CN201535595U - Solar secondary source, heat source tower and heat pump complete plant - Google Patents
Solar secondary source, heat source tower and heat pump complete plant Download PDFInfo
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- CN201535595U CN201535595U CN2009203123012U CN200920312301U CN201535595U CN 201535595 U CN201535595 U CN 201535595U CN 2009203123012 U CN2009203123012 U CN 2009203123012U CN 200920312301 U CN200920312301 U CN 200920312301U CN 201535595 U CN201535595 U CN 201535595U
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Abstract
A solar secondary source, heat source tower and heat pump complete plant comprises a cold-heat source tower, a low heat source cyclone heat pump, a condensed water separator, an auxiliary device and a tail load system. The solar secondary source, heat source tower and heat pump complete plant can realize the negative evaporation, cooling and refrigeration under the states of high temperature and high moisture, absorbs and promotes low-temperature heat energy from a solar secondary source under the states of low temperature and high moisture in high efficiency, can be used as a highly-effective negative evaporation water-cooling secondary energy efficiency refrigerator in summer, can be used as a heat-transfer frostless air source heat pump with wideband, high efficiency and small temperature difference in winter, integrates a water-cooling refrigerator with a boiler device and an air source heat pump with an electric auxiliary heating device which are commonly used in southern regions, omits the boiler and the electric auxiliary heating, realizes the combination of cold and heat air conditioning and hot water, has three purposes, and is beneficial for energy conservation and emission reduction, and the comprehensive economic performance index thereof is higher 25-50% than an existing central air conditioning system in southern region.
Description
Technical field
The utility model relates to a kind of solar energy secondary heat-source tower heat pump complete set of equipments, especially relates to a kind of solar energy secondary heat-source tower heat pump complete set of equipments device that uses under " low temperature and high relative humidity " state in " hot and humid " winter in summer.
Background technology
China's south located in subtropical zone monsoon climatic region, winter, north cold air is gone down south and is converged from equatorial warm moist air, makes 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.
But because the conventional air source heat pump air-conditioner prolongs usefulness is big different transfer of heat technology under the external weather conditions, winter, 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.This is up to now, in decades, and unsolved always technical barrier.
And existing earth source heat pump, because of mountain region structure and the cold and hot imbalance of weather, the initial stage one-time investment is big, has only the energy-saving benefit about 30 days the whole year, and return rate is lower, and the comprehensive economic performance index is on the low side.
The utility model content
The purpose of this utility model is to overcome the above-mentioned defective that existing air source heat pump 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 absorb/promote airborne cold (heat) source efficiently, comprehensive economic performance index higher solar energy secondary heat-source tower heat pump complete set of equipments device.
The technical solution of the utility model is: it comprises, and Cooling and Heat Source tower, low heat eddy flow heat pump, condensed moisture are disembarked, servicing unit, terminal load system;
The Cooling and Heat Source tower can use existing known Cooling and Heat Source tower, the Cooling and Heat Source tower of preferred following structure: it comprises the heat exchange blower fan that is installed on the support, heat exchange blower fan top is provided with high molecular weight hydrophilic aerosol separator, the bottom is provided with frost prevention spray assembly, frost prevention spray assembly bottom is provided with the secondary demister, and secondary demister bottom is provided with heat exchanger, and the heat exchanger bottom is provided with the cool water shower device, cool water shower device bottom is provided with drip tray, and the drip tray bottom is provided with the solution regulating reservoir;
Described low heat eddy flow heat pump comprises condenser, and condenser is communicated with little different transfer of heat evaporimeter, and little different transfer of heat evaporimeter links to each other with the low heat helical-lobe compressor, and the wideband electronic expansion valve is communicated with condenser shell side refrigeration working medium liquid outlet;
Described condensed moisture is disembarked and is comprised the condensation film separator, and condensation film separator top is provided with the heat pump device;
Described servicing unit comprises Cooling and Heat Source pump, first four-way change-over valve, second four-way change-over valve, terminal partial load pump;
