CN109595668A - The concurrent heating of solar energy and lithium bromide heat pump and heating installation - Google Patents
The concurrent heating of solar energy and lithium bromide heat pump and heating installation Download PDFInfo
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- CN109595668A CN109595668A CN201811565105.6A CN201811565105A CN109595668A CN 109595668 A CN109595668 A CN 109595668A CN 201811565105 A CN201811565105 A CN 201811565105A CN 109595668 A CN109595668 A CN 109595668A
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- AMXOYNBUYSYVKV-UHFFFAOYSA-M lithium bromide Chemical compound [Li+].[Br-] AMXOYNBUYSYVKV-UHFFFAOYSA-M 0.000 title claims abstract description 188
- 238000010438 heat treatment Methods 0.000 title claims abstract description 54
- 238000009434 installation Methods 0.000 title claims abstract description 10
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 385
- 239000002918 waste heat Substances 0.000 claims abstract description 39
- JEGUKCSWCFPDGT-UHFFFAOYSA-N h2o hydrate Chemical compound O.O JEGUKCSWCFPDGT-UHFFFAOYSA-N 0.000 claims abstract description 25
- 238000011084 recovery Methods 0.000 claims abstract description 23
- 238000009825 accumulation Methods 0.000 claims description 22
- 230000007704 transition Effects 0.000 claims description 17
- 230000009466 transformation Effects 0.000 claims description 2
- 230000001172 regenerating effect Effects 0.000 claims 1
- 238000001704 evaporation Methods 0.000 abstract description 12
- 238000004064 recycling Methods 0.000 abstract description 8
- 230000000694 effects Effects 0.000 abstract description 5
- 230000001737 promoting effect Effects 0.000 abstract description 4
- 238000009826 distribution Methods 0.000 abstract description 2
- 239000005329 float glass Substances 0.000 description 40
- 238000001816 cooling Methods 0.000 description 21
- 238000000034 method Methods 0.000 description 13
- 238000003860 storage Methods 0.000 description 13
- 230000004087 circulation Effects 0.000 description 12
- WHXSMMKQMYFTQS-UHFFFAOYSA-N Lithium Chemical compound [Li] WHXSMMKQMYFTQS-UHFFFAOYSA-N 0.000 description 9
- 229910052744 lithium Inorganic materials 0.000 description 9
- 230000008859 change Effects 0.000 description 6
- 239000000498 cooling water Substances 0.000 description 6
- 230000005855 radiation Effects 0.000 description 6
- 230000008901 benefit Effects 0.000 description 5
- 230000031709 bromination Effects 0.000 description 5
- 238000005893 bromination reaction Methods 0.000 description 5
- 230000005611 electricity Effects 0.000 description 5
- 238000009413 insulation Methods 0.000 description 5
- 239000000446 fuel Substances 0.000 description 4
- 238000002156 mixing Methods 0.000 description 4
- 238000002360 preparation method Methods 0.000 description 4
- 239000000284 extract Substances 0.000 description 3
- 238000004519 manufacturing process Methods 0.000 description 3
- 230000008569 process Effects 0.000 description 3
- WKBOTKDWSSQWDR-UHFFFAOYSA-N Bromine atom Chemical compound [Br] WKBOTKDWSSQWDR-UHFFFAOYSA-N 0.000 description 2
- GDTBXPJZTBHREO-UHFFFAOYSA-N bromine Substances BrBr GDTBXPJZTBHREO-UHFFFAOYSA-N 0.000 description 2
- 229910052794 bromium Inorganic materials 0.000 description 2
- 230000008878 coupling Effects 0.000 description 2
- 238000010168 coupling process Methods 0.000 description 2
- 238000005859 coupling reaction Methods 0.000 description 2
- 239000007789 gas Substances 0.000 description 2
- 239000012774 insulation material Substances 0.000 description 2
- 238000010025 steaming Methods 0.000 description 2
- 239000002699 waste material Substances 0.000 description 2
- 206010021036 Hyponatraemia Diseases 0.000 description 1
- ZBBLARZXVZFXMM-UHFFFAOYSA-N [Br-](Br)Br.[Li+] Chemical compound [Br-](Br)Br.[Li+] ZBBLARZXVZFXMM-UHFFFAOYSA-N 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
- 238000005265 energy consumption Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000008020 evaporation Effects 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
- 150000002641 lithium Chemical class 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000005457 optimization Methods 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
- 239000008400 supply water Substances 0.000 description 1
- 239000003643 water by type 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)
- Chemical & Material Sciences (AREA)
- Physics & Mathematics (AREA)
- Mechanical Engineering (AREA)
- Thermal Sciences (AREA)
- General Engineering & Computer Science (AREA)
- Combustion & Propulsion (AREA)
- Materials Engineering (AREA)
- Heat-Pump Type And Storage Water Heaters (AREA)
Abstract
The concurrent heating of solar energy and lithium bromide heat pump and heating installation, belong to the recycling of heat supply waste heat and heat distribution field, in order to solve to improve evaporating temperature, evaporating temperature is set to be maintained at the operational efficiency for promoting solar energy waste-heat recovery device in certain temperature, and ladder utilizes energy, the problem of greatly reducing energy loss, 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, the water out of the steam water heat exchanger of entrance connection power plant's cogeneration system of the high-temperature heat transfer section, the entrance of the high temperature heat exchanging water pipe of the outlet connecting plate type heat exchanger of high-temperature heat transfer section, the first entrance of the outlet connection water-water jet of the high temperature heat exchanging water pipe of plate heat exchanger, effect is by lithium bromide heat pump and plate heat exchanger bi-directional association , realize ladder energy utilization.
