CN110150710A - A method of cigarette pipe tobacco is prepared by tobacco leaf or raw material pipe tobacco - Google Patents
A method of cigarette pipe tobacco is prepared by tobacco leaf or raw material pipe tobacco Download PDFInfo
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- CN110150710A CN110150710A CN201910358544.8A CN201910358544A CN110150710A CN 110150710 A CN110150710 A CN 110150710A CN 201910358544 A CN201910358544 A CN 201910358544A CN 110150710 A CN110150710 A CN 110150710A
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- Prior art keywords
- tobacco
- pipe tobacco
- temperature
- cigarette
- smoke agent
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Classifications
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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
- A24B15/00—Chemical features or treatment of tobacco; Tobacco substitutes, e.g. in liquid form
- A24B15/18—Treatment of tobacco products or tobacco substitutes
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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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- 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
- A24B3/06—Loosening tobacco leaves or cut tobacco
-
- 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
- A24B3/14—Forming reconstituted tobacco products, e.g. wrapper materials, sheets, imitation leaves, rods, cakes; Forms of such products
-
- 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
- A24B3/18—Other treatment of leaves, e.g. puffing, crimpling, cleaning
-
- A—HUMAN NECESSITIES
- A24—TOBACCO; CIGARS; CIGARETTES; SIMULATED SMOKING DEVICES; SMOKERS' REQUISITES
- A24B—MANUFACTURE OR PREPARATION OF TOBACCO FOR SMOKING OR CHEWING; TOBACCO; SNUFF
- A24B7/00—Cutting tobacco
-
- A24F47/004—
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- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Manufacture Of Tobacco Products (AREA)
Abstract
The present invention relates to a kind of method by tobacco leaf or raw material pipe tobacco preparation cigarette pipe tobacco, this method includes pipe tobacco screening, charging, the screening of wire distribution steel wire storage, tobacco shreds drying, pipe tobacco container, pipe tobacco and flavoring.The present invention is added in pipe tobacco with large scale smoke agent with uniform effective means, modulated moisture content of cut tobaccos and tobacco structure are suitable for regular volume smoke machine and roll, the cigarette rolled realizes that smoke amount is adjustable, controllable, sustainability under the conditions of magnetic force soaking heating technique, and high-quality, efficient, low consumption and environmental protection are realized in pipe tobacco and cigarette production.
Description
[technical field]
The invention belongs to tobacco leaf production technical fields.More particularly it relates to which a kind of prepare cigarette pipe tobacco by tobacco leaf
Method, further relate to it is a kind of by raw material pipe tobacco preparation cigarette pipe tobacco method.
[background technique]
New type low temperature heats the cigarette that do not burn, existing for heating the smoke grenade part of smoke, ordered arrangement for heating
The complex process of the production of cigarette core material and its composite molding, to realize that the pipe tobacco of traditional cigarette can be used for heating the cigarette that do not burn
Cigarette core need to solve large scale smoke agent and be applied on the pipe tobacco of traditional cigarette, and the pipe tobacco for applying smoke agent is able to achieve just again
Normal cigarette machine rolls, and cigarette generates smog after can realizing low-temperature heat.
The present invention sufficiently excavates traditional cigarette throwing and rolls fundamental technology and equipment, and exploitation is suitable for smoke agent large scale
Uniformly, the technology being effectively applied in pipe tobacco, modulated moisture content of cut tobaccos and tobacco structure are suitable for regular volume smoke machine
It rolls, realizes that pipe tobacco arrange the do not burn industrialization of Cigarette of low-temperature heat naturally and processes, the production of pipe tobacco and cigarette reality
Existing high-quality, efficient, low consumption and environmental protection.For the cigarette rolled in magnetic grain soaking heating technique condition, realization smoke amount is adjustable, can
It controls, is sustainable.
[summary of the invention]
[technical problems to be solved]
The object of the present invention is to provide a kind of methods by tobacco leaf preparation cigarette pipe tobacco.
It is a further object to provide a kind of methods by raw material pipe tobacco preparation cigarette pipe tobacco.
[technical solution]
The present invention is achieved through the following technical solutions.
