CN206055984U - A kind of photothermal conversion device - Google Patents
A kind of photothermal conversion device Download PDFInfo
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- CN206055984U CN206055984U CN201620971272.0U CN201620971272U CN206055984U CN 206055984 U CN206055984 U CN 206055984U CN 201620971272 U CN201620971272 U CN 201620971272U CN 206055984 U CN206055984 U CN 206055984U
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- 238000006243 chemical reaction Methods 0.000 title claims abstract description 27
- 239000012530 fluid Substances 0.000 claims abstract description 45
- 238000010438 heat treatment Methods 0.000 claims abstract description 43
- 230000008859 change Effects 0.000 claims abstract description 34
- 239000007788 liquid Substances 0.000 claims abstract description 16
- 238000005338 heat storage Methods 0.000 claims abstract description 10
- ATJFFYVFTNAWJD-UHFFFAOYSA-N Tin Chemical group [Sn] ATJFFYVFTNAWJD-UHFFFAOYSA-N 0.000 claims description 20
- 238000009825 accumulation Methods 0.000 claims description 12
- VEXZGXHMUGYJMC-UHFFFAOYSA-M Chloride anion Chemical compound [Cl-] VEXZGXHMUGYJMC-UHFFFAOYSA-M 0.000 claims description 11
- 229910052756 noble gas Inorganic materials 0.000 claims description 11
- 150000002835 noble gases Chemical class 0.000 claims description 11
- 238000010992 reflux Methods 0.000 claims description 11
- 239000003795 chemical substances by application Substances 0.000 claims description 8
- 230000007704 transition Effects 0.000 claims description 8
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims description 6
- 230000009466 transformation Effects 0.000 claims description 5
- 238000004891 communication Methods 0.000 claims description 3
- 239000000463 material Substances 0.000 claims description 3
- 229910052757 nitrogen Inorganic materials 0.000 claims description 3
- 239000007787 solid Substances 0.000 claims description 3
- 230000006978 adaptation Effects 0.000 abstract description 2
- 230000009286 beneficial effect Effects 0.000 abstract description 2
- 239000003921 oil Substances 0.000 description 18
- 229910045601 alloy Inorganic materials 0.000 description 10
- 239000000956 alloy Substances 0.000 description 10
- 238000000034 method Methods 0.000 description 7
- 238000012546 transfer Methods 0.000 description 6
- 229910001128 Sn alloy Inorganic materials 0.000 description 5
- 230000005540 biological transmission Effects 0.000 description 5
- TWRXJAOTZQYOKJ-UHFFFAOYSA-L Magnesium chloride Chemical compound [Mg+2].[Cl-].[Cl-] TWRXJAOTZQYOKJ-UHFFFAOYSA-L 0.000 description 4
- WCUXLLCKKVVCTQ-UHFFFAOYSA-M Potassium chloride Chemical compound [Cl-].[K+] WCUXLLCKKVVCTQ-UHFFFAOYSA-M 0.000 description 4
- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 description 4
- 239000007789 gas Substances 0.000 description 4
- PGLIUCLTXOYQMV-UHFFFAOYSA-N Cetirizine hydrochloride Chemical compound Cl.Cl.C1CN(CCOCC(=O)O)CCN1C(C=1C=CC(Cl)=CC=1)C1=CC=CC=C1 PGLIUCLTXOYQMV-UHFFFAOYSA-N 0.000 description 3
- 238000010521 absorption reaction Methods 0.000 description 3
- 239000011261 inert gas Substances 0.000 description 3
- 239000000155 melt Substances 0.000 description 3
- 230000003287 optical effect Effects 0.000 description 3
- 238000007711 solidification Methods 0.000 description 3
- 230000008023 solidification Effects 0.000 description 3
- 238000005516 engineering process Methods 0.000 description 2
- 230000008676 import Effects 0.000 description 2
- 229910001629 magnesium chloride Inorganic materials 0.000 description 2
- 238000012423 maintenance Methods 0.000 description 2
- 239000001103 potassium chloride Substances 0.000 description 2
- 235000011164 potassium chloride Nutrition 0.000 description 2
- 230000005855 radiation Effects 0.000 description 2
- 239000011780 sodium chloride Substances 0.000 description 2
- 238000013459 approach Methods 0.000 description 1
- 230000008901 benefit Effects 0.000 description 1
- 238000005660 chlorination reaction Methods 0.000 description 1
- 239000000306 component Substances 0.000 description 1
- 239000002131 composite material Substances 0.000 description 1
- 230000006835 compression Effects 0.000 description 1
- 238000007906 compression Methods 0.000 description 1
- 239000004020 conductor Substances 0.000 description 1
