CN112056605B - Energy-efficient type tobacco drying system - Google Patents
Energy-efficient type tobacco drying system Download PDFInfo
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- CN112056605B CN112056605B CN202010809041.0A CN202010809041A CN112056605B CN 112056605 B CN112056605 B CN 112056605B CN 202010809041 A CN202010809041 A CN 202010809041A CN 112056605 B CN112056605 B CN 112056605B
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- A—HUMAN NECESSITIES
- A24—TOBACCO; CIGARS; CIGARETTES; SIMULATED SMOKING DEVICES; SMOKERS' REQUISITES
- A24B—MANUFACTURE OR PREPARATION OF TOBACCO FOR SMOKING OR CHEWING; TOBACCO; SNUFF
- A24B3/00—Preparing tobacco in the factory
- A24B3/04—Humidifying or drying tobacco bunches or cut tobacco
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B30/00—Heat pumps
- F25B30/02—Heat pumps of the compression type
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- Mechanical Engineering (AREA)
- Thermal Sciences (AREA)
- General Engineering & Computer Science (AREA)
- Drying Of Solid Materials (AREA)
Abstract
The invention relates to a high-efficiency energy-saving tobacco drying system which comprises a preheating drying box (2), an infrared drying roller (5), a heat pump circulation module, an air filter (17) and an air preheater (18), wherein the preheating drying box (2) is communicated with the infrared drying roller (5), the heat pump circulation module comprises a waste heat source evaporator (12), a compressor (13), a condenser (14), an expansion valve (15) and an air source evaporator (16) which are sequentially connected end to form a loop, and the air filter (17), the air preheater (18), the condenser (14) and the infrared drying roller (5) are sequentially connected. Compared with the prior art, the invention carries out convection and radiation heating drying treatment on the tobacco raw material, and fully utilizes the heat in a grading way, and has the advantages of high drying speed, high efficiency, energy saving and the like.
Description
Technical Field
The invention belongs to the field of tobacco drying, and particularly relates to a high-efficiency energy-saving tobacco drying system.
Background
The tobacco drying process is a very important tobacco raw material treatment process, and aims to remove excess moisture in tobacco raw materials such as cut leaves, cut stems, redried leaves and the like or cut tobacco. In order to complete the drying process tasks of tobacco such as cut tobacco, cut stems, redried leaves and the like, a hot air system of an adopted dryer generally adopts air with higher temperature to dry the tobacco, and the mode has large energy consumption. At the same time, it is particularly important: the tobacco is a heat-sensitive substance, the taste of the tobacco can be damaged at high temperature, and the color, the aroma, the taste and the texture of the tobacco can be well maintained only by drying the tobacco at low temperature.
At present, the tobacco drying equipment has the technical defects of poor drying effect, high energy consumption, general energy-saving and environment-friendly performance and the like. Therefore, the traditional tobacco drying technology is improved, the drying technology level is improved, and the high-efficiency energy-saving tobacco drying system is provided, so that the system has very important industrial significance for promoting the technical development of the field of tobacco drying.
Disclosure of Invention
The invention aims to provide an efficient energy-saving tobacco drying system which is used for carrying out convection and radiation heating drying treatment on tobacco raw materials and has the advantages of high drying speed, high efficiency, energy conservation and the like.
The purpose of the invention is realized by the following technical scheme:
the utility model provides an energy-efficient type tobacco drying system, drying system is including preheating drying cabinet, infrared drying cylinder, heat pump cycle module, air cleaner and air heater, heat pump cycle module includes end to end waste heat source evaporimeter, compressor, condenser, expansion valve and the air source evaporimeter that forms the return circuit in proper order, preheat the drying cabinet with infrared drying cylinder is linked together, air cleaner, air heater, condenser and infrared drying cylinder link to each other in proper order. The air source evaporator obtains heat from ambient air, and the waste heat source evaporator obtains heat from high-temperature waste heat. The preheating drying box preheats the tobacco raw materials to be dried, so that the damage to the appearance and the taste caused by the instantaneous temperature rise of the tobacco raw materials in the infrared drying roller can be avoided. The air is filtered by the air filter before entering the air preheater, so that the purity of the air is ensured, and the tobacco raw material to be dried is prevented from being polluted. The evaporator, the compressor, the condenser, the expansion valve and the like all adopt the existing equipment.
