CN209768962U - Low-temperature cut tobacco drying device - Google Patents
Low-temperature cut tobacco drying device Download PDFInfo
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- CN209768962U CN209768962U CN201920340979.5U CN201920340979U CN209768962U CN 209768962 U CN209768962 U CN 209768962U CN 201920340979 U CN201920340979 U CN 201920340979U CN 209768962 U CN209768962 U CN 209768962U
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Abstract
The utility model discloses a low temperature cut tobacco drying device of pipe tobacco, it includes: a cylindrical body (7) having a cylindrical shape and an interlayer on the cylindrical wall; the barrel (7) is approximately horizontally arranged in the axial direction and can rotate along the axial direction, the front end of the barrel is provided with an air inlet, and the rear end of the barrel is provided with an air outlet. The utility model discloses a cut tobacco drying system dries by fire a tobacco efficiently, and the smoke agent and the essence spices that the pipe tobacco after drying by fire added obtain better maintenance, and sensory characteristic obtains obviously promoting.
Description
Technical Field
The utility model belongs to the technical field of tobacco production, concretely relates to low temperature cut tobacco drying device of pipe tobacco.
Background
The reconstituted tobacco is a main raw material for circumferentially heating non-combustible cigarettes and has the following characteristics: the comprehensive utilization rate of tobacco raw materials can be effectively improved; secondly, the cigarette oil material has better adsorbability to smoke agents, propylene glycol and other oily materials for cigarettes; preparing tobacco shred products with different tastes according to different requirements; fourthly, the harmful substances such as tar content and the like can be greatly reduced by heating the non-combustible smoke in the circumferential direction. In recent years, with the self-innovation of circumferential heating non-combustible cigarette products, the yield of reconstituted tobacco is continuously increased, and the application range of the reconstituted tobacco is continuously increased. The existing tobacco shred forming process for paper-making reconstituted tobacco generally mixes the paper-making reconstituted tobacco and natural tobacco together according to process requirements, and then the tobacco shred is made into cigarette tobacco shreds which are not combusted by heating through a series of procedures such as moisture regain, feeding, shredding, drying and the like.
The patent CN101828762A discloses a tobacco shredding process and equipment for paper-making reconstituted tobacco, and provides a new tobacco shredding process and equipment for paper-making reconstituted tobacco aiming at the defects of the paper-making reconstituted tobacco manufacturing and production application processes. The process and the equipment thereof can solve the problem that the paper-making reconstituted tobacco is difficult to be independently shredded. Patent CN102178337A discloses an independent tobacco shred making process and equipment based on paper-making method reconstituted tobacco processing characteristics, and provides a new reconstituted tobacco shred making process and equipment aiming at the universality and the processing characteristics of paper-making method reconstituted tobacco incoming materials. Patent 201210126975.X discloses a cut tobacco drying machine based on the independent cut tobacco forming characteristic of paper-making process reconstituted tobacco and a cut tobacco drying control method thereof, aiming at controlling the cut tobacco drying process of the paper-making process after the paper-making process is independently cut, the low-strength processing mode can effectively maintain the physical characteristic and the chemical characteristic of the paper-making process reconstituted tobacco after the paper-making process reconstituted tobacco is independently cut, and the sensory characteristic is effectively improved.
The above patents mention the drying process involved in the separate shredding of reconstituted tobacco leaves by the paper-making process, but all suffer from the following disadvantages: firstly, when the temperature is lower, the drying efficiency is lower, for example, the drying temperature of patent 201210126975X is 55-65 ℃; patent CN102178337A only shows vaguely that drying reduces the water content, and does not show the drying temperature and drying efficiency. Secondly, when the temperature is higher, although the drying efficiency is improved (namely the moisture content of the tobacco shreds can easily meet the requirement), the high drying temperature evaporates oily substances such as smoke agents and the like contained in the tobacco shreds and spices and essences with various tastes at high temperature, and has negative influence on the retention of the aroma of the obtained non-combustible tobacco shreds and the improvement of the sensory quality.
