CN204202213U - High-efficiency solar heat-exchange system - Google Patents
High-efficiency solar heat-exchange system Download PDFInfo
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- CN204202213U CN204202213U CN201420449376.6U CN201420449376U CN204202213U CN 204202213 U CN204202213 U CN 204202213U CN 201420449376 U CN201420449376 U CN 201420449376U CN 204202213 U CN204202213 U CN 204202213U
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- heat
- evaporimeter
- exchange system
- efficiency 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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- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
Abstract
The utility model provides high-efficiency solar heat-exchange system, comprises, evaporimeter, compressor, heat collector and the condenser be arranged 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 the loop of an energy transferring by the condenser coil of circulation line and water tank inside, the refrigerant that this product adopts is that novel environmental protection refrigerant R410a boiling point is at normal temperatures-51.8 DEG C, refrigerant is utilized to evaporate in heat collector panel and wing blade at normal temperatures, heat collector panel and wing blade is made to form low-temperature space, because the boiling point of refrigerant is far below day normal temperature, this heat transfer process is caused to be ensured stable carrying out.
Description
Technical field
The energy that the utility model relates to solar energy produces and utilizes field, particularly relates to high-efficiency 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, easy to use and install the advantages such as simple and easy owing to having structure, is widely used.Exchange in (hot water) system at common solar heat, solar energy evaporation plate is arranged at outdoor more, be convenient on position that the sun carries out irradiating, but in the circulatory system that solar heat exchanges, when indoor and outdoor lighting or environment poor time, evaporation plate will be made fully " normally to work ", thus have impact on the heat-exchange capacity of solar energy.Meanwhile, the aging of evaporation plate is exacerbated.For the problems referred to above, the embodiment adopting many evaporation plate in prior art, carrys out the deficiency in supplemental heat conversion more, but due to its subject matter be caused by illumination deficiency, therefore, still cannot solve illumination not enough cause the problem of hot-cast socket energy inefficiencies.
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-efficiency solar heat-exchange system, wherein, comprises, evaporimeter, compressor, heat collector and the condenser be arranged in heat exchange water tank; The input of described compressor is connected with the water side of described evaporimeter, output is connected with the water inlet end of described evaporimeter after connecting described condenser and described heat collector, form heat exchange loop, blanketing gas heat transfer medium in described heat exchange loop, described evaporimeter is evaporation plate, described evaporation plate comprises: organize evaporation part more, and described evaporation part comprises, drainage tube, accumulation pipe and evaporation tube; One end of described drainage tube is communicated with described accumulation pipe, and the other end of described accumulation pipe is communicated with drainage tube.
In a preferred embodiment, described evaporation tube is multiple tube banks be arranged in parallel.
In a preferred embodiment, the outer wall of described evaporation tube comprises multiple column evaporator.
In a preferred embodiment, described column evaporator is taper column evaporator, and the top of described taper column evaporator is fixedly connected with described evaporation tube.
In a preferred embodiment, described evaporation part quantity is 3 groups.
In a preferred embodiment, described heat collector is heat collector panel, the one side of described heat collector panel or two-sidedly offer media flow chamber, described media flow chamber comprises: many parallel flow cavities and converge chamber, and one end of described many parallel flow cavities is communicated with described convergence chamber; Described convergence chamber is, grid chamber, and the grid shape in described grid chamber comprises: square, circular or oval; 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 that radial direction is offered, and described helical groove is communicated with the water inlet of described heat 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 positioned inline is 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 the loop of an energy transferring by the condenser coil of circulation line and water tank inside, the refrigerant that this product adopts is that novel environmental protection refrigerant R410a boiling point is at normal temperatures-51.8 DEG C, refrigerant is utilized to evaporate in heat collector panel and wing blade at normal temperatures, heat collector panel and wing blade is made to form low-temperature space, because the boiling point of refrigerant is far below day normal temperature, this heat transfer process is caused to be ensured stable carrying out.
Accompanying drawing explanation
In order to be illustrated more clearly in the utility model embodiment or technical scheme of the prior art, be briefly described to the accompanying drawing used required in embodiment or description of the prior art below, apparently, accompanying drawing in the following describes is only embodiments more of the present utility model, for those of ordinary skill in the art, under the prerequisite not paying creative work, other accompanying drawing can also be obtained according to these accompanying drawings.