The present invention relates to a kind of methods by tobacco leaf preparation cigarette pipe tobacco, it includes loosening and gaining moisture of tobacco, storage hello cabinet, cigarette
Leaf screening, charging are sieved and flavoring step, the raw tobacco material of selection with leaf leaves storage, chopping, cut tobacco drying, pipe tobacco container, pipe tobacco
So that its water content is reached by weight 14~18% through loosening and gaining moisture step, size 6mm crumbled tobacco below is then screened out it
After be sent to addition step;
Then, smoke agent feed liquid is allowed to be heated to 45~55 DEG C of temperature in feed pot in addition step, while using full
The crumbled tobacco material from screening step is heated to 45~55 DEG C of temperature with vapor, and by smoke agent feed liquid temperature and cigarette
The difference of leaf temperature of charge is controlled at 5 DEG C or less;Then using the outer mixing nozzle of double media, the saturated water for being 2~4 bars using pressure
Smoke agent feed liquid is atomized to 50~100 microns of average grain diameter by the compressed air that steam or temperature are 100 DEG C, will be atomized smoke agent
Feed liquid is sprayed on tobacco leaf material, to reach 5~30% in an amount of from tobacco leaf weight of material;
Then it carries out that the crumbled tobacco material mixture containing atomization smoke agent feed liquid is allowed to be stored with leaf leaves storage step, makes tobacco leaf
The water content of material reaches by weight 18.0~20.0%;Then chopping, the tobacco shreds drying that will chops up dry using drying machine
It is by weight 11~13% to water content, then through pipe tobacco container, pipe tobacco screening and flavoring step, obtains a kind of for rolling
The pipe tobacco of cigarette.
According to another preferred method of implementation of the present invention, the raw tobacco material is by redrying ageing smoked sheet and reconstruction cigarette
Leaf composition, water content is by weight 10~14%.
According to another preferred method of implementation of the present invention, the pipe tobacco chopped up is dry using drying cylinder, and drying condition is
Barrel temperature is 105~145 DEG C, 82~112 DEG C of hot blast temperature and 0.1~0.3m/s of wind speed in cylinder.
According to another preferred method of implementation of the present invention, the smoke agent is by glycerine, acetin, double
What acetin and glyceryl triacetate were formed according to 5~20:20 of weight ratio~35:40~60:15~30.
According to another preferred method of implementation of the present invention, the drying equipment is that cylindrical drier or air-flowing type are dry
Dry machine.
The present invention relates to a kind of methods by raw material pipe tobacco preparation cigarette pipe tobacco, it includes pipe tobacco screening, charging, wire distribution storage
Silk, tobacco shreds drying, pipe tobacco container, pipe tobacco screening and flavoring step, sieve size 1mm raw material pipe tobacco below in screening process
Addition step is sent to after removing;
Then in addition step, smoke agent feed liquid is allowed to be heated to 45~55 DEG C of temperature in feed pot, while using full
The pipe tobacco material from screening step is heated to 45~55 DEG C of temperature with vapor, and by smoke agent feed liquid temperature and pipe tobacco
The difference of temperature of charge is controlled at 5 DEG C or less;Then using the outer mixing nozzle of double media, it is using 2~4 bars of saturated vapors or temperature
Smoke agent feed liquid is atomized to 50~100 microns of average grain diameter by 100 DEG C of compressed air, and atomization smoke agent feed liquid is sprayed onto original
Expect on pipe tobacco material, to reach 5~30% in an amount of from raw material pipe tobacco weight of material;
Again in wire distribution steel wire storage step, allows the pipe tobacco material mixture containing atomization smoke agent feed liquid to store, make the water of pipe tobacco
Content reaches by weight 14.0~16.0%;Then dry using drying machine, it is by weight by tobacco shreds drying to water content
11~13%, then through pipe tobacco container, pipe tobacco screening and flavoring step, obtain a kind of for rolling the pipe tobacco of cigarette.
According to another preferred method of implementation of the present invention, the raw material pipe tobacco be existing scrap prodn. line drying pipe tobacco,
It cuts filler, expanded cut tobacco or stem, its water content are by weight 11~13%.
According to another preferred method of implementation of the present invention, the drying condition in tobacco shreds drying using drying cylinder is barrel
Temperature is 105~145 DEG C, 82~112 DEG C of hot blast temperature and 0.1~0.3m/s of wind speed in cylinder.
According to another preferred method of implementation of the present invention, the drying equipment is cylindrical drier.
According to another preferred method of implementation of the present invention, the pipe tobacco being prepared is in the tobacco shred box of sealing in temperature 22
~27 DEG C be sealed and stored under conditions of relative humidity 55~65%.
The present invention is described in more detail below.
Traditional cigarette throwing and rolling technology are effectively integrated into an entirety by the present invention, on this basis for big ratio
Example applies smoke agent in pipe tobacco, and effectively modulates moisture content of cut tobaccos and tobacco structure, realizes and is rolled using regular volume smoke machine,
Cigarette is rolled into using the pipe tobacco that the method for the present invention is processed, under the conditions of magnetic force soaking heating technique, can be realized smoke amount can
It adjusts, controllably and sustainability.
The present invention relates to a kind of methods by tobacco leaf preparation cigarette pipe tobacco, it includes loosening and gaining moisture of tobacco, storage hello cabinet, cigarette
Leaf leaves storage, chopping, cut tobacco drying, the screening of pipe tobacco container, pipe tobacco and flavoring step are matched in leaf screening, charging, these steps are existing
The basic step of pipe tobacco preparation method, referring specifically to document " cigarette process specification ".
