CN104315753B - A kind of cold, heat and power triple supply system for including energy tower - Google Patents
A kind of cold, heat and power triple supply system for including energy tower Download PDFInfo
- Publication number
- CN104315753B CN104315753B CN201410543682.0A CN201410543682A CN104315753B CN 104315753 B CN104315753 B CN 104315753B CN 201410543682 A CN201410543682 A CN 201410543682A CN 104315753 B CN104315753 B CN 104315753B
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- Prior art keywords
- liquid storage
- solution
- storage disk
- concentrated solution
- energy tower
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- 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.)
- Expired - Fee Related
Links
- 239000007788 liquid Substances 0.000 claims abstract description 156
- 238000010521 absorption reaction Methods 0.000 claims abstract description 14
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 claims description 22
- 239000003546 flue gas Substances 0.000 claims description 22
- 239000007789 gas Substances 0.000 claims description 12
- 238000002485 combustion reaction Methods 0.000 claims description 7
- 239000000945 filler Substances 0.000 claims description 4
- 238000000034 method Methods 0.000 claims description 4
- 238000012806 monitoring device Methods 0.000 claims description 4
- 230000008569 process Effects 0.000 claims description 4
- 235000019504 cigarettes Nutrition 0.000 claims 1
- 239000002918 waste heat Substances 0.000 abstract description 7
- 230000001681 protective effect Effects 0.000 abstract description 2
- 239000003517 fume Substances 0.000 abstract 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 6
- 230000005611 electricity Effects 0.000 description 4
- 238000005516 engineering process Methods 0.000 description 3
- 230000004048 modification Effects 0.000 description 3
- 238000012986 modification Methods 0.000 description 3
- 238000012544 monitoring process Methods 0.000 description 3
- 230000008859 change Effects 0.000 description 2
- 230000007613 environmental effect Effects 0.000 description 2
- 238000007710 freezing Methods 0.000 description 2
- 230000008014 freezing Effects 0.000 description 2
- 239000000446 fuel Substances 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- AMXOYNBUYSYVKV-UHFFFAOYSA-M lithium bromide Chemical compound [Li+].[Br-] AMXOYNBUYSYVKV-UHFFFAOYSA-M 0.000 description 2
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 2
- 238000010248 power generation Methods 0.000 description 2
- 238000004064 recycling Methods 0.000 description 2
- 238000005057 refrigeration Methods 0.000 description 2
- 230000008901 benefit Effects 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- 239000012120 mounting media Substances 0.000 description 1
- 239000003345 natural gas Substances 0.000 description 1
- 230000001737 promoting effect Effects 0.000 description 1
- 239000000779 smoke Substances 0.000 description 1
- 238000010257 thawing Methods 0.000 description 1
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B29/00—Combined heating and refrigeration systems, e.g. operating alternately or simultaneously
- F25B29/006—Combined heating and refrigeration systems, e.g. operating alternately or simultaneously of the sorption type system
Abstract
The invention discloses a kind of cold, heat and power triple supply systems for including energy tower, it includes prime mover generating equipment being sequentially connected(1), absorption type heat pump assembly(2), solution condensing device(3), concentrated solution liquid storage disk(4), concentrated solution liquid storage device(5), energy tower liquid storage disk(6), energy tower(7), energy tower liquid storage disk(6)With weak solution liquid storage device(8)It is connected, weak solution liquid storage device(8)With concentrated solution liquid storage disk(4)It is connected, energy tower liquid storage disk(6)Pass through pipeline and evaporator(9)It is connected, evaporator(9)Pass through pipeline and energy tower(7)It is connected, evaporator(9)It is connected with condenser(10).The present invention is reasonable in design, easy to operate, can make full use of fume waste heat, energy utilization rate is high, environmentally protective, easily promotes, it can especially solve the problems, such as circulation solution concentration and solution concentration On-line Control of the energy tower when cold, heat and power triple supply system is applied, high degree of automation.
Description
Technical field
The present invention relates to one kind to belong to energy device, and in particular to using cold, heat and electricity three-way of the energy tower as system heat sources
For system.
