CN204187889U - A kind of co-generation system based on hot and cold, electric multiple-energy-source - Google Patents

A kind of co-generation system based on hot and cold, electric multiple-energy-source Download PDF

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CN204187889U
CN204187889U CN201420603191.6U CN201420603191U CN204187889U CN 204187889 U CN204187889 U CN 204187889U CN 201420603191 U CN201420603191 U CN 201420603191U CN 204187889 U CN204187889 U CN 204187889U
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heat
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许诺言
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Huazhong University of Science and Technology
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Abstract

The utility model discloses a kind of co-generation system based on hot and cold, electric multiple-energy-source, comprise compression absorption heat pump cycle, cryogenic fluid power generation cycle and Driven by Solar Energy absorption refrigeration heating cycle; Utilize the low temperature geothermal water of 80 DEG C ~ 90 DEG C as driving heat source, by absorbing compression heat pump device, improving the temperature of low-temperature electricity-generating working medium chloroethanes, promoting turbine generation, flowing to electric user; Utilize Driven by Solar Energy Lithium Bromide Absorption Refrigeration Cycle device, for electricity generation system provides necessary cold, unnecessary cold then brings colod-application family by chilled water simultaneously; Part solar energy supplies heat user by heat storage water tank.These hot and cold, electric three co-generation systems are while comprehensive energy utilization, reduce the consumption of non-renewable energy resources to greatest extent, reduce toxic emission and pollution, energy utilization rate is high, effects of energy saving and emission reduction is obvious, is also that popularization and the comprehensive utilization of cryogenically heat energy and solar energy provides reference simultaneously.

Description

A kind of co-generation system based on hot and cold, electric multiple-energy-source
Technical field
The utility model belongs to distributed energy technical field, more specifically, relates to a kind of co-generation system based on hot and cold, electric multiple-energy-source.
Background technology
(Combined Cooling Heating and Power is produced in hot and cold, Electricity Federation, CCHP) be that one is based upon on cascaded utilization of energy conceptual foundation, will freeze, heat the supply system of (comprising for warm supplying hot water) and power generation process integration.Its maximum feature is exactly carry out cascade utilization to the energy of different quality, temperature higher, the heat energy with larger available energy is used to generating, the heat energy that temperature is lower is then used to heat supply or refrigeration.Not only increase the utilization ratio of the energy like this, and decrease the discharge of carbide and pernicious gas, also there is good economic benefit and social benefit.
As far back as 2000, long-rangely to develop cooperatively " hot and cold, cogeneration system " with USDOE, Oak Ridge National Laboratory, University of Maryland, long-range Central Air-Conditioner is carried out " without seam " with the American-European GTG produced combine, larger Central Air-Conditioner joins less generator: combustor GTG tail gas being introduced Central Air-Conditioner.Generator tail gas utilization rate of waste heat is 80% ~ 90%.Less Central Air-Conditioner is equipped with larger generator: a combustor GTG tail gas part being introduced Central Air-Conditioner, a part introduces custom-designed waste heat generator.Generator tail gas utilization rate of waste heat about 40% ~ 80%.Directly use generator tail gas cooling and warming: specialized designs tail gas generator, generator tail gas is all introduced generator.Generator tail gas utilization rate of waste heat is 40% ~ 70%.
Although in power industry, generating set capacity is larger, and efficiency is higher, and per kilowatt investment is lower, and cost of electricity-generating is also lower; But in particular cases many, it is the indispensable important supplement of centrally connected power supply that is produced from small-sized hot and cold, Electricity Federation:
(1) demand that can meet special occasions is produced in small-sized hot and cold, Electricity Federation.Such as, to power supply safety stability requirement high user, as hospital, bank etc.; The comparatively diversified user of energy demand, also needs the supply of heat or cold energy while needing electric power.