In the present invention, the raw tobacco material of selection through loosening and gaining moisture step make its water content reach by weight 14~
18%, it then sieves, after size 6mm crumbled tobacco below is screened out, is sent to addition step;It is below broken to screen out size 6mm
Tobacco leaf is because size 6mm crumbled tobacco below easily leads to tobacco leaf conglomeration after large scale adds smoke agent.
According to the present invention, the raw tobacco material is made of redrying ageing smoked sheet and reconstituted tobacco, and water content is
By weight 10~14%.In the present invention, the water content in material is measured according to YC/T 345-2010 standard analysis,
Referring specifically to document " the measurement gas chromatography of YC/T345-2010 tobacco and tobacco product moisture ".The water content being set forth below
It is all to be measured using this analysis method, therefore will not be described in great detail below.
In the present invention, redrying ageing smoked sheet by redrying and in tobacco leaf warehouse it should be understood that be aged certain
The available tobacco leaf of time cigarette industry;The reconstituted tobacco is it should be understood that using raw tobacco material according to traditional paper maker
The homogeneous tobacco leaf of skill processing.The weight ratio of redrying ageing smoked sheet and reconstituted tobacco is not very crucial, usually 1:7~12.
In the present invention, the water content of the raw tobacco material is by weight 10~14%, if the water of raw tobacco material contains
Amount is lower than 10%, then tobacco leaf makes broken big, loss height in process;If the water content of raw tobacco material is higher than 14%, cigarette
Leaf stores perishable for a long time;Therefore, it is appropriate that the water content of raw tobacco material, which is 10~14%,;
Then, smoke agent feed liquid is allowed to be heated to 45~55 DEG C of temperature in feed pot in addition step, while using full
The crumbled tobacco material from screening step is heated to 45~55 DEG C of temperature with vapor, and by smoke agent feed liquid temperature and cigarette
The difference of leaf temperature of charge is controlled at 5 DEG C or less;Then using the outer mixing nozzle of double media, the saturated water for being 2~4 bars using pressure
Smoke agent feed liquid is atomized to 50~100 microns of average grain diameter by the compressed air that steam or temperature are 100 DEG C, will be atomized smoke agent
Feed liquid is sprayed on crumbled tobacco material, to reach 5~30% in an amount of from crumbled tobacco weight of material;
According to the present invention, the smoke agent is sweet by glycerine, acetin, diacetic acid glyceride and triacetic acid
Grease is formed according to 5~20:20 of weight ratio~35:40~60:15~30.
In the present invention, smoke agent feed liquid is heated to 45~55 DEG C of temperature.If heating temperature is more than the range,
It is worthless i.e. lower than 45 DEG C or higher than 55 DEG C, because smoke agent viscosity of sludge is big when heating temperature is lower than 45 DEG C, charging is equal
Even property is poor;Low boiling component is volatile in smoke agent feed liquid when higher than 55 DEG C and energy consumption increases.Similarly, tobacco leaf material heating temperature
Degree is more than that the range is also worthless, because tobacco leaf material is best to the absorbent properties of feed liquid in this temperature range.
In the present invention, the average grain diameter of smoke agent feed liquid atomization particle is that grain-size graph is atomized according to liquid as method standard scores
Analysis measurement.If the average grain diameter of smoke agent feed liquid atomization particle causes smoke agent to volatilize less than 50 microns;If smoke
The average grain diameter of agent feed liquid atomization particle is greater than 100 microns, then influences absorption of the tobacco leaf to smoke agent;Therefore, smoke agent feed liquid
It is reasonably preferably 65~85 microns that the average grain diameter of atomization particle, which is 50~100 microns,;
It is mixing nozzle outside double media that smoke agent feed liquid, which is atomized used equipment, they are all to sell currently on the market
Product, such as mixing nozzle outside double media for being sold by Schlick company with trade name Schlick825.
In the present invention, smoke agent feed liquid temperature and the difference of tobacco leaf temperature of charge are controlled at 5 DEG C hereinafter, if the two temperature difference is super
5 DEG C are crossed, tobacco leaf reduces smoke agent absorption efficiency, and when the smoke agent addition of large scale, smoke agent bulk deposition is in tobacco leaf table
There is clustering phenomena in face.Then it carries out that the crumbled tobacco material mixture containing atomization smoke agent feed liquid is allowed to be store with leaf leaves storage step
It deposits, the water content of tobacco leaf material is made to reach by weight 18.0~20.0%;Its basic object for controlling water content is tobacco leaf
Chopping uniformity controlling.If the water content of crumbled tobacco material, less than 18.0%, chopping is made broken big;If crumbled tobacco material
Water content is higher than 20.0%, then pipe tobacco uniformity is poor;Therefore, it is suitable that the water content of crumbled tobacco material, which is 18.0~20.0%,
's;
Then chopping, it is dry using drying machine, it is by weight 11~13% by the tobacco shreds drying chopped up to water content,
According to the present invention, the pipe tobacco chopped up is dry using drying cylinder, and drying condition is that barrel temperature is 105~145 DEG C, hot blast temperature
82~112 DEG C with cylinder in 0.1~0.3m/s of wind speed.