Description
Technical field
The invention belongs to the recycling of heat supply waste heat and heat distribution field, are related to the concurrent heating of a kind of solar energy and lithium bromide heat pump
And heating installation.
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 to improve evaporating temperature, it is maintained at evaporating temperature in certain temperature to promote solar energy waste heat recycling dress
The operational efficiency set, and ladder utilizes energy, very big the problem of reducing energy loss, the following technical solutions are proposed by the present invention:
A kind of concurrent heating and the heating installation of solar energy and lithium bromide heat pump, including solar energy waste-heat recovery device and lithium bromide
Heat pump heating device；
The 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；The outlet of the water tank is connected to the second entrance of water-water jet by water supplying pipe；
The lithium bromide heat pump heating device, including lithium bromide heat pump, the 4th heat pump, plate heat exchanger, water-water jet and
Breeching；The lithium bromide heat pump includes high-temperature heat transfer section, low-temperature heat exchange section, medium temperature heat exchanging segment, the connection of medium temperature heat exchanging segment
First output pipe, plate heat exchanger include high temperature heat exchanging water pipe and low-temperature heat exchange water pipe, and the connection second of low-temperature heat exchange water pipe is defeated
Pipeline out, heat pump include evaporator and condenser, and condenser connects third output pipe；The entrance of the high-temperature heat transfer section connects
Connect the water out of the steam water heat exchanger of power plant's cogeneration system, the high temperature of the outlet connecting plate type heat exchanger of high-temperature heat transfer section
The entrance of heat exchanging water pipe, the first entrance of the outlet connection water-water jet of the high temperature heat exchanging water pipe of plate heat exchanger, water supplying pipe connection
The second entrance of water-water jet, the entrance of the outlet connection low-temperature heat exchange section of water-water jet, the outlet of low-temperature heat exchange section connects water segregator
Entrance, the first outlet of the second water segregator are divided into two branches, and the first branch of first outlet connects the evaporator of the 4th heat pump
The second outlet of high temperature water inlet, the second water segregator connects the first water segregator.
The utility model has the advantages that system opens phase transition heat accumulation unit and releases its thermal energy stored in accumulation of heat mode, evaporation is improved
Temperature makes evaporating temperature be maintained at the operational efficiency for promoting solar energy waste-heat recovery device in certain temperature.Heat pump realizes
Ladder energy utilization, such as the first output pipe, the second output pipe, third output pipe are user's output pipe, are heating pipes
Road is associated with by lithium bromide heat pump and plate heat exchanger bi-directional association, and by lithium bromide heat pump with the 4th heat pump, this heating installation
Between association so that device convenient for exporting scheduled ladder energy, very big reduction energy loss.
Detailed description of the invention
Fig. 1 is the pipeline connecting figure of apparatus of the present 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. water tanks, 38. lithium bromide heat pumps,
39. the 4th heat pump, 40. plate heat exchangers, 41. user end pipelines, 42. steam water heat exchangers, 43. water-water jets,
44. the 17th control valve, 45. shunt valves, 46. second water segregators, 47. the 6th circulating pumps, 48. steam heat pump units, 49. first
Lithium bromide heat pump unit, 50. second lithium bromide heat pump units, 51. third lithium bromide heat pump units, 52. steam turbines, 53. is weary
Vapour device.
Specific embodiment
Embodiment 1:
One kind integrating a variety of waste heat coupling heating systems, including the recycling of float glass waste-heat recovery device, solar energy waste heat
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 (37), the condenser of heat pump (23,24,25)
Cold end input is the first water segregator (28), and the first water segregator (28) connects the second water segregator (46) of lithium bromide heat pump heating device
Second outlet.
