CN107221442A - Disc type solar energy reacts receiver - Google Patents
Disc type solar energy reacts receiver Download PDFInfo
- Publication number
- CN107221442A CN107221442A CN201710547051.XA CN201710547051A CN107221442A CN 107221442 A CN107221442 A CN 107221442A CN 201710547051 A CN201710547051 A CN 201710547051A CN 107221442 A CN107221442 A CN 107221442A
- Authority
- CN
- China
- Prior art keywords
- catalyst
- shell
- chamber
- receiver
- solar energy
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
Classifications
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01G—CAPACITORS; CAPACITORS, RECTIFIERS, DETECTORS, SWITCHING DEVICES OR LIGHT-SENSITIVE DEVICES, OF THE ELECTROLYTIC TYPE
- H01G9/00—Electrolytic capacitors, rectifiers, detectors, switching devices, light-sensitive or temperature-sensitive devices; Processes of their manufacture
- H01G9/20—Light-sensitive devices
- H01G9/2068—Panels or arrays of photoelectrochemical cells, e.g. photovoltaic modules based on photoelectrochemical cells
-
- 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
- Y02E10/542—Dye sensitized solar cells
Abstract
The present invention provides a kind of disc type solar energy reaction receiver.The receiver includes：Shell, one end of shell is provided with dish-style quartz window, shell is provided with catalyst chamber close to the position of dish-style quartz window, and first gas flow cavity is formed between catalyst chamber and dish-style quartz window；The inside of the other end of shell is provided with forming gas outlet, and connecting portion is provided between forming gas outlet and catalyst chamber, and second gas flow chamber is formed between catalyst chamber and connecting portion and shell；Third gas flow chamber is formed between catalyst chamber and connecting portion, third gas flow cavity is connected with forming gas outlet；Fossil fuel gas access is formed between forming gas outlet and shell；Catalyst chamber is the concave structure formed by multi-layer catalyst carrier, and every layer of catalyst carrier is provided with multiple holes, the material of hole surface coating catalyst in every layer of catalyst carrier is different, and solving catalyst can not be in most suitable catalytic reaction temperature the problem of inefficiency.
Description
Technical field
The present invention relates to solar energy utilization technique field, more particularly to a kind of disc type solar energy reaction receiver.
Background technology
Solar energy reaction receiver primarily serves the effect that solar radiant energy is converted into heat energy.
The receiver of conventional solar energy reaction at present is that disc type solar energy reacts receiver.Wherein, disc type solar energy reacts
Receiver, main that sunshine is converged at into focal point using butterfly parabolic condenser, the receiver for being placed in focal point absorbs too
Positive energy.However, being irradiated because receiver side receives the sunshine for converging reflection by parabolic condenser, opposite side is not received
Solar radiation, causes receiver inner surface to produce great thermograde.For example, Fig. 1 reacts for existing disc type solar energy
Temperature profile on receiver.As shown in figure 1, abscissa x is reacts the position of conversion zone on receiver, ordinate y is
Thermograde is larger in the temperature on corresponding reaction receiver surface, the circumference of conversion zone, so as to cause the disc type solar energy
Reaction receiver catalyst can not be completely under most suitable catalytic reaction temperature, influence heat energy reaction process, it is difficult to efficiently enter
The heat chemistry of row solar energy and fossil fuel is complementary.
The content of the invention
The present invention provides a kind of disc type solar energy reaction receiver, is urged with solving existing disc type solar energy reaction receiver
Agent can not be completely in be caused to be difficult to the efficient heat chemistry for carrying out solar energy and fossil fuel under most suitable catalytic reaction temperature
Complementary the problem of.
The present invention provides a kind of disc type solar energy reaction receiver, including：Shell, one end of the shell is provided with dish-style
Position in quartz window, the shell close to the dish-style quartz window is provided with catalyst chamber, the catalyst chamber and institute
State and be formed with first gas flow cavity between dish-style quartz window；
The other end of the shell is internally provided with forming gas outlet, and the forming gas outlet urges with described
Change is provided with connecting portion between room, and second gas flow cavity is formed between the catalyst chamber and the connecting portion and the shell
Room；Be formed with third gas flow chamber between the catalyst chamber and the connecting portion, the third gas flow cavity with it is described
Forming gas outlet is connected；
Fossil fuel gas access is formed between the forming gas outlet and the shell；
The catalyst chamber is the concave structure formed by multi-layer catalyst carrier, and every layer of catalyst carrier is provided with more
The material of the catalyst of hole surface coating in individual hole, every layer of catalyst carrier is different, as every layer of catalyst is carried
The catalyst on the hole surface between body and the dish-style quartz window in the increase of distance, every layer of catalyst carrier it is most suitable
Reaction temperature is successively reduced；
Wherein, fossil fuel gas enters the second gas flow chamber from the fossil fuel gas access, passes through
The catalyst chamber enters the first gas flow chamber, and the forming gas of reaction generation enters the third gas flow chamber
And flowed out from the forming gas outlet.
