CN107997202A - Four sections of thermal cycle kelp drying units - Google Patents
Four sections of thermal cycle kelp drying units Download PDFInfo
- Publication number
- CN107997202A CN107997202A CN201711313002.6A CN201711313002A CN107997202A CN 107997202 A CN107997202 A CN 107997202A CN 201711313002 A CN201711313002 A CN 201711313002A CN 107997202 A CN107997202 A CN 107997202A
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- CN
- China
- Prior art keywords
- drying
- air
- kelp
- heat
- gas
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- 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.)
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Classifications
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- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23N—MACHINES OR APPARATUS FOR TREATING HARVESTED FRUIT, VEGETABLES OR FLOWER BULBS IN BULK, NOT OTHERWISE PROVIDED FOR; PEELING VEGETABLES OR FRUIT IN BULK; APPARATUS FOR PREPARING ANIMAL FEEDING- STUFFS
- A23N12/00—Machines for cleaning, blanching, drying or roasting fruits or vegetables, e.g. coffee, cocoa, nuts
- A23N12/08—Machines for cleaning, blanching, drying or roasting fruits or vegetables, e.g. coffee, cocoa, nuts for drying or roasting
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23N—MACHINES OR APPARATUS FOR TREATING HARVESTED FRUIT, VEGETABLES OR FLOWER BULBS IN BULK, NOT OTHERWISE PROVIDED FOR; PEELING VEGETABLES OR FRUIT IN BULK; APPARATUS FOR PREPARING ANIMAL FEEDING- STUFFS
- A23N12/00—Machines for cleaning, blanching, drying or roasting fruits or vegetables, e.g. coffee, cocoa, nuts
- A23N12/08—Machines for cleaning, blanching, drying or roasting fruits or vegetables, e.g. coffee, cocoa, nuts for drying or roasting
- A23N12/12—Auxiliary devices for roasting machines
- A23N12/125—Accessories or details
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- Life Sciences & Earth Sciences (AREA)
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Food Science & Technology (AREA)
- Polymers & Plastics (AREA)
- Drying Of Solid Materials (AREA)
Abstract
Four sections of thermal cycle kelp drying unit heat sources are combustion gas, and the heat that fuel gas buring produces in two ways dries kelp particle, are heat radiation drying and heated-air drying respectively.Heated-air drying is divided into three, is waste heat drying materials, the drying of heat radiation return air, gas hot-air drying respectively.Radiative oven dry is Gas Infrared heating plate, and by infrared radiation heating steel plate, material in heat radiation drying box is dried.
Description
Technical field
The present invention relates to thermal cycle drying technology, and in particular to the application of a main laminaria drying unit, belongs to thermal energy ladder
Utilize field.
Background technology
Kelp particle is dried, and commonly used boiler heats air, using hot air kelp particle, by the water in particle
Point evaporated, thermal energy among hot wind just discharges it only by once utilizing, and hot-air humidity increases on a small quantity, but simultaneously
Not up to saturation, the drying of hot wind blow-through are the significant wastages to the energy.
The content of the invention
Four sections of thermal cycle kelp drying unit heat sources are combustion gas, and the heat that fuel gas buring produces is in two ways to kelp
Grain is dried, and is heat radiation drying and heated-air drying respectively.Heated-air drying is divided into three, is waste heat drying materials, heat respectively
Radiate return air drying, gas hot-air drying.Radiative oven dry is Gas Infrared heating plate, by infrared radiation heating steel plate, to heat
Material is dried in radiant drying case.
Combustion gas produce heat in different humidity with being utilized under temperature conditionss, using the heat finally discharged to sea
Band material is preheated, and the kelp after preheating is sent into level-one return air drying chamber by carrier chain and carries out secondary drying, after drying
Hot wind is once heated to entering the combustion-supporting air of fuel chamber, makes the air themperature higher into fuel chamber, improves combustion gas combustion
Temperature is burnt, by gas infrared radiation plate heating radiation drying chamber, the kelp particle on carrier chain is dried three times, is dried
Being used containing water gas as level-one return air drying chamber hot wind afterwards, the high-temperature discharge gas in fuel gas buring room is by filtering, note
Enter to gas hot-air drying chamber, gas emission gas temperature is high, for still containing amount of heat after drying, then is changed by air
Hot device, reheating is carried out to entering the indoor air that burns.
