CN101935962A - Production method of tipping base cigarette paper with high natural air permeability - Google Patents
Production method of tipping base cigarette paper with high natural air permeability Download PDFInfo
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Abstract
The invention relates to a production method of tipping base paper with high natural air permeability as well as cigarette paper. The production method of the tipping base cigarette paper with the high natural air permeability comprises a pulping step, a papermaking step and a calendaring step; in the pulping step, softwood pulp, eucalyptus pulp and Spain straw pulp are respectively pulped, the softwood pulp has the pulping concentration of 3.4-3.6 percent, the beating degree/ wet weight of 66-680 SR/8-11g, the eucalyptus pulp has the pulping concentration of 3.6-3.8 percent and the beating degree of 20-220 SR, the Spain straw pulp has the beating degree of 18-220 SR; and 40-60 percent of softwood pulp, 30-40 percent of eucalyptus pulp and 10-20 percent of Spain straw pulp which are well-pulped are proportioned. The invention has higher air permeability and obvious action of diluting mainstream smoke, can greatly decrease the production cost and improve the production efficiency without static electricity or laser printing, the favorable combination strength can satisfy the requirement of a high-speed printer, the base paper is smooth and fine, has good oil print leveling effect and is fully suitable for the production requirement of a gravure printing machine.
Description
Technical field
The present invention relates to cigarette paper, particularly a kind of production method of high natural permeable degree body paper for tobacco-use tipping paper.
Background technology
Along with the quickening of globalization of world economy process and the continuous progress and the fast development of national economy of Chinese society, especially after China became a full member of WTO and signature WHO " Framework Convention on Tobacco Control ", Chinese cigarette and tobacco leaf market internationalization level were deepened day by day, market competition is growing more intense.Health problem more and more is subjected to the extensive concern of society, carries forward vigorously the cigarette lowering harm and decreasing coking, makes great efforts to promote the industry technology innovation level, and is significant for the tobacco business reform and development; On the other hand, " level on the cigarette " work has also proposed new, higher requirement to Chinese style cigarette lowering harm and decreasing coking, and lowering harm and decreasing coking has become lifting Chinese style cigarette core competitiveness, the important channel of realizing level on the cigarette.For reaching the requirement of lowering harm and decreasing coking, the burnt means of falling that domestic enterprise adopts mainly still adopt the physics that adds expanded cut tobacco, stem to fall Jiao, select the low tobacco leaf leaf group of nicotine content; Use the cooperation of tow, high natural permeable degree filter rod forming paper and the perforated tipping paper of different size, perhaps use special-shaped mouth rod to reach the purpose of reducing tar and reducing harm.And perforated tipping paper is to adopt laser or static to punch in advance, exists production efficiency to hang down shortcomings such as reaching the cost height.
Summary of the invention
Technical problem to be solved by this invention is: the production method that the low high natural permeable degree body paper for tobacco-use tipping paper of a kind of production efficiency height and cost is provided.
Technical solution of the present invention is: it comprises the steps:
(1), beater floor, respectively to softwood pulp, eucalyptus pulp and esparto pulp making beating, the softwood pulp beating consistency is 3.4～3.6%, beating degree/weight in wet base is 66～68
0Between SR/8～11g; The eucalyptus pulp beating consistency is 3.6～3.8%, beating degree is 20～22
0Between the SR; The esparto pulp beating degree is 18～22
0Between the SR; Join slurry by weight softwood pulp, eucalyptus pulp and the esparto pulp that will accomplish fluently slurry with the ratio of 40～60%:30～40%:10～20%;
(2), machine hand's section, in the slurry for preparing, attach neutral sizing agent alkyl ketene dimer and wet strength agent polyamide polyamines-epichlorohydrin resins, and add the double base retention agent that cationic polyacrylamide and cationic starch are formed, be shaped through wet end and press section dehydration then, do the stage before the l Water Paper page or leaf enters, table is coated with oven dry again behind the composite mixture of printability agent acrylic resin and oxidized starch;
(3), press polish workshop section, the body paper after the oven dry carries out press polish.
Technique effect of the present invention is: it has higher air permeability, and the effect of dilution main flume is obvious; Need not static or laser boring, can reduce production costs greatly, enhance productivity; Its good binding intensity can satisfy the high-speed press requirement; Body paper is level and smooth, fine and smooth, and the printing ink levelling is effective, adapts to the intaglio press production requirement fully.
High natural permeable degree tipping paper body paper, need not the effect that static or laser boring and high natural permeable degree filter rod forming paper fit applications have the dilution main flume, and in printing process, can intactly contact with the picture and text of forme, can finish ink transfer equably, make picture and text clear, full.
