CN106123557A - Phase-change energy-storage solar exsiccator in pipe - Google Patents
Phase-change energy-storage solar exsiccator in pipe Download PDFInfo
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- CN106123557A CN106123557A CN201610150379.3A CN201610150379A CN106123557A CN 106123557 A CN106123557 A CN 106123557A CN 201610150379 A CN201610150379 A CN 201610150379A CN 106123557 A CN106123557 A CN 106123557A
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- Prior art keywords
- exsiccator
- pipe
- solar
- vacuum heat
- heat collection
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Classifications
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B21/00—Arrangements or duct systems, e.g. in combination with pallet boxes, for supplying and controlling air or gases for drying solid materials or objects
- F26B21/06—Controlling, e.g. regulating, parameters of gas supply
- F26B21/08—Humidity
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24S—SOLAR HEAT COLLECTORS; SOLAR HEAT SYSTEMS
- F24S10/00—Solar heat collectors using working fluids
- F24S10/40—Solar heat collectors using working fluids in absorbing elements surrounded by transparent enclosures, e.g. evacuated solar collectors
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24S—SOLAR HEAT COLLECTORS; SOLAR HEAT SYSTEMS
- F24S10/00—Solar heat collectors using working fluids
- F24S10/90—Solar heat collectors using working fluids using internal thermosiphonic circulation
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24S—SOLAR HEAT COLLECTORS; SOLAR HEAT SYSTEMS
- F24S23/00—Arrangements for concentrating solar-rays for solar heat collectors
- F24S23/70—Arrangements for concentrating solar-rays for solar heat collectors with reflectors
- F24S23/77—Arrangements for concentrating solar-rays for solar heat collectors with reflectors with flat reflective plates
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24S—SOLAR HEAT COLLECTORS; SOLAR HEAT SYSTEMS
- F24S60/00—Arrangements for storing heat collected by solar heat collectors
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24S—SOLAR HEAT COLLECTORS; SOLAR HEAT SYSTEMS
- F24S70/00—Details of absorbing elements
- F24S70/20—Details of absorbing elements characterised by absorbing coatings; characterised by surface treatment for increasing absorption
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B21/00—Arrangements or duct systems, e.g. in combination with pallet boxes, for supplying and controlling air or gases for drying solid materials or objects
- F26B21/06—Controlling, e.g. regulating, parameters of gas supply
- F26B21/10—Temperature; Pressure
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B21/00—Arrangements or duct systems, e.g. in combination with pallet boxes, for supplying and controlling air or gases for drying solid materials or objects
- F26B21/06—Controlling, e.g. regulating, parameters of gas supply
- F26B21/12—Velocity of flow; Quantity of flow, e.g. by varying fan speed, by modifying cross flow area
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B25/00—Details of general application not covered by group F26B21/00 or F26B23/00
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B2200/00—Drying processes and machines for solid materials characterised by the specific requirements of the drying good
- F26B2200/06—Grains, e.g. cereals, wheat, rice, corn
-
- 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
-
- 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
- Y02P60/00—Technologies relating to agriculture, livestock or agroalimentary industries
- Y02P60/80—Food processing, e.g. use of renewable energies or variable speed drives in handling, conveying or stacking
- Y02P60/85—Food storage or conservation, e.g. cooling or drying
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Life Sciences & Earth Sciences (AREA)
- Sustainable Development (AREA)
- Sustainable Energy (AREA)
- Thermal Sciences (AREA)
- Chemical & Material Sciences (AREA)
- Combustion & Propulsion (AREA)
- Drying Of Solid Materials (AREA)
Abstract
The present invention relates to solar dryer, particularly relate to phase-change energy-storage solar exsiccator in a kind of pipe, belong to Solar use, energy storage technology and technical field of drying.Vacuum heat collection pipe of the present invention is obliquely installed, and thermal-collecting tube uses bimetallic tube, is provided with energy storage phase change material in inner tube, and outer wall of inner tube has plated film absorbed layer, and Super-conductive conduit one end is placed in vacuum heat collection pipe through inner tube sealing-plug, is provided with O-ring seal between inner tube and the outer tube mouth of pipe；The Super-conductive conduit other end is placed in drying baker housing, Super-conductive conduit fin fixed plate fix.The present invention utilizes vacuum heat collection pipe thermal-arrest and energy storage, secondary reflecting strengthens solar energy utilization ratio, and utilize hot superconduction finned tube one-way transmission heat cyclic drying air, integrated exhaust gas waste heat recovery preheats new wind, and integrated small chamber dryer designs, and has Integrated Energy efficiency high, baking temperature is constant, good reliability, the feature such as full automation control, can be widely used for rural residence houses grain, seed, fruit and vegerable, agricultural byproducts, meat, the drying and dewatering of Chinese herbal medicine preserve.
