CN204191559U - A kind of finished product cut tobacco production system adopting SH93 air flow type cut tobacco drier - Google Patents
A kind of finished product cut tobacco production system adopting SH93 air flow type cut tobacco drier Download PDFInfo
- Publication number
- CN204191559U CN204191559U CN201420613408.1U CN201420613408U CN204191559U CN 204191559 U CN204191559 U CN 204191559U CN 201420613408 U CN201420613408 U CN 201420613408U CN 204191559 U CN204191559 U CN 204191559U
- Authority
- CN
- China
- Prior art keywords
- cut tobacco
- air flow
- moisture meter
- warming
- flow type
- 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.)
- Active
Links
Abstract
The utility model relates to a kind of finished product cut tobacco production system adopting SH93 air flow type cut tobacco drier, and this system comprises leaf storing cabinet, the first bin type feeding machine, the first control gauge line, the first control type belt conveyer scale, warming and humidifying cylinder, the second bin type feeding machine, filament cutter, the second bin type feeding machine, the second gauge line, the second control type belt conveyer scale, SH93 air flow type cut tobacco drier and winnowing machine on the spot successively; Moisture Meter is provided with between the first described control type belt conveyer scale and warming and humidifying cylinder, Moisture Meter and temperature measurer is provided with between warming and humidifying cylinder and the second bin type feeding machine, Moisture Meter is provided with between second control type belt conveyer scale and SH93 air flow type cut tobacco drier, SH93 air flow type cut tobacco drier and be provided with Moisture Meter and temperature measurer between winnowing machine on the spot, winnowing machine rear end, ground is also provided with Moisture Meter and temperature measurer.The utility model operation result shows, after SH93 air-flow dries the baking of silk, moisture content of cut tobacco stability and control accuracy increase substantially.
Description
Technical field
The utility model relates to a kind of finished product cut tobacco production system.
Background technology
Under the overall situation of current domestic tobacco leaf resource scarcity, how to improve utilization ratio and the crudy of tobacco leaf resource, become a large problem of each Cigarette manufacturing enterprises.And also clearly propose in [tobacco business medium & long term sci-tech development program outline (2006-the year two thousand twenty)] that State Tobacco Monopoly Bureau formulates and target will be turned to General Promotion Chinese-style cigarette integrated quality, outstanding cigarette product aromatic style and taste profile, the use value giving full play to raw tobacco material, the characteristic that realizes cigarette product, more new technology theory, reinforcement process is innovated, highlight craft feature, construct Chinese-style cigarette technique independent core technology, realize cigarette product systematization of design, processing become more meticulous, intelligent control, production intensification target.Pneumatic drying of cut tobacco technology can be controlled in 20%-30% because of the expansion rate with cut tobacco and can remove blue foreign smell taste and free nicotine, aroma of tobacco shreds more alcohol and and make cut tobacco have the features such as good crimpness and laxity and generally be applied in tobacco business, to improve utilization rate and the product quality of tobacco leaf.
The SH93 type air current type tobacco shred drying machine that Hangzhou Cigarette Factory introducing Jiangsu intelligence thinks the production of mechanical group company carries out cut tobacco drying processing, the conventional machining process system adopted is as Fig. 1, in actual production, the raising of cut tobacco Filling power and the target of reducing tar and reducing harm after baking, obtain good realization; But air-flow dries silk and cylinder thin plate and dries silk and contrast and find, SH93 air-flow baking silk baking afterwards cut tobacco exists the problems such as moisture control precision is on the low side, the less stable of moisture content, over-dried cut tobacco amount are relatively higher.By analysis, there is the problem of 3 aspects in traditional manufacturing process system: (1) is concerning SH93 air-flow dries filament processing process system, the stability of cut tobacco supplied materials flow, moisture content is vital, because pipe tobacco only has 1-2 second drying time in the baking fiber tube road of SH93 air current type tobacco shred drying machine, within the so short time, moisture content of cut tobaccos to be dried to 12% from 26-28%, if supplied materials flow of tobacco or water ratio uniformity poor, directly will have influence on the stability of moisture content and the precision of tobacco leaf silk after drying.(2) although control type belt conveyer scale in Fig. 1 stabilizes the cut tobacco flow into super moisture-regaining tube, favourable to the control of super moisture-regaining tube warming and humidifying, but after super moisture-regaining tube, due to the rotation of ordering cylinder, pipe tobacco usually forms wave twisted state, cause the cut tobacco instability of flow directly entering SH93 air flow type cut tobacco drier after super super moisture-regaining tube, thus the crudy of rear cut tobacco is dried in impact; (3) directly enter SH93 air current type tobacco shred drying machine after cut tobacco discharging after super moisture-regaining tube, therefore just there is certain problem with fully complete permeability in the uniformity of the moisture content of the cut tobacco of warming and humidifying, thus affect product quality.Therefore, the product quality that the pneumatic drying of cut tobacco manufacturing process system how further optimization is current, raising SH93 air-flow dry silk just seems very necessary, must explore the manufacturing process system of the pneumatic drying of cut tobacco setting up optimization further.
