CN109764562A - A kind of control method of energy resource system - Google Patents
A kind of control method of energy resource system Download PDFInfo
- Publication number
- CN109764562A CN109764562A CN201910018821.0A CN201910018821A CN109764562A CN 109764562 A CN109764562 A CN 109764562A CN 201910018821 A CN201910018821 A CN 201910018821A CN 109764562 A CN109764562 A CN 109764562A
- Authority
- CN
- China
- Prior art keywords
- heat
- water heater
- energy
- mixed cell
- temperature
- 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.)
- Granted
Links
- 238000000034 method Methods 0.000 title claims abstract description 42
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 178
- 238000010521 absorption reaction Methods 0.000 claims abstract description 98
- 238000005265 energy consumption Methods 0.000 abstract description 2
- 238000005516 engineering process Methods 0.000 abstract description 2
- 239000002699 waste material Substances 0.000 abstract description 2
- 230000009102 absorption Effects 0.000 description 92
- 239000007788 liquid Substances 0.000 description 39
- 238000003860 storage Methods 0.000 description 37
- 238000012546 transfer Methods 0.000 description 35
- 238000001816 cooling Methods 0.000 description 32
- 238000010586 diagram Methods 0.000 description 19
- 238000005338 heat storage Methods 0.000 description 18
- 238000009825 accumulation Methods 0.000 description 16
- 238000010438 heat treatment Methods 0.000 description 10
- 238000004146 energy storage Methods 0.000 description 8
- 210000004262 dental pulp cavity Anatomy 0.000 description 7
- 230000000694 effects Effects 0.000 description 7
- 239000012530 fluid Substances 0.000 description 7
- 239000004065 semiconductor Substances 0.000 description 6
- 238000004891 communication Methods 0.000 description 5
- 238000009413 insulation Methods 0.000 description 5
- 239000000463 material Substances 0.000 description 5
- 150000003839 salts Chemical class 0.000 description 5
- 230000008859 change Effects 0.000 description 4
- 238000006243 chemical reaction Methods 0.000 description 4
- 230000008569 process Effects 0.000 description 4
- 230000006870 function Effects 0.000 description 3
- 238000004519 manufacturing process Methods 0.000 description 3
- 230000007704 transition Effects 0.000 description 3
- 238000004378 air conditioning Methods 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 239000003507 refrigerant Substances 0.000 description 2
- 229910000831 Steel Inorganic materials 0.000 description 1
- 230000009471 action Effects 0.000 description 1
- 230000006978 adaptation Effects 0.000 description 1
- 230000005540 biological transmission Effects 0.000 description 1
- 239000000919 ceramic Substances 0.000 description 1
- 230000004087 circulation Effects 0.000 description 1
- 238000005520 cutting process Methods 0.000 description 1
- 238000013461 design Methods 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 238000007667 floating Methods 0.000 description 1
- 239000011159 matrix material Substances 0.000 description 1
- 230000004089 microcirculation Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 230000003472 neutralizing effect Effects 0.000 description 1
- 230000000704 physical effect Effects 0.000 description 1
- 238000004321 preservation Methods 0.000 description 1
- 230000000750 progressive effect Effects 0.000 description 1
- 238000005057 refrigeration Methods 0.000 description 1
- 230000006641 stabilisation Effects 0.000 description 1
- 238000011105 stabilization Methods 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
- 239000011232 storage material Substances 0.000 description 1
- 230000003245 working effect Effects 0.000 description 1
Classifications
-
- 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
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E10/00—Energy generation through renewable energy sources
- Y02E10/40—Solar thermal energy, e.g. solar towers
Landscapes
- Heat-Pump Type And Storage Water Heaters (AREA)
Abstract
The invention discloses a kind of control methods of energy resource system, belong to field of energy-saving technology.For this method for controlling an energy resource system, the energy resource system includes two or more solar thermal collectors and two or more water heaters, and terminal heat exchanger is provided in the water heater；The energy resource system further includes heat exchanger and two or more mixed cells in two or more；It the described method comprises the following steps: according to the target temperature of the water heater, controlling the service time of two heat absorption valves of the mixed cell being connected with the water heater；According to the difference of the target temperature of the water heater and actual temperature, the service time of the heat release valve for the mixed cell being connected with the water heater is controlled.Using the alternative embodiment, the collection and scheduling to discarded energy are realized, supply other equipment use, and reduce energy consumption and waste, realize energy-saving and emission-reduction.
Description
Technical field
The present invention relates to field of energy-saving technology, in particular to a kind of control method of energy resource system.
Background technique
Solar water heater is the heating device for converting solar energy to thermal energy, by water from low-temperature heat to high temperature, with
Meet hot water of the people in life, production to use.Solar water heater is divided into vacuum pipe solar water by structure type
Device and flat solar water heater occupy the market share of the country 95% mainly based on vacuum pipe solar water heater.
Electron tubes type domestic solar water heater is made of the related spare and accessory parts such as thermal-collecting tube, water tank and bracket, and solar energy is converted
Evacuated collector tube is relied primarily at thermal energy, the principle that evacuated collector tube utilizes hot water floating cold water to sink makes water generate microcirculation
And obtain required hot water.
But current solar water heater, it needs to guide in cold water and be heated in outdoor evacuated collector tube, repaired
Inconvenience can make troubles to the daily life of entire unit building once leakage accident occurs.
How solar energy is converted into thermal energy, then realizes the distribution of thermal energy, for heating the water in indoor water heater,
It is current urgent problem to be solved.
Summary of the invention
The embodiment of the invention provides a kind of control methods of energy resource system.For some aspects of the embodiment to disclosure
There is a basic understanding, simple summary is shown below.The summarized section is not extensive overview, nor to determine pass
Key/important composition element or the protection scope for describing these embodiments.Its sole purpose is some general with the presentation of simple form
It reads, in this, as the preamble of following detailed description.
According to a first aspect of the embodiments of the present invention, a kind of control method of energy resource system is provided.
In some optional embodiments, this method for control an energy resource system, the energy resource system include two or
Multiple solar thermal collectors and two or more water heaters are provided with terminal heat exchanger in the water heater；The energy system
System further includes heat exchanger and two or more mixed cells, described two or multiple middle transition heats in two or more
It include heat exchanger and heat exchanger in one or more low temperature in one or more high temperature in device；The middle heat exchanger
Including a heat absorbing end and multiple release end of heat, the heat absorbing end of the middle heat exchanger is connected to the solar thermal collector, described
The release end of heat of middle heat exchanger is connected to the heat absorbing end of different mixed cells；The mixed cell includes two heat absorbing ends and one
A release end of heat, one of heat absorbing end of the mixed cell are connected to heat exchanger in the high temperature, the mixed cell
Another heat absorbing end is connected to heat exchanger in the low temperature, and the release end of heat of the mixed cell is connected to corresponding one
Two heat absorbing ends of the terminal heat exchanger of water heater, the mixed cell are respectively arranged with heat absorption valve, the mixed cell
Release end of heat is provided with heat release valve；It the described method comprises the following steps: according to the target temperature of the water heater, control and the heat
The service time of two heat absorption valves of the connected mixed cell of hydrophone；According to the target temperature and actual temperature of the water heater
Difference, control the service time for the heat release valve of mixed cell being connected with the water heater.
Optionally, according to the target temperature of the water heater, two suctions of the mixed cell being connected with the water heater are controlled
The step of service time of thermal valve door, comprising: according to the target temperature of the water heater, obtain the mesh of medium in terminal heat exchanger
Mark temperature；According to the target temperature of medium in terminal heat exchanger, two suctions of the mixed cell being connected with the water heater are adjusted
The service time of thermal valve door.
Optionally, the method also includes: obtain the quantity for the water heater being currently running；According to the water heater being currently running
Quantity, it is open-minded to control the heat release valve timesharing of mixed cell being connected with the water heater.
Optionally, the quantity for the water heater that the basis is currently running controls the mixed cell being connected with the water heater
The step opened of heat release valve timesharing, comprising: when the quantity for the water heater being currently running is less than preset value, control with it is described
The heat release valve of the connected mixed cell of water heater is full-time open-minded.
Optionally, the quantity for the water heater that the basis is currently running controls the mixed cell being connected with the water heater
The step opened of valve timesharing, comprising: when the quantity for the water heater being currently running is greater than preset value, control and the hot water
The heat release valve timesharing of the connected mixed cell of device is open-minded.
Optionally, described when the quantity for the water heater being currently running is greater than preset value, control is connected with the water heater
Mixed cell the step opened of heat release valve timesharing, comprising: all water heaters are carried out using single-entry single-out switch mode
Cycle heat exchange.
Optionally, the method also includes: according to the quantity for the water heater being currently running and the target of each water heater
The difference of temperature and actual temperature controls the service time of the heat release valve for the mixed cell being connected with each water heater.
Optionally, the service time of the heat release valve for the mixed cell being connected with the water heater
Wherein, K is proportionality coefficient, Δ TnFor the target temperature of the water heater and the difference of actual temperature, Δ TavFor each water heater
The average value of the difference of target temperature and actual temperature, tbaseFor benchmark service time.
Optionally, the benchmark service time tbaseAccording to be currently running water heater quantity setting.
Optionally, the Δ TnThe difference for subtracting actual temperature for target temperature, as Δ TnWhen≤0, control and the water heater phase
The heat release valve of the mixed cell of pass is closed.
Technical solution provided in an embodiment of the present invention can include the following benefits:
The collection and scheduling to discarded energy are realized, supply other equipment use, and reduce energy consumption and waste, realize
Energy-saving and emission-reduction.
