CN108344202A - Combined thermal storage heat pump system - Google Patents
Combined thermal storage heat pump system Download PDFInfo
- Publication number
- CN108344202A CN108344202A CN201810077488.6A CN201810077488A CN108344202A CN 108344202 A CN108344202 A CN 108344202A CN 201810077488 A CN201810077488 A CN 201810077488A CN 108344202 A CN108344202 A CN 108344202A
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- CN
- China
- Prior art keywords
- heat pump
- absorption
- heat
- subsystem
- combined thermal
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
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- 238000010521 absorption reaction Methods 0.000 claims abstract description 58
- 238000005338 heat storage Methods 0.000 claims abstract description 41
- 238000006243 chemical reaction Methods 0.000 claims abstract description 16
- 239000006096 absorbing agent Substances 0.000 claims abstract description 12
- 238000001704 evaporation Methods 0.000 claims abstract description 10
- 230000008676 import Effects 0.000 claims abstract description 5
- 239000000203 mixture Substances 0.000 claims abstract description 4
- 239000007787 solid Substances 0.000 claims description 36
- 239000003507 refrigerant Substances 0.000 claims description 8
- 239000002250 absorbent Substances 0.000 claims description 7
- 230000002745 absorbent Effects 0.000 claims description 7
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 claims description 6
- AMXOYNBUYSYVKV-UHFFFAOYSA-M lithium bromide Chemical group [Li+].[Br-] AMXOYNBUYSYVKV-UHFFFAOYSA-M 0.000 claims description 6
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 5
- BPQQTUXANYXVAA-UHFFFAOYSA-N Orthosilicate Chemical compound [O-][Si]([O-])([O-])[O-] BPQQTUXANYXVAA-UHFFFAOYSA-N 0.000 claims description 3
- 229910021529 ammonia Inorganic materials 0.000 claims description 3
- 239000011449 brick Substances 0.000 claims description 3
- 239000011819 refractory material Substances 0.000 claims description 3
- 238000000926 separation method Methods 0.000 claims description 3
- 238000000855 fermentation Methods 0.000 claims description 2
- 230000004151 fermentation Effects 0.000 claims description 2
- 238000009834 vaporization Methods 0.000 claims description 2
- 230000008016 vaporization Effects 0.000 claims description 2
- 238000009833 condensation Methods 0.000 claims 1
- 230000005494 condensation Effects 0.000 claims 1
- 238000010025 steaming Methods 0.000 claims 1
- 229910052751 metal Inorganic materials 0.000 abstract description 4
- 239000002184 metal Substances 0.000 abstract description 4
- 238000010276 construction Methods 0.000 description 4
- 238000009434 installation Methods 0.000 description 4
- 238000004378 air conditioning Methods 0.000 description 3
- 239000000498 cooling water Substances 0.000 description 3
- 238000010586 diagram Methods 0.000 description 3
- 238000001816 cooling Methods 0.000 description 2
- 230000005611 electricity Effects 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 230000008569 process Effects 0.000 description 2
- 229920006395 saturated elastomer Polymers 0.000 description 2
- 238000009825 accumulation Methods 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 230000001808 coupling effect Effects 0.000 description 1
- 125000004122 cyclic group Chemical group 0.000 description 1
- 238000005868 electrolysis reaction Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000013028 medium composition Substances 0.000 description 1
- 230000003287 optical effect Effects 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 238000005057 refrigeration Methods 0.000 description 1
- 239000002594 sorbent Substances 0.000 description 1
- 230000032258 transport Effects 0.000 description 1
Classifications
-
- 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
-
- 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
-
- 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
- F25B41/00—Fluid-circulation arrangements
- F25B41/40—Fluid line arrangements
-
- 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
-
- 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
Landscapes
- Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Mechanical Engineering (AREA)
- Thermal Sciences (AREA)
- General Engineering & Computer Science (AREA)
- Heat-Pump Type And Storage Water Heaters (AREA)
Abstract
The present invention is a kind of combined thermal storage heat pump system, it includes electric heat storage boiler, circulating fan, absorption heat pump subsystem, electric-control system, and technical essential is：The absorption heat pump subsystem and frequency conversion circulating fan of electric heat storage boiler configuration；The absorption heat pump subsystem includes the generator being connected by pipeline, condenser, evaporator, absorber, heat exchanger, circulating pump, and working media is filled in subsystem；The generator includes with high temperature air import, outlet and the thermal cycle channel and metal component being connected with electric heat storage boiler；The metal component includes to be arranged along hot-air circulation canal by heat exchange pipeline, input port, output port, vaporium, evaporating surface, converge chamber, the airtight cavity of splitter cavity connection composition, the input port of the airtight cavity is connected to heat exchanger, and output port is connected with condenser；Overflow port is additionally provided on airtight cavity.The Energy Efficiency Ratio of combined thermal storage heat pump system of the present invention is more than 1.
