CN114601190A - Method for regulating and controlling drying moisture of slice threads - Google Patents
Method for regulating and controlling drying moisture of slice threads Download PDFInfo
- Publication number
- CN114601190A CN114601190A CN202210276625.5A CN202210276625A CN114601190A CN 114601190 A CN114601190 A CN 114601190A CN 202210276625 A CN202210276625 A CN 202210276625A CN 114601190 A CN114601190 A CN 114601190A
- Authority
- CN
- China
- Prior art keywords
- moisture
- cut
- airflow
- tobacco
- drying
- 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.)
- Granted
Links
Images
Classifications
-
- 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
Landscapes
- Manufacture Of Tobacco Products (AREA)
Abstract
The invention provides a method for regulating and controlling the dry moisture of thin slices, wherein a first moisture meter collects the feed moisture of the thin slices of a leaf-silk damping machine and transmits the collected data to an atomization water-adding control module; the atomized water adding control module adjusts the water adding flow of the cut tobacco conditioner to be 60kg/h-200kg/h, and converts the water adding flow into a stable control program of PID outlet water feedback control of the cut tobacco conditioner after the water adding flow lasts for 10s-60 s; the second moisture meter collects the moisture of the thin slice filament feeding of the air flow filament dryer and transmits the collected data to the air flow drying strength control module; the airflow drying strength control module reduces the temperature and the air quantity of hot air, reduces the frequency of a moisture exhaust fan and reduces the heat value of the airflow cut tobacco dryer. The invention adopts the methods of water feedforward and low-temperature processing control, greatly reduces the proportion of the dry materials of the stub bar of the slice thread, reduces the dry materials of the stub bar by nearly 70 percent, improves the processing identity of partial materials of the stub bar and the whole batch, and improves the quality of cigarette products.
Description
Technical Field
The invention relates to the technical field of a tobacco shred making process in tobacco processing, in particular to a method for regulating and controlling the drying moisture of thin slices.
Background
In the tobacco industry, the conventional water control technology has a good effect on common cut tobacco, but because the cut tobacco has the characteristic of rapid water absorption and water loss, the conventional technologies cannot meet the requirements of the novel process when the material characteristics are changed. After the cut tobacco drying is finished, the drying moisture of the stub cut thin slices in a certain proportion does not meet the requirement, and when the thin slices are mixed into the cut tobacco, the influence on the product quality of cigarettes, particularly the smoking taste, is large.
In the prior art, when a deviation between actual moisture and a set value of cut tobacco is detected by a cut tobacco outlet moisture meter, a PID controller corrects a water adding initial value, but for the cut tobacco of a stub bar, because no outlet moisture exists at the beginning, feedback control cannot be carried out, so that serious hysteresis exists, and the moisture content of the cut tobacco of a certain proportion does not meet the requirement.
The existing control parameters and working time of the roller airflow cut-tobacco drier are designed aiming at steady-state materials, the flow of stub bar materials is small, the existing control parameters can cause the processing strength of equipment to be not matched with the flow of the stub bar, and finally the stub bar materials are excessively dehydrated, so that the problem of pertinently researching the moisture control of the stub bar of the slice shreds is needed on the basis of the original moisture control technology according to the characteristics of the slice shreds.
SUMMARY OF THE PATENT FOR INVENTION
In order to solve the technical problems, the invention provides a method for regulating and controlling the drying moisture of thin-sheet threads, which adopts a method of moisture feedforward and low-temperature processing control to strengthen the moisture retention of materials in the initial feeding stage of the thin-sheet threads and reduce the moisture loss at the same time, thereby improving the moisture content of a stub bar of the thin-sheet threads, reducing the material proportion of the stub bar with lower moisture content of the thin-sheet threads, and improving the processing identity of partial materials of the stub bar and the whole batch.