The infrared drying drum is provided with a drying drum tobacco raw material inlet, a drying drum tobacco raw material outlet, an infrared drying drum air inlet and an infrared drying drum air outlet, wherein the infrared drying drum air inlet and the infrared drying drum air outlet are communicated with the condenser, one end of the infrared drying drum is provided with a motor for driving the infrared drying drum to rotate, and an infrared heating column is arranged inside the infrared drying drum.
The infrared drying drum comprises an inner drum body and an outer drum body sleeved on the outer side of the inner drum body, the air inlet and the air outlet of the infrared drying drum are both located on the outer drum body, and a plurality of drying drum vent holes are formed in the side wall of the inner drum body along the circumferential direction. The drying drum vent holes can be used as air equalizing plates, so that high-temperature air is distributed more uniformly, the air is contacted with the tobacco raw materials to be dried more fully, and the drying effect is better.
The inner wall of the inner cylinder body is provided with a plurality of convex teeth, and the air vent of the drying cylinder is positioned between the adjacent convex teeth. The convex teeth can fully stir the tobacco raw materials.
The preheating drying oven is provided with a drying oven tobacco raw material inlet, a drying oven tobacco raw material outlet and a drying oven air inlet, wherein the drying oven tobacco raw material outlet is communicated with the infrared drying roller.
The drying oven tobacco raw material inlet is located above the preheating drying oven, and the drying oven tobacco raw material outlet is located below the preheating drying oven.
The preheating drying box comprises an inner box body and an outer box body sleeved on the outer side of the inner box body, a plurality of drying box air vents are formed in the side wall of the inner box body along the circumferential direction, and air inlets of the drying boxes are located on the outer box body. A plurality of drying cabinet air vents can be regarded as the board of wind-sharing, make the low wet waste gas of high temperature distribute more evenly to contact more fully with the tobacco raw materials that will be dried, it is better to preheat the effect.
And a three-way valve is arranged between the infrared drying roller and the waste heat source evaporator and is communicated with the waste heat source evaporator through the three-way valve, the three-way valve is also communicated with the preheating drying box, and the three-way valve is connected with an air outlet of the infrared drying roller.
And a high-temperature dehumidifier is arranged between the three-way valve and the preheating drying box. The three-way valve leads out a part of high-temperature waste gas flowing out of the infrared drying drum to enter the high-temperature dehumidifier for removing moisture, and then the high-temperature waste gas enters the preheating drying box for preheating the tobacco raw materials.
And an air pump is arranged between the infrared drying drum (namely the air outlet of the infrared drying drum) and the three-way valve.
The air preheater is also communicated with the waste heat source evaporator. And after a part of high-temperature waste gas flowing out of the infrared drying roller is utilized by the waste heat source evaporator, the high-temperature waste gas enters the air preheater to further preheat the air, and the air is utilized in multiple stages.
The evaporator, the compressor, the condenser, the expansion valve, the infrared drying roller, the preheating drying box, the air preheater, the air filter, the air pump and the like all adopt the existing equipment.
The invention dries tobacco based on infrared radiation heat transfer and hot air convection heat transfer. The drying mechanism of the infrared drying is that the moisture-containing material is heated by electromagnetic wave radiation, and the radiation electromagnetic wavelength with the heating effect is mainly located in an infrared ray section within 0.76-20.00 mu m, so the infrared radiation heat transfer drying is also called, has the advantages of non-contact heating, small thermal inertia, good heating uniformity of irregular particle materials and the like, and can realize uniform heating on the surface layer of the material and a certain depth below the surface layer due to the penetrability of the infrared ray on the material. In the infrared radiation heating process, when the frequency of infrared radiation irradiated on the material is the same as the inherent frequency of molecules forming the material, the molecules can generate resonance absorption, and meanwhile, because the molecular motion is accelerated, the internal energy of the molecules is increased, so that the internal temperature of the material is increased, and the internal and external temperature difference is 5-10 ℃. The temperature gradient existing in the material temperature and the water content gradient act together to cause the internal moisture of the material to be continuously diffused, thereby achieving the aim of drying. The infrared radiation heat transfer and the hot air convection heat transfer both play a role in strengthening the mass transfer process, and the elasticity, filling value and cut tobacco size of the cut tobacco can be controlled by adjusting the temperature of infrared drying, the humidity and temperature of hot air and the like, and the drying speed is high.
