CN109595669A - Solar energy waste-heat recovery device - Google Patents
Solar energy waste-heat recovery device Download PDFInfo
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- CN109595669A CN109595669A CN201811565148.4A CN201811565148A CN109595669A CN 109595669 A CN109595669 A CN 109595669A CN 201811565148 A CN201811565148 A CN 201811565148A CN 109595669 A CN109595669 A CN 109595669A
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- Prior art keywords
- water
- heat
- control valve
- temperature
- water tank
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- 239000002918 waste heat Substances 0.000 title claims abstract description 38
- 238000011084 recovery Methods 0.000 title claims abstract description 27
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 374
- 238000009825 accumulation Methods 0.000 claims abstract description 27
- 230000007704 transition Effects 0.000 claims abstract description 24
- 238000003860 storage Methods 0.000 claims abstract description 17
- AMXOYNBUYSYVKV-UHFFFAOYSA-M lithium bromide Chemical compound [Li+].[Br-] AMXOYNBUYSYVKV-UHFFFAOYSA-M 0.000 claims description 129
- 238000010438 heat treatment Methods 0.000 claims description 40
- 230000005619 thermoelectricity Effects 0.000 claims description 2
- 238000004064 recycling Methods 0.000 abstract description 4
- 230000000694 effects Effects 0.000 abstract description 3
- 238000009826 distribution Methods 0.000 abstract description 2
- 239000005329 float glass Substances 0.000 description 33
- 238000001816 cooling Methods 0.000 description 21
- 238000000034 method Methods 0.000 description 11
- 238000012546 transfer Methods 0.000 description 10
- 230000004087 circulation Effects 0.000 description 9
- 230000008859 change Effects 0.000 description 8
- WHXSMMKQMYFTQS-UHFFFAOYSA-N Lithium Chemical compound [Li] WHXSMMKQMYFTQS-UHFFFAOYSA-N 0.000 description 5
- 230000008901 benefit Effects 0.000 description 5
- 230000005611 electricity Effects 0.000 description 5
- 239000007789 gas Substances 0.000 description 5
- 238000009413 insulation Methods 0.000 description 5
- 229910052744 lithium Inorganic materials 0.000 description 5
- 239000000446 fuel Substances 0.000 description 4
- 238000004519 manufacturing process Methods 0.000 description 4
- WKBOTKDWSSQWDR-UHFFFAOYSA-N Bromine atom Chemical compound [Br] WKBOTKDWSSQWDR-UHFFFAOYSA-N 0.000 description 3
- GDTBXPJZTBHREO-UHFFFAOYSA-N bromine Substances BrBr GDTBXPJZTBHREO-UHFFFAOYSA-N 0.000 description 3
- 229910052794 bromium Inorganic materials 0.000 description 3
- 239000000498 cooling water Substances 0.000 description 3
- 239000000284 extract Substances 0.000 description 3
- 238000012423 maintenance Methods 0.000 description 3
- 238000002360 preparation method Methods 0.000 description 3
- 230000005855 radiation Effects 0.000 description 3
- 239000008400 supply water Substances 0.000 description 3
- 230000008878 coupling Effects 0.000 description 2
- 238000010168 coupling process Methods 0.000 description 2
- 238000005859 coupling reaction Methods 0.000 description 2
- 239000012774 insulation material Substances 0.000 description 2
- 230000008569 process Effects 0.000 description 2
- 206010021036 Hyponatraemia Diseases 0.000 description 1
- 238000009529 body temperature measurement Methods 0.000 description 1
- 230000031709 bromination Effects 0.000 description 1
- 238000005893 bromination reaction Methods 0.000 description 1
- 235000014171 carbonated beverage Nutrition 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 239000003245 coal Substances 0.000 description 1
- 238000002485 combustion reaction Methods 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000013461 design Methods 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000007667 floating Methods 0.000 description 1
- 239000011521 glass Substances 0.000 description 1
- JEGUKCSWCFPDGT-UHFFFAOYSA-N h2o hydrate Chemical compound O.O JEGUKCSWCFPDGT-UHFFFAOYSA-N 0.000 description 1
- 238000005338 heat storage Methods 0.000 description 1
- 239000008236 heating water Substances 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 239000002440 industrial waste Substances 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 150000002641 lithium Chemical class 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000000465 moulding Methods 0.000 description 1
- 238000003303 reheating Methods 0.000 description 1
- 230000008439 repair process Effects 0.000 description 1
- 238000010025 steaming Methods 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
- 230000009466 transformation Effects 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24D—DOMESTIC- OR SPACE-HEATING SYSTEMS, e.g. CENTRAL HEATING SYSTEMS; DOMESTIC HOT-WATER SUPPLY SYSTEMS; ELEMENTS OR COMPONENTS THEREFOR
- F24D3/00—Hot-water central heating systems
- F24D3/18—Hot-water central heating systems using heat pumps
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24D—DOMESTIC- OR SPACE-HEATING SYSTEMS, e.g. CENTRAL HEATING SYSTEMS; DOMESTIC HOT-WATER SUPPLY SYSTEMS; ELEMENTS OR COMPONENTS THEREFOR
- F24D3/00—Hot-water central heating systems
- F24D3/10—Feed-line arrangements, e.g. providing for heat-accumulator tanks, expansion tanks ; Hydraulic components of a central heating system
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B15/00—Sorption machines, plants or systems, operating continuously, e.g. absorption type
- F25B15/02—Sorption machines, plants or systems, operating continuously, e.g. absorption type without inert gas
- F25B15/06—Sorption machines, plants or systems, operating continuously, e.g. absorption type without inert gas the refrigerant being water vapour evaporated from a salt solution, e.g. lithium bromide
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B27/00—Machines, plants or systems, using particular sources of energy
- F25B27/02—Machines, plants or systems, using particular sources of energy using waste heat, e.g. from internal-combustion engines
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24D—DOMESTIC- OR SPACE-HEATING SYSTEMS, e.g. CENTRAL HEATING SYSTEMS; DOMESTIC HOT-WATER SUPPLY SYSTEMS; ELEMENTS OR COMPONENTS THEREFOR
- F24D2200/00—Heat sources or energy sources
- F24D2200/32—Heat sources or energy sources involving multiple heat sources in combination or as alternative heat sources
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24D—DOMESTIC- OR SPACE-HEATING SYSTEMS, e.g. CENTRAL HEATING SYSTEMS; DOMESTIC HOT-WATER SUPPLY SYSTEMS; ELEMENTS OR COMPONENTS THEREFOR
- F24D2220/00—Components of central heating installations excluding heat sources
- F24D2220/10—Heat storage materials, e.g. phase change materials or static water enclosed in a space
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A30/00—Adapting or protecting infrastructure or their operation
- Y02A30/27—Relating to heating, ventilation or air conditioning [HVAC] technologies
- Y02A30/274—Relating to heating, ventilation or air conditioning [HVAC] technologies using waste energy, e.g. from internal combustion engine