The technical scheme adopted by the invention for solving the technical problems is as follows:
a method for regulating and controlling the drying moisture of thin slices adopts a regulating and controlling device for the drying moisture of the thin slices to process, the regulating and controlling device comprises a cut leaf moisture regaining machine and an airflow cut tobacco drying machine, the cut leaf moisture regaining machine is used for heating and humidifying cut leaves, and the airflow cut tobacco drying machine is arranged at the downstream of the cut leaf moisture regaining machine and is used for drying the cut leaves;
a first moisture meter is arranged at the inlet of the cut tobacco conditioning machine and used for collecting the material moisture at the inlet of the cut tobacco conditioning machine;
a second moisture meter is arranged at the inlet of the airflow cut-tobacco drier and used for collecting the material moisture at the inlet of the airflow cut-tobacco drier;
a third moisture meter is arranged at the outlet of the airflow cut-tobacco drier and used for collecting the material moisture at the outlet of the airflow cut-tobacco drier;
the cut tobacco conditioning machine is provided with an atomization water adding control module which is used for receiving data collected by the first moisture meter and the second moisture meter and controlling the material moisture in the cut tobacco conditioning machine;
the airflow cut-tobacco drier is provided with an airflow drying strength control module which is used for receiving data collected by the second moisture meter and the third moisture meter and controlling the drying strength of the material in the airflow cut-tobacco drier;
the method specifically comprises the following steps:
s1: the first moisture meter collects the feed moisture of the thin sheet wires of the leaf wire conditioner and transmits the collected data to the atomization water adding control module;
s2: the atomization water adding control module adjusts the water adding amount of the cut tobacco conditioning machine, and specifically comprises the following steps:
when the first moisture meter detects that the moisture of the material at the inlet of the cut tobacco conditioning machine is 16-19%, the atomization water adding control module adjusts the water adding flow to be 60-200 kg/h, the delay working time is 10-30 s, and the duration time is 10-60 s;
s3: the control program of the atomization water adding control module is converted into a control program of the PID outlet moisture feedback control of the steady-state cut tobacco conditioning machine;
s4: the second moisture meter collects the moisture of the thin slice filament feeding of the air flow filament dryer and transmits the collected data to the air flow drying strength control module;
s5: the airflow drying strength control module adjusts the drying strength of the materials in the airflow cut-tobacco drier at the stub bar stage, and specifically comprises the following steps:
and when the second moisture meter detects that the moisture of the material at the inlet of the airflow cut-tobacco drier is 20-24%, reducing the heat value of the airflow cut-tobacco drier.
Further, the method for reducing the heat value of the airflow cut-tobacco drier comprises the following steps:
s51, reducing the heat value of the airflow cut tobacco dryer by using simulated water, and adjusting the flow of the simulated water to 50kg/h-180 kg/h;
s52, the working duration of the simulated water is within 30min, and when the second moisture meter detects that the moisture value of the incoming material reaches 6%, the simulated water stops working;
s53, adjusting the opening degree of a hot air damper, reducing the temperature by 5-10 ℃, simultaneously reducing the frequency of a moisture exhaust fan by 5-50%, simultaneously reducing the air quantity by 5-15%, wherein the time delay of the combined action is 5-10S, and the duration is 10-60S;
and S54, converting the control program of the airflow drying strength control module into a control program of PID (proportion integration differentiation) outlet moisture feedback control of the airflow cut-tobacco drier in a steady state.
Furthermore, the airflow drying strength control module comprises a simulated water control unit, a hot air control unit, a moisture exhaust fan control unit and an air flow control unit, and the simulated water and the hot air flow are respectively controlled and adjusted.
Further, the outlet moisture of the steady-state tobacco shred damping machine PID outlet moisture feedback control is the material moisture collected by the second moisture meter.
Further, the outlet moisture of the steady-state airflow cut-tobacco drier PID outlet moisture feedback control is the material moisture collected by the third moisture meter.
Furthermore, the regulating device also comprises a slice shred cutting machine arranged at the upstream of the cut tobacco conditioning machine and a slice shred storage cabinet arranged at the downstream of the airflow shred drying machine.
