CN104000299A - Tobacco roller far infrared composite dying experimental equipment - Google Patents
Tobacco roller far infrared composite dying experimental equipment Download PDFInfo
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- CN104000299A CN104000299A CN201410275016.3A CN201410275016A CN104000299A CN 104000299 A CN104000299 A CN 104000299A CN 201410275016 A CN201410275016 A CN 201410275016A CN 104000299 A CN104000299 A CN 104000299A
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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
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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
- Y02P70/50—Manufacturing or production processes characterised by the final manufactured product
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Abstract
Provided is tobacco roller far infrared composite dying experimental equipment. The tobacco roller far infrared composite dying experimental equipment is characterized by comprising a horizontal roller, a hot air conveying system connected with the roller and a far infrared heating device arranged in an inner cavity of the roller. The hot air conveying system comprises an air source, an air preheater, a steam generator, a heat exchanger and an air conveying pipeline communicated with the inner cavity of the roller, and the air source, the air preheater, the steam generator, the heat exchanger and the air conveying pipeline are connected in sequence. A material opening is formed in the rear end wall of the roller, and a moisture discharge pipe is arranged. According to the experimental equipment, roller wall heat conduction heating, hot air convection heating and far infrared radiation heating in traditional cut tobacco roller drying are combined. A plurality of heating modes are combined, the cut tobacco can be dried fast at low roller wall temperature, and products with even moisture and the good filling effect are obtained. The roller wall temperatures and far infrared radiation strength of different roller drying stages are controlled according to different raw materials and different product targets, and then differentiation production and fine production are achieved.
Description
technical field
The present invention relates to the tobacco shreds drying equipment in tobacco process process, especially a tobacco drum far infrared composite drying experimental facilities, the composite drying equipment that specifically utilizes barrel, hot blast, Far infrared heating plate that heat conduction, convection heat transfer' heat-transfer by convection, radiant heat transfer multiple heating mode are combined.And can adopt heat stepwise segmentation control technology to realize the processing that becomes more meticulous in tobacco shreds drying process.
Background technology
Being dried in tobacco processing is very important operation, and different drying equipments, different drying means physical characteristic, organoleptic attribute, the chemical composition on tobacco has the impact of highly significant.At present, tobacco shreds drying mainly contain pneumatic conveying drying and two kinds of forms of roller drying.Pneumatic conveying drying mainly relies on the mode of convection heat transfer' heat-transfer by convection to be dried pipe tobacco, and cut tobacco is added in drying tube continuously, in the course of conveying of hot and humid gas, makes pipe tobacco slough moisture.The product filling value that the feature of pneumatic conveying drying is that the thermal efficiency is high, drying time is short, treating capacity is large, obtain is higher, but the water uniformity of pneumatic conveying drying product is poor, fragrance matter loss is larger.Drum drying equipment is realized the dry of pipe tobacco by heat conduction between the convection heat transfer' heat-transfer by convection between hot blast and pipe tobacco, cylinder wall and pipe tobacco.The harmony of the product index of roller drying is better, but product filling value is relatively low.
Still can not solve following problem completely for existing drum drying equipment.First, tobacco shreds drying product filling value and pipe tobacco are protected the contradiction between perfume (or spice).Secondly, the lifting of rate of drying and energy utilization rate in roller drying process.Finally, the space that drum drying equipment carries out differentiation production, diversification control according to the difference of the difference of raw material, product objective is less.
Along with the development of dry technology, some novel dry technologies are applied gradually in the industry such as food, chemical industry.Novel drying equipment also more and more trends towards adopting the composite drying mode of multiple heating mode use.For example traditional mode of heating and Far-infrared Heating mode are combined, due to Far-infrared Heating have quick rising temperature of charge improve rate of drying, homogeneous heating, heat conversion higher, there is the advantages such as certain penetrability, probably solve some problems that exist in traditional pipe tobacco dry run in conjunction with the mode of heating of existing roller drying.
