CN205412274U - Solar energy enrichment facility - Google Patents
Solar energy enrichment facility Download PDFInfo
- Publication number
- CN205412274U CN205412274U CN201521043013.3U CN201521043013U CN205412274U CN 205412274 U CN205412274 U CN 205412274U CN 201521043013 U CN201521043013 U CN 201521043013U CN 205412274 U CN205412274 U CN 205412274U
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- CN
- China
- Prior art keywords
- raw material
- heat
- solar energy
- enrichment facility
- concentration
- 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.)
- Expired - Fee Related
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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
Abstract
The utility model relates to a combine supporting equipment to use with the material storing jar that needs the concentration dustpan type enrichment facility, utilize the heat energy of solar energy production, realize the device concentrated to the raw materials, belong to solar energy light and heat and utilize the field. Solar energy enrichment facility to current carries out technological transformation and innovation, makes it become an upgrading device. Large -scale concentrated with the automatic circulation of raw and other materials under the low temperature condition, in the middle of the concentration process, the change of gelatinization, coking, unstability can not appear in the raw materials. Reach that the equipment investment is few, degree of automation is high, concentration efficiency is high, do not need the professional to operate, reach save time, laborsaving, economize the merit, economize people's effect. It need concentrated jar of body of multiple -effect with dedicated concentrator, the supporting use of cooling tower to solve original solar energy enrichment facility, and materials requirements is special, and is with high costs, uses the defect that science and technology expected much.
Description
Technical field
This utility model belongs to solar energy heat utilization field, relates generally to dustpan shaped circulating enrichment facility with needing the raw material storage tanks concentrated to combine supporting assembling use, utilizes the heat energy that solar energy produces, it is achieved a kind of solar energy enrichment facility concentrating raw material.
Background technology
Solar energy is a kind of regenerative resource, its aboundresources, be widely used, pollution-free.Can be as the alternate resources of numerous energy such as electricity, coal, oil, gas.It is mainly used in several big field such as photo-thermal, Generate, Generation, Generator.The most most widely used is exactly photo-thermal field, generally according to the temperature that can reach and the difference of purposes, and it is divided into low temperature to utilize (＜ 200 DEG C), middle temperature to utilize (200～800 DEG C) and high temperature to utilize (＞ 800 DEG C) solar energy heat utilization.The device that low temperature utilizes at present mainly has solar water heater, solar energy enrichment facility.
At present, known solar energy enrichment facility, mainly the burning of boiler is replaced to produce heat energy with solar energy resources, supply special Multi-effect concentration equipment, cooling tower supports the use the function that could realize concentrating, its defect is: Multi-effect concentration tank body is many, expending material amount big, material requires special (usually corrosion-resistant stainless steel), with high costs；Equipment conveying, installation difficulty, floor space are big, and installation environment requirement condition is high, need reinforced concrete to thicken ground, applicating technology requirement height, operation complexity, need professional to use.
Therefore, in solar energy concentration field, it is badly in need of wanting a kind of equipment cost low, transports, install simply, it is not necessary to the novel device of professional's operation.
Summary of the invention
For overcoming the defect of existing solar energy enrichment facility, this utility model provides a kind of and solar source combines with raw material storage tanks and adds a kind of solar energy enrichment facility that dustpan shaped circulating enrichment facility assembling match uses.
This utility model is by solving the technical scheme that technical problem is used:
A kind of solar energy enrichment facility be on the basis of original raw material storage tanks, with the addition of a solar heat-collection plate, a dustpan shaped circulating enrichment facility (hereinafter referred to as dustpan), a non-conservation tank, three circulating pumps, a boiler, a condenser and various pipe fitting, instrument collectively forms.
Overall operation has 3 systems:
1, feedstock circulation concentration systems:
2, hot water cyclesystem:
Solar energy changes into heat energy, and a part adds hot water for boiler, and a part acts on the thermal-collecting tube inside dustpan device.
3, steam cooling system:
Dustpan closed between raw material storage tanks and non-conservation tank high low dip put, its centre is heat-conducting plate, and thermal-collecting tube is presented herein below.Thermal-collecting tube helical form dish turns bottom dustpan, and the inside moisture source is the supply of boiler.The heat energy that its constant absorption solar energy converts, heats heat-conducting plate mounted thereon.Heat-conducting plate is stair Wrinkleds, controls at about 1cm by the most lasting circulation trickling raw thickness so that raw material flow rate is uniform, wave overturns, is heated comprehensively, repeatedly moisture distillation inside raw material is become steam and discharge from steam pipe, reach concentrated effect.This function can replace the use of the Multi-effect concentration tank body of special concentrator inside original solar energy enrichment facility.Being equipped with acdity and basicity measuring meter, thermometer, concentration meter on this device respectively, 9 can grasp the situation of change of raw material in time, need offer to process foundation for producing.