- 230000008602 contraction Effects 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 239000008358 core component Substances 0.000 description 1
- 239000012043 crude product Substances 0.000 description 1
- 230000006866 deterioration Effects 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 238000007710 freezing Methods 0.000 description 1
- 230000008014 freezing Effects 0.000 description 1
- PCHJSUWPFVWCPO-UHFFFAOYSA-N gold Chemical compound [Au] PCHJSUWPFVWCPO-UHFFFAOYSA-N 0.000 description 1
- 239000010931 gold Substances 0.000 description 1
- 229910052737 gold Inorganic materials 0.000 description 1
- 238000005286 illumination Methods 0.000 description 1
- 239000011229 interlayer Substances 0.000 description 1
- 239000010410 layer Substances 0.000 description 1
- 238000001755 magnetron sputter deposition Methods 0.000 description 1
- 238000010338 mechanical breakdown Methods 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 239000007769 metal material Substances 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 230000008569 process Effects 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 238000007789 sealing Methods 0.000 description 1
- 238000001179 sorption measurement Methods 0.000 description 1
- 230000006641 stabilisation Effects 0.000 description 1
- 238000011105 stabilization Methods 0.000 description 1
- 239000011232 storage material Substances 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
- 238000005303 weighing Methods 0.000 description 1
Classifications
-
- 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
Landscapes
- Central Heating Systems (AREA)
Abstract
This utility model is related to a kind of photothermal conversion device, including housing, light hot receiver, balance bunker;Housing is provided with the double Shell of inner shell and shell, and the thermal of closing is constituted between inner shell and shell, and heat storage medium is filled with thermal;Heating chamber being provided with the bottom of inner shell, torus being provided with the top of inner shell, heat conduction with phase change medium is filled with heating chamber, fluid heat carrier medium is filled with torus;Light hot receiver is arranged in the heating chamber;The upper end of torus connects a thermal medium output pipe, is communicated with the top gaseous state interface of the heating chamber on the top of balance bunker, is communicated with thermal medium output pipe liquid interface in the lower end of balance bunker;The beneficial effects of the utility model are:Being transmitted using heat conduction with phase change media implementation high temperature heat, improve the temperature adaptation scope of the heat-conducting medium of photothermal conversion device output, exportable is higher than 1000 DEG C of high temperature heat conducting medium, solar energy can be made full use of in the big environment of sunlight collecting variable quantity.
Description
Technical field
This utility model belongs to clean energy resource system, more particularly to using a kind of photothermal conversion device of solar energy.
Background technology
There is multiple technologies scheme using field in house clean energy resource at present, include that photo-thermal is sent out in field of solar energy utilization
The modes such as electricity, photovoltaic generation and solar water.Photothermal conversion device is the nucleus equipment of too heat-energy utilizing device, due to from certainly
So the solar energy of boundary's collection is very big with the variable quantity of the factors such as weather, time, and common solar energy heat conversion device cannot be fitted
The situation for answering solar energy variable quantity big, cannot make equipment normal work, in solar energy acquisition amount when solar energy acquisition amount is relatively low
When excessive, heat-conducting medium cannot adapt to too high temperature, hamper and solar energy is made full use of, and constrain Solar use skill
The development of art.
The content of the invention
The purpose of this utility model is to propose a kind of technical scheme of photothermal conversion device, improves photothermal conversion device to becoming
The adaptability of the big solar energy acquisition of change amount, improves solar energy composite utilization benefit.