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02B—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO BUILDINGS, e.g. HOUSING, HOUSE APPLIANCES OR RELATED END-USER APPLICATIONS
- Y02B30/00—Energy efficient heating, ventilation or air conditioning [HVAC]
- Y02B30/62—Absorption based systems
- Y02B30/625—Absorption based systems combined with heat or power generation [CHP], e.g. trigeneration
Landscapes
- Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Chemical & Material Sciences (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Combustion & Propulsion (AREA)
- Materials Engineering (AREA)
- Heat-Pump Type And Storage Water Heaters (AREA)
Abstract
Solar energy waste-heat recovery device, belong to the recycling of heat supply waste heat and heat distribution field, in order to solve the problems, such as to improve water storage temperature, including solar water heater, phase transition heat accumulation unit, water tank, temperature sensor, 5th circulating pump, 13rd control valve, 14th control valve, 15th control valve, by piping connection between the loop exit and solar water heater of water tank, and the 15th control valve is set in the line segments, the outlet pipe branch two-way parallel connection water pipe of solar water heater, 13rd control valve is set on water pipe all the way, and it is connect with the 5th circulating pump, 14th control valve is set on another way water pipe, and it is connect with phase transition heat accumulation unit, 5th circulating pump is connected by phase transition heat accumulation unit, the loop head of the outlet connection water tank of 5th circulating pump, effect is to promote the temperature of intermediary's water.
Description
Technical field
The invention belongs to the recycling of heat supply waste heat and heat distribution field, are related to a kind of solar energy waste-heat recovery device.
Background technique
In recent years, with the increase of China's urban heat supplying area and the increasing of industrial premises building of production line, so that I
State's heating power consumption figure rapid growth, is analyzed, China resident heating is mainly the following mode at present from heat-supplying mode:
Cogeneration of heat and power mode, middle-size and small-size district boiler room central heating, household small-size gas water-heating furnace, family's coal furnace etc., wherein heat
Electricity Federation produces after mode is high-grade heat energy power-generating using fuel, by the comprehensive energy utilization technology of its low grade heat energy heat supply.
The average generating efficiency of 3,000,000 kilowatts of China firepower electrical plant is 33% at present, and when steam power plant's heat supply, generating efficiency is reachable
20%, remaining 80%, 70% or more in heat can be used for heat supply, the fuel of 10000 kilojoule heats, using cogeneration of heat and power side
Formula can produce 2000 kilojoule electric power and 7000 kilojoule heats, and common thermal power plant is used to generate electricity, this 2000 kilojoule electric power needs
6000 kilojoule fuel are consumed, therefore by the electric power of cogeneration of heat and power mode output, according to the generating efficiency of common power plant, deduct its combustion
Material consumption, remaining 4000 kilojoule fuel can produce 7000 kilojoule heats.In this sense, then the efficiency of steam power plant's heat supply
It is 170%, about twice of medium small boiler room heating efficiency.In conditions permit, the heating of cogeneration of heat and power should be first developed
Mode.It supplies to hanker in cogeneration of heat and power mode, or there is some problems, such as；One side power plant high-temperature steam is expensive,
On the other hand, a large amount of thermal insulation material is needed to reduce thermal loss in the steam heating pipeline of high temperature, it is higher in heating temperature
In the case where, although will cause biggish thermal losses using more thermal insulation material.It needs to look for other cheap productions thus
The heat sources such as big industrial waste heat are measured to replace the high-temperature steam of power plant part.And it is useless by the low-temperature industrial of representative of float glass factory
Heat is discarded in vain at present, or is additionally discharged using hydroelectric resources, is abandoned very unfortunate.
Summary of the invention
In order to solve the problems, such as to improve water storage temperature, the following technical solutions are proposed by the present invention:
A kind of solar energy waste-heat recovery device, including solar water heater, phase transition heat accumulation unit, water tank, temperature sensing
Device, the 5th circulating pump, the 13rd control valve, the 14th control valve, the 15th control valve, the loop exit and solar energy of water tank
By piping connection between water heater, and the 15th control valve, the outlet pipe branch two-way of solar water heater are set in the line segments
The 13rd control valve is arranged all the way, and connect with the 5th circulating pump for water pipe in parallel on water pipe, the is arranged on another way water pipe
14 control valves, and connect with phase transition heat accumulation unit, the 5th circulating pump is connected by phase transition heat accumulation unit, the 5th circulating pump
The loop head of outlet connection water tank.
Further, the high temperature output end connection of the condenser of the entrance and heat pump of water tank or the entrance and collection of water tank
Hydrophone connection.
Further, the water collector is connect with the high temperature output end of the condenser of more than one heat pump.
Further, the water tank is connect by heat exchanging pipe with the second water segregator, and the heat exchanging segment of heat exchanging pipe is located at storage
Inside water pot, and the second water segregator is set on cogeneration system, and cogeneration system is connected to bromine via the second water segregator
Change the high temperature section entrance of lithium heat pump heating device.
Further, the outlet of water tank by piping connection to lithium bromide heat pump heating device low-temperature heat exchange section entrance.
Further, with the pipeline of the water supply of the outlet connection of water tank, it is provided with the 17th control valve.
Further, the cogeneration system its be connected to power plant, vapor (steam) temperature therein is about 100 DEG C, the storage
The temperature of the water exported in water pot is about 45 DEG C, and remains defeated in water tank by the second water segregator and the tank connected heat exchanging segment of water storage
The temperature of water out is about 45 DEG C.
It further, further include temperature sensor, temperature sensor is mounted in water tank to measure water storage temperature.
