CN103704867A - Method for improving quality of cut stems - Google Patents

Method for improving quality of cut stems Download PDF

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Publication number
CN103704867A
CN103704867A CN201410002912.2A CN201410002912A CN103704867A CN 103704867 A CN103704867 A CN 103704867A CN 201410002912 A CN201410002912 A CN 201410002912A CN 103704867 A CN103704867 A CN 103704867A
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China
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stalk
stem
sheet
temperature
offal
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CN201410002912.2A
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CN103704867B (en
Inventor
李华杰
李跃锋
余志强
林凯
陈河祥
罗登炎
李茂毅
马鹏飞
赖炜扬
李易非
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China Tobacco Fujian Industrial Co Ltd
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China Tobacco Fujian Industrial Co Ltd
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Abstract

The invention provides a method for improving the quality of cut stems. The method comprises the following steps that (1) tobacco stems are washed and degraded; (2) moisture regain is conducted on the tobacco stems and the tobacco stems are stored; (3) the tobacco stems are expanded and pressed; (4) stem pieces are degraded and stored; (5) material adding is conducted on the stem pieces; (6) the stem pieces are dried; (7) the dried stem pieces are stored; (8) moisture regain is conducted on the dried stem pieces and the dried stem pieces are expanded and pressed; (9) the stem pieces are cut into shreds and materials are added; (10) the cut stems are expanded and dried. Cigarettes with the cut stems prepared through the method are clear in fragrance characteristic, the fragrance quality is good, the smoke state is improved, the fine and smooth performance is improved, the harmony is better, miscellaneous gases are reduced, the dry sensation is reduced, and taste is more comfortable.

Description

A kind of method that improves cut stem quality
Technical field
The invention belongs to tobacco manufacture field, relate to a kind of processing method that improves cut stem quality.
Background technology
The features such as stem has tar, nicotine content is low, and filling capacity is good, are one of main filler of cigarette tobacco leaf formulation, in cigarette composition, play an important role.Under product design allows, increase stem consumption, be one of important means of reducing tar and reducing harm, be also cost-saving good method.Stem is processed by offal, but owing to containing the macromolecular substances such as a large amount of celluloses, pectin and lignin in offal, these macromolecular substances are the restraining factors that improve cut stem quality.Conventional machining process technology cannot make these macromolecular substances fully be degraded, can not control the palliating degradation degree of these macromolecular substances, finished product stem exists on sense organ stimulates the shortcomings such as large, concentration is high, assorted gas is obvious, by reinforced, can only cover its shortcoming, and effect is limited, cannot be from dealing with problems in essence, the application in cigarette composition is restricted.
Technical staff is carrying out a large amount of research work improving aspect stem comprehensive quality in recent years, mainly contains the following aspects: the application of (1) novel technique, adopt new technology, new technology improves stem quality.For example, the people such as He Ju adopt microwave expansion offal, offal after microwave expansion aspect the relative amount of aroma component, organic acid etc. all to being significantly improved same as before, suction taste improves, and interior quality is improved, and filling capacity improves, comprehensive quality promotes (He Ju, Liu Weijuan etc. to some extent, < < tobacco science and technology > >, the 2nd phase in 2006, the research of microwave expansion tobacco stalk quality).(2) chemical treatment, by the quality of the some chemical properties raising stem in solvent extraction or extraction offal or stem.For example, the people such as Li Jun make stem after utilizing spirit solvent to extract offal, and the furfural after this technical finesse in stem, 5 methyl furfural and phenmethylol etc. obviously reduce the disadvantageous chemical composition of aesthetic quality, and stem interior quality is improved.(3) process optimization, by technological process reproduce, technology optimization etc. improves stem quality.For example, patent ZL200910065889.0 discloses a kind of technology and equipment of cabo shredding, and offal, through operations such as immersion, Terrier Storage, steaming stalk, row's stalk, pressure stalk, row's stalk sheets, is reduced to stem to make broken, the stem of making is close with cut tobacco shape, improves the use value of stem; Patent ZL200810154171.4 discloses a kind of cut rolled stem processing procedure, offal through warming and humidifying, cut stalk, stem warming and humidifying, stem expansion, cut the operations such as stem, offal, through twice cutting, has improved stability and the use value of stem quality.(4) biotechnology is processed, and utilizes complex enzyme or microorganism to degrade to the macromolecular components such as cellulose in offal or stem, improves the quality of stem.For example, the people such as Lin Xiang adopt complex enzyme to process stem, the products relevant to aesthetic quality such as the total sugar content after processing in stem, mailland reaction product, carotenoid catabolite are all improved, stem flavouring essence quality make moderate progress (Lin Xiang, Tao Hong, Shen Guanglin etc., < < Agriculture of Anhui science > >, the 4th phase in 2011, utilize the research of compound enzyme improved cabo quality).