Fig. 1 is that in a kind of embodiment of the utility model, High Efficiency Thermal exchanges the composition schematic diagram of defrost system;
Fig. 2 is in a kind of embodiment of the utility model, the generalized section of evaporation tube;
Fig. 3 is that in the another kind of embodiment of the utility model, solar heat exchanges the composition schematic diagram of defrost system;
Fig. 4 is in another embodiment of the utility model, and solar heat exchanges the composition schematic diagram of defrost system;
Fig. 5 is in a kind of embodiment of the utility model, the schematic cross-section of evaporation tube;
Fig. 6 is in a kind of embodiment of the utility model, the structural representation of heat collector panel.
Detailed description of the invention
Below in conjunction with accompanying drawing of the present utility model, be clearly and completely described the technical solution of the utility model, obviously, described embodiment is only the utility model part embodiment, instead of whole embodiments.Based on the embodiment in the utility model, those of ordinary skill in the art are not making the every other embodiment obtained under creative work prerequisite, all belong to the scope of the utility model protection.
Consisting of of high-efficiency solar heat-exchange system in a kind of embodiment of the utility model: the water side 11 of evaporimeter 10 is connected by the input port of connecting line with compressor 20, the delivery outlet 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 are connected with the water inlet end 12 of evaporimeter 10 after connecting heat collector 50 by connecting line.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 adopted in the application is that a kind of novel environmental protection refrigerant R410a boiling point is at normal temperatures-51.8 DEG C, refrigerant is utilized to evaporate in heat collector panel and wing blade at normal temperatures, heat collector panel and wing blade is made to form low-temperature space, because the boiling point of refrigerant is far below day normal temperature, this heat transfer process is caused to be ensured stable carrying out.
For increasing evaporation effect, in a kind of embodiment of the utility model, as shown in Figure 2, evaporimeter 10 is evaporation plate.Single evaporation plate comprises: organize evaporation part more, as three evaporation parts 101,102,103, in single evaporation part, for 101, comprise, drainage tube 1011, accumulation pipe 1012 and evaporation tube 1013.One end of drainage tube 1011 is communicated with accumulation pipe 1012.The other end piling up pipe 1012 is communicated with drainage tube 1011.Wherein, evaporation tube 1012 is multiple tube banks be arranged in parallel.For reducing the chamber pressure of evaporation tube 1012, comprise relief pipe 1014 in the bottom of every beam evaporation pipe, this relief pipe 1014 is capillary shape curved pipe.Working medium, from working medium import one dividing into three, is respectively 1,2, No. 3 pipeline, and working medium is equal to the flow process of 1,2, No. 3 pipeline from working medium diffluence pass.This evaporimeter 10 in use as shown in the figure, is vertically placed.Drainage tube 1011 length of three evaporation parts 101,102,103, namely flow process is equal, and working medium reduces pressure through capillary-compensated relief pipe 1014.When just starting, working medium is after flowing to accumulation pipe 1012 position, because pressure is inadequate, can pile up at this position, and along with the carrying out of evaporation, pressure meeting herein constantly increases, the tubule at relief pipe 1014 position, the effect of the reducing pressure by regulating flow that just in time can get up.Number of tubes calculates according to disengagement area.
For ensureing good evaporation effect, in a kind of embodiment of the utility model, as shown in Figure 5, the one-body molded multiple column evaporator 10131 of outer wall of evaporation tube 1013, this column evaporator 10131 is on the upside of evaporation tube 1012 or the outer wall distribution of downside.As a kind of preferred embodiment of the present utility model, column evaporator 10131 is taper column evaporator, and top and the evaporation tube 1013 of taper column evaporator 10131 are welded and fixed, or adopt other forms to fix.
For ensureing good heat build-up effect, in a kind of embodiment of the utility model, as shown in Figure 6, heat collector panel 50 one side or two-sidedly offer media flow chamber, 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 structure in above-mentioned convergence 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 another 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 at barrel-shaped madial wall the helical groove 43 that radial direction offers, helical groove 43 is communicated with the water inlet 41 of heat exchange water tank 40.Its condenser 30 is condenser pipe.Condenser pipe is fixedly connected on bottom helical groove 43.Thus make the hydrothermal exchange in heat exchange water tank 40 more even, efficient.
In a kind of embodiment of the present utility model, condenser 30 is fixedly connected with the bottom side of heat exchange water tank 40.Central dividing plate by be arrangeding in parallel in heat exchange water tank 40, 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 42 of heat exchange water tank 40, intake antrum is communicated with the water inlet 41 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 embodiment of the present utility model, as shown in Figure 4, at the 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.Thus the filtration be convenient to impurity in pipeline and throttling.
