CN101281001A - Closed type heat source tower - Google Patents
Closed type heat source tower Download PDFInfo
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- CN101281001A CN101281001A CNA2008100313689A CN200810031368A CN101281001A CN 101281001 A CN101281001 A CN 101281001A CN A2008100313689 A CNA2008100313689 A CN A2008100313689A CN 200810031368 A CN200810031368 A CN 200810031368A CN 101281001 A CN101281001 A CN 101281001A
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- heat source
- closed type
- low temperature
- heat exchanger
- type heat
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- 239000003570 air Substances 0.000 claims abstract description 27
- 239000007788 liquids Substances 0.000 claims abstract description 14
- 239000011901 water Substances 0.000 claims abstract description 12
- 239000007921 sprays Substances 0.000 claims description 17
- 238000000926 separation method Methods 0.000 claims description 11
- 238000010257 thawing Methods 0.000 claims description 10
- 238000007710 freezing Methods 0.000 description 4
- 238000010521 absorption reactions Methods 0.000 description 3
- 238000001816 cooling Methods 0.000 description 3
- 241001489523 Coregonus artedi Species 0.000 description 2
- 239000012080 ambient air Substances 0.000 description 2
- 239000012141 concentrates Substances 0.000 description 2
- 238000005265 energy consumption Methods 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- 238000005057 refrigeration Methods 0.000 description 2
- 241000196324 Embryophyta Species 0.000 description 1
- 239000006096 absorbing agents Substances 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 238000007906 compression Methods 0.000 description 1
- 238000010790 dilution Methods 0.000 description 1
- 238000004134 energy conservation Methods 0.000 description 1
- 238000005516 engineering processes Methods 0.000 description 1
- 238000005530 etching Methods 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 238000005755 formation reactions Methods 0.000 description 1
- 239000007789 gases Substances 0.000 description 1
- 239000000203 mixtures Substances 0.000 description 1
- 239000003921 oils Substances 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- MYMOFIZGZYHOMD-UHFFFAOYSA-N oxygen Chemical compound data:image/svg+xml;base64,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 data:image/svg+xml;base64,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 O=O MYMOFIZGZYHOMD-UHFFFAOYSA-N 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 238000001223 reverse osmosis Methods 0.000 description 1
Abstract
Description
Technical field
The present invention relates to a kind of gaseous fluid and fluid liquid heat-exchange device, especially relate to the low level heat source absorption plant that absorbs " low temperature and high relative humidity " heat in the air under a kind of low temperature environment.
Background technology
Winter is in areas to the south, the Chinese Yangtze river basin, north cold air is gone down south, be subjected to the delay that stops on Yunnan Guanyuan, Chuan Xi plateau, Wuyi Mountain Range and Nan Ling mountain range respectively, and converge from continuous the crossing with cold air from lower Nan Ling mountain range of the warm moist air at the South Sea, make southern area become warm and cold air face-off district, " low temperature and high relative humidity " becomes this zone specific weather conditions in winter.
Southern area, 2～-5 ℃ air themperature have nearly 200-250 hour (about about 10 days), and 2～5 ℃ air themperature has nearly 900-1000 hour (about about 40 days).Low potential temperature " latent heat " content height in the air, become the harmful low level heat source of traditional narrow air source heat pump, cause the heat exchanger frosting, obstruct airflow is led to heat exchange, frequent defrosting causes arrowband air source heat pump cisco unity malfunction, is aided with high-grade electrical heat energy, oil burning boiler, coal-burning boiler as auxiliary thermal source thereupon, energy consumption height, and contaminated environment.
Chinese patent CN2932272Y discloses the thermal source absorption plant-thermal source tower that absorbs heat in the air under a kind of low temperature environment, this is a kind of open type tower, the major defect of its existence is: in winter, the solution drift is serious, contaminated environment, oxygen content height behind the sudden and violent gas of solution, etching apparatus has absorbed a large amount of moisture content in " low temperature and high relative humidity " air, solution concentration changes greatly, freezing point rises, and usually causes system's cisco unity malfunction.In summer, when being converted to cooling tower, power of fan can not speed change, the energy consumption height, and wind speed is big, and drift ice is serious.
