CN204967758U - System for utilize photovoltaic solar panel to carry out cogeneration - Google Patents
System for utilize photovoltaic solar panel to carry out cogeneration Download PDFInfo
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- CN204967758U CN204967758U CN201520462045.0U CN201520462045U CN204967758U CN 204967758 U CN204967758 U CN 204967758U CN 201520462045 U CN201520462045 U CN 201520462045U CN 204967758 U CN204967758 U CN 204967758U
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- 239000002918 waste heat Substances 0.000 claims abstract description 54
- 238000011084 recovery Methods 0.000 claims abstract description 52
- 238000010438 heat treatment Methods 0.000 claims abstract description 9
- 238000010521 absorption reaction Methods 0.000 claims description 9
- 239000000126 substance Substances 0.000 claims description 6
- 230000008676 import Effects 0.000 claims description 5
- 238000010248 power generation Methods 0.000 abstract description 5
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- 238000005516 engineering process Methods 0.000 description 6
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- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 4
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 4
- QPLDLSVMHZLSFG-UHFFFAOYSA-N CuO Inorganic materials [Cu]=O QPLDLSVMHZLSFG-UHFFFAOYSA-N 0.000 description 4
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 4
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- 229910052905 tridymite Inorganic materials 0.000 description 4
- 229910001845 yogo sapphire Inorganic materials 0.000 description 4
- UHOVQNZJYSORNB-UHFFFAOYSA-N Benzene Chemical compound C1=CC=CC=C1 UHOVQNZJYSORNB-UHFFFAOYSA-N 0.000 description 3
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 3
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- AFABGHUZZDYHJO-UHFFFAOYSA-N dimethyl butane Natural products CCCC(C)C AFABGHUZZDYHJO-UHFFFAOYSA-N 0.000 description 3
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- CSCPPACGZOOCGX-UHFFFAOYSA-N Acetone Chemical compound CC(C)=O CSCPPACGZOOCGX-UHFFFAOYSA-N 0.000 description 2
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 2
- ATUOYWHBWRKTHZ-UHFFFAOYSA-N Propane Chemical compound CCC ATUOYWHBWRKTHZ-UHFFFAOYSA-N 0.000 description 2
- RAHZWNYVWXNFOC-UHFFFAOYSA-N Sulphur dioxide Chemical compound O=S=O RAHZWNYVWXNFOC-UHFFFAOYSA-N 0.000 description 2
- 229910021529 ammonia Inorganic materials 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
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- NNPPMTNAJDCUHE-UHFFFAOYSA-N isobutane Chemical compound CC(C)C NNPPMTNAJDCUHE-UHFFFAOYSA-N 0.000 description 2
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- 239000011259 mixed solution Substances 0.000 description 2
- MSSNHSVIGIHOJA-UHFFFAOYSA-N pentafluoropropane Chemical compound FC(F)CC(F)(F)F MSSNHSVIGIHOJA-UHFFFAOYSA-N 0.000 description 2
- 230000005855 radiation Effects 0.000 description 2
- 239000008400 supply water Substances 0.000 description 2
- YTZKOQUCBOVLHL-UHFFFAOYSA-N tert-butylbenzene Chemical group CC(C)(C)C1=CC=CC=C1 YTZKOQUCBOVLHL-UHFFFAOYSA-N 0.000 description 2
- XDTMQSROBMDMFD-UHFFFAOYSA-N Cyclohexane Chemical compound C1CCCCC1 XDTMQSROBMDMFD-UHFFFAOYSA-N 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 239000001273 butane Substances 0.000 description 1
- 229910002092 carbon dioxide Inorganic materials 0.000 description 1
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- 239000012530 fluid Substances 0.000 description 1
- 230000004907 flux Effects 0.000 description 1
- 239000001282 iso-butane Substances 0.000 description 1
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- 238000000034 method Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 229910021421 monocrystalline silicon Inorganic materials 0.000 description 1
- IJDNQMDRQITEOD-UHFFFAOYSA-N n-butane Chemical compound CCCC IJDNQMDRQITEOD-UHFFFAOYSA-N 0.000 description 1
- 229910021420 polycrystalline silicon Inorganic materials 0.000 description 1
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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
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E10/00—Energy generation through renewable energy sources
- Y02E10/40—Solar thermal energy, e.g. solar towers
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E10/00—Energy generation through renewable energy sources
- Y02E10/50—Photovoltaic [PV] energy
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E10/00—Energy generation through renewable energy sources
- Y02E10/60—Thermal-PV hybrids
-
- 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