(2) small-sized hot and cold, Electricity Federation is produced power supply mode and can be made up the deficiency of bulk power grid in security and stability.Small gas cogeneration of heat and power system is actual is a kind of internet of energy facilities, it by cellular small-sized, carry out being connected to each other of energy supply facility, improve the energy supply reliability in city, under mains breakdown and unexpected storms (such as earthquake, snowstorm, artificial destruction, war) situation, the power supply of responsible consumer can be maintained.
(3) small-sized hot and cold, that Electricity Federation product power supply mode is the energy comprehensive cascade utilization provides possibility.In the centralized power supply system of routine, form of energy is relatively single-.When user not only needs electric power, and need the confession of other form of energy as cold energy and heat energy seasonable, when meeting above-mentioned needs by means of only electric power, be difficult to the comprehensive cascade utilization realizing energy; And power supply mode is produced with features such as its small scale, flexibility are strong in small-sized hot and cold, Electricity Federation, the organic combination circulated by difference can realize the comprehensive cascade utilization of energy while meeting consumers' demand, and overcome cold energy and heat energy cannot the difficulty of long-distance transmissions.
(4) small gas cogeneration of heat and power can more effective resource allocation, stablize, utilize the resource such as natural gas, coal bed gas constantly, reduce the adjustment of combustion gas, reduce the reserve-production ratio decline because gas peak regulation causes, the wasting of resources that underground natural gas storage tank loss etc. are unnecessary, reduces the construction investment of gas ductwork, improves equipment operating efficiency, thus reach and reduce combustion gas and utilize cost, improve the competitiveness of use gas enterprise.
(5) under planned economic system, industry divides with product, and product and the task of energy facilities are single, electric power, heating power, combustion gas are independent separately, and the overlapping investment construction of energy facilities, adds operating cost, reduce efficiency, directly cause the raising of energy cost.Small-sized hot and cold, Electricity Federation is produced and has been broken traditional boundary, heating, hot water, electricity, cold, combustion gas, water resources rational use and environmental pollution improvement are considered as a whole, with minimum fund, resources and environment cost, exchange the highest returns of investment, energy conversion efficiency and energy facilities usefulness for.
(6) not only self-pollution is little for small cogeneration, and the regulation effect of environmental pollution is also very outstanding.Substantially do not have the pollution of sulfur dioxide, carbon monoxide and dust, nitrogen oxide is 25-65ppm, is the 1/10-1/20 of coal-fired utility.Because the efficiency of energy utilization of user side is high, real minimizing carbon dioxide isothermal chamber gas purging.Gas turbine generating itself does not need substantially with water, and required water is all that water-saving performance is fabulous for heat supply.
Although hot and cold, chp system exists above-mentioned advantage, still there is following shortcoming in existing hot and cold, chp system: one is hot and cold, chp system small scale, is arranged in building, can only uses natural gas or oil product; Although two are hot and cold, chp system scales than big power station and large-scale cogeneration of heat and power little, but is produced from small-sized hot and cold, Electricity Federation littlely can not install one to single household, hot and cold, the CCHP of a building Huo Yige community, building can only be adapted to, flexible unlike small-sized household air-conditioner, family water heater or family space heater.
Therefore, for the shortcoming that current small-sized hot and cold, electric system exists, the utility model proposes a kind of novel hot and cold, cogeneration system, use cryogenically heat energy and solar association to drive.This kind of system, under the prerequisite of advantage having hot and cold, the electric combined supply system of tradition, can also be broken away from the dependence of traditional combined supply system to natural gas, the oil product energy, rely on the coupling of the multiple low grade energy, improve the utilization rate of the energy; Realize the zero-emission of pollutant, the propelling of energy-saving and emission-reduction is had great importance.
The utility model adopts geothermal energy.The utilization of geothermal energy can be divided into geothermal power generation for now and directly utilize two large classes, is approximately 7000MW ~ 8500MW in the world at present for the geothermal energy resources generated electricity and directly utilize.As shown in table 1, geothermal energy resources can be divided into high temperature, middle gentle low temperature three class by temperature.The underground heat that temperature is greater than 150 DEG C exists in vapour form, is high-temperature geothermal; The underground heat of 90 DEG C-150 DEG C exists with forms such as the mixtures of water and steam, is middle temperature underground heat; Temperature is greater than 25 DEG C, is less than the underground heat of 90 DEG C with form existence such as warm water (25 DEG C-40 DEG C), warm water's (40 DEG C-60 DEG C), hot water (60 DEG C-90 DEG C), is low temperature underground heat.
