CN102003895A - Closed and integrated frostproof heat source tower - Google Patents

Closed and integrated frostproof heat source tower Download PDF

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Publication number
CN102003895A
CN102003895A CN2010105564746A CN201010556474A CN102003895A CN 102003895 A CN102003895 A CN 102003895A CN 2010105564746 A CN2010105564746 A CN 2010105564746A CN 201010556474 A CN201010556474 A CN 201010556474A CN 102003895 A CN102003895 A CN 102003895A
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China
Prior art keywords
heat
tower
pipeline
crossing current
fin
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CN2010105564746A
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Chinese (zh)
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CN102003895B (en
Inventor
刘秋克
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刘秋克
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Priority to CN2010105564746A priority Critical patent/CN102003895B/en
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Publication of CN102003895B publication Critical patent/CN102003895B/en

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Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28CHEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA COME INTO DIRECT CONTACT WITHOUT CHEMICAL INTERACTION
    • F28C1/00Direct-contact trickle coolers, e.g. cooling towers
    • F28C1/14Direct-contact trickle coolers, e.g. cooling towers comprising also a non-direct contact heat exchange
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28DHEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
    • F28D3/00Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium flows in a continuous film, or trickles freely, over the conduits
    • F28D3/04Distributing arrangements
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28DHEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
    • F28D5/00Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, using the cooling effect of natural or forced evaporation
    • F28D5/02Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, using the cooling effect of natural or forced evaporation in which the evaporating medium flows in a continuous film or trickles freely over the conduits
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02BCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO BUILDINGS, e.g. HOUSING, HOUSE APPLIANCES OR RELATED END-USER APPLICATIONS
    • Y02B30/00Energy efficient heating, ventilation or air conditioning [HVAC]
    • Y02B30/70Efficient control or regulation technologies, e.g. for control of refrigerant flow, motor or heating

Abstract

The invention discloses a closed and integrated frostproof heat source tower, which comprises a tower body, wherein an outer fin air source heat exchange system, a fin inner tube liquid heat exchange system and a wet heat source condensed water separator are arranged on the tower body. Under the weather conditions of 'low temperature and high humidity' in winter and 'high temperature and high humidity' in summer, the closed and integrated frostproof heat source tower can circularly and efficiently absorb cold and heat sources in the air in a closed way, has a wet heat source condensed water separator, overcomes shortcomings of the conventional devices, avoids directly discharging a small amount of diluted solution and polluting water environment, realizes the optimal practical matching of devices, performs efficient, economic, reliable and stable operation, and is environmentally-friendly in discharge and wide in application range.

