EP2230950B1 - A process for producing tobacco products - Google Patents
A process for producing tobacco products Download PDFInfo
- Publication number
- EP2230950B1 EP2230950B1 EP08863262.5A EP08863262A EP2230950B1 EP 2230950 B1 EP2230950 B1 EP 2230950B1 EP 08863262 A EP08863262 A EP 08863262A EP 2230950 B1 EP2230950 B1 EP 2230950B1
- Authority
- EP
- European Patent Office
- Prior art keywords
- tobacco
- stem
- tobacco stem
- rollers
- lamina
- 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.)
- Active
Links
- 238000000034 method Methods 0.000 title claims description 28
- 235000019505 tobacco product Nutrition 0.000 title description 20
- 241000208125 Nicotiana Species 0.000 claims description 114
- 235000002637 Nicotiana tabacum Nutrition 0.000 claims description 114
- 238000005096 rolling process Methods 0.000 claims description 15
- 210000003850 cellular structure Anatomy 0.000 claims description 7
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 6
- 238000005520 cutting process Methods 0.000 claims description 5
- 239000007788 liquid Substances 0.000 claims description 3
- 239000000047 product Substances 0.000 description 16
- 235000019504 cigarettes Nutrition 0.000 description 6
- 230000001143 conditioned effect Effects 0.000 description 5
- 230000003750 conditioning effect Effects 0.000 description 3
- 238000010586 diagram Methods 0.000 description 3
- 238000001035 drying Methods 0.000 description 3
- 238000004519 manufacturing process Methods 0.000 description 3
- 239000002245 particle Substances 0.000 description 3
- 239000000945 filler Substances 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 239000004033 plastic Substances 0.000 description 2
- 229920003023 plastic Polymers 0.000 description 2
- 238000003860 storage Methods 0.000 description 2
- SNICXCGAKADSCV-JTQLQIEISA-N (-)-Nicotine Chemical compound CN1CCC[C@H]1C1=CC=CN=C1 SNICXCGAKADSCV-JTQLQIEISA-N 0.000 description 1
- 241000238631 Hexapoda Species 0.000 description 1
- 238000001514 detection method Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000012467 final product Substances 0.000 description 1
- 239000010419 fine particle Substances 0.000 description 1
- 238000010304 firing Methods 0.000 description 1
- 239000000796 flavoring agent Substances 0.000 description 1
- 235000019634 flavors Nutrition 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 229960002715 nicotine Drugs 0.000 description 1
- SNICXCGAKADSCV-UHFFFAOYSA-N nicotine Natural products CN1CCCC1C1=CC=CN=C1 SNICXCGAKADSCV-UHFFFAOYSA-N 0.000 description 1
- 230000000704 physical effect Effects 0.000 description 1
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
- A24B5/00—Stripping tobacco; Treatment of stems or ribs
- A24B5/08—Stripping tobacco; Treatment of stems or ribs by cutting-off, shaving off, pressing flat the thick parts of stems or ribs
-
- 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
- A24B3/04—Humidifying or drying tobacco bunches or cut 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
- A24B5/00—Stripping tobacco; Treatment of stems or ribs
- A24B5/14—Flattening machines for leaves or stems
Definitions
- the present invention relates to a process for producing a tobacco product, and in particular, to a process for producing a roll your own (RYO) tobacco product.
- Typical roll your own (RYO) tobacco products are produced using the lamina portion of harvested tobacco leaves which provides the physical characteristics required once the tobacco is cut such that the resulting shag has the desirable consistency for roll your own tobacco products.
- Tobacco stems are a bi-product of the harvested tobacco leaves that have been used as a filler material in tailor made tobacco cigarette products where the tobacco stem is cut producing the filler material and then recombined with the cut lamina portion which is then used to produce the tailor made cigarette.
- the tobacco stem is far cheaper than the tobacco lamina, the use of the tobacco lamina for the production of cigarettes reduces the overall production cost of the cigarettes.
- GB 951,485 discloses a method of treating tobacco stems for producing a tobacco article. Furthermore GB 1,089,361 discloses a method of processing tobacco for use in the production of cigarettes.