Summary of the invention
In order to solve above-mentioned technical problem, the purpose of this utility model is to provide a kind of finished product cut tobacco production system adopting SH93 air flow type cut tobacco drier, this system achieves SH93 air-flow and dries the raising of silk moisture control precision and the obvious minimizing of over-dried cut tobacco amount, suitably improve cut tobacco Filling power simultaneously, improve the utilization rate of tobacco leaf.
In order to realize above-mentioned object, the utility model have employed following technical scheme:
Adopt a finished product cut tobacco production system for SH93 air flow type cut tobacco drier, this system comprises leaf storing cabinet, the first bin type feeding machine, the first control gauge line, the first control type belt conveyer scale, warming and humidifying cylinder, the second bin type feeding machine, filament cutter, the second bin type feeding machine, the second gauge line, the second control type belt conveyer scale, SH93 air flow type cut tobacco drier and winnowing machine on the spot successively; Moisture Meter is provided with between the first described control type belt conveyer scale and warming and humidifying cylinder, Moisture Meter and temperature measurer is provided with between warming and humidifying cylinder and the second bin type feeding machine, Moisture Meter is provided with between second control type belt conveyer scale and SH93 air flow type cut tobacco drier, SH93 air flow type cut tobacco drier and be provided with Moisture Meter and temperature measurer between winnowing machine on the spot, winnowing machine rear end, ground is also provided with Moisture Meter and temperature measurer.
As preferably, described warming and humidifying cylinder adopts hot blast temperature to be 80 DEG C.
As preferably, described filament cutter adopts Italian Garbuio Dickinson company SD508 filament cutter.
The utility model, owing to have employed above-mentioned technical scheme, has following feature:
1) before warming and humidifying cylinder being advanced to filament cutter, sheet cigarette carries out balancing water content at leaf storing cabinet, from leaf storing cabinet export sheet cigarette again through warming and humidifying cylinder, loose caking tobacco leaf, adopt hot blast temperature: 80 DEG C, after controlling warming and humidifying, outlet moisture content in leaves: 18.5 ~ 28.5 ± 1.0%, mouth tobacco leaf temperature: 45 ~ 55 ± 3 DEG C;
2) arrange the first bin type feeding machine before warming and humidifying cylinder and the first control type belt conveyer scale carries out accurate flow-control, accuracy of belt scale requires :≤0.5%;
3) high-moisture Qie Yesi technique is adopted.Selection can process the import Italy Garbuio Dickinson company SD508 filament cutter of high-moisture percentage tobacco leaf, cut cut tobacco moisture content: 26%-28%, tobacco cut width: 0.8 ~ 1.2 ± 0.1mm, qualification rate: >=99%, coordinate pipe tobacco cut to lengthen cutter in order to control chopping length, be conducive to minimizing agglomerating at pneumatic conveying drying link pipe tobacco.Flexible chopping, low cutter door pressure, runs sheet, caking is few; Especially chopping moisture content is maximum to 28%, can expand the adjustable extent of chopping moisture content greatly, is conducive to meeting the requirement of pneumatic conveying drying to feed moisture;
4) cut after rear pipe tobacco carries out accurate flow-control by the second bin type feeding machine and the second control type belt conveyer scale and directly enter SH93, make the flow of tobacco entering SH93 air flow type cut tobacco drier keep stable.The balance of the temporary link such as bin type feeding machine after cutting front bin type feeding machine, cutting of the tobacco leaf simultaneously after warming and humidifying, water ratio uniformity and permeability obtain certain guarantee.