It should be understood that above general description and following detailed description be only it is exemplary and explanatory, not
It can the limitation present invention.
Detailed description of the invention
The drawings herein are incorporated into the specification and forms part of this specification, and shows and meets implementation of the invention
Example, and be used to explain the principle of the present invention together with specification.
Fig. 1 is a kind of block diagram of energy resource system shown according to an exemplary embodiment；
Fig. 2 is a kind of flow diagram of the control method of energy resource system shown according to an exemplary embodiment；
Fig. 3 a is a kind of structural schematic diagram at energy stores station shown according to an exemplary embodiment；
Fig. 3 b is a kind of structural schematic diagram at energy stores station shown according to an exemplary embodiment；
Fig. 3 c is a kind of structural schematic diagram at energy stores station shown according to an exemplary embodiment；
Fig. 3 d is a kind of structural schematic diagram at energy stores station shown according to an exemplary embodiment；
Fig. 3 e is a kind of structural schematic diagram at energy stores station shown according to an exemplary embodiment；
Fig. 3 f is a kind of structural schematic diagram at energy stores station shown according to an exemplary embodiment；
Fig. 3 g is a kind of structural schematic diagram at energy stores station shown according to an exemplary embodiment；
Fig. 4 a is a kind of structural schematic diagram of middle heat exchanger shown according to an exemplary embodiment；
Fig. 4 b is a kind of structural schematic diagram of middle heat exchanger shown according to an exemplary embodiment；
Fig. 4 c is a kind of structural schematic diagram of middle heat exchanger shown according to an exemplary embodiment；
Fig. 4 d is a kind of structural schematic diagram of middle heat exchanger shown according to an exemplary embodiment；
Fig. 4 e is a kind of structural schematic diagram of middle heat exchanger shown according to an exemplary embodiment；
Fig. 4 f is a kind of structural schematic diagram of middle heat exchanger shown according to an exemplary embodiment；
Fig. 4 g is a kind of structural schematic diagram of middle heat exchanger shown according to an exemplary embodiment；
Fig. 4 h is a kind of structural schematic diagram of middle heat exchanger shown according to an exemplary embodiment；
Fig. 5 a is a kind of structural schematic diagram of mixed cell shown according to an exemplary embodiment；
Fig. 5 b is a kind of structural schematic diagram of mixed cell shown according to an exemplary embodiment.
Specific embodiment
The following description and drawings fully show specific embodiments of the present invention, to enable those skilled in the art to
Practice them.Other embodiments may include structure, logic, it is electrical, process and other change.Embodiment
Only represent possible variation.Unless explicitly requested, otherwise individual components and functionality is optional, and the sequence operated can be with
Variation.The part of some embodiments and feature can be included in or replace part and the feature of other embodiments.This hair
The range of bright embodiment includes equivalent obtained by the entire scope of claims and all of claims
Object.Herein, each embodiment individually or can be indicated generally with term " invention ", and it is convenient that this is used for the purpose of,
And if in fact disclosing the invention more than one, the range for being not meant to automatically limit the application is any single invention
Or inventive concept.Herein, relational terms such as first and second and the like be used only for by an entity or operation with
Another entity or operation distinguish, and without requiring or implying, there are any actual relationships between these entities or operation
Or sequence.Moreover, the terms "include", "comprise" or any other variant thereof is intended to cover non-exclusive inclusion, thus
So that process, method or equipment including a series of elements not only include those elements, but also including being not explicitly listed
Other element, or further include for this process, method or the intrinsic element of equipment.In the feelings not limited more
Under condition, the element that is limited by sentence "including a ...", it is not excluded that in process, method or equipment including the element
In there is also other identical elements.Each embodiment herein is described in a progressive manner, and each embodiment stresses
Be the difference from other embodiments, the same or similar parts in each embodiment may refer to each other.For implementing
For method, product etc. disclosed in example, since it is corresponding with method part disclosed in embodiment, so the comparison of description is simple
Single, reference may be made to the description of the method.
Fig. 1 shows an alternative embodiment of energy resource system.
In the alternative embodiment, energy resource system includes two or more solar thermal collectors and two or more hot water
Device is provided with terminal heat exchanger in water heater.Energy resource system further includes heat exchanger and two or more in two or more
A mixed cell includes heat exchanger and one or more in one or more high temperature in heat exchanger in two or more
Heat exchanger in a low temperature.Middle heat exchanger includes a heat absorbing end and multiple release end of heat, and the heat absorbing end of middle heat exchanger connects
To solar thermal collector, the release end of heat of middle heat exchanger is connected to the heat absorbing end of different mixed cells.Mixed cell includes two
A heat absorbing end and a release end of heat, one of heat absorbing end of mixed cell are connected to heat exchanger in high temperature, mixed cell
Another heat absorbing end is connected to heat exchanger in low temperature, and the release end of heat of mixed cell is connected to a corresponding water heater
Terminal heat exchanger.Two heat absorbing ends of mixed cell are respectively arranged with heat absorption valve, and the release end of heat of mixed cell is provided with heat release
Valve.
Above-mentioned solar thermal collector for being heated to the medium in thermal-collecting tube, then medium by middle heat exchanger with
The terminal heat exchanger of water heater exchanges heat, and the water in water heater cavity is heated in realization.
Fig. 2 shows an alternative embodiments of the control method of above-mentioned energy resource system.
In the alternative embodiment, control method is for controlling above-mentioned energy resource system, comprising the following steps: step 11, according to
The target temperature of water heater controls the service time of two heat absorption valves of the mixed cell being connected with water heater；Step 12, root
According to the target temperature of water heater and the difference of actual temperature, the open-minded of the heat release valve for the mixed cell being connected with water heater is controlled
Time.
Using the alternative embodiment, when the heat absorption valve of mixed cell is opened, the high temperature medium of heat exchanger in high temperature
It is mixed with the low temperature medium of heat exchanger in low temperature in mixed cell, the terminal heat exchanger of mixed medium hot water supply device
It uses, for the water in heat hot water device cavity, mixing can be accurately adjusted by the service time of two heat absorption valves of control
Medium temp in unit.When the heat release valve of mixed cell is closed, water heater and mixed cell cutting are connected, and water heater stops
Only exchange heat.
Optionally, according to the target temperature of water heater, two heat absorption valves of the mixed cell being connected with water heater are controlled
Service time the step of, comprising: according to the target temperature of water heater, obtain the target temperature of medium in terminal heat exchanger；Root
According to the target temperature of medium in terminal heat exchanger, two when opening of valve of heat absorption of the mixed cell being connected with water heater are adjusted
Between.
Optionally, energy resource system is as unit of family, or as unit of entire unit building, alternatively, being with entire cell
Unit, alternatively, as unit of some region.
Optionally, target temperature is preset temperature set by user.
Using the alternative embodiment, the mixing list being connected with water heater is controlled according to the difference of target temperature and actual temperature
The temperature difference of the service time of the heat release valve of member, target temperature and actual temperature is big, then heat release valve service time is long；The temperature difference
Small, then heat release valve service time is short.
For example, the water heater needs more when the target temperature of one of water heater and the actual temperature temperature difference are larger
Heat exchange, first according to the target temperature of water heater control mixed cell two heat absorption valve service time, adjust mixing
Then medium temp in unit according to the temperature difference of the target temperature of water heater and actual temperature, controls mixed cell heat release valve
Service time.
Optionally, the actual temperature of water heater passes through the temperature sensor being arranged in water heater and obtains.
In another alternative embodiment, above-mentioned control method further include: obtain the quantity for the water heater being currently running；Root
According to the quantity for the water heater being currently running, the heat release valve timesharing for controlling the mixed cell being connected with water heater is open-minded.
Since middle heat exchanger includes multiple release end of heat, the quantity of solar thermal collector is less than or equal to mixed cell
Quantity, can by small number of solar thermal collector supply greater number of water-heater heat-exchanging.
It is open-minded using timesharing after the quantity for the water heater being currently running reaches certain numerical value using the alternative embodiment
Method control and solar thermal collector heat exchange water heater, i.e., the heat release valve of mixed cell that control is connected with water heater divides
Shi Kaitong enables each water heater uniformly to heat up or cool down to guarantee the supply of medium in solar thermal collector.
Optionally, according to the quantity for the water heater being currently running, the heat release valve for the mixed cell being connected with water heater is controlled
The step that door timesharing is opened, comprising: when the quantity for the water heater being currently running is less than preset value, what control was connected with water heater
The heat release valve of mixed cell is full-time open-minded；When the quantity for the water heater being currently running is greater than preset value, control and water heater
The heat release valve timesharing of connected mixed cell is open-minded.
Full-time open of the heat release valve of mixed cell refers to that the service time of the heat release valve of mixed cell is unrestricted, and
Be not mixed cell heat release valve it is open-minded always.
Using the alternative embodiment, the capacity of solar thermal collector can be optimized, by the way that capacity is smaller or negligible amounts
Solar thermal collector supply more water heater workings.For example, the water heater quantity that solar thermal collector can be supplied simultaneously
It is 10, when the water heater quantity being currently running is 15, in a period, what control exchanged heat with solar thermal collector
Water heater quantity is 10, and the water heater being connected with solar thermal collector is controlled using the method that timesharing is opened, and is realized multiple
The uniform heat exchange of water heater, to guarantee the supply of medium in solar thermal collector, enable each water heater uniformly heat up or
Cooling.
Optionally, when the quantity for the water heater being currently running is greater than preset value, using single-entry single-out switch mode control
The water heater making the water heater of access and exiting, all water heaters carry out cycle heat exchange using single-entry single-out switch mode.