Description

The integrated frost prevention thermal source of a kind of enclosed tower
Technical field
The present invention relates to the integrated frost prevention thermal source of a kind of enclosed tower, especially relate to and a kind ofly provide temperature lower low-temperature receiver for refrigeration machine, the integrated frost prevention thermal source of the enclosed tower of the no dilute solution discharging of renewable Lowlevel thermal energy is provided for heat pump winter in summer.
Background technology
Southern china located in subtropical zone monsoon climatic region, winter, north cold air was gone down south and converge from equatorial warm moist air, made southern wide geographic area become warm and cold air face-off district, and " low temperature and high relative humidity " becomes the specific weather conditions in areas to the south, the Yangtze river basin.Just because of this special climate condition, contained unlimited inferior source of students low temperature potential energy in the humid air by conversion of solar energy.Calorific potential content height under the humid air state, because what the conventional air source heat pump air-conditioner prolonged usefulness is big different transfer of heat technology under the external weather conditions, often low because of evaporating temperature, cause frosting frequency height, in case and frosting, just can't normally move heat supply, need directly to adopt the auxilliary heating of high power electricity heat supply, the energy consumption height.Calorific potential becomes the regenerative resource harmful to air-cooled heat pump.And this also becomes insoluble in decades technical barrier.
Existing all kinds of absorption air source low-temperature potential energy devices, mostly be to utilize low freezing point solution and air to carry out directly outer exchange circulation, concentrated solution is when carrying out heat exchange with air, absorb airborne condensate water and be divided into dilute solution, because salting liquid aeration circulation dissolved oxygen has serious corrosivity to system equipment, range of application also is only limited to more than the air themperature-3 ℃, thereby can not be used widely.Even more serious is, some with the salting liquid be the low temperature potential energy absorption plant of representative in order to keep the lower freezing point of solution concentration, the circulation solution after it will dilute causes serious water environment pollution without just directly discharging of any processing.
Chinese patent CN200810031368.9 discloses a kind of " closed type heat source tower " and Chinese patent CN200920311781.0 discloses a kind of " solar energy secondary source Cooling and Heat Source tower ".Though above-mentioned two kinds are installed and are the built-in solution loop structure of totally enclosed type, the heat exchange circulation solution does not directly contact with air, has solved the directly pollution that causes to environment of discharging of the dilute solution that caused when traditional open type cooling tower, open type energy tower etc. utilize solution aeration circulation to absorb low-temperature heat energy in the air.But the defective that these two kinds of devices exist under environment negative temperature condition is to need the damp and hot source of outer configuration condensate water separator to mate Installation and Debugging and operational management, complex operation to the user.
Summary of the invention
The objective of the invention is to overcome the above-mentioned defective that prior art exists, provide under a kind of " low temperature and high relative humidity " in the winter time and summer " hot and humid " weather conditions, all can carry the integrated frost prevention thermal source of the enclosed tower of damp and hot source condensate water separator with the airborne Cooling and Heat Source of closed circulation efficient absorption.
Technical scheme of the present invention is: it comprises tower body, and tower body is provided with pipe liquid heat-exchange system and damp and hot source condensate water separator in outer fin air source heat-exchange system, the fin.
Described outer fin air source heat-exchange system comprises tower body side crossing current air intake grid, the outer finned heat exchanger of crossing current, low temperature steam fog separate gate, variable air rate aerophor, rotational flow separation silencer and tower body enclosed structure; Tower body side crossing current air intake grid is located at tower body enclosed structure side and is communicated with the outer finned heat exchanger of crossing current, the main solution dish top that the outer finned heat exchanger that flows over is located at damp and hot source condensate water separator communicates with low temperature steam fog separate gate, low temperature steam fog separate gate is located between outer finned heat exchanger of crossing current and the variable air rate aerophor, the variable air rate aerophor is located at the tower body inner upper end, the rotational flow separation silencer is located at the tower body outer tip end, and the tower body enclosed structure is the framework that the agent structure of thermal source tower connects other parts.
Pipe liquid heat-exchange system in the described fin comprises heat exchange of heat pipe in the interior heat exchange of heat pipe lower collector pipe of flowing over, the fin crossing current, the interior heat exchange of heat pipe upper header of crossing current; Heat exchange of heat pipe is made of the main solution dish top of being located at damp and hot source condensate water separator in the fin crossing current pipe in the fin of parallel connection, the heat exchange of heat pipe lower collector pipe is that the import of low temperature circulatory mediator links to each other with external equipment low heat source heat pump heat side in the crossing current, and the heat exchange of heat pipe upper header is connected with external equipment low heat evaporator with heat pump for the circulatory mediator outlet of heating in the crossing current.
