CN109028652A - Greenhouse heat source heat pump paddy electricity accumulation of heat block energy source station - Google Patents

Abstract

A kind of greenhouse heat source heat pump paddy electricity accumulation of heat block energy source station, it is big using building heat supplying demand under paddy electricity accumulation of heat compensation ultra-low temperature surroundings that it mainly solves existing cold snap, pump the technical problems such as the problem of heating load deficiency, regenerate clean energy resource block chain powered mode, greenhouse heat source heat pump paddy electricity accumulation of heat block energy source station is the balanced adjustment of cogeneration of heat and power greenhouse gases and greenhouse waste heat effect on environment, cold-heat air-conditioning, water-heating trilogy supply can be achieved by switching in system, take into account paddy electricity accumulation of heat/cool storage function, economically scale application energy block chain technology allows the supply of distributing renewable energy to be possibly realized, haze is driven absorbing to promote greenhouse heat source while drawing peak to Atmospheric Transportation low temperature cold air-flow, realize that artificial cold source controls the economic and social benefit of haze.

Description

Greenhouse heat source heat pump paddy electricity accumulation of heat block energy source station

Technical field

A kind of greenhouse heat source heat pump paddy electricity accumulation of heat block energy source station that type of the present invention is related to, is related to China's new energy source energy-saving Technology, environmental protection and the big field of resource two.

Background technique

Greenhouse effects are made of greenhouse gases and greenhouse heat source, are being commonly called as atmosphere heat preservation effect.Suitable greenhouse effects Solar shortwave radiation can be made to reach ground, a large amount of long wave heat radiations released outward after earth's surface is heated are prevented outside by Atmospheric Absorption Space diffusion makes surface temperature be in heat preservation equilibrium state.Since the industrial revolution, thermoelectricity co-generating heat supplying, automobile power tail gas, The strong greenhouse gases of the heat absorptivities such as carbon dioxide and waste gas residual heat that industrial and agricultural production is discharged into atmosphere and greenhouse heat source are broken Global greenhouse effect balance, earth surface temperature increase global warming year by year and destroy stable atmospheric circulation, weather calamity It is difficult frequent.Therefore human needs' one kind absorbs greenhouse heat supply reduction carbon emission greenhouse gases and temperature with large-scale artificial cold source Room heat supply is the artificial control measures for preventing global warming.Conventional small coal changes electric air source heat pump equipment at present Capacity is small, the simple low-intensity of compressor design is easy to damage, it is serious to absorb the clammy heat source frosting of greenhouse haze, it is difficult to form scale Change, can not rough atmosphere inversion layer circulation realize that cold front drives haze, while outdoor heat pump unit noise is big, serious heat loss.

Summary of the invention

The present invention provides a kind of greenhouse heat source heat pump paddy electricity accumulation of heat block energy source station, technical solution: it includes including greenhouse Heat source closed loop heat source absorption system 1, the economic heat pump lifting device 2 of multi-way adverse current and block efficiency heat supply open and store closed-loop system 3, institute Stating block efficiency heat supply and opening storage closed-loop system 3 and constitute includes lotus side circulating pump 3100, block efficiency heating demand side 3200, lotus side Steady of system press device 3300 softens water supply tank 3400, level pressure expansion drum 3500, releases the dress that can exchange heat without pressure heat storage tank 3600, bilateral 3700 and paddy electricity heating device 3800 are set, lotus side circulating pump 3100 is connect with the economic heat pump lifting device 2 of multi-way adverse current, area Block efficiency heating demand side 3200 is connect with heating diversion three-way 300x, heating confluence threeway 300y respectively by pipeline, and led to Piping is connect through water-supply and pressure-stabling threeway 300z with lotus side circulating pump 3100, and the outlet 3320 of lotus side system constant pressure arrangement 3300 is logical Piping threeway is connect with level pressure expansion drum 3500, water-supply and pressure-stabling threeway 300z respectively, lotus side system constant pressure arrangement 3300 into Mouth 3310 is connect by pipeline with the outlet 3420 for softening water supply tank 3400；Without pressure heat storage tank 3600 and paddy electricity heating device 3800 Connection, paddy electricity heating device 3800 and bilateral release can heat-exchanger rig 3700 connect, bilateral release energy heat-exchanger rig 3700 respectively with add Threeway 300x, heating confluence threeway 300y, greenhouse heat source closed loop heat source absorption system 1 is thermally shunted to connect.

The import 3110 of lotus side circulating pump 3100 is by pipeline through water-supply and pressure-stabling threeway 300z and the heat supply of block efficiency The outlet 3220 of load side 3200 connects；The import 3210 of block efficiency heating demand side 3200 passes through pipeline and heating confluence three Logical 300y, paddy electricity are released can flow divider 3130, heating diversion three-way 300x connection；The import 3310 of lotus side system constant pressure arrangement 3300 It is connect by pipeline with the outlet 3420 of softening water supply tank 3400；The outlet 3320 of lotus side system constant pressure arrangement 3300 passes through pipeline Threeway is connect with level pressure expansion drum 3500, water-supply and pressure-stabling threeway 300z respectively；Lotus side pressure relief safety valve 3330 is connected across lotus side-line System 3300 both ends of constant pressure arrangement；Soften 3400 top of water supply tank and access hole is housed equipped with soft water import barrier device 3410, top 3430, bottom is equipped with sewage draining exit 3440；Outlet 3610 without pressure heat storage tank 3600 passes through pipeline and heating/heat release circulating pump 3810 Import 3811 connect；Import 3620 without pressure heat storage tank 3600 is filled by pipeline through heat release confluence threeway 380a and paddy electricity heating Set 3800 straight-through 3840 connections of accumulation of heat outlet；Without pressing floating ball water inlet 3630, floating ball access hole are housed at the top of heat storage tank 3600 3631 and level sensing temperature control device 3611；Domestic hot-water's interface 3640 and domestic hot-water's automatic control mix water circle device 3650 and connect It connects；3800 heat release of paddy electricity heating device outlet 3830 is released by pipeline and bilateral can 3700 heat release import 3750 of heat-exchanger rig company It connects；Bilateral is released energy 3700 heat release of heat-exchanger rig outlet 3760 and is connect by pipeline with heat release confluence threeway 380a；Paddy electricity heating dress 3800 inside are set equipped with primary Ioops electric calorifie installation 3801 and secondary circuit electric calorifie installation 3802；Bilateral releases energy heat-exchanger rig 3700 again 3701 import 3730 of heating coil is connect by pipeline with heating diversion three-way 300x；Bilateral is released can the reheating of heat-exchanger rig 3700 The outlet of coil pipe 3,701 3740 is connect by pipeline with heating confluence threeway 300y；Bilateral is released can 3700 defrosting heating dish of heat-exchanger rig 3702 import 3710 of pipe is connect by pipeline with cold liquid return tee joint 114y；Bilateral is released can 3700 defrosting heating coil of heat-exchanger rig 3702 outlets 3720 are connect by pipeline with hot 3770 import 3771 of defrosting circulating pump；The hot outlet of defrosting circulating pump 3,770 3772 A mouthful threeway 114x is circulated with heat by pipeline to connect.

The greenhouse heat source closed loop heat source absorption system 1 includes that haze absorption in greenhouse takes thermal 1100, chilling spray to follow Ring pump 1200, source solution circulation pump 1300, source side system constant pressure arrangement 1400, solution blend expansion tank 1500, source side system Level pressure expansion drum 1600 and source countercurrent heat-transfer commutation station 1700, the greenhouse haze absorption take thermal 1100 to pass through pipeline Mouthful threeway 114x is circulated through heat to connect with the pump discharge Mixed liquid T-branch 130y of source solution circulation pump 1300, and passes through pipeline point Not with the import of cold liquid return tee joint 114y, the interface 1740, chilling spray circulating pump 1200 of source adverse current commutation station 1700 1210 connections；The outlet 1510 of expansion tank 1500 is blent in the import 1410 of source side system constant pressure arrangement 1400 by pipeline and solution Connection；The outlet 1420 of source side system constant pressure arrangement 1400 passes through pipeline and source side system level pressure expansion drum 1600, low side respectively Mixed liquid T-branch 130x connection.