The utility model operation result shows, compare after transformation with before transformation, after SH93 air-flow dries the baking of silk, moisture content of cut tobacco stability and control accuracy increase substantially, after processing AA brand dries silk cooling, moisture content of cut tobacco is criticized qualification rate and is brought up to 0.9983% by 0.9295%, the over-dried cut tobacco amount that cut-tobacco drier produces is criticized by 25.06kg/ and is reduced to 15.05kg/ and criticizes, Filling power brings up to 6.01cm3/g by 5.81cm3/g, and cut tobacco chopping quality also meets cigarette process specification.
Accompanying drawing explanation
Fig. 1 is the structural representation of finished product cut tobacco production system before transformation.
Fig. 2 is the structural representation of the utility model finished product cut tobacco production system.
Detailed description of the invention
Below in conjunction with accompanying drawing, detailed description of the invention of the present utility model is made a detailed explanation.
A kind of finished product cut tobacco production system adopting SH93 air flow type cut tobacco drier as shown in Figure 2, this system comprises leaf storing cabinet, the first bin type feeding machine, the first control gauge line, the first control type belt conveyer scale, warming and humidifying cylinder, the second bin type feeding machine, filament cutter, the second bin type feeding machine, the second gauge line, the second control type belt conveyer scale, SH93 air flow type cut tobacco drier and winnowing machine on the spot successively; Described warming and humidifying cylinder adopts hot blast temperature to be 80 DEG C, and described filament cutter adopts Italian Garbuio Dickinson company SD508 filament cutter.Moisture Meter is provided with between the first described control type belt conveyer scale and warming and humidifying cylinder, Moisture Meter and temperature measurer is provided with between warming and humidifying cylinder and the second bin type feeding machine, Moisture Meter is provided with between second control type belt conveyer scale and SH93 air flow type cut tobacco drier, SH93 air flow type cut tobacco drier and be provided with Moisture Meter and temperature measurer between winnowing machine on the spot, winnowing machine rear end, ground is also provided with Moisture Meter and temperature measurer.
The finished product cut tobacco production system that the utility model proposes, its course of work is: before the tobacco leaf of cigar mill enters leaf storing cabinet balance, operation adds feed liquid in tobacco leaf and moisture, then through the first bin type feeding machine, first gauge line, first control type belt conveyer scale, Moisture Meter, warming and humidifying cylinder, Moisture Meter, the equipment such as temperature measurer increase tobacco leaf temperature and moisture, enter the second bin type feeding machine afterwards, tobacco leaf is cut into cut tobacco by filament cutter (SD508), this cut tobacco enters the second bin type feeding machine, second gauge line, second control type belt conveyer scale, Moisture Meter, SH93 air flow type cut tobacco drier, Moisture Meter, the equipment such as temperature measurer remove the moisture in cut tobacco, again through winnowing machine on the spot, Moisture Meter, the moisture of cut tobacco and temperature control to and can carry out mixing the qualified finished product cut tobacco of joining by temperature measurer.
The utility model stablizes the cut tobacco flow and moisture content that enter SH93 air flow type cut tobacco drier, thus ensures the moisture content stability of drying the rear cut tobacco of silk cooling.Install and use rear actual production to prove, new SH93 air-flow dries silk technique to the raising of the moisture content stability and precision of drying the rear cut tobacco of silk cooling clearly, also obtain the raising of cut tobacco Filling power extraly, chopping quality also meets code requirement, refers to table 1, table 2, table 3, table 4 simultaneously.