Further, the cut tobacco moisture regaining machine is a drum-type cut tobacco moisture regaining machine, and the airflow cut tobacco drying machine is a drum-type airflow cut tobacco drying machine.
Compared with the prior art, the invention has the beneficial effects that:
1. by adopting the method of water feedforward and low-temperature processing control, the proportion of the dry materials of the stub bar of the slice thread is greatly reduced, the dry materials of the stub bar are reduced by nearly 70 percent, and the processing identity of partial materials of the stub bar and the whole batch is improved.
2. The quality of cigarette products is improved, and each batch of slice shreds avoids influencing the sensory quality of finished cigarettes through regulating and controlling the moisture of the material at the stub bar of the slice shreds.
Drawings
FIG. 1 is a schematic structural diagram of a device for controlling the drying moisture of thin sheet yarns according to the present invention.
FIG. 2 is a flow chart of the method for controlling the drying moisture of the thin slice threads.
In the figure: 1-leaf shred conditioning machine; 11-an atomized water adding control module; 2-airflow cut tobacco drier; 21-airflow drying strength control module; 211-analog water control unit; 212-a hot air control unit; 213-moisture exhausting fan control unit; 214-air volume control unit; 31-a first moisture meter; 32-a second moisture meter; 33-a third moisture meter; 4-slice and silk cutting machine; 5-thin slice silk storing cabinet.
Detailed Description
In order to make the objects, technical solutions and advantages of the present invention more apparent, the present invention is further described in detail below with reference to the accompanying drawings and examples.
The invention provides a method for regulating and controlling the drying moisture of thin slices, which adopts a regulating and controlling device for the drying moisture of the thin slices to process. As shown in fig. 1, the regulating device includes a cut tobacco conditioner 1, an air-flow cut tobacco dryer 2, a cut sheet tobacco cutter 4 disposed at the upstream of the cut tobacco conditioner 1, and a cut sheet tobacco storage cabinet 5 disposed at the downstream of the air-flow cut tobacco dryer 2, wherein the cut tobacco conditioner 1 is used for heating and humidifying cut tobacco, and the air-flow cut tobacco dryer 2 is disposed at the downstream of the cut tobacco conditioner 1 and used for drying cut tobacco. Preferably, the cut tobacco conditioner 1 is a drum-type cut tobacco conditioner 1, and the airflow cut tobacco dryer 2 is a drum-type airflow cut tobacco dryer 2. The slice silk cutting machine 4 cuts the slices into slice silks with the width meeting the technological requirements, and after the slices are cut into slices, slice silk finished products are obtained after the procedures of leaf silk dampening, air flow silk drying and the like, and the slice silks are stored in a slice silk storage cabinet 5.
The first moisture meter 31 is arranged at the inlet of the cut tobacco conditioning machine 1 and used for collecting material moisture at the inlet of the cut tobacco conditioning machine 1, so that moisture feedforward control of the cut tobacco conditioning machine 1 is realized, and the material moisture can be detected at the initial feeding stage of thin slices. And a second moisture meter 32 is arranged at the inlet of the airflow cut-tobacco drier 2 and is used for collecting the material moisture at the inlet of the airflow cut-tobacco drier 2 and the material moisture at the outlet of the cut-tobacco resurgence machine 1. And a third moisture meter 33 is arranged at the outlet of the airflow cut-tobacco drier 2 and is used for collecting the moisture of the material at the outlet of the airflow cut-tobacco drier 2 and determining whether the material dried by the airflow cut-tobacco drier 2 is dry material. The cut tobacco resurfacing machine 1 is provided with an atomization water adding control module 11 for receiving data collected by a first moisture meter 31 and a second moisture meter 32 and controlling the material moisture in the cut tobacco resurfacing machine 1, so that the material meets the process requirement of the expansion function of cut tobacco drying equipment. The airflow cut-tobacco drier 2 is provided with an airflow drying strength control module 21 for receiving data collected by the second moisture meter 32 and controlling the drying strength of the materials in the airflow cut-tobacco drier 2.