Terminal load system comprises terminal load side water supply line, terminal load side water return pipeline, end heat exchanger;
The heat exchanger exit of Cooling and Heat Source tower is connected with the Cooling and Heat Source Pump Suction Nozzle of auxiliary equipment device by pipeline, the outlet of Cooling and Heat Source pump pressure is connected with first four-way change-over valve, first inlet by the pipeline that filter and check-valves are housed, first four-way change-over valve, first liquid outlet is connected with the little different transfer of heat evaporimeter inlet of low heat eddy flow heat pump by pipeline, the little different transfer of heat evaporimeter liquid outlet of low heat eddy flow heat pump is connected with second four-way change-over valve, first inlet by pipeline, second four-way change-over valve, first liquid outlet is connected with the heat exchanger inlet of Cooling and Heat Source tower by the pipeline that valve is housed, and constitutes the cold and hot source circulatory system thus;
Terminal load side water return pipeline is connected with the partial load pump suction inlet of auxiliary equipment device by the pipeline that valve is housed, partial load pump extrudes mouth and is connected with second inlet of first four-way change-over valve by the pipeline that filter and check-valves are housed, second liquid outlet of first four-way change-over valve is connected by the condenser water inlet of pipeline with low heat eddy flow heat pump, the condenser delivery port of low heat eddy flow heat pump is connected with second inlet of second four-way change-over valve by pipeline, second liquid outlet of second four-way change-over valve is connected with terminal load side water supply line by pipeline, constitutes the terminal load side circulatory system thus;
The condensation film separator inlet that the solution regulating reservoir liquid outlet of Cooling and Heat Source tower is disembarked by pipeline and condensed moisture is connected, condensation film separator liquid outlet is connected with the solution regulating reservoir liquid return hole of Cooling and Heat Source tower and the frost prevention spray assembly of Cooling and Heat Source tower respectively by the pipeline that valve is housed, and constitutes the condensed water concentrated separation system thus;
Described high molecular weight hydrophilic aerosol separator is made up of housing, high molecular weight hydrophilic demist layer, flow apron, and flow apron is installed in center in the shell, and high molecular weight hydrophilic demist layer is installed in the peripheral position of flow apron, and housing is provided with air inlet;
Little different transfer of heat evaporimeter inner chamber is provided with working medium four flow process EGRs, oil return evaporation tube and medium eddy flow plate, two ends are provided with the oil return end cap, an end oil revolving end wherein is covered with inlet, the oil return evaporation tube is communicated with by pipeline with the oil return heater, the oil return heater also is communicated with by pipeline with negative pressure oil return trunnion, evaporimeter back-steam mouth is inhaled steam ports by pipeline and low heat helical-lobe compressor and is connected, little different transfer of heat evaporimeter circulatory mediator inlet is connected with first four-way change-over valve by pipeline, and the outlet of evaporimeter circulatory mediator is connected with second four-way change-over valve by pipeline;
Condensed moisture is disembarked and is comprised the condensation film separator, condensation film separator top is provided with the heat pump device, the heat pump device comprises the thermal source blower fan, thermal source blower fan and air source evaporator bank are contained in the wind chamber, air source evaporimeter venthole is connected with compressor by pipeline, compressor is connected with heats cold condenser shell side by pipeline, and the shell side liquid outlet of reheater condenser is connected with the expansion valve inlet by the pipeline that filter is housed, and the expansion valve outlet is connected with air source evaporator by pipeline; The chamber circulation solution import of heats cold condenser shell side is connected by pipeline and the condensed moisture nanometer film processor of disembarking, and the backwash filter that heats cold condenser shell side chamber delivery port is disembarked by pipeline and condensed moisture is connected; The solution force (forcing) pump that condensed moisture is disembarked is connected with the backwash filter inlet by pipeline, the backwash filter outlet is connected with the chamber circulation solution import of heats cold condenser shell side by pipeline, the outlet of heats cold condenser shell side chamber circulation solution by pipeline with go into the nanometer film processor and enter the mouth and be connected, the outlet of nanometer film processor is connected with molecular film processor inlet by pipeline, and molecular film processor middle part is provided with discharge outlet; The isolated concentrated solution mouth of molecular film processor is connected with external equipment spray demisler by pipeline.