In another alternative embodiment, the method also includes: according to the quantity and heat of the water heater being currently running
The target temperature of hydrophone and the difference of actual temperature, the quantity for the water heater that control exchanges heat with solar thermal collector simultaneously.
Using the alternative embodiment, it is ensured that the reasonable supply of medium in solar thermal collector guarantees the stabilization of system
Operation.
For example, biggish water heater is differed with actual temperature for target temperature, compared to target temperature and actual temperature
Lesser water heater is differed, needs more to be exchanged heat with solar thermal collector, therefore, the difference of target temperature and actual temperature
It is the important evidence for controlling solar thermal collector access water heater quantity.For example, target temperature is differed with actual temperature compared with
Big water heater, separate unit water heater needs are more exchanged heat, and therefore, control solar thermal collector accesses above-mentioned water heater simultaneously
Quantity, prevent the situation of System Medium insufficient supply.For another example differing lesser with actual temperature for target temperature
Water heater, separate unit water heater need to carry out less heat exchange, and therefore, solar thermal collector can access on greater number of simultaneously
State water heater.
For another example solar thermal collector exchanges heat with 20 water heaters altogether, wherein target temperature is differed with actual temperature
20 DEG C or more of water heater 5, target temperature differ 10 DEG C water heater 10 below with actual temperature, and control is simultaneously and the sun
The water heater quantity of energy heat collector heat exchange is 10, wherein 10 water heaters are all that target temperature differs 10 DEG C with actual temperature
Below；Or control is simultaneously 8 with the water heater number of solar thermal collector heat exchange, wherein target temperature and actual temperature phase
Poor 10 DEG C of water heater quantity below be 6 and target temperature 20 DEG C or more of water heater quantity is differed with actual temperature is 2
Platform；Alternatively, control is simultaneously 5 with the water heater quantity of solar thermal collector heat exchange, wherein 5 water heaters are all target temperature
Degree differs 20 DEG C or more with actual temperature.
In another alternative embodiment, above-mentioned control method further include: according to the quantity for the water heater being currently running with
And the difference of water heater target temperature and actual temperature, control opening for the heat release valve for the mixed cell being connected with each water heater
The logical time.
Optionally, when target temperature is higher than actual temperature, the heat release valve for the mixed cell that control is connected with the water heater
Service time；When target temperature is lower than actual temperature, the heat release valve for controlling the mixed cell being connected with the water heater is closed.
Using the alternative embodiment, the heat-exchange time of each water heater and solar thermal collector is not identical, for target
Temperature and the big water heater of the actual temperature temperature difference, control heat release valve service time of the mixed cell being connected with the water heater compared with
It is long；The water heater small for target temperature and the actual temperature temperature difference controls the heat release valve for the mixed cell being connected with the water heater
Door service time is shorter.
Optionally, the service time of the heat release valve for the mixed cell being connected with the water heaterWherein, K is proportionality coefficient, Δ TnFor the target temperature of the water heater and the difference of actual temperature, Δ
TavFor the average value of the difference of the target temperature of water heater and actual temperature that are currently running, tbaseFor benchmark service time.
For water heater, Δ TnThe difference for subtracting actual temperature for target temperature, as Δ TnWhen < 0, control and the water heater phase
The heat release valve of mixed cell even is closed.
Optionally, benchmark service time tbaseAccording to be currently running water heater quantity setting.Optionally, it is transporting
The quantity of capable water heater is fewer, benchmark service time tbaseLonger, the quantity for the water heater being currently running is more, and benchmark is open-minded
Time tbaseIt is shorter.
Herein, temperature equipment refers to bring the temperature of itself or environment is changed to set when equipment work
It is standby, e.g., refrigerator, air conditioner, air energy compressor, solar energy heating temperature equipment, mobile robot heat release charger, hot water
Device, heating temperature equipment, heating device, compressor, the cold temperature equipment of collection, refrigerator-freezer.
In conjunction with shown in Fig. 3 a to Fig. 3 g, illustrate a kind of energy stores station of the embodiment of the present invention.
Energy stores station 10, the energy absorption end 101 at energy stores station 10 is for absorbing the tune that can generate corresponding energy
The energy of warm equipment (absorption edge temperature equipment 1011), energy release end 102 are used to (release to the temperature equipment of the corresponding energy of needs
Put end temperature equipment 1021) it releases energy.
The concrete form at energy stores station 10 does not limit, and major function is storage energy, in have can store energy
The energy-accumulation material of amount, and guarantee 10 adiabatic heat-insulation of energy storage sites.Energy stores station 10 can be an adiabatic heat-insulation
Cabinet, it is interior to fill energy-accumulation material.It is also possible to dig on the ground storage pool, the inner wall of storage pool is insulated
Isothermal holding.
The energy stores station of the embodiment of the present invention can be applied to single family, also can be applied to a cell or society
Area.Application scenarios are different, and the quantity of temperature equipment is different, and the memory capacity at energy stores station 10 is different.Such as, it is applying single
When in home scenarios, the limited amount of temperature equipment does not exceed 10 under normal circumstances.It is applying in cell, even more greatly
Community in when, the quantity of external temperature equipment is just very huge, and the energy stores amount at energy stores station 10 just needs very at this time
Greatly.As long as energy stores station has in application, determining according to actual conditions.
In the energy stores station 10 of the embodiment of the present invention, the energy of storage, can be with according to the reflected temperature of energy institute
It is divided into heat and cooling capacity, therefore, heat and cooling capacity are opposite concepts, are divided i.e. according to the boundary (e.g., temperature limit) of setting
It can.Therefore, in an alternative embodiment, the energy stores station 10 of the embodiment of the present invention can be heat storage device (heat
Measure storage sites) 11, it is also possible to cooling capacity storage device (cooling capacity storage sites) 12, or deposit including heat storage device 11 and cooling capacity
Storage device 12.
The energy absorption end 101 of heat storage device 11 is heat absorption end 111, can generate heat for absorbing
The heat of first temperature equipment 1111, energy release end 102 is heat release end 112, for needing the second of heat to adjust
Warm equipment 1121 discharges heat.Such as, air-conditioner outdoor unit, air when the first temperature equipment can be refrigerator, air conditioner refrigerating can press
Contracting machine, solar energy heating temperature equipment, mobile robot heat release charger etc..Second temperature equipment can be water heater, heating
Air-conditioning, heating temperature equipment, heating device etc..
The energy absorption end 101 of cooling capacity storage device 12 is cold absorption end 121 (that is, heat release end), for inhaling
The cooling capacity that can generate the third temperature equipment 1211 of cooling capacity is received, energy release end 102 is cooling capacity release end 122 (that is, heat
Absorption edge), for 1221 released cold quantity of the 4th temperature equipment for needing cooling capacity.Such as, third temperature equipment can be air-conditioning system
Air-conditioner outdoor unit when hot, compressor, the cold temperature equipment of collection etc..4th temperature equipment can be refrigerator, refrigerator-freezer, refrigeration air-conditioner
Deng.
The energy stores station 10 of the embodiment of the present invention may include one or more heat storage devices 11, and, one
Or multiple cooling capacity storage devices 12.As shown in Figure 3b, a kind of energy stores station, including a heat storage device 11 and one it is cold
Measure storage device 12.Specific setting number and type are determined according to the application scenarios of setting.
In the embodiment of the present invention, following energy stores stations 10 can refer to heat storage device when not doing specified otherwise
11, it can also refer to cooling capacity storage device 12.When heat storage device 11 is made at energy stores station 10, energy absorption end 101 is heat
Absorption edge is measured, energy release end 102 is heat release end.When cooling capacity storage device 12 is made at energy stores station 10, energy absorption
End 101 is cold absorption end, and energy release end 102 is cooling capacity release end.
In the embodiment of the present invention, energy stores station 10 can absorb one or absorbs the energy that multiple temperature equipments generate simultaneously
Amount, can also release energy to one or simultaneously to multiple temperature equipments, therefore, the practical feelings according to external temperature equipment
Condition, energy absorption end 101 can be one or more, energy release end 102 or one or more, specific number foundation
Actual conditions determine.
In the energy stores station 10 of the embodiment of the present invention, energy absorption end 101 can generate corresponding energy for absorbing
The energy of temperature equipment 1011 (the first temperature equipment 1111 and third temperature equipment 1211), absorption pattern multiplicity, e.g., utilizes stream
When body medium is as carrier, energy absorption end 101 is logical using heat-exchanger rig and the heat-exchanger rig of 1011 side of absorption edge temperature equipment
Pipeline connection is crossed, forms mediation cycle access between energy stores station 10 and temperature equipment.Liquid mediums absorb temperature equipment
The energy that side generates, then flows to the energy absorption end 101 at energy stores station 10, and the energy storage material in energy stores station 10 will
The energy absorption of the medium at energy absorption end 101 and storage, liquid mediums after releasing energy are changed flowing out to temperature equipment side
Thermal absorbs the energy that temperature equipment side generates, so recycles, complete the energy stores at energy stores station 10.
