field
The utility model relates to a kind of heat exchanger, relates in particular to a kind of heat pipe exchanger, belongs to technical field of refrigeration equipment.
Background technology
In electric power, communication or industry such as electric, be extensive use of the control rack.In order to prevent that moisture, dust or pernicious gas from entering rack, rack is usually to outer closure.Be in operation, because of device in the rack self evolution of heat or outdoor solar radiation, temperature can constantly raise in the rack, will certainly influence the normal operation of device in the rack as untimely heat radiation.Therefore, need in the control rack of in these industries, using the special heat exchanger of configuration to rack in the air heat radiation.
In present heat exchanger, the product that can satisfy above use occasion requirement on the performance has plate-fin heat exchanger, cross-flow plate type heat exchanger and heat exchange of heat pipe.The plate-fin heat exchanger complex manufacturing technology, consumptive material is many, and weight is heavy again, and the cost of manufacture height causes the price height.And the cross-flow plate type heat exchanger has light weight, volume is little, production technology is simple, cost of manufacture is low advantage, but it has the loss of thermograde, its heat exchange efficiency is still limited, and it need have the heat exchange both sides could operate as normal under the condition of a fixed difference difference.If summer, outdoor temperature was up to 45 degrees centigrade, and temperature is at 50 degrees centigrade in the control rack, and then the cross-flow plate type heat exchanger is with regard to cisco unity malfunction.
Heat pipe is a kind of heat transfer element with high thermal conductivity, and its equivalent heat output is the best metal hundred times as silver, copper, aluminium etc., even thousands of times, and the title of " near superconduction hot body " is therefore arranged.Its evaporation by working medium in the Totally enclosed vacuum shell is transmitted heat with condensing, but the heat transfer area with high thermal conductivity, good isothermal, cold and hot both sides can change series of advantages such as remotely transferring, temperature controllable arbitrarily.Therefore in recent years, heat pipe has all obtained very big application in each field.
Therefore, the utility model provides a kind of heat pipe exchanger of hot pipe technique of using to realize the temperature control to rack.
The utility model content
The purpose of this utility model is to provide a kind of integrated thermal heat exchanger, its heat transfer efficiency height, and fluid thermal resistance is little.
For achieving the above object, the utility model is about a kind of integrated thermal heat exchanger, the dividing plate that it comprises shell body, is contained in the heat pipe heat exchanging apparatus in the shell body and fixedlys connected with shell body at least.The heat pipe heat exchanging apparatus comprises evaporation ends and condensation end.Dividing plate and shell body are separated into the integrated thermal heat exchanger internal circulation heat-exchanging system and outer circulation heat-exchange system jointly.Described heat pipe heat exchanging apparatus has along the connecting portion that extends to form with horizontal direction inclination certain angle.Thereby this connecting portion connects condensation end and evaporation ends and passed by dividing plate and to be separated to form first connecting portion and second connecting portion.Wherein first connecting portion and above-mentioned evaporation ends are positioned at the internal circulation heat-exchanging system jointly, and second connecting portion and above-mentioned condensation end are positioned at the outer circulation heat-exchange system jointly.
As further improvement of the utility model, the angle of inclination of described connecting portion and horizontal direction is between 1 ° to 89 °.
As further improvement of the utility model, the condensation end and the evaporation ends of described heat pipe heat exchanging apparatus are parallel to each other.
As further improvement of the utility model, described connecting portion is formed with some hollow out grooves, and its median septum comprises upper spacer and the lower clapboard that passes the hollow out groove respectively and seal the hollow out groove.
As further improvement of the utility model, described upper spacer lower end and lower clapboard upper end is formed with some dentation shims respectively, and the dentation shim of each upper spacer and the dentation shim of each lower clapboard overlap each other and pass the hollow out groove jointly and seal this hollow out groove.
As further improvement of the utility model, described upper spacer and lower clapboard are stepped, upper spacer have first installation portion parallel with condensation end, with the first installation portion almost parallel and be formed with above-mentioned dentation shim first spacer portion, and tilt to extend and be connected respectively first extension of above-mentioned first installation portion and first spacer portion; Lower clapboard have second installation portion parallel with evaporation ends, with the second installation portion almost parallel and be formed with above-mentioned dentation shim second spacer portion, and tilt to extend and be connected respectively second extension of above-mentioned second installation portion and second spacer portion.
As further improvement of the utility model, also have the evaporation fan that is installed on above-mentioned first installation portion and be installed on the condensation fan of above-mentioned second installation portion, wherein condensation fan and condensation end align and are positioned at the outer circulation heat-exchange system jointly, and evaporation fan and evaporation ends align and be positioned at the internal circulation heat-exchanging system jointly.
