CN201740352U - Tunnel-type drying device - Google Patents

Tunnel-type drying device Download PDF

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Publication number
CN201740352U
CN201740352U CN2010202981127U CN201020298112U CN201740352U CN 201740352 U CN201740352 U CN 201740352U CN 2010202981127 U CN2010202981127 U CN 2010202981127U CN 201020298112 U CN201020298112 U CN 201020298112U CN 201740352 U CN201740352 U CN 201740352U
Authority
CN
China
Prior art keywords
tail gas
type drying
hot air
exhaust gas
tunnel
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
Application number
CN2010202981127U
Other languages
Chinese (zh)
Inventor
胡明辅
李斌
颜永明
杨春曦
刘辉
王伟民
马福华
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
YUNNAN NENGGONG SOLAR ENERGY ENGINEERING Co Ltd
Kunming University of Science and Technology
Original Assignee
YUNNAN NENGGONG SOLAR ENERGY ENGINEERING Co Ltd
Kunming University of Science and Technology
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by YUNNAN NENGGONG SOLAR ENERGY ENGINEERING Co Ltd, Kunming University of Science and Technology filed Critical YUNNAN NENGGONG SOLAR ENERGY ENGINEERING Co Ltd
Priority to CN2010202981127U priority Critical patent/CN201740352U/en
Application granted granted Critical
Publication of CN201740352U publication Critical patent/CN201740352U/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Abstract

The utility model relates to a tunnel-type drying device which comprises a tunnel-type drying cabinet (9), hot air circulating fans (6 and 12), hot air circulating pipes (4 and 14), hot air heaters (5 and 13), hot air heating temperature sensors (8 and 11), a fresh air inlet (16), a material carrying device (18), an exhaust gas fan (1), an exhaust gas pipe (24), a controller (21) and the like, and is characterized in that the exhaust gas pipe is provided with a humidity sensor (27); the outlet end of the exhaust gas fan is provided with an exhaust gas return pipe (23) which reaches the tunnel-type drying cabinet and an exhaust gas inlet pipe (28) which reaches the feeding end of the drying cabinet; and the gas flowing speed, temperature distribution, humidity distribution, exhaust gas humidity and the like in the drying cabinet can be controlled and regulated, thereby facilitating the creation of quite appropriate environment conditions for drying materials, and minimizing the energy consumption.