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P80/00—Climate change mitigation technologies for sector-wide applications
- Y02P80/10—Efficient use of energy, e.g. using compressed air or pressurized fluid as energy carrier
- Y02P80/15—On-site combined power, heat or cool generation or distribution, e.g. combined heat and power [CHP] supply
Landscapes
- Heat-Pump Type And Storage Water Heaters (AREA)
- Photovoltaic Devices (AREA)
Abstract
The utility model relates to a system for utilize photovoltaic solar panel to carry out cogeneration, including solar photovoltaic power generation system, solar cell panel waste heat recovery system and supplementary radiator, solar module and electric feeding means are connected, solar module is as an organic whole with the combination of waste heat recovery heater, the waste heat recovery heater is located solar cell panel's back, the waste heat recovery heater passes through circulation pipeline, normally open solenoid valve I is connected with water heater, water in the water heater heating solar energy water tank, water heater passes through circulation pipeline, normally open solenoid valve II and waste heat recovery heater working medium inlet connection, be equipped with temperature sensor and control end on the solar energy water tank, waste heat recovery heater working medium outlet passes through the pipeline, normally -closed solenoid valves I is connected with the fin radiator, the fin radiator export is through normally -closed solenoid valves II and waste heat recovery heater working medium access connection, control end and temperature sensor, the solenoid valve is connected. This system can high -efficient cascade utilization solar energy.
Description
Technical field
The utility model relates to a kind of system utilizing solar photovoltaic cell panel to carry out cogeneration, belongs to energy and environment technical field.
Background technology
Heat supply plays more and more important role with power supply in modern production is lived.Since oneth century, heat supply and power supply depend critically upon fossil fuel.Although in recent years along with the application of the technology such as overcritical Rankine cycle, coal electrical efficiency progressively improves (state-of-the-art technology can reach the heat efficiency of nearly 50% in the world now), but power industry is still the emission source that carbon dioxide and sulfur dioxide Heavy environmental pollution owner want, simultaneously along with the exhaustion of fossil fuel, cost and the difficulty of exploitation can be increasing, therefore the dynamics to new energy development is strengthened, reduce dependence to fossil fuel, use the more clean energy to be the inevitable choice of the present mankind.
The sun is as the permanent energy the abundantest in the world, and radiant power reaches 3.8x1023kW, and wherein, the solar radiation energy flux that the earth intercepts is 1.7x1014kW, and than nuclear energy, underground heat and gravitational energy reserves summation also want large more than 5000 times.It is estimated, the sun is radiated tellurian energy within January, and can comprise 10 times more than of all non-renewable energy resources gross reserves of fossil fuel, atomic energy etc. on the earth, solar energy is really inexhaustible, the nexhaustible energy.China belongs to the country that solar energy resources quite enriches, and a 2/3 area year sunshine time of area is greater than 2200h, and unit are solar radiation total amount is higher than 5016MJ/m
2.Therefore, the sustainable development of solar energy generation technology to China and even the whole mankind is studied significant.Solar power generation under environment not being brought to any pollution and public hazards situation, can convert solar energy into electrical energy, and solar power generation is described as following optimal generation mode.By the difference of conversion regime, photovoltaic generation and light-Re-electricity two kinds of modes can be divided into.Along with becoming better and approaching perfection day by day of photovoltaic material (brilliant material or non-crystalline material) production technology, the cost of photovoltaic generating system reduces gradually, photovoltaic power generation technology also obtains increasing commercial application, but the efficiency of general photovoltaic generation is all within 10%, and therefore how improving the overall utilization of solar energy is still key subjects.Utilize the waste heat of photovoltaic battery panel to user's heat supply, thus realize the effective way that cogeneration is the overall utilization improving solar energy.