Summary of the invention
In order to overcome above-mentioned the deficiencies in the prior art, the invention provides a kind of pipe tobacco cylinder far infrared composite drying experimental facilities.This experimental facilities can combine barrel heat conduction heating, hot air convection heating in traditional pipe tobacco roller drying with Heated by Far-Infrared Radiation.Can meet pipe tobacco rapid draing at lower barrel temperature by the combination of multiple heating mode, obtain the good product of moisture uniform filling effect.And by the modularization of barrel heater, Far infrared heating plate being installed and controlling, can realize barrel temperature and the far infrared radiation intensity of controlling the different roller drying stage according to raw material difference, product objective difference, and then realize differentiation and produce the production that becomes more meticulous.
The object of the invention is to realize by following technical measures:
A kind of tobacco drum far infrared composite drying experimental facilities, comprise by actuating unit and drive the horizontal drum that is provided with central shaft, the hot air delivery system being connected with cylinder of rotation and be arranged on the far infrared heater in drum cavity, on cylinder barrel, be provided with successively zone of heating and heat-insulation layer, on drum cavity wall, be installed with material flight, described hot air delivery system comprises source of the gas, gas preheater, steam generator, the heat exchanger connecting successively and passes into the gas pipeline of drum cavity; Described far infrared heater is the semicircle heating panel that adopts ceramic Far infrared radiant panel composition, and the radiant power of heating panel is adjustable, offers material mouth and be provided with humidity discharging pipe on the aft bulkhead of cylinder.
Gas preheater and steam generator are arranged in hot air delivery system with parallel way, are connected respectively with source of the gas with heat exchanger.
Described far infrared heater is to adopt the semicircle heating of ceramic Far infrared radiant panel composition panel, installs along cylinder axial direction.According to the direction of drum rotating, because the tipping effect material of material flight mainly tends to direction of rotation one side, semicircle Far infrared heating plate is arranged on central shaft by support as the position of 30 ° taking axial angle, central shaft is fixed on cylinder two ends and does not rotate with cylinder, can effectively improve radiation heating efficiency, the radiant power of heating panel is by the control of Far-infrared Heating controller.Simultaneously can be according to processing needs, the radiant power of radiant panel can programme-control, regulates, thereby adopt different heating powers to be dried at different drying stages within the scope of 0-5KW.
In steam generator exit, air preheater exit, heat exchanger exit place be separately installed with wireless humiture sensor, so that control the output humiture of relevant device
Zone of heating on cylinder barrel is that the heating tube by being laid on barrel heats, and heating tube can be along drum shaft to step-by-step arrangement, and in zone of heating, is laid with radio temperature sensor, and by PID controller, barrel temperature is implemented to control.
The cross section of material flight is pyrometric cone structure, drift angle is 90 °, this particular design of material flight can effectively increase heat exchange area, strength imparting material stirring action, the flight structure of triangular form makes material in rollers roll process, can reduce material and sheds height simultaneously, reduce material make broken, improve utilization of materials.。
Described actuating unit is variable-frequency motor, can realize drum rotation speed is adjusted in 0-20rpm.
Described cylinder is fixed on chassis overhang, carrys out the rotating speed of index drum by controlling motor speed, realizes drum rotation speed and regulates within the scope of 0-20rpm.The material mouth that the aft bulkhead of cylinder is offered, can realize the reinforced and discharging to material, and can carry out feeding to material at different drying stages, facilitates experimental study.Material mouth is made up of lucite, conveniently experimentation is observed.
According to the difference of requirement of experiment, the hot blast entering in cylinder can have two kinds, and one is over dry hot blast, and another kind is the hot blast of certain moisture content.In the time of needs over dry hot blast, gas is directly entered in heat exchanger gas is heated by gas preheater.Regulate the temperature of over dry hot blast by the power of controller control heat exchanger.In the time of the hot blast of the certain moisture content of needs, can set respectively to control by gas flow control device and enter the gas flow in steam generating device and enter the gas flow of air preheater, by regulate different tolerance by gas speed control in cylinder built in 0-0.5m/s scope.Gas after gas and the air preheater preheating that steam generator is produced passes into heat exchanger heating after mixing, gas temperature can regulate as required within the scope of 0-200 DEG C.Gas after heating is delivered to cylinder entrance by pipeline, enters cylinder inside by swivel joint, after material is heated, finally discharges by the humidity discharging pipe being arranged on the swivel joint of cylinder rear end.