In addition, the above patent does not solve the following problems: the obtained reconstituted tobacco shreds produced by the paper-making method must be blended with other tobacco shreds, and cannot be independently used as non-combustible tobacco shreds for circumferential heating. Secondly, the low-temperature cut tobacco dryer equipment and the control method which are needed aiming at the characteristic that the reconstituted tobacco is used for heating the non-burning cut tobacco in the circumferential direction independently are not involved. And thirdly, the drying efficiency and the drying effect (namely the maintenance of the smoke agent and the spice essence) of the tobacco shreds which are not combusted during heating can not be considered at the same time.
The utility model discloses solve above-mentioned problem and propose.
SUMMERY OF THE UTILITY MODEL
the utility model discloses a cut tobacco drying system for circumferentially heating non-burning cut tobacco and a use method thereof. Use the utility model discloses a cut tobacco system of drying can satisfy the pipe tobacco technological requirement that circumference heating incombustible cigarette rolled up, does not provide strong guarantee for the processing production of circumference heating incombustible cigarette.
The technical scheme of the utility model as follows:
The utility model discloses a first aspect discloses a cut tobacco drying system that is used for circumference heating incombustible cigarette pipe tobacco, it includes: a cylindrical body 7 having a cylindrical shape and having an interlayer on a cylindrical wall; the barrel 7 is approximately horizontally arranged in the axial direction and can rotate along the axial direction, the front end of the barrel is provided with an air inlet, and the rear end of the barrel is provided with an air outlet.
Preferably, an air inlet at the front end of the cylinder is connected with a hot air pipe 5, and a hot air temperature sensor 20 and an air speed sensor 21 are mounted on the hot air pipe 5; an air outlet at the rear end of the barrel is provided with a moisture exhaust pipe network 8, the moisture exhaust pipe network 8 is connected with a moisture exhaust air pipe 6, and the moisture exhaust air pipe 6 is provided with a negative pressure sensor 23 and an electric valve positioner 24; the other end of the hot air duct 5 is connected with a heat exchanger 27 through a hot air fan 25; the heat exchanger 27 is connected with a second steam pipe 3, the second steam pipe 3 is connected with a hot air steam valve 13 and a second pneumatic membrane valve 28, and the tail end of the second steam pipe 3 is provided with a drain valve 15; the second steam pipe 3 is connected to a steam source 1.
Preferably, the interlayer of the cylinder wall of the cylinder body 7 is connected with a delivery water pipe 11 and a return water pipe 12; the delivery water pipe 11 and the return water pipe 12 are communicated with the water tank 9; a backflow water temperature sensor 22 is arranged on the backflow water pipe 12, a water pump 26 is arranged between the delivery water pipe 11 and the water tank 9, and an air dredging valve 16 is arranged at the tail end of the water pump 26; the upper part of the front end of the water tank 9 is connected with a first steam pipe 2, the lower part of the rear end of the water tank is connected with a steam recovery device 30, and a water-bath heating steam valve 14 and a first pneumatic membrane valve 17 are arranged on the first steam pipe 2; a water tank water temperature sensor 19 is also arranged on the water tank 9; the first steam pipe 2 is connected to a steam source 1.
Preferably, the water tank 9 is connected to the water inlet pipe 10 through a water inlet valve 29.
Preferably, a rotary net cleaning air pipe 4 is arranged between the hot air pipe 5 and the moisture exhaust pipe network 8.
