EP1925218A1 - Système pour la production de tabac expansé - Google Patents

Système pour la production de tabac expansé Download PDF

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Publication number
EP1925218A1
EP1925218A1 EP06405497A EP06405497A EP1925218A1 EP 1925218 A1 EP1925218 A1 EP 1925218A1 EP 06405497 A EP06405497 A EP 06405497A EP 06405497 A EP06405497 A EP 06405497A EP 1925218 A1 EP1925218 A1 EP 1925218A1
Authority
EP
European Patent Office
Prior art keywords
tobacco
expansion
supply unit
silo
expanded
Prior art date
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.)
Withdrawn
Application number
EP06405497A
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German (de)
English (en)
Inventor
Vincent Thong Nguyen
Pierre Wetzel
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Philip Morris Products SA
Original Assignee
Philip Morris Products SA
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Philip Morris Products SA filed Critical Philip Morris Products SA
Priority to EP06405497A priority Critical patent/EP1925218A1/fr
Priority to US11/984,658 priority patent/US20080135057A1/en
Publication of EP1925218A1 publication Critical patent/EP1925218A1/fr
Withdrawn legal-status Critical Current

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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
    • A24B3/00—Preparing tobacco in the factory
    • A24B3/18—Other treatment of leaves, e.g. puffing, crimpling, cleaning
    • A24B3/182—Puffing