Table 1 geothermal energy resources press temperature classifications
China's geothermal energy resources are very abundant, report according to interrelated data, China has high-temperature geothermal system more than 180, high-temperature geothermal systems generate electricity potentiality are at 6,740,000 more than kW, middle low temperature geothermal field is extensively distributed in the inside of plate, and the geothermal field of China North China, Beijing-Tianjin area belongs to middle low temperature geothermal field more, has found natural hot spring 2700 many places, artificial hot water is appeared about 130 places, fully utilizes 300 places.
Because middle high-temperature geothermal resource has higher fire value, can be higher so be used for generating efficiency, but geothermal power generation requires higher to underground hot water temperature, and the thermal efficiency is lower.Statistics, the cycle efficieny of 165 DEG C of geothermal energy resources generatings is 12%.In the world in the geothermal energy resources of more than 90 DEG C, only have about 25% for high temperature heat source, all the other are the middle temperature-heat-source of less than 150 DEG C.And middle low-temperature geothermal resource major part directly utilizes.Because in world wide, energy shortage increasingly sharpens, world environments progressively worsens, and how to find new alternative energy source and how more effectively to utilize known energy source to become the problem of joint research in world wide.
Along with the continuous progress of heat pump techniques and the maturation of high-temperature geothermal generation technology, the temperature utilizing heat pump to improve low temperature underground heat to generate electricity this technology approve by people.Utilize heat pump techniques, set up a kind of absorption compression heat pump-electricity generation system, utilize Driven by Solar Energy Lithium Bromide Absorption Refrigeration Cycle to provide necessary cold for electricity generation system simultaneously, unnecessary cold flows to colod-application family, unnecessary heat is supplied to heat user by heat storage water tank, thus realize multi-heat source coupling, hot and cold, electric three coproduction.Wish the Land use systems that can improve the energy in this way, what expand the existing energy utilizes scope, realizes sustainable development to greatest extent.
Utility model content
For the defect of prior art, the purpose of this utility model is to provide a kind of co-generation system based on hot and cold, electric multiple-energy-source, wherein by improving its key component such as thermal source, the circulatory system etc., compared with prior art effectively can solve existing hot and cold, problem that cogeneration system thermal source is single, reach the technique effect that energy utilization rate is high.
For achieving the above object, according to an aspect of the present utility model, provide a kind of co-generation system based on hot and cold, electric multiple-energy-source, it is characterized in that, comprise compression absorption heat pump cycle, cryogenic fluid power generation cycle and Driven by Solar Energy absorption refrigeration heating cycle;
Described compression absorption heat pump cycle comprises generator 29, compressor 21, absorber 1, solvent valve 9, solution heat exchanger 10 and solution circulation pump 32, temperature is that the GEOTHERMAL WATER of 80 DEG C ~ 90 DEG C is introduced in described generator 29 as driving heat source, containing the first working medium in described generator 29, the steam (vapor) outlet of described generator 29 is connected with described absorber 1 through described compressor 21; The taphole of described generator 29 is connected with described absorber 1 through described solution circulation pump 32, described solution heat exchanger 10 successively; The taphole of described absorber 1 is connected with described generator 29 through described solvent valve 9, described solution heat exchanger 10 successively;
Described cryogenic fluid power generation cycle comprises described absorber 1, steam turbine 2, generator 3, second condenser 6, working medium pump 5 in described compression absorption heat pump cycle; Containing the second working medium in described absorber 1; The second working medium exported from described absorber 1 gets back to described absorber 1 through described steam turbine 2, described second condenser 6, described working medium pump 5 successively; Described steam turbine 2 is connected, for generation of electric energy with described generator 3;