Background technology
Energy tower heat pump is that a kind of appearance is in turriform, and using air as heat source, the heat exchange for passing through tower body and air acts on, and realizes
Refrigeration, heating and the new equipment that the multiple functions such as domestic hot-water are provided.Although the heat source of energy tower heat pump system is also from sky
Gas, but it is different from the mode that conventional air source heat pump obtains energy from air, but utilize water resource heat pump by energy tower from
The low-grade heat source absorbed in air provides domestic hot-water for freezing, for warm.In summer, energy tower heat pump unit is the energy
Tower is as cooling tower, and using the evaporative heat loss of water, Energy Efficiency Ratio is up to more than 5.0;In winter, energy tower heat pump unit utilizes freezing point
Low-grade heat under the higher low temperature environment of mounting medium less than 0 DEG C, -9 DEG C of high efficiency extraction or more, relative humidity in air
Heat supply can be carried out, solves the problems, such as conventional air source heat pump temperature, the electricity auxiliary for eliminating conventional air source heat pump adds
Heat.
But as energy tower absorbs the latent heat in air, circulatory mediator solution concentration will reduce constantly, weak solution how into
Row concentration recycling is a critical issue in energy tower application process.It is sharp again that solution concentration is carried out currently with conventional energy resource
With, the energy cost of consumption is more than the energy consumption of air source heat pump defrosting sometimes, influences system winter operation entirety efficiency, and
The storage of weak solution will occupy a large amount of land area, influence its utilization and extention, and the concentration of energy tower circulation solution and solution are dense
Degree automatically control be the energy tower technology application major obstacle.
Invention content
Goal of the invention:It, should It is an object of the present invention to solve the deficiency of the existing technology and provide a kind of reasonable in design
With in extensive range, convenient operation and control, environmental protection and energy saving can make full use of heat source, especially can efficiently realize that weak solution concentration is sharp again
By the use of using energy tower as the cold, heat and power triple supply system of system heat sources.The cold, heat and power triple supply system can solve winter heat source
Insufficient problem greatly promotes system winter saving energy, and relative to conventional system, system winter saving energy rate promotes 30% ~ 40%.
Technical solution:In order to achieve the object of the present invention, the technical solution adopted by the present invention is:
A kind of cold, heat and power triple supply system for including energy tower, it includes prime mover generating equipment, generates electricity with prime mover
The absorption type heat pump assembly that equipment is connected, the solution condensing device being connected with absorption type heat pump assembly by flue gas delivery pipe road,
The concentrated solution liquid storage disk being connected with solution condensing device, the concentrated solution liquid storage device being connected with concentrated solution liquid storage disk are stored up with concentrated solution
The energy tower liquid storage disk that liquid device is connected, energy tower liquid storage disk are connected with energy tower, and the energy tower liquid storage disk is stored up with weak solution
Liquid device is connected, and weak solution liquid storage device is connected with concentrated solution liquid storage disk, and the energy tower liquid storage disk passes through pipeline and evaporator phase
Even, evaporator is connected by pipeline with energy tower, and evaporator is connected with condenser;
The solution condensing device is connected with flue gas emission pipeline.
Preferably, the above-described cold, heat and power triple supply system for including energy tower, solution concentration
Liquid pump processed is installed on the pipeline that device is connected with concentrated solution liquid storage disk.When solution concentration is less than concentrated solution in concentrated solution liquid storage disk
When storing concentration requirement, liquid pump processed is opened by computerized control system, solution in concentrated solution liquid storage disk is transported to solution concentration
Device carries out concentration until reaching the concentration of needs.
Preferably, the above-described cold, heat and power triple supply system for including energy tower, concentrated solution storage
Liquid storage pump is installed on the pipeline that liquid disk is connected with concentrated solution liquid storage device.When solution concentration reaches requirement in concentrated solution liquid storage disk
When, liquid storage is opened by computerized control system and is pumped, concentrated solution is delivered to concentrated solution liquid storage device, until filling or concentrated solution liquid storage
Disk liquid level drops to minimum liquid level requirement.