After table 1 AA brand cigarette in 2013 dries silk cooling, moisture content of cut tobacco criticizes qualification rate average statistical form
As can be seen from Table 1, after transforming the cooling of latter 2013 annual baking silks, moisture content of cut tobacco criticizes qualification rate average is 0.9983.Raising 0.0688 compared with before transformation.
Table 2 AA brand cigarette in 2013 dries the rear cut tobacco over-dried cut tobacco amount statistical form of silk cooling
As can be seen from Table 2, the over-dried cut tobacco gross weight often criticized after transformation drops to 15.05Kg.The over-dried cut tobacco gross weight often criticized compared with before transformation have dropped 11.01Kg.
Table 3 AA brand cigarette in 2013 dries the rear cut tobacco Filling power statistical form of silk cooling
As can be seen from Table 3, after drying after transformation, cut tobacco Filling power is 6.01 cm3/g, improves 0.2cm3/g compared with before transformation, and after drying, the quality of cut tobacco improves further.
Table 4 AA brand cigarette tobacco leaf chopping (rod wax-200) measurement data statistical form
SD5 filament cutter adopts the high-moisture percentage chopping of 28% as can be seen from Table 4, chopping qualification rate
98.17%,chopping quality can meet process specification requirements.
The utility model transformation is forward and backward to be compared, the cut tobacco test result of production same brand shows, after SH93 air-flow dries, the moisture content stability of pipe tobacco improves, after processing AA brand cigarette dries silk cooling, moisture content of cut tobacco is criticized qualification rate and is brought up to 0.9983% by 0.9295%, raising 0.0688 compared with before transformation.The over-dried cut tobacco total amount often criticized is reduced to improved 15.05kg by the 25.06kg before transforming.Transform forward and backward Filling power to compare and improve 0.2cm3/g, after drying silk cooling, the quality of cut tobacco improves further, and improved new technology effect is obvious.
Claims (3)
1. adopt a finished product cut tobacco production system for SH93 air flow type cut tobacco drier, it is characterized in that: this system comprises leaf storing cabinet, the first bin type feeding machine, the first control gauge line, the first control type belt conveyer scale, warming and humidifying cylinder, the second bin type feeding machine, filament cutter, the second bin type feeding machine, the second gauge line, the second control type belt conveyer scale, SH93 air flow type cut tobacco drier and winnowing machine on the spot successively; Moisture Meter is provided with between the first described control type belt conveyer scale and warming and humidifying cylinder, Moisture Meter and temperature measurer is provided with between warming and humidifying cylinder and the second bin type feeding machine, Moisture Meter is provided with between second control type belt conveyer scale and SH93 air flow type cut tobacco drier, SH93 air flow type cut tobacco drier and be provided with Moisture Meter and temperature measurer between winnowing machine on the spot, winnowing machine rear end, ground is also provided with Moisture Meter and temperature measurer.
2. a kind of finished product cut tobacco production system adopting SH93 air flow type cut tobacco drier according to claim 1, is characterized in that: warming and humidifying cylinder adopts hot blast temperature to be 80 DEG C.