High natural permeable degree body paper for tobacco-use tipping paper is compared with common tipping paper body paper, network of fibers with loose structure, higher air permeability is arranged, the abundant brooming of common tipping paper body paper fiber in paper-making process, and add filler such as calcium carbonate, fiber leans on hydrogen bonded together, and porosity is very low, and the natural permeable degree is higher than 10CU hardly.And high natural permeable degree tipping paper body paper is guaranteeing that tensile strength satisfies under the prerequisite of print request, and the natural permeable degree can reach (60～80) CU.
Adopt high natural permeable degree body paper for tobacco-use tipping paper, effect is to utilize the nature hole that air is introduced in the main flume of cigarette, and the composition in the main flume is reduced relatively, thereby reduces the tar content that human body is taken in, and reaches the purpose of harm reduction tar.In actual applications, the ventilation filter tip is the tipping paper and high saturating filter rod forming paper fit applications that adopts laser or the pre-punching of static, and coupling reduces cigarette tar content mutually.And the tipping paper of high natural permeable degree need not laser or static punches in advance, with the saturating filter rod forming paper of high fit applications, tar in the flue gas, nicotine, carbon monoxide content all can reduce because of the ventilation dilution effect, and in general, the minimizing of nicotine is less, and carbon monoxide is owing to when smoking, can outwards spread the reduction maximum by the nature hole.For example: when the flue gas dilution rate was 33.3%, the dilution rate of nicotine only was 25%, and the dilution rate of carbon monoxide then is 40%.
The specific embodiment
The present invention has the eucalyptus pulp and esparto pulp (the Test climate ISO 187:50%relative Humidity HR of the effect that improves the body paper air permeability by adapted; 23
0C magma air permeability 350～650cm
3/ m.Pa.s), carry out beating after, make that eucalyptus pulp and esparto pulp and softwood pulp are sufficient to be combined, under the prerequisite that keeps high natural permeable degree, handle through top sizing and press polish.
The production method of high natural permeable degree body paper for tobacco-use tipping paper comprises the steps:
(1), beater floor, adopt two disks mills respectively to softwood pulp, eucalyptus pulp and esparto pulp continuous beating, the softwood pulp beating consistency is 3.4～3.6%, beating degree/weight in wet base is 66～68
0Between SR/8～11g; The eucalyptus pulp beating consistency is 3.6～3.8%, beating degree is 20～22
0Between the SR; Esparto pulp (Test climate ISO 187:50%relative Humidity HR; 23
0C, magma air permeability 350～650cm
3/ m.Pa.s) beating degree is 18～22
0Between the SR; Join slurry by weight softwood pulp, eucalyptus pulp and the esparto pulp that will accomplish fluently slurry with the ratio of 40～60%:30～40%:10～20%;
(2), machine hand's section, in the slurry for preparing, adopt the mode that attaches continuously to attach neutral sizing agent alkyl ketene dimer and wet strength agent polyamide polyamines-epichlorohydrin resins, and in the mixed pulp for preparing, add the double base retention agent that cationic polyacrylamide and cationic starch are formed, then after wet end and press section dehydration shaping, do the stage before the l Water Paper page or leaf enters, continue oven dry again after the agent machine shows to be coated with the composite mixture of printability agent acrylic resin and oxidized starch through executing;
(3), press polish workshop section, the body paper after the oven dry carries out press polish.
The solid content of described neutral sizing agent alkyl ketene dimer is 10%, and its tret that adds in paper pulp is 0.02～0.38% of a paper pulp gross weight.
The solid content of described wet strength agent polyamide polyamines-epichlorohydrin resins is 15%, and its tret that adds in paper pulp is 0.15～0.30% of a paper pulp gross weight.
The molecular weight of described cationic polyacrylamide is 7,000,000, and the substitution value of cationic starch is 0.25, and the dosage of cationic polyacrylamide is 0.11 of paper pulp gross weight～0.13 ‰, and the dosage of cationic starch is 0.8～1.2% of a paper pulp gross weight.
The dosage of described surperficial printability agent acrylic resin accounts for 1/10～1/2 of over dry oxidized starch amount, and the oxidized starch table is coated with concentration 2～4%.
Body paper adopts soft press-polishing machine to carry out press polish, and the linear pressure of soft press-polishing machine is 195～264kN/m in the press polish workshop section.