Summary of the invention
The purpose of this utility model utilizes solar photovoltaic cell panel to carry out cogeneration, this system can utilize photovoltaic battery panel and waste heat thereof to carry out cogeneration simultaneously, efficient cascade utilization solar energy: first solar energy be transformed into electricity by monocrystalline silicon or polysilicon solar cell plate and export, the heat energy of cell panel discharge realizes carrying out heating hot-water supply to the cold water in solar water container by residual neat recovering system again, and the utility model is achieved through the following technical solutions.
Utilize solar photovoltaic cell panel to carry out a system for cogeneration, this system comprises solar photovoltaic generation system, solar panel residual neat recovering system and additional cooler, described solar photovoltaic generation system comprises solar module 1, storage battery 2, controller 3, inverter 4 and interconnective pipeline, solar panel residual neat recovering system comprises waste heat recovery heater 5, water heater 6, solar water container 7, circulation line, normally open solenoid valve I 11 and normally open solenoid valve II 12, additional cooler comprises fin radiator 8, normally closed solenoid valve I 9, normally closed solenoid valve II 10, pipeline, temperature sensor, control end and interconnective pipeline, solar module 1 by controller 3 respectively with storage battery 2, direct current user, alternating current user connects, and controller 3 is connected with alternating current user by inverter 4, and solar module 1 is also connected with waste heat recovery heater 5, and waste heat recovery heater 5 working substance steam of absorbing heat exports and passes through circulation line, normally open solenoid valve I 11 is connected with water heater 6, the water in water heater 6 heating solar water tank 7, and water heater 6 passes through circulation line, normally open solenoid valve II 12 and the waste heat recovery heater 5 working medium entrance point that absorbs heat is connected, and solar water container 7 is provided with temperature sensor and control end, and waste heat recovery heater 5 sender property outlet that absorbs heat passes through pipeline, normally open solenoid valve I 11, normally closed solenoid valve I 9 is connected with fin radiator 8, and fin radiator 8 is exported and is connected by the working medium import of absorbing heat of normally closed solenoid valve II 10 and waste heat recovery heater 5, control end and temperature sensor, normally closed solenoid valve I 9, normally closed solenoid valve II 10, normally open solenoid valve I 11, normally open solenoid valve II 12 connects.
Described waste heat recovery heater 5 has two kinds of forms, and one adopts and drift tube type heater, and another adopts concurrent flow multi-channel flat tubular type heater.
Heat absorption working medium in described waste heat recovery heater 5 is the mixed solution of one or more any working medium compositions in water, methyl alcohol, ethanol, benzene, toluene, adjacent dimethylethyl benzene, R123, R245fa, R113, R11, R21, R134a, butane, iso-butane, pentane, isopentane, propane, hexane, isohexane, cyclohexane, acetone, ammonia, also can add CuO, Al2O3, TiO2, SiO2, BaCl2, CNT (many walls carbon mitron) nanoparticle in working medium.
This utilizes solar photovoltaic cell panel to carry out the operation principle of the system of cogeneration:
(1) solar photovoltaic generation system: the same with conventional solar energy power generating, solar energy is by the photoelectric material photoproduction volt effect generation current of solar module 1, realize customer power supply by controller 3 and storage battery 2 again, device inverter 4 is also needed for interchange user, (2) solar panel residual neat recovering system: under normal power generation and heat supply situation, heat absorption working medium in waste heat recovery heater 5 absorbs the heat of vaporization that cell panel produces, flow through normally open solenoid valve I 11 along steam delivery line and enter water heater 6 upper interface, flow out from balanced supply water tank 13 and flow in solar water container 7 by after the cool water heating that need heat, heat absorption working medium condenses into liquid, at waste heat recovery heater 5 with under the water heater 6 flow differential pressure effect that place vertical duct fluid density contrast is formed respectively, condensation water flows into waste heat recovery heater 5 by normally open solenoid valve II 12 and liquid line and completes a circulation, meanwhile cold water is heated, user is delivered to from tank hot water outlet, , (3) auxiliary heat dissipating system: in the user's heat water yield in less or intermittent time longer situation, when water tank temperature transducer detected temperatures is more than 55 DEG C, control end closes normally open solenoid valve I 11, normally open solenoid valve II 12, open normally closed solenoid valve I 9, normally closed solenoid valve II 10 simultaneously, now flow into finned tube fin 8 from the heat absorption working substance steam of waste heat recovery heater 5 through normally closed solenoid valve I 9, steam is condensed into liquid, flow into waste heat recovery heater 5 by liquid line and complete a circulation, thus guarantee that photovoltaic cell backplane temperature is unlikely too high.When water tank temperature transducer detected temperatures is lower than 50 DEG C, control end opens normally open solenoid valve I 11, normally open solenoid valve II 12, closes normally closed solenoid valve I 9, normally closed solenoid valve II 10 simultaneously, realizes to the normal heating of cold water with to user's supplying hot water.