The utility model discloses a second aspect discloses a circumference heating non-combustible cigarette tobacco's cut tobacco drying method uses foretell cut tobacco drying system, and its step includes: starting a steam source 1 to enable steam to enter a water tank 9 and a heat exchanger 27 through a first steam pipe 2 and a second steam pipe 3 respectively, and heating water in the steam and exchanging heat with low-humidity air in the heat exchanger 27; when the temperature in the water tank 9 and the temperature of the low-humidity air reach set values, a hot air blower 25 is started, the temperature and the speed of the low-humidity air entering the cylinder 7 are controlled through a hot air temperature sensor 20 and an air speed sensor 21, and the gas in the cylinder 7 is discharged through a negative pressure sensor 23 and an electric valve positioner 24; starting a water pump 26 to enable hot water to enter the interlayer of the cylinder wall of the cylinder body 7 to heat the inner cylinder wall; the cylinder body 7 is rotated to bake circumferentially-heated non-combustible cigarette tobacco shreds, and the opening degree of the electric valve positioner 24 is automatically controlled through the negative pressure sensor 23; when the water content of the cut tobacco meets the requirement, the cut tobacco can be discharged for drying the next batch of cut tobacco;
When the moisture removal pipe network 8 is blocked, the moisture removal pipe network 8 can be reversely blown through the rotating net cleaning air pipe 4 to clean the rotating net cleaning air pipe 4.
Preferably, the low-humidity air is air having a relative humidity of not more than 10% at 3 ℃ or less.
Preferably, the temperature of the low-humidity air entering the cylinder 7 is set to be 55-65 ℃; the temperature of the inner wall of the cylinder 7 is set to 65-75 ℃, and the rotating speed of the cylinder 7 is set to 8-10 rmp.
Preferably, the steps are both automatic control and automatic adjustment.
The utility model has the advantages that:
1. The utility model discloses a cylinder of cut-tobacco drying system uses the hot water intermediate layer for the first time, satisfies the requirement of carrying out the low temperature cut-tobacco drying below 100 ℃.
2. The utility model discloses a cut-tobacco drier system enables traditional cut-tobacco drier to be applicable to completely that circumference heating does not burn the requirement of the independent filamentation of reconstituted tobacco behind the required addition smoke former of cigarette and essence spices, need not use new equipment, and the cost is lower.
3. The tobacco shred drying system of the utility model is used for drying tobacco shreds which are not combusted in circumferential heating, so that the control requirement of 5-8 wt% of moisture at the tobacco shred outlet can be realized, and substances such as smoke agent essence and spice added in the tobacco shreds can be better kept, so that the material characteristics of the tobacco shreds which are not combusted at low temperature are improved, the chemical characteristics and the physical characteristics of the reconstituted tobacco shreds are better kept, and the sensory characteristics are obviously improved; meanwhile, the quality and the effective utilization rate of the single shredding of the reconstituted tobacco can be improved.
4. Use the utility model discloses a cut tobacco drying system does not burn the cut tobacco drying of cigarette pipe tobacco to the circumference heating can adopt full automatic control and regulation, has not only saved manpower and materials, makes cut tobacco drying efficiency drive obviously to improve moreover.
Drawings
fig. 1 is a schematic view of a tobacco shred drying system for circumferentially heating non-burning tobacco shreds according to the present invention.
Reference numerals: 1-a steam source, 2-a first steam pipe, 3-a second steam pipe, 4-a moisture discharge rotating net cleaning pipe, 5-a hot air pipe, 6-a moisture discharge pipe, 7-a cylinder, 8-a moisture discharge rotating net, 9-a water tank, 10-a water inlet pipe, 11-a conveying water pipe, 12-a return water pipe, 13-a hot air steam valve, 14-a water bath heating steam valve, 15-a drain valve, 16-a gas relief valve, 17-a pneumatic membrane valve, 18-a flowmeter, 19-a water tank temperature sensor, 20-a hot air temperature sensor, 21-a wind speed sensor, 22-a return water temperature sensor, 23-a negative pressure sensor, 24-an electric valve positioner, 25-a hot air fan, 26-a water pump, 27-a heat exchanger, 28-a pneumatic membrane valve, 29-a water inlet valve, and 30-a steam recovery device.