The method for regulating and controlling the drying moisture of the thin slices specifically comprises the following steps:
s1: the first moisture meter 31 collects the feed moisture of the thin sheet wires of the leaf wire conditioning machine 1 and transmits the collected data to the atomization water adding control module 11;
s2: the atomization water adding control module 11 adjusts the water adding amount of the cut tobacco conditioning machine 1, and specifically comprises the following steps:
when the first moisture meter 31 detects that the moisture of the material at the inlet of the cut tobacco conditioning machine 1 is 16-19%, the atomization water adding control module 11 adjusts the water adding flow to be 60-200 kg/h, the delay working time is 10-30 s, and the duration is 10-60 s;
s3: the control program of the atomized water adding control module 11 is converted into a control program of the PID outlet water feedback control of the steady-state cut tobacco conditioning machine;
s4: the second moisture meter 32 collects the moisture of the thin sheet wire fed by the airflow cut-tobacco drier 2 and transmits the collected data to the airflow drying strength control module 21;
s5: the airflow drying strength control module 21 adjusts the drying strength of the material in the airflow cut-tobacco drier 2 at the stub bar stage, and specifically comprises the following steps:
when the second moisture meter 32 detects that the moisture of the material at the inlet of the airflow cut-tobacco drier 2 is 20-24%, the heat value of the airflow cut-tobacco drier 2 is reduced.
Referring to fig. 1 and 2, the thin slice filament cutting machine 4 cuts the thin slice filaments into thin slice filaments with the width meeting the process requirement and then sends the thin slice filaments to the cut leaf filament conditioning machine 1, a first moisture meter 31 is arranged at the inlet of the cut leaf filament conditioning machine 1, and when the material is sent to the position of the first moisture meter 31, the first moisture meter 31 detects the moisture of the material, which indicates that the material starts to be fed. Under the condition of stable material flow, the moisture of the material at the inlet of the cut tobacco conditioning machine 1 is generally above 19%, and the moisture of the material head is generally in the interval of 16-19%. Therefore, when the first moisture meter 31 detects that the moisture content of the material at the inlet of the cut tobacco conditioning machine 1 is 16% -19%, the acquired data are sent to the atomization water adding control module 11, after the delay of 10s-30s, the atomization water adding control module 11 adjusts the water adding flow to be 60kg/h-200kg/h and the duration to be 10s-60s, and then the control is converted into the PID outlet moisture feedback control of the steady-state cut tobacco conditioning machine. Because the first moisture meter 31 is a certain distance away from the cut tobacco conditioning machine 1, a period of time is needed from the detection point to the processing point, when the first moisture meter 31 detects that the moisture of the material is 16% -19%, the atomization water adding control module 11 does not need to respond immediately, and works after the time delay is 10-30 s. When partial material at the material head passes through the cut tobacco conditioner 1, the material flow reaches a stable state, and then the stable state is converted to the PID outlet moisture feedback control of the cut tobacco conditioner, the atomization water adding control module 11 receives the data collected by the second moisture meter 32, and the PID controller of the cut tobacco conditioner 1 controls the material moisture in the cut tobacco conditioner 1 according to the material moisture collected by the second moisture meter 32.