Described Driven by Solar Energy absorption refrigeration heating cycle comprises solar heat collection circulation, Absorption Cooling System and water circulation, described solar heat collection circulation comprises hot water storage tank 18, water circulating pump 25, solar thermal collector 14, control valve, the outlet of described hot water storage tank 18 is connected with the entrance of described hot water storage tank 18 through described water circulating pump 25, described solar thermal collector 14, described control valve successively, and described solar thermal collector 14 collects heat, described Absorption Cooling System comprises condenser 12, pressure-reducing valve 16, evaporimeter 20, 3rd absorber 19, 3rd solution pump 17, 3rd solution heat exchanger 15, 3rd generator 11, described 3rd generator 11 gathers the heat drive of circulating collection by described solar heat, containing the 3rd working medium in described 3rd generator 11, the steam (vapor) outlet of described 3rd generator 11 is successively through described condenser 12, described pressure-reducing valve 16, described evaporimeter 20, described 3rd absorber 19, described 3rd solution pump 17, described 3rd solution heat exchanger 15 is connected with the entrance of described 3rd generator 11, the taphole of described 3rd generator 11 is connected through the solution inlet of described 3rd solution heat exchanger 15 with described 3rd absorber 19, described water circulation comprises described evaporimeter 20 in described Absorption Cooling System, regenerator 8, cooling water pump 7, described cryogenic fluid power generation cycle comprise described second condenser 6 in described compression absorption heat pump cycle, and the outlet of described regenerator 8 is connected with the entrance of described regenerator 8 through described cooling water pump 7, described second condenser 6 successively, the chilled water outlet of described evaporimeter 20 is connected with the entrance of described regenerator 8, and the chilled water entrance of described evaporimeter 20 is connected with the outlet of described regenerator 8.
As of the present utility model preferred further, it is characterized in that, described first working medium is R22-DMA working medium pair, and described second working medium is chloroethanes, and described 3rd working medium is lithium bromide-device of working medium pair.
As of the present utility model preferred further, it is characterized in that, described Absorption Cooling System also comprises GEOTHERMAL WATER flow control valve, and the GEOTHERMAL WATER that described 3rd absorber 19 is 80 DEG C ~ 90 DEG C by described GEOTHERMAL WATER flow control valve by temperature drives.
By the above technical scheme that the utility model is conceived, compared with prior art, owing to have employed solar energy, underground heat as thermal source, break away from the dependence of traditional combined supply system to natural gas, the oil product energy, by relying on the coupling of low-grade geothermal energy and solar energy, and corresponding improvement is made to the circulatory system, can obtain pollution less, improve the beneficial effect of energy utilization rate.
Accompanying drawing explanation
Fig. 1 is hot and cold, the electric three co-generation system schematic diagrames of multi-heat source coupling;
Fig. 2 is compression absorption heat pump cycle schematic diagram;
Fig. 3 is cryogenic fluid power generation cycle schematic diagram;
Fig. 4 is Driven by Solar Energy absorption refrigeration, heating cycle schematic diagram.
In above accompanying drawing, the implication represented by Reference numeral sees the following form:
Detailed description of the invention
In order to make the purpose of this utility model, technical scheme and advantage clearly understand, below in conjunction with drawings and Examples, the utility model is further elaborated.Should be appreciated that specific embodiment described herein only in order to explain the utility model, and be not used in restriction the utility model.
Combined supply system driving heat source is low-temperature water heating (80 DEG C ~ 90 DEG C) and solar energy.Low-temperature water heating drives compression absorption type heat pump work, and Driven by Solar Energy refrigeration system with lithium bromide absorption runs.Figure 1 shows that three co-generation system schematic diagrames.
Three co-generation systems have three systemic circulations, namely compress absorption heat pump cycle, cryogenic fluid power generation cycle, Driven by Solar Energy absorption refrigeration heating cycle, can adopt different working medium respectively.