It includes steel construction overlapping frame maintenance 1110, bilateral guiding air intake grid that haze absorption in greenhouse, which takes thermal 1100, 1120, bilateral dust refractor 1130, double sided cathodes anti-corrosion finned tube 1140, bilateral water mist absorber 1150, variable air rate circulation Device 1160, double-sided cooled sprayer-washer 1170 and bilateral receive water water storage tank 1180, the steel construction overlapping frame maintenance 1110 interior bottom portion truss installa-tions have bilateral to receive water water storage tank 1180；Bilateral receives the bidirectional arrangements in order above of water water storage tank 1180 Bilateral guiding air intake grid 1120, bilateral dust refractor 1130, double sided cathodes anti-corrosion finned tube 1140, bilateral water mist are installed to inhale Device 1150 is received, intermediate position is fixed by 1110 inside middle part truss of steel construction overlapping frame maintenance；Variable air rate circulator 1160 It is installed on steel construction overlapping frame 1110 inside top central truss of maintenance and atmosphere；Double-sided cooled sprayer-washer 1170 bidirectional arrangements be installed on steel construction overlapping frame safeguard 1110 placed on top two sides, below equipment be bilateral dust refractor 1130, double sided cathodes anti-corrosion finned tube 1140, bilateral water mist absorber 1150.

The inlet tube 1141 of double sided cathodes anti-corrosion finned tube 1140 circulates mouthful threeway 114x through heat by pipeline and source is molten The pump discharge Mixed liquid T-branch 130y connection of liquid circulating pump 1300；The outlet tube 1142 of double sided cathodes anti-corrosion finned tube 1140 passes through pipe Road is connect with the interface 1740 of cold liquid return tee joint 114y, source adverse current commutation station 1700 respectively；Bilateral receives water water storage tank 1180 Water outlet 1183 connect with the import 1210 of chilling spray circulating pump 1200 by pipeline；Chilling spray circulating pump 1200 goes out Mouth 1220 is connect by pipeline with the import 1171 of double-sided cooled sprayer-washer 1170；Heat circulates a mouthful threeway 114x and passes through pipeline The outlet 3772 for opening hot defrosting circulating pump 3770 in storage closed-loop system 3 with the efficiency heat supply of lotus side is connect；Cold liquid return tee joint 114y It is connect by pipeline with the import 3710 that hot defrosting heating coil 3702 in storage closed-loop system 3 is opened in the efficiency heat supply of lotus side；Source is molten The import 1310 of liquid circulating pump 1300 connecing through low side Mixed liquid T-branch 130x and source countercurrent heat-transfer commutation station 1700 by pipeline Mouth 1730 connects；The outlet 1320 of source solution circulation pump 1300 circulates mouth three through high-end Mixed liquid T-branch 130y, heat by pipeline Logical 114x is connect with the inlet tube 1141 of double sided cathodes anti-corrosion finned tube 1140；The import 1410 of source side system constant pressure arrangement 1400 It is connect by pipeline with the outlet 1510 that solution blends expansion tank 1500；Distinguish the outlet 1420 of source side system constant pressure arrangement 1400 It is connect by pipeline with source side system level pressure expansion drum 1600, low side Mixed liquid T-branch 130x；Source expansion relief valve 1430 bridges In 1400 both ends of source side system constant pressure arrangement；Solution blends expansion tank 1500 and is disposed with soft water import 1520, blends liquid return hole 1530, liquid feeding cover board 1540, bottom position sewage draining exit 1550；Liquid return hole 1530 is blent to connect by pipeline and high-end Mixed liquid T-branch 130y It connects；The interface 1710 of source countercurrent heat-transfer commutation station 1700 is connect by pipeline with the economic heat pump lifting device 2 of multi-way adverse current.

It includes low heat oil cold compressor 2100, multi-order refractive silk that the economic heat pump lifting device 2 of the multi-way adverse current, which is constituted, Net oil device 2200, liquid leaching commutation evaporator/condensers 2300, middle pressure synergy economizer 2400, vacuole absorb economizer 2500, liquid Control throttling set 2600 and multipaths commutation condensation/vaporization device 2700,2100 air entry 2110 of low heat oil cold compressor It soaks commutation 2300 outlet valve 2317 of evaporator/condensers with liquid to connect, 2100 exhaust outlet 2120 of low heat oil cold compressor passes through pipe Road is connect with 2200 air inlet 2210 of multi-order refractive silk screen oil eliminator, and 2200 gas outlet 2220 of multi-order refractive silk screen oil device is logical It crosses pipeline to connect with liquid leaching commutation evaporator/condensers 2300, multipaths commutation condensation/vaporization device 2700 respectively, low heat oil is cold Compressor 2100 is connect by pipeline with middle pressure synergy economizer 2400, and liquid leaching commutation evaporator/condensers 2300 are passed through by pipeline Low pressure liquid stream threeway 273x is connect with multipass flow commutation condensation/vaporization device 2700, and liquid leaching commutation evaporator/condensers 2300 pass through pipe Road is connect through vacuole oil return threeway 273w with multipaths commutation condensation/vaporization device 2700, and liquid leaching commutation evaporator/condensers 2300 are logical Cross pipeline and connect through high pressure liquid stream threeway 273z with middle pressure synergy economizer 2400, vacuole absorb economizer 2500 by pipeline with Hydraulic-control throttling device 2600 connects.

The air entry 2110 of the low heat oil cold compressor 2100 is by pipeline through oil oil return threeway 210n, return-air rainbow It inhales threeway 210v, airflow-reversing threeway 210x and is connect with the outlet valve 2317 that liquid soaks commutation evaporator/condensers 2300；Low heat oil The exhaust outlet 2120 of cold compressor 2100 is connect by pipeline with the air inlet 2210 of multi-order refractive silk screen oil eliminator 2200；It is more Soak the interface of commutation evaporator/condensers 2300 with liquid respectively by pipeline in the gas outlet 2220 of grade refraction silk screen oil device 2200 2320, the interface 2711 of multipaths commutation condensation/vaporization device 2700 connects；The throttling of 2200 oil discharge outlet of multi-order refractive silk screen oil device Valve group 2230 is connect by pipeline with oil oil return threeway 210n；The 2100 cold import 2140 of oil of low heat oil cold compressor passes through pipe Road is connect with the oil outlet 2161 of oil cooler 2160；Low heat oil cold compressor 2100 oil it is cold outlet 2150 by pipeline with The oil inlet 2162 of oil cooler 2160 connects；Oil cooler 2160 is connected to cooling water inlet 2163 and cooling water outlet respectively 2164；The gas returning port 2420 that the increasing enthalpy mouth 2130 of low heat oil cold compressor 2100 passes through pipeline and middle pressure synergy economizer 2400 Connection；The interface 2311 of liquid leaching commutation evaporator/condensers 2300 is commutated by pipeline through low pressure liquid stream threeway 273x and multipass flow The interface 2719 of condensation/vaporization device 2700 connects；Liquid leaching commutation 2300 micropore vacuole oil return apparatus 2318 of evaporator/condensers passes through Pipeline is connect through vacuole oil return threeway 273w with multipaths commutation 2700 micropore vacuole oil return apparatus 2718 of condensation/vaporization device；Liquid Leaching commutation 2300 interface 2319 of evaporator/condensers is connect by pipeline through high pressure liquid stream threeway 273z and middle pressure synergy economizer 2400 Mouth 2440 connects；Multipaths commutation 2700 interface 2717 of condensation/vaporization device is connect by pipeline with high pressure liquid stream threeway 273z；In The pressure supercooling expansion valve group import 2410 of synergy economizer 2400 is connect by pipeline with high pressure liquid stream threeway 273y；Vacuole absorbs warp Ji 2500 interface 2540 of device is connect by pipeline with high pressure liquid stream threeway 273y；Vacuole absorbs 2500 interface 2530 of economizer and passes through Pipeline is connect with 2600 import 2610 of hydraulic-control throttling device；The outlet of hydraulic-control throttling device 2,600 2620 passes through pipeline and low pressure liquid stream Threeway 273x connection；Heating evaporation fluid level controller 2640 is installed in the middle part of liquid leaching commutation 2300 outer housing of evaporator/condensers；System Cold evaporation fluid level controller 2630 is installed in the middle part of multipaths commutation 2700 outer housing of condensation/vaporization device；Vacuole absorbs economizer 2500 interfaces 2510 are connect by pipeline with vacuole oil return threeway 273w；Vacuole absorbs 2500 interface 2520 of economizer and passes through pipeline It is connect with return-air siphon threeway 210v；Liquid leaching commutation 2300 interface 2322 of evaporator/condensers passes through pipeline and source countercurrent heat-transfer The connection of 1700 interface 1710 of commutation station；Liquid leaching commutation 2300 interface 2321 of evaporator/condensers passes through pipeline and source countercurrent heat-transfer The connection of 1700 interface 1720 of commutation station；1700 interface 1710 of source countercurrent heat-transfer commutation station by pipeline and liquid leaching commutation evaporation/ The connection of 2300 interface 2322 of condenser；1700 interface 1720 of source countercurrent heat-transfer commutation station by pipeline and liquid leaching commutation evaporation/ The connection of 2300 interface 2321 of condenser；Multipaths commutation 2700 interface 2722 of condensation/vaporization device shunts three by the way that pipeline is heated Logical 300x releases energy flow divider 3130 with paddy electricity and connect；Multipaths commutation 2700 interface 2721 of condensation/vaporization device passes through pipeline and lotus 3120 connection of the outlet of side circulating pump 3100.