To achieve these goals, the technical solution of the utility model is:A kind of photothermal conversion device, converts light energy into
Heat energy is supplied to heat energy utilization equipment(7), the photothermal conversion device includes housing(1), light hot receiver(2), balance bunker
(3);The housing is provided with the double Shell of inner shell and shell, and the thermal of closing is constituted between the inner shell and shell
(1-1), in the thermal, it is filled with heat storage medium(0-1);Heating chamber is provided with the bottom of the inner shell(1-2), described
The top of inner shell is provided with torus(1-3), between the heating chamber and torus, it is communicated with pipe(1-8), the communicating pipe
Upper end connects the bottom of the torus, and the lower end of the communicating pipe extend into the bottom of the heating chamber;In the heating chamber
Filled with heat conduction with phase change medium(0-2-1), the heat conduction with phase change medium is from solid state transformation when temperature is increased to phase transition temperature
For the material of liquid, fluid heat carrier medium in the torus, is filled with(0-2-2);The smooth hot receiver is arranged on described adding
In hot chamber;The upper end of the torus connects a thermal medium output pipe(5-1), the other end of the thermal medium output pipe
Connect the thermal medium entrance of the heat energy utilization equipment, the lower end of the torus connects a reflux pipe(5-2), described time
The other end on flow tube road connects the thermal medium outlet of the heat energy utilization equipment;The balance bunker is the cavity of closing, described
The top of balance bunker is provided with gaseous state interface, is provided with liquid interface in the lower end of the balance bunker, and the gaseous state interface is by being provided with
Compressor(4)Pipeline communication described in heating chamber top, thermal medium output pipe described in the liquid orifice, described
Filled with noble gases in balance bunker, the fluid heat carrier medium is preserved in the bottom of the balance bunker.
Further, the position of the housing is less than the heat energy utilization equipment, and the position of the balance bunker is higher than described
Heat energy utilization equipment.
Further, it is provided with the smooth hot receiver and receives the heat conduction cone for injecting light(2-2), receive in the photo-thermal
The outer surface of device is provided with conducting strip(2-3,2-4), the conducting strip contacted with the heat conduction with phase change medium in the heating chamber.
Further, temperature sensor is provided with the reflux pipe(5-4).
Further, the heat storage medium filled in the thermal(0-1)It is phase-change heat accumulation medium, the phase-transition heat-storage is situated between
Matter includes ternary chloride;Noble gases in the balance bunker are nitrogen.
Further, the heat conduction with phase change medium filled in the heating chamber(0-2-1)It is metallic tin.
Further, the fluid heat carrier medium filled in the torus(0-2-2)It is conduction oil.
Further, the heat energy utilization equipment(7)It is Stirling engine expanding end heater.
The beneficial effects of the utility model are:Conventional heat energy transmission is carried out using conventional liquid heat-carrying agent, using phase
Become heat-conducting medium and realize that high temperature heat is transmitted, improve the temperature adaptation scope of the heat-conducting medium of photothermal conversion device output, can
High temperature heat conducting medium of the output higher than 1000 DEG C, can make full use of solar energy in the big environment of sunlight collecting variable quantity.
With reference to the accompanying drawings and examples this utility model is described in detail.
Description of the drawings
Fig. 1 is this utility model structure chart;
Fig. 2 is this utility model photo-thermal receiver architecture figure;
Fig. 3 is the A direction views of Fig. 2;
Fig. 4 is that this utility model fluid heat carrier medium carries out heat energy utilization circulation schematic diagram:
Fig. 5 is this utility model by fluid heat carrier medium to be switched to heat conduction with phase change medium and carries out heat energy utilization circulation and illustrate
Figure;
Fig. 6 is this utility model by heat conduction with phase change medium to be switched to fluid heat carrier medium and carries out heat energy utilization circulation and illustrate
Figure.
Specific embodiment
Embodiment one:
As shown in Figure 1, Figure 2, a kind of photothermal conversion device, converts light energy into heat energy and is supplied to heat energy utilization equipment 7, heat energy profit
It is Stirling engine expanding end heater with equipment, Stirling engine is a kind of external-heat electromotor.
Photothermal conversion device includes housing 1, light hot receiver 2, balance bunker 3.
The position of housing is less than heat energy utilization equipment, and the position of balance bunker is higher than the heat energy utilization equipment.