As further improvement of the utility model, also have the blower fan fixed head, described evaporation fan and condensation fan are fixed in first, second installation portion after being installed on the blower fan fixed head respectively.
As further improvement of the utility model, described heat pipe heat exchanging apparatus comprises the last header that is positioned at the condensation end top, is positioned at the lower header of evaporation ends bottom, respectively with last header and lower header is communicated with and the flat tube of the negotiable fluid media (medium) in middle part, wherein each flat tube is Z-shaped.
As further improvement of the utility model, described heat pipe heat exchanging apparatus also comprises the radiating fin that is distributed between the adjacent flat tube, and wherein the connecting portion place is not provided with radiating fin, thereby forms above-mentioned hollow out groove.
The beneficial effects of the utility model are: the integrated thermal exchanger arrangement, and the heat transfer efficiency height, the fluid resistance is decreased little, and the merit ratio of specific heat is big.
Description of drawings
Fig. 1 is the assembling schematic perspective view of the utility model integrated thermal heat exchanger.
Fig. 2 is the assembling schematic perspective view of another angle of the utility model integrated thermal heat exchanger.
Fig. 3 is the perspective exploded view of the utility model integrated thermal heat exchanger.
Fig. 4 is the perspective exploded view of another angle of structure shown in Figure 3.
Fig. 5 is the part assembling schematic perspective view of structure shown in Figure 4.
Fig. 6 is the side view of structure shown in Figure 5.
The specific embodiment
The utility model provides a kind of integrated thermal heat exchanger 100 that adopts heat pipe as heat-exchanger rig.Heat pipe is a kind of heat transfer element with high thermal conductivity, its evaporation by working medium in the Totally enclosed vacuum shell is transmitted heat with condensing, but the heat transfer area with high thermal conductivity, good isothermal, cold and hot both sides can change series of advantages such as remotely transferring, temperature controllable arbitrarily.The heat pipe exchanger of being made up of heat pipe has the heat transfer efficiency height, advantages such as little, that the merit ratio of specific heat is big are decreased in the fluid resistance.And heat pipe exchanger does not need compressor, does not need freon working medium, its compact conformation, and quality and profile are less.
The operation principle of heat pipe is to utilize the evaporation of fluid media (medium) and condensation to transmit heat.The fluid media (medium) of heat pipe is different according to composition and ratio, is divided into a few class heat pipes such as low temperature, middle gentle high temperature, and comparatively common fluid media (medium) has ammonia, water, acetone and methyl alcohol etc.The heat pipe two ends are respectively evaporation ends (fire end) and condensation end (radiating end), take adiabatic measure between the two ends as required.When the heat pipe evaporation ends was heated, tube fluid medium vaporization absorbed heat of vaporization from thermal source, and vaporization back steam flows and meets the condensation knot and emit latent heat to radiating area to the opposite side condensation end.Condensate liquid borrows the effect of capillary force or gravity to reflux, the vaporization that continues to be heated, and the phase transition process of the interior heat of heat pipe by the working medium reciprocation cycle of carrying out is conducted like this, and a large amount of heats are delivered to radiating area from the thermal treatment zone.
See also Fig. 1 to Fig. 4, in the utility model preferred implementation, the utility model integrated thermal heat exchanger 100 is used to devices such as rack, accumulator cell heat preserving cabinet to regulate temperature.Integrated thermal heat exchanger 100 comprises pin-connected panel shell body 3, is housed in heat pipe heat exchanging apparatus 2, evaporation fan 5, condensation fan 8 and electric control system 1 in the shell body 3.The utility model integrated thermal heat exchanger 100 also comprises with shell body 3 and jointly integrated thermal heat exchanger 100 is separated into the isolated mutually internal circulation heat-exchanging system and the dividing plate 4 of outer circulation heat-exchange system.Above-mentioned heat pipe heat exchanging apparatus 2 lays respectively in internal circulation heat-exchanging system and the outer circulation heat-exchange system after being separated by dividing plate 4.