The drying equipment is cylindrical drier or pneumatic convey drier, they are all current market sales of productions
Product, for example, sold by Hauni company with trade name KLD cylindrical drier, sold with trade name CTD by Comas company
Pneumatic convey drier.
Then, dry pipe tobacco obtains a kind of for rolling cigarette through conventional steps such as pipe tobacco container, pipe tobacco screening and flavorings
Pipe tobacco.
The pipe tobacco that is prepared needs in the tobacco shred box of sealing in 22~27 DEG C of temperature and relative humidity 55~65%
Under the conditions of be sealed and stored, main purpose is to make pipe tobacco further to absorb smoke agent and fragrance, realizes flavors and fragrances in pipe tobacco
Surface is uniformly distributed with internal.A kind of cigarette can be rolled by this pipe tobacco using conventional method for coiling.
The present invention relates to a kind of methods by raw material pipe tobacco preparation cigarette pipe tobacco, it includes pipe tobacco screening, charging, wire distribution storage
Silk, tobacco shreds drying, pipe tobacco container, pipe tobacco screening and flavoring step, these steps are the basic steps of existing pipe tobacco preparation method,
Referring specifically to document " cigarette process specification ".
According to the present invention, the raw material pipe tobacco is the drying pipe tobacco of existing scrap prodn. line, cuts filler, expanded cut tobacco or stalk
Silk, its water content are by weight 11~13%.
In the present invention, the drying pipe tobacco is it should be understood that pipe tobacco after the drying manufactured using single-grade tobacco leaf;
Described cuts filler it should be understood that using the existing pipe tobacco for being formulated mixed tobacco leaf manufacture;
The expanded cut tobacco is it should be understood that the pipe tobacco prepared using conventional carbon dioxide expansion process;
The stem is it should be understood that the filiform manufactured using offal according to traditional stem preparation process;
In the present invention, the water content of the raw material pipe tobacco is by weight 11~13%, if the water of raw material pipe tobacco contains
Amount is lower than 11%, then pipe tobacco is easily made broken;If the water content of raw material pipe tobacco is higher than 13%, pipe tobacco stores perishable for a long time;
Therefore, it is appropriate that the water content of raw material pipe tobacco, which is 11~13%,;
It is sent to addition step after screening out size 1mm raw material pipe tobacco below in screening process, screens out size 1mm or less
Raw material pipe tobacco be because large scale addition smoke agent after size 1mm pipe tobacco below easily lead to pipe tobacco conglomeration;
Then in addition step, smoke agent feed liquid is allowed to be heated to 45~55 DEG C of temperature in feed pot, while using full
The pipe tobacco material from screening step is heated to 45~55 DEG C of temperature with vapor;Then the outer mixing nozzle of double media is used,
Smoke agent feed liquid is atomized micro- to average grain diameter 50~100 by the compressed air for being 100 DEG C using 2~4 bars of saturated vapors or temperature
Atomization smoke agent feed liquid is sprayed on raw material pipe tobacco material by rice, with reach 5 in an amount of from raw material pipe tobacco weight of material~
30%;
In the present invention, smoke agent feed liquid temperature and the difference of pipe tobacco temperature of charge are controlled at 5 DEG C hereinafter, if the two temperature difference is super
5 DEG C are crossed, pipe tobacco reduces smoke agent absorption efficiency, and when the smoke agent addition of large scale, smoke agent bulk deposition is in pipe tobacco table
There is clustering phenomena in face.
In relation to smoke agent, atomization and its equipment situation with it is described identical in front, therefore details are not described herein.
Again in wire distribution steel wire storage step, allows the pipe tobacco material mixture containing atomization smoke agent feed liquid to store, make the water of pipe tobacco
Content reaches by weight 14.0~16.0%;It is the uniform pickup that basic object is pipe tobacco to smoke agent that it, which controls water content,
With the stabilization of drying process parameter.If the water content of pipe tobacco material less than 14.0%, is unfavorable for the uniform pickup of smoke agent;
If the water content of pipe tobacco material is higher than 16.0%, it is unfavorable for process drying parameter stability and smoke agent assimilation effect
Control;Therefore, it is appropriate that the water content of pipe tobacco material, which is 14.0~16.0%,;
Then dry using drying machine, it is by weight 11~13% by tobacco shreds drying to water content.What the present invention used
Drying equipment is cylindrical drier.Drying condition in tobacco shreds drying using drying cylinder is that barrel temperature is 105~145
DEG C, 82~112 DEG C of hot blast temperature and 0.1~0.3m/s of wind speed in cylinder.