It is of the invention to be for technical scheme applied to solve the technical problem:
1st, four sections of thermal cycle kelp drying units are divided into hot-air seasoning, and two parts are dried with radiant heat, need to pass through kelp
Pre-heating drying, micro humid air hot-air seasoning, radiant heat drying, gas emission hot air seasoning, four-stage is handled, to heat
Circulation ladder can be carried out to utilize.
2nd, using the hot gas of front and rear hot air drying box twice, after being heated to air, still possess certain temperature, pass through this portion
Hot wind is divided to preheat raw material, as one section of drying.
3rd, heat radiation drying baker is when carrying out radiative oven dry, and the vapor contained in inner air and not up to saturation, are
Drying effect is improved, it is necessary to this partial air be extracted out, the air containing a large amount of thermal energy, the kelp for just entering device is carried out
Two sections of drying.
4th, heat radiation drying baker is converted for combustion gas by infrared radiation panel, makes the more targeted release of heat, is heated
Drying baker, gas-fired infrared radiative oven dry are the 3rd section of drying.
5th, the exhaust gas produced after fuel gas buring be high temperature, low humidity, be pipelined to filter, it is right after impurity screening
Kelp particle carries out the 4th section of hot-air seasoning.
6th, gas emission gas is filtered, avoid burning caused by dust kelp particle is polluted.
7th, heat radiation heating can concentrate heat, improve combustion gas directly acting on to drying object, reduce scattering and disappearing for heat.
The beneficial effects of the invention are as follows:
1st, make heat obtain circulation ladder to utilize, reduce gas consumption.
2nd, pair the air with combustion gas mixing heats, and improves ignition temperature.
Brief description of the drawings
Fig. 1 is the front view of embodiment;
In figure:1. kelp carrier chain entrance, 2. level-one return air drying bakers, 3. heat radiation drying bakers, the drying of 4. gas hot-airs
Case, 5. gas hot-air filters, 6. wind turbine, 3,7. wind turbine, 2,8. wind turbine, 1,9. secondary air heat exchanger, the heat exchange of 10. main airs
Device, the pre- heat channel of 11. kelps, 12. combustion gas, 13. gas-fired infrared radiant panels, 14. radiative oven dry case heating plates, 15. air intakes,
16. hot air inlet, 17. heat radiation drying baker discharge pipes, the hot discharge pipe of 18. combustion gas, 19. main air exchanger heat air hoses,
20. secondary air exchanger heat air hose, the outlet of 21. two level hot air heat exchangers, the outlet of 22. level-one hot air heat exchangers, 23. enter material list
Xiang Men, the outlet of 24. kelp carrier chains.
Embodiment
Embodiment:
Level-one return air drying baker 2 is connected with 3 front end of heat radiation drying baker, and 3 end of heat radiation drying baker is dried with gas hot-air
Dry case 4 is connected, and all drying baker inlet and outlet all install pan feeding unilateral gate 23.Kelp particle need to pass through the pre- heat channel 11 of kelp and carry out one
Section drying.Kelp particle is sent into level-one return air drying baker 2 by kelp carrier chain entrance 1 and carries out two sections of drying.It is defeated by kelp
Send chain that the kelp particle by two sections of drying is sent into heat radiation drying baker 3 and carry out three sections of drying, the kelp after three sections of drying
Grain, gas hot-air drying baker 4 is sent into by kelp carrier chain, carries out four sections of drying, and the kelp particle after drying is defeated by kelp
Chain outlet 24 is sent to send out.