Summary of the invention
The object of the present invention is to provide thermal source absorption plant-closed type heat source tower that a kind of runnability is stable, reliable, the low temperature environment of non-corrosiveness environmentally safe absorbs low level heat source heat in the air down.
The objective of the invention is to be achieved through the following technical solutions: it comprises safeguards framework, safeguards that framework comprises the tower body framework, and the tower body frame roof is provided with chimney fan, and sidewall is provided with maintenance panel, and the tower body base of frame is provided with air intake grid; Be provided with the pneumatic system of eddy flow in the chimney fan; Safeguard and be provided with low temperature broadband heat exchanger in the framework; Heat exchanger top, low temperature broadband is provided with vapor-liquid separation; Heat exchanger below, low temperature broadband is provided with the condensate water piece-rate system.
Described low temperature broadband heat exchanger preferred broadband fin and heat exchanger tube constitute.
Preferred oblique flow refraction separator of described vapor-liquid separation and oblique fire cyclone separator constitute.
Preferred variable speed electric motors, particularly control device of the pneumatic system of described eddy flow and oblique fire eddy flow variable air rate blower fan constitute.
Described condensate water piece-rate system can be made of drip tray, condensate water control device and solution control valve.
In the preferred version, also be provided with the anti-defrosting system of the negative temperature that prevents the heat exchanger frosting of low temperature broadband.The anti-defrosting system of described negative temperature can be made of solution pool, spray pump control device and spray thrower, and spray thrower is positioned at heat exchanger top, low temperature broadband, the vapor-liquid separation top, and solution pool should place safeguards frame underneath.
The present invention is the frostless low level heat source absorber in a high efficiency broadband, both can absorb airborne low level heat source heat under low temperature environment, can provide the evaporation low-temperature receiver that is higher than 2 times of cooling towers in summer again; Or/and the source pump combination can be refrigeration machine or/and heat pump provides renewable cold (heat) energy, realize high efficiency cooling and heating with refrigeration unit, winter, heating temperature can reach 30 ℃ under auxiliary thermal source conditions such as no boiler.
Runnability of the present invention is stable, and is reliable, non-corrosiveness, energy-conservation environmentally safe.
Description of drawings
Fig. 1 is the structural representation of one embodiment of the invention.
The specific embodiment
The invention will be further described below in conjunction with accompanying drawing.
With reference to accompanying drawing, present embodiment comprises safeguards framework 1, safeguards that framework 1 comprises tower body framework 1-1, and tower body framework 1-1 top is provided with chimney fan 1-2, and sidewall is provided with maintenance panel 1-3, maintenance panel 1-3 is provided with air intake grid 1-4; Be provided with the pneumatic system 2 of eddy flow that constitutes by variable speed electric motors, particularly control device 2-1, oblique fire eddy flow blower fan 2-2 among the chimney fan 1-2; Safeguard to be provided with the low temperature broadband heat exchanger 3 that is made of broadband fin 3-1, heat exchanger tube 3-2 in the framework 1, low temperature broadband heat exchanger 3 is provided with inlet 3-3 and liquid outlet 3-4; Heat exchanger 3 tops, low temperature broadband are provided with the vapor-liquid separation 4 that is made of oblique flow refraction separator 4-1 and oblique fire cyclone separator 4-2; Heat exchanger 3 belows, low temperature broadband are provided with the condensate water piece-rate system 5 that is made of drip tray 5-1, condensate water control device 5-2 and solution control valve 5-3; Also be provided with the anti-defrosting system 6 of the negative temperature that is made of solution pool 6-1, spray pump control device 6-2, spray thrower 6-3, spray thrower 6-3 is positioned at heat exchanger 3 tops, low temperature broadband, vapor-liquid separation 4 belows, and solution pool 6-1 is positioned at and safeguards framework 1 below.
