CN1087918C - Reconstituted tobacco - Google Patents
Reconstituted tobacco Download PDFInfo
- Publication number
- CN1087918C CN1087918C CN96198982A CN96198982A CN1087918C CN 1087918 C CN1087918 C CN 1087918C CN 96198982 A CN96198982 A CN 96198982A CN 96198982 A CN96198982 A CN 96198982A CN 1087918 C CN1087918 C CN 1087918C
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- China
- Prior art keywords
- tobacco
- agent
- reconstituted tobacco
- particles
- substance
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- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
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Classifications
-
- A—HUMAN NECESSITIES
- A24—TOBACCO; CIGARS; CIGARETTES; SIMULATED SMOKING DEVICES; SMOKERS' REQUISITES
- A24B—MANUFACTURE OR PREPARATION OF TOBACCO FOR SMOKING OR CHEWING; TOBACCO; SNUFF
- A24B15/00—Chemical features or treatment of tobacco; Tobacco substitutes, e.g. in liquid form
- A24B15/10—Chemical features of tobacco products or tobacco substitutes
- A24B15/12—Chemical features of tobacco products or tobacco substitutes of reconstituted tobacco
- A24B15/14—Chemical features of tobacco products or tobacco substitutes of reconstituted tobacco made of tobacco and a binding agent not derived from 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
- A24B15/00—Chemical features or treatment of tobacco; Tobacco substitutes, e.g. in liquid form
- A24B15/18—Treatment of tobacco products or tobacco substitutes
- A24B15/28—Treatment of tobacco products or tobacco substitutes by chemical substances
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- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Health & Medical Sciences (AREA)
- General Health & Medical Sciences (AREA)
- Toxicology (AREA)
- Manufacture Of Tobacco Products (AREA)
Abstract
一种烟草工业操作程序,其中颗粒间具有粘连倾向的粒状再制烟草与粒状防粘剂进行掺混处理。让防粘剂与再制烟草颗粒的掺混料体处于如果不含防粘剂便会促使再制烟草由于颗粒间粘连而发生结团的条件之下,在所述料体暴露于所述条件之后,对所述料体再进行分离处理,从而将防粘剂与再制烟草分开。采用了这种程序,再制烟草就可在压实状态下贮存而不发生结团。A tobacco industry procedure in which granulated reconstituted tobacco with a tendency to stick between particles is blended with a granulated anti-sticking agent. subjecting a blend of detackifier and reconstituted tobacco particles to conditions which, in the absence of the detackifier, would promote clumping of reconstituted tobacco due to particle-to-particle adhesion, upon exposure of said mass to said conditions Afterwards, the material body is further subjected to a separation process, thereby separating the release agent from the reconstituted tobacco. Using this procedure, reconstituted tobacco can be stored in a compact state without clumping.
Description
本发明涉及烟草的再制及再制的烟草。The present invention relates to the reconstitution of tobacco and reconstituted tobacco.
烟草可采用挤出、铸带或造纸技术加以再制。用于烟草再制的挤出方法公开在GB 2 201 081中。在GB 2 201 081的方法中,粒状烟草、淀粉、粘结剂、水及甘油被喂入到螺杆挤出机中。挤出物,此时为薄带状形式,经过冷却,然后沿纵向切碎并沿横向切断,从而生产出细长粒状的再制烟草产品。当这种粒状再制烟草以散料形式打包时,例如为了运输及贮存的需要,常常出现再制烟草压缩或压实现象,因此烟草颗粒具有彼此粘连倾向。故而,当再制烟草开包时,经常出现的情况是一部分再制烟草料发生结团现象。机械开松方法会造成作为处理对象的再制烟草部分地破碎成粉末。Tobacco can be reconstituted using extrusion, tape casting or papermaking techniques. Extrusion methods for tobacco remanufacturing are disclosed in GB 2 201 081. In the method of GB 2 201 081 granulated tobacco, starch, binder, water and glycerin are fed into a screw extruder. The extrudate, now in the form of thin ribbons, is cooled, then shredded longitudinally and cut transversely to produce a reconstituted tobacco product in the form of elongated pellets. When such granulated reconstituted tobacco is packaged in bulk form, eg, for transportation and storage, compression or compaction of the reconstituted tobacco often occurs, so that the tobacco particles have a tendency to stick to each other. Therefore, when the remanufactured tobacco is unpacked, it often occurs that a part of the remanufactured tobacco material is agglomerated. The mechanical opening method causes the reconstituted tobacco to be processed to be partially broken into powder.