The utility model, winter, with existing source pump relatively, in southern heat supply, the pipe laying that need not to dig a well uses boiler electric heating, can obtain to be higher than the energy-saving effect of existing water source/earth-source hot-pump system about 20%, about 10 ℃ of ambient air temperatures are equivalent to raise; Summer, compare with existing refrigeration unit, be equivalent to reduce about 8 ℃ of ambient air temperatures, improved the economic performance of refrigeration machine/heat pump, need not auxiliary thermal source, realize cold-heat air-conditioning, water-heating three alliances, a machine three-use.Solve the 200-2000KW single cooler and can't realize the technical barrier of heat pumpization, cancelled boiler.Help energy-saving and emission-reduction, the comprehensive economic performance index is higher than 25～50% of China's existing central air conditioner system in south.
The utility model is specially adapted to substitute water-loop heat pump+electric heating system, water source/earth-source hot-pump system, air source heat pump+electric heating system, the single cooler+steam generator system that uses at present.
Description of drawings
Fig. 1 is the structure complete set of equipments schematic diagram of the utility model one embodiment;
Fig. 2 is the hydrophilic aerosol cyclone separator arrangement of a Cooling and Heat Source tower height molecule embodiment illustrated in fig. 1 schematic diagram;
Fig. 3 is the little different transfer of heat evaporation structure of a low heat eddy flow heat pump embodiment illustrated in fig. 1 schematic diagram;
Fig. 4 is heat pump device embodiment illustrated in fig. 1 and the condensed moisture structural representation of disembarking.
The specific embodiment
The utility model is described in further detail below in conjunction with accompanying drawing.
With reference to Fig. 1, present embodiment comprises that Cooling and Heat Source tower 1, low heat eddy flow heat pump 2, condensed moisture disembark 3, servicing unit 4, terminal load system 5;
Cooling and Heat Source tower 1 comprises the heat exchange blower fan 1-1 that is installed on the support, heat exchange blower fan 1-1 top is provided with high molecular weight hydrophilic aerosol separator 1-5, the bottom is provided with frost prevention spray assembly 1-6, frost prevention spray assembly 1-6 bottom is provided with secondary demister 1-7, secondary demister 1-7 bottom is provided with heat exchanger 1-2, heat exchanger 1-2 bottom is provided with cool water shower device 1-8, and cool water shower device 1-8 bottom is provided with drip tray 1-3, and drip tray 1-3 bottom is provided with solution regulating reservoir 1-4;
Low heat eddy flow heat pump 2 comprises condenser 2-2, condenser 2-2 is communicated with little different transfer of heat evaporimeter 2-4, little different transfer of heat evaporimeter 2-4 links to each other with low heat helical-lobe compressor 2-1, and wideband electronic expansion valve 2-3 is communicated with condenser 2-2 shell side refrigeration working medium liquid outlet;
Condensed moisture is disembarked and 3 is comprised condensation film separator 3-1, and condensation film separator 3-1 top is provided with heat pump device 3-2;
Described servicing unit 4 comprises Cooling and Heat Source pump 4-4, the first four-way change-over valve 4-2, the second four-way change-over valve 4-3, terminal partial load pump 4-1;
The heat exchanger 1-2 outlet of Cooling and Heat Source tower 1 is connected with the Cooling and Heat Source pump 4-4 suction inlet of auxiliary equipment device 4 by pipeline, Cooling and Heat Source pump 4-4 extrudes mouth and is connected with the first four-way change-over valve 4-2, first inlet by the pipeline that filter and check-valves are housed, the first four-way change-over valve 4-2, first liquid outlet is connected with the little different transfer of heat evaporimeter 2-4 inlet of low heat eddy flow heat pump 2 by pipeline, the little different transfer of heat evaporimeter 2-4 liquid outlet of low heat eddy flow heat pump 2 is connected with the second four-way change-over valve 4-3, first inlet by pipeline, the second four-way change-over valve 4-3, first liquid outlet is connected with the heat exchanger 1-2 inlet of Cooling and Heat Source tower 1 by the pipeline that valve is housed, and constitutes the cold and hot source circulatory system thus;