The thin slices are heated and humidified in the leaf shred damping machine 1, and then are conveyed to the air flow shred drying machine 2 for drying. When the second moisture meter 32 at the inlet of the airflow cut-tobacco drier 2 detects that the moisture of the material at the inlet of the airflow cut-tobacco drier 2 is 20% -24%, the airflow drying strength control module 21 reduces the heat value of the airflow cut-tobacco drier 2 according to the moisture value collected by the second moisture meter 32. Specifically, the method for reducing the heat value of the airflow cut-tobacco drier 2 comprises the following steps:
s51, reducing the heat value of the airflow cut-tobacco drier 2 by using simulated water, and adjusting the simulated water flow to 50kg/h-180 kg/h;
s52, the working duration of the simulated water is within 30min, and when the second moisture meter 32 detects that the moisture value of the incoming material reaches 6%, the simulated water stops working;
s53, adjusting the opening degree of a hot air door, reducing the temperature by 5-10 ℃, simultaneously reducing the frequency of a moisture exhaust fan by 5-50%, simultaneously reducing the air quantity by 5-15%, wherein the time delay of the combined action is 5-10S, and the duration is 10-60S;
and S54, converting the control program of the airflow drying strength control module 21 into a control program of PID (proportion integration differentiation) outlet moisture feedback control of the airflow cut-tobacco drier in a steady state.
The airflow drying strength control module 21 includes a simulated water control unit 211, a hot air control unit 212, a moisture exhaust fan control unit 213, and an air volume control unit 214, which respectively control and adjust the simulated water and the hot air flow. When there is material in the air flow cut tobacco dryer 2, the simulated water is not available in the process, therefore, the simulated water is generally used with hot air under the condition that the equipment is standby or the batch equipment has no material. Because the air flow drying strength control module 21 needs to perform a series of work when being stopped and started, which consumes more time and affects the production progress, generally, under the conditions that the equipment is standby for a short time and no material exists in batches, the air flow drying strength control module 21 can be continuously in a working state.
Before the materials enter the airflow cut-tobacco drier 2, within 30min, the simulated water control unit 211 works, the simulated water is used for reducing the heat value of the roller airflow cut-tobacco drier 2 or keeping the heat value of the roller airflow cut-tobacco drier 2 relatively lower, and the simulated water flow is 50kg/h-180 kg/h. When the second moisture meter 32 detects that the moisture value of the incoming material reaches 6%, it indicates that the material starts to enter the airflow cut-tobacco drier 2, the use of the simulated water is stopped, the processing intensity of the equipment is reduced, and the low-temperature processing control is performed. The hot air control unit 212 adjusts the opening degree of a hot air damper and reduces the temperature of hot air for drying materials by 5-10 ℃; meanwhile, the moisture exhaust fan control unit 213 reduces the frequency of the moisture exhaust fan by 5% -50%; the air volume control unit 214 also simultaneously reduces the hot air volume by 5-15%. The delay time of the combined action of the hot air control unit 212, the moisture exhaust fan control unit 213 and the air control unit 214 is 5s-10s, the duration time is 10s-60s, and then the control is converted into the PID outlet moisture feedback control of the steady airflow cut-tobacco drier. At this time, the material at the head of the material passes through the airflow cut-tobacco drier 2, the material flow rate reaches a stable state, and the PID controller of the airflow cut-tobacco drier 2 controls the material processing strength in the airflow cut-tobacco drier 2 according to the material moisture collected by the third moisture meter 33.
The weight of three batches of the dry material of the chip scrap processed according to the above method was counted and compared with the weight of three batches of the dry material of the chip scrap not processed according to the above method, and the results are shown in table 1:
TABLE 1 comparison table of the weight of dry materials processed by the method for controlling the dry moisture of thin slices according to the present invention and the method for controlling the dry moisture of thin slices not according to the present invention
In table 1, the weight of the dry material is the weight of the dry material measured according to the cigarette technical code. According to the requirements of the cigarette technical specification, the material with the moisture content smaller than the standard moisture content (the set value of moisture) by more than 2.5 percent is called as the dry material after the thin slices are dried by the airflow cut-tobacco drier 2. For example, a moisture set point of 10% is 2.5% or more less than 10%, i.e., a material having a moisture content of less than 7.5% is a "dry material".
As shown in Table 1, after the method for regulating and controlling the drying moisture of the thin slice threads is adopted, the weight of dry materials of the stub bar of the thin slice threads is greatly reduced, and the quality of the materials is effectively improved.