Description
Technical field
The present invention relates to solar dryer, particularly relate to phase-change energy-storage solar exsiccator in a kind of pipe, belong to too
Sun can utilize, energy storage technology and technical field of drying.
Technical background
Solar drying technology is the drying and dehydrating technology that solar utilization technique combines with drying process monotechnics.
Solar utilization technique, than traditional dry technology, is introduced dry run by this technology, be applied to herbage, grain, seed, in
The dry run such as mongolian medicine, food, had both saved the energy, had protected again environment, be particularly suitable for remote, energy scarcity is regional.This dry
The material that dry technology is obtained has many advantages: sensation quality better, material maintains the intrinsic color and luster of fresh feed, local flavor substantially
And fragrance.Nutritional labeling is high, and owing to dry run is carried out under conditions of can reach constant temperature, this makes nutrient component damages pole
Few.Dehydration is thoroughly, lightweight, is suitable for preserving for a long time and transporting for long-distance.
Phase early 1990s, China just takes to the exploitation of solar drying technology and the manufacture of equipment, and nearly three
Over 5 years, the agricultural product industry development such as herbage, grain is very fast, existing tens of production lines, but production scale is the least, from state
Inside and outside market demand situation is seen, the development prospect of the solar drying technology of China is the most wide.
For a long time, during gathering in the crops and preparing Radix Glycyrrhizae, prepared by forage grass field curing technique always China's Radix Glycyrrhizae
Main process.In green fodder harvesting season, the chance of continuous fine a couple of days is little, therefore many areas because of forage grass wet tide in harvesting season many
Rain, the high quality grass such as Herba Medicaginis can not be prepared as Radix Glycyrrhizae in good time, causes forage grass dry loss during field curing serious and battalion
Form code insurance holdup low.According to relevant department of the Ministry of Agriculture add up, China every year lose storage grass about at 300,000,000 tons, grass drying is
Becoming the bottlenecks of preparation high-quality Radix Glycyrrhizae, the research and development of advanced forage drying plant are extremely the most urgent.At present, domestic
Artificial drying herbage equipment mainly has drum-type grass drier, 93QH series fire coal mow-drying unit, 93QH series to be dried
Unit, 93QH1000 type fuel oil (gas) mow-drying unit, all use fuel oil, fire coal and combustion gas as main energy sources, therefore do
The high expensive of dry rear herbage, industrialization is relatively difficult, and economic benefit is inconspicuous.
Solar energy is a kind of cleaning, efficiently and the new forms of energy of never exhaustion.At present, national governments are all by solar energy resources profit
It is used as the important content of National Sustainable Development Strategies.Solar dryer meets the development of low-carbon economy, be continuable,
Energy-saving and emission-reduction product, is the opportunity of solar energy industry development.Solar energy industry is huge, and market development has the latentest
Power.Government supported the development of solar energy industry energetically in recent years, within 2009, had put into effect a series of policies for Solar use,
Build a resource-conserving and environment-friendly society, strengthen the requirement of the capability of sustainable development.The prospect of solar energy industry is bright
, but road is tortuous.Specific to each enterprise, owing to technology, product and the level etc. of each enterprise differ, so,
The bright other shore of industry can be arrived and depend on the comprehensive strength of enterprise.At present, China's solar dryer industry industry development
Lack of standardization, enterprise's self-disciplining is more weak.But the development of solar energy industry will return rationality, enterprise need to more focus on product
The lifting of quality.
Summary of the invention
It is an object of the invention to provide one and utilize regenerative resource--solar energy is as drying source, empty to dry medium heat
Gas is circulated heating, uses waste-heat recovery device that the waste heat of hot-air is carried out secondary utilization simultaneously, solves energy sources,
Ambient pressure and the problem in Solar use cycle, improve the efficient directly-heated box-type solar exsiccator of energy utilization rate.