Housing is provided with inner shell and shell double Shell, and the thermal 1-1 of closing, accumulation of heat are constituted between inner shell and shell
Heat storage medium 0-1 is filled with chamber;The heat storage medium filled in thermal is a kind of phase-change heat accumulation medium, using ternary chlorination
Thing, ternary chloride are the mixture of potassium chloride, Sodium Chloride and magnesium chloride.
Heating chamber 1-2 is provided with the bottom of inner shell, torus 1-3 is provided with the top of inner shell, heating chamber and torus it
Between be communicated with pipe 1-8, the bottom in the upper end communication loop chamber of communicating pipe, the lower end of communicating pipe extend into the bottom of heating chamber.
Heat conduction with phase change medium 0-2-1 is filled with heating chamber, heat conduction with phase change medium is when temperature is increased to phase transition temperature
From the material that solid state transformation is liquid, the heat conduction with phase change medium in the present embodiment is metallic tin.
Fluid heat carrier medium 0-2-2 is filled with torus, fluid heat carrier medium is liquid heat conductive material, the present embodiment
In, the fluid heat carrier medium filled in torus is conduction oil, and the conduction oil of the present embodiment is that maximum operating temperature is not less than 360
DEG C conduction oil.
Light hot receiver is arranged in heating chamber;Light hot receiver is provided with cylinder blanket 2-1, is provided with light hot receiver
The heat conduction cone 2-2 of light is injected in reception, is provided with annular conducting strip 2-3 in the outer surface of photo-thermal receiver casing, is received in photo-thermal
The two ends of device shell are provided with rectangle conducting strip 2-4, and conducting strip is contacted with the heat conduction with phase change medium in heating chamber.Light hot receiver
The light that reception is input into by light guide 6.
The upper end of torus is provided with fluid heat carrier medium outlet 1-6, and fluid heat carrier medium outlet one thermal medium of connection is defeated
Go out pipeline(5-1), the heating medium inlet of the other end connection heat energy utilization equipment of thermal medium output pipe;Under torus
End is provided with fluid heat carrier medium import 1-7, and fluid heat carrier medium import connects a reflux pipe(5-2), reflux pipe it is another
One end connects the Crude product input of heat energy utilization equipment.
Balance bunker is arranged on the platform higher than heat energy utilization equipment;Balance bunker is the cavity of closing, in the upper of balance bunker
Portion is provided with gaseous state interface 3-1, is provided with liquid interface 3-2 in the lower end of balance bunker;Noble gases are provided with the top of heating chamber to connect
Mouth 1-5, the gaseous state interface of balance bunker connect inert gas interface by being provided with the inert gas duct 4-1 of compressor 4;Balance bunker
Liquid interface thermal medium output is connected by fluid heat carrier medium expiration and inspiration pipe 5-3 in the peak of thermal medium output pipe
Pipeline.
Filled with noble gases 0-3 in balance bunker, in the present embodiment, the noble gases in balance bunker are nitrogen.In balance
Preserve fluid heat carrier medium in the bottom in storehouse.
Temperature sensor 5-4 is provided with reflux pipe.
Embodiment two:
A kind of photo-thermal conversion method, methods described are the photo-thermal conversion methods of one photothermal conversion device of embodiment;The side
Method includes:
Such as Fig. 4, light hot receiver 2 receive the light source containing heat energy of the input of light guide 6 and produce and add described in energy heats
Heat conduction with phase change medium 0-2-1 in hot chamber, heat conduction with phase change medium is the good metallic tin of heat-conductive characteristic, and heat conduction with phase change medium adds
Fluid heat carrier medium 0-2-2 in heat torus above, while the heat storage medium in thermal absorbs and stores part heat
Energy.