Compression absorption heat pump cycle comprises generator 29, compressor 21, absorber 1, solvent valve 9, solution heat exchanger 10 and solution circulation pump 32;
Cryogenic fluid power generation cycle comprises described absorber 1, steam turbine 2, generator 3, second condenser 6, working medium pump 5 in described compression absorption heat pump cycle;
Described Driven by Solar Energy absorption refrigeration heating cycle comprises solar heat collection circulation, Absorption Cooling System and water circulation; Described solar heat collection circulation comprises hot water storage tank 18, water circulating pump 25, solar thermal collector 14, control valve.
Embodiment 1
Compression absorption heat pump cycle adopts working medium to be that R22-DMA working medium is to (that is, R22 (CHClF 2, monochlorodifluoromethane) and DMA (C 2h 7n, dimethylamine) mixture), cryogenic fluid power generation cycle adopt working medium be chloroethanes, Driven by Solar Energy absorption refrigeration heating cycle adopt working medium be lithium bromide-device of working medium pair.
1) absorption heat pump cycle is compressed
As shown in Figure 2, temperature be the GEOTHERMAL WATER of 85 DEG C as driving heat source, through suction pump be introduced into compression absorption heat pump cycle in generator 29 in, input Q gheat energy, heat cycles working medium R22-DMA, produces R22 steam, after compressor 21 input work W, enters in absorber 1; Weak solution becomes concentrated solution after producing steam and leaves generator 1, enters solution heat exchanger 10, enter absorber 1 with from after the weak solution heat exchange of absorber 1 after solution circulation pump 32 boosts, and with R22 steam in absorber 1, produces and absorbs hot Q a, drive low-temperature electricity-generating working medium; Concentrated solution becomes weak solution simultaneously, goes out absorber 1 after solvent valve 9 with solution heat exchanger 10, gets back in generator 29 and complete circulation.
2) cryogenic fluid power generation cycle
As shown in Figure 3, in absorber 1, produced high-temperature steam by the cryogenic fluid chloroethanes heated, produce electric energy E by turbogenerator (i.e. the one of steam turbine 2) acting, flow to electric user 4; Exhaust steam after acting enters in the second condenser 6 and exports Q 2heat energy, become liquid after cooling, send in absorber 1 through working medium pump 5 and again heated circulation.
3) Driven by Solar Energy absorption refrigeration heating cycle
As shown in Figure 4, Driven by Solar Energy absorption refrigeration heating cycle gathers cyclic part and Absorption Cooling System part by solar heat and circulating part is grouped into.Recirculated water in solar heat collection circulation in heat storage water tank 18, by water pump 25, enters solar collector 14, absorbs Q tsolar energy, be heated to temperature about 90 DEG C, consume Q fenergy drive Absorption Cooling System to run, enter heat storage water tank 18 accumulation of heat through control valve afterwards and complete circulation; Cooling water takes away Q through condenser 12 kheat, the hot water in heat storage water tank 18 is flowed to heat user 28 by extraction system, and the heat of conveying is Q r, refrigerant backwater takes back air conditioner heat load Q 1cooled by Absorption Cooling System evaporimeter 20, come back to cooling in air-conditioning system, the chilled water of being drawn by evaporimeter 20 is also transported to the low-temperature receiver as cooling generating working medium in cryogenic fluid power generation cycle simultaneously.Lithium Bromide Absorption Refrigeration Cycle device, for electricity generation system provides necessary cold, unnecessary cold then brings colod-application family 24 by chilled water; Part solar energy supplies heat user 28 by heat storage water tank 18.The working medium used in Driven by Solar Energy absorption refrigeration heating cycle is lithium bromide-device of working medium pair
4) Study on Variable Condition Features
When solar energy is sufficient, close GEOTHERMAL WATER flow control valve, underground heat is only supplied to compression absorption type heat pump system; When running night, open GEOTHERMAL WATER flow control valve, geothermal energy Q g0be introduced in Absorption Cooling System, drive refrigeration system to run; When cloudy solar energy is not enough time, can opening controlling valve, underground heat drives two system cloud gray model simultaneously.