In a word, although the research in the recent period cut stem quality being improved is more, the lifting effect of cut stem quality is bad.Some novel technique energy consumptions are high, and brought potential safety hazard (as microwave leakage etc.), be unfavorable for production application, and chemical treatment method easily causes secondary pollution, and cost is higher, commercial Application difficulty, during biotechnology is processed, due to cellulose in offal, the biomass components such as pectin are to wrap up in order existence, and the activity between different biologic products can suppress mutually, the disposable of biologic product directly adds, cannot well to offal inside, need degradable component effectively to process, degradation effect is bad, and all to degrade online, be stored as master, not through off-line storage alcoholization, produce fragrant effect bad, quality improving is not obvious, need to adopt classification biological treatment, after processing, alcoholization is produced fragrant, could obviously improve cut stem quality.
Summary of the invention
The object of the invention is to have difficult point and deficiency for prior art, a kind of new method that improves cut stem quality is provided.
A first aspect of the present invention provides a kind of method that improves cut stem quality, comprises following steps:
(1) offal cleans and degraded: offal adopts circulating protein enzyme aqueous solution soak or clean, and stores 4-8 hour after drainage, obtains moisture content and be 18%-22%(for example 19%, 21%) offal;
(2) regaining moisture of cabo and storage: step (1) gained offal through conventional warming and humidifying device processes, is obtained to moisture content and be 25%-30%(for example 27%, 29%) offal;
(3) cabo expansion and pressure stalk: adopt high-temperature steam moisture regain offal, obtain temperature 50-80 ℃ of (for example 60 ℃, 65 ℃), moisture content and be 30%-40%(for example 31%, 33%, 36%) expanded cabo, directly enter and press stalk equipment to press stalk, obtain the thick stalk sheet of even thickness;
(4) degraded of stalk sheet and storage: adopt conventional feed way, according to a certain percentage complex enzyme liquid is sprayed on thick stalk sheet, store 6 hours above (for example 8-10 hour);
(5) stalk sheet is reinforced: in proportion additive is applied on the stalk sheet of step (4) gained, and storage at normal temperature 0.5 hour above (for example 1-2 hour), wherein, described additive is Freamine Ⅲ;
(6) stalk sheet is dry: the stalk sheet that step (5) is obtained is dried, and obtains stick sheet;
(7) stick sheet is stored: the stick sheet that step (6) is obtained packs, and stores >=30 days (for example 30-45 days);
(8) stick sheet moisture regain is expanded and is pressed stalk: adopt steam the mixings warming and humidifying mode stick sheet that gets damp again, obtain temperature for the expansion stem sheet that (50-80) ℃, moisture content are (30-38) %, directly enter and press stalk equipment to press to obstruct, obtain the thin stalk sheet of even thickness;
(9) cut stem: the thin stalk sheet of gained is cut into conventional stem, selectively applies according to demand necessary feed liquid;
(10) stem expansion is with dry: adopt steam moisture regain stem, then carry out stem and be dried, obtain finished product stem.