Preferably, the above-described cold, heat and power triple supply system for including energy tower, concentrated solution storage
Concentration control pump is installed on the pipeline that liquid device is connected with energy tower liquid storage disk.When in energy tower liquid storage disk solution concentration less than setting
During fixed circulating solution concentration, concentration control pump is opened by computerized control system, until solution concentration in energy tower liquid storage disk
Reach the circulating solution concentration of setting.
Preferably, the above-described cold, heat and power triple supply system for including energy tower, weak solution storage
Elevator pump is installed on the pipeline that liquid device is connected with concentrated solution liquid storage disk.Can elevator pump be opened by computerized control system, it will
The solution reduced from energy tower liquid storage disk concentration, is transported to by weak solution liquid storage device in concentrated solution liquid storage disk by elevator pump,
Realize cycle.
Preferably, the above-described cold, heat and power triple supply system for including energy tower, the absorption type heat
Flue gas delivery pipe road between pump assembly and solution condensing device is connected with branch, and flue gas delivery pipe Lu Yuzhi roads are all pacified
Equipped with switch valve.When solution concentration is less than concentrated solution storage concentration requirement, computerized control system will open flue gas delivery pipe
The switch valve on road, the flue gas of high-temperature are transported to solution condensing device, provide thermal energy to the low concentration in solution condensing device
Solution is concentrated, and is then exhausted from using the flue gas after waste heat, the smoke heat energy that absorption type heat pump assembly is made full use of to discharge, environmental protection
Property is stronger.
Preferably, the above-described cold, heat and power triple supply system for including energy tower, described prime mover hair
Electric equipment is gas internal-combustion engine, gas turbine or miniature combustion engine etc..
Preferably, the above-described cold, heat and power triple supply system for including energy tower, concentrated solution storage
Concentration sensor is mounted in liquid disk and energy tower liquid storage disk.Level monitoring dress is installed in the weak solution liquid storage device
It puts.And the concentration sensor, level monitoring device, liquid pump processed, liquid storage pump, concentration control pump elevator pump and switch valve
It is connected with computerized control system.Concentration sensor can solution in real time on-line monitoring concentrated solution liquid storage disk and energy tower liquid storage disk
Concentration, so as to by computerized control system come open associated pump realize concentration control, the degree of automation higher, working efficiency
Higher.
The cold, heat and power triple supply system provided by the invention for including energy tower, can be dynamic using original using natural gas as fuel
Machine(The equipment such as gas turbine, gas internal-combustion engine or miniature combustion engine)Power generation, lithium bromide absorption type heat pump unit, while recycle prime mover
The waste heat of generation, waste heat are utilized winter for heating in the form of flue gas, steam or hot water, and summer then passes through Absorption Refrigerator
Refrigeration, while domestic hot-water can also be provided.Cold, heat and power triple supply system can realize the Efficient Conversion and cascade utilization of the energy, connection
Fuel combustion waste heat and waste heat can be made full use of for system, primary energy ratio is up to more than 70%, and overall efficiency is higher than
Conventional system.Energy tower is introduced combined supply system by the present invention, can solve the problems, such as winter heat source insufficiency, greatly promotes system winter
Energy saving, relative to conventional system, system winter saving energy rate promotes about 30% -40%.And combined supply system is made full use of to pass through
The flue gas after absorption heat pump heat exchange utilizes is crossed, exhaust gas temperature is generally at 100 DEG C or more, using the waste heat effectively to energy tower
Weak solution is concentrated, and does not expend other energy, and can be with On-line Control solution concentration, to energy tower in combined supply system
Using there is high promotional value.
Advantageous effect:Compared to the prior art the cold, heat and power triple supply system provided by the invention for including energy tower has
It has the advantage that:
The cold, heat and power triple supply system provided by the invention for including energy tower, it is reasonable in design, have a wide range of application
It is general, it is easy to operate, the energy can be made full use of, it is environmentally protective, it easily promotes, can especially solve energy tower in cold, heat and electricity triple supply system
Circulation solution concentration and solution concentration On-line Control problem during system application, high degree of automation.
