CN203518515U - Heat recovery type solar drying system - Google Patents
Heat recovery type solar drying system Download PDFInfo
- Publication number
- CN203518515U CN203518515U CN201320617517.6U CN201320617517U CN203518515U CN 203518515 U CN203518515 U CN 203518515U CN 201320617517 U CN201320617517 U CN 201320617517U CN 203518515 U CN203518515 U CN 203518515U
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- China
- Prior art keywords
- heat
- type solar
- outlet
- heat exchanger
- regenerator
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- Expired - Fee Related
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- 238000001035 drying Methods 0.000 title claims abstract description 33
- 238000011084 recovery Methods 0.000 title abstract 3
- 239000012530 fluid Substances 0.000 claims abstract description 12
- 238000005338 heat storage Methods 0.000 claims abstract description 8
- 238000010438 heat treatment Methods 0.000 claims abstract description 5
- 239000002912 waste gas Substances 0.000 claims description 6
- 238000009423 ventilation Methods 0.000 claims description 4
- 230000005540 biological transmission Effects 0.000 abstract 2
- 239000007789 gas Substances 0.000 description 5
- 239000002918 waste heat Substances 0.000 description 3
- 238000010586 diagram Methods 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 239000000956 alloy Substances 0.000 description 1
- 229910045601 alloy Inorganic materials 0.000 description 1
- REDXJYDRNCIFBQ-UHFFFAOYSA-N aluminium(3+) Chemical class [Al+3] REDXJYDRNCIFBQ-UHFFFAOYSA-N 0.000 description 1
- OKTJSMMVPCPJKN-UHFFFAOYSA-N carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- 239000003245 coal Substances 0.000 description 1
- 238000004134 energy conservation Methods 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 239000003345 natural gas Substances 0.000 description 1
- 239000003921 oil Substances 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
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Classifications
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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
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P70/00—Climate change mitigation technologies in the production process for final industrial or consumer products
- Y02P70/10—Greenhouse gas [GHG] capture, material saving, heat recovery or other energy efficient measures, e.g. motor control, characterised by manufacturing processes, e.g. for rolling metal or metal working
Abstract
A heat recovery type solar drying system comprises a trough type solar thermal collector, a heat transmission pipeline, a heating medium pump, a heat storage tank, a heat exchanger, an air blower and a ventilating duct, wherein an outlet of the air blower is connected with an inlet of a thermal fluid channel of the heat exchanger, an outlet of the thermal fluid channel of the heat exchanger is connected with an inlet of a drying oven, and a heat-absorbing tube of the trough type solar thermal collector, the heat storage tank, the heating medium pump and a thermal fluid channel coil of the heat exchanger are connected in series through a heat transmission pipeline. The heat recovery type solar drying system is characterized in that a heat regenerator which has a heat exchanging function is arranged, an inlet of a thermal fluid channel of the heat regenerator is connected with an exhaust gas outlet of the drying oven, and an outlet of a cold fluid channel of the heat regenerator is connected with an inlet of the air blower.
Description
Technical field
The utility model relates to a kind of system of recycling solar energy drying waste gas residual heat, especially adopts the middle high temperature solar drying system of slot light collection thermal-arrest, belongs to solar energy utilization technique field.
Background technology
In the main trend of current this energy resource consumption, the conventional energy resources such as coal, oil, natural gas can to environment cause huge pollution and some day can exhaustion totally, solar energy is wherein played the part of more and more important role as a kind of emerging energy at this.Solar energy drying with its feature such as easy, energy-conservation, pollution-free, has replaced rapidly other traditional drying technology as solar thermal utilization one important branch, becomes at present one of primary study project both at home and abroad.Solar energy drying is human use's solar energy a kind of form generally with the longest history, most widely used, and solar energy drying is to replace conventional energy resource to carry out the process of heat medium with solar energy.
The solar energy drying system relating to is at present mostly open system, imports and exports onrelevant, and the using waste heat from tail gas after drying medium is not used and directly discharge; Some drying system is designed to enclosed drying system, although now the waste heat of tail gas is recycled, but reenter and in the tail gas of system, contain a large amount of steam and EGR is done perfectly not to the dehumidifying of this portion gas, therefore the efficiency of whole dry run can not make moderate progress.
Summary of the invention
The purpose of this utility model is to have proposed a kind of solar energy drying system, and this drying system can be recycled the part of waste heat of getting rid of from drying box, thereby can improve the thermal efficiency of solar energy drying system.
The utility model completes by the following technical programs: a kind of back-heating type solar energy drying system, comprises trough type solar heat-collector, heat transfer pipe, heat medium pump, heat storage can, heat exchanger, air blast and ventilation shaft; The outlet of air blast is connected with the entrance of the zone of heat liberation of heat exchanger, and the outlet of the zone of heat liberation of heat exchanger is connected with the entrance of drying box; The endothermic tube of trough type solar heat-collector, heat storage can, heat medium pump and heat exchanger zone of heat liberation coil pipe are connected in series by heat transfer pipe, it is characterized in that: be provided with a regenerator with heat exchange effect, the entrance of the zone of heat liberation of this regenerator connects the waste gas outlet of drying box, and the outlet of the cold fluid pass of regenerator connects the entrance of air blast.Like this, the Cryogenic air of the regenerator cold fluid pass of flowing through heats the higher dry waste gas of temperature of the regenerator zone of heat liberation of being flowed through, will be lower and be discharged into airborne dry waste gas temperature, thus improved the thermal efficiency of cycle of drying system.