According to the method described in first aspect present invention, wherein said protease is neutral proteinase, and preferred concentration is 0.5%~1.5%(for example 0.8%, 1% or 1.2%),
Preferably, to adopt temperature be that 35-45 ℃, PH are the water modulation of 6-7, electrical conductivity≤50 μ s/cm to aqueous solution of protease;
Preferably, the temperature of described circulating protein enzyme liquid is 40 ± 2 ℃, flow velocity≤5m/s;
Preferably, the time of immersion or cleaning is more than 10 seconds;
Preferably, the storage temperature 25-30 ℃ in step (1).
According to the method described in first aspect present invention, wherein the pressure of the high-temperature vapour described in step (3) is more than 2.0bar;
Preferably, the pressure stalk gap of the stalk of the pressure described in step (3) equipment is set in the arbitrary numerical value (for example 1.0mm or 1.1mm) within the scope of 1.0-1.2mm.
According to the method described in first aspect present invention, wherein said complex enzyme is comprised of pectase, cellulase and zytase;
Preferably, in every kilogram of composite enzyme solution, pectase total activity is (for example 9,000,000 U, 1,500 ten thousand U) between ten thousand U of 3,000,000 U~3000, cellulase total activity is (for example 6,000,000 U, 1,000 ten thousand U) between ten thousand U of 2,000,000 U~2000, and zytase total activity is (for example 3,000,000 U, 5,000,000 U) between ten thousand U of 1,000,000 U~1000;
Preferably, in described composite enzyme solution, the total activity of various enzymes is than being (2-4): (1-3): (0.5-1.5) (be preferably 3:2:1),
Preferably, the addition of described complex enzyme is offal weight (1~4) %(for example 1.5%, 2%, 3%, 3.5%);
Preferably, to adopt temperature be that 40-50 ℃, PH are the water modulation of 4-6, electrical conductivity≤50 μ s/cm for described complex enzyme;
Preferably, the storage temperature described in step (4) is that 25-35 ℃ of (being preferably 30 ± 2 ℃), relative humidity are that 60-70%(is preferably 65 ± 2%).
According to the method described in first aspect present invention, wherein saidly be selected from glutamic acid, phenylalanine, aspartic acid, proline or its combination, be preferably the mixed solution of aspartic acid and proline, in preferred mixed solution, aspartic acid and proline mass ratio are 1~1.5 ︰ 1;
Preferred amino acid concentration is 0.1~2.0%(for example 0.5%, 1.%, 1.2%, 1.5% or 1.8%);
Preferably, the consumption of described additive is stalk the more than 1% of tablet quality (be preferably 1.0%~3.0%, for example 1.5%, 1.8% or 2.0%).
According to the method described in first aspect present invention, wherein the dry employing drum drying equipment in step (6) is dried;
Preferably, the baking temperature in step (6) is 100-130 ℃ (for example 110 ℃ or 120 ℃);
The moisture content of the stick sheet preferably, obtaining in step (6) is 10-13%(for example 12.0 ± 0.5%).
According to the method described in first aspect present invention, wherein the storage requirement in step (7) is that temperature is the closed environment that 20-30 ℃, humidity are 50%-70%.
According to the method described in first aspect present invention, wherein the steam mixing warming and humidifying mode steam pressure described in step (8) is greater than 2.0bar(and is preferably 2.0~3.5bar, for example 2.2bar or 2.5bar or 3.0bar), amount of water is greater than 120L/h(and is preferably 120~160L/h, for example 140L/h or 150L/h);
Preferably, in step (8), pressing the pressure stalk gap of stalk equipment is the arbitrary numerical value (for example 0.7mm or 0.8mm) within the scope of 0.7-1.0mm.
According to the method described in first aspect present invention, wherein in step (9), can apply according to demand necessary feed liquid (for example feed liquid of flavouring, humectation).