Then it through pipe tobacco container, pipe tobacco screening and flavoring step, obtains a kind of for rolling the pipe tobacco of cigarette.It is prepared
Pipe tobacco need in the tobacco shred box of sealing at 22~27 DEG C of temperature with relative humidity 55~65% under conditions of be sealed and stored.
A kind of low temperature can be rolled by this pipe tobacco using conventional method for coiling not burning mating cigarette.
The cigarette that the present invention obtains is referred to " YC_T138-1998_ tobacco and tobacco product sensory evaluation method " standard
The regulation tissue expert that smokes panel test smokes panel test, and evaluation criterion and smoking result are listed in table 1 and 2.Simultaneously according to traditional cigarette work
Skill parameter preparation cigarette sample is also evaluated as control sample, and technique and Analyses Methods for Sensory Evaluation Results are also shown in Table 2 below.This
A little evaluation results show: pipe tobacco technology described in the invention is suitble to low temperature not burn matched pipe tobacco nature arrangement type
The high efficiency manufacture of cigarette, and aesthetic quality is whole higher, especially aspirates uniformity.
[beneficial effect]
The beneficial effects of the present invention are: the present invention realizes that large scale smoke agent is added in pipe tobacco with uniform effective means,
Modulated moisture content of cut tobaccos and tobacco structure are suitable for conventional high-speed cigarette machine and roll, and the cigarette rolled heats skill in magnetic grain soaking
Realize that smoke amount is adjustable, controllable, sustainability and suction uniformity are good under the conditions of art, pipe tobacco and cigarette production realize it is high-quality,
Efficiently, low consumption and environmental protection.
[specific embodiment]
It will be better understood that the present invention by following embodiments.
Embodiment 1: cigarette pipe tobacco is prepared by tobacco leaf
The embodiment of the embodiment is as follows:
Method by tobacco leaf preparation cigarette pipe tobacco includes loosening and gaining moisture of tobacco, cabinet is fed in storage, tobacco leaf sieves, is fed, with leaf
Leaves storage, chopping, cut tobacco drying, the screening of pipe tobacco container, pipe tobacco and flavoring step.
Raw tobacco material is reproduced by cigarette in the redrying ageing smoked sheet of China Tobacco Anhui Industrial Co., Ltd.'s buying and Anhui
What the reconstituted tobacco of tobacco leaf science and technology limited Company manufacture was formed according to weight ratio 1:9, water content is by weight 10%.
Raw tobacco material makes its water content reach by weight 16% through loosening and gaining moisture step, then sieves, by size 6mm with
Under crumbled tobacco screen out after be sent to addition step;
Then, the smoke agent which uses is by glycerine, acetin, diacetic acid glyceride and triacetic acid
Glyceride is formed according to weight ratio 5:20:45:20.
It allows smoke agent feed liquid to be heated to temperature 45 C in feed pot in addition step, while using saturated steam will
Tobacco leaf material from screening step is heated to temperature 45 C;Then it uses by Schlick company with trade name Schlick825
Smoke agent feed liquid, is atomized to average grain diameter 50 by the outer mixing nozzle of double media of sale using the saturated vapor that pressure is 2 bars
~100 microns, atomization smoke agent feed liquid is sprayed on tobacco leaf material, to reach 16% in an amount of from tobacco leaf weight of material;
Then it carries out that the crumbled tobacco material mixture containing atomization smoke agent feed liquid is allowed to be stored with leaf leaves storage step, makes broken cigarette
The water content of leaf material reaches by weight 18.0%;Then chopping uses the rolling sold by Hauni company with trade name KLD
Cylinder drying machine, by the pipe tobacco chopped up under the conditions of barrel temperature is 105 DEG C, 82 DEG C of hot blast temperature is with wind speed 0.1m/s in cylinder
Drying to water content is by weight 12%, then through pipe tobacco container, pipe tobacco screening and flavoring step, obtains one kind and is used to roll up
The pipe tobacco of tobacco curing branch.
This pipe tobacco is rolled by a kind of cigarette using conventional method for coiling, is commented according to the method that this specification describes
It inhales, technology assessment is also shown in Table 2 below with sensory evaluating smoking's result.
Embodiment 2: cigarette pipe tobacco is prepared by tobacco leaf
The embodiment of the embodiment is identical as the embodiment of embodiment 1, and only raw tobacco material is by cigarette work in Anhui
The reconstruction of cigarette reconstituted tobacco science and technology limited Company manufacture in the redrying ageing smoked sheet of industry Co., Ltd buying and Anhui
Tobacco leaf is formed according to weight ratio 1:7, and water content is by weight 10%.