A kind of solar energy waste-heat recovery device, including solar water heater, phase transition heat accumulation unit, water tank, temperature sensing
Device, the 5th circulating pump, the 13rd control valve, the 14th control valve, the 15th control valve, the second water segregator, temperature sensor peace
In water tank, by piping connection between the loop exit and solar water heater of water tank, and it is arranged the tenth in the line segments
Five control valves, the outlet pipe branch two-way parallel connection water pipe of solar water heater, all the way on water pipe be arranged the 13rd control valve, and with
5th circulating pump connects, and the 14th control valve is arranged on another way water pipe, and connect with phase transition heat accumulation unit, is stored by phase transformation
Thermal connects the 14th circulating pump, the loop head of the outlet connection water tank of the 14th circulating pump；Water tank enters
Mouth is connect with water collector, and the 4th circulating pump, the height of water collector and the condenser of more than one heat pump are arranged on the pipeline of connection
Warm output end connection；Water tank is connect by heat exchanging pipe with water segregator, and the heat exchanging segment of heat exchanging pipe is located inside water tank, and the
Breeching is set on cogeneration system, and cogeneration system is connected to lithium bromide heat pump heating device via water segregator
High temperature section entrance, low-temperature heat exchange section entrance of the outlet of water tank by piping connection to lithium bromide heat pump heating device, the connection
Pipeline be provided with the 17th control valve.
The utility model has the advantages that releasing its thermal energy stored in accumulation of heat mode by phase transition heat accumulation unit, leaving water temperature is improved, is made
Leaving water temperature is maintained at set temperature；Water storage heat cycles are recycled, until mode changes, under Three models, water tank enters
Mouth connection water collector is to supply water to water tank, the low-temperature heat exchange section of the outlet lithium bromide heat pump of the water tank, and to it
Transporting low temperature heat-exchanging water.
Detailed description of the invention
Fig. 1 is the pipeline connecting figure of apparatus of the present invention.
Fig. 2 is the pipeline connecting figure of power plant's cogeneration system of the invention.
1. float glass workshop, 2. preparation water tanks, 3. first control valves, 4. second control valves, 5. first circulations pump, 6. is cold
But tower, 7. third control valves, 8. the 4th control valves, 9. the 5th control valves, 10. the 6th control valves, 11. the 7th control valves, 12.
Eight control valves, 13. the 9th control valves, 14. the tenth control valves, 15. the 11st control valves, 16. the 12nd control valves, 17. second
Circulating pump, 18. third circulating pumps, 19. gaps, 20. thermal insulation layers, 21. cold drops, 22. hot ponds, 23. first heat pumps, 24. second
Heat pump, 25. third heat pumps, 26. water collectors, 27. the 4th circulating pumps, 28. first water segregators, 29. temperature sensors, 30. the 5th
Circulating pump, 31. phase transition heat accumulation units, 32. the 13rd control valves, 33. the 14th control valves, 34. solar water heaters, 35.
15 control valves, 36. the 16th control valves, 37. the 17th control valves, 38. second water segregators, 39. water tanks, 40. lithium bromides
Heat pump, 41. user terminal pipelines, 42. the 4th heat pumps, 43. plate heat exchangers, 44. cogeneration systems, 45. power plant's condensing gases return
Water pipe, 46. the 6th circulating pumps, 47. lithium bromide heat pump high temperature heat source water outlets.
1-1. steam heat pump unit, 1-2. third lithium bromide heat pump unit, 1-3. the second lithium bromide heat pump unit, 1-4.
Monobromination lithium heat pump unit, 1-5. steam water heat exchanger, 1-6. steam exhaust device, 1-7. steam turbine.
Specific embodiment
Embodiment 1: one kind integrating a variety of waste heat coupling heating systems, including float glass waste-heat recovery device, solar energy
Waste-heat recovery device and lithium bromide heat pump heating device.
The float glass waste-heat recovery device, including float glass workshop (1), hot pond (22), cold drop (21), second follow
Ring pumps (17), third circulating pump (18) two-step evolution valve, cooling tower (6), heat pump, first water outlet of float glass workshop (1)
It is passed through hot pond (22) by the first water pipe, the entrance of cooling tower (6) is connected to upper hose, and the export pipeline of cooling tower (6) is passed through cold drop
(21), upper hose installation two-step evolution valve and circulating pump, upper hose are passed through hot pond (22), and the hot pond of upper hose is arranged in circulating pump
(22) it at the position between two-step evolution valve, is connected between the valve of two-step evolution valve by the upper hose, and is located at the part
Upper hose connected component water pipe, the branch water pipe is by piping connection heat pump, and the pipeline for being located at the part is equipped with the 7th control
Valve (11) processed.
Heat pump includes three groups, i.e. heat pump 23, heat pump 24 and heat pump 25, the hot end of the evaporator of each heat pump (23,24,25) is defeated
Enter for branch water pipe, cold end output connection cooling tower (6) of the evaporator of heat pump.The cold end output and cooling of the evaporator of heat pump
Connecting pipeline between tower (6) is provided with the 12nd control valve (16).The hot end of the condenser of heat pump (23,24,25) exports
Water collector (26), the front end pipeline of the water collector (26) install the 4th circulating pump (27), before the 4th circulating pump (27)
It is held to be connected to the circulation water inlet of the water tank of solar energy waste-heat recovery device (39), the condenser of heat pump (23,24,25)
Cold end input is the first water segregator (28), and the first water segregator (28) connects going out for the low-temperature heat exchange section of lithium bromide heat pump heating device
Mouthful.
Upper hose described in the entrance of the cooling tower (6) two-way at least in parallel, often installs one group of control on water pipe on the way
Valve group processed, every group of control valve group include at least the two-step evolution valve of two-way parallel connection, by described between the valve of each road two-step evolution valve
Water pipe connection, and it is located at the upper hose connected component water pipe of the part, the branch water pipe connects multichannel heat pump by pipeline parallel connection,
And the pipeline for being located at the part is equipped with the 7th control valve (11).Specifically, the upper hose includes water in the first via in parallel
Pipe and the second road water pipe, first via upper hose install first group of control valve group, and first group of control valve group includes the first of parallel connection
Road two-step evolution valve and the second road two-step evolution valve, first via two-step evolution valve include the 8th control valve (12) and third control valve
(7), the second road two-step evolution valve includes the 9th control valve (13) and the 4th control valve (8)；Second road water pipe installs second group
Control valve group, second group of control valve group include first via two-step evolution valve and the second road two-step evolution valve in parallel, the first via two
Grade control valve includes the tenth control valve (14) and the 5th control valve (9), and the second road two-step evolution valve includes the 11st control valve
(15) and the 6th control valve (10)；The heat pump includes the first heat pump (23), the second heat pump (24) and third heat pump (25).
