CN103292513B - Driven by Solar Energy list economic benefits and social benefits coupled mode lithium bromide refrigerator - Google Patents
Driven by Solar Energy list economic benefits and social benefits coupled mode lithium bromide refrigerator Download PDFInfo
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- CN103292513B CN103292513B CN201310161559.8A CN201310161559A CN103292513B CN 103292513 B CN103292513 B CN 103292513B CN 201310161559 A CN201310161559 A CN 201310161559A CN 103292513 B CN103292513 B CN 103292513B
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- AMXOYNBUYSYVKV-UHFFFAOYSA-M Lithium bromide Chemical compound [Li+].[Br-] AMXOYNBUYSYVKV-UHFFFAOYSA-M 0.000 title claims abstract description 98
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 84
- 229940059936 lithium bromide Drugs 0.000 claims abstract description 48
- 239000006096 absorbing agent Substances 0.000 claims abstract description 27
- 238000005338 heat storage Methods 0.000 claims abstract description 18
- 238000001816 cooling Methods 0.000 claims abstract description 15
- 239000000498 cooling water Substances 0.000 claims abstract description 14
- 239000003507 refrigerant Substances 0.000 claims abstract description 8
- 238000005057 refrigeration Methods 0.000 claims description 19
- 238000010438 heat treatment Methods 0.000 claims description 14
- 230000000875 corresponding Effects 0.000 claims description 3
- 239000007789 gas Substances 0.000 description 12
- 238000010521 absorption reaction Methods 0.000 description 9
- 238000004378 air conditioning Methods 0.000 description 8
- 230000000694 effects Effects 0.000 description 5
- 238000000034 method Methods 0.000 description 4
- 238000005516 engineering process Methods 0.000 description 3
- 150000001875 compounds Chemical class 0.000 description 2
- 230000023298 conjugation with cellular fusion Effects 0.000 description 2
- 230000001276 controlling effect Effects 0.000 description 2
- 238000010790 dilution Methods 0.000 description 2
- 238000001704 evaporation Methods 0.000 description 2
- 239000003517 fume Substances 0.000 description 2
- WHXSMMKQMYFTQS-UHFFFAOYSA-N lithium Chemical compound [Li] WHXSMMKQMYFTQS-UHFFFAOYSA-N 0.000 description 2
- 229910052744 lithium Inorganic materials 0.000 description 2
- 230000013011 mating Effects 0.000 description 2
- 230000001105 regulatory Effects 0.000 description 2
- 230000021037 unidirectional conjugation Effects 0.000 description 2
- 210000004369 Blood Anatomy 0.000 description 1
- 208000008425 Protein Deficiency Diseases 0.000 description 1
- 239000008280 blood Substances 0.000 description 1
- UGFAIRIUMAVXCW-UHFFFAOYSA-N carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 239000000567 combustion gas Substances 0.000 description 1
- 238000002485 combustion reaction Methods 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 239000003546 flue gas Substances 0.000 description 1
- 239000002737 fuel gas Substances 0.000 description 1
- 239000000295 fuel oil Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000003921 oil Substances 0.000 description 1
- 230000001172 regenerating Effects 0.000 description 1
- 239000007921 spray Substances 0.000 description 1
- 239000002918 waste heat Substances 0.000 description 1
Classifications
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A30/00—Adapting or protecting infrastructure or their operation
- Y02A30/27—Relating to heating, ventilation or air conditioning [HVAC] technologies
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02B—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO BUILDINGS, e.g. HOUSING, HOUSE APPLIANCES OR RELATED END-USER APPLICATIONS
- Y02B30/00—Energy efficient heating, ventilation or air conditioning [HVAC]
- Y02B30/62—Absorption based systems
Abstract
The invention provides a kind of Driven by Solar Energy list economic benefits and social benefits coupled mode lithium bromide refrigerator, comprise solar energy medium-temperature collectors, gas fired-boiler, heat storage water tank, thermal-arrest circulating pump, high-temperature heat exchanger, low temperature heat exchanger, lithium-bromide solution pump, absorber, water as refrigerant circulating pump, evaporimeter, heat exchange end, air-conditioned room, expansion valve, cooling water circulating pump, cooling tower, condenser, low pressure generator, high pressure generator, hot water circulating pump, first valve, second valve, 3rd valve, 4th valve, 5th valve, 6th valve, 7th valve, 8th valve.The present invention according to the feature of solar thermal collection system, can switch, utilizes solar energy fully efficiently with utilizing system single-action and economic benefits and social benefits, reduces conventional gas and drives lithium bromide refrigerator to the consumption of primary energy, environmental protection.