Operation principle:
Cryogenic air in the pneumatic system of eddy flow 2 bumpy weathers, make Cryogenic air safeguard framework 1 bottom from the thermal source tower, by air intake grid 1-4, enter low temperature broadband heat exchanger 3, the broadband fin 3-1 of low temperature broadband heat exchanger 3 passes to heat exchanger tube 3-2 with sensible heat and latent heat, passes to the interior circulation solution of pipe by the tube wall of heat exchanger tube 3-2 again, as source heat pump heat, discharge the sensible heat between formation broadband fin 3-1 heat-transfer area and the surrounding air and the exchange of latent heat then via vapor-liquid separation 4.
From the low temperature circulation solution that is lower than environment temperature 6-8 ℃, enter low temperature broadband heat exchanger 3, obtain to be lower than environment temperature 2-3 ℃ solution, discharge the thermal source of low potential temperature sensible heat source as the low heat heat pump.
When ambient air temperature was higher than 1.0 ℃, relative air humidity was bigger, " latent heat " content height, the low temperature broadband heat exchanger 3 airborne large quantity of moisture that when carrying out heat exchange, condensed, and condensate water piece-rate system 5 can be discharged the moisture that condenses automatically.
When ambient air temperature is lower than 1.0 ℃, relative air humidity is less, meet cold for preventing humid air, heat exchanger 3 frostings of low temperature broadband, the anti-defrosting system 6 of negative temperature is according to design temperature control requirement, and automatic spray environmental protection anti-freezing solution reduces low temperature broadband heat exchanger 3 surperficial freezing points, anti-freezing solution after the dilution treats after the low thermoperiod that spray concentrates or adopt reverse osmosis concentrated compression apparatus to concentrate certainly.
Claims (10)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2008100313689A CN101281001B (en) | 2008-05-23 | 2008-05-23 | Closed type heat source tower |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2008100313689A CN101281001B (en) | 2008-05-23 | 2008-05-23 | Closed type heat source tower |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN101281001A true CN101281001A (en) | 2008-10-08 |
| CN101281001B CN101281001B (en) | 2011-05-04 |
Family
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2008100313689A CN101281001B (en) | 2008-05-23 | 2008-05-23 | Closed type heat source tower |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN101281001B (en) |
Cited By (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102003895A (en) * | 2010-11-24 | 2011-04-06 | 刘秋克 | Closed and integrated frostproof heat source tower |
| CN102003838A (en) * | 2010-11-16 | 2011-04-06 | 刘秋克 | Solar-powered primary source heat source tower heat pump complete device |
| WO2011044801A1 (en) * | 2009-10-12 | 2011-04-21 | Liu Qiuke | Complete set of heat source tower heat pump using solar energy secondary source |
| CN102147134A (en) * | 2011-01-05 | 2011-08-10 | 东南大学 | Solution dehumidifying and regenerating device |
| CN102345908A (en) * | 2011-08-26 | 2012-02-08 | 东南大学 | Solution dehumidification regenerating unit |
| CN103134343A (en) * | 2011-11-25 | 2013-06-05 | 北京紫荆信达节能科技有限公司 | Heat source tower having solution regeneration function |
| CN103245211A (en) * | 2013-05-15 | 2013-08-14 | 海门市大生水处理设备（厂）有限公司 | Circulating cooling tower |
| CN103697554A (en) * | 2013-12-27 | 2014-04-02 | 湖南大学 | Water collecting, water distributing and collected-liquid circulating system of closed-type heat source tower |