Detailed Description
The utility model discloses a cut tobacco drying system that is used for circumference heating incombustible cigarette pipe tobacco, it includes: a cylindrical body 7 having a cylindrical shape and having an interlayer on a cylindrical wall; the barrel 7 is approximately horizontally arranged in the axial direction and can rotate along the axial direction, the front end of the barrel is provided with an air inlet, and the rear end of the barrel is provided with an air outlet. An air inlet at the front end of the cylinder is connected with a hot air pipe 5, and a hot air temperature sensor 20 and an air speed sensor 21 are arranged on the hot air pipe 5; an air outlet at the rear end of the barrel is provided with a moisture exhaust pipe network 8, the moisture exhaust pipe network 8 is connected with a moisture exhaust air pipe 6, and the moisture exhaust air pipe 6 is provided with a negative pressure sensor 23 and an electric valve positioner 24; the other end of the hot air duct 5 is connected with a heat exchanger 27 through a hot air fan 25; the heat exchanger 27 is connected with a second steam pipe 3, the second steam pipe 3 is connected with a hot air steam valve 13 and a second pneumatic membrane valve 28, and the tail end of the second steam pipe 3 is provided with a drain valve 15; the second steam pipe 3 is connected to a steam source 1. The interlayer of the cylinder wall of the cylinder body 7 is connected with a delivery pipe 11 and a return pipe 12; the delivery water pipe 11 and the return water pipe 12 are communicated with the water tank 9; a backflow water temperature sensor 22 is arranged on the backflow water pipe 12, a water pump 26 is arranged between the delivery water pipe 11 and the water tank 9, and an air dredging valve 16 is arranged at the tail end of the water pump 26; the upper part of the front end of the water tank 9 is connected with a first steam pipe 2, the lower part of the rear end of the water tank is connected with a steam recovery device 30, and a water-bath heating steam valve 14 and a first pneumatic membrane valve 17 are arranged on the first steam pipe 2; a water tank water temperature sensor 19 is also arranged on the water tank 9; the first steam pipe 2 is connected to a steam source 1. The water tank 9 is connected to the water inlet pipe 10 through a water inlet valve 29. And a rotary net cleaning air pipe 4 is arranged between the hot air pipe 5 and the moisture exhaust pipe network 8.
The cut tobacco drying method for circumferentially heating the non-burning cut tobacco of the cigarette comprises the following steps of: starting a steam source 1 to enable steam to enter a water tank 9 and a heat exchanger 27 through a first steam pipe 2 and a second steam pipe 3 respectively, and heating water in the steam and exchanging heat with low-humidity air in the heat exchanger 27; when the temperature in the water tank 9 and the temperature of low-humidity air (low-humidity air is air with the relative humidity of 10% at 0 ℃) reach set values, a hot air blower 25 is started, the temperature and the speed of the low-humidity air entering the cylinder 7 are controlled through a hot air temperature sensor 20 and an air speed sensor 21, and the gas in the cylinder 7 is discharged through a negative pressure sensor 23 and an electric valve positioner 24; starting a water pump 26 to enable hot water to enter the interlayer of the cylinder wall of the cylinder body 7 to heat the inner cylinder wall; the temperature of the low-humidity air entering the cylinder 7 is set to be 60 ℃; the temperature of the inner cylindrical wall of the cylinder 7 was set to 70 ℃ and the rotational speed of the cylinder 7 was set to 10 rmp. The cylinder body 7 is rotated to bake circumferentially-heated non-combustible cigarette tobacco shreds, and the opening degree of the electric valve positioner 24 is automatically controlled through the negative pressure sensor 23; and when the water content of the cut tobacco reaches 6 wt%, discharging and drying the cut tobacco of the next batch.
when the moisture removal pipe network 8 is blocked, the moisture removal pipe network 8 can be reversely blown through the rotating net cleaning air pipe 4 to clean the rotating net cleaning air pipe 4.