- tobacco stem On characteristic of tobacco stem is that it has a lower amount of nicotine and tar compared to the lamina portion of the tobacco leaf. Accordingly, it is possible to produce a tobacco product with less of these harmful bi-products if more of the tobacco stem is used in place of the tobacco lamina to produce the tobacco product.
- the present invention seeks to provide a process whereby a proportion of tobacco stem may be incorporated with tobacco lamina and used to produce a roll your own tobacco product.
- the present invention provides a process for producing a tobacco product from tobacco lamina and tobacco stem, the process including the steps of:
- the tobacco product is a roll your own tobacco product.
- the cellular structure of the tobacco stem is broken down after step a. to an extent that the tobacco stem loses rigidity.
- the tobacco stem is preconditioned prior to step a. wherein the preconditioning of the stem increases the moisture content and softens the tobacco stem.
- the preconditioning of the stem includes contacting the stem with steam and/or liquid water.
- the stem is contacted with steam at a temperature of between 100 °C and 150 °C, and more preferably between 101 °C and 115 °C.
- the preconditioning step further includes a bulking step whereby the tobacco stem is allowed to rest after being contacted with steam and/or liquid water to allow further moisture to absorb into the tobacco stem increasing the overall moisture content of the tobacco stem.
- the tobacco is allowed to rest for a period of between 4 hours and 4 days.
- the step a. includes a two step rolling process.
- the two step rolling process includes:
- the tobacco stem may be optionally preconditioned to increase the moisture content of the stems.
- the stem is contacted with steam at a temperature of between 100 °C and 150 °C, and more preferably between 101 °C and 115 °C.
- the tobacco stem is flattened in order to break down the cellular structure of the tobacco stem to a point where the tobacco stem becomes quite pliable and flat, which is not dissimilar to the structure of the lamina portion of the tobacco leaf.
- This flattened tobacco stem can then be recombined with a tobacco lamina and subsequently cut to provide a shag that is suitable for use in tobacco roll your own products. If flattened and combined with the lamina prior to cutting to produce the shag, the resulting tobacco stem particles stay within the shag product as they are quite similar in structure and physicality and don't fall to the bottom the tobacco pouch or container.
- the overall proportion of tobacco stem incorporated in the final roll your own shag product may be up to 20% wt without significant appearance or structural difference from a customer's perspective of the product.
- a proportion of 10% wt to 15% wt of the tobacco stem appears in the final roll your own tobacco product after being mixed with the lamina.
- the flattening process wherein the tobacco stems have their cellular structure broken down to a sufficient level may be undertaken in any suitable manner.
- the tobacco stems are conditioned to increase their moisture content after which they pass through two roller steps.
- the first roller step flattens the tobacco stem between two rollers with a gap of approximately 0.3 to 1.0mm gap between the rollers, and preferably a 0.4 to 0.7mm gap
- the second rolling step flattens the tobacco between two further rollers with a 0.1 to 0.6mm gap, and preferably a 0.1 to 0.4mm gap between the rollers.
- the tobacco stems are sufficiently flattened wherein their cellular structures have been broken down such that the stems have lost their rigidity and are substantially similar in nature to the lamina portion of the tobacco leaf.
- the tobacco stem is flattened and takes on similar physical properties to the lamina portion of the leaf, it can be combined with the tobacco lamina with the resulting mixture being subsequently cut providing a shag with the suitable characteristics required for a roll your own tobacco product.
- FIG 1 there is shown a detailed process flow diagram of the various stages of a preferred embodiment of the present invention.
- cartons of whole tobacco stem are loaded onto a loading station where they are automatically conveyed to a tipper 20 which empties the stem into a feeder 30.
- the whole tobacco stem is fed from the feeder 30 through a metering tube which controls the delivery of product into a double vibratory sieve 40.
- the sieve 40 removes both very large objects and very fine stem for discarding.
- Belt conveyors then transport the product tobacco stem to the vibratory conveyors leading to the foreign body detector also at 40.
- the tobacco stem After passing from the foreign body detector 40, the tobacco stem passes to an air lift 50 which captures and pneumatically conveys the whole stem product to a weight conveyor. From there the stem moves to the add moist tunnel 70 where the stem is conditioned by contact with water and/or steam to increase the stem's overall moisture content, after which the stem moves to whole stem bins 80 before proceeding to the flattening process stages.