Experimental rig provided by the invention has three kinds of different complex heat transfer back tender operation modes, comprises radiation-convection current complex heat transfer, radiation-convection current-conduction complex heat transfer and convection current-conduction complex heat transfer, and its course of work is as follows respectively:
1, under radiation-convection current complex heat transfer mode of operation, the barrel heating system of experimental rig is closed, and the flow of dry-heat air, temperature, humidity are pressed to predetermined experimental condition setting; After hot blast is in stable condition, open far-infrared heater by setting radiant power, the quantitative pipe tobacco that modulates moisture is put into cylinder, open cylindrical shell rotational drive motor by the drum rotation speed of setting simultaneously, start timing dry; In dry run, to pipe tobacco sampling in cylinder, can carry out analyzing and testing by the timing of material mouth to the physical qualities such as moisture, temperature, tobacco structure and aesthetic quality.
2,, under radiation-convection current-conduction complex heat transfer mode of operation, the flow of barrel temperature and dry-heat air, temperature, humidity are pressed to predetermined experimental condition setting; Until barrel temperature and hot blast in stable condition after, open far-infrared heater by setting radiant power, the quantitative pipe tobacco that modulates moisture is put into cylinder, open cylindrical shell rotational drive motor by the drum rotation speed of setting simultaneously, start timing dry, can be to pipe tobacco timing sampling analyzing and testing physical quality and aesthetic quality in dry run.
3, under convection current-conduction complex heat transfer mode of operation, far-infrared heater cuts out, the flow of barrel temperature and dry-heat air, temperature, humidity are pressed to predetermined experimental condition setting; Until barrel temperature and hot blast in stable condition after, the quantitative pipe tobacco that modulates moisture is put into cylinder, open cylindrical shell rotational drive motor by the drum rotation speed of setting simultaneously, start timing dry, can be to pipe tobacco timing sampling analyzing and testing physical quality and aesthetic quality in dry run.
Tool of the present invention has the following advantages:
1, the present invention combines Heated by Far-Infrared Radiation in drum apparatus with heat conduction, convection heat transfer' heat-transfer by convection mode, because Heated by Far-Infrared Radiation mode regulates and controls response rapidly, and material is had to certain penetrability, compared with traditional single conduction heating and Convective Heating roller drying device, this device is conducive to improve tobacco shreds drying quality uniformity.
2, apparatus of the present invention possess the drying test function of different heat transfer complex method, can be for different dried feed, specific aim is carried out the drying property research under the different cooked modes such as radiation-convection current complex heat transfer, radiation-convection current-conduction complex heat transfer and convection current-conduction complex heat transfer.
3, in drum apparatus of the present invention, the system heating parameter of radiation, convection current, three kinds of basic diabatic processes of conduction is all adjustable flexibly, and in dry run, pipe tobacco sampling is convenient, is conducive to form the drying test study condition of wide region.
Brief description of the drawings
Fig. 1 is: equipment principle schematic diagram.
Fig. 2 is: equipment schematic cross-section.
Fig. 3 is: far-infrared heater structural representation.
In figure, mark: 1-cylinder, 2-cylinder heat-insulation layer, 3-zone of heating, 4-drum cavity chamber wall, 5-material flight, 6, 25-swivel joint, 7-humidity discharging pipe, 8-material mouth, 9-motor, 10-rotating idler, 11-drive system controller, 12-Far-infrared Heating controller, 13-hot-air system controller, 14-barrel heating controller, 15, 16-gas flowmeter, 17-steam generator, 18-gas preheater, 19, 20, 22-wireless humiture sensor, 21-heat exchanger, 23-radio temperature sensor, 24-central shaft, 26-far infrared heater, 27-pottery Far infrared radiant panel, 28-cylinder support carrying roller, 29-cylinder bearing.
Detailed description of the invention
The present invention further describes below in conjunction with accompanying drawing:
As shown in Figure 1: a kind of tobacco drum far infrared composite drying experimental facilities, comprise by variable-frequency motor 9 drive the horizontal drum that is provided with central shaft 24 1 of rotation, the hot air delivery system that is connected with cylinder and be arranged on the far infrared heater in drum cavity, on cylinder barrel, be provided with successively zone of heating 3 and heat-insulation layer 2, on drum cavity chamber wall 4, be installed with material flight 5, described hot air delivery system comprises source of the gas, gas preheater 18, steam generator 17, the heat exchanger 21 connecting successively and passes into the gas pipeline of drum cavity; The semicircle heating panel that described far infrared heater 26 forms for adopting ceramic Far infrared radiant panel 27, and the radiant power of heating panel is adjustable, offers material mouth and be provided with humidity discharging pipe 7 on the aft bulkhead of cylinder.