In an alternative embodiment, the energy absorption end 101 at energy stores station 10 is one or more, each energy
Absorption edge 101 is independently arranged.For example, the energy absorption end 101 at energy stores station 10 includes one (as shown in Figure 3 e) or multiple
First heat-exchanger rig (as shown in Figure 3d), the first heat-exchanger rig have inlet tube 141 and outlet tube 142 (that is, one group of connecting pipeline
14) group, is connected to by two root canal roads with the heat-exchanger rig of 1011 side of absorption edge temperature equipment, in temperature equipment, (the first temperature adjustment is set
Standby 1111 and third temperature equipment 1211) between energy stores station 10 energy turn is carried out by respective mediation cycle access
It changes.For another example, as shown in Figure 3c, energy absorption end 101 is first heat-exchanger rig, and is connected in the liquid feeding end of the first heat-exchanger rig
Lead to multiple inlet tubes 141, outlet end is connected to multiple outlet tubes 142.One inlet tube 141 and an outlet tube 142 are used as one
Connecting pipeline group 14 constitutes multiple connecting pipeline groups being independently arranged, passes through multiple connecting pipeline group and external temperature equipment
The terminal heat-exchanger rig of side is connected to.Adapt to the field that multiple external temperature equipments carry out energy input to energy absorption end 101 simultaneously
Scape.It is filled by the way that flow control is arranged at multiple inlet tubes of the liquid feeding end in the first heat-exchanger rig and multiple outlet tubes of outlet end
It sets, by the control to each volume control device, it can be achieved that absorbing the energy that one or more temperature equipments generate simultaneously, and
The flow for adjusting medium in the mediation cycle pipeline of each temperature equipment realizes different heat exchange efficiencies.Further alternative reality
It applies in example, the energy absorption end 101 at energy stores station 10 can also include multiple terminal heat-exchanger rigs, each terminal heat-exchanger rig
With terminal inlet tube and terminal outlet tube, pass through the corresponding outlet tube and inlet tube with the first heat-exchanger rig in two root canal roads respectively
Connection.The setting of terminal heat-exchanger rig is in 1011 side of absorption edge temperature equipment, for absorbing the energy of temperature equipment generation.First changes
Thermal and terminal heat-exchanger rig constitute a mediation cycle access, and the energy for generating temperature equipment side is completed by liquid mediums
In amount conversion to energy stores station 10.Wherein, when energy stores station 10 is heat storage device 11, the setting of terminal heat-exchanger rig exists
First temperature equipment, 1111 side.When energy stores station 10 is cooling capacity storage device 12, terminal heat-exchanger rig is arranged in third temperature adjustment
1211 side of equipment.
In an alternative embodiment, the energy absorption end 101 at energy stores station 10 is multiple, multiple energy absorptions
The pipeline at end 101 interconnects.There are many mode interconnected, as long as realizing the heat-exchanger rig and energy absorption of temperature equipment side
End 101 may make up mediation cycle access.For example, as illustrated in figure 3f, multiple energy absorption ends 101 pass through feed liquor transfer pipeline
151 are connected to liquid transfer pipeline 152 out, and the inlet tube 141 at each energy absorption end 101 is connected to feed liquor transfer pipeline 151,
The outlet tube 142 at each energy absorption end 101 is connected to liquid transfer pipeline 152 out.Again by feed liquor transfer pipeline 151 and out
Liquid transfer pipeline 152 is used as one group of connecting pipeline group, is connected to by two root canal roads with the terminal heat-exchanger rig of temperature equipment side,
Pass through respective mediation cycle access between temperature equipment (the first temperature equipment and third temperature equipment) and energy stores station 10
Carry out energy conversion.Multiple inlets of multiple energy absorption ends 101 (multiple first heat-exchanger rigs) are connected to, multiple liquid out
Mouth connection.By the way that volume control device is arranged at each communication port on feed liquor transfer pipeline 151 and out liquid transfer pipeline 152,
The energy that one or more temperature equipments generate is realized while being absorbed, and can be conveyed to one or more energy absorption ends 101
Energy.
Similarly, energy release end 102, for releasing energy to the temperature equipment of the corresponding energy of needs.Delivery mode multiplicity,
Such as, using liquid mediums as when carrier, energy release end 102 passes through pipeline using the heat-exchanger rig of heat-exchanger rig and equipment side
Connection, energy stores station 10 and release end temperature equipment 1021 (the second temperature equipment 1121 and the 4th temperature equipment 1221) it
Between formed mediation cycle access.Liquid mediums absorb the energy in the energy-accumulation material at energy stores station 10 in energy release end 102
Amount, then flows to the terminal heat-exchanger rig of 1021 side of release end temperature equipment, and temperature equipment side absorbs the energy in liquid mediums
Amount, the liquid mediums after releasing energy flow back into the energy release end 102 at energy stores station 10 again, so recycle, and complete energy
The energy of storage sites 10 discharges.
In an alternative embodiment, the energy release end 102 at energy stores station 10 is one or more, each energy
The pipeline of release end 102 is independently arranged.For example, the energy release end 102 at energy stores station 10 includes one (as shown in Figure 3 e)
Or multiple second heat-exchanger rigs (as shown in Figure 3d), each second heat-exchanger rig have inlet tube 141 and outlet tube 142 (that is, one
Group connecting pipeline group 14), it is connected to by two root canal roads with the terminal heat-exchanger rig of 1021 side of temperature equipment, in temperature equipment (tool
Body is the second temperature equipment 1121 and the 4th temperature equipment 1221) and energy stores station 10 between pass through medium independent
Circulation path carries out energy conversion.For another example, as shown in Figure 3c, energy release end 102 includes second heat-exchanger rig, and second changes
The liquid feeding end of thermal is connected to multiple inlet tubes 141, and outlet end is connected to multiple outlet tubes 142.One inlet tube 141 and one go out
Liquid pipe 142 is used as a connecting pipeline group 14, constitutes the connecting pipeline group 14 that multiple groups are independently arranged, is respectively used to and external release
Hold the terminal heat-exchanger rig connection of 1021 side of temperature equipment.Adapt to energy release end 102 simultaneously to multiple external temperature equipments into
The scene of row energy output.At multiple inlet tubes of the liquid feeding end in the second heat-exchanger rig and multiple outlet tubes of outlet end
Volume control device is set, then by the control to each volume control device, it can be achieved that setting simultaneously to one or more temperature adjustments
It is standby to release energy, and the flow of medium in the mediation cycle pipeline of each temperature equipment is adjusted, realize different heat exchange efficiencies.
In further alternative embodiment, the energy release end 102 at energy stores station 10 can also include multiple terminal heat-exchanger rigs, often
A terminal heat-exchanger rig has terminal inlet tube and terminal outlet tube, passes through two root canals road correspondence and the second heat-exchanger rig respectively
Outlet tube 142 and inlet tube 141 connect.The setting of terminal heat-exchanger rig is generated in temperature equipment side for absorbing temperature equipment
Energy.Second heat-exchanger rig and terminal heat-exchanger rig constitute a mediation cycle access, are completed by liquid mediums by energy
Energy in storage sites 10 is released to temperature equipment side.Wherein, when energy stores station 10 is heat storage device 11, terminal heat exchange
Device is arranged in 1121 side of the second temperature equipment.When energy stores station 10 is cooling capacity storage device 12, the setting of terminal heat-exchanger rig
In 1221 side of the 4th temperature equipment.
In an alternative embodiment, the energy release end 102 at energy stores station 10 is multiple, multiple energy releases
End 102 interconnects.There are many mode interconnected, as long as realizing the heat-exchanger rig and energy release end 102 of temperature equipment side
It may make up mediation cycle access.For example, as illustrated in figure 3f, multiple energy release ends 102 (multiple second heat-exchanger rigs) are logical
Feed liquor transfer pipeline 151 is crossed to be connected to liquid transfer pipeline 152 out, each energy release end 102 (each second heat-exchanger rig)
Inlet tube 141 is connected to feed liquor transfer pipeline 151, the outlet tube of each energy release end 102 (each second heat-exchanger rig)
142 are connected to liquid transfer pipeline 152 out.It is connected to again with liquid transfer pipeline 152 out as one group by feed liquor transfer pipeline 151
Pipeline group is connected to, in temperature equipment (the first temperature equipment and third tune with the heat-exchanger rig of temperature equipment side by two root canal roads
Warm equipment) and energy stores station 10 between pass through respective mediation cycle access carry out energy conversion.Multiple energy are discharged
Hold multiple inlets connection of 102 (multiple second heat-exchanger rigs), multiple liquid outlet connections.By in feed liquor transfer pipeline and out
Volume control device is set at each communication port on liquid transfer pipeline, realizes and is released simultaneously by one or more energy release ends 102
Exoergic amount, and can release energy simultaneously to one or more temperature equipments.
In the embodiment of the present invention, the heat exchange dress of the energy absorption end 101 at energy stores station 10 and the use of energy release end 102
It sets, it can be using plate heat exchanger, evaporator, condenser, heat exchange coil etc..
In the energy stores station 10 of the embodiment of the present invention, the set-up mode of energy absorption end 101 and energy release end 102 can
It, can not also be identical with identical.
In an alternative embodiment, the structure at the energy absorption end 101 at energy stores station 10 and energy release end 102
It is identical.Specifically, energy stores station 10 includes following four specific embodiment:
As shown in Figure 3 e, the first energy stores station 10, energy absorption end 101 are first heat-exchanger rig, pass through one
Group connecting pipeline group is connected to the heat-exchanger rig of temperature equipment side.Energy release end 102 is second heat-exchanger rig, passes through one
Group connecting pipeline group is connected to the heat-exchanger rig of temperature equipment side.That is, the pipeline and energy release end 102 at energy absorption end 101
Pipeline be independently arranged.That is, the energy absorption end 101 at the first energy stores station 10 is first heat-exchanger rig, have
One group of independent communication pipeline group, energy release end 102 are second heat-exchanger rig, have one group of independent communication pipeline group, use
It is connected in the heat-exchanger rig of temperature equipment side.