Embodiment one,
Present embodiment adopts the making beating mode of low concentration, by eucalyptus pulp and esparto pulp are carried out light cutter (low specific beating pressure) beating, alleviates branch silk, the brooming effect of fiber as far as possible, makes body paper have good natural porosity; Softwood pulp is adopted the first swollen making beating mode of beating again, make long fiber obtain certain brooming effect, the more hydroxyl that can dissociate improves the bond strength with staple fibre, satisfies the double requirements of high natural permeable degree and good combination intensity.
Beater floor adopts two disks mill continuous beatings, and the softwood pulp beating consistency is 3.8%, beating degree guarantees 66～68
0Between the SR; The eucalyptus pulp beating consistency is 3.6%, beating degree guarantees 20～22
0Between the SR; The esparto pulp beating consistency is 3.6%, beating degree guarantees 20～22
0Between the SR; It is stand-by that softwood pulp, eucalyptus pulp and the esparto pulp of accomplishing fluently slurry joined slurry with the ratio of weight 40%:40%:20%;
Machine hand's section, in the mixed pulp for preparing, adopt the mode that attaches continuously to attach neutral sizing agent AKD (alkyl ketene dimer) and wet strength agent PAE(polyamide polyamines-epichlorohydrin resins), and in the mixed pulp for preparing, attach the CPAM(cationic polyacrylamide) and the double base retention agent formed of cationic starch, then after wet end and press section dehydration shaping, do the stage before the l Water Paper page or leaf enters, continue again to dry after the agent machine shows to be coated with the composite mixture of printability agent (acrylic resin) and oxidized starch through executing;
Press polish workshop section, body paper after the oven dry adopts soft press-polishing machine to carry out press polish (to make product have smoothness height, characteristic that glossiness is good, can make tipping paper obtain splendid levelling effect and perfect printing figure message), produce the finished product body paper for tobacco-use tipping paper, the natural permeable degree is 70～80.
The solid content of neutral sizing agent AKD (alkyl ketene dimer) is 10%, and it adds (0.02～0.38) % that tret is the paper pulp gross weight in paper pulp, and it is used for controlling the water imbibition of body paper for tobacco-use tipping paper.
Wet strength agent PAE(polyamide polyamines-epichlorohydrin resins) solid content is 15%, and its tret that adds in paper pulp is 0.15～0.30% of a paper pulp gross weight, and it is used for controlling an anti-wet strength and the laterally green deformation of body paper for tobacco-use tipping paper.
The CPAM(cationic polyacrylamide) molecular weight is 7,000,000, the substitution value of cationic starch is 0.25, the CPAM(cationic polyacrylamide) and cationic starch cook retention agent jointly and improve retention rate, the CPAM dosage is a paper pulp gross weight (0.11～0.13) ‰, the dosage of cationic starch is 0.8～1.2% of a paper pulp gross weight, guarantees that paper evenness is good.
The linear pressure of soft press-polishing machine is 195～264kN/m in the press polish workshop section, becomes paper light face smoothness to reach more than the 200s.
Embodiment two,
Softwood pulp, eucalyptus pulp and esparto pulp are joined slurry with the ratio of weight 50%:30%:20%, and all the other are identical with embodiment one.The finished product body paper for tobacco-use tipping paper that present embodiment is produced, natural permeable degree are 70～80.
Embodiment three,
Softwood pulp, eucalyptus pulp and esparto pulp are joined slurry with the ratio of weight 60%:30%:10%, and all the other are identical with embodiment one.The finished product body paper for tobacco-use tipping paper that present embodiment is produced, natural permeable degree are 60～75.
The high natural permeable degree body paper for tobacco-use tipping paper method of inspection is carried out according to following standard method:
YC/T 172 cigarette paper, shaping paper, tipping paper and have the mensuration (YC/T 172-2002, ISO 2965:IDT) of the material air permeability of directed air permeable belt
The mensuration of GB/T 456 paper and cardboard smoothness (Buick method) (GB/T 456-2002, idt ISO 5627:1995)
GB/T 1540 paper and the absorptive mensuration of cardboard (Cobb method) (GB/T 1540-2002, neq ISO 535:1991)
The mensuration of GB/T 12914-2008 paper and cardboard tensile strength (ISO 1924-1:1992, MOD; ISO 1924-2:1994)
Mensuration diffusion/the normal beam technique of GB/T 7974 paper, cardboard and brightness of pulp (whiteness) (GB/T 7974-2002, neq ISO 2470:1999)
The mensuration diffuse reflection method of GB/T 1543 paper and cardboard opacity (paper backing) (GB/T 1543-2005, ISO 2471:1998, MOD)
The mensuration of GB/T 2679.15 paper and cardboard printing surface strength (electronic accelerated process) (GB/T 2679.15-1997, eqv ISO 3783:1980)
The mensuration of GB/T 459 paper and cardboard retractility (GB/T 459-2002, eqv ISO 5635:1978).