This utility model can reach following beneficial effect:
The circulation of raw material automatization being concentrated on a large scale under this utility model cryogenic conditions, in the middle of concentration process, raw material does not haves gelatinizing, coking, unstable change.Equipment investment cost is low, and automaticity is high, transport, install simple, it is not necessary to professional operates, reach to save time, laborsaving, save merit, save the effect of people.
Accompanying drawing explanation
Below in conjunction with the accompanying drawings this utility model is further illustrated.
Fig. 1 is integral installation figure of the present utility model: 1, collecting plate；2, non-conservation tank；3, concentration meter；4, connecting tube；5, circulating pump 1；6, dustpan shaped circulating enrichment facility；7, thermometer；8, discharging opening；9, water-circulating pipe；10, acdity and basicity measuring meter；11, discharge outlet；12, condenser；13, conveying pipeline；14, circulating pump 2；15, boiler；16, feed pipe；17, temp autocontrolled valve；18, water inlet pipe；19, heat circulation pipe；20, drainage conduit；21, circulating pump 3；22, steam pipe；23, raw material storage tanks；24, feeding tube；25, pillar.
Fig. 2 is the A-A sectional view of holding vessel and non-conservation tank in Fig. 1
Fig. 3 is the front elevational schematic of dustpan shaped circulating enrichment facility (6) in Fig. 1
Fig. 4 is the B1-B1 sectional view of Fig. 3
Fig. 5 is the upward view of Fig. 4
Detailed description of the invention
Non-conservation tank (2) is empty, and raw material enters raw material storage tanks (23) by feeding tube (24), and upper doses can not exceed the capacity of non-conservation tank (2).Boiler (15) is arranged on above two tanks by support, fills with water, the upper water of thermal-collecting tube (in Fig. 5 26) of dustpan shaped enrichment facility (6) the inside.Solar energy is converted to heat energy by the collecting plate (1) that pillar (25) supports, and a part is for the water heating of boiler (15) the inside, and a part is for thermal-collecting tube (in Fig. 5 26) heat energy regular supply.The temperature of boiler (15) the inside water reaches requirement, temp autocontrolled valve (17) is opened, a part flows into heat circulation pipe (19), and a part is used for the moisturizing of thermal-collecting tube (in Fig. 5 26) by water inlet pipe (18).Heat circulation pipe (19) is coiled in raw material storage tanks (23) inwall, raw material in hot water flowing heating tank, is entered the water-circulating pipe (9) being coiled in non-conservation tank (2) inwall by connecting tube (4).The temperature of water-circulating pipe (9) the inside same non-conservation tank of coolant-temperature gage (2) the inside enrichment materials neutralizes, and enters boiler (15), complete hot water circuit under the effect of circulating pump 1 (5).
Thermometer (7) shows dustpan shaped circulating enrichment facility (6) internal temperature, temperature reaches requirement, circulating pump 3 (21) starts, by drainage conduit (20), the raw material of holding vessel (23) the inside is continuously supplied in heat conduction thin plate Fig. 4 on the surface of (in Fig. 4 27) under the effect of feed pipe (16), the slow Uniform Flow of raw material.Thermal-collecting tube (in Fig. 5 26) is positioned at below heat conduction thin plate (in Fig. 4 27), the a large amount of heat energy of constant absorption also conducts to heat-conducting plate (in Fig. 4 27), and then trickling by steam pipe (22), is discharged into condenser (12) is cooled to distilled water at the above raw material evaporation and concentration of heat-conducting plate (in Fig. 4 27), steam.When this device does not works, the inner water of thermal-collecting tube (in Fig. 5 26) discharges dustpan shaped circulating enrichment facility (6) by discharge outlet (11).The acid-base value of acdity and basicity measuring meter (10) record raw material, the acid-base value of raw material, thermometer (7) displays temperature situation are controlled in convenient regulation.Final raw material enters non-conservation tank (2) by discharging opening (8), reaches once to circulate the effect of concentration.
Non-conservation tank (2) avris installs a concentration meter (3), the concentration of the enrichment materials of display non-conservation tank (2) the inside.If concentration is not reaching to requirement, circulating pump 2 (14) starts, and by conveying pipeline (13), enrichment materials is delivered into raw material storage tanks (23) from non-conservation tank (2) is, carries out next circulation and concentrate.This circulation can the most unrestrictedly be carried out, until being concentrated to raw material specify requirement, and the outer otherwise processed of drain tank.
Claims (5)
1. a solar energy enrichment facility, is characterized in that dustpan shaped circulating enrichment facility, with needing the raw material storage tanks concentrated to combine supporting assembling use, utilizes the heat energy that solar energy produces, it is achieved the concentration to raw material.