Description
Technical field
The invention belongs to technical field of energy saving and environmental protection, specifically a kind of absorption type heat for improving electric heat storage formula boiler Energy Efficiency Ratio
The combined thermal storage heat pump system that pump freezes, heats.
Background technology
It is well known that it is the target that scientific worker constantly pursues to improve Energy Efficiency Ratio in technical field of energy utilization.This
What applicant was formerly declared《Solid electric heat storage formula air-conditioning device》Patent application is that solution wind-power electricity generation and optical energy power are efficient
Utilize the effective way of problem.It presses《Solid electric heat storage formula air-conditioning device》Technology path manufacture product when, first to pacify at the scene
Solid electric heat storage boiler is filled, then connects absorption heat pump hair in each high-temperature hot air circulation canal of solid electric heat storage boiler
Raw device, makes each absorption heat pump generator form closed loop cycle with place high-temperature hot air circulation canal, can be easily
The high-temperature hot air feed track absorption heat pump generator in solid electric heat storage boiler, absorption type heat pump system is made to be moved
Power.But the pipeline of joint connection in site absorption type heat pump system, and reaching vacuum degree and purity requirements, equipment could reliably be grown
Service life runs, this technical solution is more demanding to the technical capability and construction tool of construction personnel.In order to reduce difficulty of construction
The present invention proposes new technical solution：Installed in each high-temperature hot air circulation canal of solid electric heat storage boiler one by
Generator, condenser, evaporator, absorber, heat exchanger, circulating pump, the absorption heat pump subsystem of working media composition use
When the cold output port of each absorption heat pump subsystem is in parallel, then again by the thermal output of each absorption heat pump subsystem
It is user service that port parallel connection, which forms total hot and cold output port,.This technical solution is to the technical capability of construction personnel and applies
Work tool demands are relatively low, reduce installation difficulty at the scene.
Invention content
The object of the present invention is to provide a kind of absorption heat pump refrigeration, the combined thermal storage heat pump systems of heating.The system
It is to store the hot-air that formula boiler provides using solid electricity for power, realizes the absorption heat pump dress that can be heated and can also freeze
It sets.The solid electric heat storage formula boiler of user installation is typically all more and is applied in combination, more than one absorption is arranged in every boiler again
Formula heat pump subsystem, it is logical that each absorption heat pump subsystem corresponds to the cycle of a high-temperature hot air in solid electric heat storage formula boiler
Road, and it is furnished with one group of frequency conversion fan, the hot and cold output port of each absorption heat pump subsystem is connected in parallel respectively to be constituted always
Hot and cold output port provides a user hot and cold output service.
The purpose of the present invention is what is be achieved by following technical side：It includes solid electric heat storage boiler, frequency conversion
Circulating fan, absorption heat pump subsystem, power supply and control system, it is characterised in that：Every solid electric heat storage boiler is configured with
Several absorption heat pump subsystems；Each absorption heat pump subsystem is configured with independent frequency conversion circulating fan；The suction
Receipts formula heat pump subsystem includes the generator being connected by pipeline, condenser, evaporator, absorber, heat exchanger, circulating pump,
And working media is filled in absorption heat pump subsystem；The generator includes carrying to be connected with solid electric heat storage boiler
High temperature air import, high temperature air outlet, hot-air circulation canal and metallic shell members；The metallic shell members include
Have be arranged along hot-air circulation canal by heat exchange pipeline, input port, output port, vaporium, evaporating surface, converge chamber,
The airtight cavity of splitter cavity connection composition, the input port and the heat exchanger in absorption heat pump subsystem of the airtight cavity are defeated
Outlet is connected to, and the output port of the airtight cavity is connected to the condenser input terminal in absorption heat pump subsystem；Closed
It is additionally provided with overflow port between vaporium and evaporating surface on cavity, the overflow port and the heat exchanger in absorption heat pump subsystem
Input terminal is connected to, and set overflow port clamps down on working media in the evaporating surface of confluence intracavitary and retains and can meet working media vapour
Change the vaporium space of separation.