- the stem may remain in the bins, or bulked, for a period of between 4 hours and 4 days. This has the effect of increasing the moisture content of the stems as the water and/or steam contacted with the stem just prior has more time to absorb into the stem.
- Whole conditioned tobacco stem is discharged from the whole stem bins 80 onto the bin discharge belt conveyor 100.
- Stem is sent via a metering tube 110 to a weigh conveyor before entering the conditioning heat tunnel 120 which increases the moisture content of the stem again by contacting the tobacco stem with steam at 1.2 - 2 kPA.
- the tobacco stem is then conveyed to a first flattening step 130 where the tobacco stem is passed through two rollers designed to flatten the moist stem to between 0.4 mm to 0.7 mm.
- the flattened tobacco stem is then conveyed from 140 to a second flattening step 150 where the stem is passed through two further rollers designed to flatten the moist tobacco stem to between 0.1 mm to 0.4 mm.
- the flattening of the tobacco stem breaks down the cellular structure of the tobacco stem where the stem loses its rigidity and becomes significantly malleable.
- the flattened tobacco stem is then filled into tubs 160 where it is stored until combined with bright and dark lamina.
- the flattened tobacco stem feed stock 160 is then combined at a proportion of 15% stem to 85% lamina with the conditioned lamina 2 and 3 and then enters the casing cylinder 200 via a small vibrating conveyor. Casing is applied to the lamina and flattened tobacco stem combination in the casing cylinder 200 at temperatures between 70 and 80°C. Water is added to the tobacco via steam atomising nozzles at the entry and exit of the cylinder which increases the moisture content of the lamina and flattened tobacco stem combination.
- the lamina and flattened tobacco stem combination exits the casing cylinder 200 onto a belt conveyor to one of two blending bins, each of which has the capacity to hold one operation worth of the lamina and flattened tobacco stem combination.
- a foreign body detector 220 sorts and rejects foreign bodies present in the product e.g. plastics, non tobacco leaves, strings, paper, insects, etc. The detection is via a low power laser which is capable of determining subtle differences in colour and texture of non tobacco product.
- Good product consisting of the lamina and flattened tobacco stem combination is transported away via belt conveyors leading to a vibratory conveyor which delivers the product to foreign matter detector can and then to the cutting and conditioning area of the process.
- the lamina and flattened tobacco stem combination then enters a feeder bin 230. From here it is conveyed via an s-elevating conveyor and through a metering tube to regulate the lamina and flattened tobacco stem combination before entering the cutter.
- the lamina and flattened tobacco stem combination is then fed to one of two cutters 240 where it is cut at rate of typically between 38 cpi (cuts per inch) and 80 cpi (cuts per inch) or 15 cuts per cm and 31 cuts per cm. Cut tobacco is then sent to a feeder bin. From here it is conveyed via an s-elevator, through a metering tube to a weigh conveyor before entering the drying cylinder 260.
- the Cylindrical gas fired drying unit 260 reduces the cut tobacco moisture content to the desired value.
- the required process gas temperature in the dryer at tobacco inlet point is achieved by modulating the burner firing rate. After being discharged from the dryer the tobacco is passed under a NDC moisture meter which is used to monitor the drying process.
- the cut tobacco product exiting the dryer 260 passes over a vibrating filter conveyor that separates the fine particles from the good product.
- Certain blends of RYO tobacco are then passed through a top flavouring cylinder 280 which adds distinctive flavours to suit the final product requirements.
- a second belt conveyor 270 allows the product not requiring flavouring to bypass the top flavouring cylinder and proceed directly to the loading room.
- These skips 290 are conveyed to one of two robotic arms that automatically stack them onto storage trolleys. These trolleys are then manually wheeled to a humidity controlled storage room, where they are stored before being packaged as RYO tobacco products.
Description
- The present invention relates to a process for producing a tobacco product, and in particular, to a process for producing a roll your own (RYO) tobacco product.