Float glass waste-heat recovery device further includes prepared water tank (2), and the outlet pipe of the prepared water tank (2) is passed through cold
Pond (21), second water outlet of float glass workshop (1) are connected to the second water pipe, the water outlet of the second outlet pipe and preparation water tank (2)
The first control valve (3) are installed in pipe connection, the outlet pipe of the second water pipe two sides, side, and the second control valve is installed in the other side
(4), first circulation pump (5) is installed on the outlet pipe in the second control valve (4) downstream.Between the hot pond (22) and cold drop (21) by
Thermal insulation layer (20) separates, and setting is connected to the gap (19) in two ponds on thermal insulation layer (20).
The execution method of above-mentioned apparatus is as follows: a kind of float glass exhaust heat recovering method, and float glass workshop (1) generates
37~39 DEG C of recirculated water is passed through hot pond (22) by the first water pipe, pressurizes, adds to second circulation pump (17), third circulating pump (18)
Pressure finishes, and opens the 8th control valve (12), the 9th control valve (13), the tenth control valve (14), the 11st control valve (15), closes
Third control valve (7), the 4th control valve (8), the 5th control valve (9), the 6th control valve (10), and open the 7th control valve
(11), 37~39 DEG C of recirculated water in hot pond (22) by upper hose circulating pump extract, and be drawn into the first heat pump (23),
Evaporator in second heat pump (24), third heat pump (25), as evaporator hot end input, 37~39 DEG C of the recirculated water with
24~26 DEG C of intermediary's water of the cold end of condenser exchanges heat, and after heat exchange, the hot end of condenser exports 33~35 DEG C of intermediary's water, steams
The cold end of hair device exports 31~33 DEG C of recirculated water and is supplied to cooling tower (6), and by being discharged into cold drop after cooling tower (6) cooling
(21), the recirculated water of cold drop (21) is opened the second control valve (4), the recirculated water quilt of cold drop (21) by first circulation pump (5) pressurization
Float glass workshop (1) is delivered to as float glass cooling water, when not needing heat exchange, opens the 8th control valve
(12), the 9th control valve (13), the tenth control valve (14), the 11st control valve (15), third control valve (7), the 4th control valve
(8), the 5th control valve (9), the 6th control valve (10), and the 7th control valve (11) is closed, 37~39 DEG C in hot pond (22)
Recirculated water is extracted by the circulating pump of upper hose, and it is cooling to be directly extracted cooling tower (6).The cold end output about 31 of evaporator~
33 DEG C of recirculated water is simultaneously supplied to cooling tower (6), and cooling water temperature requires to be 20~30 DEG C, i.e. cold drop in process flow production
(21) water temperature in should be maintained at 20~30 DEG C of metastable temperature environments, if evaporator cold end output circulating water temperature is higher than
At 30 DEG C, then by being discharged into cold drop (21) after cooling tower (6) cooling, if evaporator cold end output circulating water temperature is lower than 30 DEG C,
Then cold drop (21) directly are discharged into via cooling tower (6).
First heat pump (23), the second heat pump (24), third heat pump (25) condenser hot end export 33~35 DEG C in
Jie's water is collected by water collector (26).The pipeline of the front end of the water collector is installed for extracting intermediary's water in water collector (26)
4th circulating pump (27), the 4th circulating pump front end connect the water tank (39) of solar energy waste-heat recovery device.First heat pump (23),
Second heat pump (24), third heat pump (25) condenser cold end input 24~26 DEG C of intermediary's water by the first water segregator (28)
Supply, which connects the outlet of the low-temperature heat exchange section of lithium bromide heat pump heating device, by low-temperature heat exchange section
Heat-exchanging water recycles dress by solar energy waste heat as 24~26 DEG C of intermediary's water, to form intermediary's water of float glass waste heat recycling
Reheating is set, and the partial heat and the high-temperature-hot-water of power plant exchange heat together in lithium bromide heat pump heating device and managed to user
Road, using float glass waste heat and solar energy waste heat as heating source, and by the intermediary with relatively stable low temperature after heat exchange
Cold end output of the water for the condenser end of heat pump unit, circulation participate in heat exchange, play the role of saving to water and heat.
In the state of power-off, the second control valve (4) is closed, and the first control valve (3) is opened, the water in preparation water tank (2)
It can be the cooling water that float glass workshop (1) provides 15 minutes.By thermal insulation layer (20) between the hot pond (22) and cold drop (21)
Separate, and setting is connected to the gap (19) in two ponds, the dilutional hyponatremia in Re Chi (22) or cold drop (21) on thermal insulation layer (20)
And be more than gap (19) and enter corresponding pond in so that not because in independent pond because water excessively cause water by pond directly overflow
Out.
The solar energy waste-heat recovery device, including solar water heater (34), phase transition heat accumulation unit (31), water tank
(39), temperature sensor (29), the 5th circulating pump (30), the 13rd control valve (32), the 14th control valve (33), the 15th control
Valve (35) processed by piping connection between the loop exit and solar water heater (34) of water tank (39), and is arranged in the line segments
15th control valve (35), the outlet pipe branch two-way parallel connection water pipe of solar water heater (34) are arranged the tenth all the way on water pipe
Three control valves (32), and connect with the 5th circulating pump (30), the 14th control valve (33) of setting on another way water pipe, and with
Phase transition heat accumulation unit (31) connection connects the 5th circulating pump (30), the 5th circulating pump (30) by phase transition heat accumulation unit (31)
Outlet connection water tank (39) loop head.The entrance of water tank (39) is connect with water collector (26), the water collector (26)
The as water collector (26) of float glass waste-heat recovery device, the water collector (26) and float glass waste-heat recovery device
The high temperature output end of the condenser of three groups of heat pumps connects.