Claims (6)
1. the production method of high natural permeable degree body paper for tobacco-use tipping paper is characterized in that it comprises the steps:
(1), beater floor, respectively to softwood pulp, eucalyptus pulp and esparto pulp making beating, the softwood pulp beating consistency is 3.4～3.6%, beating degree/weight in wet base is 66～68
0Between SR/8～11g; The eucalyptus pulp beating consistency is 3.6～3.8%, beating degree is 20～22
0Between the SR; The esparto pulp beating degree is 18～22
0Between the SR; Join slurry by weight softwood pulp, eucalyptus pulp and the esparto pulp that will accomplish fluently slurry with the ratio of 40～60%:30～40%:10～20%;
(2), machine hand's section, in the slurry for preparing, attach neutral sizing agent alkyl ketene dimer and wet strength agent polyamide polyamines-epichlorohydrin resins, and add the double base retention agent that cationic polyacrylamide and cationic starch are formed, be shaped through wet end and press section dehydration then, do the stage before the l Water Paper page or leaf enters, table is coated with oven dry again behind the composite mixture of printability agent acrylic resin and oxidized starch;
(3), press polish workshop section, the body paper after the oven dry carries out press polish.
2. the production method of high natural permeable degree body paper for tobacco-use tipping paper as claimed in claim 1 is characterized in that the solid content of described neutral sizing agent alkyl ketene dimer is 10%, and its tret that adds in paper pulp is 0.02～0.38% of a paper pulp gross weight.
3. the production method of high natural permeable degree body paper for tobacco-use tipping paper as claimed in claim 1, it is characterized in that, the solid content of described wet strength agent polyamide polyamines-epichlorohydrin resins is 15%, and its tret that adds in paper pulp is 0.15～0.30% of a paper pulp gross weight.
4. the production method of high natural permeable degree body paper for tobacco-use tipping paper as claimed in claim 1, it is characterized in that, the molecular weight of described cationic polyacrylamide is 7,000,000, the substitution value of cationic starch is 0.25, the dosage of cationic polyacrylamide is 0.11 of paper pulp gross weight～0.13 ‰, and the dosage of cationic starch is 0.8～1.2% of a paper pulp gross weight.
5. the production method of high natural permeable degree body paper for tobacco-use tipping paper as claimed in claim 1 is characterized in that the dosage of described surperficial printability agent acrylic resin accounts for 1/10～1/2 of over dry oxidized starch amount, and the oxidized starch table is coated with concentration 2～4%.
6. the production method of high natural permeable degree body paper for tobacco-use tipping paper as claimed in claim 1 is characterized in that, body paper adopts soft press-polishing machine to carry out press polish, and the linear pressure of soft press-polishing machine is 195～264kN/m in the press polish workshop section.
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| CN2010102744126A CN101935962B (en) | 2010-09-07 | 2010-09-07 | Production method of tipping base cigarette paper with high natural air permeability |
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|---|---|---|---|
| CN2010102744126A CN101935962B (en) | 2010-09-07 | 2010-09-07 | Production method of tipping base cigarette paper with high natural air permeability |
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Cited By (21)
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| CN102180979A (en) * | 2011-03-12 | 2011-09-14 | 牡丹江恒丰纸业股份有限公司 | Cationization modification method for nano-crystalline cellulose and preparation method of high-strength cigarette paper |
| CN102926250A (en) * | 2012-11-15 | 2013-02-13 | 贵州省赤水华龙纸业有限公司 | Novel technology for papermaking through waste paper with low cost and high purity |
| CN102936865A (en) * | 2012-10-18 | 2013-02-20 | 民丰特种纸股份有限公司 | Transparent tipping paper production method |
| CN103103859A (en) * | 2013-02-26 | 2013-05-15 | 牡丹江恒丰纸业股份有限公司 | Production method of base paper of tipping paper used by cigarettes with high natural air permeability |
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| CN104428466A (en) * | 2012-07-09 | 2015-03-18 | 德尔福特集团有限公司 | Cigarette paper with improved air-permeability |
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| CN112482092B (en) * | 2020-11-25 | 2022-12-30 | 牡丹江恒丰纸业股份有限公司 | Production process of transparent hand cigarette paper |
| CN115341403A (en) * | 2022-05-07 | 2022-11-15 | 浙江唐丰特种纸有限公司 | Production method of high-smoothness tipping base paper for cigarettes |
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