Working media of the present invention is made of refrigerant and absorbent；Refrigerant is water；Absorbent is lithium bromide, ammonia.
Absorption heat pump operating condition is pressed between generator of the present invention, evaporator, condenser, absorber, heat exchanger
Configuration.
Frequency conversion circulating fan of the present invention is to be located at the axial-flow type that hot-air cycle is driven in high temperature air ring channel
Or centrifugal high-temperature blower can be by separate unit or more according to the requirement of absorption heat pump subsystem high temperature circulation air mass flow
Configuration.
Solid electric heat storage boiler internal of the present invention using solid brick made of silicate refractory material as heat-storage medium,
The solid electric heat storage boiler of 100 DEG C~700 DEG C hot-airs can be exported.
Power supply of the present invention and control system are that the power supply of solid electric heat storage boiler connects and draws and control working condition
Component；
Circulating pump of the present invention is that absorption type heat pump assembly special tool makees medium circulation pump.
High-temperature hot air circulation canal of the present invention is in solid electric heat storage boiler and each absorption heat pump subsystem
Generator between complete thermal energy exchange closed loop channel.
The beneficial effects of the invention are as follows：Generator architecture in the combined thermal storage heat pump system and conventional absorption heat
The generator architecture of pump configuration has carried out completely new design, is allowed to adapt to the high-efficient disposition of the present invention.Conventional generator shell side
All it is the closed container of pressure-bearing respectively with tube side, shell side fills working media, and tube side is heat source passages；If the routinely design present invention
Generator, walk the tube side cavity cross-section used in identical energy high temperature air than walking the tube side used in high-temperature water or saturated vapor
Cavity cross-section wants big decades of times, causes generator bulky.It need to can be injected when work than just common high-temperature water or saturated vapor
Thermodynamic generator is made, the working media for having more decades of times volume could reliably working.So being designed using opposition thinking
The generator of the present invention, shell side walk high temperature air tube side dress working media；Tube side is the closed container of pressure-bearing, and shell side is not pressure-bearing
Close passage.If finned tube is selected to do the metallic conduit of generator, the exterior surface area of metallic conduit can be increased, further
Improve the efficiency that pipeline absorbs high temperature air thermal energy.The combined thermal storage heat pump system will be inhaled on plant produced assembly line
Receipts formula heat pump subsystem transports scene to after debugging, reduce user installation difficulty.It, can be very using combined mounting structure
Easily with solid electric heat storage boiler matching, electric heat storage formula air conditioning system for building is done.Especially do Hazards in Power Plant flexibility
The electric heat storage boiler of peak regulation is arranged by this technical solution, not only performs heat, the electrolysis coupling effect of Hazards in Power Plant, moreover it is possible to
By the thermal energy recycling in power plant cooling water.The Energy Efficiency Ratio of combined thermal storage heat pump system is more than 1.
Description of the drawings
Fig. 1 is the mounting structure simplified schematic diagram of the present invention；
Fig. 2 is the absorption heat pump subsystem connection structure simplified schematic diagram of the present invention；
Fig. 3 is the generator architecture simplified schematic diagram of the present invention；
The symbol description of major part in attached drawing：1, solid electric heat storage boiler, 2, frequency conversion circulating fan, 3, power supply and control system
System, 4, absorption heat pump subsystem, 5, generator, 6, absorber, 7, condenser, 8, evaporator, 9, heat exchanger, 10, circulating pump,
11, circulating pump, 12, heat exchange pipeline, 13, input port, 14, output port, 15, working media, 16, high temperature air import, 17,
High temperature air exports, and 18, hot-air circulation canal, 19, vaporium, 20, evaporating surface, 21, confluence chamber, 22, splitter cavity, 23, overflow
Head piece.