Description
Technical field
The present invention relates to Solar use and air-conditioning technical field, be specially a kind of Driven by Solar Energy list economic benefits and social benefits coupled mode lithium bromide refrigerator.
Background technology
Solar energy is widely distributed, that use is clean regenerative resource, is expected to play in future society energy resource structure more importantly act on.Wherein utilize solar energy carry out heat supply, heating and refrigeration be realize scale, important channel that low cost utilizes solar energy.Particularly; in recent years along with the scale of solar energy heating and heating system is applied; summer, solar heat excess phenomenon was very outstanding; scholars can realize utilizing summer solar energy to carry out the effective ways of air conditioner refrigerating positive searching; object is the annual utilization ratio that can improve solar thermal collector, can open up a brand-new technological approaches utilizing solar energy to solve air conditioner refrigerating demand on the other hand.The great advantage of solar airconditioning refrigeration is that it has matching in good season, and weather is warmmer, when more needing refrigeration, solar radiation condition is better, and the refrigerating capacity of solar refrigeration system is also larger.
Because current solar thermal collector is mainly used in hot-water heating system, usual heat-collecting temperature is below 90 DEG C, therefore the solar airconditioning technical elements that mating with ordinary solar heat collector of the priority application of solar airconditioning research in the past, particularly the single-effective absorption refrigerating machine group of production technology relative maturity, applies more.But the solar airconditioning be combined with low-temperature solar energy heat collection technology also exists some problems, on the one hand due to heat source temperature low (60-90 DEG C), the absorption of mating with it or absorption refrigeration unit generally freeze heating power COP between 0.4-0.7.On the other hand in order to ensure the continuity problem of solar airconditioning, general combustion gas or the oil burning boiler of adopting is as auxiliary thermal source.For the solar air-conditioner system that solar insuring rate is low, often lose due advantage (compared with conventional air conditioning system) because heating power COP is low.Mate with lithium bromide absorption type air conditioner can select the heating power COP that freezes be 1.2 economic benefits and social benefits product, but it needs the thermal source of 150 DEG C, and conventional direct-fired lithiumbromide absorption refrigerating machine is exactly the suction-type lithium bromide double-effect chiller adopting fuel oil or gas fired-boiler to drive.To adopt Driven by Solar Energy, then system needs to mate corresponding medium-temperature collectors.
In addition, for solar thermal collector, by the restriction of level of solar radiation, in the middle of one day, heat collector to supply heat temperature is lower when the morning and evening, reaches the highest before midday afterwards.To the solar air-conditioner system that medium-temperature collectors drives, generally close to noon, heat-collecting temperature could meet dual-effect refrigeration service requirement, the morning and afternoon portion of time, only can meet single-action refrigerating operaton condition.Therefore, extend solar airconditioning refrigeration system cooling time, best bet is the operational mode adopting single-action/economic benefits and social benefits to automatically switch, according to solar heat collector to supply heat variations in temperature in a day, automatically switch between single-action and economic benefits and social benefits pattern, to meet efficient, long-time refrigeration demand.