According to the method described in first aspect present invention, wherein the steam pressure described in step (10) is for example 2.5bar, 3.0bar or 3.8bar of 2.0bar-4.0bar(),
Preferably, the dry employing drum drying equipment in step (10) is dried;
Preferably, the baking temperature in step (10) is 100-130 ℃ (for example 110 ℃ or 120 ℃);
The moisture content of the finished product stem preferably, obtaining in step (10) is 11-13%(preferably 12.5 ± 0.5% or 12.0 ± 0.5%).
A second aspect of the present invention provides a kind of stem, and it is prepared by the method described in first aspect present invention any one.
A third aspect of the present invention provides a kind of cigarette, wherein contains the stem described in second aspect present invention.
In the present invention, if described units of percent is without dated especially, be mass percent, described enzyme and related solution are food grade products.
In a specific embodiment of the present invention, the method described in first aspect present invention comprises the following steps:
(1) offal cleans and degraded: more than offal adopts the circulating protein enzyme liquid of temperature (40 ± 2) ℃, flow velocity≤5m/s to soak or cleans 10s, this enzyme liquid is neutral proteinase liquid, concentration is controlled between (0.5%~1.5%), after drainage, under the environment of temperature (25-30) ℃, store (4-8) h, obtain the offal that moisture content is (18-22) %, wherein, to adopt temperature be that (35-45) ℃, PH are that the water of (6-7), electrical conductivity≤50 μ s/cm is modulated to neutral proteinase liquid.
(2) regaining moisture of cabo and storage: gained offal, through conventional warming and humidifying device processes, obtains the offal that moisture content is 25%-30%.
(3) cabo expansion and pressure stalk: adopt high-temperature steam moisture regain offal more than 2.0bar, the expanded cabo that to obtain temperature (50-80) ℃, moisture content be 30%-40%, directly enter and press stalk equipment to press stalk, press stalk gap to be set in the arbitrary numerical value within the scope of (1.0-1.2) mm, the thick stalk sheet that to obtain even thickness, moisture content be (30-40) %.
(4) degraded of stalk sheet and storage: adopt conventional feed way, complex enzyme liquid is sprayed on thick stalk sheet according to a certain percentage, and be placed in temperature (30 ± 2) ℃, more than storing 6h in the environment of relative humidity (65 ± 5) %, obtaining moisture content is the stalk sheet of 30%-40%, wherein, complex enzyme is by pectase, cellulase and zytase form, in 1kg composite enzyme solution, pectase total activity is between (3,000,000 U~3000, ten thousand U), cellulase total activity is between (2,000,000 U~2000, ten thousand U), zytase total activity is between (1,000,000 U~1000, ten thousand U), the total activity ratio of each enzyme requires as 3:2:1, it is (40-50) ℃ that complex enzyme liquid adopts temperature, PH is (4-6), the water modulation of electrical conductivity≤50 μ s/cm.
(5) stalk sheet is reinforced: adopt conventional feed way, ratio according to >=1% is applied to additive feed liquid on stalk sheet, more than storage at normal temperature 0.5h, wherein, additive Main Function is to react with other component generation synthetic chemistries in (1), (4) gained catabolite and stalk sheet in the process of follow-up described technical method, plays the fragrant effect of producing.
(6) stalk sheet is dry: adopt drum drying equipment under the baking temperature condition of (100-130) ℃, the stalk sheet after storing to be dried, obtain the stick sheet that moisture content is (12.0 ± 0.5) %.
(7) stick sheet is stored: stick sheet is packed, in the closed environment that to be placed on (20-30) ℃, humidity be (50-70) %, store >=30 days, allow degraded afterproduct, outer doping, the original component of offal produce fragrant combined reaction.
(8) stick sheet moisture regain is expanded and is pressed stalk: adopt the steam mixing warming and humidifying mode stick sheet that gets damp again, wherein steam pressure should be greater than 2.0bar, amount of water should be greater than 120L/h, obtain the expansion stem sheet that temperature is (30-38) % for (50-80) ℃, moisture content, directly enter and press stalk equipment to press stalk, press stalk gap to be set in the arbitrary numerical value within the scope of (0.7-1.0) mm, the thin stalk sheet that to obtain even thickness, moisture content be (30-35%).