Described damp and hot source condensate water separator is made up of heat pump heating system, film condensate water piece-rate system.
Described heat pump heating system comprises heat pump compressor, heats cold condenser, expansion valve, steam fog evaporimeter; Heat pump compressor is located at the tower body inner bottom, the heat pump compressor exhaust outlet is connected with heats cold condenser working medium air inlet by pipeline, import is connected with expansion valve with filter by pipeline in heats cold condenser working medium gas outlet, the expansion valve outlet is connected with the steam fog evaporator by pipeline, the steam fog evaporator outlet is inhaled steam ports by pipeline and heat pump compressor and is connected, and the steam fog evaporimeter is located between outer finned heat exchanger of crossing current and the variable air rate aerophor.
Described film condensate water piece-rate system comprise high-pressure pump, with shared heats cold condenser, more medium filter, film separator tube, solution spraying assembly, main solution dish and the solution baffle-box of heat pump heating system; Main solution dish is located at the following middle part of tower body of tower body enclosed structure and is positioned at condensate water separator top, damp and hot source, main solution tray bottom collecting tank liquid outlet is connected with solution baffle-box inlet with motor-driven valve by pipeline, solution baffle-box liquid outlet is connected with the high-pressure pump inlet by pipeline, the high-pressure pump liquid outlet is connected with heats cold condenser medium inlet with valve by pipeline, heats cold condenser medium liquid outlet is connected with the more medium filter inlet with valve by pipeline, import is connected the more medium filter liquid outlet with the film separator tube with valve by pipeline, film separator tube liquid outlet passes through pipeline, motor-driven valve is connected with solution spraying assembly inlet with control valve, and the solution spraying assembly is located at heat exchange of heat pipe upper end in the fin crossing current.
The present invention can realize under weather " hot and humid " state that the negative pressure evaporation cooling discharges heat energy; Built-in circulation solution of enclosed and the application of air negative temperature compressible environmental protection solution of spray macromolecule frost prevention outside intermittence under weather " low temperature and high relative humidity " state, the source, solar energy secondary source renewable cold (heat) of cheap no any pollution is provided to the low heat heat pump, import a spot of high-grade energy (as the electric power secondary clean energy) to heat pump, efficient absorption is from solar energy secondary source low-temperature heat energy, realize that low-grade energy is to high potential temperature (height potential temperature energy, the height of energy amount temperature, what can directly utilize is high potential, what need that regeneration promotes is the low temperature potential energy) transfer, be reached for building refrigeration be provided, the purpose of heat supply and health hot water.Under abominable " low temperature and high relative humidity " climatic environment, heating efficiency of the present invention improves 100% than conventional air source heat pump.The present invention can be used as the main Cooling and Heat Source absorption plant supporting with the low heat heat pump.
The present invention carries damp and hot source condensate water separator, has overcome the defective that existing apparatus exists, and has avoided a spot of dilute solution is directly discharged the water environment pollution that causes; Realized best practical coupling, high-efficiency and economic operation, environment protection emission between the equipment, reliable stable, have wide range of applications.
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 drawings and Examples.
With reference to Fig. 1, present embodiment comprises tower body, and tower body is provided with pipe liquid heat-exchange system and damp and hot source condensate water separator in outer fin air source heat-exchange system, the fin.
Described outer fin air source heat-exchange system comprises tower body side crossing current air intake grid 1-1, crossing current outer finned heat exchanger 1-2, low temperature steam fog separate gate 1-3, variable air rate aerophor 1-4, rotational flow separation silencer 1-5 and tower body enclosed structure 1-6; Tower body side crossing current air intake grid 1-1 is located at tower body enclosed structure 1-6 side and communicates with the outer finned heat exchanger 1-2 of crossing current, the main solution dish 3-25 top that the outer finned heat exchanger 1-2 that flows over is located at damp and hot source condensate water separator communicates with low temperature steam fog separate gate 1-3, low temperature steam fog separate gate 1-3 is located between outer finned heat exchanger 1-2 of crossing current and the variable air rate aerophor 1-4, variable air rate aerophor 1-4 is located at the tower body inner upper end, rotational flow separation silencer 1-5 is located at the tower body outer tip end, and tower body enclosed structure 1-6 is the framework that the agent structure of thermal source tower connects other parts.
Pipe liquid heat-exchange system in the described fin comprises heat exchange of heat pipe 2-2 in the interior heat exchange of heat pipe lower collector pipe 2-1 that flows over, the fin crossing current, the interior heat exchange of heat pipe upper header 2-3 of crossing current; Heat exchange of heat pipe 2-2 is made of the main solution dish 3-25 top of being located at damp and hot source condensate water separator in the fin crossing current pipe in the fin of parallel connection, heat exchange of heat pipe lower collector pipe 2-1 is that the import of low temperature circulatory mediator links to each other with external equipment low heat source heat pump heat side (not shown) in the crossing current, and heat exchange of heat pipe upper header 2-3 is connected with external equipment low heat evaporator with heat pump (not shown) for the circulatory mediator outlet of heating in the crossing current.