When the drying system works, tobacco raw materials enter the preheating drying box, are preheated by the dehumidified high-temperature waste gas, and then enter the infrared drying drum to be heated and dried by infrared radiation and hot air. After the air is heated up through the preheating of the air preheater and the heat exchange of the condenser, high-temperature air is formed, and then the air enters the infrared drying roller to dry the tobacco, so that high-temperature waste gas is formed, and the high-temperature waste gas flows out of the infrared drying roller under the action of the air suction pump. At the moment, a part of high-temperature waste gas enters the waste heat source evaporator at the three-way valve, is subjected to heat recycling by the heat pump circulation module, then enters the air preheater, is further preheated by waste heat, and finally is discharged to the ambient air. And the other part of high-temperature waste gas enters the high-temperature dehumidifier at the three-way valve to remove moisture, and then enters the preheating drying box to preheat the tobacco raw materials. In the heat pump circulation module, low-temperature and low-pressure liquid heat pump circulation working media firstly obtain heat from ambient air through an air source evaporator, then obtain heat from waste gas through a waste heat source evaporator to form gaseous heat pump circulation working media, then the temperature of the gaseous heat pump circulation working media is increased through compression of a compressor to form high-temperature and high-pressure gaseous heat pump circulation working media, the gaseous heat pump circulation working media and air exchange are carried out in a condenser, the gaseous heat pump circulation working media are expanded through an expansion valve to be continuously cooled after condensation, the gaseous heat pump circulation working media are changed into low-temperature and low-pressure liquid heat pump circulation working media, and then the liquid heat pump circulation working media enter the air source evaporator to form a circulation loop.
Compared with the prior art, the invention obtains heat from ambient air through the air source evaporator, recovers heat from high-temperature waste gas through the waste heat source evaporator and the air preheater, and carries out convection and radiation heating drying treatment on the tobacco raw material through the preheating drying box and the infrared drying drum, and the structural design of the air holes of the drying drum and the drying box is beneficial to full contact of the tobacco raw material and hot air flow, and has the advantages of high drying speed, high efficiency, energy saving and the like.
Drawings
Fig. 1 is a schematic view of a drying system.
In the figure: 1-tobacco raw material inlet of drying box; 2-preheating a drying box; 201-inner box body; 202-outer box body; 203-drying oven vent; 3-a pipeline; 4-an electric motor; 5-infrared drying roller; 501-inner cylinder body; 502-outer cylinder; 503-drying drum vent hole; 6-infrared heating column; 7-convex teeth; 8-drying drum tobacco material outlet; 9-an air pump; 10-three-way valve; 11-high temperature dehumidifier; 12-a waste heat source evaporator; 13-a compressor; 14-a condenser; 15-an expansion valve; 16-an air source evaporator; 17-an air filter; 18-an air preheater; 19-a tobacco raw material outlet of the drying box; 20-drying oven air inlet; 21-drying drum tobacco material inlet; 22-infrared drying drum air inlet; 23-Infrared drying drum air outlet.
Detailed Description
The invention is described in detail below with reference to the figures and specific embodiments.
Examples
As shown in fig. 1, the drying system comprises a preheating drying box 2, an infrared drying drum 5, a heat pump circulation module, an air filter 17, an air preheater 18, an air pump 9, a three-way valve 10 and a high-temperature dehumidifier 11, wherein the heat pump circulation module comprises a waste heat source evaporator 12, a compressor 13, a condenser 14, an expansion valve 15 and an air source evaporator 16 which are sequentially connected end to form a loop, the preheating drying box 2 is communicated with the infrared drying drum 5, the air filter 17, the air preheater 18, the condenser 14, the infrared drying drum 5, the air pump 9, the three-way valve 11, the waste heat source evaporator 12 and the air source evaporator 18 are sequentially connected, one interface of the three-way valve 11 is also communicated with the high-temperature dehumidifier 11, and the high-temperature dehumidifier 11 is communicated with the preheating drying box 2. Wherein, the dotted line is the flowing direction of the waste gas, the single solid line is the flowing direction of the air, and the double solid lines are the flowing direction of the heat pump cycle working medium.