Description of the drawings
Fig. 1 is the structure diagram of the cold, heat and power triple supply system provided by the invention for including energy tower.
Specific embodiment
In the following with reference to the drawings and specific embodiments, the present invention is furture elucidated, it should be understood that these embodiments are merely to illustrate
It the present invention rather than limits the scope of the invention, after the present invention has been read, those skilled in the art are to of the invention each
The modification of kind equivalent form falls within the application range as defined in the appended claims.
As shown in Figure 1, a kind of cold, heat and power triple supply system for including energy tower, it includes prime mover generating equipment(1),
With prime mover generating equipment(1)Connected absorption type heat pump assembly(2), with absorption type heat pump assembly(2)Pass through flue gas delivery pipe
The solution condensing device that road is connected(3), with solution condensing device(3)Connected concentrated solution liquid storage disk(4), with concentrated solution liquid storage disk
(4)Connected concentrated solution liquid storage device(5), with concentrated solution liquid storage device(5)Connected energy tower liquid storage disk(6), energy tower liquid storage disk
(6)It is connected with energy tower(7), the energy tower liquid storage disk(6)With weak solution liquid storage device(8)It is connected, weak solution liquid storage device(8)
With concentrated solution liquid storage disk(4)It is connected, the energy tower liquid storage disk(6)Pass through pipeline and evaporator(9)It is connected, evaporator(9)
Pass through pipeline and energy tower(7)It is connected, evaporator(9)It is connected with condenser(10);
The solution condensing device(3)It is connected with flue gas emission pipeline.
The above-described cold, heat and power triple supply system for including energy tower, the solution condensing device(3)With it is dense molten
Liquid liquid storage disk(4)Liquid pump processed is installed on connected pipeline(11).The concentrated solution liquid storage disk(4)With concentrated solution liquid storage device
(5)Liquid storage pump is installed on connected pipeline(12).The concentrated solution liquid storage device(5)With energy tower liquid storage disk(6)Connected
Concentration control pump is installed on pipeline(13).The weak solution liquid storage device(8)With concentrated solution liquid storage disk(4)On connected pipeline
Elevator pump is installed(14).
The above-described cold, heat and power triple supply system for including energy tower, the absorption type heat pump assembly(2)With it is molten
Liquid enrichment facility(3)Between flue gas delivery pipe road be connected with branch, and flue gas delivery pipe Lu Yuzhi roads are fitted with cutting
Change valve(15).
The above-described cold, heat and power triple supply system for including energy tower, which is characterized in that prime mover power generation
Equipment(1)For gas internal-combustion engine or gas turbine etc..
The above-described cold, heat and power triple supply system for including energy tower, the concentrated solution liquid storage disk(4)And the energy
Tower liquid storage disk(6)In be mounted on concentration sensor.The weak solution liquid storage device(8)In level monitoring device is installed.
The above-described cold, heat and power triple supply system for including energy tower, the concentration sensor, level monitoring dress
It puts, liquid pump processed(11), liquid storage pump(12), concentration control pump(13)Elevator pump(14)And switch valve(15)And computer control is
System is connected.