Described damp and hot source condensate water separator is made up of heat pump heating system, film condensate water piece-rate system.
Described heat pump heating system comprises heat pump compressor 3-11, heats cold condenser 3-12, expansion valve 3-13, steam fog evaporimeter 3-14; Heat pump compressor 3-11 is located at the tower body inner bottom, heat pump compressor 3-11 exhaust outlet is connected with heats cold condenser 3-12 working medium air inlet by pipeline, import is connected with expansion valve 3-13 with filter by pipeline in heats cold condenser 3-12 working medium gas outlet, expansion valve 3-13 outlet is connected with steam fog evaporimeter 3-14 import by pipeline, steam fog evaporimeter 3-14 outlet is inhaled steam ports by pipeline with heat pump compressor 3-11 and is connected, and steam fog evaporimeter 3-14 is located between outer finned heat exchanger 1-2 of crossing current and the variable air rate aerophor 1-4.
Described film condensate water piece-rate system comprise high-pressure pump 3-21, with shared heats cold condenser 3-12, more medium filter 3-22, film separator tube 3-23, solution spraying assembly 3-24, main solution dish 3-25 and the solution baffle-box 3-26 of heat pump heating system; Main solution dish 3-25 is located at the following middle part of tower body of tower body enclosed structure 1-6 and is positioned at condensate water separator top, damp and hot source, main solution dish 3-25 bottom collecting tank liquid outlet is connected with solution baffle-box 3-26 inlet with motor-driven valve by pipeline, solution baffle-box 3-26 liquid outlet is connected with high-pressure pump 3-21 inlet by pipeline, high-pressure pump 3-21 liquid outlet is connected with heats cold condenser 3-12 medium inlet with valve by pipeline, heats cold condenser 3-12 medium liquid outlet is connected with more medium filter 3-22 inlet with valve by pipeline, import is connected more medium filter 3-22 liquid outlet with film separator tube 3-23 with valve by pipeline, film separator tube 3-23 liquid outlet passes through pipeline, motor-driven valve is connected with solution spraying assembly 3-24 inlet with control valve, and solution spraying assembly 3-24 is located at heat exchange of heat pipe 2-2 upper end in the fin crossing current.
Operation principle:
Outer fin air source heat-exchange system operation principle: the damp and hot source of low temperature air enters the low-temperature heat energy that finned heat exchanger 1-2 release air carries outside the crossing current through tower body side crossing current air intake grid 1-1, circulating air temperature descends and enters low temperature steam fog separate gate 1-3, pressurize via variable air rate aerophor 1-4, forced air is pressed into rotational flow separation silencer 1-5 and removes and to enter surrounding air behind the mist elimination vapour and carry out the heat exchange circulation of heating, and is entered by tower body side crossing current air intake grid 1-1 and finishes outer fin air source heat-exchange system and circulate.
Manage liquid heat-exchange system works principle in the fin: low heat source heat pump heat side (not shown) low temperature circulatory mediator enters the low-temperature heat energy that the absorption of heat exchange of heat pipe 2-2 pipe group is carried by the outer finned heat exchanger 1-2 release of crossing current air in the fin crossing current by the interior heat exchange of heat pipe lower collector pipe 2-1 of crossing current, the circulation solution temperature raises, and heat exchange of heat pipe upper header 2-3 discharge enters low heat evaporator with heat pump (not shown) in flowing over, and finishes cyclic process.
The operation principle of the heat pump heating system of described damp and hot source condensate water separator: heat pump compressor 3-11 high pressure gas enters heats cold condenser 3-12 working medium side by pipeline, after discharging the latent heat of condensation, heats cold condenser 3-12 side medium is condensed into highly pressurised liquid, highly pressurised liquid enters expansion valve 3-13 throttling step-down by pipeline and filter, the low-temperature heat energy that enters in the inner circulating air of steam fog evaporimeter 3-14 absorption tower by pipeline is evaporated to low-pressure steam, and low-pressure steam enters heat pump compressor 3-11 suction steam ports by pipeline and finishes circulation through heat pump work done lifting.
The operation principle of the film condensate water piece-rate system of described damp and hot source condensate water separator: main solution dish 3-25 has received by the outer finned heat exchanger 1-2 fin surface of the crossing current dilute solution that moisture solubilization liquid becomes that condenses, after the collecting tank liquid outlet enters solution baffle-box 3-26 by pipeline and motor-driven valve bottom main solution dish 3-25, enter high-pressure pump 3-21 pressurized circulation through solution baffle-box 3-26 liquid outlet by pipeline again, pressurized solution goes out by pipeline and valve to enter heats cold condenser 3-12 side medium heat temperature raising, solution behind the heat temperature raising enters more medium filter 3-22 by pipeline and valve and filters, the solution that filters enters film separator tube 3-23 by pipeline and valve and isolates concentrated solution and condensate water, concentrated solution passes through pipeline, motor-driven valve and control valve enter solution spraying assembly 3-24 finned heat exchanger 1-2 spray outside crossing current, reduce the heat exchanger surface freezing point, absorption water in air branch, concentrated solution becomes dilute solution and enters main solution dish 3-25, finishes film condensate water separating cycle.