(9) cut stem and reinforced: the thin stalk sheet of gained is cut into conventional stem, applies according to demand necessary feed liquid.
(10) stem expansion is with dry: adopt pressure between the steam moisture regain stem of 2.0bar-4.0bar, then adopt drum drying equipment under (100-130) ℃ temperature conditions, to carry out stem and be dried, obtaining moisture content is (12.5 ± 0.5) % stem.
The method of raising cut stem quality provided by the invention has the following advantages:
(1) water to modulation enzyme liquid of the present invention has carried out index control, has effectively improved the vigor of enzyme, can improve degradation effect.
(2) the technology of the present invention adopts two-stage biological degraded, has solved the problem that several enzymes exist mutual inhibition simultaneously, can effectively improve the biodegradation effect of offal macromolecular components.
(3) the technology of the present invention offal steams stalk through biotechnology degraded and three high-temperature steams, can effectively remove the unfavorable component in offal, removes the assorted gas of stem.
(4) additive that the technology of the present invention is reacted at the after-applied product perfume of offal biodegradation, and produce perfume by the storage of roller drying and stick sheet, can significantly improve the flavor component content in offal.
(5) the technology of the present invention offal is directly pressed stalk through twice hot and humid expansion and twice, offal is pressed stalk after hot and humid expansion, press stalk technique to control by the pressure stalk gap of equipment, can improve and press stalk effect, improve qualification rate and the uniformity of stalk sheet thickness, increase the spalling degree of stalk sheet, promote offal to enzyme preparation, the absorption of additive, simultaneously, offal obstructs through twice pressure, stalk sheet can get damp again fast, after moisture regain, directly press stalk and cut stem, gained stem and pipe tobacco shape approach, be conducive to being mixed of stem and pipe tobacco, in cigarette, application has higher promotional value.
(6) after cigarette adds stem prepared by method of the present invention, odor characteristic is more clear, and fragrance qualitative change is good, and smoke behavior improves, and sophistication improves, and hamony is better, and assorted gas reduces, and dry sensation reduces, and mouthfeel is more comfortable.
The specific embodiment
Below in conjunction with embodiment, embodiment of the present invention are described in detail, but it will be understood to those of skill in the art that the following example is only for the present invention is described, and should not be considered as limiting scope of the present invention.Unreceipted actual conditions person in embodiment, carries out according to the condition of normal condition or manufacturer's suggestion.The unreceipted person of production firm of agents useful for same or instrument, being can be by the conventional products of commercial acquisition.
Embodiment 1
Adopt the neutral proteinase liquid that concentration is 1.0% to clean the offal of getting ready, under normal condition, store 4 hours, obtain the offal that moisture content is (19.0 ± 1.0) %, through warming and humidifying and normal condition, store afterwards, obtain the offal that moisture content is (27.0 ± 1.0) %, adopting pressure is the steam moisture regain offal of 3.0bar again, obtain temperature for (60 ± 3) ℃, moisture content is the expanded cabo of (31.0 ± 1.0) %, expanded cabo enters presses the pressure stalk equipment that stalk gap is 1.0mm to carry out offal extruding, obtain thick stalk sheet, then adopt conventional charging (feeding) equipment that complex enzyme liquid is applied on thick stalk sheet by 2% of offal weight, pectase in described complex enzyme liquid unit mass, cellulase, Xylanase activity is 9,000,000 U respectively, 6000000 U and 3,000,000 U, the thick stalk sheet applying after complex enzyme liquid is (30 ± 2) ℃ in temperature, under the condition that relative humidity is (60 ± 5) %, store 8 hours, (wherein the concentration of aspartic acid is 0.6% by the mixed liquor of aspartic acid and proline after storing, to adopt conventional charging (feeding) equipment, the concentration of proline is 0.4%) by 2.0% of offal weight, be applied on thick stalk sheet and store 1 hour, adopt afterwards drum drying equipment to obstruct sheet to be dried to moisture content be (12.0 ± 1.0) % for (110 ± 3) ℃ will wet in barrel temperature, gained stick sheet packs to store under routine storage condition and within 30 days, produces perfume, after storing, stick sheet is at steam pressure 2.2bar, add under the condition of discharge 150L/h and get damp again, obtain temperature for (60 ± 3) ℃, moisture content is the expansion stem sheet of (31.0 ± 1.0) %, enter and press the pressure stalk equipment that stalk gap is 0.70mm to obstruct sheet extruding, obtain thin stalk sheet, the thin stalk sheet of gained carries out routine and cuts stem, stem after cutting adopts the steam moisture regain expansion that pressure is 3.0bar (this stem carries out steam moisture regain expansion process after also can applying necessary humectation feed liquid again), then adopt drum drying equipment to dry stem, obtain the finished product stem that moisture content is (12.0 ± 0.5) %.