By finding the retrieval of prior art document, Chinese patent application publication No. is: CN101886854A, and denomination of invention is: Singledouble effect absorptive refrigerating machine.Propose the refrigeration machine that a kind of single economic benefits and social benefits switch, focus on setting forth the running ability how controlling middle weak solution pump according to the change of refrigeration load.Structure, it adds additional the generator and condenser that run for single-action on the basis of former direct combustion double-effect absorption refrigerating machine, and its generator run for single-action needs other heat source water to supply.And when single-action runs, high-low pressure generator and the condenser of former direct-fired economic benefits and social benefits unit all do not work, and system unit utilization rate is low.
Chinese patent application publication number is: CN101231043A, and denomination of invention is: single and double effect absorption refrigerator and method of controlling operation thereof thereof.The single double-effect chiller structure proposed is similar to the Singledouble effect absorptive refrigerating machine in CN10188854A, is the increase in the extra generator for single-action operation and condenser equally.And economic benefits and social benefits are run and are only leaned on gas fired-boiler as thermal source, and do not relate to Solar use, primary energy consumption is large.
Chinese patent application publication number is: CN101526283A, and denomination of invention is: fume hot-water single-double effect compound type lithium bromide absorption type cold water, water chiller-heater unit.The main distinction that the fume hot-water single-double effect compound type lithium bromide absorption type cold water proposed, water chiller-heater unit and above-mentioned publication number are the technical scheme disclosed in CN101231043A and CN101886854A is that it merely add the hot water generator run for single-action on former economic benefits and social benefits unit, simple both structure is comparatively above.What itself and the main distinction of the present invention were that its economic benefits and social benefits run that thermal source adopts is that other devices produce high-temperature flue gas, belong to field of waste heat utilization, and thermal source when economic benefits and social benefits are run in the present invention is provided by solar energy medium-temperature collectors, for new forms of energy and renewable resource utilize field, and due to the form of both generator thermals source different, its version also will have significant difference.And it adds additional a solution pump when single-action runs, and only tube road valve transfer practical function in the present invention.
Summary of the invention
The present invention is directed to above the problems of the prior art and deficiency, propose a kind of Driven by Solar Energy list economic benefits and social benefits coupled mode lithium-bromide absorption-type refrigerating machine.By adding single-action hot water heat exchanger in low pressure generator, the control of line correlation valve opening and closing of going forward side by side, realizes the switching of refrigeration unit single-action operating mode and economic benefits and social benefits operating mode when different water temperature.The grade of the solar thermal collection system hot water of Different periods can be made full use of, realize single economic benefits and social benefits to automatically switch, utilize solar refrigeration efficiently, solve the problem of solar energy system heat surplus in summer and solar thermal collection system can provide domestic hot-water simultaneously, winter also can be used for heating.Solar irradiation is not enough but when having refrigeration demand, employing gas fired-boiler drives dual-effect refrigeration operating mode to run.
Driven by Solar Energy list economic benefits and social benefits coupled mode lithium bromide refrigerator provided by the invention, comprise solar energy medium-temperature collectors 1, gas fired-boiler 3, heat storage water tank 6, thermal-arrest circulating pump 7, high-temperature heat exchanger 9, low temperature heat exchanger 10, lithium-bromide solution pump 13, absorber 14, water as refrigerant circulating pump 15, evaporimeter 16, heat exchange end 17, air-conditioned room 18, expansion valve 19, cooling water circulating pump 20, cooling tower 21, condenser 22, low pressure generator 23, high pressure generator 24, hot water circulating pump 26, first valve 2, second valve 4, 3rd valve 5, 4th valve 8, 5th valve 11, 6th valve 12, 7th valve 25, 8th valve 27, wherein: solar energy medium-temperature collectors 1 is connected to form thermal-arrest loop with heat storage water tank 6 and thermal-arrest circulating pump 7, high pressure generator 24 connects low pressure generator 23, low