The beneficial effects of the utility model are: the utility model effectively utilizes solar energy and realizes photovoltaic cell capable of generating power and to user's hot-water supply, realize the efficient cascade utilization of solar energy.Native system is by the cooling of heat supplying pipeline realization to cell panel simultaneously, guarantees stability and the high efficiency of photovoltaic cell capable of generating power, is expected to become the important technique measure building distributed heat Electricity Federation system.
Accompanying drawing explanation
Fig. 1 is the utility model structural representation.
In figure, each label is: 1-solar module, 2-storage battery, 3-controller, 4-inverter, 5-waste heat recovery heater, 6-water heater, 7-solar water container, 8-fin radiator, 9-normally closed solenoid valve I, 10-normally closed solenoid valve II, 11-normally open solenoid valve I, 12-normally open solenoid valve II, 13-balanced supply water tank.
Embodiment
Below in conjunction with the drawings and specific embodiments, the utility model is described in further detail.
Embodiment 1
As shown in Figure 1, this utilizes solar photovoltaic cell panel to carry out the system of cogeneration, and this system comprises solar photovoltaic generation system, solar panel residual neat recovering system and additional cooler, described solar photovoltaic generation system comprises solar module 1, storage battery 2, controller 3, inverter 4 and interconnective pipeline, solar panel residual neat recovering system comprises waste heat recovery heater 5, water heater 6, solar water container 7, circulation line, normally open solenoid valve I 11 and normally open solenoid valve II 12, additional cooler comprises fin radiator 8, normally closed solenoid valve I 9, normally closed solenoid valve II 10, pipeline, temperature sensor, control end and interconnective pipeline, solar module 1 by controller 3 respectively with storage battery 2, direct current user, alternating current user connects, and controller 3 is connected with alternating current user by inverter 4, and solar module 1 is also connected with waste heat recovery heater 5, and waste heat recovery heater 5 working substance steam of absorbing heat exports and passes through circulation line, normally open solenoid valve I 11 is connected with water heater 6, the water in water heater 6 heating solar water tank 7, and water heater 6 passes through circulation line, normally open solenoid valve II 12 and the waste heat recovery heater 5 working medium entrance point that absorbs heat is connected, and solar water container 7 is provided with temperature sensor and control end, and waste heat recovery heater 5 sender property outlet that absorbs heat passes through pipeline, normally open solenoid valve I 11, normally closed solenoid valve I 9 is connected with fin radiator 8, and fin radiator 8 is exported and is connected by the working medium import of absorbing heat of normally closed solenoid valve II 10 and waste heat recovery heater 5, control end and temperature sensor, normally closed solenoid valve I 9, normally closed solenoid valve II 10, normally open solenoid valve I 11, normally open solenoid valve II 12 connects.Wherein waste heat recovery heater 5 adopts and drift tube type heater, and the heat absorption working medium in waste heat recovery heater 5 is methyl alcohol, also can add CuO, Al2O3, TiO2, SiO2, BaCl2, CNT (many walls carbon mitron) nanoparticle in working medium.