Liquid leaching commutation 2300 enclosure interior of evaporator/condensers is respectively disposed with lower homogenizing plate 2312 from the bottom to top, impregnates and erect Row's evaporation tube bundle 2313, vacuole absorb tube bundle 2314, aerosol absorbs frost prevention tube bundle 2315, upper homogenizing plate 2316.

Multipaths commutation 2700 enclosure interior of condensation/vaporization device be from top to bottom respectively disposed with flow distribution plate 2712, Superheated steam level-one heat absorption tube bundle 2713, opens wing vertical setting of types condenser pipe 2715, lower flow distribution plate at steam second level heat absorption tube bundle 2714 2716。

The beneficial effects of the present invention are:

Type greenhouse heat source heat pump paddy electricity accumulation of heat block energy source station purpose of the present invention, is economically scale application energy park Block chain technology allows the supply of distributing renewable energy to be possibly realized, and promotes greenhouse heat source simultaneously to Atmospheric Transportation low temperature cold absorbing Air-flow draws peak and drives haze, realizes that artificial cold source controls the economic and social benefit of haze.

The cold snap problem big using building heat supplying demand under paddy electricity accumulation of heat compensation ultra-low temperature surroundings, as a new generation Regenerate clean energy resource block chain powered mode, greenhouse heat source heat pump paddy electricity accumulation of heat block energy source station be cogeneration of heat and power greenhouse gases and The balanced adjustment of greenhouse waste heat effect on environment, it has following four main feature:

1. it is directly facing the demand of zone user, is arranged in use as the cold and hot energy supply center for serving different zones Near family, the system that can simplify provides the conveying process of user's energy, and then reduces the energy damage of conduits of energy transmission process It loses and conveys cost, while increasing the safety of user's energy supply, greenhouse haze is absorbed using greenhouse heat pump system and is purified Regional environment air quality.

2. since it does not use the mode of extensive, remote output channel energy, and mainly for regional area user Energy requirement, the scale of system is customized by zone user demand, using greenhouse heat pump+paddy electricity accumulation of heat (cold-storage) heat supply (cooling supply) be for traditional centralized energy supplying system at present relatively in, low capacity it is economical.

3. especially the positive of greenhouse haze heat pump renewable energy and paddy electricity accumulation of energy pushes away with the development of economy, technology Wide application realizes that the energy requirement economy of zone user is high, and greenhouse heat pump paddy electricity accumulation of heat distributed energy resource system is as a kind of Open energy resource system starts that growth trend is presented, meets the energy requirement of zone user.

4. the idea of people is constantly changing, new requirement (efficiently, reliable, economy, ring are constantly proposed to energy resource system Guarantor, sustainable development etc.), greenhouse heat pump paddy electricity accumulation of heat distributed energy resource system is by selecting suitable period energy mix skill Art, the integration of optimization and paddy electricity accumulation of heat by absorbing haze clammy heat source in greenhouse to ultra-low temperature surroundings multipaths are realized different The energy generates efficiently functional objective in the different economy periods.

Detailed description of the invention

Fig. 1 is greenhouse heat source heat pump paddy electricity accumulation of heat block energy source station systematic schematic diagram of the present invention；

Fig. 2 is 1 schematic diagram of greenhouse heat source closed loop heat source absorption system；

Fig. 3 is economic 2 schematic diagram of heat pump lifting device of multi-way adverse current；

Fig. 4 is that storage 3 schematic diagram of closed-loop system is opened in the heat supply of block efficiency.

Illustrate: hollow arrow indicates air-flow direction in figure, and filled arrows indicate circulatory mediator, water circulation flowing side To.

Specific embodiment

The present invention is described in further details with reference to the accompanying drawings and examples.

Referring to attached drawing, paddy electricity accumulation of heat block energy source station of the present invention includes that greenhouse heat source closed loop heat source absorption system 1, multi-way are inverse It flows through Ji heat pump lifting device 2 and block efficiency heat supply opens and stores closed-loop system 3.

The greenhouse heat source closed loop heat source absorption system 1 includes that haze absorption in greenhouse takes thermal 1100, chilling spray to follow Ring pump 1200, source solution circulation pump 1300, source side system constant pressure arrangement 1400, solution blend expansion tank 1500, source side system Level pressure expansion drum 1600 and source countercurrent heat-transfer commutation station 1700.

It includes steel construction overlapping frame maintenance 1110, bilateral guiding air intake grid that the haze absorption, which takes thermal 1100, 1120, bilateral dust refractor 1130, double sided cathodes anti-corrosion finned tube 1140, bilateral water mist absorber 1150, variable air rate circulation Device 1160, double-sided cooled sprayer-washer 1170 and bilateral receive water water storage tank 1180.

The steel construction overlapping frame safeguards that 1110 interior bottom portion truss installa-tions have bilateral to receive water water storage tank 1180；Bilateral is received Bidirectional arrangements are equipped with bilateral guiding air intake grid 1120, bilateral dust refractor 1130, double to water water storage tank 1180 in order above Side cathodic protection finned tube 1140, bilateral water mist absorber 1150, intermediate position are safeguarded inside 1110 by steel construction overlapping frame Middle part truss is fixed；Variable air rate circulator 1160 be installed on steel construction overlapping frame safeguard 1110 inside top central truss it Upper and atmosphere；1170 bidirectional arrangements of double-sided cooled sprayer-washer are installed on 1110 top of steel construction overlapping frame maintenance Face two sides, below equipment be bilateral dust refractor 1130, double sided cathodes anti-corrosion finned tube 1140, bilateral water mist absorber 1150；1140 inlet tube 1141 of double sided cathodes anti-corrosion finned tube circulates mouthful threeway 114x through heat by pipeline and pump discharge mixes liquid three Logical 130y connection；1140 outlet tube 1142 of double sided cathodes anti-corrosion finned tube by pipeline respectively with cold liquid return tee joint 114y, source The connection of 1700 interface 1740 of side adverse current commutation station；Bilateral is received 1180 water outlet 1183 of water water storage tank and is followed by pipeline and chilling spray Ring pumps 1200 imports 1210 connection；The outlet of chilling spray circulating pump 1,200 1220 passes through pipeline and double-sided cooled sprayer-washer 1170 imports 1171 connection；Heat, which circulates mouthful threeway 114x and opened by pipeline and the efficiency heat supply of lotus side, to be stored the hot defrosting of closed-loop system 3 and follows 3770 outlet of ring pump, 3772 connection；Cold liquid return tee joint 114y opens storage 3 heat of closed-loop system with the efficiency heat supply of lotus side by pipeline and melts White 3702 import 3710 of heating coil connection；1300 import 1310 of source solution circulation pump is by pipeline through low side Mixed liquid T-branch 130x is connect with 1700 interface 1730 of source countercurrent heat-transfer commutation station；The outlet of source solution circulation pump 1,300 1320 is passed through by pipeline High-end Mixed liquid T-branch 130y, heat circulate mouthful threeway 114x and connect with 1140 inlet tube 1141 of double sided cathodes anti-corrosion finned tube；Source 1400 import 1410 of steady of system press device is blent the outlet of expansion tank 1,500 1510 with solution by pipeline and is connect；Source side system level pressure The outlet of device 1,400 1420 is connect by pipeline with source side system level pressure expansion drum 1600, low side Mixed liquid T-branch 130x respectively；Source The bridging of side expansion relief valve 1430 and 1400 both ends of source side system constant pressure arrangement；Solution blend expansion tank 1500 be disposed with soft water into Mouth 1520 blends liquid return hole 1530, liquid feeding cover board 1540, bottom position sewage draining exit 1550；It blends liquid return hole 1530 and passes through pipeline and height Hold Mixed liquid T-branch 130y connection；1700 interface 1710 of source countercurrent heat-transfer commutation station passes through pipeline and liquid leaching commutation evaporation/condensation The connection of 2300 interface 2322 of device；1700 interface 1720 of source countercurrent heat-transfer commutation station passes through pipeline and liquid leaching commutation evaporation/condensation The connection of 2300 interface 2321 of device.

