CN204006782U - High-performance solar heat-exchange system - Google Patents
High-performance solar heat-exchange system Download PDFInfo
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- CN204006782U CN204006782U CN201420449258.5U CN201420449258U CN204006782U CN 204006782 U CN204006782 U CN 204006782U CN 201420449258 U CN201420449258 U CN 201420449258U CN 204006782 U CN204006782 U CN 204006782U
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- Prior art keywords
- heat
- exchange system
- evaporimeter
- performance solar
- solar heat
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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
- Y02E10/44—Heat exchange systems
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Abstract
The utility model provides high-performance solar heat-exchange system, comprises evaporimeter, compressor, heat collector and be arranged at the condenser in heat exchange water tank, the input of compressor is connected with the water side of evaporimeter, output is connected with the water inlet end of evaporimeter after connecting condenser and heat collector, form heat exchange loop, blanketing gas heat transfer medium in heat exchange loop, compressor of the present utility model, wing blade, heat collector panel is connected to form by the condenser coil of circulation line and water tank inside the loop that an energy transmits, the refrigerant that this product adopts is that novel environmental protection refrigerant R410a boiling point is at normal temperatures-51.8 DEG C, utilize refrigerant in heat collector panel and wing blade, to evaporate at normal temperatures, make heat collector panel and wing blade form low-temperature space, because the boiling point of refrigerant is far below day normal temperature, cause this heat transfer process to be ensured stable carrying out.
Description
Technical field
The energy that the utility model relates to solar energy produces and utilizes field, relates in particular to high-performance solar heat-exchange system.
Background technology
Along with applying of green energy resource, solar energy heat collector and system have been widely used in industry, construction and daily field.Wherein, solar water heater is simple in structure owing to having, easy to use and the advantages such as simple and easy are installed, and is widely used.In common solar heat exchange (hot water) system, solar energy evaporation plate is arranged at outdoor more, be convenient on position that the sun irradiates, but in the circulatory system of solar heat exchange, when indoor and outdoor lighting or environment are when poor, to make evaporation plate fully " normally work ", thereby affect the heat-exchange capacity of solar energy.Meanwhile, aggravated the aging of evaporation plate.For the problems referred to above, the embodiments that adopt many evaporation plate in prior art, carry out the deficiency in supplemental heat conversion more, but because its subject matter is that illumination deficiency is caused, therefore, still cannot solve the not enough low problem of hot switching energy that causes of illumination.
Utility model content
For solving in above-mentioned prior art, when solar illuminating is not enough, the low problem that evaporation plate illumination conversion ratio is low.
In order to achieve the above object, the utility model provides following technical scheme: high-performance solar heat-exchange system, comprises evaporimeter, compressor, heat collector and be arranged at the condenser in heat exchange water tank; The input of described compressor is connected with the water side of described evaporimeter, and output is connected with the water inlet end of described evaporimeter after connecting described condenser and described heat collector, forms heat exchange loop, blanketing gas heat transfer medium in described heat exchange loop.
In a preferred embodiment, the structure of described evaporimeter is for sticking up shape blade construction.
In a preferred embodiment, described heat collector is heat collector panel.
In a preferred embodiment, the one side of described heat collector panel or the two-sided media flow chamber of offering, described media flow chamber comprises: many parallel flow cavities and converge chamber, one end of described many parallel flow cavities with described in converge chamber and be communicated with.
In a preferred embodiment, described in converge chamber and be, grid chamber, the grid shape in described coral lattice chamber comprises: square, circular or oval.
In a preferred embodiment, described heat collector panel is of a size of: 1500mm × 800mm.
In a preferred embodiment, described heat exchange water tank is barrel-shaped, and described barrel-shaped madial wall comprises the helical groove of radially offering, and described helical groove is communicated with the water inlet of described exchange water tank.
In a preferred embodiment, described condenser is condenser pipe, and described condenser pipe is series in the front end pipeline of described evaporimeter.
In a preferred embodiment, also comprise filter; Described filter is series in the front end pipeline of described evaporimeter.
In a preferred embodiment, also comprise flow controller; Described flow controller is series in the front end pipeline of described evaporimeter.