Embodiment 2
As shown in Figure 1, this utilizes solar photovoltaic cell panel to carry out the system of cogeneration, and this system comprises solar photovoltaic generation system, solar panel residual neat recovering system and additional cooler, described solar photovoltaic generation system comprises solar module 1, storage battery 2, controller 3, inverter 4 and interconnective pipeline, solar panel residual neat recovering system comprises waste heat recovery heater 5, water heater 6, solar water container 7, circulation line, normally open solenoid valve I 11 and normally open solenoid valve II 12, additional cooler comprises fin radiator 8, normally closed solenoid valve I 9, normally closed solenoid valve II 10, pipeline, temperature sensor, control end and interconnective pipeline, solar module 1 by controller 3 respectively with storage battery 2, direct current user, alternating current user connects, and controller 3 is connected with alternating current user by inverter 4, and solar module 1 is also connected with waste heat recovery heater 5, and waste heat recovery heater 5 working substance steam of absorbing heat exports and passes through circulation line, normally open solenoid valve I 11 is connected with water heater 6, the water in water heater 6 heating solar water tank 7, and water heater 6 passes through circulation line, normally open solenoid valve II 12 and the waste heat recovery heater 5 working medium entrance point that absorbs heat is connected, and solar water container 7 is provided with temperature sensor and control end, and waste heat recovery heater 5 sender property outlet that absorbs heat passes through pipeline, normally open solenoid valve I 11, normally closed solenoid valve I 9 is connected with fin radiator 8, and fin radiator 8 is exported and is connected by the working medium import of absorbing heat of normally closed solenoid valve II 10 and waste heat recovery heater 5, control end and temperature sensor, normally closed solenoid valve I 9, normally closed solenoid valve II 10, normally open solenoid valve I 11, normally open solenoid valve II 12 connects.Wherein waste heat recovery heater 5 adopts concurrent flow multi-channel flat tubular type heater, the mixed solution of to be mass ratio the be R245fa+R134a of 0.3:0.7 of the heat absorption working medium in waste heat recovery heater 5, also can add CuO, Al2O3, TiO2, SiO2, BaCl2, CNT (many walls carbon mitron) nanoparticle in working medium.
Embodiment 3
As shown in Figure 1, this utilizes solar photovoltaic cell panel to carry out the system of cogeneration, and this system comprises solar photovoltaic generation system, solar panel residual neat recovering system and additional cooler, described solar photovoltaic generation system comprises solar module 1, storage battery 2, controller 3, inverter 4 and interconnective pipeline, solar panel residual neat recovering system comprises waste heat recovery heater 5, water heater 6, solar water container 7, circulation line, normally open solenoid valve I 11 and normally open solenoid valve II 12, additional cooler comprises fin radiator 8, normally closed solenoid valve I 9, normally closed solenoid valve II 10, pipeline, temperature sensor, control end and interconnective pipeline, solar module 1 by controller 3 respectively with storage battery 2, direct current user, alternating current user connects, and controller 3 is connected with alternating current user by inverter 4, and solar module 1 is also connected with waste heat recovery heater 5, and waste heat recovery heater 5 working substance steam of absorbing heat exports and passes through circulation line, normally open solenoid valve I 11 is connected with water heater 6, the water in water heater 6 heating solar water tank 7, and water heater 6 passes through circulation line, normally open solenoid valve II 12 and the waste heat recovery heater 5 working medium entrance point that absorbs heat is connected, and solar water container 7 is provided with temperature sensor and control end, and waste heat recovery heater 5 sender property outlet that absorbs heat passes through pipeline, normally open solenoid valve I 11, normally closed solenoid valve I 9 is connected with fin radiator 8, and fin radiator 8 is exported and is connected by the working medium import of absorbing heat of normally closed solenoid valve II 10 and waste heat recovery heater 5, control end and temperature sensor, normally closed solenoid valve I 9, normally closed solenoid valve II 10, normally open solenoid valve I 11, normally open solenoid valve II 12 connects.Wherein waste heat recovery heater 5 adopts and drift tube type heater, and the heat absorption working medium in waste heat recovery heater 5 is ammonia, also can add CuO, Al2O3, TiO2, SiO2, BaCl2, CNT (many walls carbon mitron) nanoparticle in working medium.