It includes low heat oil cold compressor 2100, multi-order refractive silk that the economic heat pump lifting device 2 of the multi-way adverse current, which is constituted, Net oil device 2200, liquid leaching commutation evaporator/condensers 2300, middle pressure synergy economizer 2400, vacuole absorb economizer 2500, liquid Control throttling set 2600 and multipaths commutation condensation/vaporization device 2700.

2100 air entry 2110 of low heat oil cold compressor is by pipeline through oil oil return threeway 210n, return-air siphon Threeway 210v, airflow-reversing threeway 210x soak commutation 2300 outlet valve 2317 of evaporator/condensers with liquid and connect；The cold pressing of low heat oil 2100 exhaust outlet 2120 of contracting machine is connect by pipeline with 2200 air inlet 2210 of multi-order refractive silk screen oil eliminator；Multi-order refractive silk 2200 gas outlet 2220 of net oil device soaks commutation 2300 interface 2320 of evaporator/condensers with liquid respectively by pipeline, multipaths is changed It is connected to 2700 interface 2711 of condensation/vaporization device；2200 oil discharge outlet of multi-order refractive silk screen oil device throttling valve group 2230 passes through pipe Road is connect with oil oil return threeway 210n；The 2100 cold import 2140 of oil of low heat oil cold compressor passes through pipeline and oil cooler The connection of 2160 oil outlets 2161；The cold outlet 2150 of 2100 oil of low heat oil cold compressor passes through pipeline and 2160 oil inlet of oil cooler Mouth 2162 connects；Oil cooler 2160 is connected to cooling water inlet 2163 and cooling water outlet 2164 respectively；Low heat oil cold compression 2100 increasing enthalpy mouth 2130 of machine is connect by pipeline with middle 2400 gas returning port 2420 of pressure synergy economizer；Liquid leaching commutation evaporation/condensation 2300 interface 2311 of device is connected by pipeline through low pressure liquid stream threeway 273x and multipass flow commutation 2700 interface 2719 of condensation/vaporization device It connects；Liquid leaching commutation 2300 micropore vacuole oil return apparatus 2318 of evaporator/condensers is by pipeline through vacuole oil return threeway 273w and more Process commutation 2700 micropore vacuole oil return apparatus 2718 of condensation/vaporization device connection；Liquid leaching commutation 2300 interface of evaporator/condensers 2319 are connect through high pressure liquid stream threeway 273z with middle 2400 interface 2440 of pressure synergy economizer by pipeline；Multipaths commutation is cold Solidifying/2700 interface 2717 of evaporator is connect by pipeline with high pressure liquid stream threeway 273z；Middle pressure synergy economizer 2400 is subcooled swollen Swollen valve group import 2410 is connect by pipeline with high pressure liquid stream threeway 273y；Vacuole absorbs 2500 interface 2540 of economizer and passes through pipe Road is connect with high pressure liquid stream threeway 273y；Vacuole absorbs 2500 interface 2530 of economizer and passes through pipeline and hydraulic-control throttling device 2600 Import 2610 connects；The outlet of hydraulic-control throttling device 2,600 2620 is connect by pipeline with low pressure liquid stream threeway 273x；Heating evaporation Fluid level controller 2640 is installed in the middle part of liquid leaching commutation 2300 outer housing of evaporator/condensers；Refrigeration evaporator fluid level controller 2630 It is installed in the middle part of multipaths commutation 2700 outer housing of condensation/vaporization device；Vacuole absorbs 2500 interface 2510 of economizer and passes through pipeline It is connect with vacuole oil return threeway 273w；Vacuole absorbs 2500 interface 2520 of economizer and is connected by pipeline and return-air siphon threeway 210v It connects；Liquid leaching commutation 2300 interface 2322 of evaporator/condensers is connected by pipeline and 1700 interface 1710 of source countercurrent heat-transfer commutation station It connects；Liquid leaching commutation 2300 interface 2321 of evaporator/condensers is connected by pipeline and 1700 interface 1720 of source countercurrent heat-transfer commutation station It connects；Multipaths commutation 2700 interface 2722 of condensation/vaporization device is released and can be shunted by the heated diversion three-way 300x of pipeline and paddy electricity Valve 3130 connects；Multipaths commutation 2700 interface 2721 of condensation/vaporization device passes through pipeline and the outlet of lotus side circulating pump 3,100 3120 Connection.Liquid leaching commutation 2300 enclosure interior of evaporator/condensers is respectively disposed with lower homogenizing plate 2312 from the bottom to top, impregnates vertical setting of types steaming Send out tube bundle 2313, vacuole absorbs tube bundle 2314, aerosol absorbs frost prevention tube bundle 2315, upper homogenizing plate 2316；Multipaths commutation condensation/ 2700 enclosure interior of evaporator be from top to bottom respectively disposed with flow distribution plate 2712, superheated steam level-one heat absorption tube bundle 2713, Steam second level heat absorption tube bundle 2714 opens wing vertical setting of types condenser pipe 2715, lower flow distribution plate 2716.

It includes lotus side circulating pump 3100, block efficiency heating demand that the block efficiency heat supply, which is opened storage closed-loop system 3 and constituted, Side 3200, lotus side system constant pressure arrangement 3300 soften water supply tank 3400, level pressure expansion drum 3500, without pressure heat storage tank 3600, bilateral Releasing can heat-exchanger rig 3700 and paddy electricity heating device 3800.

Circulating pump 3100 import 3710 in the lotus side is negative through water-supply and pressure-stabling threeway 300z and the heat supply of block efficiency by pipeline 3220 connection of the outlet of lotus side 3200；3200 import 3210 of block efficiency heating demand side passes through the heated confluence threeway of pipeline 300y, paddy electricity are released can flow divider 3130, heating diversion three-way 300x connection；3300 import 3310 of lotus side system constant pressure arrangement passes through Pipeline is connect with softening water supply tank 3400 outlet 3420；Distinguished by branch pipe tee connection the outlet of lotus side system constant pressure arrangement 3,300 3320 It is connect with level pressure expansion drum 3500, water-supply and pressure-stabling threeway 300z；The bridging of lotus side pressure relief safety valve 3330 is filled with lotus side system level pressure Set 3300 both ends；Soften 3400 top of water supply tank and is filled equipped with soft water import barrier device 3410, top equipped with access hole 3430, bottom There is sewage draining exit 3440；It is connect by pipeline with 3810 import 3811 of heating/heat release circulating pump without pressure heat storage tank 3600 outlet 3610； Accumulation of heat is led directly to paddy electricity heating device 3800 through heat release confluence threeway 380a by pipeline without pressure 3600 import 3620 of heat storage tank to go out Mouth 3840 connects；It is filled at the top of heat storage tank 3600 equipped with floating ball water inlet 3630, floating ball access hole 3631, level sensing temperature control without pressing Set 3611；Domestic hot-water's interface 3640 mixes water circle device 3650 with domestic hot-water's automatic control and connect；Paddy electricity heating device 3800 is released Energy 3700 heat release import 3750 of heat-exchanger rig is released with bilateral by pipeline and is connect in heat outlet 3830；Bilateral is released can heat-exchanger rig 3700 Heat release outlet 3760 is connect by pipeline with heat release confluence threeway 380a；Primary Ioops electric heating is housed inside paddy electricity heating device 3800 Device 3801 and secondary circuit electric calorifie installation 3802；Bilateral releases energy reheating 3701 import 3730 of coil pipe of heat-exchanger rig 3700 and passes through pipe Road is connect with heating diversion three-way 300x；Bilateral release can heat-exchanger rig 3700 reheat coil pipe 3701 outlet 3740 by pipeline with Heating confluence threeway 300y connection；Bilateral release can 3702 import 3710 of heat-exchanger rig 3700 defrosting heating coil by pipeline with it is cold The 114y connection of liquid return tee joint；Bilateral release can the outlet of 3700 defrosting heating coil 3702 of heat-exchanger rig 3720 melted by pipeline and heat White 3770 import 3771 of circulating pump connection；The hot outlet of defrosting circulating pump 3,770 3772 circulates a mouthful threeway 114x by pipeline and heat Connection.