Alternatively, every layer of catalyst carrier is the first side close to the side of the dish-style quartz window, with described first
The relative side in side is the second side；
From first side to second side, the quality of catalyst gradually increases, and corresponding porosity is gradually reduced.
Alternatively, the cross section of the shell is shaped as boss type, and the material of the shell is stainless steel.
Alternatively, the catalyst chamber is shaped as tubular, and the tubular includes vertical tube part and tapered portion, the tapered portion with
The dish-style quartz window is oppositely arranged；
The connecting portion, the vertical tube part and the company are provided between the forming gas outlet and the vertical tube part
Second gas flow chamber is formed between socket part and the shell；The 3rd gas is formed between the tapered portion and the connecting portion
Body flow chamber.
Alternatively, the thickness of the vertical tube part is less than the thickness of the tapered portion.
Alternatively, the material of the dish-style quartz window is high light line penetrance material.
The disc type solar energy reaction receiver that the present invention is provided, by setting catalyst chamber to be the formation of multi-layer catalyst carrier
Concave structure, and the difference that the hole surface that is provided with multiple holes, every layer of catalyst carrier of every layer of catalyst carrier is coated with
The catalyst of material, and with the increase of distance between every layer of catalyst carrier and dish-style quartz window, every layer of catalyst is carried
The optimal reactive temperature of the catalyst on the hole surface in body is successively reduced, the structure arrangement of reasonably optimizing catalyst chamber, is reduced
The disc type solar energy reacts the peripheral temperature gradient of receiver.The present invention solves the temperature that existing disc type solar energy reacts receiver
Degree inequality brings the influence that efficiency is reduced, and passes through being layered of catalyst carrier, porous setting so that in every layer of catalyst carrier
Hole surface catalyst material it is different so that catalyst is at optimal reactive temperature, optimize the dish-style
Solar energy reacts the Temperature Distribution of receiver, improves the complementary reaction efficiency of heat chemistry so that disc type solar energy reaction connects
Receive device more economical, safe.
Brief description of the drawings
Fig. 1 is the temperature profile on existing disc type solar energy reaction receiver；
Fig. 2 reacts the overall structure diagram of receiver for the disc type solar energy that the present invention is provided；
Fig. 3 reacts the vertical section structure schematic diagram of receiver for the disc type solar energy that the present invention is provided；
Fig. 4 reacts the cross section structure schematic diagram of receiver for the disc type solar energy that the present invention is provided；
The vertical section schematic diagram of catalyst in the disc type solar energy reaction receiver that Fig. 5 provides for the present invention.
Embodiment
Fig. 2 reacts the overall structure diagram of receiver for the disc type solar energy that the present invention is provided, and Fig. 3 provides for the present invention
Disc type solar energy react receiver vertical section structure schematic diagram, Fig. 4 for the present invention provide disc type solar energy reaction reception
The vertical section of catalyst shows in the cross section structure schematic diagram of device, the disc type solar energy reaction receiver that Fig. 5 provides for the present invention
It is intended to.As in Figure 2-4, the disc type solar energy reaction receiver that the present embodiment is provided includes：Shell 10, one end of shell 10 is set
It is equipped with the position in dish-style quartz window 20, shell 10 close to dish-style quartz window 20 and is provided with catalyst chamber 30, catalyst chamber
First gas flow cavity 40 is formed between 30 and dish-style quartz window 20.The other end of shell 10 is internally provided with synthesis
Gas outlet tube 50, is provided with connecting portion 60, catalyst chamber 30 and connecting portion 60 between forming gas outlet 50 and catalyst chamber 30
Second gas flow chamber 70 is formed between shell 10.Third gas flow cavity is formed between catalyst chamber 30 and connecting portion 60
Room 80, third gas flow cavity is connected with forming gas outlet 50.It is formed between forming gas outlet 50 and shell 10
Fossil fuel gas access 90.The catalyst chamber 30 is the concave structure formed by multi-layer catalyst carrier, and the catalyst
Carrier is provided with the catalyst of the different materials of the hole surface coating in multiple holes, every layer of catalyst carrier, with every
The catalysis on the hole surface between layer catalyst carrier and dish-style quartz window 20 in the increase of distance, every layer of catalyst carrier
The optimal reactive temperature of agent is successively reduced.Wherein, fossil fuel gas enters second gas stream from fossil fuel gas access 90
Dynamic chamber 70, enters the Room of first gas flow cavity 40 by catalyst chamber 30, and the forming gas of reaction generation enters third gas stream
Dynamic chamber 80 simultaneously flows out from forming gas outlet 50.