As illustrated in figure 3f, second of energy stores station 10, energy absorption end 101 are multiple first heat-exchanger rigs, pass through one
The heat-exchanger rig company of group connecting pipeline group (by feed liquor transfer pipeline 151 and out liquid transfer pipeline 152 is constituted) and temperature equipment side
It is logical.Energy release end 102 is multiple second heat-exchanger rigs, by one group of connecting pipeline group (by feed liquor transfer pipeline 151 and liquid out
Transfer pipeline 152 is constituted) it is connected to the heat-exchanger rig of temperature equipment side.That is, the pipeline at multiple energy absorption ends 101 is mutually connected
Logical, the pipeline of multiple energy release ends 102 interconnects.That is, the energy absorption end 101 at second of energy stores station 10 is more
A, the inlet tube and outlet tube at multiple energy absorption end interconnect, and pass through one group of connecting pipeline group and temperature equipment side
Heat-exchanger rig connection.Energy release end 102 be it is multiple, the inlet tube and outlet tube of multiple energy release end interconnect, lead to
One group of connecting pipeline group is crossed to be connected to the heat-exchanger rig of temperature equipment side.
As shown in Fig. 3 a and Fig. 3 c, the third energy stores station 10, energy absorption end 101 is first heat-exchanger rig,
It is connected to by multiple groups connecting pipeline group with the heat-exchanger rig of temperature equipment side.Energy release end 102 is second heat-exchanger rig,
It is connected to by multiple groups connecting pipeline group with the heat-exchanger rig of temperature equipment side.Multiple connecting pipelines at one energy absorption end 101
Group is independently arranged, and multiple connecting pipeline groups of an energy release end 102 are independently arranged.That is, the third energy stores station 10
Energy absorption end 101 is one, and with the connecting pipeline group that multiple groups are independently arranged, energy release end 102 is one, has multiple groups
The connecting pipeline group being independently arranged.
As shown in Figure 3d, the 4th kind of energy stores station 10, energy absorption end 101 is multiple first heat-exchanger rigs, by every
The connecting pipeline group 14 and the heat-exchanger rig of temperature equipment side of a heat-exchanger rig respective inlet tube 141 and the composition of outlet tube 142
Connection.Energy release end 102 is multiple second heat-exchanger rigs, passes through the respective inlet tube 141 of each heat-exchanger rig and outlet tube
The 142 connecting pipeline groups 14 constituted are connected to the heat-exchanger rig of temperature equipment side.The connecting pipeline group at each energy absorption end 101
It is independently arranged, the connecting pipeline group of each energy release end 102 is independently arranged.That is, the energy absorption at the 4th kind of energy stores station
To be multiple, the connecting pipeline group at each energy absorption end 101 is independently arranged at end 101；The energy release end 102 at energy stores station is
Multiple, the connecting pipeline group at each energy release end end 102 is independently arranged.
Certainly, the energy absorption end 101 at energy stores station 10 and the set-up mode of energy release end 102 can not be identical.
The specific set-up mode used is combined according to situation and determines, this is no longer going to repeat them.
In an alternative embodiment, energy stores station 10 further includes multiple volume control devices 13, multiple flow controls
Device 13 processed is separately positioned on the energy absorption end 101 at energy stores station 10 and the pipeline of energy release end 102.Flow control
Device has the function of adjusting flow, including power effect and throttling action.Wherein, power effect throttles for increasing flow
Effect is for reducing flow.In the embodiment for carrying out energy exchange using liquid mediums, volume control device can be power
Pump and solenoid valve, alternatively, expansion valve etc..The energy absorption end 101 at energy stores station 10 and energy release end 102 pass through pipe respectively
Road (inlet tube 141 and outlet tube 142) and external temperature equipment carry out energy exchange, that is, a temperature equipment and energy absorption
101 (or energy release ends 102) are held to constitute a mediation cycle pipeline, volume control device setting is opposite in each temperature equipment
On the mediation cycle pipeline answered.By the setting of volume control device, the mediation cycle where adjusting respectively can control
The flow of medium in pipeline can be adjusted from zero between maximum stream flow, thus control the energy of energy storage station 10
Amount of storage or burst size.In a kind of specific embodiment, volume control device be separately positioned on energy absorption end 101 it is each into
The interface and each inlet tube 141 of energy release end 102 of liquid pipe 141 and each outlet tube 142 and connecing for each outlet tube 142
At mouthful.
In the embodiment of the present invention, a kind of structure at specific energy stores station 10 is provided, as shown in figure 3g, including, one
Or multiple accumulation of energy heaps 100, each accumulation of energy heap 100 include Storage Unit 110, are used for storage energy；Absorption edge heat-exchanger rig 101,
The absorption edge heat-exchanger rig is embedded in the accumulation of energy heap 110；Release end heat-exchanger rig 102, the release end heat-exchanger rig
It is embedded in the accumulation of energy heap 110.
In the embodiment of the present invention, Storage Unit 110 can use existing energy-accumulation material, and e.g., fused salt can store heat
Amount.There are many type of fused salt, e.g., ceramic matrix fused salt.For another example, ice bag can store cooling capacity.The shape of Storage Unit is unlimited
It is fixed, it is determined according to the physical property of energy-accumulation material itself, e.g., when using fused salt, Storage Unit uses rigidity shell, steel
Property shell in encapsulate fused salt, and groove is formed on rigidity shell, for being embedded absorption edge heat-exchanger rig and release end heat exchange dress
It sets.
Absorption edge heat-exchanger rig, i.e. energy absorption edge 101 can be set one or more absorption edges in each accumulation of energy heap and change
Thermal.The connecting pipeline of absorption edge heat-exchanger rig in multiple accumulation of energy heaps can be independently arranged, and can also be interconnected.With reference to
Foregoing teachings.
Release end heat-exchanger rig, i.e. energy release end 102 can be set one or more release ends in each accumulation of energy heap and change
Thermal.The connecting pipeline of release end heat-exchanger rig in multiple accumulation of energy heaps can be independently arranged, and can also be interconnected.With reference to
Foregoing teachings.
Certainly, energy stores station 10 further includes the shell of adiabatic heat-insulation, plays heat preservation heat insulating function, prevents energy loss.
In the present embodiment, absorption edge heat-exchanger rig uses the first heat exchange coil；Release end heat-exchanger rig is using the second heat exchange
Coil pipe.Had using coil pipe using the heat exchange area increased with thermal storage unit, improves the efficiency of storage or release.
Further, the first heat exchange coil and the second heat exchange coil are staggered in Storage Unit.
When only having an accumulation of energy heap 100 in the energy stores station 10 of the present embodiment, absorption edge heat-exchanger rig 101 and release end
The connecting pipeline of heat-exchanger rig 102 using it is above-mentioned the first to the 4th kind of energy stores station 10 structure.
When having multiple accumulation of energy heaps 100 in the energy stores station 10 of the present embodiment, the absorption edge in each accumulation of energy heap 100 is changed
The connecting pipeline of thermal 101 and release end heat-exchanger rig 102 uses the set-up mode as shown in Fig. 3 e or Fig. 3 f.And it is absorbing
End 101 end of heat-exchanger rig is further added by the total inlet tube of setting and main drain pipe, the inlet tube (141 of each absorption edge heat-exchanger rig 101
Or 151) it is connected to total inlet tube, the outlet tube (142 or 152) of each absorption edge heat-exchanger rig 101 is connected to main drain pipe.
Similarly, the total inlet tube of setting and main drain pipe, each release end heat-exchanger rig are also further added by 102 end of release end heat-exchanger rig
102 inlet tube (141 or 151) is connected to total inlet tube, the outlet tube (142 or 152) of each release end heat-exchanger rig 102
It is connected to main drain pipe.
In conjunction with shown in Fig. 4 a to Fig. 4 f, illustrate a kind of middle heat exchanger of the invention, be denoted as heat exchanger 20 in first, wraps
It includes: heat absorbing end 201, for being connected to 10/ temperature equipment of energy stores station (e.g., the first temperature equipment 1111 or the 4th temperature adjustment
Equipment 1221)；With release end of heat 202, for being connected to temperature equipment (e.g., the second temperature equipment 1121 or third temperature equipment
1211)/energy stores station 10.
Heat exchanger 20 in the first of the embodiment of the present invention accesses between energy stores station 10 and temperature equipment, to energy
Energy between storage sites 10 and multiple temperature equipments has converted transfer effect.In practical application, the quantity of temperature equipment is not
It is fixed, it can be one, it is also possible to it is two, it is even more；And energy stores station 10 also can have one or more, because
This, the heat absorbing end 201 of the middle heat exchanger of the embodiment of the present invention is one or more, and release end of heat 202 is also one or more, real
Now turn multichannel all the way, multichannel turns all the way or multichannel turns multichannel, can facilitate and adjust energy stores station 10 and temperature equipment (suction
Receiving end temperature equipment 1011 or release end temperature equipment 1021) between energy stores and release, and access is easy to control,
According to actual conditions, part of access can be connected and carry out energy exchange.It can also enough simplifying energy stores station and adjusting
Connecting pipeline between warm equipment facilitates the layout of pipeline, reduces cost.
In the middle heat exchanger 20 of the embodiment of the present invention, when heat absorbing end 201 is connected to energy stores station 10, release end of heat 202
It is connected to temperature equipment, energy stores station 10 supplies heat to temperature equipment by middle heat exchanger 20, is also possible to temperature adjustment and sets
It is standby that cooling capacity is supplied to energy stores station by middle heat exchanger 20.When heat absorbing end 201 is connected to temperature equipment, release end of heat 202
It is connected to energy stores station 10, temperature equipment supplies heat to energy stores station 10, is also possible to energy stores station 10 to temperature adjustment
Equipment supplies cooling capacity.