1 working principle of greenhouse heat source closed loop heat source absorption system:

Conventional air source heat pump technology utilizes the low area structure of narrow finned tube, with low pressure working fluid expansion humid gas in narrow finned tube Steam low level heat source in air is absorbed, narrow finned tube frosting, poor heat transfer is average at 15 DEG C or more between air and working medium, and heat pump supplies Hot property is low.The following external salting liquid, aeration cycle absorb in air steam low level heat source by traditional water source Heat pump is promoted, and causes dilute solution exhaust emission water body, air circulation salt fog drift pollution air, salting liquid evaporation endothermic, heat Source temperature is low, and heat pump heat supply performance is low.

Using the high small different transfer of heat of area piece finned tube in broadband, with the circular flow turbulent flow velocity on 10 times in wide finned tube It absorbs from steam low level heat source in air, reducing finned tube frosting probability is more than 98% or more, air heat source temperature and working medium Between temperature heat transfer difference it is average less than 5 DEG C, heat source temperature is high, and heat pump heat supply performance is high.Working principle is as follows:

Negative pressure shape is presented under the driving of system variable air rate circulator 1160 in greenhouse haze heat source from atmospheric environment in system State, atmospheric greenhouse haze heat source are oriented to air intake grid 1120, bilateral dust refractor 1130, double sided cathodes anti-corrosion finned tube through bilateral 1140,1150 absorption of bilateral water mist absorber is handled, and atmospheric greenhouse haze heat source passes through in double sided cathodes anti-corrosion finned tube 1140 Cryogenic freezing solution heat transfer medium absorbs enthalpy and is declined to become low temperature purification cold air, and driving through variable air rate circulator 1160 will Cold air directive lower than atmospheric temperature completes cold and hot exchange process in the air.It is low from the economic heat pump lifting device 2 of multi-way adverse current Warm frozen soln enters 1700 interface 1720 of source adverse current commutation station, is followed by interface 1730 into source solution through reversal valve 170d Ring pumps 1300 imports 1310, through circulating pump pressurised driving, enters 1140 inlet tube of double sided cathodes anti-corrosion finned tube by outlet 1320 1141, in cryogenic freezing solution double sided cathodes anti-corrosion finned tube, the low level heat source that counter-current absorption is passed to from finned tube, solution Temperature rise heat content increase, by outlet tube 1142 enter 1700 interface 1740 of source adverse current commutation station, through reversal valve 170b by Interface 1710 enters the small temperature difference turbulent circulation heat transfer that the economic heat pump lifting device 2 of multi-way adverse current completes cryogenic freezing solution medium Process.

Economic 2 working principle of heat pump lifting device of multi-way adverse current

Traditional technology absorbs low level heat source using two process evaporators, it was demonstrated that heat transfer efficiency only has the 50% of air conditioning condition, unit The evaporator liquid in-out temperature difference generally only has 2 degree, and excessive unsaturation humid gas, which enters heat pump compressor, to be continued to absorb heat, and causes compressor Frosting is serious, and evaporating pressure is higher, and circulating frozen solution is caused to go out liquid temperature height and difference in air temperature reduction, absorbs low temperature position heat Source capability deficiency becomes art technology problem.

It is conducted heat using low-temperature heat source circulatory mediator multipaths microchannel, the supercooling of level-one economizer absorbs pressure increasing enthalpy in progress and mends Repay, second level micro channel heat power foam oil return siphon return-air simultaneously worker quality liquid after cold multinomial technical application ensure refrigeration it is low Pressure working medium is sufficiently evaporated, and the unit evaporator liquid in-out temperature difference is big, and compressor frost-free evaporating pressure is low, and evaporating temperature low circulation is cold Freeze-thaw liquid goes out that liquid temperature is low to be increased with difference in air temperature, and the low level heat source ability increasing of absorption is solved as art technology hardly possible Topic.Unit is using a small amount of electric energy as driving force, using refrigeration working medium as carrier, continuously absorbs and is difficult in air or natural environment The low grade heat energy utilized is converted into high-grade thermal energy, realizes transfer of the low temperature heat energy to high temperature heat, high-grade thermal energy is released It is put into hot water preparing in water, summer can realize refrigerating function by valve transfer.Working principle is as follows:

From 1 frozen soln heat transfer medium solution temperature highest heat content highest of greenhouse heat source closed loop heat source absorption system by interface 2322, which enter liquid leaching commutation 2300 aerosol of evaporator/condensers, absorbs 2315 tube side of frost prevention tube bundle, to shell side working medium unsaturation gas Discharge low temperature position energy, the decline of tube side frozen soln heat-transfer medium temperature；Enter vacuole through tube sheet and absorb 2314 tube side of tube bundle, to shell Journey working medium foam droplet continues to discharge low temperature position energy, the decline of tube side frozen soln heat-transfer medium temperature；It is perpendicular to enter immersion through tube sheet Tube side on row's evaporation tube bundle 2313 continues to discharge under the energy tube side frozen soln heat-transfer medium temperature of low temperature position to shell side worker quality liquid Drop；Enter the lower tube side of immersion vertical setting of types evaporation tube bundle 2313 through tube sheet to continue to discharge low temperature position energy to shell side worker quality liquid, tube side is cold Freeze-thaw liquid heat-transfer medium temperature drops to the minimum evaporator/condensers 2300 that commutate of soaking through liquid of the minimum heat content of minimum solution temperature and connects Mouth 2321 enters greenhouse heat source closed loop heat source absorption system 1 and completes evaporator tube side medium heat-transfer process.

From 2600 low pressure working fluid expanding liquid of hydraulic-control throttling device, enter liquid leaching commutation evaporation/condensation through interface 2311 The lower homogenizing plate 2312 of device 2300 flows, and evaporates the outer explosive evaporation of tube bundle 2313 into vertical setting of types is impregnated, the bubbles burst of generation carries Drop absorbs the absorption of tube bundle 2314 through vacuole and is evaporated to working medium unsaturation gas, then finally absorbs through frost prevention tube bundle 2315 as work Matter saturated gas converges through upper homogenizing plate 2312, and it is cold into low heat oil to soak commutation 2300 interface 2317 of evaporator/condensers through liquid 2100 air entry 2110 of compressor is promoted to working medium high pressure superheater gas through compressor work, is entered by exhaust outlet 2120 multistage 2200 air inlet 2210 of silk screen oil eliminator is reflected, working medium high pressure superheater gas isolates mist of oil in oil and is deposited on container bottom Portion's intermittent oil returning, working medium high pressure superheater gas enter multipaths commutation condensation/vaporization device 2700 through gas outlet 2220, interface 2711 Storage closed loop is opened to tube side block efficiency heat supply after flow distribution plate 2712 shunts on shell side, through superheated steam level-one heat absorption tube bundle 2713 3 interlude of system to water outlet discharges sensible heat, is condensed into working medium high-pressure saturated steam, into second level heat absorption tube bundle 2714, opens Wing vertical setting of types condenser pipe 2715 discharges condensation latent heat, transfers heat to tube side block efficiency heat supply and opens storage 3 backwater end of closed-loop system It to interlude, is condensed into working medium high pressure saturated liquid and converges through lower flow distribution plate 2716, by multipaths commutation condensation/vaporization device 2700 Interface 2717 presses 2400 interface 2440 of synergy economizer in entering, and high pressure saturated liquid discharges sensible heat temperature decline cooling during rolling and steams Body of getting angry is sucked the performance for realizing Gas-supplying enthalpy-increasing by compressor intermediary interface, is entered back into vacuole and is absorbed the leaching of 2500 absorbing liquid of economizer Commutate refrigerant entrained by 2300 micropore vacuole oil return apparatus 2318 of evaporator/condensers, and boil-off gas is by return-air siphon threeway 210v enters compressor, and working medium high pressure saturated liquid is lower by secondary supercooling evaporating temperature, absorbs economizer 2500 by vacuole After interface 2520 enters 2600 reducing pressure by regulating flow of hydraulic-control throttling device, low pressure working fluid liquid enters liquid leaching commutation through interface 2311 and steams Hair/condenser 2300 completes refrigeration working medium against Carnot cycle.