The water tank (39) is connect by heat exchanging pipe with the second water segregator (38), and the heat exchanging segment of heat exchanging pipe is located at water storage
Tank (39) is internal, and the second water segregator (38) is set on cogeneration system (44), and cogeneration system (44) is via second
Water segregator (38) is connected to the high temperature section entrance of lithium bromide heat pump heating device.The outlet of water tank (39) is by piping connection to bromine
Change the low-temperature heat exchange section entrance of lithium heat pump heating device.With the pipeline of the water supply of the outlet connection of water tank (39), it is arranged thereon
There is water of the 17th control valve (37) for controlling solar energy waste-heat recovery device to lithium bromide heat pump heating unit feeding water storage
Amount and speed.It is connected to power plant to the cogeneration system (44), and vapor (steam) temperature therein is about 100 DEG C, the water tank
(39) temperature of the water exported in is about 45 DEG C, and maintains storage by the heat exchanging segment that the second water segregator (38) is connect with water tank (39)
The temperature of the water exported in water pot (39) is about 45 DEG C.Temperature sensor (29) is mounted in water tank (39) to water storage temperature
Measurement.
The execution method of above-mentioned apparatus is as follows: solar energy exhaust heat recovering method,
Normal mode: when solar radiation intensity rather moderate, i.e. same day 7:00 to same day 11:00 and same day 15:00
When to same day 19:00, the 15th control valve (35) is opened, closes the 14th control valve (33), opens the 13rd control valve (32),
Extract the water in water tank (39) by the 5th circulating pump (30) by the loop exit of water tank (39), and by solar water
Device (34) heats the water in water tank (39), and via the pipeline for being equipped with the 13rd control valve (32), by the water after heating
Water tank (39) directly are extracted to, by the recirculated water inlet return of water tank (39) to water tank (39)；Recycle above-mentioned water storage
Heat cycles, until mode changes or the measured value of the temperature sensor (29) in water tank (39) reaches given threshold；
Energy accumulation mode: when solar radiation intensity is relatively excessive, i.e. when same day 11:00 to 15:00, the 15th control is opened
Valve (35) processed closes the 13rd control valve (32), opens the 14th control valve (33), starts phase transition heat accumulation unit (31), makes to store up
Water in water pot (39) is extracted by the loop exit of water tank (39) by the 5th circulating pump (30), and by solar water heater
(34) water in water tank (39) is heated, and via the pipeline for being equipped with phase transition heat accumulation unit (31), by phase transition heat accumulation unit
(31) excessive thermal energy is stored, leaving water temperature is made to be maintained at set temperature；Above-mentioned water storage heat cycles are recycled, until mode changes
Become；
Glow mode: when solar radiation intensity relative deficiency, i.e. when same day 19:00 to next day 7:00 or temperature sensing
When device (29) measures water temperature in half an hour and is consistently less than 40 DEG C；The 13rd control valve (32) is closed, the 14th control valve is opened
(33), start phase transition heat accumulation unit (31), make the water in water tank (39) by the loop exit of water tank (39) by the 5th circulation
Pump (30) extracts, and is heated by solar water heater (34) to the water in water tank (39), and via being equipped with phase-transition heat-storage
The pipeline of device (31) releases its thermal energy stored in accumulation of heat mode by phase transition heat accumulation unit (31), improves leaving water temperature,
Leaving water temperature is set to be maintained at set temperature；Above-mentioned water storage heat cycles are recycled, until mode changes.
Under the Three models, entrance connection water collector (26) of the water tank (39) is to supply water tank (39)
Water.The low-temperature heat exchange section of the outlet lithium bromide heat pump (40) of the water tank (39), and to its transporting low temperature heat-exchanging water.It is low
Warm heat-exchanging water is 45 DEG C.
Lithium bromide heat pump heating device, including lithium bromide heat pump (40), plate heat exchanger (43), the 4th heat pump (42)；Institute
The lithium bromide heat pump (40) stated includes high-temperature heat transfer section, low-temperature heat exchange section, medium temperature heat exchanging segment；The entrance of the high-temperature heat transfer section
It connects cogeneration system (44), the high temperature heat exchanging water pipe of the outlet connecting plate type heat exchanger (43) of high-temperature heat transfer section, low temperature changes
The entrance of hot arc connects water supplying pipe, and the outlet of low-temperature heat exchange section connects the first output pipe, the second output of medium temperature heat exchanging segment connection
Pipeline；The plate heat exchanger (43) includes high temperature heat exchanging water pipe, low-temperature heat exchange water pipe, and the outlet of the high temperature heat exchanging water pipe connects
The hot end of the 4th heat pump (42) evaporator is connect, the low-temperature heat exchange water pipe connects third output pipe；4th heat pump (42)
Evaporator cold end output connection power plant's condensing gas return pipe (45), the condenser of heat pump hot end output connection the 4th output
Pipeline.The cogeneration system (44) of the entrance of high-temperature heat transfer section is connected, the high-temperature heat transfer section of lithium bromide heat pump (40) is connected to, and
High temperature heat-exchanging water is conveyed to it, second water segregator (38) connects water tank (39) by heat exchanging pipe, and heat exchanging pipe changes
It is internal that hot arc is located at the water tank (39).The entrance of the low-temperature heat exchange section connects water supplying pipe, water supplying pipe and water tank (39)
Outlet connection.First output pipe connects the first water segregator (28), and water segregator is connected to the cold of heat pump (23,24,25)
The connecting line of the cold end of condenser, output pipe and the first water segregator (28) installs the 6th circulating pump (46).Described second is defeated
Pipeline, third output pipe, the 4th output pipe connect user terminal pipeline out, and are classification output.The cogeneration system
(44) it is connected to power plant, and vapor (steam) temperature therein is about 100 DEG C, and the temperature of the water exported in the water tank (39) is about 45
DEG C, and it is about 45 DEG C that the heat exchanging segment being connect by water segregator with water tank (39), which maintains the temperature of the water exported in water tank (39),；
The input temp of the high-temperature heat transfer section of lithium bromide heat pump (40) is about 100 DEG C, and output temperature is about 60 DEG C, low-temperature heat exchange section it is defeated
Entering temperature is about 45 DEG C, and output temperature is about 24~26 DEG C, and the output temperature of medium temperature heat exchanging segment is about 55 DEG C；Plate heat exchanger
(43) input temp of high temperature heat exchanging water pipe is about 60 DEG C, and output temperature is 28~32 DEG C, the output temperature of low-temperature heat exchange water pipe
About 55 DEG C of degree；The hot end input temp of the evaporator of heat pump is 28~32 DEG C, and output temperature is about 5 DEG C, the output of condenser
Temperature is about 40~42 DEG C.