- Typical roll your own (RYO) tobacco products are produced using the lamina portion of harvested tobacco leaves which provides the physical characteristics required once the tobacco is cut such that the resulting shag has the desirable consistency for roll your own tobacco products.
- Tobacco stems are a bi-product of the harvested tobacco leaves that have been used as a filler material in tailor made tobacco cigarette products where the tobacco stem is cut producing the filler material and then recombined with the cut lamina portion which is then used to produce the tailor made cigarette. As the tobacco stem is far cheaper than the tobacco lamina, the use of the tobacco lamina for the production of cigarettes reduces the overall production cost of the cigarettes.
-
GB 951,485 GB 1,089,361 - On characteristic of tobacco stem is that it has a lower amount of nicotine and tar compared to the lamina portion of the tobacco leaf. Accordingly, it is possible to produce a tobacco product with less of these harmful bi-products if more of the tobacco stem is used in place of the tobacco lamina to produce the tobacco product.
- However, it is difficult to combine the tobacco stem with tobacco lamina in order to produce a suitable tobacco product that has the necessary physical characteristics to be used as a roll your own tobacco product. The tobacco stems are significantly harder than the tobacco laminar and not able to be cut to provide a shag with the right physical characteristics for the roll your own tobacco product. Some attempts have been made, however the inability of the cut stem particles to matt with the lamina and become evenly distributed throughout the product causes the cut stem particles to simply separate from the lamina shag and fall to the bottom of the tobacco pouch where they can't be used to make the roll your own cigarettes.
- Accordingly, the present invention seeks to provide a process whereby a proportion of tobacco stem may be incorporated with tobacco lamina and used to produce a roll your own tobacco product.
- According to one aspect, the present invention provides a process for producing a tobacco product from tobacco lamina and tobacco stem, the process including the steps of:
- a. flattening the tobacco stem to break down the cellular structure of the tobacco stem;
- b. combining the flattened tobacco stem with the tobacco lamina; and,
- c. cutting the combined flattened tobacco stem and tobacco lamina to produce the tobacco product.
- In one form the tobacco product is a roll your own tobacco product.
- According to a preferred form the cellular structure of the tobacco stem is broken down after step a. to an extent that the tobacco stem loses rigidity.
- According to a preferred form, the tobacco stem is preconditioned prior to step a. wherein the preconditioning of the stem increases the moisture content and softens the tobacco stem. In a preferred form, the preconditioning of the stem includes contacting the stem with steam and/or liquid water. In a more preferred form the stem is contacted with steam at a temperature of between 100 °C and 150 °C, and more preferably between 101 °C and 115 °C.
- In a further preferred form, the preconditioning step further includes a bulking step whereby the tobacco stem is allowed to rest after being contacted with steam and/or liquid water to allow further moisture to absorb into the tobacco stem increasing the overall moisture content of the tobacco stem. In a preferred form the tobacco is allowed to rest for a period of between 4 hours and 4 days.
- According to one form, the step a. includes a two step rolling process. In a preferred form, the two step rolling process includes:
- a first rolling step, wherein the tobacco stem is passed through a set of rollers with a 0.3 to 1.0mm gap between the rollers, and preferably a 0.4 to 0.7mm gap; and,
- a second rolling step wherein the tobacco stem is passed through a set of rollers with a 0.1 to 0.6mm gap between the rollers, and preferably a 0.1 to 0.4mm gap.
- The present invention will become better understood from the following detailed description of a preferred but non-limiting embodiment thereof, described in connection with the accompanying figures, wherein:
- Figure 1 is a process diagram detailing various stages in the flattening step of the tobacco stem of a preferred embodiment according to the present invention; and
- Figure 2 is a process diagram detailing the various stages in the combining and cutting steps of a preferred embodiment according to one aspect of the present invention.
- According to one embodiment of the present invention the tobacco stem may be optionally preconditioned to increase the moisture content of the stems. In a preferred form the stem is contacted with steam at a temperature of between 100 °C and 150 °C, and more preferably between 101 °C and 115 °C.