Terminal load side water return pipeline 5-2 is connected with the partial load pump 4-1 suction inlet of auxiliary equipment device 4 by the pipeline that valve is housed, partial load pump 4-1 extrudes mouth and is connected with second inlet of the first four-way change-over valve 4-2 by the pipeline that filter and check-valves are housed, second liquid outlet of the first four-way change-over valve 4-2 is connected with the condenser 2-2 water inlet of low heat eddy flow heat pump 2 by pipeline, the condenser 2-2 delivery port of low heat eddy flow heat pump 2 is connected by second inlet of pipeline with the second four-way change-over valve 4-3, second liquid outlet of the second four-way change-over valve 4-3 is connected with terminal load side water supply line 5-1 by pipeline, constitutes the terminal load side circulatory system thus;
The solution regulating reservoir 1-4 liquid outlet of Cooling and Heat Source tower 1 is connected by disembark 3 condensation film separator 3-1 inlet of pipeline and condensed moisture, condensation film separator 3-1 liquid outlet is connected with the solution regulating reservoir 1-4 liquid return hole of Cooling and Heat Source tower 1 and the frost prevention spray assembly 1-8 of Cooling and Heat Source tower 1 respectively by the pipeline that valve is housed, and constitutes the condensed water concentrated separation system thus;
With reference to Fig. 2, described high molecular weight hydrophilic aerosol separator 1-5 is made up of housing 1-54, high molecular weight hydrophilic demist layer 1-51, flow apron 1-52, flow apron 1-52 is installed in center in the shell, high molecular weight hydrophilic demist layer 1-51 is installed in the peripheral position of flow apron 2-3, and housing 1-54 is provided with air inlet 1-53;
With reference to Fig. 3, little different transfer of heat evaporimeter 2-4 inner chamber is provided with working medium four flow process EGR 2-42, oil return evaporation tube 2-45 and medium eddy flow plate 2-49, two ends are provided with oil return end cap 2-44, an end oil return end cap 2-44 wherein is provided with inlet 2-41, oil return evaporation tube 2-45 is communicated with by pipeline with oil return heater 2-46, oil return heater 2-46 also is communicated with by pipeline with negative pressure oil return trunnion 2-47, evaporimeter back-steam mouth 2-43 inhales steam ports by pipeline with low heat helical-lobe compressor 2-1 and is connected, little different transfer of heat evaporimeter circulatory mediator inlet 2-48 is connected with first four-way change-over valve by pipeline, and evaporimeter circulatory mediator outlet 2-410 is connected with second four-way change-over valve by pipeline;
With reference to Fig. 4, heat pump device 3-2 comprises thermal source blower fan 3-25, thermal source blower fan 3-25 and air source evaporimeter 3-24 are assembled in the wind chamber, air source evaporimeter 3-24 venthole is connected with compressor 3-21 by pipeline, compressor 3-21 is connected with heats cold condenser 3-22 shell side by pipeline, the shell side liquid outlet of reheater condenser 3-22 is connected with expansion valve 3-23 inlet by the pipeline that filter is housed, and expansion valve 3-23 outlet is connected with the evaporimeter 3-24 import of air source by pipeline; The chamber circulation solution import of heats cold condenser 3-22 shell side is connected by pipeline and the condensed moisture 3-1 nanometer film processor 3-13 that disembarks, and heats cold condenser 3-22 shell side chamber delivery port is connected by the disembark backwash filter 3-12 of 3-1 of pipeline and condensed moisture; The disembark solution force (forcing) pump 3-11 of 3-1 of condensed moisture is connected by pipeline and backwash filter 3-12 inlet, backwash filter 3-12 outlet is connected with the chamber circulation solution import of heats cold condenser 3-22 shell side by pipeline, the outlet of heats cold condenser 3-22 shell side chamber circulation solution by pipeline with go into nanometer film processor 3-13 and enter the mouth and be connected, nanometer film processor 3-13 outlet is connected with molecular film processor 3-14 inlet by pipeline, and molecular film processor 3-14 middle part is provided with discharge outlet; The isolated concentrated solution mouth of molecular film processor 3-14 is connected with external equipment spray demisler by pipeline.