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 (37) 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 second outlet of the second water segregator (46) of lithium bromide heat pump heating device, by bromination
Return water after lithium heat pump heat exchanging is as 24~26 DEG C of intermediary's water, to form intermediary's water of float glass waste heat recycling by the sun
Energy waste-heat recovery device reheats, and changes the partial heat and the high-temperature-hot-water of power plant together in lithium bromide heat pump heating device
Heat gives user's pipeline, using float glass waste heat and solar energy waste heat as such as heating source, and having after heat exchange is relatively steady
Determine cold end of the intermediary's water of low temperature for the condenser end of heat pump unit to export, circulation participates in heat exchange, plays water and heat
To the effect of saving.
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 (33), phase transition heat accumulation unit (31), water tank
(37), temperature sensor (29), the 5th circulating pump (30), the 13rd control valve (32), the 14th control valve (34), the 15th control
Valve (35) processed by piping connection between the loop exit and solar water heater (34) of water tank (37), 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 (34) 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 (37) loop head.The entrance of water tank (37) 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 second entrance of the connection water-water jet (43) of water tank (37) the outlet lithium bromide heat pump unit.The storage
The connecting pipeline of water pot (37) and water-water jet is provided with the 16th control valve (36), the i.e. confession with the outlet connection of water tank (37)
The pipeline of water is provided with the 16th control valve (36) for controlling solar energy waste-heat recovery device to lithium bromide heat pump heating
The water and speed of unit feeding water storage.Power plant's condensing gas introduces pipe (41), and it is connected to power plant, vapor (steam) temperature therein
About 100 DEG C, the temperature of the middle water exported of the water tank (37) is about 45 DEG C.Temperature sensor (29) is mounted on water tank
(37) to measure water storage temperature in.
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 (34), opens the 13rd control valve (32),
Extract the water in water tank (37) by the 5th circulating pump (30) by the loop exit of water tank (37), and by solar water
Device (33) heats the water in water tank (37), and via the pipeline for being equipped with the 13rd control valve (32), by the water after heating
Water tank (37) directly are extracted to, by the recirculated water inlet return of water tank (37) to water tank (37)；Recycle above-mentioned water storage
Heat cycles, until mode changes or the measured value of the temperature sensor (29) in water tank (37) 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 (34), starts phase transition heat accumulation unit (31), makes to store up
Water in water pot (37) is extracted by the loop exit of water tank (37) by the 5th circulating pump (30), and by solar water heater
(33) water in water tank (37) 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, evaporating 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
(34), start phase transition heat accumulation unit (31), make the water in water tank (37) by the loop exit of water tank (37) by the 5th circulation
Pump (30) extracts, and is heated by solar water heater (33) to the water in water tank (37), 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 evaporating temperature,
Evaporating 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 (37) is to supply water tank (37)
Water.The second entrance of the outlet water-water jet (43) of the water tank (37), and deposited from water collector 26 to the conveying of water tank 37
Water storage, storage water is 45 DEG C.
Lithium bromide heat pump heating device, including it is lithium bromide heat pump (38), the 4th heat pump (39), plate heat exchanger (40), mixed
Hydrophone (43) and the second water segregator (46)；The lithium bromide heat pump (38) includes that high-temperature heat transfer section, low-temperature heat exchange section, medium temperature are changed
Hot arc, medium temperature heat exchanging segment connect the first output pipe, and plate heat exchanger (40) includes high temperature heat exchanging water pipe and low-temperature heat exchange water pipe,
Low-temperature heat exchange water pipe connects the second output pipe, and heat pump includes evaporator and condenser, and condenser connects third output pipe；Institute
The water out of the steam water heat exchanger (42) of the entrance connection power plant's cogeneration system for the high-temperature heat transfer section stated, high-temperature heat transfer section
Outlet connecting plate type heat exchanger (40) high temperature heat exchanging water pipe entrance, the high temperature heat exchanging water pipe of plate heat exchanger (40) go out
The first entrance of mouth connection water-water jet (43), water supplying pipe connect the second entrance of water-water jet (43), and the outlet of water-water jet (43) connects
The entrance of low-temperature heat exchange section is connect, the outlet of low-temperature heat exchange section connects the entrance of water segregator, the first outlet point of the second water segregator (46)
For two branches, the first branch of first outlet connects the high temperature water inlet of the evaporator of the 4th heat pump (39), the second water segregator
(46) second outlet connects the first water segregator (28).
The outlet connection of water supplying pipe connection water tank (37), the low temperature water outlet of the evaporator of the 4th heat pump (39)
The low-temperature inlet of the condenser of the steam heat pump unit (48) of connection power plant's cogeneration system, second of the first outlet
Road connects the middle temperature-heat-source of the first lithium bromide heat pump unit (49) of power plant's cogeneration system.The water supplying pipe installation the tenth
Six control valves (36).The Pipe installing the 6th that the second outlet of second water segregator (46) is connect with the first water segregator (28)
Circulating pump (47).First output pipe, the second output pipe, third output pipe are user's output pipe, are heating pipelines.