Definitions

  • the present invention relates to a system for producing expanded tobacco.
  • the tobacco is treated before expansion, either only with water or with additional chemical solvents, for example liquid or gaseous carbon dioxide, nitrogen or iso-pentane or other suitable solvents in gaseous or liquid form.
  • additional chemical solvents for example liquid or gaseous carbon dioxide, nitrogen or iso-pentane or other suitable solvents in gaseous or liquid form.
  • Typical expansion rates of tobacco treated only with water are in the range of from about 5 percent to about 15 percent.
  • Typical expansion rates of tobacco treated with additional chemical solvents may be in the range of from about 80 percent to about 120 percent.
  • the systems for expanding tobacco known in the art comprise a supply unit of tobacco, an expansion apparatus and a feed unit that feeds the tobacco from the supply unit into the expansion apparatus.
  • the supply unit may comprise a treatment unit where the tobacco is treated to prepare the tobacco for expansion.
  • These systems are for example known from US-A-4,340,073 or US-A-4,407,306 .
  • the present invention provides a system for producing expanded tobacco comprising at least a first tobacco supply unit for providing tobacco containing at least one suitable chemical solvent other than water to prepare the tobacco for expansion and at least a second tobacco supply unit for providing tobacco containing only water as a solvent to prepare the tobacco for expansion.
  • the system for producing expanded tobacco further comprises a tobacco expansion apparatus and at least one feed unit.
  • the feed unit is configured to introduce the tobacco into the tobacco expansion apparatus from the at least first tobacco supply unit or the at least second tobacco supply unit. Additionally, the feed unit may feed tobacco simultaneously from the first or the second supply unit.
  • tobacco is used throughout the specification to encompass all parts of any tobacco plant, treated or untreated, that are expandable.
  • tobacco refers to cut or shredded tobacco. It is also meant to include other parts of the tobacco plant, for example stems or pre-treated tobacco, for example flavoured cut tobacco.
  • chemical expansion is used throughout the specification to refer to any process of expanding tobacco containing an additional suitable chemical solvent other than water to prepare the tobacco for expansion.
  • tower drying is used throughout the specification to refer to any process of expanding tobacco containing only water as a solvent to prepare the tobacco for expansion.
  • chemical solvent is used throughout the specification to refer to any substance which is suitable to enhance the expansion of the tobacco inside the tobacco expanding apparatus, for example liquid or gaseous carbon dioxide, nitrogen or iso-pentane or other suitable solvents in gaseous or liquid form.
  • the system comprises at least two feed units.
  • Each feed unit is configured to feed tobacco from either one of the supply units to the tobacco expansion apparatus.
  • the tobacco expansion apparatus has two separate entries for the introduction of the tobacco.
  • more than two feed units are used to feed the tobacco from more than two supply units into the tobacco expansion apparatus at one or several locations.
  • some of the supply units contain tobacco which has been treated by a different treatment process.
  • the same system according to the invention allows the expansion of tobacco that has been treated in different ways to facilitate expansion, that is, tobacco treated with water as a solvent and tobacco treated with at least an additional chemical solvent.
  • the expansion apparatus is then operated with process parameters suited to the specific type of pre-treatment of the tobacco.
  • the system allows combinations of both types of processes to be performed. Accordingly, substantial investments can be saved, since the system can be used for both types of processes, requiring only one tobacco expansion apparatus.
  • products which are produced using chemical expansion can be produced in the same system as products which are produced using tower drying.
  • This allows using production capacities for chemical expansion systems which may otherwise be unused. The same holds for production capacities for tower drying.
  • the system according to the invention to produce a superior quality of expanded tobacco in terms of expansion rate of a water solvent expanded product by lowering the moisture of the tobacco leaving the tobacco expansion apparatus below typical tower dryer conditions. For example moisture levels in the range from about 2 percent to about 15 percent may be achieved.
  • the tobacco pre-treated with water for expansion may be exposed to the process parameters normally used for chemical expansion of tobacco. This results in a greater expansion rate and a reduced moisture level compared to conventional tower drying.
  • An additional advantage of the system according to the invention is that the combination of the chemical expansion with the tower drying reduces the fire risk in the tobacco expansion apparatus.
  • the fire risk is reduced when the conditions of tower drying heat treatment are applied for chemical expansion, as the tower drying process runs at a lower temperature as the chemical expansion.
  • the tobacco expansion apparatus comprises a expansion tower dryer.
  • the apparatus for providing the tobacco treated for expansion with at least one chemical solvent other than water comprises an impregnator where the tobacco is exposed to the chemical solvent, for example carbon dioxide.
  • the chemical solvent to which the tobacco is exposed in the impregnator is gaseous carbon dioxide. This is possible for tobacco that has been cooled to a temperature below the temperature of the pressurized gaseous carbon dioxide which is at or near saturation. Then controlled condensation of carbon dioxide on the tobacco occurs and the tobacco gets soaked.
  • the apparatus for providing the tobacco containing water as a solvent comprises a silo for storing the tobacco.
  • the silo has an outlet and a detangling unit for detangling the shreds of tobacco is arranged in the silo.
  • the silos for the tobacco are equipped with large slow moving doffers to feed tobacco from the entire height of the silo to the outlet of the silo.
  • tobacco may tend to form pads and clumps at the exit of the storage silos. The higher the moisture content, the more the tobacco tends to form pads and clumps.
  • Such pads and clumps may have an adverse effect on tower drying systems, since they may cause blockage at the feed unit where the tobacco is introduced into the stream of process gas, for example superheated steam. As a consequence, this may lead to non-uniform heat treatment which may adversely affect the quality of the expanded tobacco.
  • the detangling unit comprise a plurality of slowly rotating short doffers which are arranged essentially over the entire width and height of the silo. Due to the larger number of doffers a high speed for detangling is not required and thus, the tobacco is slowly detangled and degradation of the tobacco is significantly reduced. Also, the detangling is performed in the silo thus eliminating the need for any additional space.
  • Fig. 1a shows a schematic representation of a first embodiment of a system for producing expanded tobacco according to the invention.