In the present embodiment, using the self-loopa heating heat energy utilization equipment that is heated of fluid heat carrier medium, when fluid heat-carrying is situated between
Matter(Conduction oil)Can flow up after being heated, heated fluid heat carrier medium is defeated by heat energy by thermal medium output pipe 5-1
Heat energy utilization equipment 7 is delivered to, the fluid heat carrier medium for completing heat energy utilization returns to the torus by reflux pipe 5-2
It is interior, complete heat energy utilization circulation;
Such as Fig. 5, as the phase transition temperature of the stannum of heat conduction with phase change medium(Or fusing point)For 232 DEG C, when heat conduction with phase change medium
Temperature is changed into after liquid more than phase transition temperature(The present embodiment is when the temperature of heat conduction with phase change medium is higher than 300 DEG C), start pressure
Contracting machine 4, and ventilating control valve 4-2 is opened, the noble gases in balance bunker 3 are filled with heating chamber, in the top shape of heating chamber
Into inflation interlayer 1-4, the heat conduction with phase change medium in heating chamber is made to enter torus by communicating pipe 1-8, the fluid in torus
Heat-carrying agent enters balance bunker by the liquid interface of balance bunker lower end, after whole fluid heat carrier mediums enter balance bunker,
Close compressor, stops inflating in heating chamber;Now heat conduction with phase change medium substitution fluid heat-carrying agent carries out heat energy utilization and follows
Ring.Heat energy is delivered to the heat energy utilization equipment 7 by thermal medium output pipe 5-1 by heat conduction with phase change medium, completes heat energy profit
Heat conduction with phase change medium returns to the bottom of the torus by reflux pipe 5-2, completes heat energy utilization circulation.
Such as Fig. 6, when the temperature of the heat conduction with phase change medium is reduced(The present embodiment is less than when the temperature of heat conduction with phase change medium
When 250 DEG C), noble gases in heating chamber are returned to before the temperature of heat conduction with phase change medium is reduced to phase transition temperature described flat
In weighing apparatus storehouse, operational approach is to open recycle control valve 4-3, and in heating chamber, noble gases are back in balance bunker, are made into circulation
Heat conduction with phase change medium back flow in chamber makes into the fluid heat carrier medium in balance bunker to be back in torus to heating chamber, stream
Body heat-carrying agent substitutes heat conduction with phase change medium and carries out heat energy utilization circulation.Fluid heat carrier medium passes through thermal medium output pipe 5-1
Heat energy is delivered to into the heat energy utilization equipment 7, the fluid heat carrier medium for completing heat energy utilization is returned to by reflux pipe 5-2
The bottom of the torus, completes heat energy utilization circulation.
Photothermal converter is to receive the high density sunlight focusing that the transmission of sunlight transmission and reflection device comes, and is converted into heat
Can, fluid heat carrier medium is conducted to while phase-transition heat-storage, fluid heat carrier medium relies on itself thermodynamic cycle, is CETRINE
Electromotor automatic transport heat energy.
The housing 1 and its associated components of photothermal converter is made by heating resisting metal material.
In the quiescent state, exocoel 1-1 fillings ternary chloride phase-change heat accumulation medium 0-1;Heating cavity of resorption 1-2 filling metallic tins
(Or tin alloy)0-2-1, circulation epicoele 1-3 filling conduction oil 0-2-2;Indifferent gas gap 1-4 is situated between in switching fluid heat-carrying
It is used for accommodating compressed inert 0-3 during matter.
Light hot receiver 2 is used for the photo-thermal energy of the high-energy focusing hot spot F that the projection of receiving light heat transfer catheters transmitting terminal comes,
It is translated into medium and high temperature thermal energy conduction and gives heat conduction with phase change medium.
Light hot receiver 2 is the core component of photothermal converter.Light hot receiver 2 is cylindrical hermetic housing structure.Circle
Cylindricality enclosure is the absorption space of high-energy focusing hot spot F.It is to fill to put heat conduction with phase change outside cylindrical hermetic housing 2-1
The heating cavity of resorption 1-2 of medium 0-2-1.
Inside cylindrical hermetic housing 2-1, closely it is covered with the positive rib of multiaspect for receiving high-energy focusing hot spot F along inner wall surface
2-2 is bored in cone heat conduction, and the cone of heat conduction cone 2-2 is directed to housing axle center;The cylinder outside the cylindrical hermetic housing 2-1, along post
The annular conducting strip 2-3 of face axially spaced-apart arrangement.In hull outside termination, vertical rectangle conducting strip is arranged laterally at a spacing along end face
2-4.Housing is provided with taper photo-thermal reception conduit 2-5, and photo-thermal reception conduit 2-5 is welded as a whole with photothermal converter housing 1.
The surface that 2-2 is bored in the heat conduction of multiaspect pyramid carries out metallic plasma magnetron sputtering technique process.Make polygonal prism
Cone heat conduction cone 2-2 Surface Creation optical absorption characteristics surface.To improve light thermal absorptivity, photo-thermal reverse radiation is reduced.