Specifically, in the present embodiment shell 10 to dish-style quartz window 20, catalyst chamber 30, connecting portion 60 and synthesis gas
Body outlet 50 plays a part of fixed support.The cross section of shell 10 can be square or irregular shape in the present embodiment
Both sides Deng, shell 10 can outer camber line, or straight line.The concrete shape of shell 10 can be according to actual conditions in the present embodiment
It is fixed, it need to only ensure that catalyst can be placed in shell 10.In order to increase the use intensity of shell 10, alternatively, shell
10 cross section is shaped as boss type, and the material of shell 10 is stainless steel.
Further, one end of shell 10 is dish-style quartz window 20 in the present embodiment, and dish-style quartz window 20 is
Dish-style condenser, has the advantages that high temperature resistant, chemical temperatures, can be by solar light focusing formation hot spot direct irradiation in dish-style
On solar energy reaction receiver, and in the way of radiation the fossil fuel gas temperature reacted in receiver is raised, so that
Reach solar energy and the complementary required temperature of fossil fuel heat chemistry.In order that sunshine well penetrate dish-style quartz glass
Window 20, alternatively, the material of dish-style quartz window 20 is high light line penetrance material.Dish-style quartz window in the present embodiment
20 can be attached with shell 10 using kovar alloy with glass sealing process, can be also attached using other technologies.
The present embodiment is not limited the connected mode of shell 10 and dish-style quartz window 20, and only need to meet both can be reliably connected
.
Further, catalyst chamber 30 is provided with close to the position of dish-style quartz window 20 in shell 10 in the present embodiment,
Because photocatalytic process mainly occurs in catalyst surface, therefore, it is by multi-layer catalyst carrier shape to set in catalyst chamber 30
Into concave structure, and apply on the hole surface that is provided with multiple holes, every layer of catalyst carrier of every layer of catalyst carrier
The material of catalyst is different.Again because catalyst carrier is close to one layer of dish-style quartz window 20, temperature is higher；Catalysis
Agent carrier is close to one layer of dish-style quartz window 20, and temperature is relatively low so that the temperature distributing disproportionation of conversion zone is even, reaction zone
Thermograde is larger in the circumference in domain, causes the catalyst that the disc type solar energy reacts receiver can not be completely in most suitable catalysis
Under reaction temperature, so disc type solar energy reaction receiver efficiency declines.Therefore, it is catalyzed in the present embodiment by reasonably optimizing
The structure of room 30 arranges to avoid above mentioned problem.
Specifically, catalyst carrier can be layered and set in the present embodiment, and the catalyst of different materials is plated on every layer
The surface of catalyst carrier Hole, wherein the surface of one layer of catalyst Hole is coated with the catalyst of identical material, one layer is urged
Agent carrier Hole and one layer of catalyst carrier Hole are coated with the catalyst of different materials respectively.Catalyst in the present embodiment
The inside of carrier can use porous media, in cellular, such as use aluminum oxide material.To catalyst carrier in the present embodiment
The size of material and catalyst carrier Hole is not limited, and can be set according to actual conditions, only need to be by catalyst carrier
The surface of Hole is coated with catalyst and can be placed in catalyst chamber 30.And the material in the present embodiment to catalyst
Do not limit, only need catalyst to be catalyzed solar heat chemical reaction.And can be by catalyst carrier in the present embodiment
Openend and the madial wall of dish-style quartz window 20 realize fixation by the way of being welded to connect, due to dish-style quartz window
20 are firmly connected with shell 10, to enable catalyst carrier to be placed in shell 10.The present embodiment is to catalyst carrier and dish
The specific connected mode of formula quartz window 20 is not limited, and only need to meet every layer of catalyst support surface scribbles different materials
Catalyst.