Gas preheater 18 is arranged in hot air delivery system with parallel way with steam generator 17, is connected respectively with source of the gas with heat exchanger 21.
Described far infrared heater is to adopt the semicircle heating of ceramic Far infrared radiant panel composition panel, installs along cylinder axial direction.According to the direction of drum rotating, because the tipping effect material of material flight mainly tends to direction of rotation one side, semicircle Far infrared heating plate is arranged on central shaft on (referring to Fig. 2) as the position of 30 ° by support taking axial angle, can effectively improve radiation heating efficiency, the radiant power of heating panel is controlled by Far-infrared Heating controller 12.Simultaneously can be according to processing needs, the radiant power of radiant panel can programme-control, regulates, thereby adopt different heating powers to be dried at different drying stages within the scope of 0-5KW.
In steam generator exit, air preheater exit, heat exchanger exit place be separately installed with wireless humiture sensor 19,20,22, so that control the output humiture of relevant device
Zone of heating on cylinder barrel is that the heating tube by being laid on barrel heats, and heating tube can be along drum shaft to step-by-step arrangement, and in zone of heating, is laid with radio temperature sensor 23, and by PID controller 14, barrel temperature is implemented to control.
The cross section of material flight is pyrometric cone structure, drift angle is 90 °, this particular design of material flight can effectively increase heat exchange area, strength imparting material stirring action, the flight structure of triangular form makes material in rollers roll process, can reduce material and sheds height simultaneously, reduce material make broken, improve utilization of materials.
Described cylinder is fixed on chassis overhang, carrys out the rotating speed of index drum by controlling motor speed, realizes drum rotation speed and regulates within the scope of 0-20rpm.The material mouth 8 that the aft bulkhead of cylinder is offered, can realize the reinforced and discharging to material, and can carry out feeding to material at different drying stages, facilitates experimental study.Material mouth is made up of lucite, conveniently experimentation is observed.
Operation principle of the present invention is as follows: cylinder 1 drives and complete preheating by motor 9, sets barrel temperature by barrel heating controller 14, after the temperature after temperature sensor 23 feedbacks reaches setting value, completes preheating.Need to set by Far-infrared Heating controller 12 power of first infrared hot plate 26 according to processing.Enter in steam generator 17 and the flow of gas preheater 18 interior gases by setting, and the temperature of steam generator 17 insulating box water, make to enter hot blast in cylinder 1 and reach the temperature and humidity of technological requirement.Cut tobacco water balance after chopping, to technological requirement value, is joined in cylinder 1 and is dried by material mouth 8, pass through material mouth 8 feedings according to requirement of experiment in different time sections.
The course of work of hot air delivery system is described below by reference to the accompanying drawings:
As shown in Figure 1, hot air heating system is in the time of needs over dry hot blast, and gas directly enters in gas preheater 18 by flowmeter 16, is entered in heat exchanger 21 gas is further heated by the gas of preheating.The swivel joint 25 that the hot blast producing connects by air inlet pipe enters in cylinder 1, can regulate the power of heat exchanger 21 and then the temperature that adjusting enters the interior over dry hot blast of cylinder 1 by hot-air system controller 13 simultaneously.In the time need to entering hot blast in cylinder and there is certain humidity, first the constant temperature water tank water of steam generator 17 is set in to certain temperature, after gas is by steam generator 17, the gas of generation will carry a certain amount of moisture.Another group gas makes gas through preliminary preheating by air preheater 18, after preventing from mixing with steam, condensation occurs.Mixed gas, by heat exchanger 21, further heats up gas.Regulate the heating power of heat exchanger 21 by the data after hot-air system controller 13 and gas temperature humidity wireless senser (19,20,22) feedback, make to enter hot blast in cylinder 1 and remain on the temperature and humidity of setting.
Gas after heating is delivered to cylinder entrance by pipeline, enters cylinder 1 inside by swivel joint 25, after material is heated, finally discharges by the humidity discharging pipe 7 being arranged on cylinder rear end swivel joint 6.