Invention will be described in further detail by example below, but following examples is only present invention example therein
Son, does not represent rights protection scope defined by the present invention, the scope of the present invention is with claims
It is accurate.
Specific implementation mode
Embodiment 1
Shown in Fig. 1-3, the combined thermal storage heat pump system of the present embodiment is by solid electric heat storage boiler 1, frequency conversion circulating fan 2,
Power supply and control system 3, which are connected with three absorption heat pump subsystems 4 with corresponding pipeline, to be formed, each absorption heat pump subsystem
Under unified central planning to be equipped with independent frequency conversion circulating fan 2, which is axial-flow type or centrifugal high-temperature blower.Such as Fig. 2 institutes
Show, the absorption heat pump subsystem 4 includes the generator 5 being connected by pipeline, condenser 7, evaporator 8, absorber
6, heat exchanger 9, circulating pump 10 and circulating pump 11, and working media 15 is filled in absorption heat pump subsystem；As shown in Figure 3,
The generator 5 includes passing through frequency conversion circulating fan with the high temperature air import 16 being connected with solid electric heat storage boiler 1
2 ports being connect with high temperature air outlet 17, hot-air circulation canal 18 and metallic shell members；The metallic shell members packet
Include be arranged along hot-air circulation canal 18 by heat exchange pipeline 12, input port 13, output port 14, vaporium 19 steams
Fermentation 20, converge chamber 21, the airtight cavity of the connection composition of splitter cavity 22；The airtight cavity can be with multiple used in parallel；It is described
The input port 13 of airtight cavity is connected to 9 output end of heat exchanger in absorption heat pump subsystem 4, the airtight cavity it is defeated
Exit port 14 is connected to 7 input terminal of condenser in absorption heat pump subsystem；Vaporium 19 on airtight cavity and evaporation
Overflow port 23 is additionally provided between face 20, which is connected to 9 input terminal of heat exchanger in absorption heat pump subsystem 4,
Set overflow port 23 clamps down on working media can meet working media vaporization separation in the evaporating surface and retaining of confluence intracavitary
Vaporium space.Power supply and control system 3 are that the power supply of solid electric heat storage boiler connects the component for drawing and controlling working condition；It is described
Circulating pump 11 be absorption type heat pump assembly working media circulating pump, the circulating pump 11 setting evaporator and condenser it
Between.
Above-mentioned working media is made of refrigerant and absorbent；Refrigerant is water；Absorbent is lithium bromide or ammonia.
Above-mentioned solid electric heat storage boiler internal can be exported using solid brick made of silicate refractory material as heat-storage medium
The solid electric heat storage boiler of 100 DEG C~700 DEG C hot-airs.
It is complete in parallel that the present invention can be equipped with absorption heat pump subsystem 4 of the several groups with frequency conversion circulating fan 2 as needed
Setting, each absorption heat pump subsystem 4 are respectively provided with independent separate unit or more frequency conversion circulating fans 2；The absorption type heat
It pumps subsystem 4 to be arranged in 1 closed high-temperature hot air circulation canal of solid electric heat storage boiler, be followed in high temperature air by being arranged
Frequency conversion fan 2 in ring channel directly drives high temperature air cyclic absorption thermal energy.As shown by the arrows in Figure 1, each absorption type heat
Pump subsystem 4 has independent high-temperature hot air circulation canal 18.
The chamber outer surface area being arranged in high-temperature hot air circulation canal will meet working media in cavity from high temperature
The needs of thermal energy are drawn in air；Condenser, evaporator, absorber, heat exchanger are to corrode made of metal by being resistant to working media
At shell-and-tube heat exchanger.Overflow port of the present invention is that working media overflows the feeding completion heat exchange of heat exchanger 9 of generator 5
Outlet；Pipeline of the present invention be resistant to working media corrosion top, lower part respectively with the confluence chamber being horizontally mounted,
The metal tube that splitter cavity is tightly connected, outer surface is solderable to be connected to fin；Input port of the present invention is that working media enters
The entrance of generator；Output port of the present invention is the steam (vapor) outlet of working media；Vaporium of the present invention has been
At the space evaporated by thermodynamic medium；Evaporating surface of the present invention is the hot release plane of working media in pipeline.