| CN104676798A (en) * | 2015-03-17 | 2015-06-03 | 黄国和 | All-weather solar water source heat pump air conditioning system |
| CN105588470A (en) * | 2014-11-14 | 2016-05-18 | 北京方道环保科技有限公司 | Circulating water cooling tower capable of heating turbulent flow tube bank |
Family Cites Families (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2000337790A (en) * | 1999-05-24 | 2000-12-08 | Ishikawajima Harima Heavy Ind Co Ltd | Snow-melting system for cooling tower |
| CN2482033Y (en) * | 2001-05-23 | 2002-03-13 | 王德元 | Combined condensing and cooling device for small central air conditioner |
| CN101169299A (en) * | 2007-11-30 | 2008-04-30 | 清华大学 | Indirect evaporation type cooling/condensing device |
-
2008
- 2008-05-23 CN CN2008100313689A patent/CN101281001B/en active IP Right Grant
Cited By (15)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2011044801A1 (en) * | 2009-10-12 | 2011-04-21 | Liu Qiuke | Complete set of heat source tower heat pump using solar energy secondary source |
| CN102003838A (en) * | 2010-11-16 | 2011-04-06 | 刘秋克 | Solar-powered primary source heat source tower heat pump complete device |
| CN102003895B (en) * | 2010-11-24 | 2012-04-25 | 刘秋克 | Closed and integrated frostproof heat source tower |
| CN102003895A (en) * | 2010-11-24 | 2011-04-06 | 刘秋克 | Closed and integrated frostproof heat source tower |
| CN102147134A (en) * | 2011-01-05 | 2011-08-10 | 东南大学 | Solution dehumidifying and regenerating device |
| CN102345908A (en) * | 2011-08-26 | 2012-02-08 | 东南大学 | Solution dehumidification regenerating unit |
| CN103134343B (en) * | 2011-11-25 | 2015-02-25 | 北京紫荆信达节能科技有限公司 | Heat source tower with solution capable of regeneration function |
| CN103134343A (en) * | 2011-11-25 | 2013-06-05 | 北京紫荆信达节能科技有限公司 | Heat source tower having solution regeneration function |
| CN103245211A (en) * | 2013-05-15 | 2013-08-14 | 海门市大生水处理设备（厂）有限公司 | Circulating cooling tower |
| CN103697554A (en) * | 2013-12-27 | 2014-04-02 | 湖南大学 | Water collecting, water distributing and collected-liquid circulating system of closed-type heat source tower |
| CN103697554B (en) * | 2013-12-27 | 2016-02-03 | 湖南大学 | A kind of closed type heat source tower water receiving divides the water liquid collecting circulatory system |
| CN105588470A (en) * | 2014-11-14 | 2016-05-18 | 北京方道环保科技有限公司 | Circulating water cooling tower capable of heating turbulent flow tube bank |
| CN105588470B (en) * | 2014-11-14 | 2020-11-17 | 北京方道环保科技有限公司 | Circulating water cooling tower capable of heating turbulent flow calandria |
| CN104676798A (en) * | 2015-03-17 | 2015-06-03 | 黄国和 | All-weather solar water source heat pump air conditioning system |
| CN104676798B (en) * | 2015-03-17 | 2017-04-05 | 黄国和 | A kind of all-weather solar water source heat pump air conditioning system |
Also Published As
| Publication number | Publication date |
|---|---|
| CN101281001B (en) | 2011-05-04 |
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Effective date of registration: 20121127 Address after: 412000 Tianyuan District of Zhuzhou City, Hunan Province, No. 208 Xuelin Yayuan Patentee after: Hunan Qiuke Heat Towers Heat Pump Technology Engineering Co., Ltd. Address before: 410001 Hunan province Changsha Wuyi Square in Jingjiang Eastern Mansion 906F Patentee before: Liu Qiuke |
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Effective date of registration: 20130104 Address after: 412007 Taishan Road, Hunan city of Zhuzhou province Tianyuan District No. 233 hi tech Industrial Building A2 Patentee after: Liu Bocheng Address before: 412000 Tianyuan District of Zhuzhou City, Hunan Province, No. 208 Xuelin Yayuan Patentee before: Hunan Qiuke Heat Towers Heat Pump Technology Engineering Co., Ltd. |
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