pressure generator 23 connects condenser 22, condenser 22 connects evaporimeter 16 by expansion valve 19, evaporimeter 16 connects absorber 14, absorber 14 is connected with low temperature heat exchanger 10 with high-temperature heat exchanger 9 respectively by lithium-bromide solution pump 13, high-temperature heat exchanger 9 is connected with high pressure generator 24, and low temperature heat exchanger 10 is connected with low pressure generator 23, to form single double-effect lithium bromide refrigeration machine, cooling tower 21 is connected to form cooling water loop with absorber 14 and condenser 22 respectively by cooling water circulating pump 20, heat exchange end 17 is placed in air-conditioned room 18, and heat exchange end 17 and evaporimeter 16 are connected to form end circulation loop, first valve (2) connects solar energy medium-temperature collectors 1 and heat storage water tank 6 respectively, second valve 4 connects gas fired-boiler 3 and high pressure generator 24 respectively, 3rd valve 5 connects gas fired-boiler 3 and high pressure generator 24 respectively, 4th valve 8 connects heat storage water tank 6 and high pressure generator 24 respectively, 5th valve 11 connects lithium-bromide solution pump 13 and high-temperature heat exchanger 9 respectively, 6th valve 12 connects lithium-bromide solution pump 13 and low temperature heat exchanger 10 respectively, 7th valve 25 connects hot water circulating pump 26 and low pressure generator 23 respectively, 8th valve 27 connects high pressure generator 24 and solar energy medium-temperature collectors 1 respectively, water as refrigerant circulating pump 15 two ends all connect evaporimeter 16, and lithium-bromide solution pump 13 two ends all connect absorber 14.
Preferably, two groups of heat exchangers are provided with in described low pressure generator 23, one group is vapor heat exchanger 2307, another group is hot water heat exchanger 2304, wherein: vapor heat exchanger 2307 and hot water heat exchanger 2304 are all placed in low pressure generator 23, vapor heat exchanger 2307 connects high pressure generator 24 and condenser 22 respectively, and hot water heat exchanger 2304 is connected with heat storage water tank 6 by hot water circulating pump 26.
Preferably, there are three kinds of different operational modes:
First mode, Driven by Solar Energy list economic benefits and social benefits coupled mode lithium bromide refrigerator economic benefits and social benefits are run: the hot water that solar energy medium-temperature collectors 1 produces directly enters high pressure generator 24;
Second pattern, the single-action of Driven by Solar Energy list economic benefits and social benefits coupled mode lithium bromide refrigerator runs: the hot water that solar energy medium-temperature collectors 1 produces enters the hot water generator in low pressure generator 23;
3rd pattern, gas fired-boiler drives single economic benefits and social benefits coupled mode lithium bromide refrigerator economic benefits and social benefits to run: the hot water that gas fired-boiler 3 produces enters high pressure generator 24.
Preferably, automatically select corresponding operational mode according to solar energy medium-temperature collectors 1 outlet temperature, and control the switch of relevant water pump valve.
Preferably, utilize hot water that solar energy medium-temperature collectors 1 produces as main heating source, utilize gas fired-boiler 3 when radiation parameter is bad as a supplement.
Compared with prior art, the present invention according to the feature of solar thermal collection system, can switch, utilizes solar energy fully efficiently with utilizing system single-action and economic benefits and social benefits, reduces conventional gas and drives lithium bromide refrigerator to the consumption of primary energy, environmental protection.
Accompanying drawing explanation
By reading the detailed description done non-limiting example with reference to the following drawings, other features, objects and advantages of the present invention will become more obvious:
Fig. 1 is the schematic flow sheet of Driven by Solar Energy list economic benefits and social benefits coupled mode lithium bromide refrigerator of the present invention;
Fig. 2 is mesolow generator detail drawing of the present invention;
Fig. 3 is the control logic figure that in the present invention, single economic benefits and social benefits switch.
Detailed description of the invention
Below in conjunction with specific embodiment, the present invention is described in detail.Following examples will contribute to those skilled in the art and understand the present invention further, but not limit the present invention in any form.It should be pointed out that to those skilled in the art, without departing from the inventive concept of the premise, some distortion and improvement can also be made.These all belong to protection scope of the present invention.