The present invention is accomplished by:
The present invention includes vacuum heat collection pipe, drying baker housing, Super-conductive conduit, and vacuum heat collection pipe is obliquely installed, and thermal-collecting tube uses double
Layer pipe, has working medium, is provided with energy storage phase change material in inner tube in bimetallic tube interlayer, outer wall of inner tube has plated film absorbed layer, Super-conductive conduit
One end is placed in vacuum heat collection pipe through inner tube sealing-plug, is provided with O-ring seal between inner tube and the outer tube mouth of pipe；Super-conductive conduit is another
One end is placed in drying baker housing, Super-conductive conduit fin fixed plate fix.
Described vacuum heat collection pipe is placed on collector bracket, is provided with conduit saddle, vacuum heat collection pipe 1 bottom bottom collector bracket
It is placed on conduit saddle.
It is provided with reflector below described collector bracket.
Described drying baker housing forward end face is provided with double door, and inwall is provided with drying baker insulation material, drying baker housing
Middle part is provided with at least one of which exsiccator material frame, and exsiccator material frame is provided with anti-material spilling net, and exsiccator material frame is with dry
It is provided with gas flow between dry tank shell；It is provided with heat exchanger below exsiccator material frame, is positioned at the drying baker at heat exchanger
Housing wall is provided with shutter net, is fumer below heat exchanger, and aerofluxus tank wall is provided with blower fan.
The innovative point of the present invention:
The advanced volume drying equipment of the most fully utilized solar energy, device integrated level is high, and compact conformation, floor space is little, completely
Utilizing solar energy to carry out drying materials dehydration, dry rate is fast, and Energy Efficiency Ratio is high, easy to use, and automaticity is high, applies model
Enclose the widest.
2. solar energy heating and dry run Integral design, pioneering vacuum heat collection pipe+hot superconduction finned tube thermal-arrest and secondary
Reflective concurrent heating technology, the total heat utilization efficiency of solar energy improves to more than 80%.
3. initiating phase-change accumulation energy in vacuum heat collection pipe pipe, balance solar energy changes over temperature and the heat flow ripple of generation
Dynamic, control heat output, it is achieved within 24 hours, continuous process is dried.
4. integrated cross-current type exhaust-heat exchanger in drying box, reclaims and gets rid of heat in damp and hot waste gas, pre-for new wind
Heat, device Energy Efficiency Ratio significantly improves.Heat exchanger
5. Multifunctional design drying box, designs multilayers bin, both can use drawer type body feed tank, it would however also be possible to employ draw and insert-type
Material disc, input and output material is convenient；Cold-hot flow passage warming plate is isolated, and saves space, and air-flow is unimpeded；Bottom design gas collection fumer and leading
Stream plate, it is simple to waste gas is discharged and condensed moisture is from discharge.
6. use the fin Super-conductive conduit that cryogenic property is good, unidirectional heat transfer, condensation segment enhanced fin heat transfer and increase heat transfer
Area, not only solar energy organic efficiency is high, and dry air is heated by the fin of double-flow, and heat exchanger effectiveness is high.
7. device climate adaptability is good, and autumn and winter summer in winter hold concurrently and can use, even if the winter of-40 DEG C, it is possible to normally work.
8. utilizing Super-conductive conduit thermal-arrest and transmission, thermal resistance is little, direct drying air, and baking temperature is high, can be at 50-
Being dried operation between 150 DEG C, this is that conventional solar energy drying does not reaches completely.
9. it is automatically adjusted baking temperature, it is achieved freeze-day with constant temperature process.Drying device control design case uses PWM to control blower fan stream
Amount, compressor flow is according to setting baking temperature regulation.
10. utilize blower fan to carry out forced convertion, improve dry rate.
Accompanying drawing explanation
Fig. 1 is apparatus of the present invention-I type front views；
Fig. 2 is apparatus of the present invention-I type rearviews；
Fig. 3 is apparatus of the present invention-I type side views；
Fig. 4 is apparatus of the present invention-I type top views；
Fig. 5 is apparatus of the present invention-I type profile figures；
Fig. 6 is apparatus of the present invention-II type front views；
Fig. 7 is apparatus of the present invention-II type rearviews；
Fig. 8 is apparatus of the present invention-II type side views；
Fig. 9 is apparatus of the present invention-II type top views；
Figure 10 is apparatus of the present invention-II type profile figures.