By above-mentioned, lithium bromide heat pump heating device is exchanged heat between storage water, user terminal and power plant water, by high temperature
The heat of power plant water and storage water supplies user terminal, i.e., completes heat exchange by lithium bromide heat pump, heat pump, and by the low temperature after heat exchange
Water returns to power plant and the first water segregator respectively, so that the water at low temperature after heat exchange continues to participate in circulation, not only completes high temperature heat
With the output together of low-temperature heat quantity, also water is recycled, realize the saving at water source and heat and is sufficiently used.And in order to
Water at low temperature can be directly applied for the use of lithium bromide heat pump, filled in float glass waste-heat recovery device and lithium bromide heat pump heating
Increase solar energy waste-heat recovery device between setting, partial heat is supplemented with clean energy resource.
The execution method of above-mentioned apparatus is as follows, a kind of lithium bromide heat pump heating method, and power plant condenser introduces pipe and is connected to bromine
Change the high-temperature heat transfer section of lithium heat pump (40), and conveys high temperature heat-exchanging water (100 DEG C), the outlet bromination of water tank (39) to it
The low-temperature heat exchange section of lithium heat pump (40), and to its transporting low temperature heat-exchanging water (45 DEG C), high-temperature heat transfer section, low-temperature heat exchange section, medium temperature
In heat exchanging segment water heat exchange so that medium temperature heat exchanging segment output in (55 DEG C) supply clients of warm water；The output of low-temperature heat exchange section connects
Logical first water segregator (28), and to its transporting low temperature water (25 DEG C)；
The high temperature heat exchanging water pipe of output pipe connection plate heat exchanger (43) of high-temperature heat transfer section, and it is conveyed through high temperature
Heat-exchanging water (60 DEG C) after heat exchanging segment heat exchange, high temperature heat exchanging water pipe exchange heat with the water in low-temperature heat exchange water pipe so that low-temperature heat exchange
(55 DEG C) supply clients of warm water in water pipe output；
The output of the high temperature heat exchanging water pipe of plate heat exchanger (43) is connected to the hot end input of the evaporator of the 4th heat pump (42),
And the heat-exchanging water (28~32 DEG C) after high temperature heat exchanging water pipe heat exchange is conveyed to it, the cold end output connection electricity of the evaporator of heat pump
Factory's condenser return pipe, and condensed water (5 DEG C) are provided it, evaporator is with the water heat exchange in condenser so that the heat of condenser
End output (34~36 DEG C) supply clients of water at low temperature.
The second water segregator (38) that the cogeneration system (44) of the entrance of high-temperature heat transfer section is arranged thereon is connected, it will be high
Low-temperature heat exchange water in warm heat-exchanging water (100 DEG C) and water tank (39) exchanges heat, the low-temperature heat exchange water (45 in supply water tank (39)
DEG C) with heat.
Power plant's cogeneration system described in above scheme, including steam exhaust device (1-6), steam turbine (1-7), steam
Heat pump unit (1-1), third lithium bromide heat pump unit (1-2), the second lithium bromide heat pump unit (1-3), the first lithium bromide heat pump
Unit (1-4), each lithium bromide heat pump unit include high temperature heat source, low-temperature heat source and middle temperature-heat-source, the steam exhaust device (1-6)
Heat exchanging pipe be connected to the evaporator of steam heat pump unit (1-1) and the low-temperature heat source of each lithium bromide heat pump unit parallel, it is described
The heat exchanging pipe of steam turbine (1-7) is connected to the high temperature heat source of each lithium bromide heat pump unit, the high-temperature water outlet mouth of condenser parallel
Connect the entrance connection of the middle temperature-heat-source of the first lithium bromide heat pump unit (1-4), the outlet of the first lithium bromide heat pump unit (1-4)
It is connected to the entrance of the middle temperature-heat-source of the second lithium bromide heat pump unit (1-3), the middle warm of the second lithium bromide heat pump unit (1-3)
The outlet in source is connected to the entrance of the middle temperature-heat-source of third lithium bromide heat pump unit (1-2).
The entrance connection inlet tube of steam exhaust device (1-6), outlet connection outlet pipe, inlet tube, outlet parallel arranged,
Inlet tube is connected to the outlet of the low-temperature heat source of the first lithium bromide heat pump unit (1-4), and outlet is connected to the first lithium bromide heat pump machine
The entrance parallel connection access of the entrance of the low-temperature heat source of group (1-4), the low-temperature heat source of the second lithium bromide heat pump unit (1-3) is described out
Mouth pipe, exports the access inlet tube in parallel, and the entrance parallel connection of the low-temperature heat source of third lithium bromide heat pump unit (1-2) accesses
The outlet exports the access inlet tube in parallel, the entrance connection outlet of the evaporator of steam heat pump unit (1-1)
The outlet of pipe, the evaporator of steam heat pump unit (1-1) connects inlet tube；The entrance of steam turbine (1-7) connects inlet tube,
Connection outlet pipe, inlet tube, outlet parallel arranged are exported, inlet tube is connected to the vapor outlet of steam water heat exchanger (1-5), outlet
Pipe is connected to the vapour entrance of steam water heat exchanger (1-5), the entrance of the high temperature heat source of the first lithium bromide heat pump unit (1-4) and connection
Enter the outlet, exports the access inlet tube in parallel, the entrance of the high temperature heat source of the second lithium bromide heat pump unit (1-3)
Parallel connection accesses the outlet, exports the access inlet tube in parallel, the high temperature heat source of third lithium bromide heat pump unit (1-2)
Entrance parallel connection access the outlet, export it is in parallel access the inlet tube, the evaporator of steam heat pump unit (1-1)
The outlet of entrance connection outlet pipe, the evaporator of steam heat pump unit (1-1) connects inlet tube.
The low temperature water inlet of the condenser of the steam heat pump unit (1-1) connects water inlet line (5 degree or so).
The low-temperature heat source of the third lithium bromide heat pump unit (1-2) is also connected with water inlet line (25 degree or so).