The system works principle:
1) cold and hot source circulatory system heat supply operation principle: the heat exchange blower fan 1-1 bumpy weather air that starts Cooling and Heat Source tower 1, the heat exchanger 1-2 fin of Cooling and Heat Source tower 1 absorbs from airborne low-temperature heat energy passes to circulatory mediator in the finned tube, circulatory mediator in the heat exchanger 1-2 absorbs from behind the airborne low-temperature heat energy, medium temperature raises, enthalpy increases, enter Cooling and Heat Source pump 4-4 suction inlet by heat exchanger 1-2 outlet by pipeline again, behind Cooling and Heat Source pump 4-4 adherence pressure, extrude mouth and enter the first four-way change-over valve 4-2 by the pipeline that filter and check-valves are housed by it, finish high enthalpy circulatory mediator commutation, enter the little different transfer of heat evaporimeter 2-4 of low heat eddy flow heat pump 2 again by pipeline from the first four-way change-over valve 4-2 liquid outlet, high enthalpy circulatory mediator forms the eddy flow heat exchange in the shell side rotational flow generator of little different transfer of heat evaporimeter 2-4, low-temperature heat energy is passed in the tube side of little different transfer of heat evaporimeter 2-4 after the cold working medium of control, temperature reduces, enthalpy descends, enter the second four-way change-over valve 4-3 by little different transfer of heat evaporimeter 2-4 liquid outlet by pipeline, after finishing low enthalpy circulatory mediator commutation, enter the heat exchanger 1-2 of Cooling and Heat Source tower 1 by pipeline from the second four-way change-over valve 4-3 liquid outlet, low enthalpy circulatory mediator absorbs from airborne low-temperature heat energy at heat exchanger 1-2, finishes the circuit cycle process;
2) terminal load side circulatory system heat supply operation principle: provide hot water by terminal load side water supply line 5-1 terminad load, hot water temperature after air conditioner 5-2 discharges heat energy descends, become low enthalpy hot water, low enthalpy hot water enters partial load pump 4-1 by water return pipeline 5-3 by pipeline, behind partial load pump 4-1 adherence pressure by enter the first four-way change-over valve 4-2, second inlet by the pipeline that filter and check-valves are housed, finish low enthalpy hot water commutation, enter the condenser 2-2 of low heat eddy flow heat pump 2 by pipeline through the first four-way change-over valve 4-2, second liquid outlet, discharge heat of high temperature by condenser 2-2 shell side cold-producing medium, low enthalpy hot water temperature raises, become high enthalpy hot water, high enthalpy hot water enters the second four-way change-over valve 4-3 through condenser 2-2 delivery port by pipeline, finish high enthalpy hot water commutation, enter terminal load side water supply 5-1 pipeline terminad load through the second four-way change-over valve 4-3 liquid outlet by pipeline again hot water is provided, finish cyclic process.