  • the shown embodiment of the system comprises a feed unit 10 for introducing tobacco into a tobacco expansion apparatus comprising a tower dryer 20.
  • the tower dryer 20 is connected to a conduit 21 through which a stream of process gas flows during operation.
  • the process gas may be, for example, hot air or superheated steam.
  • the upper end of the tower dryer 20 opens out into a tangential separator 22.
  • a cyclone may be used to separate the expanded tobacco from the process gas.
  • the stream of process gas carrying the tobacco is separated from the tobacco in the tangential separator.
  • the tobacco discharges at the bottom of the tangential separator 22.
  • the process gas is further processed, for example cleaned and reheated, and then reintroduced into the conduit 21.
  • a first supply unit 30 for providing the treated tobacco comprises a silo 40, an impregnator 31 and a vibrating silo 33.
  • the clump breaker 32 is optional and typically used only for a liquid carbon dioxide impregnation of the tobacco.
  • a second supply unit 35 for providing the tobacco containing water as a solvent comprises a silo 40 in which a detangling unit 400 is arranged. Both supply units 30, 35 may share the same silo 40. Alternatively, different silos 40 may be provided for tobacco to be expanded using chemical expansion and for tobacco to be expanded using tower drying. This may be especially useful since the moisture content of the tobacco to be expanded using chemical expansion typically is different from the moisture content of the tobacco to be expanded using tower drying. On the other hand, the moisture content of the tobacco from any one of the supply units 30, 35 may be changed after leaving the silo 40, as well.
  • the detangling unit 400 arranged in the silo 40 is schematically represented in Fig. 2.
  • the detangling unit 400 comprises a number of small doffers 401, which are arranged in the silo essentially over the entire width and height of the silo 40. In Fig. 2, only some small doffers 401 are shown. The small arrows indicate the respective direction of rotation of the small doffers 401 during operation. Since the doffers 401 are arranged over the entire width and height of the silo 40 they need to rotate only slowly compared to the doffers of the detangling units according to the state of the art. Due to the continuous and careful detangling of the shreds of tobacco in the silo, tobacco degradation is substantially reduced if not completely avoided. Since the detangling unit is completely arranged in the silo 40, no additional space is needed.
  • the feed unit 10 comprises means to advance the tobacco to the entry section 210 of the conduit 21 of the tobacco expansion apparatus 20.
  • the tobacco is introduced into the stream of hot air at the entry section 210 of the conduit 21.
  • a stream 23 of hot air loaded with tobacco then flows through the tower 20 and discharges into the tangential separator 22.
  • the entry section 210 may include a rotary valve and a Venturi type nozzle.
  • each feed unit 10, 11 is dedicated to a supply unit 30, 35 and feeds into a separate entry of the conduit 21.
  • the described embodiment of the system according to the invention works essentially as follows for chemical expansion.
  • tobacco is introduced from the silo 40 into the impregnator 31.
  • the impregnator 31 is then closed and purged with gaseous carbon dioxide to remove the air from the impregnator 31.
  • the impregnator 31 is then pressurized for example at 30 bar, at the same time cooling the tobacco to about minus 10 degrees Celsius.
  • the tobacco is soaked by liquid carbon dioxide.
  • carbon dioxide hydrates are formed which act as a puffing agent of the tobacco.
  • the depressurization cools the tobacco to about minus 80 degrees Celsius.
  • Excessive carbon dioxide that has remained in the impregnator 31 upon depressurization forms dry ice. For this reason tobacco expanded by this process is sometimes referred to as dried ice expanded tobacco.
  • tobacco leaves the impregnator 31 and enters the clump breaker 32 to break any clumps that may have formed.
  • the tobacco then enters the vibrating silo 33 to achieve an essentially continuous flow of tobacco towards the first feed unit 10.
  • tobacco is treated by gaseous carbon dioxide instead of liquid carbon dioxide. In this method no clumps are formed and accordingly the clump breaker 32 is not necessary.
  • the impregnated tobacco is now introduced into a stream of hot air flowing through the conduit 21, for example at the entry section 210 of conduit 21.
  • a venturi nozzle may be used. This avoids expansion of the treated tobacco before the tobacco expansion apparatus 20.
  • the hot air which is typically at a temperature in the range of from 300 degrees Celsius to 380 degrees Celsius causes the tobacco to be expanded.
  • the stream of hot air 23 carrying the expanded tobacco is then discharged into the tangential separator 22, at the outlet of which the expanded tobacco can be recollected.
  • the parameters that affect the expansion rate of the tobacco are the impregnation solvent, the load of the tobacco expansion apparatus, the steam concentration in the conduit 21, the process gas velocity and the temperature of the process gas.
  • expanded tobacco which has been produced using only the afore-described chemical expansion technology typically has a moisture content which is in the range of from about 2 percent to about 5 percent. However, this moisture content is considered too low for further processing. Therefore, the expanded tobacco is typically moisturized in a subsequent reordering step (not shown in the drawings) to achieve a final moisture content for the processed tobacco of typically about 11 percent.
  • the tobacco is removed from the silo 40 with the aid of the small doffers 401 of the detangling unit 400.
  • Substantially pad-free and clump free tobacco is forwarded to the first feed unit 10, or, if two feed units 10, 11 are used to second feed unit 11, so that no blockage occurs at the second feed unit 11.
  • the tobacco is then introduced into a stream of non-saturated superheated steam, which may typically have a temperature in a range of about 180 degrees Celsius to about 400 degrees Celsius, preferably between about 180 degrees Celsius to about 250 degrees Celsius.
  • the speed of the stream of superheated steam typically may be within the speed range of from about 18 meters per second to about 25 meters per second.
  • the moisture content of the tobacco in the silo 40 typically may be within the range of from about 20 percent to about 32 percent.
  • the moisture content of the tobacco when recollected from the tangential separator 22 typically may be within the range of from about 11 percent to about 14 percent.
  • the system of the invention allows producing expanded tobacco by using only tower drying, only chemical expansion, and any combinations thereof to achieve any desired final tobacco moisture contents within predetermined ranges, and corresponding expansion rates. Also, the system allows to use capacities for one type of process which would remain otherwise unused, or it avoids additional investments in a system for the respective other type of process. Also, since the system allows combinations of the described types of processes to be performed, it may substantially reduce the fire risk when tower drying heat treatment conditions are applied to tobacco treated with a chemical solvent for the expansion.