The beneficial effects of the utility model are: utilize cold air to carry out heat exchange with tail gas in bootstrap system, before the heat exchanger that arrives drying system, reach a higher temperature, reduce to a certain extent the load of groove type solar light-condensing and heat-collecting device, improve the efficiency of whole drying system.
Accompanying drawing explanation
The structural principle schematic diagram of Fig. 1 the utility model embodiment.
Fig. 2 is a kind of internal structure schematic diagram of the utility model regenerator.
In figure, 1. trough type solar heat-collector, 2. endothermic tube, 3a, 3b, 3c, 3d. heat transfer pipe, 4. heat exchanger, 5. heat exchanger zone of heat liberation coil pipe, 6. heat medium pump, 7. heat storage can, 8. drying box, 9. regenerator, 10. ventilation shaft, 11. air blasts, 12. hot fluid shuntings, 13. thermofins.
The specific embodiment
In the embodiment shown in Fig. 1 and Fig. 2, endothermic tube (2) in trough type solar heat-collector (1), the heat exchanger zone of heat liberation coil pipe (5) in heat exchanger (4), heat medium pump (6) and heat storage can (7) are by heat transfer pipe (3a, 3b, 3c, 3d) serial connection.The entrance of the zone of heat liberation of regenerator (9) connects the waste gas outlet of drying box (8), the outlet of the cold fluid pass of regenerator (9) connects the entrance of air blast (11), the outlet of air blast (11) is connected with the entrance of the zone of heat liberation coil pipe (5) of heat exchanger (4), and the outlet of the cold fluid pass of heat exchanger (4) is connected with the entrance of drying box (8).Cold air through ventilation shaft (10) can fully contact the heat exchange efficiency that reaches maximum with the thermofin (13) on heat passage in regenerator (9), and now cold air will enter drying box (8) by air blast (11) with a higher temperature.Zone of heat liberation in regenerator (9) is the structure that the hot fluid shunting (12) by the circular tube shaped of a plurality of band thermofins (13) forms, and thermofin (13) is metal or the alloy composition that heat transfer coefficient is higher.
Claims (1)
1. a back-heating type solar energy drying system, comprises trough type solar heat-collector, heat transfer pipe, heat medium pump, heat storage can, heat exchanger, air blast and ventilation shaft; The outlet of air blast is connected with the entrance of the zone of heat liberation of heat exchanger, and the outlet of the zone of heat liberation of heat exchanger is connected with the entrance of drying box; The endothermic tube of trough type solar heat-collector, heat storage can, heat medium pump and heat exchanger zone of heat liberation coil pipe are connected in series by heat transfer pipe, it is characterized in that: be provided with a regenerator with heat exchange effect, the entrance of the zone of heat liberation of this regenerator connects the waste gas outlet of drying box, and the outlet of the cold fluid pass of regenerator connects the entrance of air blast.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201320617517.6U CN203518515U (en) | 2013-10-09 | 2013-10-09 | Heat recovery type solar drying system |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201320617517.6U CN203518515U (en) | 2013-10-09 | 2013-10-09 | Heat recovery type solar drying system |
Publications (1)
Publication Number | Publication Date |
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CN203518515U true CN203518515U (en) | 2014-04-02 |
Family
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Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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CN201320617517.6U Expired - Fee Related CN203518515U (en) | 2013-10-09 | 2013-10-09 | Heat recovery type solar drying system |
Country Status (1)
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CN (1) | CN203518515U (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN104351368A (en) * | 2014-11-14 | 2015-02-18 | 三江县陆氏茶叶机械制造有限公司 | Tea blowing device |
CN104567282A (en) * | 2014-12-31 | 2015-04-29 | 伯恩太阳能科技有限公司 | Intelligent multifunctional drying room |
CN110030742A (en) * | 2019-04-18 | 2019-07-19 | 金昌鸿远建材加工有限责任公司 | A kind of solar energy thermal conductance drying tower |
-
2013
- 2013-10-09 CN CN201320617517.6U patent/CN203518515U/en not_active Expired - Fee Related
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN104351368A (en) * | 2014-11-14 | 2015-02-18 | 三江县陆氏茶叶机械制造有限公司 | Tea blowing device |
CN104567282A (en) * | 2014-12-31 | 2015-04-29 | 伯恩太阳能科技有限公司 | Intelligent multifunctional drying room |
CN104567282B (en) * | 2014-12-31 | 2017-04-19 | 伯恩太阳能科技有限公司 | Intelligent multifunctional drying room |
CN110030742A (en) * | 2019-04-18 | 2019-07-19 | 金昌鸿远建材加工有限责任公司 | A kind of solar energy thermal conductance drying tower |
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Legal Events
Date | Code | Title | Description |
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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: 20140402 Termination date: 20141009 |
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EXPY | Termination of patent right or utility model |