Heat pipe heat exchanging apparatus 2 integral body are zigzag, some flat tubes 25 of the negotiable fluid media (medium) in middle part that it comprises the upper and lower header 24 that is positioned at upper/lower terminal, be communicated with upper and lower header 24 and the some radiating fins (not label) that are connected with adjacent flat tube 25 solderings.The heat pipe heat exchanging apparatus 2 that is positioned at the below constitutes the evaporation ends 21 of the utility model integrated thermal heat exchangers 100, is positioned at the condensation end 22 that top and the heat pipe heat transfer apparatus 2 parallel with evaporation ends 21 constitute the utility model integrated thermal heat exchangers 100.Heat pipe heat exchanging apparatus 2 also has the connecting portion 23 that the inclination in the middle part of being positioned at extends to form and is connected with evaporation ends 21 and condensation end 22 respectively.Wherein, between the flat tube 25 of the connecting portion 23 at middle part, be not welded to connect radiating fin, so be formed with some hollow out grooves 230 that vertically connect between adjacent two flat tubes 25 of connecting portion 23.Evaporation ends 21 is positioned at the internal circulation heat-exchanging system, and condensation end 22 is positioned at the outer circulation heat-exchange system, thereby connecting portion 23 is connected condensation end 22 lower ends and evaporation ends 21 upper ends along tilting to extend at an angle with horizontal direction.Angle of inclination connecting portion 23 and horizontal direction changes between can be from 1 ° to 89 °.Therefore, connecting portion 23 has second connecting portion 232 that is positioned at intrasystem first connecting portion 231 of internal circulation heat-exchanging and is positioned at the outer circulation heat-exchange system.Above-mentioned hollow out groove 230 is formed between first connecting portion 231 and second connecting portion 232.
Therefore, the evaporation fan 5 that aligns by back shroud 31, with the inboard air inlet 311 of the cabinet of back shroud 31 of the internal circulation heat-exchanging system of the utility model integrated thermal heat exchanger 100, dividing plate 4, and the evaporation ends 21 of the heat pipe heat exchanging apparatus 2 that aligns with cabinet inboard air outlet 312 form.When 100 work of the utility model integrated thermal heat exchanger, the hot-air of cabinet inside is under the effect of evaporation fan 5, the inboard air inlet 311 of the cabinet of flowing through also from up to down flows to first connecting portion 231 of heat pipe heat exchanging apparatus 2, passing these first connecting portion, 231 backs is tackled by lower clapboard 42, blowback is to the evaporation ends 21 of heat exchange of heat pipe device 2, be evaporated end 21 coolings after the inboard air outlet 312 of cabinet is sent in the rack, rack is lowered the temperature.Lower clapboard 42 is the ladder gradient, helps the water conservancy diversion of wind direction, strengthens heat exchange efficiency.Because strengthen at interval between lower clapboard 42 tops and the heat pipe heat exchanging apparatus 2, help the more wind-force of drainage, and lower clapboard 42 bottoms are straight, and the interval between the heat pipe heat exchanging apparatus 2 dwindles, the wind-force that the helps drainage evaporation ends 21 that oppositely rebounds.
The condensation end 22 of the condensation fan 8 that the outer circulation heat-exchange system of the utility model integrated thermal heat exchanger 100 aligns by front shroud 32, with the cabinet of front shroud 32 outside air inlet 321, dividing plate 4 and the heat pipe heat exchanging apparatus 2 that aligns with cabinet outside air outlet 322 is formed.When the air outside the cabinet under the effect of condensation fan 8, enter condensation fan 8, and flow to second connecting portion 232 of heat pipe heat exchanging apparatus 2 from bottom to top through cabinet outside air inlet 321, passing these second connecting portion, 232 backs is tackled by upper spacer 41, blowback is to the condensation end 22 of heat exchange of heat pipe device 2, to after evaporation ends 21 is heated, vaporize and flow to the fluid media (medium) cooling of condensation end 22, and become hot-air then and be expelled to integrated thermal heat exchanger 100 outsides through cabinet outside air outlet 322.Fluid media (medium) after being cooled is re-condensed into liquid, and is back to that evaporation ends 21 cools off hot-air in the cabinet again and self vaporization by the effect of capillary force or gravity.Upper spacer 41 is the ladder gradient, helps the water conservancy diversion of wind direction, strengthens heat exchange efficiency.Because upper spacer 41 bottoms are the ladder gradient, and strengthen at interval between the heat pipe heat exchanging apparatus 2, help the more wind-force of drainage, and upper spacer 41 tops are straight, and the interval between the heat pipe heat exchanging apparatus 2 dwindles, the wind-force that the helps drainage condensation end 22 that oppositely rebounds.
At the highdensity radiating fin of flat tube 25 appearance cross-under, can reduce the volume of heat pipe heat exchanging apparatus 2 significantly, improve radiating efficiency simultaneously greatly.