Claims (1)

1. the integrated frost prevention thermal source of an enclosed tower is characterized in that, comprises tower body, and tower body is provided with pipe liquid heat-exchange system and damp and hot source condensate water separator in outer fin air source heat-exchange system, the fin;
Described outer fin air source heat-exchange system comprises tower body side crossing current air intake grid, the outer finned heat exchanger of crossing current, low temperature steam fog separate gate, variable air rate aerophor, rotational flow separation silencer and tower body enclosed structure; Tower body side crossing current air intake grid is located at tower body enclosed structure side and is communicated with the outer finned heat exchanger of crossing current, the main solution dish top that the outer finned heat exchanger that flows over is located at damp and hot source condensate water separator communicates with low temperature steam fog separate gate, low temperature steam fog separate gate is located between outer finned heat exchanger of crossing current and the variable air rate aerophor, the variable air rate aerophor is located at the tower body inner upper end, the rotational flow separation silencer is located at the tower body outer tip end, and the tower body enclosed structure is the framework that the agent structure of thermal source tower connects other parts;
Pipe liquid heat-exchange system in the described fin comprises heat exchange of heat pipe in the interior heat exchange of heat pipe lower collector pipe of flowing over, the fin crossing current, the interior heat exchange of heat pipe upper header of crossing current; Heat exchange of heat pipe is made of the main solution dish top of being located at damp and hot source condensate water separator in the fin crossing current pipe in the fin of parallel connection, the heat exchange of heat pipe lower collector pipe is that the import of low temperature circulatory mediator links to each other with external equipment low heat source heat pump heat side in the crossing current, and the heat exchange of heat pipe upper header is connected with external equipment low heat evaporator with heat pump for the circulatory mediator outlet of heating in the crossing current;
Described damp and hot source condensate water separator is made up of heat pump heating system, film condensate water piece-rate system;
Described heat pump heating system comprises heat pump compressor, heats cold condenser, expansion valve, steam fog evaporimeter; Heat pump compressor is located at the tower body inner bottom, the heat pump compressor exhaust outlet is connected with heats cold condenser working medium air inlet by pipeline, import is connected with expansion valve with filter by pipeline in heats cold condenser working medium gas outlet, the expansion valve outlet is connected with the steam fog evaporator by pipeline, the steam fog evaporator outlet is inhaled steam ports by pipeline and heat pump compressor and is connected, and the steam fog evaporimeter is located between outer finned heat exchanger of crossing current and the variable air rate aerophor;
Described film condensate water piece-rate system comprise high-pressure pump, with shared heats cold condenser, more medium filter, film separator tube, solution spraying assembly, main solution dish and the solution baffle-box of heat pump heating system; Main solution dish is located at the following middle part of tower body of tower body enclosed structure and is positioned at condensate water separator top, damp and hot source, main solution tray bottom collecting tank liquid outlet is connected with solution baffle-box inlet with motor-driven valve by pipeline, solution baffle-box liquid outlet is connected with the high-pressure pump inlet by pipeline, the high-pressure pump liquid outlet is connected with heats cold condenser medium inlet with valve by pipeline, heats cold condenser medium liquid outlet is connected with the more medium filter inlet with valve by pipeline, import is connected the more medium filter liquid outlet with the film separator tube with valve by pipeline, film separator tube liquid outlet passes through pipeline, motor-driven valve is connected with solution spraying assembly inlet with control valve, and the solution spraying assembly is located at heat exchange of heat pipe upper end in the fin crossing current.
CN2010105564746A 2010-11-24 2010-11-24 Closed and integrated frostproof heat source tower CN102003895B (en)

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Application Number Priority Date Filing Date Title
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CN102003895A true CN102003895A (en) 2011-04-06
CN102003895B CN102003895B (en) 2012-04-25