Embodiment 1 gained stem by analysis, make the stem comparison of (wash stalk, moisture regain, Terrier Storage, warming and humidifying, pressure stalk, cut stem, stem is reinforced, expand and be dried) with traditional handicraft, the cell wall substance contents such as pectin, cellulose and protein reduce, and total sugar content, flavor component total amount obviously improve, and stem flue gas is finer and smoother, odor characteristic is remarkable, concentration is moderate, and assorted tolerance reduces, and mouthfeel is more comfortable, pleasant impression is cleaner, and interior quality obviously improves.
Embodiment 1 gained stem and traditional stem (stem that above-mentioned traditional handicraft is made) are added in same cigarette tobacco leaf formulation with 10% ratio, pass through sensory quality assessment, comparative result shows that cigarette adds the stem of the embodiment of the present invention 1 preparation, fragrance matter, sophistication improve, assorted gas reduces, stimulate and reduce, pleasant impression is more comfortable, and overall quality improves.
Example 2
Adopt the neutral proteinase liquid that concentration is 1.5% to clean the offal of getting ready, under normal condition, store 6h, obtain the offal that moisture content is (21.0 ± 1.0) %, through warming and humidifying and normal condition, store afterwards, obtain the offal that moisture content is (29.0 ± 1.0) %, adopting pressure is the steam moisture regain offal of 3.5bar again, obtain temperature for (65 ± 3) ℃, moisture content is the expanded cabo of (33.0 ± 1.0) %, enter and press the pressure stalk equipment that stalk gap is 1.1mm to carry out offal extruding, obtain thick stalk sheet, then adopt conventional charging (feeding) equipment that complex enzyme liquid is applied on thick stalk sheet by 1.5% of offal weight, pectase in described complex enzyme liquid unit mass, cellulase, Xylanase activity is 1,500 ten thousand U respectively, 1000 ten thousand U and 5,000,000 U, the thick stalk sheet applying after complex enzyme liquid is (30 ± 2) ℃ in temperature, under the condition that relative humidity is (60 ± 5) %, store 10h, (wherein the concentration of aspartic acid is 0.6% for the aspartic acid that after storing, the conventional charging (feeding) equipment of employing is 1.2% by concentration and proline mixed liquor, the concentration of proline is 0.6%) by 2.0% of offal weight, be applied on thick stalk sheet and store 2h, adopt afterwards drum drying equipment to obstruct sheet to be dried to moisture content be (12.0 ± 1.0) % for (110 ± 3) ℃ will wet in barrel temperature, gained stick sheet packs to store under routine storage condition and within 45 days, produces perfume, after storing, stick sheet is at steam pressure 2.5bar, add under discharge 140L/h condition and get damp again, obtain temperature for (65 ± 3) ℃, moisture content is the expansion stem sheet of (33.0 ± 1.0) %, enter and press the pressure stalk equipment that stalk gap is 0.80mm to obstruct sheet extruding, obtain thin stalk sheet, the thin stalk sheet of gained carries out routine and cuts stem, the steam moisture regain expansion that the stem obtaining after cutting is 2.5bar through excess pressure (this stem carries out steam moisture regain expansion process after also can applying necessary feed liquid again), then adopt drum drying equipment to dry stem, obtain the finished product stem that moisture content is (12.0 ± 0.5) %.