Referring to Fig. 1 and Fig. 2, embodiments of the invention are described.Fig. 1 is schematic flow sheet of the present invention, described Driven by Solar Energy list economic benefits and social benefits coupled mode lithium bromide refrigerator comprises: solar energy medium-temperature collectors 1, gas fired-boiler 3, heat storage water tank 6, thermal-arrest circulating pump 7, high-temperature heat exchanger 9, low temperature heat exchanger 10, lithium-bromide solution pump 13, absorber 14, water as refrigerant circulating pump 15, evaporimeter 16, heat exchange end 17, air-conditioned room 18, expansion valve 19, cooling water circulating pump 20, cooling tower 21, condenser 22, low pressure generator 23, high pressure generator 24, hot water circulating pump 26, first valve 2, second valve 4, 3rd valve 5, 4th valve 8, 5th valve 11, 6th valve 12, 7th valve 25, 8th valve 27.Respectively the present invention is set forth by reference to the accompanying drawings with regard to various operational mode below.Fig. 2 shows weak solution mouth spray 2301, thermal source hot water inlet 2302, thermal source hot water outlet 2303, hot water heat exchanger 2304, concentrated solution outlet mouth 2305, high pressure generator steam (vapor) outlet 2306, vapor heat exchanger 2307, high pressure generator steam inlet 2308, steam outlet 2309.
1. drive refrigeration machine by solar energy, the second valve 4, the 3rd valve 5 are in closed condition:
(1) solar energy medium-temperature collectors 1 export water temperature meet economic benefits and social benefits run: the 4th valve 8 is opened, and the 5th valve 11 is opened, and the 6th valve 12 is opened, and the 8th valve 27 is opened, and the first valve 2 is closed, and the 7th valve 25 is closed.Solar energy medium-temperature collectors 1 outlet hot water enters high pressure generator 24, and in high pressure generator 24, lithium-bromide solution produces high-temperature vapor after being heated, and self concentration increases.The high-temperature vapor produced by high pressure generator 24 enters coupled low pressure generator 23 by pipeline, enters in condenser 22 and be condensed into aqueous water after again heating the lithium-bromide solution in low pressure generator 23.Molten also being entered in condenser 22 by the steam heating rear generation of lithium bromide in low pressure generator 23 is condensed into aqueous water.Aqueous water in condenser 22 enters the lower evaporimeter of pressure 16 after the reducing pressure by regulating flow through expansion valve 19, evaporate and absorb the heat from heat exchange end 17 in air-conditioned room 18, reduce the temperature of its medium, realize continuous cooling by water as refrigerant circulating pump 15.Low pressure steam in evaporimeter 16 after evaporation enters coupled absorber 14, absorbed by the bromize lithium concentrated solution from high pressure generator 24 and low pressure generator 23, make the concentrated solution dilution entered in absorber 14 be weak solution, and be sent to high-temperature heat exchanger 9 and low temperature heat exchanger 10 by lithium-bromide solution pump 13.After lithium-bromide solution in high pressure generator 24 discharges steam, self concentration increases, and enters high-temperature heat exchanger 9 by pipeline, with complete heat exchange from the weak solution in absorber 14 after enter absorber 14.Weak solution in absorber 14 enters high pressure generator 24 after high-temperature heat exchanger 9, continues generating process.Similarly, after the lithium-bromide solution in low pressure generator 23 discharges steam, self concentration increases, and enters low temperature heat exchanger 10 by pipeline, with complete heat exchange from the weak solution in absorber 14 after enter absorber 14.Weak solution in absorber 14 enters low pressure generator 23 after low temperature heat exchanger 10, continues generating process.Heat storage water tank 6 is entered from high pressure generator 24 hot water out.Water in heat storage water tank 6 is sent in solar energy medium-temperature collectors 1 and is again heated by thermal-arrest circulating pump 7, completes thermal-arrest circulation.Cooling water circulating pump 20 enters cooling tower 21 evaporative cooling after being delivered to by the cooling water in cooling tower 21 and completing heat exchange in absorber 14 and condenser 22 again, completes cooling water circulation.