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 steam water heat exchanger (42) is connected to bromination
The high-temperature heat transfer section of lithium heat pump (38), and high temperature heat-exchanging water (100 DEG C) are conveyed to it, the outlet connecting plate type of high-temperature heat transfer section changes
The entrance of the high temperature heat exchanging water pipe of hot device (40), and high temperature heat-exchanging water (70 DEG C), the high temperature of plate heat exchanger (40) are exported to it
The first entrance of outlet connection water-water jet (43) of heat exchanging water pipe, and heat exchange cold water (50 DEG C) is exported to it, water supplying pipe connection is mixed
The second entrance of hydrophone (43), and storage water (45 DEG C) is exported to it, heat exchange cold water mixes in water-water jet (43) with storage water
It is formed mixing water (46 DEG C), the entrance of the outlet connection low-temperature heat exchange section of water-water jet (43), and exports mixing water to it, low temperature changes
The entrance of the outlet connection water segregator of hot arc, and exports low-temperature heat exchange water (25 DEG C) to it, and low-temperature heat exchange water is by the of water segregator
One outlet and second outlet output, the first branch of two branches of first outlet branch, first outlet connect the 4th heat pump (39)
Evaporator high temperature water inlet, and low-temperature heat exchange water is exported to it, by the low temperature water outlet of the evaporator of the 4th heat pump (39)
It exports water at low temperature (5 DEG C), the second outlet of water segregator connects the first water segregator (28), and low-temperature heat exchange water (25 is exported to it
DEG C), medium temperature heat exchanging segment and high-temperature heat transfer section and low-temperature heat exchange section exchange heat, and connect the first output pipe to supply the first output water
(60 DEG C), high temperature heat exchanging water pipe and low-temperature heat exchange water pipe exchange heat, and connect the second output pipe to supply the second output water (55
DEG C), evaporator and condenser exchange heat, and connect third output pipe to supply third output water (45 DEG C).
The low temperature of the condenser of low temperature water outlet connection steam heat pump unit (48) of the evaporator of 4th heat pump (39) enters
Mouthful, and the condensers of (5 DEG C) of water at low temperature supplies steam heat pump unit (48) are exported to it, the second branch connection the of first outlet
The middle temperature-heat-source of monobromination lithium heat pump unit (49), and the middle temperature-heat-source of the first lithium bromide heat pump unit (49) supply medium temperature is changed
Hot water (25 DEG C).The three tunnels output of the water segregator 28 is connected to the cold end of the condenser of heat pump (23,24,25), supplies it
Low-temperature heat exchange water (25 DEG C).
Power plant's cogeneration system that the above-mentioned apparatus is related to, including steam exhaust device (53), steam turbine (52), steaming
Vapour heat pump unit (48), the first lithium bromide heat pump unit (49), the second lithium bromide heat pump unit (50), third lithium bromide heat pump machine
Group (51), each lithium bromide heat pump unit include high temperature heat source, low-temperature heat source and middle temperature-heat-source, and steam exhaust device (53) are changed
Pipe line is connected to the evaporator of steam heat pump unit (48) and the low-temperature heat source of each lithium bromide heat pump unit, the vapor wheel parallel
The heat exchanging pipe of machine (52) is connected to the high temperature heat source of each lithium bromide heat pump unit, the high-temperature water outlet mouth connection first of condenser parallel
The entrance of the middle temperature-heat-source of lithium bromide heat pump unit (49) is connected to, the outlet and the second bromination of the first lithium bromide heat pump unit (49)
The entrance of the middle temperature-heat-source of lithium heat pump unit (50) is connected to, the outlet of the middle temperature-heat-source of the second lithium bromide heat pump unit (50) and the
The entrance of the middle temperature-heat-source of tribromide lithium heat pump unit (51) is connected to.