The above description is only for the purpose of illustrating the preferred embodiments of the present invention and is not to be construed as limiting the invention, and any modifications, equivalents, improvements and the like that fall within the spirit and principle of the present invention are intended to be included therein.
Claims (7)
1. A method for regulating and controlling the drying moisture of thin slices is characterized in that a regulating and controlling device for the drying moisture of the thin slices is adopted for processing, the regulating and controlling device comprises a cut leaf moisture regaining machine and an airflow cut tobacco drying machine, the cut leaf moisture regaining machine is used for heating and humidifying cut leaves, and the airflow cut tobacco drying machine is arranged at the downstream of the cut leaf moisture regaining machine and is used for drying the cut leaves;
a first moisture meter is arranged at the inlet of the cut tobacco conditioning machine and used for collecting the material moisture at the inlet of the cut tobacco conditioning machine;
a second moisture meter is arranged at the inlet of the airflow cut-tobacco drier and used for collecting the material moisture at the inlet of the airflow cut-tobacco drier;
a third moisture meter is arranged at the outlet of the airflow cut-tobacco drier and used for collecting the material moisture at the outlet of the airflow cut-tobacco drier;
the cut tobacco conditioning machine is provided with an atomization water adding control module for receiving data collected by the first moisture meter and the second moisture meter;
the airflow cut-tobacco drier is provided with an airflow drying strength control module for receiving data collected by the second moisture meter and the third moisture meter;
the method specifically comprises the following steps:
s1: the first moisture meter collects the feed moisture of the thin cut tobacco of the cut tobacco conditioner and transmits the collected data to the atomization water adding control module;
s2: the atomization water adding control module adjusts the water adding amount of the cut tobacco conditioning machine, and specifically comprises the following steps:
when the first moisture meter detects that the moisture of the material at the inlet of the cut tobacco conditioning machine is 16-19%, the atomization water adding control module adjusts the water adding flow to be 60-200 kg/h, the delay working time is 10-30 s, and the duration time is 10-60 s;
s3: the control program of the atomization water adding control module is converted into a control program of the PID outlet moisture feedback control of the steady-state cut tobacco conditioning machine;
s4: the second moisture meter collects the moisture of the thin slice filament feeding of the air flow filament dryer and transmits the collected data to the air flow drying strength control module;
s5: the airflow drying strength control module adjusts the drying strength of the materials in the airflow cut-tobacco drier at the stub bar stage, and specifically comprises the following steps:
and when the second moisture meter detects that the moisture of the material at the inlet of the airflow cut-tobacco drier is 20-24%, reducing the heat value of the airflow cut-tobacco drier.
2. The method of controlling sheet wire drying moisture content according to claim 1, wherein the method of reducing the heating value of the air-jet dryer comprises the steps of:
s51, reducing the heat value of the airflow cut tobacco dryer by using simulated water, and adjusting the flow of the simulated water to 50kg/h-180 kg/h;
s52, the working duration of the simulated water is within 30min, and when the second moisture meter detects that the moisture value of the incoming material reaches 6%, the simulated water stops working;
s53, adjusting the opening degree of a hot air door, reducing the temperature by 5-10 ℃, simultaneously reducing the frequency of a moisture exhaust fan by 5-50%, simultaneously reducing the air quantity by 5-15%, wherein the time delay of the combined action is 5-10S, and the duration is 10-60S;
and S54, converting the control program of the airflow drying strength control module into a control program of PID (proportion integration differentiation) outlet moisture feedback control of the airflow cut-tobacco drier in a steady state.
3. The method for regulating and controlling the drying moisture of the thin sheet yarns according to claim 1 or 2, wherein the airflow drying strength control module comprises a simulated water control unit, a hot air control unit, a moisture exhaust fan control unit and an air flow control unit, and the simulated water and the hot air flow are respectively controlled and regulated.
4. The method for regulating and controlling the dry moisture of the thin sheet silk according to claim 1, wherein the outlet moisture of the PID outlet moisture feedback control of the steady-state tobacco shred damping machine is the material moisture collected by the second moisture meter.