Because the high-energy focusing hot spot F that the projection of light heat transfer catheters 6 comes has very high temperature.The polygonal prism of light hot receiver 2
Cone 2-2 must possess high temperature resistant, anti-yaw damper and low thermal resistance performance.
The light principle of light hot receiver 2:According to stealth technique principle, sunlight focus on light beam is in photo-thermal reception conduit 2-5
Interior focusing along light transmission direction projects heat conduction cone 2-2 surfaces, wherein most luminous energy are heat energy by sorption enhanced.On a small quantity
Luminous energy is by heat conduction cone 2-2 surface reflections.Because of the intensive arrangements of multiple heat conduction cone 2-2, the luminous energy that 2-2 surfaces reflect is bored by heat conduction
Heat energy can be converted in each heat conduction cone 2-2 surfaces interreflection until being absorbed totally by heat conduction cone 2-2.And seldom can be reverse
Return incident direction.
Light heat ray Jing poles multiple reflections on heat conduction cone 2-2, make 2 inner chamber of light hot receiver be formed close to optical black
Depth grey body;Because boring 2-2 in the multiple heat conduction of the intensive setting of 2 inner chamber of light hot receiver, so as to increase optical heat radiation heating surface
Product;Reduce heat transfer interface thermal resistance, so as to improve heat transfer efficiency.
The heat conduction principle of light hot receiver 2:From the high density focus on light beam Jing light heat transfer catheters of light heat transfer catheters 6
2-5 passages are radiated on multiaspect pyramid 2-2 in the high-energy focusing hot spot F that focus is pooled, because multiple heat conduction cone 2-2 has very
High surface area, most light heat rays are absorbed to be formed after medium and high temperature heat energy, by conducting strip by heat conduction cone 2-2(2-3、2-4)
It is conducted to metallic tin(Or tin alloy)0-2-1.
The money saving function of heat energy:To make hot systems keep stable, operating mode in a balanced way, photothermal converter to be provided simultaneously with accumulation of heat work(
Energy.Heat accumulation function experiences solid-liquid state change in phase transition temperature by ternary chloride and realizes.
Ternary chloride is mixed according to a certain percentage by potassium chloride, Sodium Chloride and magnesium chloride, is allowed to phase transition temperature and is close to
400°C.So that its expiration and inspiration heat energy by solidification, fusing near the temperature, maintains unit temp stable.
Binary fluid heat-carrying agent(Including 0-2-1,0-2-2)Itself thermodynamic cycle transporting heat energy:To adopt solar energy
The heat energy that collection transmitting device is collected realizes wide temperature range(Low temperature-middle temperature-high temperature)Transmission, improves the thermodynamics effect of thermal power machinery
Rate, reduces the kinetic energy consumption of heat energy conveying, maintains hot systems stable operation.Photothermal conversion device adopts conduction oil 0-2-2 and gold
Category stannum(Or tin alloy)0-2-1 binary fluids heating agent conveys heat energy.Whole hot systems are enable from room temperature to 1200C °
Normal work in wide temperature province, is gathered and in fluid heat carrier medium 0-2 under different illumination conditions with adapting to whole hot systems
Transporting heat energy during different temperatures.Device is in low, middle temperature(Less than 400C °)Interval fluid heat carrier medium can adopt conduction oil 0-2-2;
In high temperature(Higher than 300C °)Interval fluid heat carrier medium 0-2 can adopt metallic tin(Or tin alloy)0-2-1.300C ° to 400C °
Between be two kinds of fluid heat carrier medium handover operation temperature ranges.Two kinds of fluid heat carrier medium handover operation temperature ranges of system
It is defined by the temperature measured by temperature sensor 5-4.
Because binary fluid heat-carrying agent is to realize switching with indifferent gas under photothermal converter inner sealing environment, therefore conduction oil
0-2-2 and metallic tin(Or tin alloy)0-2-1 will not occur oxidation deterioration.
The system operation principle of photothermal converter:Middle temperature phase change heat storage material under normal temperature state, in photothermal converter
Ternary chloride 0-1 and metallic tin(Or its alloy)0-2-1 is solid-state, and conduction oil 0-2-2 is liquid.