Be equipped with drying cylinder tobacco raw materials entry 21 on infrared drying cylinder 5, drying cylinder tobacco raw materials export 8, infrared drying cylinder air inlet 22 that is linked together with condenser 14 and the infrared drying cylinder gas outlet 23 that is linked together with aspiration pump 9, the one end of infrared drying cylinder 5 is equipped with and is used for driving infrared drying cylinder 5 pivoted motor 4, the inside of infrared drying cylinder 5 is equipped with infrared heating post 6, infrared drying cylinder 5 includes interior barrel 501 and the outer barrel 502 of cover in the barrel 501 outside, infrared drying cylinder air inlet 22 and infrared drying cylinder gas outlet 23 all are located outer barrel 502, be equipped with a plurality of drying cylinder air vents 503 along circumference on the lateral wall of interior barrel 501, be equipped with a plurality of protruding teeth 7 along circumference on the inner wall of interior barrel 501, drying cylinder air vent 503 is located between the adjacent protruding tooth 7.
Preheating drying cabinet 2 is last to be equipped with drying cabinet tobacco raw material entry 1, drying cabinet tobacco raw material export 19 (connecting through pipeline 3 between drying cabinet tobacco raw material export 19 and the drying drum tobacco raw material entry 21) and the drying cabinet air inlet 20 that are linked together with drying drum tobacco raw material entry 21 of infrared drying drum 5, preheating drying cabinet 2 includes that interior box 201 and cover establish the outer box 202 in the interior box 201 outside, be equipped with a plurality of drying cabinet air vents 203 along circumference on the lateral wall of interior box 201, drying cabinet air inlet 20 is located outer box 202 and is linked together with high temperature dehumidifier 11.
When the drying system works, tobacco raw materials to be dried firstly enter the preheating drying box 2 through the tobacco raw material inlet 1 of the drying box, and then enter the infrared drying drum 5 from the tobacco raw material outlet 19 of the drying box, the pipeline 3 and the tobacco raw material inlet 21 of the drying drum after being preheated. The air is heated up through the filtration of the air filter 17, the preheating of the air preheater 18 and the heat exchange of the condenser 14 to form high-temperature air, and then the high-temperature air enters the infrared drying drum 5 through the air inlet 22 of the infrared drying drum and the vent 503 of the drying drum in sequence to dry the tobacco, so that the high-temperature waste gas is formed, and the tobacco which is dried at the moment is discharged out of the infrared drying drum 5 through the tobacco raw material outlet 8 of the drying drum. The high-temperature waste gas flows out of the infrared drying drum 5 from the infrared drying drum air outlet 23, and a part of the high-temperature waste gas sequentially enters the waste heat source evaporator 12 and the air preheater 18 through the air suction pump 9 and the three-way valve 10 to recycle heat, and then is discharged out of the system to enter ambient air. The other part of the high-temperature waste gas enters the high-temperature dehumidifier 11 through the air pump 9 and the three-way valve 10, after moisture is removed by the high-temperature dehumidifier 11, the other part of the high-temperature waste gas enters the preheating drying box 2 through the drying box air inlet 20 and the drying box vent hole 203 to heat the tobacco raw materials. In the heat pump circulation module, low-temperature and low-pressure liquid heat pump circulation working media firstly obtain heat from ambient air through an air source evaporator 16, then obtain heat from high-temperature waste gas through a waste heat source evaporator 12 to form gaseous heat pump circulation working media, then the gaseous heat pump circulation working media are compressed by a compressor 13 to be increased in temperature to become high-temperature and high-pressure gaseous heat pump circulation working media, then the gaseous heat pump circulation working media exchange heat with air in a condenser 14, and the gaseous heat pump circulation working media are expanded by an expansion valve 15 to be continuously reduced in temperature after being condensed to become low-temperature and low-pressure liquid heat pump circulation working media, and then the low-temperature and low-pressure liquid heat pump circulation working media enter the air source evaporator 16 to form a circulation loop.
The embodiments described above are described to facilitate an understanding and use of the invention by those skilled in the art. It will be readily apparent to those skilled in the art that various modifications to these embodiments may be made, and the generic principles described herein may be applied to other embodiments without the use of the inventive faculty. Therefore, the present invention is not limited to the above embodiments, and those skilled in the art should make improvements and modifications within the scope of the present invention based on the disclosure of the present invention.