Raw tobacco material makes its water content reach by weight 14% through loosening and gaining moisture step;
The smoke agent that the embodiment uses is by glycerine, acetin, diacetic acid glyceride and triacetic acid glycerol
Ester is formed according to weight ratio 12:28:50:15.
In addition step, smoke agent feed liquid is heated to 55 DEG C of temperature, and tobacco leaf material is heated to 55 DEG C of temperature;
Smoke agent feed liquid is atomized to 50~100 microns of average grain diameter, by mist using the saturated vapor that pressure is 4 bars
Change smoke agent feed liquid to be sprayed on tobacco leaf material, to reach 5% in an amount of from tobacco leaf weight of material;
Then it carries out with leaf leaves storage step, the water content of tobacco leaf material reaches by weight 19.0%;
The pipe tobacco chopped up is dry under the conditions of barrel temperature is 120 DEG C, 98 DEG C of hot blast temperature is with wind speed 0.2m/s in cylinder
It is by weight 11% to water content.
This pipe tobacco is rolled by a kind of cigarette using conventional method for coiling, is commented according to the method that this specification describes
It inhales, technology assessment is also shown in Table 2 below with sensory evaluating smoking's result.
Embodiment 3: cigarette pipe tobacco is prepared by tobacco leaf
The embodiment of the embodiment is identical as the embodiment of embodiment 1, and only raw tobacco material is adopted by cigarette in Anhui
The reconstituted tobacco of cigarette reconstituted tobacco science and technology limited Company manufacture is according to weight ratio 1 in the redrying ageing smoked sheet of purchase and Anhui:
12 compositions, water content is by weight 14%.
Raw tobacco material makes its water content reach by weight 18% through loosening and gaining moisture step;
The smoke agent that the embodiment uses is by glycerine, acetin, diacetic acid glyceride and triacetic acid glycerol
Ester is formed according to weight ratio 20:35:60:30.
In addition step, smoke agent feed liquid is heated to temperature 50 C, and tobacco leaf material is heated to temperature 45 C;
Smoke agent feed liquid is atomized to 50~100 microns of average grain diameter using the compressed air that temperature is 100 DEG C, will be atomized
Smoke agent feed liquid is sprayed on tobacco leaf material, to reach 30% in an amount of from tobacco leaf weight of material;
Then it carries out with leaf leaves storage step, the water content of tobacco leaf material reaches by weight 20.0%;
The pipe tobacco chopped up is dry under the conditions of barrel temperature is 145 DEG C, 112 DEG C of hot blast temperature is with wind speed 0.3m/s in cylinder
It is dry to water content be by weight 13%.
This pipe tobacco is rolled by a kind of cigarette using conventional method for coiling, is commented according to the method that this specification describes
It inhales, technology assessment is also shown in Table 2 below with sensory evaluating smoking's result.
Embodiment 4: cigarette pipe tobacco is prepared by raw material pipe tobacco
The embodiment of the embodiment is as follows:
Method by raw material pipe tobacco preparation cigarette pipe tobacco includes pipe tobacco screening, charging, wire distribution steel wire storage, tobacco shreds drying, pipe tobacco
Container, pipe tobacco screening and flavoring step.
Raw material pipe tobacco is the drying pipe tobacco of China Tobacco Anhui Industrial Co., Ltd.'s production, and water content is by weight
12%.
After size 1mm raw material pipe tobacco below being screened out in screening process be sent to addition step;
Then, the smoke agent which uses is that glycerine, acetin, diacetic acid glyceride and triacetic acid are sweet
Grease is formed according to weight ratio 8:22:45:18.Smoke agent feed liquid is allowed to be heated to temperature 48 in feed pot in addition step
DEG C, while the crumbled tobacco material from screening step is heated to 48 DEG C of temperature using saturated steam;Then use by
Mixing nozzle outside double media that Schlick company is sold with trade name Schlick825, using 4 bars of saturated vapors by smoke agent
Feed liquid is atomized to 50~100 microns of average grain diameter, atomization smoke agent feed liquid is sprayed on pipe tobacco, to reach in an amount of from pipe tobacco object
Expect the 10% of weight;
Then wire distribution steel wire storage step is carried out, allows the pipe tobacco material mixture containing atomization smoke agent feed liquid to store, makes pipe tobacco object
The water content of material reaches by weight 14.2%;Then the cylindrical drier sold using Hauni company with trade name KLD,
By the pipe tobacco chopped up barrel temperature be 110 DEG C, 88 DEG C of hot blast temperature with wind speed 0.1m/s in cylinder under conditions of dry to water and contain
Amount is by weight 11.4%, then through pipe tobacco container, pipe tobacco screening and flavoring step, is obtained a kind of for rolling the cigarette of cigarette
Silk.