Therefore, be negative pressure in the flat tube 25 of heat pipe heat exchanging apparatus 2, fluid media (medium) circulates between flat tube 25 and thermal-collecting tube 24, and stream is simply smooth and easy, and the fluid resistance is decreased little.The utility model integrated thermal heat exchanger 100 is by being separated and be formed with the heat pipe heat exchanging apparatus 2 of evaporation ends 21 and condensation end 22 by dividing plate 4, it is simple in structure, heat transfer efficiency is high, and the merit ratio of specific heat is big.
Special needs to be pointed out is, in the utility model specific embodiment only with this integrated thermal heat exchanger 100 as example, the integrated thermal heat exchanger of other types all is suitable for the principle that the utility model discloses in actual applications.For the person of ordinary skill of the art, that is done under instruction of the present utility model changes at equivalence of the present utility model, must be included in the scope that the utility model claim advocated.
Claims (10)
1. integrated thermal heat exchanger, the dividing plate that it comprises shell body, is contained in the heat pipe heat exchanging apparatus in the shell body and fixedlys connected with shell body at least; The heat pipe heat exchanging apparatus comprises evaporation ends and condensation end; Dividing plate and shell body are separated into the integrated thermal heat exchanger internal circulation heat-exchanging system and outer circulation heat-exchange system jointly; It is characterized in that: described heat pipe heat exchanging apparatus has along the connecting portion that extends to form with horizontal direction inclination certain angle, thereby this connecting portion connects condensation end and evaporation ends and passed by dividing plate and to be separated to form first connecting portion and second connecting portion, wherein first connecting portion and above-mentioned evaporation ends are positioned at the internal circulation heat-exchanging system jointly, and second connecting portion and above-mentioned condensation end are positioned at the outer circulation heat-exchange system jointly.
2. integrated thermal heat exchanger as claimed in claim 1 is characterized in that, the angle of inclination of described connecting portion and horizontal direction is between 1 ° to 89 °.
3. integrated thermal heat exchanger as claimed in claim 1 is characterized in that, the condensation end and the evaporation ends of described heat pipe heat exchanging apparatus are parallel to each other.
4. integrated thermal heat exchanger as claimed in claim 1 is characterized in that, described connecting portion is formed with some hollow out grooves, and its median septum comprises upper spacer and the lower clapboard that passes the hollow out groove respectively and seal the hollow out groove.
5. integrated thermal heat exchanger as claimed in claim 4, it is characterized in that, described upper spacer lower end and lower clapboard upper end is formed with some dentation shims respectively, and the dentation shim of each upper spacer and the dentation shim of each lower clapboard overlap each other and pass the hollow out groove jointly and seal this hollow out groove.
6. integrated thermal heat exchanger as claimed in claim 5, it is characterized in that, described upper spacer and lower clapboard are stepped, upper spacer have first installation portion parallel with condensation end, with the first installation portion almost parallel and be formed with above-mentioned dentation shim first spacer portion, and tilt to extend and be connected respectively first extension of above-mentioned first installation portion and first spacer portion; Lower clapboard have second installation portion parallel with evaporation ends, with the second installation portion almost parallel and be formed with above-mentioned dentation shim second spacer portion, and tilt to extend and be connected respectively second extension of above-mentioned second installation portion and second spacer portion.
7. integrated thermal heat exchanger as claimed in claim 6, it is characterized in that, also have the evaporation fan that is installed on above-mentioned first installation portion and be installed on the condensation fan of above-mentioned second installation portion, wherein condensation fan and condensation end align and are positioned at the outer circulation heat-exchange system jointly, and evaporation fan and evaporation ends align and be positioned at the internal circulation heat-exchanging system jointly.
8. integrated thermal heat exchanger as claimed in claim 7 is characterized in that, also has the blower fan fixed head, and described evaporation fan and condensation fan are fixed in first, second installation portion after being installed on the blower fan fixed head respectively.
9. integrated thermal heat exchanger as claimed in claim 1, it is characterized in that, described heat pipe heat exchanging apparatus comprises the last header that is positioned at the condensation end top, is positioned at the lower header of evaporation ends bottom, respectively with last header and lower header is communicated with and the flat tube of the negotiable fluid media (medium) in middle part, wherein each flat tube is Z-shaped.