Claims (8)
1. a tobacco drum far infrared composite drying experimental facilities, it is characterized in that: comprise by actuating unit and drive the horizontal drum that is provided with central shaft, the hot air delivery system being connected with cylinder of rotation and be arranged on the far infrared heater in drum cavity, on cylinder barrel, be provided with successively zone of heating and heat-insulation layer, on drum cavity wall, be installed with material flight, described hot air delivery system comprises source of the gas, gas preheater, steam generator, the heat exchanger connecting successively and passes into the gas pipeline of drum cavity; Described far infrared heater is the semicircle heating panel that adopts ceramic Far infrared radiant panel composition, and the radiant power of heating panel is adjustable, offers material mouth and be provided with humidity discharging pipe on the aft bulkhead of cylinder.
2. tobacco drum far infrared composite drying experimental facilities according to claim 1, is characterized in that: gas preheater and steam generator are arranged in hot air delivery system with parallel way, is connected respectively with source of the gas with heat exchanger.
3. tobacco drum far infrared composite drying experimental facilities according to claim 1, is characterized in that: semicircle heating panel is arranged on central shaft by support as the position of 30 ° taking axial angle.
4. tobacco drum far infrared composite drying experimental facilities according to claim 1, is characterized in that: in steam generator exit, air preheater exit, heat exchanger exit place be separately installed with wireless humiture sensor.
5. tobacco drum far infrared composite drying experimental facilities according to claim 1, is characterized in that: the radiant power of heating panel is by the control of Far-infrared Heating controller.
6. tobacco drum far infrared composite drying experimental facilities according to claim 1, it is characterized in that: the zone of heating on cylinder barrel is that the heating tube by being laid on barrel heats, heating tube can be along drum shaft to step-by-step arrangement, and in zone of heating, be laid with radio temperature sensor, and by PID controller, barrel temperature implemented to control.
7. tobacco drum far infrared composite drying experimental facilities according to claim 1, is characterized in that: the cross section of material flight is pyrometric cone structure, and drift angle is 90 °.
8. tobacco drum far infrared composite drying experimental facilities according to claim 1, is characterized in that: described actuating unit is variable-frequency motor, can realize drum rotation speed is adjusted in 0-20rpm.
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| CN201410275016.3A CN104000299B (en) | 2014-06-19 | 2014-06-19 | Tobacco drum far infrared composite drying experimental facilities |
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| CN201410275016.3A CN104000299B (en) | 2014-06-19 | 2014-06-19 | Tobacco drum far infrared composite drying experimental facilities |
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Cited By (24)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104643281A (en) * | 2015-01-25 | 2015-05-27 | 中国烟草总公司黑龙江省公司牡丹江烟草科学研究所 | Tobacco baking room |
| CN104930832A (en) * | 2015-06-25 | 2015-09-23 | 湖北叶威(集团)智能科技有限公司 | Double-drum crop dryer |
| CN105686041A (en) * | 2016-03-15 | 2016-06-22 | 厦门烟草工业有限责任公司 | Shred drying machine and shred drying method |
| CN106288662A (en) * | 2016-09-26 | 2017-01-04 | 宁波宝硕美机械设备工程有限公司 | A kind of far infrared three-pass rotary drum drying machine |
| CN106338189A (en) * | 2016-07-22 | 2017-01-18 | 厦门点将集团有限公司 | Drying system |
| CN106562464A (en) * | 2016-04-04 | 2017-04-19 | 邓君 | Remote control type tobacco re-baking oven |