In the embodiment of the present invention, heat absorbing end 201, for absorbing energy stores station 10 (alternatively, first temperature equipment 1111)
Heat, namely the amount of letting cool end (released cold quantity).The specific structure multiplicity of use, e.g., using liquid mediums as carrier, heat absorption
End 201 uses the heat exchange of the heat release end 112 (alternatively, first temperature equipment 1111) of heat-exchanger rig and 11 side of heat storage sites
Device absorbs the heat of 11 side of heat storage sites (alternatively, first temperature equipment 1111), fluid by pipeline connection, liquid mediums
Medium flows to the heat absorbing end 201, the medium fluid progress heat exchange of heat absorbing end 201 and release end of heat 202, so that heat be converted
To release end of heat 202.Alternatively, heat absorbing end 201 is using the cold absorption end 121 of heat-exchanger rig and cooling capacity storage sites 12 (alternatively, the 4th
Temperature equipment 1221) heat-exchanger rig by pipeline connection, at this point, heat absorbing end 201 can be understood as released cold quantity end 201, stream
Body medium absorbs the heat (absorbing heat, i.e. released cold quantity) of 12 side of cooling capacity storage sites (alternatively, the 4th temperature equipment 1221), stream
Body medium flows to the heat absorbing end 201, the medium fluid progress heat exchange of heat absorbing end 201 and release end of heat 202, so that heat be turned
Shift to release end of heat 202.
Similarly, release end of heat 202 are used to discharge heat to energy stores station 10 (alternatively, second temperature equipment 1121), namely
Absorb cooling capacity end (absorbing cooling capacity).The specific structure multiplicity of use, e.g., using liquid mediums as carrier, release end of heat 202 is used
Heat-exchanger rig and the heat-exchanger rig at the heat absorption end 111 (alternatively, second temperature equipment 1121) of 11 side of heat storage sites pass through
Pipeline connection, liquid mediums absorb the heat of 11 side of heat storage sites (alternatively, second temperature equipment 1121), liquid mediums flowing
To the release end of heat 202, the medium fluid of release end of heat 202 and heat absorbing end 201 carries out heat exchange, to converting heat to heat absorbing end
201.Alternatively, release end of heat 202 is using the cooling capacity release end 122 of heat-exchanger rig and cooling capacity storage sites 12 (alternatively, third temperature equipment
1211) heat-exchanger rig is released by pipeline connection, liquid mediums to 12 side of cooling capacity storage sites (alternatively, third temperature equipment 1211)
Thermal discharge (release heat, i.e. absorption cooling capacity), liquid mediums flow to the release end of heat 202, release end of heat 202 and heat absorbing end 201
Medium fluid carries out heat exchange, to converting heat to heat absorbing end 201.
That is, when by transfer heat exchanger applications to cooling capacity storage device, the inverse mistake of the transmitting of heat in middle heat exchanger 20
Journey is cooling capacity transmitting, that is, heat absorption is released cold quantity.
In an alternative embodiment, heat absorbing end 201 specifically use heat-exchanger rig, e.g., plate heat exchanger, evaporator or
Person's heat exchange coil etc..Release end of heat 202 is specifically using heat-exchanger rig, e.g., plate heat exchanger, condenser, alternatively, heat exchange coil etc..
In the first of the embodiment of the present invention in heat exchanger 20, the number of heat absorbing end 201 and release end of heat 202, and, heat absorption
The setting of the external connecting pipeline group of end 201 and release end of heat 202, according to connection side (energy stores station side and temperature equipment side)
The quantity (can participate in the content hereinafter with regard to energy storage portion) of the connecting pipeline group of heat-exchanger rig determines.
In an alternative embodiment, in the first of the embodiment of the present invention heat exchanger 20 heat absorbing end 201 be one or
Multiple, the pipeline of each heat absorbing end 201 is independently arranged.For example, heat absorbing end 201 includes one (such as Fig. 4 a, Fig. 4 b and Fig. 4 f institute
Show) or multiple (release end of heat 202 of the middle heat exchanger 20 of d referring to fig. 4) third heat-exchanger rigs, each third heat-exchanger rig have
Have inlet tube 211 and outlet tube 212 (that is, one group of connecting pipeline group 21), by two pipelines and energy stores station 10 (alternatively,
First temperature equipment 1111 or the 4th temperature equipment 1221) side heat-exchanger rig connection, using liquid mediums by energy stores
Stand 10 (alternatively, the first temperature equipment 1111 or the 4th temperature equipment 1221) sides heat transfer to heat absorbing end 201.That is,
Each third heat-exchanger rig is independently with energy stores station 10 (alternatively, the first temperature equipment 1111 or the 4th temperature equipment
1221) it is connected to.For another example, as shown in Fig. 4 c, Fig. 4 e, heat absorbing end 201 is a third heat-exchanger rig, and in third heat-exchanger rig
Liquid feeding end is connected to multiple inlet tubes 211, and outlet end is connected to multiple outlet tubes 212.One inlet tube 211 and an outlet tube 222
As a connecting pipeline group 21, constitute multiple independent connecting pipeline groups, by multiple independent communication pipeline group respectively with
The third heat-exchanger rig of external temperature equipment side is connected to.
In another alternative embodiment, heat absorbing end 201 is multiple, and the pipeline of multiple heat absorbing ends 201 interconnects.Mutually
There are many mode of connection, if realize can multiple heat absorbing ends with energy stores station 10 (alternatively, the first temperature equipment 1111 or
The 4th temperature equipment 1221 of person) connection.For example, as shown in figure 4d, multiple heat absorbing ends 201 pass through feed liquor transfer pipeline 221
Liquid transfer pipeline 222 is connected to out, and the inlet tube 211 of each heat absorbing end 201 is connected to feed liquor transfer pipeline 221, each suction
The outlet tube 212 in hot end 201 is connected to liquid transfer pipeline 222 out.Pass through feed liquor transfer pipeline 221 and out liquid transfer pipeline again
222 are used as one group of connecting pipeline group, by two root canal roads and energy stores station 10 (alternatively, the first temperature equipment 1111 or the
Four temperature equipments 1221) side heat-exchanger rig connection.
Similarly, when release end of heat 202 is one or more, the pipeline of each release end of heat 202 is independently arranged, and set-up mode is the same
The heat absorbing end 201 stated is identical.When release end of heat 202 is multiple, the pipeline of multiple release end of heat 202 is interconnected, and mode of communicating is the same
The heat absorbing end 201 stated is identical.Details are not described herein.
Therefore, in the first of the embodiment of the present invention in heat exchanger, the pipeline of foundation heat absorbing end 201 and heat-exchange end 202
Set-up mode has following several specific embodiments.
As shown in fig. 4 a, the first transfer heat exchanger I, heat absorbing end 201 are one, have a connecting pipeline group；Release end of heat
202 is multiple, and the connecting pipeline group of multiple release end of heat 202 is independently arranged.That is, the pipeline of heat absorbing end 201 and release end of heat 202 is independent
Setting.Turn multichannel all the way.
As shown in Figure 4 b, the first transfer heat exchanger II, heat absorbing end 201 are one, have a connecting pipeline group；Release end of heat
202 be one, and a release end of heat 202 has multiple connecting pipeline groups being independently arranged.That is, heat absorbing end 201 and release end of heat 202
Pipeline is independently arranged.Turn multichannel all the way.
As illustrated in fig. 4 c, heat exchanger III in first, heat absorbing end 201 are one, and a heat absorbing end 201 has multiple independences
The connecting pipeline group of setting；Release end of heat 202 is one, has a connecting pipeline group.That is, heat absorbing end 201 and release end of heat 202
Pipeline is independently arranged.Multichannel turns all the way.
As shown in figure 4d, heat exchanger V in first, heat absorbing end 201 be it is multiple, multiple heat absorbing ends 201 are interconnected by one
Group communicating pipe group is connected to the heat-exchanger rig of energy stores station 10 (or absorption edge temperature equipment 1011) side；Release end of heat 202 is
Multiple, the connecting pipeline group of multiple release end of heat 202 is independently arranged.That is, the pipeline of multiple heat absorbing ends 201 is interconnected, Duo Gefang
The pipeline in hot end 202 is independently arranged.Turn multichannel all the way.
As shown in fig 4e, heat exchanger IV in first, heat absorbing end 201 are one, and a heat absorbing end 201 has multiple independences
The connecting pipeline group of setting；Release end of heat 202 is one, and a release end of heat 202 has multiple connecting pipeline groups being independently arranged.
That is, the pipeline of heat absorbing end 201 and release end of heat 202 is independently arranged.Multichannel turns multichannel.
As shown in fig. 4f, heat exchanger VI in first, heat absorbing end 201 are one, have a connecting pipeline group；Release end of heat
202 be one, has a connecting pipeline group.That is, the pipeline of heat absorbing end 201 and release end of heat 202 is independently arranged.Turn one all the way
Road.
Certainly, the structure of heat exchanger is not limited to above-mentioned six kinds in the first of the embodiment of the present invention, wherein 201 He of heat absorbing end
The structure of release end of heat 202 can be interchanged, can also be in any combination.It is connected to the heat exchange of side (energy stores station side and temperature equipment side)
The quantity of the connecting pipeline group of device determines the structure of the middle heat exchanger of adaptation.In addition, in first heat exchanger suction
When the connecting pipeline group in hot end 201 (or release end of heat 202) is multiple groups, number is not limited, the energy storage according to required access
Stand 10 or temperature equipment number determine.