3) condensed water concentrated separation system operation principle: when ambient air temperature is lower than zero degree, when Cooling and Heat Source tower 1 hangs down potential temperature latent heat source in the absorbing environmental air, the meeting frosting of little different transfer of heat evaporimeter 2-4 surface, when frosting thickness reaches certain value, can influence the heat exchange effect, need to adopt the spray frost-proof solution to reduce little different transfer of heat evaporimeter 2-4 surface freezing point.Disembark when condensed moisture and 3 to detect ambient air temperature and be lower than zero degree, automatically close Cooling and Heat Source tower 1, drip tray 1-3 condensed water draining valve starts condensed moisture and disembarks, the dilution frost-proof solution enters disembark 3 condensation film separator 3-1 of condensed moisture by solution regulating reservoir 1-4 liquid outlet, the dilution frost-proof solution enters condensation film separator 3-1 after heater 3-2 heating, the condensed water of separating is discharged through condensed moisture 3 delivery ports of disembarking; The dense frost-proof solution of separating enters the spraying frost prevention assembly 1-8 of Cooling and Heat Source tower 1 through pipeline, to the spraying of the heat exchanger 1-2 of Cooling and Heat Source tower 1 fin, reduces the fin surface freezing point, reaches the purpose of frost prevention operation; The heat exchanger 1-2 fin of Cooling and Heat Source tower 1 absorbs the condensate water of airborne latent heat generation and mixes the formation dilute solution with frost-proof solution, the drip tray 1-3 that dilute solution enters Cooling and Heat Source tower 1 discharges the solution regulating reservoir 1-4 that enters Cooling and Heat Source tower 1 by tapping valve, constitutes looped cycle.
The high molecular weight hydrophilic aerosol separator 1-5 operation principle of Cooling and Heat Source tower 1: Cooling and Heat Source tower 1 for preventing the negative temperature frosting, needs the intermittent shower frost-proof solution carrying out in the heat exchanging process with surrounding air, stops the drift of mist vapour with the high molecular weight hydrophilic demister.Mist vapour swirling eddy in Cooling and Heat Source tower 1 is entered by high molecular weight hydrophilic aerosol separator 1-5 air inlet 1-53, when mist vapour swirling eddy passes high molecular weight hydrophilic demist layer 1-51 inner chamber, water conservancy diversion plate washer 1-52 makes air-flow be partial to the high molecular weight hydrophilic demist layer 1-51 of centrifugal side, high molecular weight hydrophilic demist layer 1-51 removes mist elimination vapour, gas penetrates through air outlet 5.4, finishes the heat exchange circulation with surrounding air.
The little different transfer of heat evaporimeter 2-4 operation principle of low heat eddy flow heat pump 2: from two kinds of fluids of vapour-liquid of throttle expansion valve 2-3, enter the working medium four flow path device 2-42 circulatory systems through little different transfer of heat evaporimeter 2-4 inlet 2-41, when evaporating temperature is lower than 0 ℃, lubricating oil lubricating oil separation occurs in the working medium four flow path device 2-42 circulatory systems, oil mixture is by oil return end cap 2-44, suck oil return evaporation tube 2-45 by negative-pressure pipeline, oil return evaporation tube 2-45 continues the refrigeration working medium of evaporation of residual in lubricating oil, lubricating oil enters oil return heater 2-46 oil-in A by pipeline, oil return heater 2-46 promotes lubricating oil temperature, the lubricating oil viscosity descends, again through oil return heater 2-46 oil drain out B and pipeline, negative pressure trunnion 2-47 sucks low heat heat pump compressor 2-1, finishes the oil return process.
The heat pump device 3-2 course of work: condensed moisture is disembarked and is detected ambient air temperature and be lower than zero degree, automatically start the heat pump device, thermal source blower fan 3-25 disturbance air circulation, airborne low-temperature heat energy is passed to air source evaporimeter 3-24, cold-producing medium in the finned tube of air source evaporimeter 3-24 absorbs airborne low-temperature heat energy and is evaporated to the saturated gas of low pressure, enter compressor 3-21 by air source evaporimeter 3-24 venthole and pipeline, it is high pressure-temperature gas that the saturated gas of low pressure is promoted by compressor compresses, enter in the heats cold condenser 3-22 shell side chamber by pipeline via compressor 3-21 exhaust outlet, high pressure-temperature gas release heat in heats cold condenser 3-22 shell side chamber is given tube side circulatory mediator (solution heat process), be condensed into the high-pressure refrigerant saturated liquid, enter expansion valve 3-23 from the shell side liquid outlet discharge of heats cold condenser 3-22 by the filter on the pipeline, after finishing the throttling expansion process, enter air source evaporimeter 3-24 by pipeline and absorb airborne low-temperature heat energy.