Embodiment 2 gained stems by analysis, make the stem comparison of (wash stalk, moisture regain, Terrier Storage, warming and humidifying, pressure stalk, cut stem, stem is reinforced, expand with dry) with traditional handicraft, the cell wall substance total amounts such as pectin, cellulose reduce, total sugar content, the raising of flavor component total amount, stem flue gas is fine and smooth, odor characteristic is remarkable, and concentration is moderate, stimulates and reduces, assorted tolerance is few, comfortable taste, pleasant impression is clean, and interior quality obviously improves.
Embodiment 2 gained stems and traditional stem (stem that above-mentioned traditional handicraft is made) are added in seven wolves (red) cigarette with 12% ratio respectively, cigarette adds after the embodiment of the present invention 2 gained stems, odor characteristic is more clear, fragrance qualitative change is good, smoke behavior improves, sophistication improves, hamony is better, assorted gas reduces, dry sensation reduces, mouthfeel is more comfortable, interior quality obviously improves, simultaneously, in seven wolves (red) cigarette, stem ratio is brought up to 20% interpolation embodiment 2 gained stems from 12%, with original cigarette comparison, perfume quantity slightly reduces, strength sense improves, overall quality changes little.
Above are only the better scheme that the technology of the present invention is implemented, but design concept of the present invention is not limited to this, allly utilizes this design to carry out the change of unsubstantiality to the present invention, all should belong to the behavior of invading protection domain of the present invention.

Claims (12)

1. a method that improves cut stem quality, comprises following steps:
(1) offal cleans and degraded: offal adopts circulating protein enzyme aqueous solution soak or clean, and stores 4-8 hour after drainage, obtains moisture content and be 18%-22%(for example 19%, 21%) offal;
(2) regaining moisture of cabo and storage: step (1) gained offal through conventional warming and humidifying device processes, is obtained to moisture content and be 25%-30%(for example 27%, 29%) offal;
(3) cabo expansion and pressure stalk: adopt high-temperature steam moisture regain offal, obtain temperature 50-80 ℃ of (for example 60 ℃, 65 ℃), moisture content and be 30%-40%(for example 31%, 33%, 36%) expanded cabo, directly enter and press stalk equipment to press stalk, obtain the thick stalk sheet of even thickness;
(4) degraded of stalk sheet and storage: adopt conventional feed way, according to a certain percentage complex enzyme liquid is sprayed on thick stalk sheet, store 6 hours above (for example 8-10 hour);
(5) stalk sheet is reinforced: in proportion additive is applied on the stalk sheet of step (4) acquisition, and storage at normal temperature 0.5 hour above (for example 1-2 hour), wherein, described additive is Freamine Ⅲ;
(6) stalk sheet is dry: step (5) is obtained reinforced after stalk sheet be dried, obtain stick sheet;
(7) stick sheet is stored: the stick sheet that step (6) is obtained packs, and stores >=30 days (for example 30-45 days);
(8) stick sheet moisture regain is expanded and is pressed stalk: adopt steam the mixings warming and humidifying mode stalk sheet that gets damp again, obtain temperature for the expansion stem sheet that (50-80) ℃, moisture content are (30-38) %, directly enter and press stalk equipment to press to obstruct, obtain the thin stalk sheet of even thickness;
(9) cut stem: the thin stalk sheet of gained is cut into conventional stem, selectively applies according to demand necessary feed liquid;
(10) stem expansion is with dry: adopt steam moisture regain stem, then carry out stem and be dried, obtain finished product stem.