Through analysis, the smoke agent and the essence perfume added in the obtained cut tobacco basically have no loss, and the taste completely meets the requirement of singly heating the non-combustible cut tobacco of the cigarette in the circumferential direction; the obtained tobacco shreds can also be added into common cigarette for use. In addition, the utility model has the advantages of obviously improving the tobacco shred drying efficiency.
Claims (5)
1. A low temperature cut tobacco drying device is characterized by comprising: a cylindrical body (7) having a cylindrical shape and an interlayer on the cylindrical wall; the barrel (7) is approximately horizontally arranged in the axial direction and can rotate along the axial direction, the front end of the barrel is provided with an air inlet, and the rear end of the barrel is provided with an air outlet.
2. The device according to claim 1, characterized in that the air inlet of the front end of the cylinder is connected with a hot air pipe (5), and the hot air pipe (5) is provided with a hot air temperature sensor (20) and an air speed sensor (21); an air outlet at the rear end of the barrel is provided with a moisture exhaust pipe network (8), the moisture exhaust pipe network (8) is connected with a moisture exhaust air pipe (6), and the moisture exhaust air pipe (6) is provided with a negative pressure sensor (23) and an electric valve positioner (24); the other end of the hot air pipe (5) is connected with a heat exchanger (27) through a hot air fan (25); the heat exchanger (27) is connected with a second steam pipe (3), the second steam pipe (3) is connected with a hot air steam valve (13) and a second pneumatic membrane valve (28), and the tail end of the second steam pipe (3) is provided with a drain valve (15); the second steam pipe (3) is connected with the steam source (1).
3. The device according to claim 1, characterized in that the interlayer of the cylinder wall of the cylinder body (7) is connected with a delivery water pipe (11) and a return water pipe (12); the conveying water pipe (11) and the return water pipe (12) are communicated and connected with the water tank (9); a backflow water temperature sensor (22) is arranged on the backflow water pipe (12), a water pump (26) is arranged between the delivery water pipe (11) and the water tank (9), and an air exhaust valve (16) is arranged at the tail end of the water pump (26); the upper part of the front end of the water tank (9) is connected with a first steam pipe (2), the lower part of the rear end of the water tank is connected with a steam recovery device (30), and a water-bath heating steam valve (14) and a first pneumatic membrane valve (17) are arranged on the first steam pipe (2); a water tank water temperature sensor (19) is also arranged on the water tank (9); the first steam pipe (2) is connected with a steam source (1).
4. A device according to claim 3, characterized in that the water tank (9) is connected to the inlet pipe (10) by means of an inlet valve (29).
5. The device according to claim 2, characterized in that a rotary screen cleaning air pipe (4) is arranged between the hot air pipe (5) and the moisture exhaust pipe network (8).
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CN201920340979.5U CN209768962U (en) | 2019-03-18 | 2019-03-18 | Low-temperature cut tobacco drying device |
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CN201920340979.5U CN209768962U (en) | 2019-03-18 | 2019-03-18 | Low-temperature cut tobacco drying device |
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Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN109820231A (en) * | 2019-03-18 | 2019-05-31 | 云南中烟工业有限责任公司 | A kind of baking silk system and its application method heating the cigarette shreds that do not burn for circumferential direction |
CN113383982A (en) * | 2021-07-09 | 2021-09-14 | 四川三联新材料有限公司 | Shred preparation blending method for disordered heating cigarette |
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2019
- 2019-03-18 CN CN201920340979.5U patent/CN209768962U/en active Active
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN109820231A (en) * | 2019-03-18 | 2019-05-31 | 云南中烟工业有限责任公司 | A kind of baking silk system and its application method heating the cigarette shreds that do not burn for circumferential direction |
CN109820231B (en) * | 2019-03-18 | 2024-02-23 | 云南中烟工业有限责任公司 | Cut tobacco drying system for circumferentially heating non-combustible cigarette cut tobacco and use method thereof |
CN113383982A (en) * | 2021-07-09 | 2021-09-14 | 四川三联新材料有限公司 | Shred preparation blending method for disordered heating cigarette |
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