The working fluids characteristic of table 2 chloroethanes and R22
Carry out heat Balance Calculation in the ideal situation:
1) absorption heat pump cycle is compressed
Q a=Q g+W
2) cryogenic fluid power generation cycle
If the efficiency of turbine is η
Then Q 2 + E η = Q a
3) Driven by Solar Energy absorption refrigeration heating cycle
Solar heat water circulation: Q t=Q f+ Q r
BrLi chiller: Q k=Q f+ Q 1+ Q 2
4) system heat balance
When daytime, solar energy was sufficient: W + Q g + Q t + Q 1 = E η + Q k + Q r
When evening, solar energy was inadequate: W + Q g + Q g 0 + Q 1 = E η + Q k
Ratio for input and output: ρ = E + Q r + Q 1 W
Above-mentioned three co-generation systems compare traditional hot and cold, electric three co-generation systems, have the following advantages:
1) energy consumption is little, temperature is adopted to be that the GEOTHERMAL WATER of 80 DEG C ~ 90 DEG C and solar energy two kinds of low-grade energies are as driving heat source, except a small amount of electric energy of equipment component consumption, without the need to consuming high-grade energy, without the need to using fossil energy (as coal, natural gas etc.), can comprehensive energy utilization, and reduce to greatest extent non-renewable energy resources consumption, reduce toxic emission and pollution; Water-saving performance is good, and the generating of system own does not need with water, and required water is all that water-saving performance is fabulous for heat supply, and energy utilization rate is high;
2) system is closed loop, does not pollute and waste gas discharge, has stopped the pollution of sulfur dioxide, carbon monoxide and dust, achieved to greatest extent and natural harmony;
3) design of system flow, for common geothermal power generation, have employed heat pump techniques, cryogenic fluid closed loop generation technology, for common absorption system, native system adopts Driven by Solar Energy, again both is combined simultaneously;
4) current combined supply system driving belongs to passive type mostly, and the tail gas etc. namely after the consumption of many employing high-grade energies carrys out the operation of drive system, so it is insufficient to have utilizing of portion of energy unavoidably in running; And the utility model adopts active, namely with a small amount of cost, initiatively go the temperature improving low-grade energy, make it reach available standard;
5) safety and stability, can make up the deficiency of bulk power grid in security and stability, under mains breakdown and unexpected storms (such as earthquake, snowstorm, artificial destruction, war) situation, can maintain the power supply of responsible consumer;
6) comprehensive cascade utilization, in the centralized power supply system of routine, form of energy is relatively single, when user not only needs electric power, and need the confession of other form of energy as cold energy and heat energy seasonable, be difficult to the comprehensive cascade utilization realizing energy when meeting above-mentioned needs by means of only electric power; This system can realize the comprehensive cascade utilization of energy by the organic combination of different circulation while meeting consumers' demand, and overcome cold energy and heat energy cannot the difficulty of long-distance transmissions;
7) broken traditional boundary, heating, hot water, electricity, cold, water resources rational use and environmental pollution improvement have been considered as a whole, with minimum fund, resources and environment cost, exchanges the highest returns of investment, energy conversion efficiency and energy facilities usefulness for.
Progressively promote about the application of CCHP technology at present, compare the system that traditional use combustion gas excess heat drives, native system further decreases the use of fossil energy, achieves zero-emission, therefore in energy-saving and emission-reduction further.Native system has certain requirement for the selection of drive energy, there being sufficient terrestrial heat resources, having the countries and regions of plentiful solar energy resources, having very large development potentiality.
The technical solution of the utility model is that the research of small-sized hot and cold, electric three co-generation systems provides a new research direction, for the large-scale development of low-temperature geothermal resource and utilization provide theoretical foundation and model; Simultaneously also can solve the energy and environmental problem that become increasingly conspicuous, to the popularization of energy-saving and emission-reduction, there is profound significance, there is important theory significance and application prospect widely.
Those skilled in the art will readily understand; the foregoing is only preferred embodiment of the present utility model; not in order to limit the utility model; all do within spirit of the present utility model and principle any amendment, equivalent to replace and improvement etc., all should be included within protection domain of the present utility model.