- After this the tobacco stem is flattened in order to break down the cellular structure of the tobacco stem to a point where the tobacco stem becomes quite pliable and flat, which is not dissimilar to the structure of the lamina portion of the tobacco leaf. This flattened tobacco stem can then be recombined with a tobacco lamina and subsequently cut to provide a shag that is suitable for use in tobacco roll your own products. If flattened and combined with the lamina prior to cutting to produce the shag, the resulting tobacco stem particles stay within the shag product as they are quite similar in structure and physicality and don't fall to the bottom the tobacco pouch or container. The overall proportion of tobacco stem incorporated in the final roll your own shag product may be up to 20% wt without significant appearance or structural difference from a customer's perspective of the product.
- Preferably a proportion of 10% wt to 15% wt of the tobacco stem appears in the final roll your own tobacco product after being mixed with the lamina.
- The flattening process wherein the tobacco stems have their cellular structure broken down to a sufficient level may be undertaken in any suitable manner. In a preferred form of the present invention, the tobacco stems are conditioned to increase their moisture content after which they pass through two roller steps. The first roller step flattens the tobacco stem between two rollers with a gap of approximately 0.3 to 1.0mm gap between the rollers, and preferably a 0.4 to 0.7mm gap, and the second rolling step flattens the tobacco between two further rollers with a 0.1 to 0.6mm gap, and preferably a 0.1 to 0.4mm gap between the rollers. After these two rolling stages, the tobacco stems are sufficiently flattened wherein their cellular structures have been broken down such that the stems have lost their rigidity and are substantially similar in nature to the lamina portion of the tobacco leaf.
- Once the tobacco stem is flattened and takes on similar physical properties to the lamina portion of the leaf, it can be combined with the tobacco lamina with the resulting mixture being subsequently cut providing a shag with the suitable characteristics required for a roll your own tobacco product.
- Referring to figure 1 there is shown a detailed process flow diagram of the various stages of a preferred embodiment of the present invention.
- Referring to figure 1 at process step 10 cartons of whole tobacco stem are loaded onto a loading station where they are automatically conveyed to a tipper 20 which empties the stem into a feeder 30. The whole tobacco stem is fed from the feeder 30 through a metering tube which controls the delivery of product into a double vibratory sieve 40. The sieve 40 removes both very large objects and very fine stem for discarding. Belt conveyors then transport the product tobacco stem to the vibratory conveyors leading to the foreign body detector also at 40.
- After passing from the foreign body detector 40, the tobacco stem passes to an air lift 50 which captures and pneumatically conveys the whole stem product to a weight conveyor. From there the stem moves to the add moist tunnel 70 where the stem is conditioned by contact with water and/or steam to increase the stem's overall moisture content, after which the stem moves to whole stem bins 80 before proceeding to the flattening process stages. Here the stem may remain in the bins, or bulked, for a period of between 4 hours and 4 days. This has the effect of increasing the moisture content of the stems as the water and/or steam contacted with the stem just prior has more time to absorb into the stem.
- Whole conditioned tobacco stem is discharged from the whole stem bins 80 onto the bin discharge belt conveyor 100. Stem is sent via a metering tube 110 to a weigh conveyor before entering the conditioning heat tunnel 120 which increases the moisture content of the stem again by contacting the tobacco stem with steam at 1.2 - 2 kPA. The tobacco stem is then conveyed to a first flattening step 130 where the tobacco stem is passed through two rollers designed to flatten the moist stem to between 0.4 mm to 0.7 mm.
- The flattened tobacco stem is then conveyed from 140 to a second flattening step 150 where the stem is passed through two further rollers designed to flatten the moist tobacco stem to between 0.1 mm to 0.4 mm. The flattening of the tobacco stem breaks down the cellular structure of the tobacco stem where the stem loses its rigidity and becomes significantly malleable.
- The flattened tobacco stem is then filled into tubs 160 where it is stored until combined with bright and dark lamina.
- Referring to figure 2 bright lamina and/or dark lamina is conditioned and deposited as a feed stock at process steps 2 and 3. The conditioning stage for both types of lamina increases the moisture content of the lamina feed stock.
- The flattened tobacco stem feed stock 160 is then combined at a proportion of 15% stem to 85% lamina with the conditioned lamina 2 and 3 and then enters the casing cylinder 200 via a small vibrating conveyor. Casing is applied to the lamina and flattened tobacco stem combination in the casing cylinder 200 at temperatures between 70 and 80°C. Water is added to the tobacco via steam atomising nozzles at the entry and exit of the cylinder which increases the moisture content of the lamina and flattened tobacco stem combination.