Description

A kind of tunnel passage type drying device
Technical field
The utility model relates to a kind of tunnel passage type drying device, belongs to using energy source and field of energy-saving technology.
Background technology
The tunnel passage type drying device adopts the pneumatic conveying drying mode, is usually used in dry natural rubber, tealeaves, melon and fruit, vegetables, medicinal material, grain etc., is a kind of drying device commonly used.Present tunnel passage type drying device, temperature and humidity for exhaust emissions is not controlled basically, for the design of the flow and the air circulation of exhaust emissions, mainly consider to make that the hot blast that flows through material has certain flow velocity, so that promote mass transfer and heat transfer between thermal current and the material.Given this, for for the purpose of holding, often select the blower fan of big flow, and the flow of blower fan is unadjustable in the design.So, cause that the tail gas exhaust air rate is bigger than normal, exhaust steam moisture is on the low side, meaningless consumption a large amount of energy, reduced rate of energy.In addition,, also strengthened the power consumption of blower fan, caused power consumption higher because the blower fan model is bigger than normal.
Summary of the invention
The purpose of this utility model is in order to overcome the deficiencies in the prior art, and providing a kind of can significantly cut down the consumption of energy, and improves the tunnel passage type drying device of energy utilization rate.
The technical solution of the utility model is: comprise compositions such as tunnel passage type drying cupboard, hot air circulation blower, hot air circulation airduct, storage heater, hot blast heating-up temperature sensor, fresh inlet, material carrying device, tail gas exhaust blower, tail gas exhaust duct, controller, it is characterized in that humidity sensor being set at the tail gas exhaust duct, the tail gas backwind tube is set to the tunnel passage type drying cupboard at the tail gas exhaust blower port of export, the tail gas blast pipe is set to the drying cupboard feed end.
At exhaust pipe and tail gas backwind tube control valve is set respectively, variable-frequency governor is set respectively at tail gas exhaust blower and hot air circulation blower.The material carrying device enters from an end of tunnel passage type drying cupboard (calling drying cupboard in the following text), and heat transfer, effect of mass transmitting by thermal current in drying cupboard are finished dry run, and the other end of self-desiccation cabinet is released.The purpose of this dry device is with less power consumption and thermal energy consumption, keeps air-flow distribution, Temperature Distribution and moisture distribution suitable in the drying cupboard.System is in service, by the rotating speed that the control valve and the variable-frequency governor of adjusting tail gas exhaust duct are regulated the tail gas exhaust blower, the capacity of control tail gas, the humidity of tail gas is controlled in certain scope, be tail gas humidity hour, reduce the capacity of tail gas, otherwise increase the capacity of tail gas; By the rotating speed that the control valve and the variable-frequency governor of adjusting tail gas backwind tube are regulated air exhauster, the air circulation of control tail gas; By the temperature sensor monitors return air temperature, adopt variable-frequency governor, by regulating the rotational speed regulation air circulation of hot air circulation blower, return air temperature is remained in the suitable scope.
Description of drawings
Fig. 1 is the utility model structural representation.
The specific embodiment
The utility model is described in further detail below in conjunction with the accompanying drawing illustrated embodiment.
Embodiment be one be used for natural rubber the tunnel passage type drying device, by known tunnel passage type drying cupboard 9, hot air circulation blower 6,12, hot air circulation airduct 4,14, storage heater 5,13, hot blast heating-up temperature sensor 8,11, fresh inlet 16, material carrying device 18, tail gas exhaust blower 1, tail gas exhaust duct 24, controller 21 compositions such as grade, at the tail gas exhaust duct temperature sensor 26 is set in addition, humidity sensor 27, the place is provided with temperature sensor 3 at the hot air circulation return air inlet, 15, tail gas backwind tube 23 is set to drying cupboard at the tail gas exhaust blower port of export, at exhaust pipe and tail gas backwind tube control valve 25 is set respectively, 22, at tail gas exhaust blower and hot air circulation blower variable-frequency governor 2 is set respectively, 7,11.The material carrying device is a materials vehicle 18 in the present embodiment, and track 17 is set matches with it, the exhaust emissions end that materials vehicle loads natural rubber self-desiccation cabinet enters, heat transfer, effect of mass transmitting by thermal current in drying cupboard are finished dry run, and the other end of self-desiccation cabinet (fresh inlet end) is released.The formation of this dry device, its purpose are with less power consumption and thermal energy consumption, keep air-flow distribution, Temperature Distribution and moisture distribution suitable in the drying cupboard, and its operating parameter can be regulated as required and control.
System is in service, and the tail gas of discharge is taken away a large amount of heats, thereby the capacity of control tail gas and the controlled factor that exhaust steam moisture is the system energy consumption index.Theoretically, capacity is more little, and energy resource consumption is low more, and the relative humidity that its least limit capacity is a tail gas reaches 100%.Among the embodiment relative humidity of tail gas is controlled in 70%~85% scope.By the control valve 25 of adjusting tail gas exhaust duct and the rotating speed of variable-frequency governor 2 adjusting tail gas exhaust blowers 1, the capacity of control tail gas is controlled at the humidity of tail gas in the scope of setting, and promptly tail gas humidity hour, reduce the capacity of tail gas, otherwise increase the capacity of tail gas.
Capacity by control tail gas, making the drying cupboard afterbody pass material bed hot air flow reduces, be unfavorable for hot blast and material bed between heat and mass, therefore tail gas backwind tube 23 and control valve 22 thereof are set, make its part tail gas reuse, pass material bed hot air flow so that strengthen the drying cupboard afterbody, promote hot blast and material bed between heat and mass.
Temperature sensor 26 is set, in order to the delivery temperature of monitoring tail gas, for the operation of regulating and control drying device provides reference on the tail gas exhaust duct.
Be provided with two groups of storage heaters 5,13 among the embodiment at the middle part of drying cupboard.Its objective is and in drying cupboard, import heat, promote gas to pass material bed flowing simultaneously, promote its heat and mass.Therefore, air circulation reaches as above that two purposes get final product, and excessively increases its power consumption then meaninglessly.Temperature sensor 8,10 monitoring heating-up temperatures are set, in 110 ℃~120 ℃ scopes, too high or too low for temperature heating and temperature control, regulate by electrically heated input power; Temperature sensor 3,15 monitoring return air temperatures are set, return air temperature is controlled in 90 ℃~100 ℃ scopes, and temperature is low excessively, can increase rotation speed of fan by variable-frequency governor 7,11, otherwise the reduction rotation speed of fan, but minimum can not the making of rotation speed of fan passed material bed hot blast flow velocity and is lower than 1.5m/s.
Among the embodiment, fresh air enters and passes material bed from the discharging one end air inlet 16 of drying cupboard, on the one hand material is cooled off, and is convenient to subsequent packages; On the other hand heat is reclaimed the new wind of preheating, help energy-conservation.New wind enters and is divided into two parts, and a part of inner passage by drying cupboard enters one group of hot air circulation heating system and heats; Another part enters another group hot air circulation heating system by fresh wind tube 20 and heats.Control valve is set on fresh wind tube, is used to regulate the ratio of the new wind of two parts.
The material carrying device is " car-track " carrying mode in the present embodiment, can be used for " chain-sprocket wheel " carrying mode in addition.