The cold and hot function working medium side switching of system is that commutation evaporator/condensers 2300, multipaths commutation condensation/steaming are soaked by liquid It sends out the mutually switching of device 2700 and realizes power and energy.

Liquid leaching commutation 2300 heat supply mode of evaporator/condensers: interface 2317 is opened；Interface 2311 is opened；Interface 2320 closes；Interface 2319 close.

Liquid leaching commutation 2300 refrigeration mode of evaporator/condensers: interface 2317 closes；Interface 2311 closes；Interface 2320 is opened；Interface 2319 open.

Multipaths commutation 2700 heat supply mode of condensation/vaporization device: interface 2711 is opened；Interface 2717 is opened；Interface 2720 closes； Interface 2719 closes.

Multipaths commutation 2700 heat supply mode of condensation/vaporization device: interface 2711 closes；Interface 2717 closes；Interface 2720 is opened； Interface 2719 is opened.

The switching of system Cooling and Heat Source circulated in countercurrent, is by the adaptive switched power and energy of source countercurrent heat-transfer commutation station 1700.

Heat supply: valve 170 closes a；Valve 170b is opened；Valve 170b closes c；Valve 170b opens d；

Refrigeration: valve 170 opens a；Valve 170b is closed；Valve 170b opens c；Valve 170b closes d.

Block efficiency heat supply, which is opened, stores 3 working principle of closed-loop system

The closed type heat source tower heat pump techniques of emerging birth use opening type thermal-storage energy frost prevention technology, and accumulation of heat energy medium is molten with frozen soln Liquid is carrier, and system needs huge accumulation of heat energy medium to cause to invest excessively high and waste.

Country makes full use of paddy electricity storing energy and supplying hot, and paddy electricity energy-storage open system investments are relatively low, but can not be with end high level Closed circulation system is in parallel；The investment of paddy electricity accumulation of energy closed system is relatively high, and pressure of equipment is subject to certain restrictions also can not be the same as end Hold Super High closed circulation system in parallel.And pure paddy electricity accumulation of heat energy heating system is huge, and it also requires utilizing a little peak ordinary telegrams The instant heat supply of valence, total energy consumption cost is relatively high, is more than gas fired-boiler heat cost.

Greenhouse heat source heat pump system is in conjunction with paddy electricity energy-storage open system, in greenhouse when the economic heat source of the higher heat pump of heat source Economic 2 heat supply of heat pump lifting device of Duan Liyong multi-way adverse current, utilizes low valley power storage or instant heat supply temperature at cold climate night Low reheating supplement is spent, releases that can release using bilateral can be during one channel of heat-exchanger rig realizes that open type high temperature storage slot hot water circuit is converted to Warm water's heat supply releases energy two channel of heat-exchanger rig using bilateral and realizes that open type high-temperature heat accumulation slot hot water circuit is cold by low temperature negative temperature Freeze-thaw liquid replaces the warm circulation solution that is positive, and solves under special low temperature and high relative humidity weather conditions as heat energy carrier is stored, greenhouse heat source is inhaled Hot defrosting origin of heat required for receiving apparatus frosting eliminates huge opening type thermal-storage energy demisler, realizes paddy electricity open type The enclosed of high-temperature heat accumulation takes the multifunctional application of heat to reduce project investment cost.Caused by the different periods heat pump and paddy electricity not Same economic performance, the high heat supply mode that System Priority selects economic performance high.Working principle is as follows:

Heating load increase load is big in cold weather, follows from economic 2 interface 2722 of heat pump lifting device of multi-way adverse current Ring hot water temperature is insufficient, and heated shuntings import threeway 300x respectively enters paddy electricity and releases that energy flow divider 3130, bilateral is released to exchange heat 3700 import 3730 of device, which enters, reheats the raising of 3701 relation reheating temperature of coil pipe, enters heating confluence threeway by outlet 3740 300y with from paddy electricity release can 3130 hot water mixed flow of flow divider through interface 3210 enter block efficiency heating demand side 3200 discharge Thermal energy, the decline of circulating hot water temperature flow back into lotus side circulating pump 3100 by interface 3220 and drive pressurization feeding multi-way adverse current economical 2 interface 2721 of heat pump lifting device completes the cyclic process that hot water heat pump circulation and paddy electricity reheat.

Paddy electricity accumulation of heat circulation process, recirculated water is by entering heat/heat release circulating pump 3810 without pressure heat storage tank 3600 outlet 3610 Driving pressurization is added into 3800 recirculated water of paddy electricity heating device by primary Ioops electric calorifie installation 3801 and secondary circuit electric calorifie installation 3802 Heat, accumulation of heat high temperature circulation hot water are directly entered through straight-through accumulation of heat outlet 3840 and carry out accumulation of heat exchange cycles without pressure heat storage tank 3600, Reach set temperature and stops accumulation of heat.

Directly-heated heat release circulation process, it is to close 3840 conditions of straight-through accumulation of heat outlet that heat pump cycle hot water, which reheats circulation, Under, by entering heating/driving pressurization of heat release circulating pump 3810 without pressure heat storage tank 3600 outlet 3610, into paddy electricity heating device 3800 recirculated waters are heated by primary Ioops electric calorifie installation 3801 and secondary circuit electric calorifie installation 3802, and accumulation of heat high temperature circulation hot water is through straight-through Accumulation of heat outlet 3840 is directly entered bilateral and releases energy 3700 interface 3750 of heat-exchanger rig, and high-temperature position thermal energy is transmitted to reheating coil pipe 3701 release sensible heats, the decline of circulating hot water temperature enter through interface 3760 without pressure 3600 heat exchange cycle of heat storage tank, and it is straight to complete paddy electricity Middle whose heat transfer process of warm are heated to be to high-temperature-hot-water isolation for heat and energy storage heat release.

Defrosting solution heating procedure is high temperature under the conditions of closing paddy electricity heating device 3800 leads directly to accumulation of heat outlet 3840 Circulating hot water is heated by entering heating/driving pressurization of heat release circulating pump 3810 without pressure heat storage tank 3600 outlet 3610 into paddy electricity 3800 recirculated water of device is heated by primary Ioops electric calorifie installation 3801 and secondary circuit electric calorifie installation 3802, and high temperature circulation hot water is through heat release Energy 3700 interface 3750 of heat-exchanger rig is released into bilateral in outlet 3830, and high-temperature position thermal energy is transmitted to defrosting heating coil 3702 and is discharged Sensible heat, hot water temperature's decline enters through interface 3760 to exchange heat without pressure heat storage tank 3600, completes cryogenic freezing solution isolation cycle and adds Thermal process.Being released by the frozen soln of hot water isolation heating by bilateral can 3700 defrosting heating coil of heat-exchanger rig, 3702 interface 3720 enter hot 3770 pressurised driving of defrosting circulating pump, and the frozen soln of heating enters greenhouse heat source closed loop heat source absorption system 1 Interior cryogenic freezing solution reflux is managed in the displacement of double sided cathodes anti-corrosion finned tube 1140, while discharging sensible heat defrosting, cryogenic freezing solution Reflux is released energy 3700 defrosting heating coil 3702 of heat-exchanger rig into bilateral and is recycled through cold liquid return tee joint 114y, interface 3710 Heating.

Domestic hot-water's functional sequence: water circulation is mixed with domestic hot-water's automatic control without 3600 domestic hot-water's interface 3640 of pressure heat storage tank The connection of device 3650 obtains high-temperature-hot-water.