曾提出各种各样方法来克服上述粒状再制烟草结团现象,然而没有一种证明是完全成功的。例如,将粒状再制烟草在低于传统含湿量的状态下打包。然而,在湿、热环境条件盛行的情况下,要维持低含湿量就有困难。而且,粒状再制烟草当维持在低含湿量时更易于破碎。Various methods have been proposed to overcome the agglomeration phenomenon of granulated reconstituted tobacco described above, however, none have proved to be completely successful. For example, granulated reconstituted tobacco is packaged at lower than conventional moisture contents. However, there are difficulties in maintaining low moisture levels in the presence of humid, hot environmental conditions prevailing. Also, granulated reconstituted tobacco is more prone to crumbling when maintained at a low moisture content.
本发明的一个目的是提供一种避免或大大减少粒状再制烟草结团的完全有效措施。It is an object of the present invention to provide a completely effective means of avoiding or substantially reducing agglomeration of granulated reconstituted tobacco.
本发明提供一种烟草工业操作程序,其中颗粒间具有粘连倾向的粒状再制烟草与粒状防粘剂进行掺混处理,让防粘剂与再制烟草颗粒的掺混料体处于如果不含防粘剂便会促使再制烟草由于颗粒间粘连而发生结团的条件之下,在所述料体暴露于所述条件之后,对所述料体再进行分离处理,从而将防粘剂与再制烟草分开。The present invention provides a tobacco industry operation procedure, wherein the granular reconstituted tobacco with a tendency of sticking among the particles is mixed with the granular anti-sticking agent, so that the blended body of the anti-sticking agent and the remanufactured tobacco particles is in the After the body has been exposed to the conditions under conditions where the sticky agent will promote agglomeration of the reconstituted tobacco due to sticking between particles Tobacco is made separately.
要指出的是,防粘剂的性状就象粉尘似的。It should be pointed out that the anti-blocking agent behaves like dust.
较好的是,防粘剂包含,或由烟草粉末组成。Preferably, the detackifying agent comprises, or consists of, tobacco powder.
在实施按照GB 2 201 081公开内容的方法中,初始步骤可包括将烟草磨碎成细颗粒的形式。在这种情况下,有利的是将磨碎的烟草中的一定级分用作为本发明的防粘剂。这一级分就称之为细粒度级分,例如不超过100微米。迄今,通常的做法是将该细粒度级分当作废物丢掉。一般而言,烟草研磨并过筛以便为GB 2,201,081中所公开的挤出工艺备料时所产生的粉末量,不是超过就是等于每生产单位数量再制烟草所需要的粉末量。In carrying out the method according to the disclosure of GB 2 201 081, an initial step may include grinding the tobacco into fine particle form. In this case it is advantageous to use a fraction of the ground tobacco as detackifying agent according to the invention. This fraction is referred to as the fine particle size fraction, for example not exceeding 100 microns. Hitherto, it has been common practice to discard this fine-grained fraction as waste. In general, the amount of powder produced when tobacco is ground and sieved for the extrusion process disclosed in GB 2,201,081 is either greater than or equal to that required per unit quantity of reconstituted tobacco produced.
其他颗粒形式的物质也可用作防粘剂或其组成部分,例如二氧化钛、白垩、氢氧化镁、碳酸镁、硫酸镁及淀粉。Other substances in granular form can also be used as antiblocking agents or components thereof, such as titanium dioxide, chalk, magnesium hydroxide, magnesium carbonate, magnesium sulfate and starch.
两种或更多种防粘剂也可一起使用。Two or more release agents may also be used together.
优选的是,粒状防粘剂在防粘剂与再制烟草的掺混料体中的含量最高为约20%(重量)。更优选的是,防粘剂的含量不超过约15%(重量)。Preferably, the particulate detackifier is present in an amount of up to about 20% by weight of the admixture of detackifier and reconstituted tobacco. More preferably, the amount of release agent does not exceed about 15% by weight.
该防粘剂或其组成部分可以是干燥剂,如无水形式的硫酸镁或者氧化镁。The detackifying agent or a component thereof may be a desiccant such as magnesium sulfate or magnesium oxide in anhydrous form.
合适的是,防粘剂由该再制过程中所使用的物质构成。Suitably, the anti-adhesive agent consists of the substances used in the reconstitution process.
该掺混过程优选在再制烟草被变成粒状之后直接进行。正如本领域技术人员所能理解的,重要的是,该掺混过程不迟于,或不显著迟于再制烟草开始结团的时刻。This blending process is preferably carried out directly after the reconstituted tobacco is pelletized. As will be appreciated by those skilled in the art, it is important that the blending process be performed no later than, or not significantly later than, the point at which the reconstituted tobacco begins to agglomerate.
掺混过程可采用回转混合圆筒进行,在该圆筒中,粒状再制烟草借助翻滚作用而实现与粒状防粘剂的掺混。The blending process can be carried out using a revolving mixing drum in which the granulated reconstituted tobacco is blended with the granulated anti-sticking agent by tumbling action.
一种替代的掺混手段可包括气力输送装置,可操纵该装置以借助气力作用使再制烟草颗粒悬浮在例如空气流中实现输送。该装置包括引入手段,借以将防粘剂颗粒引入到靠气力输送的再制烟草颗粒流中,借此与再制烟草颗粒实现掺混。An alternative means of blending may include a pneumatic conveying device operable to pneumatically suspend reconstituted tobacco particles in, for example, a stream of air for conveyance. The device includes introduction means for introducing detackifying agent particles into the pneumatically conveyed flow of reconstituted tobacco particles, whereby blending with the reconstituted tobacco particles is effected.
粒状防粘剂可施于粒状再制烟草的移动料层上,如此施用之后,必要的话,可接着进行掺混或进一步掺混的步骤。The particulate detackifier may be applied to the moving bed of particulate reconstituted tobacco, and after such application, may be followed by a step of blending or further blending, if necessary.
作为一种促使防粘剂与再制烟草有效掺混的措施,上述材料的颗粒可各自带上静电,一种材料颗粒的电荷与另一种材料颗粒的电荷相反。As a means of facilitating effective blending of the detackifying agent with the reconstituted tobacco, the particles of the aforementioned materials may each be electrostatically charged, with particles of one material being oppositely charged to particles of the other material.
由于防粘剂与再制烟草之间的粘连程度微乎其微,譬如是零或基本为零,因此足以从再制烟草颗粒中分离掉防粘剂至少绝大部分,譬如说80%,的分离过程的激烈程度,可能远低于会导致再制烟草破碎的激烈程度。相反,如果防粘剂与再制烟草颗粒之间的粘连程度超过某一极小数值,例如在防粘剂与再制烟草颗粒掺混料体之外还存在着某种粘结剂,则分离过程的激烈程度就不得不大到招致再制烟草发生不可接受的降等的激烈程度。Since the degree of adhesion between the anti-adhesive agent and the reconstituted tobacco is negligible, such as zero or substantially zero, it is sufficient to separate at least a substantial portion, such as 80%, of the anti-adhesive agent from the reconstituted tobacco particles. The level of intensity may be much lower than that which would cause the reconstituted tobacco to break down. Conversely, if the degree of adhesion between the anti-adhesive agent and the remanufactured tobacco particles exceeds a certain minimum value, for example, there is some kind of binder outside the admixture of the anti-adhesive agent and remanufactured tobacco particles, the separation The severity of the process would have to be so severe as to induce unacceptable degradation of the reconstituted tobacco.
分离过程可采用例如振动多孔输送机、筛子或空气分离系统来完成。Separation can be accomplished using, for example, vibrating perforated conveyors, screens or air separation systems.
除去在生产线中设立其设置专门为达到分离这一特定目的设备之外,分离过程可以由为完成生产线加工目的而设置在生产线中,然而却又可同时承担将防粘剂颗粒与再制烟草颗粒分离任务的设备来完成。In addition to setting up equipment in the production line which is set up specifically for the specific purpose of separation, the separation process can be set up in the production line for the purpose of completing the production line processing, but it can simultaneously undertake the separation of anti-sticking agent particles and reconstituted tobacco particles. Devices that separate tasks to accomplish.
在本发明的第一个实施例中,按照GB 2 201 081的挤出方法生产出粒状再制烟草。该粒状再制烟草随后与含量相当于再制烟草重量10%的、粒度小于100微米的淀粉粉末掺混。经过一个月贮存之后,发现在掺混的再制烟草与淀粉粉末中仅有0.6%的再制烟草结了团,相比之下,未经掺混防粘剂的相同再制烟草的对比料体在放置一个月之后结团竟达15%。In a first embodiment of the present invention, pelletized reconstituted tobacco is produced according to the extrusion method of GB 2 201 081. The granulated reconstituted tobacco is then blended with starch powder having a particle size of less than 100 microns in an amount equivalent to 10% by weight of the reconstituted tobacco. After one month of storage, only 0.6% of the reconstituted tobacco was found to be agglomerated in the blended reconstituted tobacco and starch powder, compared to a control of the same reconstituted tobacco not blended with anti-sticking agent The body clumped up to 15% after being placed for one month.
在本发明的第二个实施例中,按照GB 2 201 081生产出粒状再制烟草之后,该再制烟草与12%(重量)作为防粘剂的烟草粉末相掺混,该粉尘的粒度小于100微米。在此例中发现,结团程度降至同一种再制烟草料体所对应程度的三分之一。In a second embodiment of the present invention, after the granulated reconstituted tobacco is produced according to GB 2 201 081, the reconstituted tobacco is blended with 12% by weight of tobacco powder as an anti-sticking agent, the particle size of which is less than 100 microns. In this case it was found that the degree of agglomeration was reduced to one third of the corresponding level for the same reconstituted tobacco body.
优选该再制烟草的结团不大于约5%(重量),更优选不大于约2~3%(重量),最优选是0%。Preferably, the reconstituted tobacco has no agglomeration of greater than about 5% by weight, more preferably no greater than about 2-3% by weight, and most preferably 0%.
利用粒度远大于100微米的烟草粉末(12%(重量))作为防粘剂的实验表明,该粒度等级的烟草粉末在减少再制烟草结团方面比粒度小于100微米的烟草粉末效力低。Experiments using tobacco powders much larger than 100 microns (12% by weight) as a detackifier showed that tobacco powders of this size class were less effective at reducing reconstituted tobacco agglomeration than tobacco powders with particle sizes below 100 microns.
Claims (11)
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| GBGB9525625.1A GB9525625D0 (en) | 1995-12-15 | 1995-12-15 | Reconstituted tobacco |
| GB9525625.1 | 1995-12-15 |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN1204234A CN1204234A (en) | 1999-01-06 |
| CN1087918C true CN1087918C (en) | 2002-07-24 |
Family
ID=10785450
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN96198982A Expired - Fee Related CN1087918C (en) | 1995-12-15 | 1996-11-29 | Reconstituted tobacco |
Country Status (9)
| Country | Link |
|---|---|
| CN (1) | CN1087918C (en) |
| AU (1) | AU7701696A (en) |
| BR (1) | BR9604690A (en) |
| GB (1) | GB9525625D0 (en) |
| PL (1) | PL184657B1 (en) |
| RU (1) | RU2170537C2 (en) |
| UA (1) | UA44915C2 (en) |
| WO (1) | WO1997022267A1 (en) |
| ZA (1) | ZA9610151B (en) |
Families Citing this family (34)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB0011351D0 (en) * | 2000-05-12 | 2000-06-28 | British American Tobacco Co | Tobacco reconstitution |
| DE102004059388B4 (en) * | 2004-12-09 | 2006-11-30 | British American Tobacco (Germany) Gmbh | Defibration of tobacco material |
| RU2365314C1 (en) * | 2008-05-15 | 2009-08-27 | Олег Иванович Квасенков | Production method of reconstituted tobacco |
| RU2352209C1 (en) * | 2008-05-15 | 2009-04-20 | Олег Иванович Квасенков | Method of production reconstituted tobacco |
| RU2352214C1 (en) * | 2008-05-15 | 2009-04-20 | Олег Иванович Квасенков | Method of production reconstituted tobacco |
| RU2352211C1 (en) * | 2008-05-15 | 2009-04-20 | Олег Иванович Квасенков | Method of production reconstituted tobacco |
| RU2352213C1 (en) * | 2008-05-15 | 2009-04-20 | Олег Иванович Квасенков | Method of production reconstituted tobacco |
| RU2352220C1 (en) * | 2008-05-16 | 2009-04-20 | Олег Иванович Квасенков | Method of obtaining reconstituted tobacco |
| RU2357620C1 (en) * | 2008-05-16 | 2009-06-10 | Олег Иванович Квасенков | Reconstituted tobacco production method |
| RU2353231C1 (en) * | 2008-05-20 | 2009-04-27 | Олег Иванович Квасенков | Method for producing reconstituted tobacco |
| RU2353226C1 (en) * | 2008-05-20 | 2009-04-27 | Олег Иванович Квасенков | Method for producing reconstituted tobacco |
| RU2353225C1 (en) * | 2008-05-20 | 2009-04-27 | Олег Иванович Квасенков | Method for producing reconstituted tobacco |
| RU2353270C1 (en) * | 2008-05-20 | 2009-04-27 | Олег Иванович Квасенков | Method of producing reconstituted tobacco |
| RU2353237C1 (en) * | 2008-05-20 | 2009-04-27 | Олег Иванович Квасенков | Method for producing reconstituted tobacco |
| RU2353269C1 (en) * | 2008-05-20 | 2009-04-27 | Олег Иванович Квасенков | Method of producing reconstituted tobacco |
| RU2353240C1 (en) * | 2008-05-20 | 2009-04-27 | Олег Иванович Квасенков | Method for producing reconstituted tobacco |
| RU2353235C1 (en) * | 2008-05-20 | 2009-04-27 | Олег Иванович Квасенков | Method for producing reconstituted tobacco |
| RU2353234C1 (en) * | 2008-05-20 | 2009-04-27 | Олег Иванович Квасенков | Method for producing reconstituted tobacco |
| RU2353273C1 (en) * | 2008-05-21 | 2009-04-27 | Олег Иванович Квасенков | Method of producing reconstituted tobacco |
| RU2368291C1 (en) * | 2008-05-21 | 2009-09-27 | Олег Иванович Квасенков | Method of reconstituted tobacco production |
| RU2353282C1 (en) * | 2008-05-23 | 2009-04-27 | Олег Иванович Квасенков | Method of producing reconstituted tobacco |
| RU2356466C1 (en) * | 2008-05-26 | 2009-05-27 | Олег Иванович Квасенков | Method for producing reconstituted tobacco |
| RU2356427C1 (en) * | 2008-05-26 | 2009-05-27 | Олег Иванович Квасенков | Method for producing reconstituted tobacco |
| RU2356467C1 (en) * | 2008-05-26 | 2009-05-27 | Олег Иванович Квасенков | Method for producing reconstituted tobacco |
| RU2356426C1 (en) * | 2008-05-26 | 2009-05-27 | Олег Иванович Квасенков | Method for producing reconstituted tobacco |
| RU2356468C1 (en) * | 2008-05-28 | 2009-05-27 | Олег Иванович Квасенков | Method for producing reconstituted tobacco |
| RU2356471C1 (en) * | 2008-05-28 | 2009-05-27 | Олег Иванович Квасенков | Method for producing reconstituted tobacco |
| RU2356411C1 (en) * | 2008-05-28 | 2009-05-27 | Олег Иванович Квасенков | Method for producing reconstituted tobacco |
| RU2356470C1 (en) * | 2008-05-28 | 2009-05-27 | Олег Иванович Квасенков | Method for producing reconstituted tobacco |
| RU2356469C1 (en) * | 2008-05-28 | 2009-05-27 | Олег Иванович Квасенков | Method for producing reconstituted tobacco |
| EP2617299A1 (en) * | 2012-01-18 | 2013-07-24 | Delfortgroup AG | Paper filled with tobacco particles |
| KR102638408B1 (en) * | 2017-05-24 | 2024-02-21 | 필립모리스 프로덕츠 에스.에이. | Homogenized plant material containing basic pH regulator |
| TR2021013986A2 (en) * | 2021-09-07 | 2021-11-22 | Kon Tek Kontrol Teknolojileri Ve Otomasyon Sanayi Anonim Sirketi | Inline tobacco dust recycling unit |
| CN114098149A (en) * | 2021-11-30 | 2022-03-01 | 云南中烟工业有限责任公司 | A method for batch stirring preparation of aerosol generating matrix rods with high porosity |
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3012915A (en) * | 1957-11-21 | 1961-12-12 | Minerals & Chem Philipp Corp | Tobacco composition including comminuted solid material affixed thereto |
| US3118452A (en) * | 1961-04-17 | 1964-01-21 | American Mach & Foundry | Tobacco sheet |
| SU923512A1 (en) * | 1980-10-14 | 1982-04-30 | Всесоюзный Научно-Исследовательский Институт Табака И Махорки | Method of obtaining recovered tobacco |
| GB8704196D0 (en) * | 1987-02-23 | 1987-04-01 | British American Tobacco Co | Tobacco reconstitution |
-
1995
- 1995-12-15 GB GBGB9525625.1A patent/GB9525625D0/en active Pending
-
1996
- 1996-11-29 AU AU77016/96A patent/AU7701696A/en not_active Abandoned
- 1996-11-29 CN CN96198982A patent/CN1087918C/en not_active Expired - Fee Related
- 1996-11-29 PL PL96327165A patent/PL184657B1/en not_active IP Right Cessation
- 1996-11-29 RU RU98114100/13A patent/RU2170537C2/en not_active IP Right Cessation
- 1996-11-29 UA UA98063072A patent/UA44915C2/en unknown
- 1996-11-29 WO PCT/GB1996/002933 patent/WO1997022267A1/en not_active Ceased
- 1996-12-03 ZA ZA9610151A patent/ZA9610151B/en unknown
- 1996-12-13 BR BR9604690A patent/BR9604690A/en not_active IP Right Cessation
Also Published As
| Publication number | Publication date |
|---|---|
| WO1997022267A1 (en) | 1997-06-26 |
| ZA9610151B (en) | 1997-06-17 |
| UA44915C2 (en) | 2002-03-15 |
| PL327165A1 (en) | 1998-11-23 |
| BR9604690A (en) | 1998-06-23 |
| AU7701696A (en) | 1997-07-14 |
| RU2170537C2 (en) | 2001-07-20 |
| CN1204234A (en) | 1999-01-06 |
| HK1015637A1 (en) | 1999-10-22 |
| PL184657B1 (en) | 2002-11-29 |
| GB9525625D0 (en) | 1996-02-14 |
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