The execution method of above-mentioned power plant's cogeneration system: 5 DEG C or so of power plant water enters steam heat pump unit (1-1)
The cold water inlet of condenser, by steam exhaust device (1-6) generate steam exhaust water steam heat pump unit (1-1) evaporator end and steaming
5 DEG C or so of power plant water of the condenser end of vapour heat pump unit (1-1) exchanges heat, by the condenser end of steam heat pump unit (1-1)
The level-one heat-exchanging water of 30 DEG C or so of output, level-one heat-exchanging water enter the middle temperature-heat-source of the first lithium bromide heat pump unit (1-4) and make
It intakes for it；The steam exhaust water that steam exhaust device (1-6) generates enters the first lithium bromide heat pump unit (1-4) and is used as low-temperature heat source, steams
Steam turbine (1-7) generate 100 DEG C of high-temperature steam enter the first lithium bromide heat pump unit (1-4) be used as high temperature heat source, first
50 DEG C of water outlet or so of secondary heat exchange water of the middle temperature-heat-source of lithium bromide heat pump unit (1-4)；Steam exhaust device (1-6) generates weary
Carbonated drink enters the second lithium bromide heat pump unit (1-3) and is used as low-temperature heat source, and the high-temperature steam that steam turbine (1-7) generates enters the
Dibrominated lithium heat pump unit (1-3) be used as high temperature heat source, 70 DEG C of water outlet of the middle temperature-heat-source of the second lithium bromide heat pump unit (1-3)
The three-level heat-exchanging water of left and right；The steam exhaust water that steam exhaust device (1-6) generates enters third lithium bromide heat pump unit (1-2) as low temperature
Heat source, the high-temperature steam that steam turbine (1-7) generates enter third lithium bromide heat pump unit (1-2) as high temperature heat source, third
90 DEG C of water outlet or so of level Four heat-exchanging water of the middle temperature-heat-source of lithium bromide heat pump unit (1-2), level Four heat-exchanging water enter vapour-water and change
Hot device (1-5) and the high-temperature steam generated with steam turbine (1-7) heat exchange, 100 DEG C of heat is exported by steam water heat exchanger (1-5)
Water.
The client is user's heating pipeline.First water segregator (28) received water at low temperature (25 DEG C), is delivered to
First heat pump (23), the second heat pump of (24), third heat pump (25) condenser cold end as intermediary's water.
Provided in this embodiment is that a kind of power plant's high-temperature steam with the low temperature exhaust heat coupling that float glass factory generates combines confession
Hot systems not only can satisfy heat demand but also reduce the use of power plant's high-temperature steam, heating cost is greatly reduced.
Float glass on-site builds heat exchange computer room, in winter by the industry in float glass plant area cooling-tower circulating water
Waste heat (38 DEG C) is cooled to 32 DEG C by heat exchanger, and the temperature of intermediary's water is promoted to 35 DEG C by 25 DEG C, drops temperature after heat exchange
As low as 31~33 DEG C, it is transmitted back to float glass heat exchange computer room, has thus obtained a large amount of low-temperature heat source.And utilize float glass
The low temperature exhaust heat of generation has following advantage:
Do not change HVAC system: being only transformed in cooling tower line segments, do not influence other systems.
Do not increase operation power expense: increasing heat exchanger computer room in on-site, heating season cooling tower is not run, and saves electricity
Take.
Do not increase and decrease counterpart device: not cancelling cooling tower, non-heating season can also continue to using not influencing other equipment.
Do not change operating temperature: temperature remains at 32 DEG C after heat exchanger heat exchange, does not influence requirement, does not increase energy
Consumption.
Using the above scheme, do not change the original service condition of factory, do not increase electric power consumption, do not influence product yield
In the case of, a large amount of waste heats can be recycled.The height that the technical solution of the present embodiment can provide a large amount of low-temperature heat source and power plant provides
Warm steam couples heat supply, under conditions of not influencing heating effect, greatly reduces the dosage of power plant's high-temperature steam, and sufficiently benefit
The low-temperature heat source generated with float glass factory, reduces heat cost, improves economic benefit.Therefore, the present invention is to realization
Target for energy-saving and emission-reduction has immeasurable effect.
Float glass factory operating condition is relatively stable, and the repair time is few, but for maintenance when the less proposition following two control of heat
Molding formula:
Normal mode: under the conditions of float glass factory nominal situation, system all run in a manner described.
Maintenance model: in the maintenance of float glass factory, the coolant-temperature gage in water tank 39 is lower, under these conditions, thermoelectricity
Combined production device 44 increases inflow, opens the 16th control valve 36, and the second water segregator 38 separates a certain amount of water to water tank 39
Interior water heating, reaches design conditions temperature and leaving water temperature can be used as the high of lithium bromide heat pump at 95~100 DEG C and warm
Source uses.
Lithium bromide heat pump heating device includes cogeneration system 44, lithium bromide heat pump 40, plate heat exchanger 43, heat pump
42, user terminal pipeline 41, water segregator 38, control valve 36, power plant's condensing gas return pipe 45, lithium bromide heat pump high temperature heat source water outlet
47, circulating pump 46.Its main operational principle are as follows: 100 DEG C or so of high-temperature steam introduces power plant as lithium bromide from return pipe 44
The high temperature heat source of heat pump 40；Lithium bromide heat pump high temperature heat source water outlet is discharged (60 DEG C or so), into plate heat exchanger 43 and uses
The water that the hot water that the heat exchange of family end pipe road 41 is 55 DEG C obtains 28~32 DEG C for users to use, after heat exchange is changed by heat pump 42
Heat, leaving water temperature are then sent through power plant's condensing gas return pipe 45 and then send power plant back at 5 DEG C or so.Obtain float glass waste heat
44~45 DEG C of intermediary's water enters the Low Temperature Thermal source of lithium bromide heat pump 40 by control valve 37, and leaving water temperature is on 24~26 DEG C of left sides
The right side, intermediary's water are sent to water segregator 28 by the pressurization of circulating pump 46 and complete intermediary's water circulation.User terminal pipeline output water temperature 34~
36 DEG C, return water water temperature is at 54~55 DEG C.Ladder energy is exported, energy loss is not caused, on the other hand, by float glass, too
For the low-quality heat and power plant steam high-quality heat of positive energy as heat source, heat exchange means make low-quality heat will not nothing
Ample scope for abilities, energy is by more ultimate attainment use and ladder energy utilization.In this process, for cogeneration system, floating
The heat of method glass in the recycling of the water at low temperature after heat exchange, has first used cooling capacity, also realizes simultaneously for recirculated water
It reuses, water resource is more saved.Power plant's high-temperature steam is in use, cogeneration system promotes heat product step by step
Matter, to be formed in the high-temperature water for being suitable for heat exchange, temperature is reachable or close to 100 DEG C.