The entrance connection inlet tube of steam exhaust device (53), outlet connection outlet pipe, inlet tube, outlet parallel arranged,
Inlet tube is connected to the outlet of the low-temperature heat source of third lithium bromide heat pump unit (51), and outlet is connected to third lithium bromide heat pump unit
(51) the entrance parallel connection of the entrance of low-temperature heat source, the low-temperature heat source of the second lithium bromide heat pump unit (50) accesses the outlet
Pipe, exports the access inlet tube in parallel, and the entrance parallel connection of the low-temperature heat source of the first lithium bromide heat pump unit (49) accesses institute
Outlet is stated, the access inlet tube in parallel is exported, the entrance connection outlet pipe of the evaporator of steam heat pump unit (48) steams
The outlet of the evaporator of vapour heat pump unit (48) connects inlet tube；
The entrance connection inlet tube of steam turbine (52), outlet connection outlet pipe, inlet tube, outlet parallel arranged,
Inlet tube is connected to the vapor outlet of steam water heat exchanger (42), and outlet is connected to the vapour entrance of steam water heat exchanger (42), third bromination
The entrance parallel connection of the high temperature heat source of lithium heat pump unit (51) accesses the outlet, exports the access inlet tube in parallel, the
The entrance parallel connection of the high temperature heat source of dibrominated lithium heat pump unit (50) accesses the outlet, exports the access entrance in parallel
The entrance parallel connection of pipe, the high temperature heat source of the first lithium bromide heat pump unit (49) accesses the outlet, exports access institute in parallel
State inlet tube, the entrance connection outlet pipe of the evaporator of steam heat pump unit (48), the evaporator of steam heat pump unit (48)
Outlet connection inlet tube.
The water inlet of the outlet steam water heat exchanger (42) of the middle temperature-heat-source of third lithium bromide heat pump unit (51).Institute
4th heat pump (39) of the low temperature water inlet connection lithium bromide heat pump heating device of the condenser for the steam heat pump unit (48) stated
Evaporator low temperature water outlet.The low-temperature heat source of the first lithium bromide heat pump unit (49) is also connected with the confession of lithium bromide heat pump
The second branch of the first outlet of the water segregator of heater device.The first branch installs the 17th control valve (44).
The execution method of above-mentioned apparatus is as follows: a kind of power plant's cogeneration method, 5 DEG C or so of power plant water enter steam heat
The cold water inlet of the condenser of pump assembly (48), by steam exhaust device (53) generate steam exhaust water steam heat pump unit (48) steaming
5 DEG C or so of power plant water for sending out the condenser end of device end and steam heat pump unit (48) exchanges heat, by steam heat pump unit (48)
Condenser end exports 30 DEG C or so of level-one heat-exchanging water, and level-one heat-exchanging water enters the middle warm of the first lithium bromide heat pump unit (49)
Source simultaneously intakes as it；The steam exhaust water that steam exhaust device (53) generates enters the first lithium bromide heat pump unit (49) and is used as Low Temperature Thermal
Source, 100 DEG C of the high-temperature steam that steam turbine (52) generates enter the first lithium bromide heat pump unit (49) and are used as high temperature heat source, the
50 DEG C of water outlet or so of secondary heat exchange water of the middle temperature-heat-source of monobromination lithium heat pump unit (49)；Steam exhaust device (53) generates weary
Carbonated drink enters the second lithium bromide heat pump unit (50) and is used as low-temperature heat source, and the high-temperature steam that steam turbine (52) generates enters second
Lithium bromide heat pump unit (50) be used as high temperature heat source, 70 DEG C of water outlet or so of the middle temperature-heat-source of the second lithium bromide heat pump unit (50)
Three-level heat-exchanging water；The steam exhaust water that steam exhaust device (53) generates enters third lithium bromide heat pump unit (51) and is used as low-temperature heat source,
The high-temperature steam that steam turbine (52) generates enters third lithium bromide heat pump unit (51) as high temperature heat source, third lithium bromide heat
90 DEG C of water outlet or so of level Four heat-exchanging water of the middle temperature-heat-source of pump assembly (51), level Four heat-exchanging water enter steam water heat exchanger (42)
And the high-temperature steam generated with steam turbine (52) exchanges heat, and 100 DEG C of hot water is exported by steam water heat exchanger (42).
Evaporator of 5 DEG C or so of the power plant water from the 4th heat pump (39) of lithium bromide heat pump heating device.
The water inlet of the middle temperature-heat-source of first lithium bromide heat pump unit (49) further includes from lithium bromide heat pump heating device
25 DEG C of water inlet of the second branch of the first outlet of water segregator.
Above-mentioned lithium bromide heat pump heating device and method, realizes ladder energy utilization, such as the first output pipe, second defeated
Pipeline, third output pipe are user's output pipe out, are heating pipelines, i.e. the coolant-temperature gage that enters of the first output pipe is 45 DEG C,
It is 60 DEG C that its leaving water temperature, which is exchanged heat, by lithium bromide heat pump 38 and 40 bi-directional association of plate heat exchanger, so that the second output pipe
The coolant-temperature gage that enters be 36 DEG C, it is 55 DEG C that leaving water temperature, which is exchanged heat, and lithium bromide heat pump 38 is associated with the 4th heat pump 39 so that
The coolant-temperature gage that enters of third output pipe is 36 DEG C, and it is 45 DEG C that leaving water temperature, which is exchanged heat, the association between this heating installation so that
Device does not cause energy loss convenient for exporting scheduled ladder energy, on the other hand, by float glass, solar energy it is low-quality
Heat and power plant steam high-quality heat are as heat source, and heat exchange means make low-quality heat lack scope for their abilities, energy
Amount is by more ultimate attainment use and ladder energy utilization.In this process, for the heat of cogeneration system, float glass
It measures, in the recycling of the water at low temperature after heat exchange, has first used cooling capacity, also realizing repetition simultaneously for recirculated water makes
With more being saved for water resource.Power plant's high-temperature steam is in use, cogeneration system promotes heat quality step by step, to be formed
In the high-temperature water for being suitable for heat exchange, temperature is reachable or close to 100 DEG C.