(2) solar energy medium-temperature collectors 1 export water temperature meet single-action run: the first valve 2 is opened, and the 6th valve 12 is opened, and the 7th valve 25 is opened, and the 4th valve 8 is closed, and the 5th valve 11 is closed, and the 8th valve 27 is closed.Solar energy medium-temperature collectors 1 outlet hot water enters heat storage water tank 6.By hot water circulating pump 26, the hot water in heat storage water tank 6 is delivered in low pressure generator 23, heat wherein lithium-bromide solution, return in heat storage water tank 6 subsequently by the road.Lithium-bromide solution in low pressure generator 23 is entered in condenser 22 by the steam heating rear generation and is condensed into aqueous water.Aqueous water in condenser 22 enters the lower evaporimeter of pressure 16 after the reducing pressure by regulating flow through expansion valve 19, evaporate and absorb the heat from heat exchange end 17 in air-conditioned room 18, reduce the temperature of its medium, realize continuous cooling by water as refrigerant circulating pump 15.Low pressure steam in evaporimeter 16 after evaporation enters coupled absorber 14, absorbed by the bromize lithium concentrated solution from low pressure generator 23, making to enter concentrated solution dilution in absorber 14 is weak solution, and is sent to low temperature heat exchanger 10 by lithium-bromide solution pump 13.After lithium-bromide solution in low pressure generator 23 discharges steam, self concentration increases, and enters low temperature heat exchanger 10 by pipeline, with complete heat exchange from the weak solution in absorber 14 after enter absorber 14.Weak solution in absorber 14 enters low pressure generator 23 after low temperature heat exchanger 10, continues generating process.Water in heat storage water tank 6 is sent in solar energy medium-temperature collectors 1 and is again heated by thermal-arrest circulating pump 7, completes thermal-arrest circulation.Cooling water circulating pump 20 enters cooling tower evaporative cooling after being delivered to by the cooling water in cooling tower 21 and completing heat exchange in absorber 14 and condenser 22 again, completes cooling water circulation.
2., when solar radiation is not enough to drive refrigeration machine, driven by gas fired-boiler 3: the second valve 4 is opened, the 3rd valve 5 is opened, and the 4th valve 8 is closed, and the 7th valve 25 is closed, and the 8th valve 27 is closed.The high-temperature-hot-water produced by gas fired-boiler 3 directly enters high pressure generator 24 and carries out dual-effect refrigeration process, and situation when miscellaneous part ruuning situation is run with Driven by Solar Energy economic benefits and social benefits is identical, and thermal source switches to boiler.Solar energy heating circulation can run supply domestic hot-water as usual.This pattern is only as auxiliary mode that is not enough at overcast and rainy solar irradiation or night.
Above specific embodiments of the invention are described.It is to be appreciated that the present invention is not limited to above-mentioned particular implementation, those skilled in the art can make various distortion or amendment within the scope of the claims, and this does not affect flesh and blood of the present invention.