- The lamina and flattened tobacco stem combination exits the casing cylinder 200 onto a belt conveyor to one of two blending bins, each of which has the capacity to hold one operation worth of the lamina and flattened tobacco stem combination.
- A foreign body detector 220 sorts and rejects foreign bodies present in the product e.g. plastics, non tobacco leaves, strings, paper, insects, etc. The detection is via a low power laser which is capable of determining subtle differences in colour and texture of non tobacco product.
- Good product consisting of the lamina and flattened tobacco stem combination is transported away via belt conveyors leading to a vibratory conveyor which delivers the product to foreign matter detector can and then to the cutting and conditioning area of the process.
- The lamina and flattened tobacco stem combination then enters a feeder bin 230. From here it is conveyed via an s-elevating conveyor and through a metering tube to regulate the lamina and flattened tobacco stem combination before entering the cutter. The lamina and flattened tobacco stem combination is then fed to one of two cutters 240 where it is cut at rate of typically between 38 cpi (cuts per inch) and 80 cpi (cuts per inch) or 15 cuts per cm and 31 cuts per cm. Cut tobacco is then sent to a feeder bin. From here it is conveyed via an s-elevator, through a metering tube to a weigh conveyor before entering the drying cylinder 260.
- The Cylindrical gas fired drying unit 260 reduces the cut tobacco moisture content to the desired value. The required process gas temperature in the dryer at tobacco inlet point is achieved by modulating the burner firing rate. After being discharged from the dryer the tobacco is passed under a NDC moisture meter which is used to monitor the drying process.
- The cut tobacco product exiting the dryer 260 passes over a vibrating filter conveyor that separates the fine particles from the good product. Certain blends of RYO tobacco are then passed through a top flavouring cylinder 280 which adds distinctive flavours to suit the final product requirements. A second belt conveyor 270 allows the product not requiring flavouring to bypass the top flavouring cylinder and proceed directly to the loading room.
- Tobacco enters the loading room via a belt conveyor where it is discharged into rectangular plastic skips 290. These skips 290 are conveyed to one of two robotic arms that automatically stack them onto storage trolleys. These trolleys are then manually wheeled to a humidity controlled storage room, where they are stored before being packaged as RYO tobacco products.
Claims (10)
- A process for producing a roll your own tobacco shag from tobacco lamina and tobacco stem, the process including the steps of:a. flattening the tobacco stem to break down the cellular structure of the tobacco stem;b. combining the flattened tobacco stem with the tobacco lamina; and,c. cutting the combined flattened tobacco stem and tobacco lamina to produce a roll your own tobacco shag.
- A process according to claim 1 wherein the tobacco stem is subjected to a preconditioning step prior to step a. wherein the preconditioning step increases the moisture content of the tobacco stem wherein the preconditioning step includes an initial step of contacting the tobacco stem with steam and/or liquid water followed by an optional bulking step wherein the tobacco stem is allowed to rest prior to step a.
- A process according to claim 2 wherein the initial preconditioning step includes contacting the tobacco stem with steam at a temperature of between 100 °C and 150 °C, and preferably between 101 °C and 115 °C.
- A process according to claim 2 or 3 wherein the tobacco stem is allowed to rest during a bulking step for between 1 hour and 4 days prior to step a., and preferably for at least 4 hours.
- A process according to any one of claims 2 to 4 wherein the preconditioning step increases the moisture content of the tobacco stem to between 15 to 35% wt and preferably at least 20% wt.
- A process according to any one of claims 1 to 5 wherein the flattening of the tobacco stem in step a. includes a two step rolling process.
- A process according to claim 6 wherein the two step rolling process includes a first rolling step wherein the tobacco stem is passed through a set of two rollers with a 0.3 mm to 1.0 mm gap between the rollers.
- A process according to claim 6 wherein the two step rolling process includes a first rolling step wherein the tobacco stem is passed through a set of two rollers with a 0.4 mm to 0.7 mm gap between the rollers.