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.
Embodiment 2:
A kind of residual heat of electric power plant, solar energy, float glass waste heat couple heating system, and whole system is returned by float glass waste heat
Receiving apparatus, solar energy waste-heat recovery device, lithium bromide heat pump heating device three parts are constituted.
Float glass waste-heat recovery device main operational principle is: when winter condition carries out waste heat recycling, by float glass
37~39 DEG C of the recirculated water containing a large amount of low-temperature waste heats that workshop 1 generates is discharged into hot pond 22, is followed by third circulating pump 18, second
17 pressurization of ring pump, opens the 8th control valve 12, the 9th control valve 13, the tenth control valve 14, the 11st control valve 15 at this time, closes
Third control valve 7, the 4th control valve 8, the 5th control valve 9, the 6th control valve 10；These recirculated waters are introduced into the first heat pump
23, the second heat pump 24, in third heat pump 25, the return water that intermediary's water heat exchange with 24~26 DEG C is 31~33 DEG C or so, by control
Valve 16 processed is passed through cooling tower 6, is then discharged into cold drop 21.The water of cold drop 21 is pressurizeed by circulating pump 5 by the second control opened
Valve 4 is sent into float glass workshop 1 and is used as float glass cooling water.In the state of power-off, the second control valve 4 is closed, the
One control valve 3 is opened, and the water in preparation water tank 2 can provide 15 minutes cooling waters for workshop 1.
Solar energy waste-heat recovery device main operational principle are as follows: the first heat pump 23, the second heat pump 24, third heat pump 25 will be by
24-25 DEG C of the cooling water that first water segregator 28 is drawn is sent into water collector 26 after being heated to 34-36 DEG C, then by the 4th circulation
Water tank 37 is sent into 27 pressurization of pump；Water in water tank 37 is heated to 45 DEG C by solar energy equipment, opens the 16th control valve,
Water is sent to water-water jet 43 and carries out mixed water.
Solar energy waste-heat recovery device has following 3 kinds of operating modes:
1. normal mode
When solar radiation intensity is suitble to, control valve 32 is closed, and control valve 34 is opened, and device does not need to open phase transformation storage
Thermal 31 directly heats the water in water pot 37.
2. energy accumulation mode
When solar radiation intensity is excessive, control valve 34 is closed, and control valve 32 is opened, and system opens phase transition heat accumulation unit
31, excessive thermal energy is stored, evaporating temperature is made to be maintained at the operation effect for promoting solar energy waste-heat recovery device in certain temperature
Rate.
3. glow mode
When solar radiation intensity is insufficient or temperature sensor 29 measures that water temperature is too low in a period of time, the 14th control
Valve 34 processed is closed, and the 13rd control valve 32 is opened.System opens phase transition heat accumulation unit 31 and releases it and stores in accumulation of heat mode
Thermal energy, improve evaporating temperature, so that evaporating temperature is maintained at the operation for promoting solar energy waste-heat recovery device in certain temperature
Efficiency.
Lithium bromide heat pump heating device main operational principle are as follows: lithium bromide heat pump heating device include steam water heat exchanger 42,
Lithium bromide heat pump 38, heat pump 39, plate heat exchanger 40, user terminal pipeline 41, circulating pump 47, control valve 44.Its groundwork is former
Reason are as follows: 100 DEG C or so of high-temperature steam introduces high temperature heat source of the power plant as lithium bromide heat pump 38 from steam water heat exchanger 42；Bromine
Change lithium heat pump high temperature heat source water outlet water outlet (70 DEG C or so), is 55 DEG C into plate heat exchanger 40 and the heat exchange of user terminal pipeline 41
For users to use, leaving water temperature is at 25 DEG C or so for the hot water of left and right.Obtain 44~45 DEG C of intermediary's water warp of float glass waste heat
The Low Temperature Thermal source that control valve 36 enters lithium bromide heat pump 38 is crossed, leaving water temperature is at 24~26 DEG C or so, and intermediary's water is by circulation
42 pressurization of pump is sent to water segregator 28 and completes intermediary's water circulation.When heat pump 39 works, the 41 return water temperature of user terminal pipeline at 39 end of heat pump
Degree is at 45 DEG C or so, and output water temperature is at 36 DEG C or so.The 41 return water water temperature of user terminal pipeline at 38 end of lithium bromide heat pump is on 60 DEG C of left sides
The right side, output water temperature is at 45 DEG C or so.