10. integrated thermal heat exchanger as claimed in claim 9 is characterized in that, described heat pipe heat exchanging apparatus also comprises the radiating fin that is distributed between the adjacent flat tube, and wherein the connecting portion place is not provided with radiating fin, thereby forms above-mentioned hollow out groove.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201120020202 CN201926355U (en) | 2011-01-21 | 2011-01-21 | Integral type heat-pipe heat exchanger |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201120020202 CN201926355U (en) | 2011-01-21 | 2011-01-21 | Integral type heat-pipe heat exchanger |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201926355U true CN201926355U (en) | 2011-08-10 |
Family
ID=44430200
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 201120020202 Expired - Fee Related CN201926355U (en) | 2011-01-21 | 2011-01-21 | Integral type heat-pipe heat exchanger |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201926355U (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102607304A (en) * | 2011-01-21 | 2012-07-25 | 苏州昆拓热控系统股份有限公司 | Integral heat pipe heat exchanger |
| CN103322844A (en) * | 2013-06-27 | 2013-09-25 | 高禹丰 | Heat exchanging device |
| CN103344148A (en) * | 2013-07-10 | 2013-10-09 | 宁波司普瑞茵通信技术有限公司 | Heat exchanger core |
| CN106907810A (en) * | 2017-03-13 | 2017-06-30 | 成都育芽科技有限公司 | A kind of heavy construction space is with efficient Local cooling heat sink |
| CN113131373A (en) * | 2021-04-06 | 2021-07-16 | 盐城工业职业技术学院 | Temperature control electrical control cabinet based on sensor technology |
-
2011
- 2011-01-21 CN CN 201120020202 patent/CN201926355U/en not_active Expired - Fee Related
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102607304A (en) * | 2011-01-21 | 2012-07-25 | 苏州昆拓热控系统股份有限公司 | Integral heat pipe heat exchanger |
| CN103322844A (en) * | 2013-06-27 | 2013-09-25 | 高禹丰 | Heat exchanging device |
| CN103322844B (en) * | 2013-06-27 | 2015-01-21 | 高禹丰 | Heat exchanging device |
| CN103344148A (en) * | 2013-07-10 | 2013-10-09 | 宁波司普瑞茵通信技术有限公司 | Heat exchanger core |
| CN103344148B (en) * | 2013-07-10 | 2014-11-26 | 宁波司普瑞茵通信技术有限公司 | Heat exchanger core |
| CN106907810A (en) * | 2017-03-13 | 2017-06-30 | 成都育芽科技有限公司 | A kind of heavy construction space is with efficient Local cooling heat sink |
| CN113131373A (en) * | 2021-04-06 | 2021-07-16 | 盐城工业职业技术学院 | Temperature control electrical control cabinet based on sensor technology |
| CN113131373B (en) * | 2021-04-06 | 2021-12-21 | 盐城工业职业技术学院 | Temperature-controlled electrical control cabinet based on sensor technology |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN102607304A (en) | Integral heat pipe heat exchanger | |
| CN201503231U (en) | Compact separation type heat pipe exchanger | |
| CN101571331B (en) | Solar phase-change heat storage absorption refrigeration fresh-keeping system | |
| CN102818404A (en) | Plate-type condenser | |
| CN102818403A (en) | Plate-type evaporator | |
| CN201926355U (en) | Integral type heat-pipe heat exchanger | |
| CN102486324A (en) | Energy-saving cabinet type air-conditioner | |
| CN205119549U (en) | Multi -functional heat pump type evaporation formula condensation air conditioning unit | |
| CN104501455A (en) | Combined heating and cooling solar-assisted heat pump system | |
| CN103837027B (en) | A kind of can the microarray heat pipe solution-air heat-exchanger rig of two-way heat transfer | |
| CN202973676U (en) | Plate-type condenser | |
| CN102384682B (en) | Internal-circulation special high-efficiency heat exchanger | |
| CN104819552A (en) | Bidirectional waste heat recovery device for outdoor air pretreatment of air conditioner | |
| CN202757493U (en) | Parallel flow heat exchanger and its parallel flow heat exchange device | |
| CN201897275U (en) | Energy-saving cabinet air conditioner | |
| CN101398271A (en) | Heat extraction device for equipment room using separating hot pipe reversed flow heat exchange | |
| CN107860254B (en) | Combined heat exchanger | |
| CN203586627U (en) | Air-cooling water chilling unit for rectangular aluminum-tube heat exchanger | |
| CN201106965Y (en) | A condenser with heat recovery function | |
| CN201476415U (en) | A heat exchanger for an outdoor unit of an air-cooled heat pump air conditioner | |
| CN203024504U (en) | Plate-type evaporator | |
| CN104236174A (en) | Shell-and-tube evaporator adopting high liquid wetting flowing heat exchanging way in pipe | |
| CN203286733U (en) | Cabinet air conditioning device and cabinet air conditioning device shell | |
| CN205825778U (en) | A kind of novel heat exchange of heat pipe | |
| CN104266411B (en) | A kind of composite refrigeration system air-cooled heat exchange assembly of combined type |
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 | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20110810 Termination date: 20200121 |