This pipe tobacco is rolled by a kind of cigarette using conventional method for coiling, is commented according to the method that this specification describes
It inhales, technology assessment is also shown in Table 2 below with sensory evaluating smoking's result.
Embodiment 5: cigarette pipe tobacco is prepared by raw material pipe tobacco
The embodiment of the embodiment is identical as the embodiment of embodiment 4, and only raw material pipe tobacco is cigarette industry in Anhui
The expanded cut tobacco of Co., Ltd's production, water content are by weight 12%.
The smoke agent that the embodiment uses is glycerine, acetin, diacetic acid glyceride and glyceryl triacetate
According to weight ratio 15:26:54:24 composition.
In addition step, smoke agent feed liquid is allowed to be heated to temperature 50 C, expanded cut tobacco is heated to temperature 50 C;
Smoke agent feed liquid is atomized to 50~100 microns of average grain diameter using the compressed air that temperature is 100 DEG C, will be atomized
Smoke agent feed liquid is sprayed on expanded cut tobacco, to reach 10% in an amount of from pipe tobacco weight of material;
The water content of pipe tobacco material reaches by weight 14.2%;
The pipe tobacco chopped up is dry under conditions of barrel temperature is 122 DEG C, 98 DEG C of hot blast temperature is with wind speed 0.2m/s in cylinder
It is by weight 12.2% to water content.
This pipe tobacco is rolled by a kind of cigarette using conventional method for coiling, is commented according to the method that this specification describes
It inhales, technology assessment is also shown in Table 2 below with sensory evaluating smoking's result.
Embodiment 6: cigarette pipe tobacco is prepared by raw material pipe tobacco
The embodiment of the embodiment is identical as the embodiment of embodiment 4, and only raw material pipe tobacco is by cigarette work in Anhui
The stem of industry Co., Ltd production, water content are by weight 13%.
The smoke agent that the embodiment uses is glycerine, acetin, diacetic acid glyceride and glyceryl triacetate
According to weight ratio 18:32:58:28 composition.
Smoke agent feed liquid is heated to temperature 50 C in feed pot, and stem is heated to 55 DEG C of temperature;
Smoke agent feed liquid is atomized to 50~100 microns of average grain diameter using 2 bars of saturated vapors, smoke agent feed liquid will be atomized
It is sprayed on stem, to reach 25% in an amount of from stem weight;
The water content of the stem reaches by weight 15.6%;
The stem is dry to water under conditions of barrel temperature is 134 DEG C, 105 DEG C of hot blast temperature is with wind speed 0.3m/s in cylinder
Content is by weight 12.8%.
This pipe tobacco is rolled by a kind of cigarette using conventional method for coiling, is commented according to the method that this specification describes
It inhales, technology assessment is also shown in Table 2 below with sensory evaluating smoking's result.
Comparative example 1
The embodiment of the comparative example is identical as the embodiment of embodiment 1, only the heating temperature of smoke agent feed liquid
Degree is room temperature (25 DEG C), tobacco leaf temperature is also room temperature, and smoke agent feed liquid theory additive amount is the 16% of tobacco leaf weight of material, work
Skill evaluation is also shown in Table 2 below with sensory evaluating smoking's result
Comparative example 2
The embodiment of the comparative example is identical as the embodiment of embodiment 4, and only smoke agent is glycerine, smoke
45 DEG C of agent feed liquid temperature, pipe tobacco temperature 60 C, smoke agent feed liquid theory additive amount is the 10% of pipe tobacco weight of material, and technique is commented
Valence is also shown in Table 2 below with sensory evaluating smoking's result.
Low temperature is prepared by tobacco leaf or raw material pipe tobacco using the present invention it can be seen from the result that table 2 is listed not burn cigarette
The practical feeding homogeneity (being shown in Table 2 actual interpolation amounts) of the method for pipe tobacco, smoke agent is obviously improved, and prepared pipe tobacco is suitble to
Conventional high-speed cigarette machine rolls, and is not in upper machine bad adaptability, cigarette permeability, cigarette as caused by high smoke agent additive amount
Phenomena such as paper pleat Zou, cigarette appearance looks elegant, consumption embody.Cigarette prepared by the present invention is suitble to magnetic grain soaking heating technique, and
Smoke amount is adjustable, controllable, sustainable;And relatively conventional cigarette method of manufacturing technology, the cigarette of this method preparation aspirate uniformity
It significantly improves.