5. The method for controlling the drying moisture of the thin sheet threads according to claim 2, wherein the outlet moisture of the PID outlet moisture feedback control of the steady airflow thread dryer is the material moisture collected by a third moisture meter.
6. The method of conditioning thin-sheet silk dry moisture according to claim 1, wherein the conditioning device further comprises a thin-sheet silk cutting machine disposed upstream of the leaf-silk conditioning machine and a thin-sheet silk storage cabinet disposed downstream of the air-flow cut-sheet silk drying machine.
7. The method of controlling dry moisture content of thin sheet threads according to claim 1, wherein the leaf thread conditioner is a drum-type leaf thread conditioner, and the air-jet cut-thread dryer is a drum-type air-jet cut-thread dryer.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202210276625.5A CN114601190B (en) | 2022-03-21 | 2022-03-21 | Method for regulating and controlling drying moisture of slice threads |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202210276625.5A CN114601190B (en) | 2022-03-21 | 2022-03-21 | Method for regulating and controlling drying moisture of slice threads |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN114601190A true CN114601190A (en) | 2022-06-10 |
| CN114601190B CN114601190B (en) | 2023-04-11 |
Family
ID=81864193
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202210276625.5A Active CN114601190B (en) | 2022-03-21 | 2022-03-21 | Method for regulating and controlling drying moisture of slice threads |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN114601190B (en) |
Citations (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB1504647A (en) * | 1975-10-02 | 1978-03-22 | Tobacco Res & Dev | Drying method and apparatus |
| CN103202528A (en) * | 2013-04-10 | 2013-07-17 | 湖南中烟工业有限责任公司 | Cut lamina drying control method and cut lamina drying system based on feedforward and feedback of HT moisture compensation |
| CN204191559U (en) * | 2014-10-22 | 2015-03-11 | 浙江中烟工业有限责任公司 | A kind of finished product cut tobacco production system adopting SH93 air flow type cut tobacco drier |
| CN104432456A (en) * | 2014-10-30 | 2015-03-25 | 陕西中烟工业有限责任公司 | High-yield cut tobacco drying method |
| CN106036975A (en) * | 2016-06-29 | 2016-10-26 | 河南中烟工业有限责任公司 | Cut tobacco drying moisture stabilizing device and cut tobacco drying moisture stabilizing method |
| CN205962799U (en) * | 2016-06-29 | 2017-02-22 | 河南中烟工业有限责任公司 | A stable moisture device that dries by fire |
| CN108236125A (en) * | 2016-12-23 | 2018-07-03 | 红塔烟草(集团)有限责任公司 | A kind of baking silk method of cut tobacco over-dried cut tobacco amount after reduction EVA pneumatic conveying dryings |
| CN112021641A (en) * | 2020-07-10 | 2020-12-04 | 张家口卷烟厂有限责任公司 | On-line moisture meter calibration system and method for tobacco shred production link |
-
2022
- 2022-03-21 CN CN202210276625.5A patent/CN114601190B/en active Active
Patent Citations (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB1504647A (en) * | 1975-10-02 | 1978-03-22 | Tobacco Res & Dev | Drying method and apparatus |
| CN103202528A (en) * | 2013-04-10 | 2013-07-17 | 湖南中烟工业有限责任公司 | Cut lamina drying control method and cut lamina drying system based on feedforward and feedback of HT moisture compensation |
| CN204191559U (en) * | 2014-10-22 | 2015-03-11 | 浙江中烟工业有限责任公司 | A kind of finished product cut tobacco production system adopting SH93 air flow type cut tobacco drier |
| CN104432456A (en) * | 2014-10-30 | 2015-03-25 | 陕西中烟工业有限责任公司 | High-yield cut tobacco drying method |