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  • Manufacture Of Tobacco Products (AREA)
EP06405497A 2006-11-23 2006-11-23 Système pour la production de tabac expansé Withdrawn EP1925218A1 (fr)

Priority Applications (2)

Application Number Priority Date Filing Date Title
EP06405497A EP1925218A1 (fr) 2006-11-23 2006-11-23 Système pour la production de tabac expansé
US11/984,658 US20080135057A1 (en) 2006-11-23 2007-11-20 System for producing expanded tobacco

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
EP06405497A EP1925218A1 (fr) 2006-11-23 2006-11-23 Système pour la production de tabac expansé

Publications (1)

Publication Number Publication Date
EP1925218A1 true EP1925218A1 (fr) 2008-05-28

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Family Applications (1)

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EP06405497A Withdrawn EP1925218A1 (fr) 2006-11-23 2006-11-23 Système pour la production de tabac expansé

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US (1) US20080135057A1 (fr)
EP (1) EP1925218A1 (fr)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102183280A (zh) * 2011-03-02 2011-09-14 山东中烟工业有限责任公司 基于统计学原理与plc技术测算烟草储丝柜出料量的方法
CN104460488A (zh) * 2014-11-04 2015-03-25 山东中烟工业有限责任公司 一种提高加料机过程数据分析精度的方法
CN110638083A (zh) * 2018-06-26 2020-01-03 中国科学院理化技术研究所 一种膨胀烟丝的高效制备方法
CN115989884A (zh) * 2021-10-19 2023-04-21 贵州中烟工业有限责任公司 一种烟丝处理方法及烟丝处理设备

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103323312B (zh) * 2013-07-18 2015-05-27 中国烟草总公司郑州烟草研究院 一种配方烟丝中膨胀烟丝分离装置
CN105910943B (zh) * 2016-05-24 2019-03-01 中国烟草总公司郑州烟草研究院 一种配方烟丝中膨胀烟丝全自动分离仪及其控制方法

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4519407A (en) * 1983-06-13 1985-05-28 Hellier John A Method and apparatus for treating tobacco
EP0629352A2 (fr) * 1993-06-14 1994-12-21 R.J. Reynolds Tobacco Company Procédé et appareil d'expansion du tabac
EP0651951A2 (fr) * 1993-11-08 1995-05-10 Philip Morris Products Inc. Procédé pour la production d'un mélange de remplissage de cigarette
US5810019A (en) * 1995-07-10 1998-09-22 R.J. Reynolds Tobacco Company Process and apparatus for tobacco batch preparation and expansion
US20040182404A1 (en) * 2003-03-20 2004-09-23 Poindexter Dale Bowman Method of expanding tobacco using steam

Family Cites Families (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4340073A (en) * 1974-02-12 1982-07-20 Philip Morris, Incorporated Expanding tobacco
US4832058A (en) * 1981-07-24 1989-05-23 Molins Plc Cigarette manufacture
US4407306A (en) * 1981-12-17 1983-10-04 American Brands, Inc. Method for expanding tobacco with steam at high temperature and velocity
US4566468A (en) * 1983-05-25 1986-01-28 Brown & Williamson Tobacco Corporation Process and system for making a blended tobacco product
US5259403A (en) * 1992-03-18 1993-11-09 R. J. Reynolds Tobacco Company Process and apparatus for expanding tobacco cut filler
US5582193A (en) * 1994-08-24 1996-12-10 Philip Morris Incorporated Method and apparatus for expanding tobacco
US6067994A (en) * 1997-10-07 2000-05-30 R.J. Reynolds Tobacco Company Tobacco expansion batch forming, unloading and expansion agent purging process and apparatus

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4519407A (en) * 1983-06-13 1985-05-28 Hellier John A Method and apparatus for treating tobacco
EP0629352A2 (fr) * 1993-06-14 1994-12-21 R.J. Reynolds Tobacco Company Procédé et appareil d'expansion du tabac
EP0651951A2 (fr) * 1993-11-08 1995-05-10 Philip Morris Products Inc. Procédé pour la production d'un mélange de remplissage de cigarette
US5810019A (en) * 1995-07-10 1998-09-22 R.J. Reynolds Tobacco Company Process and apparatus for tobacco batch preparation and expansion
US20040182404A1 (en) * 2003-03-20 2004-09-23 Poindexter Dale Bowman Method of expanding tobacco using steam

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102183280A (zh) * 2011-03-02 2011-09-14 山东中烟工业有限责任公司 基于统计学原理与plc技术测算烟草储丝柜出料量的方法
CN102183280B (zh) * 2011-03-02 2012-09-05 山东中烟工业有限责任公司 基于统计学原理与plc技术测算烟草储丝柜出料量的方法
CN104460488A (zh) * 2014-11-04 2015-03-25 山东中烟工业有限责任公司 一种提高加料机过程数据分析精度的方法
CN110638083A (zh) * 2018-06-26 2020-01-03 中国科学院理化技术研究所 一种膨胀烟丝的高效制备方法
CN115989884A (zh) * 2021-10-19 2023-04-21 贵州中烟工业有限责任公司 一种烟丝处理方法及烟丝处理设备

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Publication number Publication date
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