Wind turbine 1 delivers air to, hot air inlet 16, with combustion gas 12, carries out mixed combustion, passes through gas-fired infrared spoke
Plate is penetrated, flame thermal energy is converted into infra-red radiation, to radiative oven dry case heating plate 14, is heated, heat is conducted to heat radiation
In drying baker 3, dry kelp carrier chain on kelp particle, hot-air mixed with vapor after by heat radiation drying baker outlet air
Pipe 17, is sent into level-one return air drying baker 2, carries out hot-air seasoning to the kelp particle on kelp carrier chain, using wind turbine 3, will dry
Hot gas after dry kelp, by main air exchanger heat air hose 19, is sent into main air heat exchanger 10, to air intake 15,
The air of entrance exchanges heat, and lifts air themperature.
High-temp waste gas after the burning of gas-fired infrared radiant panel 13, by the hot discharge pipe 18 of combustion gas, is transported to gas hot-air
Among filter 5, high-temp waste gas is filtered, the high-temperature gas after filtering enters gas hot-air drying baker 4, and kelp is carried out
Four sections of drying, for the combustion gas exhaust gas after drying, by wind turbine 2, are sent into secondary air heat exchanger 9, to being changed by main air
Hot device 10, the air of heating, carries out secondary heating, hot from level-one with secondary air heat exchanger 9 from main air heat exchanger 10
Wind heat exchanger exit 22, with two level hot air heat exchanger outlet 21, the low temperature hot gas of discharge, kelp is dried for the pre- heat channel 11 of kelp
Particle.
Claims (2)
1. four sections of thermal cycle kelp drying units, described device is by the heat that combustion gas produces under different humidity and temperature conditionss
Kelp particle is dried, it is characterised in that:Four sections of thermal cycle kelp drying units are divided into hot-air seasoning, are dried with radiant heat
Two parts, need to dry, gas emission hot air seasoning, four by the pre-heating drying, micro humid air hot-air seasoning, radiant heat of kelp
A stage is handled, and circulation ladder is carried out to thermal energy and is utilized.Using the hot gas of front and rear hot air drying box twice, air is heated
Afterwards, still possess certain temperature, raw material is preheated by this part hot wind, as one section of drying.
2. four sections of thermal cycles kelp drying unit according to claim 1, it is characterised in that:Heat radiation drying baker is carrying out
During radiative oven dry, the vapor that contains in inner air and not up to saturation, to improve drying effect, it is necessary to by this partial air
Extraction, the air containing a large amount of thermal energy, two sections of drying are carried out to the kelp for just entering device.Heat radiation drying baker leads to for combustion gas
Infrared radiation panel conversion is crossed, makes the more targeted release of heat, heating, drying case, gas-fired infrared radiative oven dry is the 3rd
Section drying.The exhaust gas produced after fuel gas buring is high temperature, low humidity, is pipelined to filter, after impurity screening, to kelp
Particle carries out the 4th section of hot-air seasoning.Gas emission gas is filtered, the caused dust that avoids burning is to kelp particle
Pollute.Heat radiation heating can concentrate heat, improve combustion gas directly acting on to drying object, reduce scattering and disappearing for heat.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201711313002.6A CN107997202A (en) | 2017-12-12 | 2017-12-12 | Four sections of thermal cycle kelp drying units |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201711313002.6A CN107997202A (en) | 2017-12-12 | 2017-12-12 | Four sections of thermal cycle kelp drying units |
Publications (1)
Publication Number | Publication Date |