Claims (3)

1. based on a co-generation system for hot and cold, electric multiple-energy-source, it is characterized in that, comprise compression absorption heat pump cycle, cryogenic fluid power generation cycle and Driven by Solar Energy absorption refrigeration heating cycle;
Described compression absorption heat pump cycle comprises generator (29), compressor (21), absorber (1), solvent valve (9), solution heat exchanger (10) and solution circulation pump (32), temperature is that the GEOTHERMAL WATER of 80 DEG C ~ 90 DEG C is introduced in described generator (29) as driving heat source, containing the first working medium in described generator (29), the steam (vapor) outlet of described generator (29) is connected with described absorber (1) through described compressor (21); The taphole of described generator (29) is connected with described absorber (1) through described solution circulation pump (32), described solution heat exchanger (10) successively; The taphole of described absorber (1) is connected with described generator (29) through described solvent valve (9), described solution heat exchanger (10) successively;
Described cryogenic fluid power generation cycle comprises described absorber (1), steam turbine (2), generator (3), the second condenser (6), working medium pump (5) in described compression absorption heat pump cycle; Containing the second working medium in described absorber (1); The second working medium exported from described absorber (1) gets back to described absorber (1) through described steam turbine (2), described second condenser (6), described working medium pump (5) successively; Described steam turbine (2) is connected, for generation of electric energy with described generator (3);
Described Driven by Solar Energy absorption refrigeration heating cycle comprises solar heat collection circulation, Absorption Cooling System and water circulation, described solar heat collection circulation comprises hot water storage tank (18), water circulating pump (25), solar thermal collector (14), control valve, the outlet of described hot water storage tank (18) is connected with the entrance of described hot water storage tank (18) through described water circulating pump (25), described solar thermal collector (14), described control valve successively, and described solar thermal collector (14) collects heat, described Absorption Cooling System comprises condenser (12), pressure-reducing valve (16), evaporimeter (20), 3rd absorber (19), 3rd solution pump (17), 3rd solution heat exchanger (15), 3rd generator (11), described 3rd generator (11) gathers the heat drive of circulating collection by described solar heat, containing the 3rd working medium in described 3rd generator (11), the steam (vapor) outlet of described 3rd generator (11) is successively through described condenser (12), described pressure-reducing valve (16), described evaporimeter (20), described 3rd absorber (19), described 3rd solution pump (17), described 3rd solution heat exchanger (15) is connected with the entrance of described 3rd generator (11), the taphole of described 3rd generator (11) is connected through the solution inlet of described 3rd solution heat exchanger (15) with described 3rd absorber (19), described water circulation comprises described evaporimeter (20) in described Absorption Cooling System, regenerator (8), cooling water pump (7), described cryogenic fluid power generation cycle comprise described second condenser (6) in described compression absorption heat pump cycle, and the outlet of described regenerator (8) is connected with the entrance of described regenerator (8) through described cooling water pump (7), described second condenser (6) successively, the chilled water outlet of described evaporimeter (20) is connected with the entrance of described regenerator (8), and the chilled water entrance of described evaporimeter (20) is connected with the outlet of described regenerator (8).
2., as claimed in claim 1 based on the co-generation system of hot and cold, electric multiple-energy-source, it is characterized in that, described first working medium is R22-DMA working medium pair, and described second working medium is chloroethanes, and described 3rd working medium is lithium bromide-device of working medium pair.
3. as claimed in claim 1 based on the co-generation system of hot and cold, electric multiple-energy-source, it is characterized in that, described Absorption Cooling System also comprises GEOTHERMAL WATER flow control valve, and the GEOTHERMAL WATER that described 3rd absorber (19) is 80 DEG C ~ 90 DEG C by described GEOTHERMAL WATER flow control valve by temperature drives.
CN201420603191.6U 2014-10-17 2014-10-17 A kind of co-generation system based on hot and cold, electric multiple-energy-source Expired - Fee Related CN204187889U (en)

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