It is of the present invention include energy tower cold, heat and power triple supply system practical work process be, when concentrated solution liquid storage
Disk(4)When middle solution concentration is less than concentrated solution storage concentration requirement, computerized control system will open cutting for flue gas delivery pipe road
Change valve(15), close branch road switch valve(15), flue tail gas is transported to solution condensing device(3).Liquid pump processed simultaneously
(11)It opens, weak solution passes through solution condensing device(3)In liquid distributor be sprayed in filler, high-temperature flue gas will be in weak solution
Excessive moisture is taken away, concentrated solution liquid storage disk(4)The concentrated solution produced is collected below filler.By constantly recycling, make concentrated solution
Liquid storage disk(4)Middle solution concentration reaches liquid pump processed after sets requirement(11)Stop, being then turned off the switching of flue gas delivery pipe road
Valve(15), open branch road switch valve(15).Solution is in concentrated solution liquid storage device(5), energy tower liquid storage disk(6), weak solution
Liquid storage device(8), concentrated solution liquid storage disk(4)Circulation process in four device for storing liquid is:Energy tower liquid storage disk(6)Middle weak solution exists
When liquid level reaches overflow requirement, weak solution flow to weak solution liquid storage device(8);Weak solution liquid storage device(8)When middle liquid level reaches requirement,
Elevator pump(14)Start, weak solution is sent to concentrated solution liquid storage disk(4)In;Solution concentration is less than concentrated solution in concentrated solution liquid storage disk
When storing concentration requirement, liquid pump processed is opened(11);Concentrated solution liquid storage disk(4)When middle solution concentration reaches requirement, liquid storage pump is opened
(12), until concentrated solution liquid storage device(5)It fills or concentrated solution liquid storage disk(4)Liquid level drops to minimum liquid level requirement.Work as energy tower
Liquid storage disk(6)When middle solution concentration is less than the circulating solution concentration set, concentration control pump is opened(13), until energy tower liquid storage
Disk(6)Middle solution concentration reaches the circulating solution concentration of setting.
The above is only the preferred embodiment of the present invention, it is noted that for the ordinary skill people of the art
For member, various improvements and modifications may be made without departing from the principle of the present invention, these improvements and modifications also should
It is considered as protection scope of the present invention.
Claims (1)
1. a kind of cold, heat and power triple supply system for including energy tower, which is characterized in that it includes prime mover generating equipment (1),
The absorption type heat pump assembly (2) being connected with prime mover generating equipment (1) passes through flue gas delivery pipe with absorption type heat pump assembly (2)
The solution condensing device (3) that road is connected, the concentrated solution liquid storage disk (4) being connected with solution condensing device (3), with concentrated solution liquid storage disk
(4) connected concentrated solution liquid storage device (5), the energy tower liquid storage disk (6) being connected with concentrated solution liquid storage device (5), energy tower liquid storage disk
(6) energy tower (7) is connected with, the energy tower liquid storage disk (6) is connected with weak solution liquid storage device (8), weak solution liquid storage device (8)
It is connected with concentrated solution liquid storage disk (4), the energy tower liquid storage disk (6) is connected by pipeline with evaporator (9), evaporator (9)
It is connected by pipeline with energy tower (7), evaporator (9) is connected with condenser (10);
The solution condensing device (3) is connected with flue gas emission pipeline;
Liquid pump processed (11) is installed on the pipeline that the solution condensing device (3) is connected with concentrated solution liquid storage disk (4);
Liquid storage pump (12) is installed on the pipeline that the concentrated solution liquid storage disk (4) is connected with concentrated solution liquid storage device (5);
Concentration control pump (13) is installed on the pipeline that the concentrated solution liquid storage device (5) is connected with energy tower liquid storage disk (6);
Elevator pump (14) is installed on the pipeline that the weak solution liquid storage device (8) is connected with concentrated solution liquid storage disk (4);
Flue gas delivery pipe road between the absorption type heat pump assembly (2) and solution condensing device (3) is connected with branch, and
Flue gas delivery pipe Lu Yuzhi roads are fitted with switch valve (15);
Prime mover generating equipment (1) is gas internal-combustion engine or gas turbine;
Concentration sensor is mounted in the concentrated solution liquid storage disk (4) and energy tower liquid storage disk (6);
Level monitoring device is installed in the weak solution liquid storage device (8);