The switching control of the invention being characterized in that herein: since power plant water is expensive, having to valuate by water,
Some is valuated by consumption of calorie；It valuates in power plant by water and 41 demand load of user terminal pipeline is larger or user terminal pipeline 41
When demand load is excessive, opening controlling valve 44 and heat pump 39 make 25 DEG C or so of water enter heat pump 39, and leaving water temperature is on 5 DEG C of left sides
The right side, then send water outlet back to power plant；It can negotiate with power plant, from economy and optimization system, so that a part of water is entered heat pump 39 and return again
Power plant, a part of water are directly wired back factory.
100 DEG C or so of high-temperature steam introduces high temperature heat source of the power plant as lithium bromide heat pump 38 from steam water heat exchanger 42；
The water outlet of lithium bromide heat pump high temperature heat source water outlet, leaving water temperature is at 70 DEG C or so, into plate heat exchanger 40 and user terminal pipeline
41 36 DEG C or so of plate heat exchanger exchanges heat, and obtains 55 DEG C or so of hot water and uses for user terminal fan coil, water outlet
Temperature is at 50 DEG C or so.Water outlet is sent to the useless containing float glass low temperature of 45 DEG C of water-water jet 43 and solar water heater heating
Intermediary's water of heat carries out mixed water, and water temperature is at 46 DEG C or so after mixing water.Mixed water is sent into lithium bromide heat pump 38 and is used as low-temperature heat source,
For leaving water temperature at 25 DEG C or so, water outlet is then sent through water segregator 46.Water segregator 46 separates the equivalent introduced with steam water heat exchanger 42
Water sends power plant back to, and water segregator 46 separates remaining water pressurization and is sent to the completion intermediary's water circulation of water segregator 28.When heat pump 39 works, beat
Control valve 44 is opened, 25 DEG C of water is introduced into heat pump 39 as the user terminal of heat source and heat pump 39 and is exchanged heat, return water temperature is at 5 DEG C
Left and right, is introduced directly into steam heat pump unit 48 and exchanges heat.When heat pump 39 does not work, control valve 44 is closed, is divided by water segregator 46
25 DEG C of water for supplying power plant out is introduced directly into lithium bromide heat pump unit 49.41 output water temperature of user terminal pipeline at heat pump end 39 exists
36 DEG C or so, return water water temperature is at 45 DEG C or so.The user terminal pipeline return water water temperature at lithium bromide heat pump end is discharged water at 60 DEG C or so
Temperature is at 45 DEG C or so.
Power plant's cogeneration of heat and power partial devices include steam heat pump unit 48, steam lithium bromide heat pump unit 49, steam bromination
Lithium heat pump unit 50, steam lithium bromide heat pump unit 51, steam-turbine plant 52, steam electric power generator 53.Its main operational principle
Are as follows: when heat pump 39 works, control valve 44 is opened, enters steam heat pump via the power plant water for obtaining 5 DEG C or so after heat pump 39 also heat
The steam exhaust heat exchange that the water that 48,5 DEG C of unit generates in steam heat pump unit 48 with steam electric power generator 53 makes water temperature be increased to 30
DEG C or so, 30 DEG C or so of water enters 49 medium temperature heat source side of next stage steam lithium bromide heat pump unit.Steam lithium bromide heat pump machine
Group 49 obtains 30 DEG C or so of the water provided by higher level's steam heat pump unit 48 and water segregator 46 gives bromine when heat pump 39 does not work
Change temperature-heat-source in 25 DEG C or so of the power plant water mixing conduct of lithium heat pump unit 49, the high-temperature steam that steam-turbine plant 52 generates is made
For high temperature heat source, 50 DEG C or so of water is obtained and has entered temperature-heat-source in the conduct of next stage steam lithium bromide heat pump unit 50.Steam
Lithium bromide heat pump unit 50 obtains temperature-heat-source in 50 DEG C or so of the water provided by higher level's steam lithium bromide heat pump unit 49 conduct,
The high-temperature steam that steam-turbine plant 52 generates has obtained 70 DEG C or so of water and has entered next stage steam lithium bromide as high temperature heat source
Temperature-heat-source in the conduct of heat pump unit 51.Steam lithium bromide heat pump unit 51 obtains being provided by higher level's steam lithium bromide heat pump unit 50
70 DEG C or so of water be used as in temperature-heat-source, steam-turbine plant 52 generate high-temperature steam as high temperature heat source, obtained 90 DEG C
The water of left and right, 100 DEG C or so of the high-temperature steam that steam-turbine plant 52 generates is toward steam water heat exchanger 42.The high-temperature steam is in vapour-
Described 90 DEG C or so of power plant water is heated to 100 DEG C of power plant water, and the height as lithium bromide heat pump 38 at water- to-water heat exchanger 42
Temperature-heat-source uses.Ladder energy is exported, energy loss is not caused, on the other hand, by the low-quality heat of float glass, solar energy
Amount is with power plant steam high-quality heat as heat source, and heat exchange means make low-quality heat lack scope for their abilities, energy
By more ultimate attainment use and ladder energy utilization.In this process, for the heat of cogeneration system, float glass,
In the recycling of water at low temperature after heat exchange, cooling capacity has first been used, has also realized reuse simultaneously for recirculated water, it is right
It is more saved in water resource.Power plant's high-temperature steam is suitable to be formed in use, cogeneration system promotes heat quality step by step
In the high-temperature water of heat exchange, temperature is reachable or close to 100 DEG C.