The condensation film separator 3-1 course of work: condensed moisture is disembarked and is detected ambient air temperature and be lower than zero degree, automatically close the drip tray 1-3 condensed water draining valve of Cooling and Heat Source tower 1, starting condensed moisture disembarks, the dilution frost-proof solution enters the condensed moisture condensation film separator 3-1 solution force (forcing) pump 3-11 that disembarks by solution regulating reservoir 1-4 liquid outlet, through solution force (forcing) pump 3-11 pressurization back by after extruding mouth and entering backwash filter 3-12 by pipeline and filter out impurity, enter heats cold condenser 3-22 tube side by pipeline and heats cold condenser 3-22 tube side end, heated solution enters nanometer film processor 3-13 from heats cold condenser 3-22 tube side end by pipeline, enter molecular film processor 3-14 after removing fine impurity, handle by molecular film processor 3-14, isolated condensed water (water in air branch) outwards discharges by pipeline through the discharge outlet at molecular film processor 3-14 middle part; The isolated concentrated solution of molecular film processor 3-14 enters external equipment spray demisler by its bottom liquid outlet by pipeline.
Claims (1)
1. the solar energy secondary heat-source tower heat pump complete set of equipments is characterized in that, it comprises, and Cooling and Heat Source tower, low heat eddy flow heat pump, condensed moisture are disembarked, servicing unit, terminal load system;
Described Cooling and Heat Source tower comprises the heat exchange blower fan that is installed on the support, heat exchange blower fan top is provided with high molecular weight hydrophilic aerosol separator, the bottom is provided with frost prevention spray assembly, frost prevention spray assembly bottom is provided with the secondary demister, secondary demister bottom is provided with heat exchanger, the heat exchanger bottom is provided with the cool water shower device, and cool water shower device bottom is provided with drip tray, and the drip tray bottom is provided with the solution regulating reservoir;
Described low heat eddy flow heat pump comprises condenser, condenser is communicated with little different transfer of heat evaporimeter, little different transfer of heat evaporimeter links to each other with the low heat helical-lobe compressor, wideband electronic expansion valve inlet is connected with the condenser liquid outlet with filter by pipeline, and wideband electronic expansion valve liquid outlet is communicated with little different transfer of heat evaporimeter refrigeration working medium inlet by pipeline;
Described servicing unit comprises Cooling and Heat Source pump, first four-way change-over valve, second four-way change-over valve, terminal partial load pump;
Described terminal load system comprises terminal load side water supply line, terminal load side water return pipeline, end heat exchanger;
The heat exchanger exit of Cooling and Heat Source tower is connected with the Cooling and Heat Source Pump Suction Nozzle of auxiliary equipment device by pipeline, the outlet of Cooling and Heat Source pump pressure is connected with first four-way change-over valve, first inlet by the pipeline that filter and check-valves are housed, first four-way change-over valve, first liquid outlet is connected with the little different transfer of heat evaporimeter inlet of low heat eddy flow heat pump by pipeline, the little different transfer of heat evaporimeter liquid outlet of low heat eddy flow heat pump is connected with second four-way change-over valve, first inlet by pipeline, second four-way change-over valve, first liquid outlet is connected with the heat exchanger inlet of Cooling and Heat Source tower by the pipeline that valve is housed, and constitutes the cold and hot source circulatory system thus;
Terminal load side water return pipeline is connected with the partial load pump suction inlet of auxiliary equipment device by the pipeline that valve is housed, partial load pump extrudes mouth and is connected with second inlet of first four-way change-over valve by the pipeline that filter and check-valves are housed, second liquid outlet of first four-way change-over valve is connected by the condenser water inlet of pipeline with low heat eddy flow heat pump, the condenser delivery port of low heat eddy flow heat pump is connected with second inlet of second four-way change-over valve by pipeline, second liquid outlet of second four-way change-over valve is connected with terminal load side water supply line by pipeline, constitutes the terminal load side circulatory system thus;