The concentration sensor, level monitoring device, liquid pump processed (11), liquid storage pump (12), concentration control pump (13),
Elevator pump (14) is connected with switch valve (15) with computerized control system;
When solution concentration is less than concentrated solution storage concentration requirement in concentrated solution liquid storage disk (4), computerized control system will open cigarette
The switch valve of letter shoot road closes branch road switch valve, flue tail gas is transported to solution condensing device (3);Together
When, liquid pump (11) processed is opened, and weak solution is sprayed to by the liquid distributor in solution condensing device (3) in filler, high-temperature flue gas
Excessive moisture in weak solution is taken away, concentrated solution liquid storage disk (4) collects the concentrated solution produced below filler;By constantly following
Ring makes solution concentration in concentrated solution liquid storage disk (4) reach liquid pump (11) stopping processed after sets requirement, is then turned off flue gas delivery pipe
The switch valve of road opens branch road switch valve;Solution is in concentrated solution liquid storage device (5), energy tower liquid storage disk (6), dilute molten
Circulation process in (4) four liquid liquid storage device (8), concentrated solution liquid storage disk device for storing liquid is:Weak solution in energy tower liquid storage disk (6)
When liquid level reaches overflow requirement, weak solution flow to weak solution liquid storage device (8);Liquid level reaches requirement in weak solution liquid storage device (8)
When, elevator pump (14) starts, and weak solution is sent into concentrated solution liquid storage disk (4);Solution concentration is less than dense in concentrated solution liquid storage disk
When solution stores concentration requirement, liquid pump (11) processed is opened;When solution concentration reaches requirement in concentrated solution liquid storage disk (4), storage is opened
Liquid pump (12), until concentrated solution liquid storage device (5) is filled or concentrated solution liquid storage disk (4) liquid level drops to minimum liquid level requirement;Work as energy
When solution concentration is less than the circulating solution concentration set in source tower liquid storage disk (6), concentration control pump (13) is opened, until energy tower
Solution concentration reaches the circulating solution concentration of setting in liquid storage disk (6).
Priority Applications (1)
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CN201410543682.0A CN104315753B (en) | 2014-10-15 | 2014-10-15 | A kind of cold, heat and power triple supply system for including energy tower |
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CN201410543682.0A CN104315753B (en) | 2014-10-15 | 2014-10-15 | A kind of cold, heat and power triple supply system for including energy tower |
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CN104315753A CN104315753A (en) | 2015-01-28 |
CN104315753B true CN104315753B (en) | 2018-06-22 |
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CN108469188A (en) * | 2018-03-08 | 2018-08-31 | 青岛大学 | A kind of cooling tower demisting and sub-cooled return water waste heat grade lifting system |
CN110319616B (en) * | 2019-06-26 | 2021-03-05 | 上海理工大学 | Frostless type gas heat pump system |
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---|---|---|---|---|
CN103604249A (en) * | 2013-11-12 | 2014-02-26 | 清华大学 | Energy tower absorption type hot and cold water unit |
CN203478477U (en) * | 2013-07-30 | 2014-03-12 | 东南大学 | Heat source tower heat pump system for efficient recovery of regenerative heat |
CN103644677A (en) * | 2013-12-05 | 2014-03-19 | 东南大学 | Solution regeneration device based on throttling flash and capable of realizing self-balance of regenerated energy |
CN203671989U (en) * | 2013-10-29 | 2014-06-25 | 山东禄禧新能源科技有限公司 | Unit for combined supply of cooling, heating and power |
CN204165276U (en) * | 2014-10-15 | 2015-02-18 | 江苏省绿色建筑工程技术研究中心有限公司 | Include the cold, heat and power triple supply system of energy tower |
Family Cites Families (1)
Publication number | Priority date | Publication date | Assignee | Title |
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JPS5944516A (en) * | 1982-09-06 | 1984-03-13 | Osaka Gas Co Ltd | Apparatus equipped with combustion furnace |
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2014
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Patent Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN203478477U (en) * | 2013-07-30 | 2014-03-12 | 东南大学 | Heat source tower heat pump system for efficient recovery of regenerative heat |
CN203671989U (en) * | 2013-10-29 | 2014-06-25 | 山东禄禧新能源科技有限公司 | Unit for combined supply of cooling, heating and power |
CN103604249A (en) * | 2013-11-12 | 2014-02-26 | 清华大学 | Energy tower absorption type hot and cold water unit |
CN103644677A (en) * | 2013-12-05 | 2014-03-19 | 东南大学 | Solution regeneration device based on throttling flash and capable of realizing self-balance of regenerated energy |
CN204165276U (en) * | 2014-10-15 | 2015-02-18 | 江苏省绿色建筑工程技术研究中心有限公司 | Include the cold, heat and power triple supply system of energy tower |
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