Claims (10)
1. it is a kind of by tobacco leaf preparation cigarette pipe tobacco method, it include loosening and gaining moisture of tobacco, storage feed cabinet, tobacco leaf screening, charging,
With leaf leaves storage, chopping, cut tobacco drying, the screening of pipe tobacco container, pipe tobacco and flavoring step, it is characterised in that the raw tobacco material of selection passes through
Loosening and gaining moisture step makes its water content reach by weight 14~18%, after then screening out size 6mm crumbled tobacco below
It is sent to addition step;
Then, it allows smoke agent feed liquid to be heated to 45~55 DEG C of temperature in feed pot in addition step, while using saturated water
Tobacco leaf material from screening step is heated to 45~55 DEG C of temperature by steam, and by smoke agent feed liquid temperature and tobacco leaf material
Temperature difference is controlled at 5 DEG C or less;Then using the outer mixing nozzle of double media, using pressure be 2~4 bars saturated vapor or
Temperature is that smoke agent feed liquid is atomized to 50~100 microns of average grain diameter by 100 DEG C of compressed air, by atomization smoke agent feed liquid spray
It is spread across on tobacco leaf material, to reach 5~30% in an amount of from tobacco leaf weight of material;
Then it carries out that the tobacco leaf material mixture containing atomization smoke agent feed liquid is allowed to be stored with leaf leaves storage step, makes tobacco leaf material
Water content reaches by weight 18.0~20.0%;Then chopping, it is dry using drying machine, the tobacco shreds drying chopped up to water is contained
Amount is by weight 11~13%, then through pipe tobacco container, pipe tobacco screening and flavoring step, obtains one kind and is suitable for rolling cigarette
Pipe tobacco.
2. pipe tobacco preparation method according to claim 1, it is characterised in that the raw tobacco material is to be aged cigarette by redrying
What piece and reconstituted tobacco formed, water content is by weight 10~14%.
3. pipe tobacco preparation method according to claim 1, it is characterised in that the pipe tobacco chopped up is dry using drying cylinder, does
Dry condition be barrel temperature be 105~145 DEG C, 82~112 DEG C of hot blast temperature and 0.1~0.3m/s of wind speed in cylinder.
4. pipe tobacco preparation method according to claim 1, it is characterised in that the smoke agent is by glycerine, single acetic acid
Glyceride, diacetic acid glyceride and glyceryl triacetate are formed according to 5~20:20 of weight ratio~35:40~60:15~30.
5. pipe tobacco preparation method according to claim 1, it is characterised in that the drying equipment is cylindrical drier
Or pneumatic convey drier.
6. it is a kind of by raw material pipe tobacco preparation cigarette pipe tobacco method, it include pipe tobacco screening, charging, wire distribution steel wire storage, tobacco shreds drying,
Pipe tobacco container, pipe tobacco screening and flavoring step, it is characterised in that screen out size 1mm raw material pipe tobacco below in screening process
Later, it is sent to addition step;
Then in addition step, smoke agent feed liquid is allowed to be heated to 45~55 DEG C of temperature in feed pot, while using saturated water
Pipe tobacco material from screening step is heated to 45~55 DEG C of temperature by steam, and by smoke agent feed liquid temperature and pipe tobacco material
Temperature difference is controlled at 5 DEG C or less;It then is 100 using 2~4 bars of saturated vapors or temperature using the outer mixing nozzle of double media
DEG C compressed air smoke agent feed liquid is atomized to 50~100 microns of average grain diameter, will atomization smoke agent feed liquid be sprayed onto raw material
On pipe tobacco material, to reach 5~30% in an amount of from raw material pipe tobacco weight of material;
Again in wire distribution steel wire storage step, allows the pipe tobacco material mixture containing atomization smoke agent feed liquid to store, make the water content of pipe tobacco
Reach by weight 14.0~16.0%;Then dry using drying machine, by tobacco shreds drying to water content be by weight 11~
13%, then through pipe tobacco container, pipe tobacco screening and flavoring step, obtain a kind of pipe tobacco suitable for rolling cigarette.
7. pipe tobacco preparation method according to claim 6, it is characterised in that the raw material pipe tobacco is existing scrap prodn. line
Dry pipe tobacco cuts filler, expanded cut tobacco, cuts filler or stem, its water content is by weight 11~13%.
8. pipe tobacco preparation method according to claim 6, it is characterised in that use the drying of drying cylinder in tobacco shreds drying
Condition be barrel temperature be 105~145 DEG C, 82~112 DEG C of hot blast temperature and 0.1~0.3m/s of wind speed in cylinder.
9. pipe tobacco preparation method according to claim 6, it is characterised in that the drying equipment is cylindrical drier.
10. according to claim 1 or preparation method as claimed in claim 6, it is characterised in that the pipe tobacco being prepared is sealing
Tobacco shred box in be sealed and stored under conditions of 22~27 DEG C of temperature with relative humidity 55~65%.
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