When light hot receiver receives and spread out of heat energy, metallic tin is directly heated in heating chamber 1-2(Or its alloy)0-2-1.
Metallic tin(Or its alloy)While by thermal energy conduction to the ternary chloride 0-1 in accumulation of heat exocoel 1-1 and circulation after 0-2-1 heats up
Conduction oil 0-2-2 in epicoele 1-3.When conduction oil 0-2-2 reaches uniform temperature, start along circulating line setting path from
It is dynamic to circulate.Electromotor is sent out for CETRINE and uninterruptedly conveys heat.
When Jing conduction oils 0-2-2 heating reaches metallic tin melt temperature, metallic tin(Or its alloy)0-2-1 melts first
Accumulation of heat simultaneously has mobility simultaneously.When circulating heat conduction oil 0-2-2 temperature stabilizations are higher than metallic tin(Or its alloy)0-2-1 fusing points with
During upper uniform temperature, start compressor(Inertia air pump)4, aspirate the noble gases 0-3 in balance bunker 3 and pass through inert gas tube
Road 4-1 is compressed into the indifferent gas gap 1-4 in heating chamber 1-2.By metallic tin(Or its alloy)0-2-1 is expressed to circulation epicoele 1-
3, take over conduction oil 0-2-2 Automatic Cycle conveying heat.System is realized in middle temperature and is progressively transitioned under the condition of high temperature running.Quilt
The conduction oil 0-2-2 for displacing is by metallic tin(Or its alloy)0-2-1 is forced in balance bunker 3.
Work as metallic tin(Or its alloy)When 0-2-1 reaches 400 C °, the ternary chloride 0-1 in thermal 1-1 start by
Step melts heat absorption, saves peak value heat energy.
After the ternary chloride 0-1 in thermal 1-1 all melts, system temperature continues to raise, and maintenance system is in
Temperature is simultaneously progressively transitioned into condition of high temperature operation.
Heat reduction is given when extraneous, when system temperature is less than 400 C °, ternary chloride 0-1 then heat release solidifications first, solidification
Institute's liberated heat is to continue heat supply with hot spot, and the system of maintenance is run in middle temperature state;Metallic tin is reduced in temperature(Or its
Alloy)Before 0-2-1 freezing pointes, system is switched to conduction oil 0-2-2 circulation patterns.This is kept with the mode of switching thermal medium
Special woods electromotor and whole hot systems are in wide temperature range stable operation.
Binary fluid thermal medium 0-2 in photothermal converter promotes metal with the compression indifferent gas 0-3 that compressor 1-4 is provided
Stannum(Or its alloy)Mutual switchover operation between two medium of 0-2-1 and conduction oil 0-2-2.
To reduce the armamentarium of thermal loss, photothermal converter and its correlation, pipeline, effectively insulating tightly must be set
Layer.
Photothermal converter must be placed lower than the position of the conjuncted machine of CETRINE generating-heat pump;4 palpus of balance bunker 3 and compressor
Installed in the position higher than photothermal converter and Stirling engine.
Because the position of photothermal converter is far below Stirling engine expanding end heater 7, therefore fluid heat carrier medium Jing light
After the heating expansion of hot receiver 2, by itself heat power to high bit flow, in the expanding end heater into Stirling engine
After 7, mechanical energy is converted heat into and contraction of lowering the temperature.Because Stirling engine expanding end heater 7 is in a high position, therefore cooling is received
Fluid heat carrier medium after contracting itself heat power reduces and settles to low level.After photothermal converter accumulation heat is flowed through, then connect
Light hot receiver 2 is heated and enters subsequent cycle.
The potential difference that fluid heat carrier medium is disposed by equipment, utilizes hot, forms itself heat power to the thermogenetic temperature difference
Circulation.Outer powered has been broken away from thoroughly.Power consumption can both have been reduced, be avoided that again because power-equipment wear and tear and occurs leak with
Mechanical breakdown.So as to realize economic, safe, the long-acting operation of hot systems device external power-free.