Claims (4)

1. tunnel passage type drying device, comprise tunnel passage type drying cupboard (9), hot air circulation blower (6,12), hot air circulation airduct (4,14), storage heater (5,13), hot blast heating-up temperature sensor (8,11), fresh inlet (16), material carrying device (18), tail gas exhaust blower (1), tail gas exhaust duct (24), controller compositions such as (21), it is characterized in that humidity sensor (27) being set at the tail gas exhaust duct, tail gas backwind tube (23) is set to the tunnel passage type drying cupboard at the tail gas exhaust blower port of export, tail gas blast pipe (28) is set to the drying cupboard feed end.
2. tunnel passage type drying device according to claim 1 is characterized in that being provided with control valve (25) on the tail gas exhaust duct, at tail gas exhaust blower (1) variable-frequency governor (2) is set.
3. tunnel passage type drying device according to claim 1 is characterized in that being provided with control valve (22) on the tail gas backwind tube.
4. tunnel passage type drying device according to claim 1 is characterized in that hot air circulation blower (6,12) is provided with variable-frequency governor (7,11), temperature sensor (3,15) is set looping back air port place.
CN2010202981127U 2010-08-20 2010-08-20 Tunnel-type drying device Expired - Fee Related CN201740352U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN2010202981127U CN201740352U (en) 2010-08-20 2010-08-20 Tunnel-type drying device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN2010202981127U CN201740352U (en) 2010-08-20 2010-08-20 Tunnel-type drying device

Publications (1)

Publication Number Publication Date
CN201740352U true CN201740352U (en) 2011-02-09

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Family Applications (1)

Application Number Title Priority Date Filing Date
CN2010202981127U Expired - Fee Related CN201740352U (en) 2010-08-20 2010-08-20 Tunnel-type drying device

Country Status (1)

Country Link
CN (1) CN201740352U (en)

Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102778113A (en) * 2012-07-30 2012-11-14 浙江大学 Surface dehydration device after cleaning of root hair traditional Chinese medicinal materials
CN102901329A (en) * 2012-10-27 2013-01-30 广西大圆机械设备有限责任公司 Wood chip drying device
CN103547874A (en) * 2011-04-15 2014-01-29 伊利诺斯工具制品有限公司 Dryer
CN103575086A (en) * 2012-08-10 2014-02-12 农业部规划设计研究院 Intelligent type straw fuel direct-discharge grain drying machine
CN105478315A (en) * 2015-12-30 2016-04-13 浙江明泉工业涂装有限公司 Air supply mechanism for coating line combined drying tunnel
CN105521931A (en) * 2015-12-30 2016-04-27 浙江明泉工业涂装有限公司 Combined drying tunnel for coating line
CN110342776A (en) * 2019-08-19 2019-10-18 王学智 A method of the reduction sludge at low temperature energy consumption for drying based on air draft humidity
CN111397346A (en) * 2020-03-30 2020-07-10 巨石集团有限公司 Energy-saving tunnel oven
CN112284112A (en) * 2020-11-21 2021-01-29 浙江衣拿智能科技股份有限公司 Dryer with heat energy recycling function

Cited By (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103547874A (en) * 2011-04-15 2014-01-29 伊利诺斯工具制品有限公司 Dryer
CN102778113A (en) * 2012-07-30 2012-11-14 浙江大学 Surface dehydration device after cleaning of root hair traditional Chinese medicinal materials
CN103575086A (en) * 2012-08-10 2014-02-12 农业部规划设计研究院 Intelligent type straw fuel direct-discharge grain drying machine
CN102901329A (en) * 2012-10-27 2013-01-30 广西大圆机械设备有限责任公司 Wood chip drying device
CN102901329B (en) * 2012-10-27 2015-10-14 广西大圆机械设备有限责任公司 Wood chip drying unit
CN105478315A (en) * 2015-12-30 2016-04-13 浙江明泉工业涂装有限公司 Air supply mechanism for coating line combined drying tunnel
CN105521931A (en) * 2015-12-30 2016-04-27 浙江明泉工业涂装有限公司 Combined drying tunnel for coating line
CN110342776A (en) * 2019-08-19 2019-10-18 王学智 A method of the reduction sludge at low temperature energy consumption for drying based on air draft humidity
CN111397346A (en) * 2020-03-30 2020-07-10 巨石集团有限公司 Energy-saving tunnel oven
CN112284112A (en) * 2020-11-21 2021-01-29 浙江衣拿智能科技股份有限公司 Dryer with heat energy recycling function

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C14 Grant of patent or utility model
GR01 Patent grant
C17 Cessation of patent right
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20110209

Termination date: 20130820