Further, as shown in figure 5, with the increasing of distance between every layer of catalyst carrier and dish-style quartz window 20
Plus, the quality of every layer of catalyst gradually increases, and the porosity of every layer of catalyst is successively reduced, the optimal reaction temperature of every layer of catalyst
Degree is successively reduced, so that every layer of catalyst can be in optimal reactive temperature scope, so as to ensure every layer of catalyst
Efficient solar heat chemical reaction can be carried out at convenient temperature.So, the arrangement being capable of reasonably optimizing catalyst chamber
30 structure, not only enables catalyst more to absorb the radiation of solar energy, and every layer of catalyst is in optimal reaction
Temperature so that fossil fuel can complete to react well into catalyst chamber 30 is interior in the presence of catalyst.
Further, the inside of the other end of shell 10 be provided with forming gas outlet 50, forming gas outlet 50 with
Fossil fuel gas access 90 is formed between shell 10, fossil fuel gas enters catalyst chamber by second gas flow cavity
First gas flow cavity 40 is entered back into after 30, in the reaction generation forming gas of first gas flow cavity 40, the forming gas stream
Enter to third gas flow cavity, finally flowed out by forming gas outlet 50.Wherein, first gas flow cavity 40 in the present embodiment
Space size and the space size that is formed by dish-style quartz window 20 and catalyst chamber 30 of shape and shape determine, second gas
Flow cavity is annular space, and the space that its space size and shape are formed between catalyst chamber 30 and connecting portion 60 and shell 10 is big
Small and shape determines, what the space size and shape of third gas flow cavity were formed by connecting portion 60 and forming gas outlet 50
Space size and shape are determined.The shape of forming gas outlet 50 can be cube in the present embodiment, or cylinder specifically may be used
Depending on the true form of shell 10.The present embodiment is not limited the concrete shape for synthesizing gas outlet tube 50, need to only be expired
Sufficient forming gas can flow out from forming gas outlet 50.
Further, one end of connecting portion 60 can be connected with catalyst carrier by the way of welding in the present embodiment
Connect, the other end of connecting portion 60 can be also attached with forming gas outlet 50 by the way of welding, and the present embodiment is to even
Socket part 60 is not limited with catalyst carrier, the connected mode of forming gas outlet 50 respectively, only need to meet 60 points of connecting portion
It can be reliably connected with catalyst carrier, forming gas outlet 50.Due to the catalyst carrier in catalyst chamber 30 with
The madial wall connection of shell 10, just may be such that forming gas outlet 50 can be fixed in shell 10.In order that obtaining synthesis gas
What body outlet 50 can more be stablized is placed in shell 10, and the present embodiment can be on the lateral wall of forming gas provided with connection
Bar, the lateral wall of one end connection forming gas outlet 50 of connecting rod, the madial wall of the other end connected with outer casing 10 of connecting rod.
Connected mode of the present embodiment to connecting rod respectively with forming gas outlet 50 and shell 10 is not limited, and the present embodiment is to even
Number, the size and shape of extension bar are not also limited, and only need to meet connecting rod can be by forming gas outlet 50 and shell 10
It is reliably connected.
Further, the present embodiment can be separated and recovered in shell 10 close to one end setting gas of forming gas outlet 50
Device.The device can separate unreacted fossil fuel gas from forming gas, again through fossil fuel gas
Entrance 90 enters the heat chemistry complementation that solar energy and fossil fuel are carried out in reaction receiver, to realize that the recovery of resource is sharp again
With.
Reacting the detailed process that is operated of receiver using the present embodiment disc type solar energy is：
Sunshine, which penetrates dish-style quartz window 20 and is focused into hot spot, to be radiated on the catalyst of catalyst chamber 30, due to catalysis
Agent carrier is layered and close arrangement, and the hole surface in every layer of catalyst carrier is coated with the most suitable of the catalyst of different materials
Reaction temperature is successively reduced, so, and fossil fuel gas enters second gas flow chamber 70 from fossil fuel gas access 90,
When entering first gas flow cavity Room 40 by catalyst chamber 30, the catalyst on each layer hole surface can all keep highest activity,
The more forming gas of generation can be reacted, forming gas enters back into third gas flow chamber 80 and from forming gas outlet
50 outflows.It just can so avoid the temperature difference existed in the circumferential due to catalyst in existing disc type solar energy reaction receiver
It is different so that catalyst activity is relatively low, the problem of reaction efficiency is low.