Claims (9)

1. a kind of greenhouse heat source heat pump paddy electricity accumulation of heat block energy source station, it is characterized in that: it includes that greenhouse heat source closed loop heat source absorbs System (1), the economic heat pump lifting device (2) of multi-way adverse current and block efficiency heat supply open and store closed-loop system (3), the block efficiency It includes lotus side circulating pump (3100), block efficiency heating demand side (3200), lotus side system that heat supply, which is opened storage closed-loop system (3) and constituted, Constant pressure arrangement (3300), softening water supply tank (3400), level pressure expansion drum (3500), without pressure heat storage tank (3600), bilateral is released to change Thermal (3700) and paddy electricity heating device (3800), lotus side circulating pump (3100) and the economic heat pump of multi-way adverse current are promoted and are filled Set (2) connection, block efficiency heating demand side (3200) by pipeline respectively with heating diversion three-way (300x), heating confluence three Logical (300y) connection, and connect through water-supply and pressure-stabling threeway (300z) with lotus side circulating pump (3100) by pipeline, lotus side system is fixed The outlet (3320) of pressure device (3300) by branch pipe tee connection respectively with level pressure expansion drum (3500), water-supply and pressure-stabling threeway (300z) Connection, the outlet (3420) that the import (3310) of lotus side system constant pressure arrangement (3300) passes through pipeline and softening water supply tank (3400) Connection；It is connect without pressure heat storage tank (3600) with paddy electricity heating device (3800), paddy electricity heating device (3800) is released with bilateral and can be changed Thermal (3700) connection, bilateral release can heat-exchanger rig (3700) respectively with heating diversion three-way (300x), heating confluence threeway The connection of (300y), greenhouse heat source closed loop heat source absorption system (1).

2. greenhouse heat source heat pump paddy electricity accumulation of heat block energy source station according to claim 1, it is characterized in that: the lotus side recycles The import (3110) for pumping (3100) passes through pipeline through water-supply and pressure-stabling threeway (300z) and block efficiency heating demand side (3200) Export (3220) connection；The import (3210) of block efficiency heating demand side (3200) passes through pipeline and heating confluence threeway (300y), paddy electricity are released can flow divider (3130), heating diversion three-way (300x) connection；Lotus side system constant pressure arrangement (3300) into Mouth (3310) is connect by pipeline with the outlet (3420) for softening water supply tank (3400)；Lotus side system constant pressure arrangement (3300) goes out Mouth (3320) is connect with level pressure expansion drum (3500), water-supply and pressure-stabling threeway (300z) respectively by branch pipe tee connection；Lotus side pressure release peace Full valve (3330) is connected across lotus side system constant pressure arrangement (3300) both ends；Soften water supply tank (3400) top and soft water import control is housed Device (3410) processed, top are equipped with sewage draining exit (3440) equipped with access hole (3430), bottom；Outlet without pressure heat storage tank (3600) (3610) it is connect by pipeline with the import (3811) of heating/heat release circulating pump (3810)；Import without pressure heat storage tank (3600) (3620) accumulation of heat outlet (3840) is led directly to paddy electricity heating device (3800) through heat release confluence threeway (380a) by pipeline to connect； Without pressure heat storage tank (3600) top equipped with floating ball water inlet (3630), floating ball access hole (3631) and level sensing temperature control device (3611)；Domestic hot-water's interface (3640) mixes water circle device (3650) with domestic hot-water's automatic control and connect；Paddy electricity heating device (3800) heat release outlet (3830) is released energy heat-exchanger rig (3700) heat release import (3750) with bilateral by pipeline and is connect；Bilateral is released Energy heat-exchanger rig (3700) heat release outlet (3760) is connect by pipeline with heat release confluence threeway (380a)；Paddy electricity heating device (3800) internal that primary Ioops electric calorifie installation (3801) and secondary circuit electric calorifie installation (3802) are housed；Bilateral is released can heat-exchanger rig (3700) reheating coil pipe (3701) import (3730) is connect by pipeline with heating diversion three-way (300x)；Bilateral, which is released, to change Thermal (3700) reheats coil pipe (3701) outlet (3740) and is connect by pipeline with heating confluence threeway (300y)；Bilateral is released Energy heat-exchanger rig (3700) defrosting heating coil (3702) import (3710) is connect by pipeline with cold liquid return tee joint (114y)； Bilateral releases energy heat-exchanger rig (3700) defrosting heating coil (3702) outlet (3720) and passes through pipeline and hot defrosting circulating pump (3770) import (3771) connects；Hot defrosting circulating pump (3770) outlet (3772) circulates a mouthful threeway by pipeline and heat (114x) connection.

3. greenhouse heat source heat pump paddy electricity accumulation of heat block energy source station according to claim 1, it is characterized in that: the greenhouse heat source Closed loop heat source absorption system (1) includes that haze absorption in greenhouse takes thermal (1100), chilling spray circulating pump (1200), source molten Liquid circulating pump (1300), source side system constant pressure arrangement (1400), solution blend expansion tank (1500), source side system level pressure expansion drum (1600) and source countercurrent heat-transfer commutation station (1700), the greenhouse haze absorption take thermal (1100) by pipeline through heat It circulates a mouthful threeway (114x) to connect with the pump discharge Mixed liquid T-branch (130y) of source solution circulation pump (1300), and passes through pipeline Respectively with interface (1740), the chilling spray circulating pump of cold liquid return tee joint (114y), source adverse current commutation station (1700) (1200) import (1210) connection；The import (1410) of source side system constant pressure arrangement (1400) is blent by pipeline with solution swollen The outlet (1510) of swell (1500) connects；The outlet (1420) of source side system constant pressure arrangement (1400) passes through pipeline and source respectively Side system level pressure expansion drum (1600), low side Mixed liquid T-branch (130x) connection.

4. greenhouse heat source heat pump paddy electricity accumulation of heat block energy source station according to claim 3, it is characterized in that: greenhouse haze absorbs Taking thermal (1100) includes steel construction overlapping frame maintenance (1110), bilateral guiding air intake grid (1120), the refraction of bilateral dust Device (1130), double sided cathodes anti-corrosion finned tube (1140), bilateral water mist absorber (1150), variable air rate circulator (1160), Double-sided cooled sprayer-washer (1170) and bilateral receive water water storage tank (1180), in the steel construction overlapping frame maintenance (1110) Portion's bottom truss is equipped with bilateral and receives water water storage tank (1180)；Bilateral receives water water storage tank (1180), and bidirectional arrangements are pacified in order above Air intake grid (1120), bilateral dust refractor (1130), double sided cathodes anti-corrosion finned tube (1140), bilateral water are oriented to equipped with bilateral Mist absorber (1150), intermediate position are fixed by the internal middle part truss of steel construction overlapping frame maintenance (1110)；Variable air rate circulation Device (1160) is installed on steel construction overlapping frame maintenance (1110) inside top central truss and atmosphere；Bilateral is cold But sprayer-washer (1170) bidirectional arrangements be installed on steel construction overlapping frame maintenance (1110) placed on top two sides, below equipment For bilateral dust refractor (1130), double sided cathodes anti-corrosion finned tube (1140), bilateral water mist absorber (1150).