3. a kind of finished product cut tobacco production system adopting SH93 air flow type cut tobacco drier according to claim 1, is characterized in that: filament cutter adopts Italian Garbuio Dickinson company SD508 filament cutter.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420613408.1U CN204191559U (en) | 2014-10-22 | 2014-10-22 | A kind of finished product cut tobacco production system adopting SH93 air flow type cut tobacco drier |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420613408.1U CN204191559U (en) | 2014-10-22 | 2014-10-22 | A kind of finished product cut tobacco production system adopting SH93 air flow type cut tobacco drier |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204191559U true CN204191559U (en) | 2015-03-11 |
Family
ID=52649582
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201420613408.1U Active CN204191559U (en) | 2014-10-22 | 2014-10-22 | A kind of finished product cut tobacco production system adopting SH93 air flow type cut tobacco drier |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN204191559U (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110013044A (en) * | 2019-04-29 | 2019-07-16 | 贵州中烟工业有限责任公司 | A method of barrel temperature is obtained by calculating KLD-2 cut-tobacco drier dehydrating amount |
| CN113273713A (en) * | 2021-06-29 | 2021-08-20 | 厦门烟草工业有限责任公司 | Tobacco shred production system and tobacco material moisture content control method |
| CN114601190A (en) * | 2022-03-21 | 2022-06-10 | 红塔烟草(集团)有限责任公司 | Method for regulating and controlling drying moisture of slice threads |
| CN115363238A (en) * | 2022-08-24 | 2022-11-22 | 龙岩烟草工业有限责任公司 | Method and device for controlling production flow of filament cutter and computer equipment |
-
2014
- 2014-10-22 CN CN201420613408.1U patent/CN204191559U/en active Active
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110013044A (en) * | 2019-04-29 | 2019-07-16 | 贵州中烟工业有限责任公司 | A method of barrel temperature is obtained by calculating KLD-2 cut-tobacco drier dehydrating amount |
| CN113273713A (en) * | 2021-06-29 | 2021-08-20 | 厦门烟草工业有限责任公司 | Tobacco shred production system and tobacco material moisture content control method |
| CN113273713B (en) * | 2021-06-29 | 2022-09-16 | 厦门烟草工业有限责任公司 | Tobacco shred production system and tobacco material moisture content control method |
| CN114601190A (en) * | 2022-03-21 | 2022-06-10 | 红塔烟草(集团)有限责任公司 | Method for regulating and controlling drying moisture of slice threads |
| CN115363238A (en) * | 2022-08-24 | 2022-11-22 | 龙岩烟草工业有限责任公司 | Method and device for controlling production flow of filament cutter and computer equipment |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN204191559U (en) | A kind of finished product cut tobacco production system adopting SH93 air flow type cut tobacco drier | |
| CN101396167B (en) | Industrialization production method of pipe tobacco | |
| CN104770844B (en) | A kind of stem that improves mixes the method joining precision | |
| CN103126045B (en) | A kind for the treatment of process for improving aromatic tobacco sensory quality | |
| CN105167154A (en) | Novel method for preparing reconstituted tobacco by virtue of papermaking process | |
| CN103383541A (en) | Moisture regaining feed-forward control method based on supplied material water content differences | |
| CN106108098A (en) | A kind of thin short cabo expansion restructuring throwing processing technique | |
| CN109875097A (en) | It is a kind of to heat the preparation method that do not burn with dry process reproduction tobacco leaf | |
| CN104770852B (en) | It is applicable to the independent technology for making tobacco threds of papermaking-method reconstituted tobaccos production factory | |
| CN103704865A (en) | Technology for cigarette production | |
| CN105167161A (en) | Fine grouped processing method for tobacco stems | |
| CN105077563A (en) | Processing method for pre-pressing threshed and re-dried tobacco stems and producing cut stems | |
| CN103315382B (en) | Cascaded PID based charging moisture control device in tobacco shred processing technology | |
| CN101444328A (en) | A cut rolled stem processing procedure | |
| CN105520186A (en) | Method for optimizing cut tobacco structure by improving structure and shape of threshed and re-dried tobacco leaves | |
| CN102217778A (en) | Method for improving using value of tobacco leaf raw material through cigarette processing | |
| CN102240063B (en) | Method for stabilizing parameters of annular shred dryer through parallel translation of water ratio | |
| CN101856140B (en) | Tobacco charging process | |
| CN101263927A (en) | Tobacco process secondary charging technique | |
| CN110326810A (en) | A kind of process of first-class cigarette beating and double roasting upgrading synergy | |
| CN104770846B (en) | A kind of raising is reproduced cut tobacco and mixes the method for joining precision | |
| CN114304704B (en) | Method for ordering disordered cut tobacco of heated cigarette | |
| CN103892431A (en) | Leaf-cutting based threshing and redrying process capable of improving uniformity of smoke sheet structures | |
| CN108703400A (en) | A kind of leaf thread material feeding process | |
| CN202941402U (en) | Manufacturing device of filter tip without wrap paper |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant |