CN103082392B - Dry-type paper-making method reengineering tobacco production process - Google Patents

Dry-type paper-making method reengineering tobacco production process Download PDF

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CN103082392B
CN103082392B CN201310006837.2A CN201310006837A CN103082392B CN 103082392 B CN103082392 B CN 103082392B CN 201310006837 A CN201310006837 A CN 201310006837A CN 103082392 B CN103082392 B CN 103082392B
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spraying
substrate
dry
setting
drying
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CN103082392A (en
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胡旺顺
梅建华
韩星
代远刚
谭新良
殷飞
刘刚
柏栋梁
葛继武
朱忠元
邱兴中
周瑾
钟科军
刘建福
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Guangzhou Jinye Science & Technology Development Co., Ltd.
China Tobacco Hunan Industrial Co Ltd
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Guangzhou Jinye Science & Technology Development Co Ltd
China Tobacco Hunan Industrial Co Ltd
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Abstract

The invention discloses a dry-type paper-making method reengineering tobacco production process which is characterized in that tobacco fibrous raw materials, or fluff pulp fibrous raw materials, or tobacco and fluff pulp fibrous raw materials are manufactured into base pieces with a high filling value through a dry-method paper-making machine by utilizing an airflow sedimentation method, tobacco powder and rubber mixture are sprayed on the front side and the reverse side of each core base piece, the base pieces are made into tobacco sheet finished products through drying and follow-up procedures, a negative pressure vacuum drawing way is adopted for spraying, the sprayed tobacco powder and the rubber mixture are absorbed in the core base pieces in an attaching mode, and the process is a way of spraying-drying and secondary spraying-drying. A coating rate of the manufactured tobacco sheet finished products is larger than or equal to 46%, the filling value is larger than or equal to 6.0 cm<3>/g, and water content is smaller than or equal to 12%.

Description

Dry type paper-making method recreated tobacco production technology
Technical field
The present invention relates to a kind of dry type paper-making method recreated tobacco production technology, be specially and outer fibre or baccy fiber are manufactured paper with pulp into sandwich layer substrate by dry method air forming device, again substrate double-face spray painting tobacco powder and glue class mixture post-drying shaping, belong to cigarette industry reconstituted tobacco technical field.
Background technology
The reconstituted tobacco of cigarette industry is by materials such as the offal produced in Cigarette processing process, broken stalk, fragments, through technical finesse and reconfigure and be processed into sheet or thread reconstituted tobacco product (being also reconstituted tobacoo), reconstituted tobacco has concurrently saves raw tobacco material and can the advantage such as flexible modulation cigarette physicochemical property.Known reconstituted tobacco production method mainly contains roll-in method, thick slurry processes, wet paper manufacturing method and dry type paper process etc., and current take wet paper manufacturing method as main flow, and dry type paper process is in developing stage.The feature of wet paper manufacturing method reconstituted tobacco production technology is first manufactured paper with pulp containing tobacco material and additional ingredients substrate, reduction coating fluid is coated with and drying and moulding again at substrate positive and negative, known coating method has roll-type transfer coated, spraying coating, the coating of V-type tunnel and folder net dip-coating coating etc., and described coating fluid is the medicinal extract of extract modulation or tobacco powder and adhesive mixture.
Improve the selected objective target that spreading rate is reconstituted tobacco industry, the reconstituted tobacoo of manufacturing paper with pulp by YC/T16.3-2003 standard, spreading rate >=40%; On the other hand, improving reconstituted tobacco Filling power, is the effective way of cigarette industry reducing tar and reducing harm.The parameters such as spreading rate and substrate surface are long-pending, mass dryness fraction and Filling power are closely related, and the substrate that wet paper manufacturing method is manufactured paper with pulp, because of reasons such as Filling power are low, poor air permeability, surface roughness are inadequate, is difficult to reach spreading rate>=46%, Filling power>=6.0cm 3/ g index.
In domestic and international published patent or document, method about dry type paper-making method recreated tobacco has multiple, one of them is Chinese invention patent " a kind of dry type paper-making method recreated tobacco and production method thereof " (application number: after being mixed with outer fiber starch by tobacco powder 200810030146.5), be settled down to shaped substrate on forming net by wind stream of supplying gas, more evenly spray trace adhesive, even spread concentrated extract on the substrate, 00808488.2) and " the dry autofrettage of filamentary tobacco and obtained product " (application number: 85105001) of applying in China of Kimberley-Clark Corporation of the U.S. another kind is patent of invention " reconstituted tobacoo and manufacture method and manufacturing system " thereof (application number: that Japan tobacco Inc applies in China, adopt sandwich-type moulding process, first plus fiber is settled down to shaping bottom substrate on forming net (making again load hold layer) by wind stream of supplying gas, uniform spreading last layer tobacco powder and glue mixture interlayer on bottom substrate again, afterwards on interlayer air flow settlement one deck plus fiber become surface layer and compress be dried into reconstituted tobacco, utility model patent " paper-making method reproduced tobacco leaf tobacco powder spraying type coating machine " (application number: 200720157214.5) is that the substrate produced for wet paper manufacturing method carries out spraying coating content, comprise about two deflector rolls be arranged in parallel, the positive and negative both sides of two deflector roll internal common tangent planes are respectively provided with the nozzle of one group of adjustable spray angle, by described nozzle by tobacco powder and amylan mixture double-face spray painting on substrate, due to the relatively fine and close and poor air permeability of substrate, therefore described tobacco powder and amylan mixture can only adhere to over the substrate surface, can not deeply penetrate in substrate internal layer section.
A kind of by baccy fiber raw material or fluff pulp fibers raw material or (baccy fiber+fluff pulp fibers) raw material by dry method of paper-making machine, utilize air flow settlement method, the higher (>=6.0cm of Filling power of manufacturing paper with pulp out 3/ g) substrate, then on substrate coating reduction medicinal extract or tobacco powder class effective ingredient, drying and subsequent handling, make reconstituted tobacoo finished product, reaches spreading rate>=46%, Filling power>=6.0cm 3the process of/g index, does not see in patent database or the open Reporting of document.
Summary of the invention
The object of the invention is asked a question for background technology, a kind of dry type paper-making method recreated tobacco production technology is disclosed, by dry method of paper-making machine by baccy fiber raw material or fluff pulp fibers raw material or (baccy fiber+fluff pulp fibers) raw material, utilize air flow settlement method, the substrate that Filling power of manufacturing paper with pulp out is higher, again after the positive and negative spraying tobacco powder and glue class mixture of described sandwich layer substrate, drying and subsequent handling, reconstituted tobacoo finished product spreading rate>=46%, the Filling power>=6.0cm that make 3/ g, moisture≤12%.
Technical scheme of the present invention is: dry type paper-making method recreated tobacco production technology, it is characterized in that: by baccy fiber raw material or fluff pulp fibers raw material or baccy fiber+fluff pulp fibers raw material by dry method of paper-making machine, utilize air flow settlement method, the substrate that Filling power of manufacturing paper with pulp out is higher, again after the positive and negative spraying tobacco powder and glue class mixture of described sandwich layer substrate, drying and subsequent handling, the reconstituted tobacoo finished product made; Adopt negative-pressure vacuum Smoking regime during spraying, the tobacco powder of ejection and glue class mixture are adsorbed in sandwich layer substrate; Process is spraying-oven dry, then sprays-drying mode again; Mass dryness fraction >=80% of setting raw material; Described drying mode is by setting bake out temperature, adopts hot-air through type drying box to dry the substrate after spraying, described shaping, spraying vacuum draw, stoving process route are as follows:
(1) measure pulverizing: the baccy fiber raw material of mass dryness fraction>=80% or fluff pulp fibers raw material or baccy fiber and fluff pulp fibers compound are delivered to dry method air flow settlement moulded head charging aperture by airduct, and in setting conveying airduct, fibre concentration is 1 ~ 6g/m 3;
(2) substrate is shaping: the substrate that manufacture paper with pulp on the dry method of paper-making machine air flow settlement moulded head baccy fiber raw material or fluff pulp fibers raw material or baccy fiber and fluff pulp fibers compound form, and setting substrate is quantitatively 18 ~ 45g/m 2, mass dryness fraction>=85%;
(3) once spray: at substrate front spraying tobacco powder and glue class mixture, substrate reverse side negative-pressure vacuum suction during spraying, setting spraying oven-dry weight is 15 ~ 35g/m 2;
(4) first drying: once spray meron and send hot-air through type drying box to dry to mass dryness fraction >=85%, setting hot blast temperature 80 ~ 150 DEG C;
(5) secondary spraying: at substrate reverse side spraying tobacco powder and glue class mixture, negative-pressure vacuum suction in substrate front during spraying, setting spraying oven-dry weight is 18 ~ 36g/m 2;
(6) secondary drying: second time spraying meron send hot-air through type drying box to dry to mass dryness fraction >=85%, and setting hot blast temperature 80 ~ 150 DEG C, prepares FINISHED.
Dry type paper-making method recreated tobacco production technology as above, is characterized in that: the mixed proportion of described baccy fiber and fluff pulp fibers compound is 1:1 ~ 5 by mass percentage.
Dry type paper-making method recreated tobacco production technology as above, is characterized in that: the finished product reconstituted tobacoo Con trolling index adopting above-mentioned technique to prepare comprises quantitative 70 ~ 110g/m 2, spreading rate>=46%, Filling power>=6.0cm 3/ g, moisture≤12%.
The invention has the beneficial effects as follows: adopt the reconstituted tobacoo finished product that production technology of the present invention is processed, its index such as spreading rate, Filling power is all better than 4.4.1 item regulation requirement in wet paper manufacturing method reconstituted tobacco standard YC/T 16.3-2003.
Accompanying drawing explanation
Fig. 1 is embodiment of the present invention process flow diagram.
Mark in accompanying drawing: 1-moulded head, 2-spray nozzle, 3-number negative-pressure ward case, 4-number drying box, 5-secondary spray nozzle, 6-No. two negative-pressure ward casees, 7-No. two drying boxes, 8-substrate, 9-finished product book sheet, 11-feeding airduct.
Detailed description of the invention
Be described in further detail below in conjunction with the enforcement of accompanying drawing to technical scheme:
Be illustrated in figure 1 dry type paper-making method recreated tobacco technological process of production schematic diagram of the present invention, in figure, baccy fiber raw material or fluff pulp fibers raw material or baccy fiber and fluff pulp fibers compound are delivered to dry method of paper-making machine moulded head 1 by airduct 11, utilize air flow settlement method, the higher (>=6.0cm of Filling power of manufacturing paper with pulp out 3/ g) substrate 8, tobacco powder and glue class mixture is successively sprayed again on substrate 8 positive and negative, negative-pressure vacuum Smoking regime is adopted during spraying, the tobacco powder of ejection and glue class mixture are firmly adsorbed in the substrate, by setting bake out temperature during oven dry, substrate 8 after adopting hot-air through type drying box to dry spraying, makes tobacco FINISHED 9.That control FINISHED 9 is quantitatively 70 ~ 110g/m 2, spreading rate>=46%, Filling power>=6.0cm 3/ g, moisture≤12%.
Shaping, spraying vacuum draw, stoving process route are set as follows:
Embodiment one, setting FINISHED are quantitatively 70g/m 2, spreading rate ≈ 78%, Filling power ≈ 7.0cm 3/ g.
(1) measure pulverizing: the fluff pulp fibers raw material of mass dryness fraction>=80% is delivered to dry method air flow settlement moulded head 1 by feeding airduct 11, in setting feeding airduct, fibre concentration is 1.5g/m 3;
(2) substrate is shaping: substrate of manufacturing paper with pulp on dry method of paper-making machine air flow settlement moulded head 1, and setting substrate is quantitatively 18g/m 2, moisture 85%;
(3) once spray: at substrate 8 front spraying tobacco powder and glue class mixture, during spraying, substrate 8 reverse side has negative-pressure ward case 3 negative-pressure vacuum to aspirate, setting spraying oven-dry weight is 24.0g/m 2;
(4) first drying: first time spraying meron 8 send a drying box 4 to dry to mass dryness fraction >=85%, setting hot blast temperature 125 DEG C;
(5) secondary spraying: at substrate 8 reverse side spraying tobacco powder and glue class mixture, during spraying, substrate 8 front has negative-pressure ward case 6 negative-pressure vacuum to aspirate, setting spraying oven-dry weight is 24.2g/m 2;
(6) secondary drying: second time spraying meron 8 send No. two drying boxes 7 to dry to mass dryness fraction >=88%, and setting hot blast temperature 130 DEG C, makes FINISHED 9.
Embodiment two, setting FINISHED are quantitatively 110g/m 2, spreading rate ≈ 64.8%, Filling power ≈ 6.3cm 3/ g, moisture≤12%, wherein non-tobacco class material ≈ 32%.
(1) measure pulverizing: the fluff pulp fibers of mass dryness fraction>=80% and cigarette fiber mixture are delivered to dry method air flow settlement moulded head 1 by feeding airduct 11, in setting feeding airduct, fibre concentration is 6g/m 3, the mixed proportion of setting baccy fiber and fluff pulp fibers compound is 1:4 by mass percentage;
(2) substrate is shaping: substrate of manufacturing paper with pulp on dry method of paper-making machine air flow settlement moulded head 1, and setting substrate is quantitatively 40g/m 2, moisture 85%;
(3) once spray: at substrate 8 front spraying tobacco powder and glue class mixture, during spraying, substrate 8 reverse side has negative-pressure ward case 3 negative-pressure vacuum to aspirate, setting spraying oven-dry weight is 31.4g/m 2;
(4) first drying: first time spraying meron 8 send a drying box 4 to dry to mass dryness fraction >=85%, setting hot blast temperature 135 DEG C;
(5) secondary spraying: at substrate 8 reverse side spraying tobacco powder and glue class mixture, during spraying, substrate 8 front has negative-pressure ward case 6 negative-pressure vacuum to aspirate, setting spraying oven-dry weight is 31.4g/m 2;
(6) secondary drying: second time spraying meron 8 send No. two drying boxes 7 to dry to mass dryness fraction >=88%, and setting hot blast temperature 130 DEG C, makes FINISHED 9.
Embodiment three, setting FINISHED are quantitatively 90g/m 2, spreading rate ≈ 51%, Filling power ≈ 6.0cm 3/ g, moisture≤12%, wherein non-tobacco class material ≈ 3%.
(1) measure pulverizing: the cigarette fiber material of mass dryness fraction>=80% is delivered to dry method air flow settlement moulded head 1 by feeding airduct 11, in setting feeding airduct, fibre concentration is 3g/m 3;
(2) substrate is shaping: substrate of manufacturing paper with pulp on dry method of paper-making machine air flow settlement moulded head 1, and setting substrate is quantitatively 45g/m 2, moisture 85%;
(3) once spray: at substrate 8 front spraying tobacco powder and glue class mixture, during spraying, substrate 8 reverse side has negative-pressure ward case 3 negative-pressure vacuum to aspirate, setting spraying oven-dry weight is 20g/m 2;
(4) first drying: first time spraying meron 8 send a drying box 4 to dry to mass dryness fraction >=85%, setting hot blast temperature 130 DEG C;
(5) secondary spraying: at substrate 8 reverse side spraying tobacco powder and glue class mixture, during spraying, substrate 8 front has negative-pressure ward case 6 negative-pressure vacuum to aspirate, setting spraying oven-dry weight is 20.4g/m 2;
(6) secondary drying: second time spraying meron 8 send No. two drying boxes 7 to dry to mass dryness fraction >=88%, and setting hot blast temperature 130 DEG C, makes FINISHED 9.
Below by reference to the accompanying drawings the specific embodiment of the present invention and FINISHED measurement result are described; but these explanations can not be understood to limit scope of the present invention, any change carried out on the claims in the present invention basis is all protection scope of the present invention.

Claims (4)

1. dry type paper-making method recreated tobacco production technology, it is characterized in that: by baccy fiber raw material or fluff pulp fibers raw material or baccy fiber and fluff pulp fibers compound by dry method of paper-making machine, utilize air flow settlement method, manufacture paper with pulp out Filling power>=6.0cm 3the substrate of/g, then after the positive and negative spraying tobacco powder and glue class mixture of described substrate, drying and subsequent handling, make reconstituted tobacoo finished product; Adopt negative-pressure vacuum Smoking regime during spraying, the tobacco powder of ejection and glue class mixture are adsorbed in the substrate; Spraying process is spraying-oven dry, then sprays-drying mode again; Mass dryness fraction>=80% of raw material; Described drying mode is by setting bake out temperature, adopts hot-air through type drying box to dry the substrate after spraying, shaping, spraying vacuum draw, stoving process route are as follows:
(1) measure pulverizing: the baccy fiber raw material of mass dryness fraction>=80% or fluff pulp fibers raw material or baccy fiber and fluff pulp fibers compound are delivered to dry method air flow settlement moulded head charging aperture by airduct, and in setting conveying airduct, fibre concentration is 1 ~ 6g/m 3;
(2) substrate is shaping: the substrate that manufacture paper with pulp on the dry method of paper-making machine air flow settlement moulded head baccy fiber raw material or fluff pulp fibers raw material or baccy fiber and fluff pulp fibers compound form, and setting substrate is quantitatively 18 ~ 45g/m 2, mass dryness fraction>=85%;
(3) once spray: at substrate front spraying tobacco powder and glue class mixture, substrate reverse side negative-pressure vacuum suction during spraying, setting spraying oven-dry weight is 15 ~ 35g/m 2;
(4) first drying: once spray meron and send hot-air through type drying box to dry to mass dryness fraction >=85%, setting hot blast temperature 80 ~ 150 DEG C;
(5) secondary spraying: at substrate reverse side spraying tobacco powder and glue class mixture, negative-pressure vacuum suction in substrate front during spraying, setting spraying oven-dry weight is 18 ~ 36g/m 2;
(6) secondary drying: second time spraying meron send hot-air through type drying box to dry to mass dryness fraction >=85%, and setting hot blast temperature 80 ~ 150 DEG C, prepares FINISHED;
The mixed proportion of described baccy fiber and fluff pulp fibers compound is 1:1 ~ 5 by mass percentage.
2. dry type paper-making method recreated tobacco production technology according to claim 1, is characterized in that, described shaping, spraying vacuum draw, stoving process route are as follows:
(1) measure pulverizing: the fluff pulp fibers raw material of mass dryness fraction>=80% is delivered to dry method air flow settlement moulded head by feeding airduct, in setting feeding airduct, fibre concentration is 1.5g/m 3;
(2) substrate is shaping: substrate of manufacturing paper with pulp on dry method of paper-making machine air flow settlement moulded head, and setting substrate is quantitatively 18g/m 2, moisture 85%;
(3) once spray: at substrate front spraying tobacco powder and glue class mixture, during spraying, substrate reverse side has negative-pressure ward case negative-pressure vacuum to aspirate, setting spraying oven-dry weight is 24.0g/m 2;
(4) first drying: first time spraying meron send a drying box to dry to mass dryness fraction >=85%, setting hot blast temperature 125 DEG C;
(5) secondary spraying: at substrate reverse side spraying tobacco powder and glue class mixture, during spraying, substrate front has negative-pressure ward case negative-pressure vacuum to aspirate, setting spraying oven-dry weight is 24.2g/m 2;
(6) secondary drying: second time spraying meron send No. two drying boxes to dry to mass dryness fraction >=88%, and setting hot blast temperature 130 DEG C, makes FINISHED.
3. dry type paper-making method recreated tobacco production technology according to claim 1, is characterized in that, described shaping, spraying vacuum draw, stoving process route are as follows:
(1) measure pulverizing: the fluff pulp fibers of mass dryness fraction>=80% and cigarette fiber mixture are delivered to dry method air flow settlement moulded head by feeding airduct, in setting feeding airduct, fibre concentration is 6g/m 3, the mixed proportion of setting baccy fiber and fluff pulp fibers compound is 1:4 by mass percentage;
(2) substrate is shaping: substrate of manufacturing paper with pulp on dry method of paper-making machine air flow settlement moulded head, and setting substrate is quantitatively 40g/m 2, moisture 85%;
(3) once spray: at substrate front spraying tobacco powder and glue class mixture, during spraying, substrate reverse side has negative-pressure ward case negative-pressure vacuum to aspirate, setting spraying oven-dry weight is 31.4g/m 2;
(4) first drying: first time spraying meron send a drying box to dry to mass dryness fraction >=85%, setting hot blast temperature 135 DEG C;
(5) secondary spraying: at substrate reverse side spraying tobacco powder and glue class mixture, during spraying, substrate front has negative-pressure ward case negative-pressure vacuum to aspirate, setting spraying oven-dry weight is 31.4g/m 2;
(6) secondary drying: second time spraying meron send No. two drying boxes to dry to mass dryness fraction >=88%, and setting hot blast temperature 130 DEG C, makes FINISHED.
4. dry type paper-making method recreated tobacco production technology according to claim 1, is characterized in that, described shaping, spraying vacuum draw, stoving process route are as follows:
(1) measure pulverizing: the cigarette fiber material of mass dryness fraction>=80% is delivered to dry method air flow settlement moulded head by feeding airduct, in setting feeding airduct, fibre concentration is 3g/m 3;
(2) substrate is shaping: substrate of manufacturing paper with pulp on dry method of paper-making machine air flow settlement moulded head, and setting substrate is quantitatively 45g/m 2, moisture 85%;
(3) once spray: at substrate front spraying tobacco powder and glue class mixture, during spraying, substrate reverse side has negative-pressure ward case negative-pressure vacuum to aspirate, setting spraying oven-dry weight is 20g/m 2;
(4) first drying: first time spraying meron send a drying box to dry to mass dryness fraction >=85%, setting hot blast temperature 130 DEG C;
(5) secondary spraying: at substrate reverse side spraying tobacco powder and glue class mixture, during spraying, substrate front has negative-pressure ward case negative-pressure vacuum to aspirate, setting spraying oven-dry weight is 20.4g/m 2;
(6) secondary drying: second time spraying meron send No. two drying boxes to dry to mass dryness fraction >=88%, and setting hot blast temperature 130 DEG C, makes FINISHED.
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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP4066653A4 (en) * 2019-11-28 2024-03-13 Sichuan Sanlian New Mat Co Ltd Dry-method reconstituted tobacco having adjustable and controllable air permeability and tightness, and preparation method and application of dry-method reconstituted tobacco

Families Citing this family (19)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103445285A (en) * 2013-08-30 2013-12-18 陕西理工机电科技有限公司 Method for processing reconstituted tobacco sheets by adopting dry-process papermaking method
CN103431514B (en) * 2013-09-02 2015-02-18 陕西理工机电科技有限公司 Bulk production line for reconstituted tobacco thin sheets by dry papermaking method
CN104131492B (en) * 2014-07-29 2017-01-18 上海华宝生物科技有限公司 Cigarette paper with tobacco fragment and tobacco powder attached to the surface and preparation method thereof
CN104336751B (en) * 2014-11-18 2015-12-09 浙江泽源植物科技有限公司 A kind of gummed dust-free paper technology manufactures the method for reconstituted tobacco
CN104473318B (en) * 2014-12-03 2017-01-18 湖北中烟工业有限责任公司 Harm-reducing and tar-lowering recombined tobacco and producing method thereof
CN104824824B (en) * 2015-03-17 2016-06-08 陕西理工机电科技有限公司 Method with the load tobacco chippings reconstituted tobacco that Paper DryForming Technology manufactures
CN105167154A (en) * 2015-07-15 2015-12-23 湖北中烟工业有限责任公司 Novel method for preparing reconstituted tobacco by virtue of papermaking process
CN105212257B (en) * 2015-11-05 2017-03-22 广东省金叶科技开发有限公司 Substrate forming device for producing reconstituted tobacco through dry method of papermaking
CN106723285A (en) * 2017-02-10 2017-05-31 杨根喜 A kind of production method of novel tobacco sheet
CN107136553A (en) * 2017-06-22 2017-09-08 中烟施伟策(云南)再造烟叶有限公司 A kind of papermaking-method reconstituted tobaccos preparation method of the tobacco powder containing ultra micro
CN107212467A (en) * 2017-06-29 2017-09-29 广东省金叶科技开发有限公司 One kind heats cigarette cigarette core material and preparation method thereof of not burning
CN107930911A (en) * 2017-12-12 2018-04-20 双登集团股份有限公司 Carbon fiber battery grid is carried out continuously the spray equipment of active material filling
CN108589409A (en) * 2018-04-04 2018-09-28 陕西理工机电科技有限公司 A kind of compound spraying method
CN109043633A (en) * 2018-09-03 2018-12-21 云南昆船烟草设备有限公司 A kind of compound reconstituted tobacco sheets and its former and manufacturing process
CN110403226A (en) * 2019-08-29 2019-11-05 普维思信(北京)科技有限公司 The technique and system of the high-intensitive tobacco-containing material that homogenizes of extruded type composite molding production
CN110537721B (en) * 2019-09-27 2021-07-27 四川中烟工业有限责任公司 Reconstituted tobacco for heating cigarettes and improved dry preparation method thereof
CN110959905B (en) * 2019-12-13 2021-12-24 河南卷烟工业烟草薄片有限公司 Preparation method of cigarette sheet capable of being heated and not combusted
CN112056608B (en) * 2020-09-03 2022-07-01 云南中烟工业有限责任公司 Multilayer recombinant tobacco vector and preparation method thereof
CN113892671B (en) * 2021-10-19 2023-01-31 湖北中烟工业有限责任公司 Method for preparing eggplant coat and eggplant sleeve based on dry-process slice technology

Family Cites Families (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS4820320B1 (en) * 1970-11-04 1973-06-20
US4421126A (en) * 1981-06-04 1983-12-20 Philip Morris Incorporated Process for utilizing tobacco fines in making reconstituted tobacco
US4681126A (en) * 1984-05-21 1987-07-21 Brown & Williamson Tobacco Corporation Process for manufacturing reconstituted tobacco
CN1005752B (en) * 1985-07-01 1989-11-15 金伯利-克拉克公司 Dry-forming of reconstituted tobacco and resulting product
CN1033359C (en) * 1993-12-10 1996-11-27 大姚县金碧造纸厂 Process and apparatus for producing tobacco sheet by paper-making process
AU5104800A (en) * 1999-06-04 2000-12-28 Japan Tobacco Inc. Sheet tobacco and method and system for producing the same
CN101168149A (en) * 2007-11-16 2008-04-30 山东中烟工业公司 Paper-making method reproduced tobacco leaf tobacco powder spraying type coating machine
CN101336749B (en) * 2008-08-08 2011-07-13 广东省金叶烟草薄片技术开发有限公司 Dry type paper-making method recreated tobacco and production method thereof

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP4066653A4 (en) * 2019-11-28 2024-03-13 Sichuan Sanlian New Mat Co Ltd Dry-method reconstituted tobacco having adjustable and controllable air permeability and tightness, and preparation method and application of dry-method reconstituted tobacco

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