| CN106766761A (en) * | 2016-12-07 | 2017-05-31 | 李政辉 | A kind of root of kudzu vine roller drying machine |
| CN107280062A (en) * | 2017-08-16 | 2017-10-24 | 池州芦山生态农庄科技开发有限公司 | A kind of multi-section roller type burley tobacco roaster |
| CN108050793A (en) * | 2017-12-22 | 2018-05-18 | 宣城市鹤鸣茶叶机械制造有限公司 | A kind of tea drier |
| CN108224945A (en) * | 2018-01-21 | 2018-06-29 | 胡和萍 | A kind of drying cotton machine that can uniformly dry |
| CN108302915A (en) * | 2018-02-01 | 2018-07-20 | 浙江倬瑜服饰有限公司 | A kind of special rotary type dryer of rubber gloves production |
| CN108679994A (en) * | 2018-07-17 | 2018-10-19 | 江西省科学院食品工程创新中心 | Lotus seeds electrical heating rotary drying device |
| CN108741201A (en) * | 2018-05-30 | 2018-11-06 | 滁州卷烟材料厂 | A kind of cut tobacco drying process in cigarette processing process |
| CN109330006A (en) * | 2018-10-31 | 2019-02-15 | 汪琴 | A kind of cut tobacco drying process in cigarette processing process |
| CN110131979A (en) * | 2019-06-18 | 2019-08-16 | 广州创特技术有限公司 | A kind of self-regulation spiral roller infra-red drying equipment |
| CN110186947A (en) * | 2019-05-13 | 2019-08-30 | 长安大学 | Pavement recycling experimental facilities based on infra-red radiation and hot wind collaboration heating |
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Citations (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4186755A (en) * | 1976-08-26 | 1980-02-05 | Hauni-Werke Korber & Co. Kg | Tobacco drying apparatus |
| JPH04187071A (en) * | 1990-11-21 | 1992-07-03 | Japan Tobacco Inc | Treatment of raw tobacco |
| CN2653900Y (en) * | 2003-08-05 | 2004-11-10 | 云南昆船第二机械有限公司 | Tobacco baking equipment for experimental use |
| CN101036532A (en) * | 2007-03-28 | 2007-09-19 | 云南昆船设计研究院 | Method and device for drying cigar lamina |
| CN201069994Y (en) * | 2007-07-25 | 2008-06-11 | 武汉烟草(集团)有限公司 | Thread baking equipment for ceramic inner container |
| US20090113751A1 (en) * | 2007-11-01 | 2009-05-07 | Shi-Yu Teng | Infrared dryer |
| CN101491368A (en) * | 2009-03-12 | 2009-07-29 | 中国烟草总公司郑州烟草研究院 | Combined thermal transmission type micro roller drying device of tobacco |
| CN202932022U (en) * | 2012-11-05 | 2013-05-15 | 广州秘理普植物技术开发有限公司 | Automatic tobacco shred drying machine |
-
2014
- 2014-06-19 CN CN201410275016.3A patent/CN104000299B/en active Active
Patent Citations (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4186755A (en) * | 1976-08-26 | 1980-02-05 | Hauni-Werke Korber & Co. Kg | Tobacco drying apparatus |
| JPH04187071A (en) * | 1990-11-21 | 1992-07-03 | Japan Tobacco Inc | Treatment of raw tobacco |
| CN2653900Y (en) * | 2003-08-05 | 2004-11-10 | 云南昆船第二机械有限公司 | Tobacco baking equipment for experimental use |
| CN101036532A (en) * | 2007-03-28 | 2007-09-19 | 云南昆船设计研究院 | Method and device for drying cigar lamina |
| CN201069994Y (en) * | 2007-07-25 | 2008-06-11 | 武汉烟草(集团)有限公司 | Thread baking equipment for ceramic inner container |
| US20090113751A1 (en) * | 2007-11-01 | 2009-05-07 | Shi-Yu Teng | Infrared dryer |
| CN101491368A (en) * | 2009-03-12 | 2009-07-29 | 中国烟草总公司郑州烟草研究院 | Combined thermal transmission type micro roller drying device of tobacco |
| CN202932022U (en) * | 2012-11-05 | 2013-05-15 | 广州秘理普植物技术开发有限公司 | Automatic tobacco shred drying machine |
Cited By (30)
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| CN104643281A (en) * | 2015-01-25 | 2015-05-27 | 中国烟草总公司黑龙江省公司牡丹江烟草科学研究所 | Tobacco baking room |
| CN104643281B (en) * | 2015-01-25 | 2016-08-17 | 中国烟草总公司黑龙江省公司牡丹江烟草科学研究所 | A kind of tobacco roasting room |
| CN104930832A (en) * | 2015-06-25 | 2015-09-23 | 湖北叶威(集团)智能科技有限公司 | Double-drum crop dryer |
| CN105686041A (en) * | 2016-03-15 | 2016-06-22 | 厦门烟草工业有限责任公司 | Shred drying machine and shred drying method |
| CN106562464A (en) * | 2016-04-04 | 2017-04-19 | 邓君 | Remote control type tobacco re-baking oven |
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