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Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103292401A (en) * 2013-06-18 2013-09-11 东南大学 Multifunctional transverse flow type heat source tower device
CN105180316A (en) * 2014-06-21 2015-12-23 刘秋克 Haze freezing and heat supply device of electrostatic field
CN105299794A (en) * 2014-07-19 2016-02-03 刘秋克 Double-channel cold and heat source haze purifying and heating tower
CN105318462A (en) * 2014-07-02 2016-02-10 刘秋克 Integrated device with static haze treating, freezing defogging, purifying and heat supplying functions
WO2018189887A1 (en) * 2017-04-14 2018-10-18 一男 中野 Falling film type heat exchanger
CN110068231A (en) * 2019-04-04 2019-07-30 华北水利水电大学 A kind of L-type cooling tower heating fog-dissipation device
CN110425907A (en) * 2019-07-12 2019-11-08 扬州安宇化工设备有限公司 A kind of evaporative heat exchanger that heat exchanger effectiveness is high

Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2000266447A (en) * 1999-03-16 2000-09-29 Hitachi Metals Ltd Cooling system
CA2327936A1 (en) * 1999-12-10 2001-06-10 Hudson Products Corporation Passive wet cooling tower plume abatement system
US20030214055A1 (en) * 2002-05-17 2003-11-20 Air Handling Engineering Ltd. Outlet silencer for cooling tower, evaporator cooler or condenser
JP2008215761A (en) * 2007-03-07 2008-09-18 Hitachi Metals Ltd Cooling device
CN101281001A (en) * 2008-05-23 2008-10-08 刘秋克 Closed type heat source tower
CN101672552A (en) * 2009-10-12 2010-03-17 湖南秋克热源塔热泵科技工程有限公司 Tower heating pump complete device with solar energy secondary heat source
CN201497390U (en) * 2009-09-29 2010-06-02 湖南秋克热源塔热泵科技工程有限公司 Solar secondary biogenous cold-heat source tower
CN201892437U (en) * 2010-11-24 2011-07-06 刘秋克 Closed integrated anti-frost heat source tower

Patent Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2000266447A (en) * 1999-03-16 2000-09-29 Hitachi Metals Ltd Cooling system
CA2327936A1 (en) * 1999-12-10 2001-06-10 Hudson Products Corporation Passive wet cooling tower plume abatement system
US20030214055A1 (en) * 2002-05-17 2003-11-20 Air Handling Engineering Ltd. Outlet silencer for cooling tower, evaporator cooler or condenser
JP2008215761A (en) * 2007-03-07 2008-09-18 Hitachi Metals Ltd Cooling device
CN101281001A (en) * 2008-05-23 2008-10-08 刘秋克 Closed type heat source tower
CN201497390U (en) * 2009-09-29 2010-06-02 湖南秋克热源塔热泵科技工程有限公司 Solar secondary biogenous cold-heat source tower
CN101672552A (en) * 2009-10-12 2010-03-17 湖南秋克热源塔热泵科技工程有限公司 Tower heating pump complete device with solar energy secondary heat source
CN201892437U (en) * 2010-11-24 2011-07-06 刘秋克 Closed integrated anti-frost heat source tower

Cited By (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103292401A (en) * 2013-06-18 2013-09-11 东南大学 Multifunctional transverse flow type heat source tower device
CN103292401B (en) * 2013-06-18 2015-06-17 东南大学 Multifunctional transverse flow type heat source tower device
CN105180316A (en) * 2014-06-21 2015-12-23 刘秋克 Haze freezing and heat supply device of electrostatic field
CN105180316B (en) * 2014-06-21 2018-10-19 刘秋克 Electrostatic field freezes haze heating plant
CN105318462A (en) * 2014-07-02 2016-02-10 刘秋克 Integrated device with static haze treating, freezing defogging, purifying and heat supplying functions
CN105318462B (en) * 2014-07-02 2018-06-29 湖南三合能水汽热泵有限公司 Electrostatic controls haze freezing demisting purification heat supply all-in-one machine
CN105299794A (en) * 2014-07-19 2016-02-03 刘秋克 Double-channel cold and heat source haze purifying and heating tower
CN105299794B (en) * 2014-07-19 2018-06-01 湖南三合能水汽热泵有限公司 The purification of binary channels Cooling and Heat Source haze takes thermal tower
WO2018189887A1 (en) * 2017-04-14 2018-10-18 一男 中野 Falling film type heat exchanger
CN110068231A (en) * 2019-04-04 2019-07-30 华北水利水电大学 A kind of L-type cooling tower heating fog-dissipation device
CN110425907A (en) * 2019-07-12 2019-11-08 扬州安宇化工设备有限公司 A kind of evaporative heat exchanger that heat exchanger effectiveness is high

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