Claims (8)
1. The high-efficiency energy-saving tobacco drying system is characterized by comprising a preheating drying box (2), an infrared drying roller (5), a heat pump circulating module, an air filter (17) and an air preheater (18), wherein the preheating drying box (2) is communicated with the infrared drying roller (5), the heat pump circulating module comprises a waste heat source evaporator (12), a compressor (13), a condenser (14), an expansion valve (15) and an air source evaporator (16) which are sequentially connected end to form a loop, the air filter (17), the air preheater (18), the condenser (14) and the infrared drying roller (5) are sequentially connected,
a three-way valve (10) is arranged between the infrared drying roller (5) and the waste heat source evaporator (12) and is communicated with the waste heat source evaporator through the three-way valve (10), the three-way valve (10) is also communicated with the preheating drying box (2),
and a high-temperature dehumidifier (11) is arranged between the three-way valve (10) and the preheating drying box (2).
2. The efficient energy-saving tobacco drying system according to claim 1, wherein the infrared drying drum (5) is provided with a drying drum tobacco raw material inlet (21), a drying drum tobacco raw material outlet (8), an infrared drying drum air inlet (22) and an infrared drying drum air outlet (23) which are communicated with the condenser (14), one end of the infrared drying drum (5) is provided with a motor (4) for driving the infrared drying drum (5) to rotate, and the infrared drying drum (5) is internally provided with an infrared heating column (6).
3. The efficient energy-saving tobacco drying system according to claim 2, wherein the infrared drying drum (5) comprises an inner drum body (501) and an outer drum body (502) sleeved outside the inner drum body (501), the infrared drying drum air inlet (22) and the infrared drying drum air outlet (23) are both located on the outer drum body (502), and a plurality of drying drum vent holes (503) are formed in the side wall of the inner drum body (501) along the circumferential direction.
4. An energy-efficient tobacco drying system according to claim 3, characterized in that the inner wall of the inner cylinder (501) is provided with a plurality of convex teeth (7) along the circumferential direction, and the drying cylinder vent holes (503) are positioned between adjacent convex teeth (7).
5. An efficient energy-saving tobacco drying system according to claim 1, characterized in that the preheating drying oven (2) is provided with a drying oven tobacco raw material inlet (1), a drying oven tobacco raw material outlet (19) communicated with the infrared drying drum (5) and a drying oven air inlet (20).
6. The high-efficiency energy-saving tobacco drying system according to claim 5, wherein the preheating drying box (2) comprises an inner box body (201) and an outer box body (202) sleeved outside the inner box body (201), a plurality of drying box vent holes (203) are formed in the side wall of the inner box body (201) along the circumferential direction, and the drying box air inlet (20) is located in the outer box body (202).
7. An energy-efficient tobacco drying system according to claim 1, characterized in that a suction pump (9) is provided between the infrared drying drum (5) and the three-way valve (10).
8. An energy efficient tobacco drying system according to claim 1 wherein the air preheater (18) is further in communication with the waste heat source evaporator (12).
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202010809041.0A CN112056605B (en) | 2020-08-12 | 2020-08-12 | Energy-efficient type tobacco drying system |
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| Application Number | Priority Date | Filing Date | Title |
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| CN202010809041.0A CN112056605B (en) | 2020-08-12 | 2020-08-12 | Energy-efficient type tobacco drying system |
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| CN112056605A CN112056605A (en) | 2020-12-11 |
| CN112056605B true CN112056605B (en) | 2021-10-08 |
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| CN108283326A (en) * | 2017-01-10 | 2018-07-17 | 秦皇岛烟草机械有限责任公司 | A kind of combined type tobacco drying equipment |
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| CN203435668U (en) * | 2013-07-18 | 2014-02-19 | 成都蓉阳科技有限公司 | Split type air source waste heat recycling type tobacco heat pump drying machine set |
| CN111174539A (en) * | 2018-11-13 | 2020-05-19 | 秦皇岛烟草机械有限责任公司 | Tobacco drying hot air circulating system |
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| Publication number | Priority date | Publication date | Assignee | Title |
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| DE102007018018A1 (en) * | 2007-04-17 | 2008-10-23 | Helmut Spielvogel | Contact-frame dryer for sliced veneer, has steel fiber tape connected with frame roller in force-fit manner, where roller is driven into dryer-sections at different temperatures, and control device obtaining air conditioning in chamber |
| CN201426364Y (en) * | 2009-06-26 | 2010-03-24 | 江苏智思机械集团有限公司 | Staged cut tobacco-drying equipment |
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| CN112056605A (en) | 2020-12-11 |
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