It is expensive in condensed water in power plant in price, and float glass water only uses power plant water work using cheap
Intermediary's water for the high temperature heat source of lithium bromide heat pump, float glass waste heat provides a large amount of low-temperature heat source.Drastically reduce electricity
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, electricity
The cleaning of factory's water, intermediary's water because be in control it is too long may contain impurity, power plant water may be polluted, the circuit design side of not mixed water
Formula has ensured the reliability of system.System integrally uses three sets of heating plants, and the reliability of heat supply greatly improved, and has ensured confession
It is warm to stablize this important livelihood issues.Heat pump is utilized and widens the temperature difference, saves space, small room is suitble to use.It can either solve
Certainly because caused heat supply and demand mismatch problem when water shortage underrun overhauls in severe cold weather or float glass factory,
Also be able to satisfy user's end load it is normal when use heat demand, realize energy ladder utilize, meet the basic reason of energy-saving and emission-reduction
It reads, saves economic cost, increase economic efficiency.
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 (1)
1. concurrent heating and the heating installation of a kind of solar energy and lithium bromide heat pump, which is characterized in that recycle and fill including solar energy waste heat
It sets and lithium bromide heat pump heating device；
The solar energy waste-heat recovery device, including solar water heater (33), phase transition heat accumulation unit (31), water tank (37),
Temperature sensor (29), the 5th circulating pump (30), the 13rd control valve (32), the 14th control valve (34), the 15th control valve
(35), by piping connection between the loop exit of water tank (37) and solar water heater (34), and it is arranged the tenth in the line segments
Five control valves (35), the outlet pipe branch two-way parallel connection water pipe of solar water heater (34), all the way the 13rd control of setting on water pipe
Valve (32) processed, and connect with the 5th circulating pump (30), the 14th control valve (34), and and phase transformation are set on another way water pipe
Regenerative apparatus (31) connection connects the 5th circulating pump (30) by phase transition heat accumulation unit (31), and the 5th circulating pump (30) goes out
The loop head of mouth connection water tank (37)；The outlet of the water tank (37) is entered by the second of water supplying pipe connection water-water jet (43)
Mouthful；
The lithium bromide heat pump heating device, including it is lithium bromide heat pump (38), the 4th heat pump (39), plate heat exchanger (40), mixed
Hydrophone (43) and the second water segregator (46)；The lithium bromide heat pump (38) includes that high-temperature heat transfer section, low-temperature heat exchange section, medium temperature are changed
Hot arc, medium temperature heat exchanging segment connect the first output pipe, and plate heat exchanger (40) includes high temperature heat exchanging water pipe and low-temperature heat exchange water pipe,
Low-temperature heat exchange water pipe connects the second output pipe, and heat pump includes evaporator and condenser, and condenser connects third output pipe；Institute
The water out of the steam water heat exchanger (42) of the entrance connection power plant's cogeneration system for the high-temperature heat transfer section stated, high-temperature heat transfer section
Outlet connecting plate type heat exchanger (40) high temperature heat exchanging water pipe entrance, the high temperature heat exchanging water pipe of plate heat exchanger (40) go out
The first entrance of mouth connection water-water jet (43), water supplying pipe connect the second entrance of water-water jet (43), and the outlet of water-water jet (43) connects
The entrance of low-temperature heat exchange section is connect, the outlet of low-temperature heat exchange section connects the entrance of water segregator, the first outlet point of the second water segregator (46)
For two branches, the first branch of first outlet connects the high temperature water inlet of the evaporator of the 4th heat pump (39), the second water segregator
(46) second outlet connects the first water segregator (28).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201811565105.6A CN109595668A (en) | 2018-12-20 | 2018-12-20 | The concurrent heating of solar energy and lithium bromide heat pump and heating installation |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
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