The condensation film separator inlet that the solution regulating reservoir liquid outlet of Cooling and Heat Source tower is disembarked by pipeline and condensed moisture is connected, condensation film separator liquid outlet is connected with the solution regulating reservoir liquid return hole of Cooling and Heat Source tower and the frost prevention spray assembly of Cooling and Heat Source tower respectively by the pipeline that valve is housed, and constitutes the condensed water concentrated separation system thus;
Described high molecular weight hydrophilic aerosol separator is made up of housing, high molecular weight hydrophilic demist layer, flow apron, and flow apron is installed in center in the shell, and high molecular weight hydrophilic demist layer is installed in the peripheral position of flow apron, and housing is provided with air inlet;
Little different transfer of heat evaporimeter inner chamber is provided with working medium four flow process EGRs, oil return evaporation tube and medium eddy flow plate, two ends are provided with the oil return end cap, wherein an end oil revolving end is covered with inlet, the oil return evaporation tube is communicated with by pipeline with the oil return heater, the oil return heater also is communicated with by pipeline with negative pressure oil return trunnion, evaporimeter back-steam mouth is inhaled steam ports by pipeline and low heat helical-lobe compressor and is connected, little different transfer of heat evaporimeter circulatory mediator inlet is connected with first four-way change-over valve by pipeline, and the outlet of evaporimeter circulatory mediator is connected with second four-way change-over valve by pipeline;
Condensed moisture is disembarked and is comprised the condensation film separator, condensation film separator top is provided with the heat pump device, the heat pump device comprises the thermal source blower fan, thermal source blower fan and air source evaporator bank are contained in the wind chamber, air source evaporimeter venthole is connected with compressor by pipeline, compressor is connected with heats cold condenser shell side by pipeline, and the shell side liquid outlet of reheater condenser is connected with the expansion valve inlet by the pipeline that filter is housed, and the expansion valve outlet is connected with air source evaporator by pipeline; The chamber circulation solution import of heats cold condenser shell side is connected by pipeline and the condensed moisture nanometer film processor of disembarking, and the backwash filter that heats cold condenser shell side chamber delivery port is disembarked by pipeline and condensed moisture is connected; The solution force (forcing) pump that condensed moisture is disembarked is connected with the backwash filter inlet by pipeline, the backwash filter outlet is connected with the chamber circulation solution import of heats cold condenser shell side by pipeline, the outlet of heats cold condenser shell side chamber circulation solution by pipeline with go into the nanometer film processor and enter the mouth and be connected, the outlet of nanometer film processor is connected with molecular film processor inlet by pipeline, and molecular film processor middle part is provided with discharge outlet; The isolated concentrated solution mouth of molecular film processor is connected with external equipment spray demisler by pipeline.
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| Application Number | Priority Date | Filing Date | Title |
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| CN2009203123012U CN201535595U (en) | 2009-10-12 | 2009-10-12 | Solar secondary source, heat source tower and heat pump complete plant |
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| Application Number | Priority Date | Filing Date | Title |
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| CN2009203123012U CN201535595U (en) | 2009-10-12 | 2009-10-12 | Solar secondary source, heat source tower and heat pump complete plant |
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| CN201535595U true CN201535595U (en) | 2010-07-28 |
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Cited By (2)
| 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 |
| WO2016146084A1 (en) * | 2015-03-17 | 2016-09-22 | 黄国和 | All-weather solar energy water source heat pump air conditioning system |
-
2009
- 2009-10-12 CN CN2009203123012U patent/CN201535595U/en not_active Expired - Lifetime
Cited By (3)
| 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 |
| WO2016146084A1 (en) * | 2015-03-17 | 2016-09-22 | 黄国和 | All-weather solar energy water source heat pump air conditioning system |
| US10436482B2 (en) | 2015-03-17 | 2019-10-08 | Hunan Dongyou Water Vapor Energy Energy-Saving CO., Ltd | All-weather solar water source heat pump air conditioning system |
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| C14 | Grant of patent or utility model | ||
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| AV01 | Patent right actively abandoned |
Granted publication date: 20100728 Effective date of abandoning: 20091012 |