In the first of the embodiment of the present invention in heat exchanger 20, the heat exchange of the heat-exchanger rig and release end of heat 202 of heat absorbing end 201
Device can be separately provided, and e.g., when using plate heat exchanger, the two is oppositely arranged and (can contact or do not contact), guarantee heat-transfer surface
Product maximizes；When using heat exchange coil, makes the interlaced setting of the coil portions of the two (can contact or do not contact), guarantee have
Effect heat exchange.Alternatively, the heat-exchanger rig design of the heat-exchanger rig and release end of heat 202 of heat absorbing end 201 is integrated.Set-up mode is unlimited
Fixed, as long as realizing, the heat-exchanger rig of heat absorbing end 201 and the heat-exchanger rig of release end of heat 202 are able to carry out heat transmitting.Such as Fig. 4 a
To shown in Fig. 4 f, being the heat-exchanger rig structure being oppositely arranged of heat absorbing end 201 and release end of heat 202 using contactless type, certainly
Heat exchanger is not limited to structure given by attached drawing in the first of the embodiment of the present invention.
In an alternative embodiment, middle heat exchanger 20 further includes the valve 231 that absorbs heat, and is arranged in series in heat absorbing end
On 201 pipeline；And/or heat release valve 232, it is arranged in series on the pipeline of release end of heat 202.The purpose that valve is arranged is control
Heat absorbing end 201 processed and release end of heat 202 open or close.In specific embodiment, in each 201 (each heat exchange dress of heat absorbing end
Set) inlet tube and outlet tube on be respectively provided with heat absorption valve 231, in the inlet tube of each release end of heat 202 (each heat-exchanger rig)
With heat release valve 232 is respectively provided on outlet tube.By the control to each valve, the release end of heat of centering heat exchanger 20 is realized respectively
202 and heat absorbing end 201 each connecting pipeline folding control, adjust the transmitting of energy, can according to actual conditions, control the energy
Storage sites 10 carry out energy release to part temperature equipment, also can control part temperature equipment case energy storage station 10 and store energy
Amount.
In conjunction with shown in Fig. 4 g and Fig. 4 h, in the embodiment of the present invention, a kind of middle heat exchanger, heat exchanger in second are also provided
30, comprising: heat absorbing end 301, for being connected to 10/ temperature equipment of energy stores station (e.g., the first temperature equipment 1111 or the 4th
Temperature equipment 1221)；Release end of heat 302, for being connected to temperature equipment, (e.g., the second temperature equipment 1121 or third temperature adjustment are set
For 1211)/energy stores station 10；With, undirectional thermal conducting 31, heat absorbing end 301 and release end of heat 302 are arranged in undirectional thermal conducting
31 both ends.
Heat exchanger 30 in the second of the embodiment of the present invention, can be at energy stores station by increasing undirectional thermal conducting 31
When releasing energy to release end temperature equipment, accurately energy is provided for temperature equipment.In addition, applying also for when energy stores station
It cannot be carried out by the direction of setting between 10 and temperature equipment (absorption edge temperature equipment 1011 or release end temperature equipment 1021)
The case where energy transmission.When general progress heat transmitting, the low one end of temperature can only be transmitted to from the high one end of temperature, if heat is deposited
Temperature itself in storage station is higher than the medium temp of temperature equipment output, and at this point, heat storage sites are deposited there are many more heating load
The capacity of storage then can not carry out heat storage by direction initialization to heat storage sites at this time, will cause heat storage sites instead
Heat losses play opposite effect.When heat storage sites carry out heat release, and identical problem can be encountered.Therefore originally
Inventive embodiments provide the heat exchanger 30 in second, using undirectional thermal conducting 31 to (cold from temperature equipment guiding heat
Amount) storage sites medium temp, and be adjusted from the medium temp of heat (cooling capacity) storage sites guide device, can
There is provided accurate energy to release end temperature equipment, or make energy storage sites 10 and temperature equipment by direction initialization normally into
Row heat transfer.
Heat exchanger 30 in the second of the embodiment of the present invention, on the basis of being heat exchanger 20 in above-mentioned first,
Undirectional thermal conducting 31 is increased between heat absorbing end and release end of heat.Therefore, the absorption edge 301 of heat exchanger 30 and heat release in second
The structure setting at end 302 and role are identical as the heat absorbing end 201 of heat exchanger 20 in first and release end of heat 202,
It can refer to foregoing teachings, details are not described herein.
Therefore, it is being inhaled according to the first transfer heat exchanger I as described in Fig. 4 a to Fig. 4 f to VI structure of heat exchanger in first
Increase undirectional thermal conducting 31 can successively obtain heat absorbing end between hot end and release end of heat and release end of heat corresponds in consistent second
Heat exchanger VI in heat exchanger I to the second.The second transfer heat exchanger II 30 as shown in figure 4g is the transition heat in first
Increase undirectional thermal conducting 31 on the basis of device II 20 to obtain, as shown in figure 4h second in heat exchanger VI 30 be the
Increase what undirectional thermal conducting 31 obtained in one on the basis of heat exchanger VI 20.
Heat exchanger 30 in the second of the embodiment of the present invention, undirectional thermal conducting 31 are realized the heat (pressure) of heat absorbing end
It exchanges to release end of heat.Refrigerant heat exchanger or semiconductor temperature adjustor can specifically be used.
In an alternative embodiment, refrigerant heat exchanger includes evaporator 311, compressor (not shown), condenser 312
Heat-exchanging loop is connected and composed with expansion valve (not shown), four.Heat exchanger 30 includes two adiabatic heat-insulation settings in second
Absorb heat chamber 303 and heat release chamber 304；The heat absorbing end 301 of heat exchanger 30 is oppositely arranged in evaporator 311 and second, and is set
It sets in heat absorption chamber 303；The release end of heat 302 of heat exchanger 30 is oppositely arranged in condenser 312 and second, and is arranged in heat release
In chamber 304.
In an alternative embodiment, semiconductor temperature adjustor, including semiconductor chilling plate, setting are in semiconductor
The first end heat exchanger of the first end of cooling piece and the second end heat exchanger and power supply unit of second end.Power supply unit is used for
Electric energy is provided for semiconductor chilling plate.By controlling the direction of supply current, the first end and second of semiconductor chilling plate can be made
It holds and is switched under the cold both of which of heat production and production.For example, first end is cold end under forward current, second end is heat
End；Behind switching electric current direction, first end is switched to hot end, and second end is switched to cold end.Heat exchanger 30 includes two in second
The heat absorption chamber 303 and heat release chamber 304 of adiabatic heat-insulation setting；The heat absorbing end of heat exchanger 30 in first end heat exchanger and second
301 are oppositely arranged, and are arranged in heat absorption chamber 303；302 phase of release end of heat of heat exchanger 30 in second end heat exchanger and second
To setting, and it is arranged in heat release chamber 304.Determine that first end heat exchanger is hot end (or cold end) and the according to actual conditions
Two end heat exchangers are cold end (or hot end).
When needing to provide accurate energy to release end temperature equipment, alternatively, energy stores station 10 and temperature equipment it
Between when cannot carry out heat transmitting by direction initialization, start undirectional thermal conducting 31, force exchange to putting the heat of heat absorbing end 301
Hot end 302, then energy stores station 10 (perhaps absorption edge temperature equipment 1011 or release are transferred heat to by release end of heat 302
Hold temperature equipment 1021).
Middle heat exchanger is for shunting the energy discharged from energy stores station, and mixed cell is by multiple middle transition heats
Energy that device distributes obtains setting energy after neutralizing, then by mixed cell will set energy export to the setting energy phase
Matched temperature equipment side.Can matching accurately be provided to the release end temperature equipment of the energy release end with energy stores station
Energy.Specifically, it is possible to provide the medium of matched temperature.
In the embodiment of the present invention, the effect of mixed cell 41 is that will there is the medium of different-energy (temperature) to mix,
The medium of setting energy (set temperature) is obtained, then exports the medium to temperature equipment (release end temperature equipment 1021)
Side.Therefore, in a kind of specific embodiment, as shown in figure 5 a and 5b, the chamber that there are two the tools of mixed cell 41 separates, one
Feed liquor chamber 411, another is back to the fluid chamber room 412, and feed liquor chamber 411 has one or more input inlet tubes 4111, and
One or more output outlet tube 4112；Back to the fluid chamber room 412 has one or more input outlet tubes 4122 and one or more
A output inlet tube 4121.One input inlet tube 4111 and an input outlet tube 4122 constitute input terminal connecting pipeline group,
One output inlet tube 4121 and an output outlet tube 4112 constitute output end connecting pipeline group.One input terminal connecting pipeline
Group is connected to an output end pipeline group of middle heat exchanger, and the terminal of an output end pipeline group and temperature equipment side, which exchanges heat, to be filled
Set connection.The input terminal connecting pipeline group of mixed cell 41 be two or more, for it is two or more in
The connecting pipeline of first energy output end of heat exchanger is connected to.And the output end connecting pipeline group of mixed cell 41 can be one
Group or multiple groups at one group, are only connected to the terminal heat-exchanger rig of a temperature equipment.When multiple groups, set respectively with multiple temperature adjustments
Standby terminal heat-exchanger rig connection, provides energy for multiple temperature equipments, moreover, at this point, in each output end connecting pipeline group
Upper setting controlled valve, facilitates the folding of control section connecting pipeline, provides energy to be embodied as one or more temperature equipments.
The invention is not limited to the structures for being described above and being shown in the accompanying drawings, and can not depart from its model
It encloses and carry out various modifications and change.The scope of the present invention is limited only by the attached claims.