It is embodied as case
The present invention is mainly by solar heat collection, energy storage part, drying materials case part, Waste Heat Recovery part, air circulation delivery section
Divide and automatically control part composition.
Solar heat collection, energy storage part, major function is to utilize solar energy to provide drier heat source, design to take hot superconduction
Thermal-arrest and secondary reflecting technology, improve Solar use efficiency；Filling phase-changing energy storage material in vacuum tube, regulation solar energy is at any time
Between change the temperature of generation and heat flow fluctuation.This part includes: vacuum heat collection pipe 1, phase-changing energy storage material 2, Super-conductive conduit 3,
Conduit saddle 4, vacuum tube sealing-plug 5, reflector 19 and mounting bracket 18.
Drying materials case part, major function contains and is oven-dried material, and charging and discharging are convenient, it is possible within a short period of time
Uniformly material drying, it is ensured that the quality of product.Design double door multilayer dose inserts disc carrier, cold-hot wind heat insulation runner heat preservation and dryness
The advantages such as box structure, has compact conformation, and heat loss is little, is suitable for material flexible, uniform drying, and speed is fast, material easy access.
This system includes: drying baker housing 10, inside thermal conservation material 9, dried object bin 11, exsiccator double door 12, fresh inlet BAIYE
Window net 15, fumer 16.
Waste Heat Recovery part, major function is to reclaim the higher heat discharged in waste gas of water capacity for preheating entrance exsiccator
Fresh air, improve device entirety efficiency of energy utilization.This system by cross-flow waste heat exchanger 14, anti-material spilling net 13 with
And seal structural part composition.Cross-flow exchanger 14 may be designed to vertical tube type, horizontal tube, the efficiently exchanger such as board-like.
Air circulation transport portion, major function is to attract fresh dried air to enter exsiccator, hands over through Waste Heat Recovery
After parallel operation preheating, pass through Super-conductive conduit radiating fin and be heated temperature rising, contacted with material by material bed, water in material
Divide and evaporate into dry air, after Waste Heat Recovery exchanger preheats new wind, discharge through blower fan 17.
Automatically controlling part, major function is regulation air circulation, controls to dry temperature, humidity and drying time.Blower fan
Air quantity is according to the setting value controlling to dry temperature, regulates blower fan incoming frequency by converter thus regulates air circulation.
The operation principle of apparatus of the present invention is, when solar irradiation is mapped on vacuum heat collection pipe 1, and the plating in thermal-collecting tube inner tube
Film absorbed layer absorbs solar radiation, and is converted into heat energy, and heat energy constant temperature is stored in phase-change material.When Super-conductive conduit 3 dissipates
During the quantity of heat given up of hot junction, in Super-conductive conduit, working fluid absorbs heat of vaporization and becomes gas phase, and gas working medium is in pipe in gas phase channel
Under the effect of pressure differential, flow to the other end, and condense in heat release herein.The heat discharged is flowed through by fins conduct heating
Air.The liquid condensed returns heat pipe evaporator section under the effect of capillary force and continues heat absorption evaporation, so goes round and begins again, thus real
The high efficiency of transmission of existing heat.
Invention device-I collecting system is not provided with reflector, and invention device-II collecting system arranges reflector 19, through true
The sunlight of empty set heat pipe 1 and inject the sunlight of reflector from device front window, is reflected and is reflected, being got to vacuum heat-collecting from the back side
On pipe 1, dramatically increase the heat-collecting capacity of unit are.
Outdoor fresh air is aspirated by blower fan 17, is entered the Waste Heat Recovery exchanger 14 of exsiccator by shutter net 15,
Indirectly carrying out heat exchange with the damp and hot waste gas through material bed discharge, fresh air is preheated, and damp and hot EGT reduces, water
Vapor portion condenses.The fresh air being preheated, through isolation runner, passes upward through the fin radiating end 8 of Super-conductive conduit, is added
Heat is to design temperature, through material bed 20 material dryings.The damp and hot waste gas discharged flows through Waste Heat Recovery exchanger 14, with fresh sky
Gas carries out indirect heat exchange, preheats entrance fresh air.Waste gas after heat exchange, discharges drying device through blower fan 17,
The baking temperature of exsiccator is regulated by air quantity.