| CN106036975A (en) * | 2016-06-29 | 2016-10-26 | 河南中烟工业有限责任公司 | Cut tobacco drying moisture stabilizing device and cut tobacco drying moisture stabilizing method |
| CN205962799U (en) * | 2016-06-29 | 2017-02-22 | 河南中烟工业有限责任公司 | A stable moisture device that dries by fire |
| CN108236125A (en) * | 2016-12-23 | 2018-07-03 | 红塔烟草(集团)有限责任公司 | A kind of baking silk method of cut tobacco over-dried cut tobacco amount after reduction EVA pneumatic conveying dryings |
| CN112021641A (en) * | 2020-07-10 | 2020-12-04 | 张家口卷烟厂有限责任公司 | On-line moisture meter calibration system and method for tobacco shred production link |
Non-Patent Citations (6)
| Title |
|---|
| 仝智强: "逆流式滚筒烘丝机干头干尾控制的一种方法", 《科技信息》 * |
| 叶宏音: "薄板烘丝机精准化控制技术研究", 《现代农业科技》 * |
| 李永杰等: "SH93型气流式叶丝气流干燥设备的出口水分稳定性改进", 《企业科技与发展》 * |
| 王根旺: "SH9型叶丝气流干燥系统过程控制能力的改进", 《广西轻工业》 * |
| 许世民: "梗丝低速气流干燥机SH23B控制特点及应用存在问题", 《工程技术研究》 * |
| 赵彬等: "SH947型管道式烘丝机模拟运行参数的优化", 《烟草科技》 * |
Also Published As
| Publication number | Publication date |
|---|---|
| CN114601190B (en) | 2023-04-11 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN108308691A (en) | A method of promoting tobacco scrap prodn quality stability | |
| CN1554293A (en) | New Process for producing tobacco shred | |
| CN106773657B (en) | A kind of optimising and adjustment method of roller drying unstable state process head material and tailing stage | |
| CN110013044B (en) | Method for obtaining barrel temperature by calculating dehydration amount of KLD-2 cut-tobacco drier | |
| CN102972856A (en) | Novel production process for cut tobacco stems | |
| CN114601190B (en) | Method for regulating and controlling drying moisture of slice threads | |
| CN208850665U (en) | One kind being used for tobacco sheet cigarette loosening steam conditioner hot blast temperature control device | |
| CN103610226A (en) | Moisture content controlling method for tobacco airflow drying | |
| CN112790418A (en) | Water adding control method and system for super moisture regain of cut tobacco | |
| JPH09163965A (en) | Processing of tobacco leaf and plant to manufacture pipe tobacco | |
| CN106036975B (en) | A kind of stable method for drying silk moisture | |
| CN108208902B (en) | Process gas temperature control method for airflow type cut tobacco dryer | |
| CN104664583A (en) | Novel fluidized bed type heating and humidifying machine for tobacco shred preparation from tobacco leaves | |
| CN110916236A (en) | Method for reducing agglomeration rate in air-flow type leaf shred drying process | |
| CN110850836A (en) | Quantitative control method for water content of outlet material of tunnel type heating and humidifying equipment | |
| CN1107461C (en) | In-line alcoholizing process for tbacco | |
| CN110771930B (en) | Control method for realizing consistency of redrying strength between batches of tobacco leaves of same grade | |
| CN114304704A (en) | Method for ordering disordered cut tobacco of heated cigarette | |
| CN113576017B (en) | Cut tobacco drying water control method | |
| CN204482997U (en) | For the Novel fluidization bed warming and humidifying machine of tobacco scrap prodn | |
| CN113040412A (en) | Intelligent control method and device for roller airflow cut-tobacco drier | |
| CN116225109B (en) | Yarn moisture regain control method and system | |
| CN108236125B (en) | Cut tobacco drying method for reducing dry head and dry tail of cut tobacco dried by EVA airflow | |
| CN112826120B (en) | Feed-forward control method and system for airflow type cut tobacco drying | |
| CN215531535U (en) | Air-flow type cut tobacco dryer |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PB01 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| GR01 | Patent grant | ||
| GR01 | Patent grant |