Claims (10)
1. a kind of control method of energy resource system, which is characterized in that the energy resource system includes two or more solar energy collection
Hot device and two or more water heaters are provided with terminal heat exchanger in the water heater；The energy resource system further includes two
Perhaps multiple middle heat exchangers and two or more mixed cells are described two or multiple middle heat exchangers in include one
Or heat exchanger and heat exchanger in one or more low temperature in multiple high temperature；The middle heat exchanger includes a heat absorption
End and multiple release end of heat, the heat absorbing end of the middle heat exchanger are connected to the solar thermal collector, the middle heat exchanger
Release end of heat is connected to the heat absorbing end of different mixed cells；The mixed cell includes two heat absorbing ends and a release end of heat, institute
The one of heat absorbing end for stating mixed cell is connected to heat exchanger in the high temperature, another heat absorbing end of the mixed cell
It is connected to heat exchanger in the low temperature, the release end of heat of the mixed cell is connected to the terminal of a corresponding water heater
Two heat absorbing ends of heat exchanger, the mixed cell are respectively arranged with heat absorption valve, and the release end of heat of the mixed cell is provided with
Heat release valve；
It the described method comprises the following steps:
According to the target temperature of the water heater, the open-minded of two heat absorption valves of the mixed cell being connected with the water heater is controlled
Time；
According to the difference of the target temperature of the water heater and actual temperature, putting for the mixed cell being connected with the water heater is controlled
The service time of thermal valve door.
2. the method as described in claim 1, which is characterized in that according to the target temperature of the water heater, control and the hot water
The step of service time of two heat absorption valves of the connected mixed cell of device, comprising:
According to the target temperature of the water heater, the target temperature of medium in terminal heat exchanger is obtained；
According to the target temperature of medium in terminal heat exchanger, two heat absorption valves of the mixed cell being connected with the water heater are adjusted
The service time of door.
3. the method as described in claim 1, which is characterized in that further include:
Obtain the quantity for the water heater being currently running；
According to the quantity for the water heater being currently running, the heat release valve timesharing for controlling the mixed cell being connected with the water heater is opened
It is logical.
4. method as claimed in claim 3, which is characterized in that the quantity for the water heater that the basis is currently running, control with
The step that the heat release valve timesharing of the connected mixed cell of the water heater is opened, comprising:
When the quantity for the water heater being currently running is less than preset value, the heat release for the mixed cell being connected with the water heater is controlled
Valve is full-time open-minded.
5. method as claimed in claim 3, which is characterized in that the quantity for the water heater that the basis is currently running, control with
The step that the valve timesharing of the connected mixed cell of the water heater is opened, comprising:
When the quantity for the water heater being currently running is greater than preset value, the heat release for the mixed cell being connected with the water heater is controlled
Valve timesharing is open-minded.
6. method as claimed in claim 5, which is characterized in that described when the quantity for the water heater being currently running is greater than preset value
When, control the step that the heat release valve timesharing for the mixed cell being connected with the water heater is opened, comprising: all water heaters use
Single-entry single-out switch mode carries out cycle heat exchange.
7. the method as described in claim 1, which is characterized in that further include:
According to the difference of the target temperature and actual temperature of the quantity for the water heater being currently running and each water heater, control with
The service time of the heat release valve of the connected mixed cell of each water heater.
8. the method for claim 7, which is characterized in that the heat release valve for the mixed cell being connected with the water heater
Service timeWherein, K is proportionality coefficient, Δ TnFor the target temperature and actual temperature of the water heater
Difference, Δ TavFor the average value of the difference of the target temperature and actual temperature of each water heater, tbaseFor benchmark service time.
9. method according to claim 8, which is characterized in that the benchmark service time tbaseAccording to the heat that is currently running
The quantity of hydrophone is arranged.
10. method according to claim 8, which is characterized in that the Δ TnThe difference for subtracting actual temperature for target temperature, when
ΔTnWhen≤0, the heat release valve for controlling mixed cell relevant to the water heater is closed.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201910018821.0A CN109764562B (en) | 2019-01-09 | 2019-01-09 | Control method of energy system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201910018821.0A CN109764562B (en) | 2019-01-09 | 2019-01-09 | Control method of energy system |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN109764562A true CN109764562A (en) | 2019-05-17 |
| CN109764562B CN109764562B (en) | 2020-09-25 |
Family
ID=66453615
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201910018821.0A Active CN109764562B (en) | 2019-01-09 | 2019-01-09 | Control method of energy system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN109764562B (en) |
Citations (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP0092251A2 (en) * | 1982-04-21 | 1983-10-26 | Hermann Kirchmayer | Device for the conversion of solar energy into heat |
| CN2580359Y (en) * | 2002-11-12 | 2003-10-15 | 苏日图 | Solar energy and gas burning mutual compensation heating device |
| CN101726156A (en) * | 2009-11-20 | 2010-06-09 | 皇明太阳能集团有限公司 | Process method and device for refrigeration, heating and water supply by utilizing solar energy |
| CN101907075A (en) * | 2010-06-25 | 2010-12-08 | 中山大学 | Multistage coupling heat accumulating type solar heat-power cogeneration system |
| WO2012021111A2 (en) * | 2010-08-10 | 2012-02-16 | Fkkp, S.R.O. | Tempering system |
| CN102985882A (en) * | 2010-05-05 | 2013-03-20 | 格林斯里弗斯有限公司 | Energy chassis and energy exchange device |
| CN103239134A (en) * | 2013-05-17 | 2013-08-14 | 上海电机学院 | Temperature adjustable and water amount controllable water dispenser |
| JP2015190696A (en) * | 2014-03-28 | 2015-11-02 | 大和ハウス工業株式会社 | Cogeneration system |
| CN108278784A (en) * | 2017-12-06 | 2018-07-13 | 上海交通大学 | A kind of heat pump heat distribution system becoming storage solar energy using heat-storage medium water phase |
-
2019
- 2019-01-09 CN CN201910018821.0A patent/CN109764562B/en active Active
Patent Citations (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP0092251A2 (en) * | 1982-04-21 | 1983-10-26 | Hermann Kirchmayer | Device for the conversion of solar energy into heat |
| CN2580359Y (en) * | 2002-11-12 | 2003-10-15 | 苏日图 | Solar energy and gas burning mutual compensation heating device |
| CN101726156A (en) * | 2009-11-20 | 2010-06-09 | 皇明太阳能集团有限公司 | Process method and device for refrigeration, heating and water supply by utilizing solar energy |
| CN102985882A (en) * | 2010-05-05 | 2013-03-20 | 格林斯里弗斯有限公司 | Energy chassis and energy exchange device |
| CN101907075A (en) * | 2010-06-25 | 2010-12-08 | 中山大学 | Multistage coupling heat accumulating type solar heat-power cogeneration system |
| WO2012021111A2 (en) * | 2010-08-10 | 2012-02-16 | Fkkp, S.R.O. | Tempering system |
| CN103239134A (en) * | 2013-05-17 | 2013-08-14 | 上海电机学院 | Temperature adjustable and water amount controllable water dispenser |
| JP2015190696A (en) * | 2014-03-28 | 2015-11-02 | 大和ハウス工業株式会社 | Cogeneration system |
| CN108278784A (en) * | 2017-12-06 | 2018-07-13 | 上海交通大学 | A kind of heat pump heat distribution system becoming storage solar energy using heat-storage medium water phase |
Also Published As
| Publication number | Publication date |
|---|---|
| CN109764562B (en) | 2020-09-25 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN109764460A (en) | A kind of energy resource system and control method | |
| CN109742978A (en) | A kind of energy source station and its control method | |
| CN109757906A (en) | A kind of control method of energy resource system | |
| CN109757904A (en) | A kind of control method of energy resource system | |
| CN109764451A (en) | A kind of control method of energy resource system | |
| CN109764550A (en) | A kind of control method of energy resource system | |
| CN109764506A (en) | A kind of control method of energy resource system | |
| CN109764562A (en) | A kind of control method of energy resource system | |
| CN109883057A (en) | A kind of mixed water tank and its control method, energy source station | |
| CN109764563A (en) | A kind of control method of energy resource system | |
| CN109945530A (en) | A kind of control method of energy resource system | |
| CN109855227A (en) | Energy resource system, the control method and device of energy resource system, storage medium | |
| CN109883056A (en) | A kind of control method of energy resource system | |
| CN109757914A (en) | A kind of control method of energy resource system | |
| CN109757919A (en) | A kind of control method of energy resource system | |
| CN109737611A (en) | A kind of control method of energy resource system | |
| CN109907581A (en) | A kind of control method of energy resource system | |
| CN109855345A (en) | A kind of control method of energy resource system | |
| CN109882900A (en) | A kind of control method of energy resource system | |
| CN109757899A (en) | A kind of control method of energy resource system | |
| CN109757915A (en) | A kind of control method of energy resource system | |
| CN109764540A (en) | A kind of control method of energy resource system | |
| CN109885110A (en) | A kind of control method of energy resource system | |
| CN109798568A (en) | A kind of control method of energy resource system | |
| CN109764546A (en) | A kind of control method of energy resource system |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PB01 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20201105 Address after: 266101 Haier Industrial Park, Haier Road, Laoshan District, Shandong, Qingdao, China Patentee after: QINGDAO HAIER AIR CONDITIONER GENERAL Corp.,Ltd. Patentee after: Haier Smart Home Co., Ltd. Address before: 266101 Haier Industrial Park, Haier Road, Laoshan District, Shandong, Qingdao, China Patentee before: QINGDAO HAIER AIR CONDITIONER GENERAL Corp.,Ltd. |
|
| TR01 | Transfer of patent right |