The disc type solar energy reaction receiver that the present embodiment is provided, by setting catalyst chamber to be formed for multi-layer catalyst carrier
Concave structure, and the hole surface that every layer of catalyst carrier is provided with multiple holes, every layer of catalyst carrier is coated with not
With the catalyst of material, and with the increase of distance between every layer of catalyst carrier and dish-style quartz window, every layer of catalyst
The optimal reactive temperature of the catalyst on the hole surface in carrier is successively reduced, the structure arrangement of reasonably optimizing catalyst chamber, reduction
The disc type solar energy reacts the peripheral temperature gradient of receiver.The present embodiment solves existing disc type solar energy reaction receiver
Temperature inequality bring the influence that efficiency is reduced, by being layered of catalyst carrier, porous set so that every layer of catalyst load
The material of the catalyst on the hole surface in body is different, so that catalyst is at optimal reactive temperature, optimizes this
Disc type solar energy reacts the Temperature Distribution of receiver, improves the complementary reaction efficiency of heat chemistry so that the disc type solar energy is anti-
Answer receiver more economical, safe.
On the basis of above-described embodiment, continuing with Fig. 3, catalyst and catalyst chamber 30 concrete shape is carried out detailed
Describe in detail bright.
First, it will be understood by those skilled in the art that receiving the side of the radiation of solar energy, temperature is higher；Dorsad receive
The side of the radiation of solar energy, temperature is relatively low.In order to reduce the temperature difference of catalyst, alternatively, every layer of catalyst carrier is leaned on
The side of nearly dish-style quartz window 20 is the first side, and the side relative with the first side is the second side.From the first side to the second side,
The quality of catalyst gradually increases, and corresponding porosity is gradually reduced.
Specifically, because the temperature distributing disproportionation of catalyst is even, whole catalyst can not the temperature in a relative equilibrium
Under degree, therefore, the hole surface in the present embodiment in every layer of catalyst carrier is coated with the catalyst of non-homogeneous porosity, can
The heat chemistry for greatly promoting solar energy and fossil fuel gas is complementary.Arranged again due to the porosity of catalyst with temperature height and be
Foundation, therefore, in the high place catalyst that less input of temperature, in many catalyst of the low place input of temperature.So, originally
Catalyst porosity is that the first side is gradually reduced to the second side in embodiment, so as to optimize the structure of catalyst, is further carried
The high solar energy efficiency complementary with the heat chemistry of fossil fuel gas, while can also play the circumferential temperature of reduction reaction receiver
Gradient, improves the temperature field of reaction receiver, improves the thermal chemical reaction efficiency that disc type solar energy reflects receiver.
Secondly as be required to accommodate lower catalyst chamber 30 in shell 10, therefore catalyst chamber 30 can basis in the present embodiment
The true form of shell 10 is configured.Catalyst chamber 30 can be the concave architecture of bowl-type, or irregular shape in the present embodiment
The concave architecture of shape, the present embodiment is not limited the shape of catalyst chamber 30, and only need to meet catalyst chamber 30 can be contained in shell
In 10.Alternatively, catalyst chamber 30 is shaped as tubular, and tubular includes vertical tube part and tapered portion, tapered portion and dish-style quartz
Windowpane 20 is oppositely arranged.Connecting portion 60, vertical tube part and connecting portion 60 are provided between forming gas outlet 50 and vertical tube part
Second gas flow chamber 70 is formed between shell 10.Third gas flow chamber is formed between tapered portion and connecting portion 60
80。
Specifically, catalyst carrier is filled with whole catalyst chamber 30 in the present embodiment, specifically can be by the catalysis in vertical tube part
Agent carrier is disposed to extend to one end of connecting portion 60 from the madial wall one end of shell 10, and the catalyst carrier in tapered portion is from connecting portion
60 side extends to the offside of connecting portion 60 so that the space of second gas flow chamber 70 becomes big, advantageously in fossil
Fuel is reacted well into catalyst chamber 30.And vertical tube part and tapered portion have straight tube in certain thickness, the present embodiment
Depending on the thickness of portion and tapered portion can be according to actual conditions.Alternatively, the thickness of vertical tube part is less than the thickness of tapered portion.Specifically
Ground, the thickness of tapered portion becomes big, and catalyst carrier becomes many, and hole is more, and catalyst also just becomes many, due to dish-style quartz window
20 just to the catalyst carrier in tapered portion, and the thermal chemical reaction efficiency of disc type solar energy reflection receiver is higher.