Beneficial effect of the present utility model is, compressor of the present utility model, evaporimeter, heat collector panel are connected to form by the condenser coil of circulation line and water tank inside the loop that an energy transmits, the refrigerant that this product adopts is that novel environmental protection refrigerant R410a boiling point is at normal temperatures-51.8 DEG C, utilize refrigerant in heat collector panel and wing blade, to evaporate at normal temperatures, make heat collector panel and wing blade form low-temperature space, because the boiling point of refrigerant is far below day normal temperature, cause this heat transfer process to be ensured stable carrying out.
Brief description of the drawings
In order to be illustrated more clearly in the utility model embodiment or technical scheme of the prior art, to the accompanying drawing of required use in embodiment or description of the Prior Art be briefly described below, apparently, accompanying drawing in the following describes is only embodiment more of the present utility model, for those of ordinary skill in the art, do not paying under the prerequisite of creative work, can also obtain according to these accompanying drawings other accompanying drawing.
Fig. 1 is in a kind of embodiment of the utility model, the composition schematic diagram of high-performance heat exchange defrost system;
Fig. 2 is in a kind of embodiment of the utility model, the structural representation of heat collector panel;
Fig. 3 is in the another kind of embodiment of the utility model, the composition schematic diagram of solar heat exchange defrost system;
Fig. 4 is in another embodiment of the utility model, the composition schematic diagram of solar heat exchange defrost system.
Detailed description of the invention
Below in conjunction with accompanying drawing of the present utility model, the technical solution of the utility model is clearly and completely described, obviously, described embodiment is only the utility model part embodiment, instead of whole embodiment.Based on the embodiment in the utility model, those of ordinary skill in the art are not making the every other embodiment obtaining under creative work prerequisite, all belong to the scope of the utility model protection.
Consisting of of high-performance solar heat-exchange system in a kind of embodiment of the utility model: the water side 11 of evaporimeter 10 is connected with the input of compressor 20 by connecting line, the output of compressor 20 is connected with 31 ends of condenser 30 by connecting line, condenser 30 is arranged in heat exchange water tank 40,32 ends connect after heat collector 50 by connecting line, be connected with the water inlet end 12 of evaporimeter 10, form heat exchange loop.Blanketing gas heat transfer medium in heat exchange loop, as coolant media.Heat exchange water tank 40 arranges water inlet 41 and delivery port 42.The structure of above-mentioned evaporimeter 10 is for sticking up shape blade construction.Above-mentioned heat collector 50 is heat collector panel.The refrigerant adopting in the application is that a kind of novel environmental protection refrigerant R410a boiling point is at normal temperatures-51.8 DEG C, utilize refrigerant in heat collector panel and wing blade, to evaporate at normal temperatures, make heat collector panel and wing blade form low-temperature space, because the boiling point of refrigerant is far below day normal temperature, cause this heat transfer process to be ensured stable carrying out.
For ensureing good heat build-up effect, in a kind of embodiment of the utility model, as shown in Figure 2, the one side of heat collector panel 50 or the two-sided media flow chamber of offering, media flow chamber comprises: many parallel flow cavities 51 and converge chamber 52, one end of many parallel flow cavities 51 with converge chamber 52 and be communicated with.The above-mentioned structure that converges chamber 52 is, grid chamber, and the grid shape in coral lattice chamber comprises: square, circular or oval.Above-mentioned heat collector panel 50 is of a size of: 1500mm × 800mm.
For making the hydrothermal exchange in heat exchange water tank 40 more even, efficient, in a kind of embodiment of the present utility model, as shown in Figure 3, the cavity shape of heat exchange water tank 40 is barrel-shaped.Comprise the helical groove 43 of radially offering at barrel-shaped madial wall, helical groove 43 is communicated with the water inlet 41 of exchange water tank 10.Its condenser 30 is condenser pipe.Condenser pipe is fixedly connected on helical groove 43 bottoms.Thereby make the hydrothermal exchange in heat exchange water tank 40 more even, efficient.
In another kind of embodiment of the present utility model, condenser 30 is fixedly connected with the bottom side of heat exchange water tank 40.In heat exchange water tank 40 by the central dividing plate be arrangeding in parallel, the body of wall of heat exchange water tank 40 inside is divided into the water chamber on upper strata and the intake antrum of lower floor, water chamber is communicated with the delivery port of heat exchange water tank 40, intake antrum is communicated with the water inlet of heat exchange water tank 40, and the bottom that condenser 30 is fixed on heat exchange water tank 40 is arranged in intake antrum.