The above; be only detailed description of the invention of the present utility model; but protection domain of the present utility model is not limited thereto; anyly be familiar with those skilled in the art in the technical scope that the utility model discloses; change can be expected easily or replace, all should be encompassed within 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-efficiency solar heat-exchange system, is characterized in that, comprises, evaporimeter, compressor, heat collector and the condenser be arranged in heat exchange water tank; The input of described compressor is connected with the water side of described evaporimeter, output is connected with the water inlet end of described evaporimeter after connecting described condenser and described heat collector, form heat exchange loop, blanketing gas heat transfer medium in described heat exchange loop, described evaporimeter is evaporation plate, described evaporation plate comprises: organize evaporation part more, and described evaporation part comprises, drainage tube, accumulation pipe and evaporation tube; One end of described drainage tube is communicated with described accumulation pipe, and the other end of described accumulation pipe is communicated with drainage tube.
2. high-efficiency solar heat-exchange system according to claim 1, is characterized in that, described evaporation tube is multiple tube banks be arranged in parallel.
3. high-efficiency solar heat-exchange system according to claim 1 and 2, is characterized in that, the outer wall of described evaporation tube comprises multiple column evaporator.
4. high-efficiency solar heat-exchange system according to claim 3, is characterized in that, described column evaporator is taper column evaporator, and the top of described taper column evaporator is fixedly connected with described evaporation tube.
5. high-efficiency solar heat-exchange system according to claim 1 and 2, is characterized in that, described evaporation part quantity is 3 groups.
6. high-efficiency solar heat-exchange system according to claim 3, it is characterized in that, described heat collector is heat collector panel, the one side of described heat collector panel or two-sidedly offer media flow chamber, described media flow chamber comprises: many parallel flow cavities and converge chamber, and one end of described many parallel flow cavities is communicated with described convergence chamber; Described convergence chamber is, grid chamber, and the grid shape in described grid chamber comprises: square, circular or oval; Described heat collector panel is of a size of: 1500mm × 800mm.
7. high-efficiency 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 that radial direction is offered, and described helical groove is communicated with the water inlet of described heat exchange water tank.
8. high-efficiency 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. the high-efficiency solar heat-exchange system according to claim 1 or 8, is characterized in that, also comprise, filter; Described positioned inline is in the front end pipeline of described evaporimeter.
10. high-efficiency solar heat-exchange system according to claim 7, is characterized in that, also comprise, flow controller; Described flow controller is series in the front end pipeline of described evaporimeter.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420449376.6U CN204202213U (en) | 2014-08-08 | 2014-08-08 | High-efficiency solar heat-exchange system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420449376.6U CN204202213U (en) | 2014-08-08 | 2014-08-08 | High-efficiency solar heat-exchange system |
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| Publication Number | Publication Date |
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| CN204202213U true CN204202213U (en) | 2015-03-11 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN201420449376.6U Active CN204202213U (en) | 2014-08-08 | 2014-08-08 | High-efficiency solar heat-exchange system |
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| CN (1) | CN204202213U (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104807222A (en) * | 2015-04-28 | 2015-07-29 | 唐玉敏 | Double-layer heat utilization plate |
| CN104807223A (en) * | 2015-04-28 | 2015-07-29 | 唐玉敏 | Hetero-state heat utilization plate |
| CN106091733A (en) * | 2016-08-04 | 2016-11-09 | 唐玉敏 | A kind of dual-purpose heat exchanger plates |
| CN106123667A (en) * | 2016-08-04 | 2016-11-16 | 唐玉敏 | A kind of heat collector panel of feed liquor span shunting |
| CN106595136A (en) * | 2016-12-14 | 2017-04-26 | 大连理工大学 | Efficient flat plate type solar evaporation panel |
-
2014
- 2014-08-08 CN CN201420449376.6U patent/CN204202213U/en active Active
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104807222A (en) * | 2015-04-28 | 2015-07-29 | 唐玉敏 | Double-layer heat utilization plate |
| CN104807223A (en) * | 2015-04-28 | 2015-07-29 | 唐玉敏 | Hetero-state heat utilization plate |
| CN106091733A (en) * | 2016-08-04 | 2016-11-09 | 唐玉敏 | A kind of dual-purpose heat exchanger plates |
| CN106123667A (en) * | 2016-08-04 | 2016-11-16 | 唐玉敏 | A kind of heat collector panel of feed liquor span shunting |
| CN106595136A (en) * | 2016-12-14 | 2017-04-26 | 大连理工大学 | Efficient flat plate type solar evaporation panel |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20200924 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. |
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| TR01 | Transfer of patent right |