Finally it should be noted that：Various embodiments above is merely illustrative of the technical solution of the present invention, rather than its limitations；To the greatest extent
The present invention is described in detail with reference to foregoing embodiments for pipe, it will be understood by those within the art that：Its according to
The technical scheme described in foregoing embodiments can so be modified, or which part or all technical characteristic are entered
Row equivalent substitution；And these modifications or replacement, the essence of appropriate technical solution is departed from various embodiments of the present invention technology
The scope of scheme.
Claims (6)
1. a kind of disc type solar energy reacts receiver, it is characterised in that including：Shell, one end of the shell is provided with dish-style
Position in quartz window, the shell close to the dish-style quartz window is provided with catalyst chamber, the catalyst chamber and institute
State and be formed with first gas flow cavity between dish-style quartz window；
The other end of the shell is internally provided with forming gas outlet, the forming gas outlet and the catalyst chamber
Between be provided with connecting portion, between the catalyst chamber and the connecting portion and the shell formed second gas flow chamber；Institute
State and third gas flow chamber is formed between catalyst chamber and the connecting portion, the third gas flow cavity and the synthesis gas
Body outlet is connected；
Fossil fuel gas access is formed between the forming gas outlet and the shell；
The catalyst chamber is the concave structure formed by multi-layer catalyst carrier, and every layer of catalyst carrier is provided with multiple holes
The material of hole surface coating catalyst in hole, every layer of catalyst carrier is different, with every layer of catalyst carrier and institute
State the optimal reaction temperature of the catalyst on hole surface in the increase of distance between dish-style quartz window, every layer of catalyst carrier
Degree is successively reduced；
Wherein, fossil fuel gas enters the second gas flow chamber from the fossil fuel gas access, by described
Catalyst chamber enter the first gas flow chamber, reaction generation forming gas enter the third gas flow chamber and from
The forming gas outlet outflow.
2. disc type solar energy according to claim 1 reacts receiver, it is characterised in that every layer of catalyst carrier is close to institute
The side for stating dish-style quartz window is the first side, and the side relative with first side is the second side；
From first side to second side, the quality of catalyst gradually increases, and corresponding porosity is gradually reduced.
3. disc type solar energy according to claim 1 reacts receiver, it is characterised in that the shape of the cross section of the shell
Shape is boss type, and the material of the shell is stainless steel.
4. disc type solar energy according to claim 1 reacts receiver, it is characterised in that the catalyst chamber is shaped as cylinder
Shape, the tubular includes vertical tube part and tapered portion, and the tapered portion is oppositely arranged with the dish-style quartz window；
The connecting portion, the vertical tube part and the connecting portion are provided between the forming gas outlet and the vertical tube part
Second gas flow chamber is formed between the shell；Third gas stream is formed between the tapered portion and the connecting portion
Dynamic chamber.
5. disc type solar energy according to claim 4 reacts receiver, it is characterised in that the thickness of the vertical tube part is less than
The thickness of the tapered portion.