The present invention, with solar energy as thermal source, utilizes vacuum heat collection pipe thermal-arrest and energy storage, and secondary reflecting strengthens Solar use
Rate, and utilize hot superconduction finned tube one-way transmission heat cyclic drying air, the integrated exhaust gas waste heat recovery new wind of preheating, one
Body small-sized box type exsiccator designs, compact conformation, and floor space is little, and outward appearance is neat, and material easy access has Integrated Energy
Efficiency is high, and the features such as baking temperature is constant, good reliability, full automation control can be widely used for rural residence houses grain, kind
Son, fruit and vegerable, agricultural byproducts, meat, the drying and dewatering of Chinese herbal medicine preserve.The present invention is directed to the farming of the vast rural residence houses of China
The advanced technology solution that the drying and dewaterings such as thing, agricultural byproducts, seed, livestock products, Chinese herbal medicine propose.Invention device uses
Regenerative resource--solar energy, as drying source, is circulated heating to dry medium heat air, uses waste heat recovery simultaneously
Device carries out secondary utilization to the waste heat of hot-air, system solves the problem energy sources problem, ambient pressure problem, solar energy profit
With periodic problem and improve energy utilization rate.
Small-sized agricultural byproducts exsiccator
Device designs:
Solar energy heating: φ 58x1800 or φ 58x1800 vacuum heat-collecting-hot superconduction finned tube 18；
Bringing-up section fin: φ 56x650, material: aluminium alloy；
Reflector: 1500x1000mm, 2 pieces；
Drying baker: 1500x650x1650mm
Drying frame: 4 layers, rustless steel, base plate 100 mesh stainless steel mesh；
Energy storage material: BT-XB80 chlorinated paraffin energy storage material, phase transition temperature: 80oC, quality: 18x2.0 kg；
Energy storage capacity: 7.0-14.0 MJ
System fan: 254 × 90,2；
Waste gas afterheat recovery unit: 2 vertical tube cross-flow tube sheet exchangers, A=4m2；
Exsiccator production capacity: 180-200kg/ days (water separation capability)；
Dry materials temperature: 50-80oC；
The exhaust waste heat response rate: 80%；
Exsiccator maximum operation (service) temperature: 120 DEG C；
Use ambient temperature :-40 DEG C-+40 DEG C.
Claims (4)
1. phase-change energy-storage solar exsiccator in pipe, including vacuum heat collection pipe (1), drying baker housing (10), Super-conductive conduit (3),
It is characterized in that, vacuum heat collection pipe (1) is obliquely installed, and vacuum heat collection pipe (1) uses bimetallic tube, has working medium in bimetallic tube interlayer,
Being provided with energy storage phase change material (2) in vacuum heat collection pipe (1) inner tube, outer wall of inner tube has plated film absorbed layer, Super-conductive conduit (3) one end
In being placed in vacuum heat collection pipe (1) through inner tube sealing-plug (5), between inner tube and the outer tube mouth of pipe, it is provided with O-ring seal (6)；Hot superconduction
Pipe (3) other end is placed in drying baker housing (10), Super-conductive conduit fin fixed plate (7) fix.
Phase-change energy-storage solar exsiccator in pipe the most according to claim 1, it is characterised in that vacuum heat collection pipe (1) is put
On collector bracket (18), collector bracket (18) bottom is provided with conduit saddle (4), and vacuum heat collection pipe (1) bottom is placed in conduit saddle (4)
On.
Efficient directly-heated box-type solar exsiccator the most according to claim 1 and 2, it is characterised in that collector bracket
(18) lower section is provided with reflector (19).