It during heating in winter, runs in the manner described above, during non-heating, closes the 12nd control valve 16 and the 7th
Control valve 11,37~39 DEG C of water in the hot pond 22 of float glass are cooled to 31~33 DEG C in cooling tower 6 and are re-fed into cold drop 21
In and cooling tower can pass through switch third control valve 7, the 4th control valve 8, the 5th control valve 9, the 6th control valve the 10, the 8th control
Valve 12 processed, the 9th control valve 13, the tenth control valve 14, the 11st control valve 15 are controlled to adjust.
It is expensive in condensed water in power plant in price, and float glass water only uses power plant water work using cheap
For the high temperature heat source of lithium bromide heat pump, intermediary's water of float glass waste heat is obtained as low-temperature heat source.Electricity is substantially reduced
The usage amount of factory's water, improves economic benefit.Power plant water and the intermediary's water recycled from float glass waste heat are unmixed, power plant
Water cleaning, intermediary's water because be in control it is too long may contain impurity, power plant water may be polluted, the usage mode guarantee of not mixed water
The reliability of system.System integrally uses three sets of heating plants, and the reliability of heat supply greatly improved, and has ensured that heating is stablized
This important livelihood issues.
In one embodiment, the arbitrary temperature in the application uses the left and right or about or equivalent non-essence of the temperature
It really indicates to the limit temperature, such as 45 DEG C or so or about 45 DEG C, then it represents that ± 1 degree of section of the temperature indicates exemplary
44~46 DEG C, actual temp numerical value then directly indicates its numerical value temperature, however in a kind of embodiment advanced optimized, for
The direct numerical value of temperature involved in the application indicates, is not understood as ± 1 degree of section of its temperature, such as exchanges heat as 45 degree out
Water, indicate it is exemplary 44~46 DEG C, in addition to have must be indicated by the numerical value except, for example, 100 DEG C of hot water.
The preferable specific embodiment of the above, only the invention, but the protection scope of the invention is not
It is confined to this, anyone skilled in the art is in the technical scope that the invention discloses, according to the present invention
The technical solution of creation and its inventive concept are subject to equivalent substitution or change, should all cover the invention protection scope it
It is interior.
Claims (9)
1. a kind of solar energy waste-heat recovery device, which is characterized in that including solar water heater (34), phase transition heat accumulation unit
(31), water tank (39), temperature sensor (29), the 5th circulating pump (30), the 13rd control valve (32), the 14th control valve
(33), the 15th control valve (35), by piping connection between the loop exit and solar water heater (34) of water tank (39), and
The 15th control valve (35), the outlet pipe branch two-way parallel connection water pipe of solar water heater (34), all the way water is arranged in the line segments
13rd control valve (32) is set on pipe, and is connect with the 5th circulating pump (30), the 14th control is set on another way water pipe
Valve (33) processed, and connect with phase transition heat accumulation unit (31), the 5th circulating pump (30) is connected by phase transition heat accumulation unit (31), the
The loop head of outlet connection water tank (39) of five circulating pumps (30).
2. solar energy waste-heat recovery device as described in claim 1, which is characterized in that the entrance of water tank (39) and heat pump
The high temperature output end of condenser connects or the entrance of water tank (39) is connect with water collector (26).
3. solar energy waste-heat recovery device as claimed in claim 2, which is characterized in that the water collector (26) with one with
On heat pump condenser high temperature output end connection.
4. solar energy waste-heat recovery device as described in claim 1, which is characterized in that the water tank (39) is by heat exchanging pipe
It is connect with the second water segregator (38), it is internal that the heat exchanging segment of heat exchanging pipe is located at water tank (39), and the second water segregator (38) is arranged
In on cogeneration system (44), cogeneration system (44) is connected to lithium bromide heat pump heating via the second water segregator (38) and fills
The high temperature section entrance set.
5. solar energy waste-heat recovery device as claimed in claim 4, which is characterized in that the outlet of water tank (39) is connected by pipeline
It is connected to the low-temperature heat exchange section entrance of lithium bromide heat pump heating device.
6. solar energy waste-heat recovery device as claimed in claim 5, which is characterized in that with the outlet connection of water tank (39)
The pipeline of water supply is provided with the 17th control valve (37).
7. solar energy waste-heat recovery device as claimed in claim 5, which is characterized in that its company of the cogeneration system (44)
It is connected to power plant, vapor (steam) temperature therein is about 100 DEG C, and the temperature of the water exported in the water tank (39) is about 45 DEG C, and by
It is about 45 DEG C that the heat exchanging segment that second water segregator (38) is connect with water tank (39), which maintains the temperature of the water exported in water tank (39),.
8. solar energy waste-heat recovery device as described in claim 1, which is characterized in that it further include temperature sensor (29), temperature
Degree sensor (29) is mounted in water tank (39) to measure water storage temperature.
9. a kind of solar energy waste-heat recovery device, which is characterized in that including solar water heater (34), phase transition heat accumulation unit
(31), water tank (39), temperature sensor (29), the 5th circulating pump (30), the 13rd control valve (32), the 14th control valve
(33), the 15th control valve (35), the second water segregator (38), temperature sensor (29) are mounted in water tank (39), water tank
(39) by piping connection between loop exit and solar water heater (34), and the 15th control valve is set in the line segments
(35), the 13rd control valve (32) is arranged in the outlet pipe branch two-way parallel connection water pipe of solar water heater (34) all the way on water pipe,
And connect with the 5th circulating pump (30), the 14th control valve (33), and and phase transition heat accumulation unit are set on another way water pipe
(31) it connects, connects the 14th circulating pump by phase transition heat accumulation unit (31), the outlet of the 14th circulating pump connects water tank
(39) loop head；The entrance of water tank (39) is connect with water collector (26), and the 4th circulating pump is arranged on the pipeline of connection
(27), water collector (26) is connect with the high temperature output end of the condenser of more than one heat pump；Water tank (39) is by heat exchanging pipe
It is connect with water segregator, it is internal that the heat exchanging segment of heat exchanging pipe is located at water tank (39), and the second water segregator (38) is set to thermoelectricity connection
It producing on device (44), cogeneration system (44) is connected to the high temperature section entrance of lithium bromide heat pump heating device via water segregator,
By the low-temperature heat exchange section entrance of piping connection to lithium bromide heat pump heating device, the pipeline of the connection set for the outlet of water tank (39)
It is equipped with the 17th control valve (37).
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| CN201811565148.4A CN109595669A (en) | 2018-12-20 | 2018-12-20 | Solar energy waste-heat recovery device |
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Application publication date: 20190409 |