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CN107997202A true CN107997202A (en) | 2018-05-08 |
Family
ID=62058117
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CN201711313002.6A Pending CN107997202A (en) | 2017-12-12 | 2017-12-12 | Four sections of thermal cycle kelp drying units |
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Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN109883047A (en) * | 2019-02-28 | 2019-06-14 | 昆山市瑞浦鑫涂装机械有限公司 | A kind of natural gas infra-red radiation combines heating device with hot air circulation |
CN112056605A (en) * | 2020-08-12 | 2020-12-11 | 同济大学 | Energy-efficient type tobacco drying system |
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EP1018306A1 (en) * | 1998-12-28 | 2000-07-12 | Kibbutz Lotan Technology Center Ltd., Kibbutz Lotan, D.N. Chevel Eilot | Machine for prolonging the shelf-life of vegetables and fruits |
CN103919249A (en) * | 2014-04-30 | 2014-07-16 | 潍坊华和食品有限公司 | Fruit and vegetable dryer |
CN104596222A (en) * | 2015-02-02 | 2015-05-06 | 吉首大学 | Heat exchanging type tail heat recycling and microwave oxygen-separating drying machine |
CN204438714U (en) * | 2015-02-02 | 2015-07-01 | 吉首大学 | Heat exchange type tail recuperation of heat microwave oxygen barrier drying machine |
CN204519269U (en) * | 2015-04-08 | 2015-08-05 | 黄红梅 | A kind of high-efficiency environment friendly Chinese chestnut dryer |
CN105546966A (en) * | 2015-12-31 | 2016-05-04 | 中国科学院理化技术研究所 | Continuous heat pump drying system for dry fruits |
CN205228065U (en) * | 2015-11-11 | 2016-05-11 | 叶昌演 | Multi -functional flowing water drying -machine |
CN205316922U (en) * | 2015-12-31 | 2016-06-15 | 温州星贝机械科技有限公司 | Drying machine |
CN106036952A (en) * | 2016-07-09 | 2016-10-26 | 陕西国防工业职业技术学院 | Fully automatic kelp drying and conveying device |
CN206196927U (en) * | 2016-08-17 | 2017-05-31 | 陈涵 | A kind of new sea sedge dryer |
CN206687128U (en) * | 2017-03-30 | 2017-12-01 | 济宁学院 | Vegetable drying device |
-
2017
- 2017-12-12 CN CN201711313002.6A patent/CN107997202A/en active Pending
Patent Citations (11)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP1018306A1 (en) * | 1998-12-28 | 2000-07-12 | Kibbutz Lotan Technology Center Ltd., Kibbutz Lotan, D.N. Chevel Eilot | Machine for prolonging the shelf-life of vegetables and fruits |
CN103919249A (en) * | 2014-04-30 | 2014-07-16 | 潍坊华和食品有限公司 | Fruit and vegetable dryer |
CN104596222A (en) * | 2015-02-02 | 2015-05-06 | 吉首大学 | Heat exchanging type tail heat recycling and microwave oxygen-separating drying machine |
CN204438714U (en) * | 2015-02-02 | 2015-07-01 | 吉首大学 | Heat exchange type tail recuperation of heat microwave oxygen barrier drying machine |
CN204519269U (en) * | 2015-04-08 | 2015-08-05 | 黄红梅 | A kind of high-efficiency environment friendly Chinese chestnut dryer |
CN205228065U (en) * | 2015-11-11 | 2016-05-11 | 叶昌演 | Multi -functional flowing water drying -machine |
CN105546966A (en) * | 2015-12-31 | 2016-05-04 | 中国科学院理化技术研究所 | Continuous heat pump drying system for dry fruits |
CN205316922U (en) * | 2015-12-31 | 2016-06-15 | 温州星贝机械科技有限公司 | Drying machine |
CN106036952A (en) * | 2016-07-09 | 2016-10-26 | 陕西国防工业职业技术学院 | Fully automatic kelp drying and conveying device |
CN206196927U (en) * | 2016-08-17 | 2017-05-31 | 陈涵 | A kind of new sea sedge dryer |
CN206687128U (en) * | 2017-03-30 | 2017-12-01 | 济宁学院 | Vegetable drying device |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN109883047A (en) * | 2019-02-28 | 2019-06-14 | 昆山市瑞浦鑫涂装机械有限公司 | A kind of natural gas infra-red radiation combines heating device with hot air circulation |
CN112056605A (en) * | 2020-08-12 | 2020-12-11 | 同济大学 | Energy-efficient type tobacco drying system |
CN112056605B (en) * | 2020-08-12 | 2021-10-08 | 同济大学 | Energy-efficient type tobacco drying system |
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Application publication date: 20180508 |
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