Claims (8)
1. a kind of photothermal conversion device, converts light energy into heat energy and is supplied to heat energy utilization equipment(7), it is characterised in that it is described
Photothermal conversion device includes housing(1), light hot receiver(2), balance bunker(3);The housing is provided with the double of inner shell and shell
Layer housing, constitutes the thermal of closing between the inner shell and shell(1-1), in the thermal, it is filled with heat storage medium
(0-1);Heating chamber is provided with the bottom of the inner shell(1-2), torus are provided with the top of the inner shell(1-3), it is described to add
Pipe is communicated between hot chamber and torus(1-8), the upper end of the communicating pipe connects the bottom of the torus, the connection
The lower end of pipe extend into the bottom of the heating chamber;Heat conduction with phase change medium is filled with the heating chamber(0-2-1), the phase transformation
Heat-conducting medium is, when temperature is increased to phase transition temperature from the material that solid state transformation is liquid, fluid to be filled with the torus
Heat-carrying agent(0-2-2);The smooth hot receiver is arranged in the heating chamber;The upper end of the torus connects a heat and is situated between
Matter output pipe(5-1), the thermal medium entrance of the other end connection heat energy utilization equipment of the thermal medium output pipe, institute
The lower end for stating torus connects a reflux pipe(5-2), the other end connection heat energy utilization equipment of the reflux pipe
Thermal medium outlet;The balance bunker is the cavity of closing, is provided with gaseous state interface on the top of the balance bunker, in the balance
The lower end in storehouse is provided with liquid interface, and the gaseous state interface is by being provided with compressor(4)Pipeline communication described in heating chamber top,
Thermal medium output pipe described in the liquid orifice, filled with noble gases in the balance bunker, in the balance bunker
Preserve the fluid heat carrier medium in bottom.
2. a kind of photothermal conversion device according to claim 1, it is characterised in that the position of the housing is less than the heat
Equipment can be utilized, the position of the balance bunker is higher than the heat energy utilization equipment.
3. a kind of photothermal conversion device according to claim 1, it is characterised in that be provided with reception in the smooth hot receiver
Inject the heat conduction cone of light(2-2), conducting strip is provided with the outer surface of the smooth hot receiver(2-3,2-4), the conducting strip
Contact with the heat conduction with phase change medium in the heating chamber.
4. a kind of photothermal conversion device according to claim 1, it is characterised in that be provided with temperature on the reflux pipe
Sensor(5-4).
5. a kind of photothermal conversion device according to claim 1, it is characterised in that the accumulation of heat filled in the thermal is situated between
Matter(0-1)It is phase-change heat accumulation medium, the phase-change heat accumulation medium includes ternary chloride;Noble gases in the balance bunker are
Nitrogen.
6. a kind of photothermal conversion device according to claim 1, it is characterised in that the phase transformation filled in the heating chamber is led
Thermal medium(0-2-1)It is metallic tin.
7. a kind of photothermal conversion device according to claim 1, it is characterised in that the fluid filled in the torus is carried
Thermal medium(0-2-2)It is conduction oil.
8. a kind of photothermal conversion device according to claim 1, it is characterised in that the heat energy utilization equipment(7)It is this
Special woods engine expansion end heater.
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CN201620971272.0U CN206055984U (en) | 2016-08-30 | 2016-08-30 | A kind of photothermal conversion device |
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CN201620971272.0U CN206055984U (en) | 2016-08-30 | 2016-08-30 | A kind of photothermal conversion device |
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CN201620971272.0U Withdrawn - After Issue CN206055984U (en) | 2016-08-30 | 2016-08-30 | A kind of photothermal conversion device |
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Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN106225264A (en) * | 2016-08-30 | 2016-12-14 | 高振刚 | A kind of photothermal conversion device and method |
CN107655062A (en) * | 2017-10-31 | 2018-02-02 | 山东圣泉新材料股份有限公司 | A kind of heater and heating system |
-
2016
- 2016-08-30 CN CN201620971272.0U patent/CN206055984U/en not_active Withdrawn - After Issue
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN106225264A (en) * | 2016-08-30 | 2016-12-14 | 高振刚 | A kind of photothermal conversion device and method |
CN107655062A (en) * | 2017-10-31 | 2018-02-02 | 山东圣泉新材料股份有限公司 | A kind of heater and heating system |
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