Below by reference to the accompanying drawings embodiment of the present utility model is explained in detail, but the utility model is not limited to above-mentioned execution mode, in the ken that those of ordinary skill in the art possess, various change can also be made under the prerequisite not departing from the utility model aim.
Claims (2)
1. utilize solar photovoltaic cell panel to carry out a system for cogeneration, it is characterized in that: this system comprises solar photovoltaic generation system, solar panel residual neat recovering system and additional cooler, described solar photovoltaic generation system comprises solar module (1), storage battery (2), controller (3), inverter (4) and interconnective pipeline, solar panel residual neat recovering system comprises waste heat recovery heater (5), water heater (6), solar water container (7), circulation line, normally open solenoid valve I (11) and normally open solenoid valve II (12), additional cooler comprises fin radiator (8), normally closed solenoid valve I (9), normally closed solenoid valve II (10), pipeline, temperature sensor, control end and interconnective pipeline, solar module (1) by controller (3) respectively with storage battery (2), direct current user, alternating current user connects, and controller (3) is connected with alternating current user by inverter (4), and solar module (1) is also connected with waste heat recovery heater (5), and circulation line is passed through in the outlet of waste heat recovery heater (5) heat absorption working substance steam, normally open solenoid valve I (11) is connected with water heater (6), the water in water heater (6) heating solar water tank (7), and water heater (6) passes through circulation line, normally open solenoid valve II (12) and waste heat recovery heater (5) the working medium entrance point that absorbs heat is connected, and solar water container (7) is provided with temperature sensor and control end, and waste heat recovery heater (5) heat absorption sender property outlet passes through pipeline, normally open solenoid valve I (11), normally closed solenoid valve I (9) is connected with fin radiator (8), and fin radiator (8) outlet is connected by the working medium import of absorbing heat of normally closed solenoid valve II (10) and waste heat recovery heater (5), control end and temperature sensor, normally closed solenoid valve I (9), normally closed solenoid valve II (10), normally open solenoid valve I (11), normally open solenoid valve II (12) connects.
2. the system utilizing solar photovoltaic cell panel to carry out cogeneration according to claim 1, it is characterized in that: described waste heat recovery heater (5) has two kinds of forms, one adopts and drift tube type heater, and another adopts concurrent flow multi-channel flat tubular type heater.
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| Application Number | Priority Date | Filing Date | Title |
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| CN201520462045.0U CN204967758U (en) | 2015-07-01 | 2015-07-01 | System for utilize photovoltaic solar panel to carry out cogeneration |
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| Application Number | Priority Date | Filing Date | Title |
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| CN201520462045.0U CN204967758U (en) | 2015-07-01 | 2015-07-01 | System for utilize photovoltaic solar panel to carry out cogeneration |
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107305069A (en) * | 2016-04-22 | 2017-10-31 | 甘肃云时代智能科技有限公司 | The auxiliary hot water boiler of energy-saving solar electricity |
| CN108843528A (en) * | 2018-06-25 | 2018-11-20 | 江苏易缘建筑节能科技有限公司 | Solar power system |
| CN114335629A (en) * | 2021-12-29 | 2022-04-12 | 山东国创燃料电池技术创新中心有限公司 | Fuel cell cogeneration control method and system |
-
2015
- 2015-07-01 CN CN201520462045.0U patent/CN204967758U/en not_active Expired - Fee Related
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107305069A (en) * | 2016-04-22 | 2017-10-31 | 甘肃云时代智能科技有限公司 | The auxiliary hot water boiler of energy-saving solar electricity |
| CN108843528A (en) * | 2018-06-25 | 2018-11-20 | 江苏易缘建筑节能科技有限公司 | Solar power system |
| CN114335629A (en) * | 2021-12-29 | 2022-04-12 | 山东国创燃料电池技术创新中心有限公司 | Fuel cell cogeneration control method and system |
| CN114335629B (en) * | 2021-12-29 | 2024-04-23 | 山东国创燃料电池技术创新中心有限公司 | Combined heat and power control method and system for fuel cell |
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