2. the process of claim 1 wherein that described protease is neutral proteinase, the preferred concentration of aqueous solution of protease is 0.5%~1.5%,
Preferably, to adopt temperature be that 35-45 ℃, PH are the water modulation of 6-7, electrical conductivity≤50 μ s/cm to neutral protein enzyme aqueous solution;
Preferably, the temperature of described circulation neutral proteinase liquid is 40 ± 2 ℃, flow velocity≤5m/s;
Preferably, the time of immersion or cleaning is more than 10 seconds;
Preferably, the storage temperature 25-30 ℃ in step (1).
3. the process of claim 1 wherein that the pressure of the high-temperature vapour described in step (3) is more than 2.0bar;
Preferably, the pressure stalk gap of the stalk of the pressure described in step (3) equipment is set in the arbitrary numerical value (for example 1.0mm or 1.1mm) within the scope of 1.0-1.2mm.
4. the process of claim 1 wherein that described complex enzyme is comprised of pectase, cellulase and zytase;
Preferably, in every kilogram of composite enzyme solution, pectase total activity is between ten thousand U of 3,000,000 U~3000, and cellulase total activity is between ten thousand U of 2,000,000 U~2000, and zytase total activity is between ten thousand U of 1,000,000 U~1000;
Preferably, in described composite enzyme solution the total activity of various enzymes than being preferably 3:2:1 for 2-4:1-3:0.5-1.5();
Preferably, the described addition that meets enzyme is (1~4) % of offal weight;
Preferably, to adopt temperature be that 40-50 ℃, PH are the water modulation of 4-6, electrical conductivity≤50 μ s/cm for described complex enzyme;
Preferably, the storage temperature described in step (4) is that 25-35 ℃ of (being preferably 30 ± 2 ℃), relative humidity are that 60-70%(is preferably 65 ± 5%).
5. the method for claim 1, wherein said amino acid is selected from glutamic acid, phenylalanine, aspartic acid, proline or its combination, be preferably the mixed solution of aspartic acid and proline, in preferred mixed solution, aspartic acid and proline mass ratio are 1~1.5 ︰ 1;
Preferred amino acid concentration is 0.1~2.0%(for example 0.5%, 1.%, 1.2%, 1.5% or 1.8%);
Preferably, the consumption of described additive is stalk the more than 1.0% of tablet quality (be preferably 1.0%~3.0%, for example 1.5%, 1.8% or 2.0%).
6. the process of claim 1 wherein that the dry employing drum drying equipment in step (6) is dried;
Preferably, the baking temperature in step (6) is 100-130 ℃ (for example 110 ℃ or 120 ℃);
The moisture content of the stick sheet preferably, obtaining in step (6) is 10-13%(for example 12 ± 0.5%).
7. the process of claim 1 wherein that storage requirement in step (7) is that temperature is the closed environment that 20-30 ℃, humidity are 50%-70%.
8. the method for claim 1, wherein the steam pressure of the steam mixing warming and humidifying mode described in step (8) is greater than 2.0bar(and is preferably 2.0~3.5bar, for example 2.2bar or 2.5bar or 3.0bar), amount of water is greater than 120L/h(and is preferably 120~160L/h, for example 140L/h or 150L/h)
Preferably, in step (8), pressing the pressure stalk gap of stalk equipment is the arbitrary numerical value (for example 0.7mm or 0.8mm) within the scope of 0.7-1.0mm.
9. the process of claim 1 wherein in step (9) and can apply according to demand necessary feed liquid (for example feed liquid of flavouring, humectation).
10. the process of claim 1 wherein that the pressure of the steam described in step (10) is for example 2.5bar, 3.0bar or 3.8bar of 2.0bar-4.0bar(),
Preferably, the dry employing drum drying equipment in step (10) is dried;
Preferably, the baking temperature in step (10) is 100-130 ℃ (for example 110 ℃ or 120 ℃);
The moisture content of the finished product stem preferably, obtaining in step (10) is 10-13%(for example 12.5 ± 0.5% or 12.0 ± 0.5%).
11. 1 kinds of stems, it is prepared by the method described in claim 1-10 any one.
12. 1 kinds of cigarette, wherein contain the stem described in claim 11.
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