Its course of work, installation is complete for combined thermal storage heat pump assembly, and control parameter is placed in power supply and control when use
In system 3, so that solid electric heat storage boiler 1 is completed accumulation of heat work, control the frequency conversion circulating fan of each absorption heat pump subsystem 4
High temperature air in solid electric heat storage boiler 1 is conveyed to the generator 5 in each absorption heat pump subsystem 4 and added by 2 work respectively
Thermodynamic medium 15, generator 5 are sent into condenser 7 by thermogenetic high pressure refrigerant vapor, and thermal energy is by 7 tube side of condenser
Cooling water absorbs, and cooling water temperature is made to increase to form thermal output；Working media 15 in condenser 7 after cooling is sent into evaporator 8
After be vaporized further cooling, complete the process of refrigerastion of heat pump, be formed simultaneously cold output；The low pressure cold that evaporator 8 is formed is steamed
Vapour enters in absorber 6, while being re-fed into condenser 7 by circulating pump 11 by the working media after absorbing heat is completed；Into
To the low pressure refrigerant vapor in absorber 6 weak solution is formed with absorbent solution；Weak solution in absorber 6 is by circulating pump 10
Boosting, the high temperature sorbent concentrated solution come out with absorption heat pump generator 5 in heat exchanger 9 are sent into generation after carrying out heat exchange
5 reciprocation cycle of device works, and completes system heat exchange acting process.
Claims (8)
1. a kind of combined thermal storage heat pump system, it includes solid electric heat storage boiler, frequency conversion circulating fan, absorption heat pump
System, power supply and control system, it is characterised in that：Every solid electric heat storage boiler is configured with several absorption heat pump subsystems
System；Each absorption heat pump subsystem is configured with independent frequency conversion circulating fan；The absorption heat pump subsystem includes logical
The generator that pipeline is connected, condenser, evaporator, absorber, heat exchanger, circulating pump are crossed, and working media is filled in absorption
In formula heat pump subsystem；The generator includes with the high temperature air import being connected with solid electric heat storage boiler, high temperature
Air outlet slit, hot-air circulation canal and metallic shell members；The metallic shell members include along hot-air circulation canal
Upper setting by heat exchange pipeline, input port, output port, vaporium, evaporating surface, converge chamber, splitter cavity connection composition it is close
The input port of closed chamber body, the airtight cavity is connected to the heat exchanger output end in absorption heat pump subsystem, described closed
The output port of cavity is connected to the condenser input terminal in absorption heat pump subsystem；Vaporium on airtight cavity and steaming
Overflow port is additionally provided between fermentation, which is connected to the heat exchanger input terminal in absorption heat pump subsystem, set
Overflow port clamp down on working media can meet in the evaporating surface and retaining of confluence intracavitary working media vaporization separation vaporium it is empty
Between.
2. combined thermal storage heat pump system according to claim 1, it is characterised in that：The working media by refrigerant and
Absorbent is constituted；Refrigerant is water；Absorbent is lithium bromide or ammonia.
3. combined thermal storage heat pump system according to claim 1, it is characterised in that：The generator, evaporator, condensation
It is configured by absorption heat pump operating condition between device, absorber and heat exchanger.
4. combined thermal storage heat pump system according to claim 1, it is characterised in that：The frequency conversion circulating fan is to set
The axial-flow type or centrifugal high-temperature blower that hot-air cycle is driven in high temperature air ring channel, are configured by separate unit or more.
5. combined thermal storage heat pump system according to claim 1, it is characterised in that：In the solid electric heat storage boiler
Portion can export the solid electric heat storage of 100 DEG C~700 DEG C hot-airs using solid brick made of silicate refractory material as heat-storage medium
Boiler.
6. combined thermal storage heat pump system according to claim 1, it is characterised in that：The power supply and control system be
The power supply of solid electric heat storage boiler connects the component for drawing and controlling working condition.
7. combined thermal storage heat pump system according to claim 1, it is characterised in that：The circulating pump is absorption type heat
The working media circulating pump of pump assembly, is additionally provided with circulating pump between evaporator and condenser.