A kind of solar energy enrichment facility the most according to claim 1, it is characterized in that dustpan shaped circulating enrichment facility (6) closed between raw material storage tanks (23) and non-conservation tank (2) high low dip put, its centre is heat-conducting plate (27), thermal-collecting tube (26) is presented herein below, thermal-collecting tube (26) helical form dish turns in dustpan shaped circulating enrichment facility (6) bottom, the inside moisture source is the supply of boiler (15), the heat energy that constant absorption solar energy converts, heat heat-conducting plate (27) mounted thereon, heat-conducting plate (27) is in stair Wrinkled, the most lasting circulation trickling raw thickness is controlled at 1cm, make raw material flow rate uniform, wave overturns, it is heated comprehensively, repeatedly moisture distillation inside raw material is become steam to discharge from steam pipe, reach concentrated effect；This function can replace the use of the Multi-effect concentration tank body of special concentrator inside original solar energy enrichment facility, acdity and basicity measuring meter (10), thermometer (7), concentration meter (3) it is equipped with respectively on this device, the situation of change of raw material can be grasped in time, need offer to process foundation for producing.
A kind of solar energy enrichment facility the most according to claim 1 and 2, it is characterized in that non-conservation tank (2) is empty, raw material enters raw material storage tanks (23) by feeding tube (24), and upper doses can not exceed the capacity of non-conservation tank (2)；Boiler (15) is arranged on above two tanks by support, fill with water, the upper water of thermal-collecting tube (in Fig. 5 26) of dustpan shaped enrichment facility (6) the inside, solar energy is converted to heat energy by the collecting plate (1) that pillar (25) supports, a part is for the water heating of boiler (15) the inside, and a part is for thermal-collecting tube (in Fig. 5 26) heat energy regular supply；Boiler (15) the inside coolant-temperature gage reaches requirement, temp autocontrolled valve (17) is opened, a part flows into heat circulation pipe (19), and a part is used for the moisturizing of thermal-collecting tube (in Fig. 5 26) by water inlet pipe (18)；Heat circulation pipe (19) is coiled in raw material storage tanks (23) inwall, raw material in hot water flowing heating tank, the water-circulating pipe (9) being coiled in non-conservation tank (2) inwall is entered by connecting tube (4), the temperature of water-circulating pipe (9) the inside same non-conservation tank of coolant-temperature gage (2) the inside enrichment materials neutralizes, under the effect of circulating pump 1 (5), enter boiler (15), complete hot water circuit.
A kind of solar energy enrichment facility the most according to claim 1 and 2, it is characterized in that thermometer (7) shows dustpan shaped circulating enrichment facility (6) internal temperature, temperature reaches requirement, circulating pump 3 (21) starts, by drainage conduit (20), the raw material of holding vessel (23) the inside is continuously supplied on the surface of heat-conducting plate (27) under the effect of feed pipe (16), the slow Uniform Flow of raw material；Thermal-collecting tube (26) is positioned at below heat-conducting plate (27), the a large amount of heat energy of constant absorption also conducts to heat-conducting plate (27), and then will trickling in the above raw material evaporation and concentration of heat-conducting plate (27), steam is discharged into condenser (12) by steam pipe (22) and is cooled to distilled water, final raw material enters non-conservation tank (2) by discharging opening (8), reaches once to circulate the effect of concentration.
A kind of solar energy enrichment facility the most according to claim 1 and 2, it is characterized in that non-conservation tank (2) avris installs a concentration meter (3), the concentration of the enrichment materials of display non-conservation tank (2) the inside, if concentration is not reaching to requirement, circulating pump 2 (14) starts, by conveying pipeline (13), enrichment materials is delivered into raw material storage tanks (23) from non-conservation tank (2) is, carry out circulation next time to concentrate, this circulation can the most unrestrictedly be carried out, until being concentrated to raw material specify requirement, the outer otherwise processed of drain tank.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201521043013.3U CN205412274U (en) | 2015-12-16 | 2015-12-16 | Solar energy enrichment facility |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201521043013.3U CN205412274U (en) | 2015-12-16 | 2015-12-16 | Solar energy enrichment facility |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205412274U true CN205412274U (en) | 2016-08-03 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201521043013.3U Expired - Fee Related CN205412274U (en) | 2015-12-16 | 2015-12-16 | Solar energy enrichment facility |
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| Country | Link |
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| CN (1) | CN205412274U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109677318A (en) * | 2018-12-28 | 2019-04-26 | 海宁市英德赛电子有限公司 | A kind of double tank transhipment tank cars |
-
2015
- 2015-12-16 CN CN201521043013.3U patent/CN205412274U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109677318A (en) * | 2018-12-28 | 2019-04-26 | 海宁市英德赛电子有限公司 | A kind of double tank transhipment tank cars |
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| DD01 | Delivery of document by public notice |
Addressee: Zhang Qian Document name: Notification of Passing Examination on Formalities |
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| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20160803 Termination date: 20191216 |
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| CF01 | Termination of patent right due to non-payment of annual fee |