Claims (4)
1. a Driven by Solar Energy list economic benefits and social benefits coupled mode lithium bromide refrigerator, is characterized in that, comprises solar energy medium-temperature collectors (1), gas fired-boiler (3), heat storage water tank (6), thermal-arrest circulating pump (7), high-temperature heat exchanger (9), low temperature heat exchanger (10), lithium-bromide solution pump (13), absorber (14), water as refrigerant circulating pump (15), evaporimeter (16), heat exchange end (17), air-conditioned room (18), expansion valve (19), cooling water circulating pump (20), cooling tower (21), condenser (22), low pressure generator (23), high pressure generator (24), hot water circulating pump (26), first valve (2), second valve (4), 3rd valve (5), 4th valve (8), 5th valve (11), 6th valve (12), 7th valve (25), 8th valve (27), wherein: solar energy medium-temperature collectors (1) is connected to form thermal-arrest loop with heat storage water tank (6) and thermal-arrest circulating pump (7), high pressure generator (24) connects low pressure generator (23), low pressure generator (23) connects condenser (22), condenser (22) connects evaporimeter (16) by expansion valve (19), evaporimeter (16) connects absorber (14), absorber (14) is connected with low temperature heat exchanger (10) with high-temperature heat exchanger (9) respectively by lithium-bromide solution pump (13), high-temperature heat exchanger (9) is connected with high pressure generator (24), low temperature heat exchanger (10) is connected with low pressure generator (23), to form single double-effect lithium bromide refrigeration machine, cooling tower (21) is connected to form cooling water loop with absorber (14) and condenser (22) respectively by cooling water circulating pump (20), heat exchange end (17) is placed in air-conditioned room (18), and heat exchange end (17) and evaporimeter (16) are connected to form end circulation loop, first valve (2) connects solar energy medium-temperature collectors (1) and heat storage water tank (6) respectively, second valve (4) connects gas fired-boiler (3) and high pressure generator (24) respectively, 3rd valve (5) connects gas fired-boiler (3) and high pressure generator (24) respectively, 4th valve (8) connects heat storage water tank (6) and high pressure generator (24) respectively, 5th valve (11) connects lithium-bromide solution pump (13) and high-temperature heat exchanger (9) respectively, 6th valve (12) connects lithium-bromide solution pump (13) and low temperature heat exchanger (10) respectively, 7th valve (25) connects hot water circulating pump (26) and low pressure generator (23) respectively, 8th valve (27) connects high pressure generator (24) and solar energy medium-temperature collectors (1) respectively, water as refrigerant circulating pump (15) two ends all connect evaporimeter (16), and lithium-bromide solution pump (13) two ends all connect absorber (14),
Two groups of heat exchangers are provided with in described low pressure generator (23), one group is vapor heat exchanger (2307), another group is hot water heat exchanger (2304), wherein: vapor heat exchanger (2307) and hot water heat exchanger (2304) are all placed in low pressure generator (23), vapor heat exchanger (2307) connects high pressure generator (24) and condenser (22) respectively, and hot water heat exchanger (2304) is connected with heat storage water tank (6) by hot water circulating pump (26).
2. Driven by Solar Energy list economic benefits and social benefits coupled mode lithium bromide refrigerator according to claim 1, is characterized in that, has three kinds of different operational modes:
First mode, Driven by Solar Energy list economic benefits and social benefits coupled mode lithium bromide refrigerator economic benefits and social benefits are run: the hot water that solar energy medium-temperature collectors (1) produces directly enters high pressure generator (24);
Second pattern, the single-action of Driven by Solar Energy list economic benefits and social benefits coupled mode lithium bromide refrigerator runs: the hot water that solar energy medium-temperature collectors (1) produces enters the hot water generator in low pressure generator (23);
3rd pattern, gas fired-boiler drives single economic benefits and social benefits coupled mode lithium bromide refrigerator economic benefits and social benefits to run: the hot water that gas fired-boiler (3) produces enters high pressure generator (24).
3. Driven by Solar Energy list economic benefits and social benefits coupled mode lithium bromide refrigerator according to claim 2, is characterized in that, automatically select corresponding operational mode according to solar energy medium-temperature collectors (1) outlet temperature, and controls the switch of relevant water pump valve.
4. Driven by Solar Energy list economic benefits and social benefits coupled mode lithium bromide refrigerator according to claim 1, it is characterized in that, utilize hot water that solar energy medium-temperature collectors (1) produces as main heating source, utilize gas fired-boiler (3) when radiation parameter is bad as a supplement.
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CN202371924U (en) * | 2011-12-26 | 2012-08-08 | 广州铁路职业技术学院 | Hybrid energy absorptive refrigerating air conditioning device |
CN202521940U (en) * | 2012-03-11 | 2012-11-07 | 东华大学 | Solar secondary lithium bromide absorption type refrigeration device |
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2013
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