8. combined thermal storage heat pump system according to claim 1, it is characterised in that：The high-temperature hot air cycle is logical
Road is the closed loop channel of the completed thermal energy exchange in generator in solid electric heat storage boiler and each absorption heat pump subsystem.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201810077488.6A CN108344202A (en) | 2018-01-26 | 2018-01-26 | Combined thermal storage heat pump system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201810077488.6A CN108344202A (en) | 2018-01-26 | 2018-01-26 | Combined thermal storage heat pump system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN108344202A true CN108344202A (en) | 2018-07-31 |
Family
ID=62960620
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201810077488.6A Withdrawn CN108344202A (en) | 2018-01-26 | 2018-01-26 | Combined thermal storage heat pump system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN108344202A (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110375435A (en) * | 2019-08-26 | 2019-10-25 | 周封 | The solid electricity heat accumulation unit of monoblock and composite structure |
| CN111023237A (en) * | 2019-12-16 | 2020-04-17 | 北京金茂绿建科技有限公司 | Fluid medium heating system based on solid heat storage electric boiler |
| CN113405276A (en) * | 2021-07-14 | 2021-09-17 | 重庆金康赛力斯新能源汽车设计院有限公司 | Integrated cold source circulation generator and absorption type refrigerating device |
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN201535596U (en) * | 2009-12-03 | 2010-07-28 | 重庆大学 | Absorption type refrigeration generator adopting lithium bromide solution falling film in vertical tubes |
| CN101963417A (en) * | 2010-03-22 | 2011-02-02 | 浪达科技（深圳）有限公司 | Generator for vehicle-mounted refrigeration device |
| CN103196170A (en) * | 2013-04-11 | 2013-07-10 | 山西大学工程学院 | Absorption heat-pump heating system capable of recycling exhaust heat of exhaust gas from power station boiler |
| CN103742291A (en) * | 2013-12-26 | 2014-04-23 | 宁波工程学院 | Waste heat recovery type distributed energy and ocean thermal energy coupling power generation system |
| CN207831733U (en) * | 2018-01-26 | 2018-09-07 | 沈阳世杰电器有限公司 | Combined thermal storage heat pump system |
-
2018
- 2018-01-26 CN CN201810077488.6A patent/CN108344202A/en not_active Withdrawn
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN201535596U (en) * | 2009-12-03 | 2010-07-28 | 重庆大学 | Absorption type refrigeration generator adopting lithium bromide solution falling film in vertical tubes |
| CN101963417A (en) * | 2010-03-22 | 2011-02-02 | 浪达科技（深圳）有限公司 | Generator for vehicle-mounted refrigeration device |
| CN103196170A (en) * | 2013-04-11 | 2013-07-10 | 山西大学工程学院 | Absorption heat-pump heating system capable of recycling exhaust heat of exhaust gas from power station boiler |
| CN103742291A (en) * | 2013-12-26 | 2014-04-23 | 宁波工程学院 | Waste heat recovery type distributed energy and ocean thermal energy coupling power generation system |
| CN207831733U (en) * | 2018-01-26 | 2018-09-07 | 沈阳世杰电器有限公司 | Combined thermal storage heat pump system |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110375435A (en) * | 2019-08-26 | 2019-10-25 | 周封 | The solid electricity heat accumulation unit of monoblock and composite structure |
| CN111023237A (en) * | 2019-12-16 | 2020-04-17 | 北京金茂绿建科技有限公司 | Fluid medium heating system based on solid heat storage electric boiler |
| CN111023237B (en) * | 2019-12-16 | 2021-07-09 | 北京金茂绿建科技有限公司 | Fluid medium heating system based on solid heat storage electric boiler |
| CN113405276A (en) * | 2021-07-14 | 2021-09-17 | 重庆金康赛力斯新能源汽车设计院有限公司 | Integrated cold source circulation generator and absorption type refrigerating device |
| CN113405276B (en) * | 2021-07-14 | 2022-07-05 | 重庆金康赛力斯新能源汽车设计院有限公司 | Integrated cold source circulation generator and absorption type refrigerating device |
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Application publication date: 20180731 |