5. greenhouse heat source heat pump paddy electricity accumulation of heat block energy source station according to claim 3 or 4, it is characterized in that: double sided cathodes The inlet tube (1141) of anti-corrosion finned tube (1140) circulates a mouthful threeway (114x) and source solution circulation pump through heat by pipeline (1300) pump discharge Mixed liquid T-branch (130y) connection；The outlet tube (1142) of double sided cathodes anti-corrosion finned tube (1140) passes through pipe Road is connect with the interface (1740) of cold liquid return tee joint (114y), source adverse current commutation station (1700) respectively；Bilateral receives water ponding The water outlet (1183) of slot (1180) is connect by pipeline with the import (1210) of chilling spray circulating pump (1200)；Chilling spray The outlet (1220) of circulating pump (1200) is connect by pipeline with the import (1171) of double-sided cooled sprayer-washer (1170)；Heat It circulates a mouthful threeway (114x) and is opened by pipeline and the efficiency heat supply of lotus side and store going out for hot defrosting circulating pump (3770) in closed-loop system (3) Mouth (3772) connection；Cold liquid return tee joint (114y) is opened by pipeline and the efficiency heat supply of lotus side stores hot defrosting in closed-loop system (3) The import (3710) of heating coil (3702) connects；The import (1310) of source solution circulation pump (1300) is by pipeline through low side Mixed liquid T-branch (130x) is connect with the interface (1730) of source countercurrent heat-transfer commutation station (1700)；Source solution circulation pump (1300) Outlet (1320) a mouthful threeway (114x) and double sided cathodes anti-corrosion fin are circulated through high-end Mixed liquid T-branch (130y), heat by pipeline Manage inlet tube (1141) connection of (1140)；The import (1410) of source side system constant pressure arrangement (1400) is hooked by pipeline and solution Convert outlet (1510) connection of expansion tank (1500)；The outlet (1420) of source side system constant pressure arrangement (1400) passes through pipeline respectively It is connect with source side system level pressure expansion drum (1600), low side Mixed liquid T-branch (130x)；Source expansion relief valve (1430) is connected across Source side system constant pressure arrangement (1400) both ends；Solution blends expansion tank (1500) and is disposed with soft water import (1520), blends back liquid Mouth (1530), liquid feeding cover board (1540), bottom position sewage draining exit (1550)；It blends liquid return hole (1530) and passes through pipeline and high-end mixed liquid three Logical (130y) connection；The interface (1710) of source countercurrent heat-transfer commutation station (1700) is mentioned by pipeline and the economic heat pump of multi-way adverse current Rise device (2) connection.

6. greenhouse heat source heat pump paddy electricity accumulation of heat block energy source station according to claim 1, it is characterized in that: multi-way adverse current Economic heat pump lifting device (2) constitute include low heat oil cold compressor (2100), multi-order refractive silk screen oil device (2200), Liquid leaching commutation evaporator/condensers (2300), middle pressure synergy economizer (2400), vacuole absorb economizer (2500), hydraulic-control throttling Device (2600) and multipaths commutation condensation/vaporization device (2700), low heat oil cold compressor (2100) air entry (2110) it soaks commutation evaporator/condensers (2300) outlet valve (2317) with liquid to connect, low heat oil cold compressor (2100) exhaust Mouth (2120) is connect by pipeline with multi-order refractive silk screen oil eliminator (2200) air inlet (2210), multi-order refractive silk screen oil Condensation/steaming that device (2200) gas outlet (2220) soaks commutation evaporator/condensers (2300) with liquid respectively by pipeline, multipaths commutates Device (2700) connection is sent out, low heat oil cold compressor (2100) is connect by pipeline with middle pressure synergy economizer (2400), liquid leaching Commutation evaporator/condensers (2300) is by pipeline through low pressure liquid stream threeway (273x) and multipass flow commutation condensation/vaporization device (2700) it connects, liquid leaching commutation evaporator/condensers (2300) is commutated by pipeline through vacuole oil return threeway (273w) and multipaths Condensation/vaporization device (2700) connection, liquid leaching commutation evaporator/condensers (2300) by pipeline through high pressure liquid stream threeway (273z) with Middle pressure synergy economizer (2400) connection, vacuole absorb economizer (2500) and are connected by pipeline and hydraulic-control throttling device (2600) It connects.

7. greenhouse heat source heat pump paddy electricity accumulation of heat block energy source station according to claim 6, it is characterized in that: the low heat is oily The air entry (2110) of cold compressor (2100) by pipeline through oil oil return threeway (210n), return-air siphon threeway (210v), Airflow-reversing threeway (210x) is connect with the outlet valve (2317) that liquid soaks commutation evaporator/condensers (2300)；The cold pressing of low heat oil The exhaust outlet (2120) of contracting machine (2100) is connected by the air inlet (2210) of pipeline and multi-order refractive silk screen oil eliminator (2200) It connects；The gas outlet (2220) of multi-order refractive silk screen oil device (2200) commutation evaporator/condensers are soaked with liquid by pipeline respectively (2300) interface (2711) connection of interface (2320), multipaths commutation condensation/vaporization device (2700)；Multi-order refractive silk screen oil Device (2200) oil discharge outlet throttling valve group (2230) is divided to connect by pipeline with oil oil return threeway (210n)；Low heat oil cold compression The cold import (2140) of machine (2100) oil is connect by pipeline with the oil outlet (2161) of oil cooler (2160)；The cold pressing of low heat oil The cold outlet (2150) of oil of contracting machine (2100) is connect by pipeline with the oil inlet (2162) of oil cooler (2160)；Oil cooler (2160) it is connected to cooling water inlet (2163) and cooling water outlet (2164) respectively；The increasing enthalpy of low heat oil cold compressor (2100) Mouth (2130) is connect by pipeline with the gas returning port (2420) of middle pressure synergy economizer (2400)；Liquid leaching commutation evaporator/condensers (2300) interface (2311) commutates condensation/vaporization device (2700) through low pressure liquid stream threeway (273x) and multipass flow by pipeline Interface (2719) connection；Liquid leaching commutation evaporator/condensers (2300) micropore vacuole oil return apparatus (2318) is by pipeline through vacuole Oil return threeway (273w) is connect with multipaths commutation condensation/vaporization device (2700) micropore vacuole oil return apparatus (2718)；Liquid leaching is changed To evaporator/condensers (2300) interface (2319) by pipeline through high pressure liquid stream threeway (273z) and middle pressure synergy economizer (2400) interface (2440) connects；Multipaths commutation condensation/vaporization device (2700) interface (2717) passes through pipeline and high pressure liquid stream Threeway (273z) connection；Middle pressure synergy economizer (2400) supercooling expansion valve group import (2410) passes through pipeline and high pressure liquid stream three Logical (273y) connection；Vacuole absorbs economizer (2500) interface (2540) and is connect by pipeline with high pressure liquid stream threeway (273y)； Vacuole absorbs economizer (2500) interface (2530) and is connect by pipeline with hydraulic-control throttling device (2600) import (2610)；Hydraulic control Throttling set (2600) outlet (2620) is connect by pipeline with low pressure liquid stream threeway (273x)；Heating evaporation fluid level controller (2640) it is installed in the middle part of liquid leaching commutation evaporator/condensers (2300) outer housing；Refrigeration evaporator fluid level controller (2630) installation In the middle part of multipaths commutation condensation/vaporization device (2700) outer housing；Vacuole absorbs economizer (2500) interface (2510) and passes through pipe Road is connect with vacuole oil return threeway (273w)；Vacuole absorbs economizer (2500) interface (2520) and passes through pipeline and return-air siphon three Logical (210v) connection；Liquid leaching commutation evaporator/condensers (2300) interface (2322) passes through pipeline and source countercurrent heat-transfer commutation station (1700) interface (1710) connects；Liquid leaching commutation evaporator/condensers (2300) interface (2321) is passed by pipeline and source adverse current Hot commutation station (1700) interface (1720) connection；Source countercurrent heat-transfer commutation station (1700) interface (1710) is soaked by pipeline and liquid Commutate evaporator/condensers (2300) interface (2322) connection；Source countercurrent heat-transfer commutation station (1700) interface (1720) passes through pipe Commutation evaporator/condensers (2300) interface (2321) is soaked with liquid and is connect in road；Multipaths commutation condensation/vaporization device (2700) interface (2722) energy flow divider (3130) is released with paddy electricity by the heated diversion three-way of pipeline (300x) to connect；Multipaths commutation condensation/ Evaporator (2700) interface (2721) is connect by pipeline with lotus side circulating pump (3100) outlet (3120).

8. greenhouse heat source heat pump paddy electricity accumulation of heat block energy source station according to claim 6, it is characterized in that: liquid leaching commutation is steamed Hair/condenser (2300) enclosure interior is respectively disposed with lower homogenizing plate (2312) from the bottom to top, impregnates vertical setting of types evaporation tube bundle (2313), vacuole absorbs tube bundle (2314), aerosol absorbs frost prevention tube bundle (2315), upper homogenizing plate (2316).

9. greenhouse heat source heat pump paddy electricity accumulation of heat block energy source station according to claim 6, it is characterized in that: the multipaths is changed To condensation/vaporization device (2700) enclosure interior is from top to bottom respectively disposed with upper flow distribution plate (2712), superheated steam level-one heat is inhaled Closed tube cluster (2713), steam second level heat absorption tube bundle (2714) open wing vertical setting of types condenser pipe (2715), lower flow distribution plate (2716).