For making the evaporation effect of evaporimeter better, in another kind of embodiment of the present utility model, as shown in Figure 4, and at a side fan attachment 90 of evaporation plate, in the pipeline of evaporation plate front end, i.e. in-line filter 91 and flow controller 92 in heat exchange loop.Thereby be convenient to filtration to impurity in pipeline and throttling the above; it is only detailed description of the invention of the present utility model; but protection domain of the present utility model is not limited to this; any be familiar with those skilled in the art the utility model disclose technical scope in; can expect easily changing or replacing, within all should being encompassed in protection domain of the present utility model.Therefore, protection domain of the present utility model should described be as the criterion with the protection domain of claim.
The above; it is only detailed description of the invention of the present utility model; but protection domain of the present utility model is not limited to this; any be familiar with those skilled in the art the utility model disclose technical scope in; can expect easily changing or replacing, within all should being encompassed in protection domain of the present utility model.Therefore, protection domain of the present utility model should described be as the criterion with the protection domain of claim.
Claims (10)
1. high-performance solar heat-exchange system, is characterized in that, comprises evaporimeter, compressor, heat collector and be arranged at the condenser in heat exchange water tank; The input of described compressor is connected with the water side of described evaporimeter, and output is connected with the water inlet end of described evaporimeter after connecting described condenser and described heat collector, forms heat exchange loop, blanketing gas heat transfer medium in described heat exchange loop.
2. high-performance solar heat-exchange system according to claim 1, is characterized in that, the structure of described evaporimeter is for sticking up shape blade construction.
3. high-performance solar heat-exchange system according to claim 1 and 2, is characterized in that, described heat collector is heat collector panel.
4. high-performance solar heat-exchange system according to claim 3, it is characterized in that, the one side of described heat collector panel or the two-sided media flow chamber of offering, described media flow chamber comprises: many parallel flow cavities and converge chamber, one end of described many parallel flow cavities with described in converge chamber and be communicated with.
5. high-performance solar heat-exchange system according to claim 4, is characterized in that, described in converge chamber and be, grid chamber, the grid shape in described grid chamber comprises: square, circular or oval.
6. according to the high-performance solar heat-exchange system described in claim 4 or 5, it is characterized in that, described heat collector panel is of a size of: 1500mm × 800mm.
7. high-performance solar heat-exchange system according to claim 1, is characterized in that, described heat exchange water tank is barrel-shaped, and described barrel-shaped madial wall comprises the helical groove of radially offering, and described helical groove is communicated with the water inlet of described exchange water tank.
8. high-performance solar heat-exchange system according to claim 1, is characterized in that, described condenser is condenser pipe, and described condenser pipe is series in the front end pipeline of described evaporimeter.
9. according to the high-performance solar heat-exchange system described in claim 1 or 8, it is characterized in that, also comprise filter; Described filter is series in the front end pipeline of described evaporimeter.
10. high-performance solar heat-exchange system according to claim 9, is characterized in that, it is characterized in that, also comprises flow controller; Described flow controller is series in the front end pipeline of described evaporimeter.
Priority Applications (1)
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CN201420449258.5U CN204006782U (en) | 2014-08-08 | 2014-08-08 | High-performance solar heat-exchange system |
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CN201420449258.5U CN204006782U (en) | 2014-08-08 | 2014-08-08 | High-performance solar heat-exchange system |
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CN204006782U true CN204006782U (en) | 2014-12-10 |
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2014
- 2014-08-08 CN CN201420449258.5U patent/CN204006782U/en active Active
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C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
TR01 | Transfer of patent right | ||
TR01 | Transfer of patent right |
Effective date of registration: 20200826 Address after: 810699 n201-n202, No.1, South Gaotie Road, Haidong Industrial Park, Ping'an District, Haidong City, Qinghai Province Patentee after: BAIGUO TECHNOLOGY Co.,Ltd. Address before: 747000 Jinshan business hall, Jintai Hotel, Gannan Tibetan Autonomous Prefecture, Gansu Province Patentee before: GANSU BAIGUO SOLAR ENERGY TECHNOLOGY Co.,Ltd. |