6. disc type solar energy according to claim 1 reacts receiver, it is characterised in that the dish-style quartz window
Material is high light line penetrance material.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710547051.XA CN107221442B (en) | 2017-07-06 | 2017-07-06 | Dish type solar reaction receiver |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710547051.XA CN107221442B (en) | 2017-07-06 | 2017-07-06 | Dish type solar reaction receiver |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN107221442A true CN107221442A (en) | 2017-09-29 |
| CN107221442B CN107221442B (en) | 2022-10-21 |
Family
ID=59952047
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201710547051.XA Active CN107221442B (en) | 2017-07-06 | 2017-07-06 | Dish type solar reaction receiver |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN107221442B (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109326446A (en) * | 2018-09-18 | 2019-02-12 | 华北电力大学（保定） | Solar energy reacts receiver |
| CN112934145A (en) * | 2021-02-07 | 2021-06-11 | 南京航空航天大学 | Spiral-flow type solar particle reactor |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20060048808A1 (en) * | 2004-09-09 | 2006-03-09 | Ruckman Jack H | Solar, catalytic, hydrogen generation apparatus and method |
| CN201401973Y (en) * | 2009-04-03 | 2010-02-10 | 方欣怡 | Concentration system for disc solar rotary parabolic reflector |
| CN103344048A (en) * | 2013-07-18 | 2013-10-09 | 北京航空航天大学 | Narrowing tube bundle structural-cavity solar receiver |
| CN207052467U (en) * | 2017-07-06 | 2018-02-27 | 华北电力大学（保定） | Disc type solar energy reacts receiver |
-
2017
- 2017-07-06 CN CN201710547051.XA patent/CN107221442B/en active Active
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20060048808A1 (en) * | 2004-09-09 | 2006-03-09 | Ruckman Jack H | Solar, catalytic, hydrogen generation apparatus and method |
| CN201401973Y (en) * | 2009-04-03 | 2010-02-10 | 方欣怡 | Concentration system for disc solar rotary parabolic reflector |
| CN103344048A (en) * | 2013-07-18 | 2013-10-09 | 北京航空航天大学 | Narrowing tube bundle structural-cavity solar receiver |
| CN207052467U (en) * | 2017-07-06 | 2018-02-27 | 华北电力大学（保定） | Disc type solar energy reacts receiver |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109326446A (en) * | 2018-09-18 | 2019-02-12 | 华北电力大学（保定） | Solar energy reacts receiver |
| CN112934145A (en) * | 2021-02-07 | 2021-06-11 | 南京航空航天大学 | Spiral-flow type solar particle reactor |
Also Published As
| Publication number | Publication date |
|---|---|
| CN107221442B (en) | 2022-10-21 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| Zhang et al. | Fabrication of CdS hierarchical multi-cavity hollow particles for efficient visible light CO 2 reduction | |
| CN100552320C (en) | Special-shaped modular type hollow space solar energy high-temperature receiver | |
| AU2015260468B2 (en) | Concentrated sunlight heat receiver, reactor, and heater | |
| CN107221442A (en) | Disc type solar energy reacts receiver | |
| CN102575359B (en) | Central tube for a linear concentrating solar thermal power plant, having an absorber layer, and method for applying said absorber layer | |
| CN101091900A (en) | Solar energy photocatalytic reactor based on condenser of composite paraboloid | |
| CN103372413A (en) | Metal foam carrier catalysis bed solar energy absorption reaction device | |
| CN207052467U (en) | Disc type solar energy reacts receiver | |
| CN109876753A (en) | A kind of solar energy high temperature reactor of integrated phase-change accumulation energy and chemical energy storage | |
| CN103797311B (en) | absorber tube | |
| Yang et al. | Solar concentrator with uniform irradiance for particulate photocatalytic hydrogen production system | |
| CN104296396B (en) | Solar energy high-temperature heat collection equipment | |
| CN211056709U (en) | Solar methanol steam reforming hydrogen production focusing reactor | |
| CN110467154A (en) | A kind of solar energy methanol steam reforming hydrogen manufacturing focusing reactor | |
| CN104534688B (en) | A kind of two-stage solar heat absorber | |
| Mu et al. | Direct solar-driven thermochemical CO2-to-fuel conversion with efficiency over 39% employing hierarchical triply periodic minimal surfaces biomimetic foam reactors | |
| US20140326235A1 (en) | Volumetric solar receiver | |
| US20090277442A1 (en) | Coiled heat exchanger with beam spreader especially for use with solar-powered gas processors | |
| CN204388382U (en) | A kind of solar heat absorber with tube bank of extending | |
| CN204141864U (en) | Solar energy high-temperature heat collection equipment | |
| CN104785185B (en) | A kind of have the suspended particles system solar heat chemical reactor preventing optical window thermal deformation and crushing | |
| CN114832732A (en) | Mass transfer enhanced bubbling fixed bed photocatalytic carbon dioxide reduction reactor and method | |
| CN109326446A (en) | Solar energy reacts receiver | |
| Bando et al. | In situ XAFS analysis system for high-pressure catalytic reactions and its application to CO2 hydrogenation over a Rh/Y-zeolite catalyst | |
| CN105222372A (en) | Concentration solar generating machine and solar collector thereof |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PB01 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| GR01 | Patent grant | ||
| GR01 | Patent grant |