Phase-change energy-storage solar exsiccator in pipe the most according to claim 1, it is characterised in that drying baker housing (10) is front
End face is provided with double door (12), and inwall is provided with drying baker insulation material (9), and drying baker housing (10) middle part is provided with at least one
Layer exsiccator material frame (11), exsiccator material frame (11) is provided with anti-material spilling net (13), exsiccator material frame (11) with
Drying baker housing is provided with gas flow between (10)；Exsiccator material frame (11) lower section is provided with heat exchanger (14), is positioned at heat friendship
Drying baker housing (10) wall at parallel operation (14) place is provided with shutter net (15), and heat exchanger (14) lower section is fumer (16),
Fumer (16) wall is provided with blower fan (17).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610150379.3A CN106123557A (en) | 2016-03-16 | 2016-03-16 | Phase-change energy-storage solar exsiccator in pipe |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610150379.3A CN106123557A (en) | 2016-03-16 | 2016-03-16 | Phase-change energy-storage solar exsiccator in pipe |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN106123557A true CN106123557A (en) | 2016-11-16 |
Family
ID=57270325
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201610150379.3A Pending CN106123557A (en) | 2016-03-16 | 2016-03-16 | Phase-change energy-storage solar exsiccator in pipe |
Country Status (1)
| Country | Link |
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| CN (1) | CN106123557A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108753264A (en) * | 2018-07-16 | 2018-11-06 | 东南大学 | Phase change energy-storage type solar dryer and its phase-change accumulation energy layer preparation method |
| WO2019220359A1 (en) * | 2018-05-16 | 2019-11-21 | JAIN, Samit | Pcm integrated solar dryer |
Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE2836526A1 (en) * | 1977-09-09 | 1979-03-22 | Fiat Spa | DRYING DEVICE OPERATING WITH SOLAR ENERGY, IN PARTICULAR FOR DRYING AGRICULTURAL PRODUCTS |
| CN2589891Y (en) * | 2002-12-18 | 2003-12-03 | 张爱军 | Horizontal hot tube type wall hanging solar water heater |
| CN201569253U (en) * | 2009-12-29 | 2010-09-01 | 北京林业大学 | Moveable solar energy drying device |
| CN102072617A (en) * | 2010-12-15 | 2011-05-25 | 内蒙古科技大学 | Solar dryer |
| CN202254392U (en) * | 2011-09-19 | 2012-05-30 | 昆明理工大学 | Vacuum pipe solar thermal collector with thermal storage function |
| CN204027034U (en) * | 2014-06-30 | 2014-12-17 | 广东都灵新能源科技有限公司 | A kind of solar air heater with superconducting pipe |
| CN205607119U (en) * | 2016-03-16 | 2016-09-28 | 内蒙古博特科技有限责任公司 | Intraductal phase change energy storage solar drying ware |
-
2016
- 2016-03-16 CN CN201610150379.3A patent/CN106123557A/en active Pending
Patent Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE2836526A1 (en) * | 1977-09-09 | 1979-03-22 | Fiat Spa | DRYING DEVICE OPERATING WITH SOLAR ENERGY, IN PARTICULAR FOR DRYING AGRICULTURAL PRODUCTS |
| CN2589891Y (en) * | 2002-12-18 | 2003-12-03 | 张爱军 | Horizontal hot tube type wall hanging solar water heater |
| CN201569253U (en) * | 2009-12-29 | 2010-09-01 | 北京林业大学 | Moveable solar energy drying device |
| CN102072617A (en) * | 2010-12-15 | 2011-05-25 | 内蒙古科技大学 | Solar dryer |
| CN202254392U (en) * | 2011-09-19 | 2012-05-30 | 昆明理工大学 | Vacuum pipe solar thermal collector with thermal storage function |
| CN204027034U (en) * | 2014-06-30 | 2014-12-17 | 广东都灵新能源科技有限公司 | A kind of solar air heater with superconducting pipe |
| CN205607119U (en) * | 2016-03-16 | 2016-09-28 | 内蒙古博特科技有限责任公司 | Intraductal phase change energy storage solar drying ware |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2019220359A1 (en) * | 2018-05-16 | 2019-11-21 | JAIN, Samit | Pcm integrated solar dryer |
| CN108753264A (en) * | 2018-07-16 | 2018-11-06 | 东南大学 | Phase change energy-storage type solar dryer and its phase-change accumulation energy layer preparation method |
| CN108753264B (en) * | 2018-07-16 | 2024-04-05 | 东南大学 | Phase-change energy-storage type solar dryer and preparation method of phase-change energy-storage layer thereof |
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Application publication date: 20161116 |