- A process according to any one of claims 6 to 8 wherein the two step rolling process includes a second rolling step wherein the tobacco stem is passed through a set of two rollers with a 0.1 to 0.6mm gap between the rollers.
- A process according to any one of claims 6 to 8 wherein the two step rolling process includes a second rolling step wherein the tobacco stem is passed through a set of two rollers with a 0.1 mm to 0.4 mm gap between the rollers.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
AU2007906969A AU2007906969A0 (en) | 2007-12-19 | A process for producing tobacco products | |
PCT/AU2008/001552 WO2009076699A1 (en) | 2007-12-19 | 2008-10-21 | A process for producing tobacco products |
Publications (4)
Publication Number | Publication Date |
---|---|
EP2230950A1 EP2230950A1 (en) | 2010-09-29 |
EP2230950A4 EP2230950A4 (en) | 2018-01-10 |
EP2230950B1 true EP2230950B1 (en) | 2019-11-20 |
EP2230950B8 EP2230950B8 (en) | 2020-01-01 |
Family
ID=40795099
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP08863262.5A Active EP2230950B8 (en) | 2007-12-19 | 2008-10-21 | A process for producing tobacco products |
Country Status (4)
Country | Link |
---|---|
EP (1) | EP2230950B8 (en) |
AU (1) | AU2008338293B2 (en) |
NZ (1) | NZ586254A (en) |
WO (1) | WO2009076699A1 (en) |
Families Citing this family (17)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
BR112013015610B1 (en) * | 2010-12-23 | 2020-11-24 | Philip Morris Products S.A. | METHOD FOR THE PRODUCTION OF EXPANDED TOBACCO RODS |
MX2013007353A (en) * | 2010-12-23 | 2013-08-01 | Philip Morris Prod | Tobacco cut filler including cut rolled stems. |
TW201233345A (en) * | 2010-12-23 | 2012-08-16 | Philip Morris Prod | Method of treating burley tobacco stems |
EP2609817A1 (en) * | 2011-12-30 | 2013-07-03 | Philip Morris Products S.A. | Method for flattening tobacco leaves |
CN102613685A (en) * | 2012-03-12 | 2012-08-01 | 红云红河烟草(集团)有限责任公司 | Pretreatment method for improving quality of tobacco stems |
CN104055217B (en) * | 2014-07-10 | 2016-07-13 | 广东省金叶科技开发有限公司 | A kind of preparation method of cabo stalk sheet |
CN104095281B (en) * | 2014-07-23 | 2016-04-06 | 广东省金叶科技开发有限公司 | A kind of offal uses new method |
CN105167161A (en) * | 2015-07-17 | 2015-12-23 | 云南中烟工业有限责任公司 | Fine grouped processing method for tobacco stems |
CN105149069B (en) * | 2015-09-01 | 2017-12-01 | 张家口市东力机械制造有限责任公司 | Offal, which crushes, squeezes rod forming processes equipment |
CN108685141A (en) * | 2018-04-25 | 2018-10-23 | 湖北中烟工业有限责任公司 | A kind of processing method promoting below average quality of tobacco |
CN109275941B (en) * | 2018-09-30 | 2021-03-16 | 红塔烟草(集团)有限责任公司 | Tobacco stem processing method using stem pieces for feeding |
CN111610276A (en) * | 2020-06-09 | 2020-09-01 | 甘肃烟草工业有限责任公司 | Cigarette raw material mixing proportion distribution measuring method based on tobacco characteristic components |
CN112869225B (en) * | 2021-01-29 | 2022-07-29 | 智思控股集团有限公司 | Method and equipment for preparing multi-variety cut stems |
CN114304706B (en) * | 2021-11-25 | 2023-04-11 | 云南昆船烟草设备有限公司 | Tobacco stem drying method and device |
CN114271525A (en) * | 2022-01-06 | 2022-04-05 | 广西中烟工业有限责任公司 | Moisture control method for pressure stem moistening |
CN114938860B (en) * | 2022-06-06 | 2023-07-11 | 福建中烟工业有限责任公司 | Method for preparing cut stems, cut tobacco composition and application |
CN114847511B (en) * | 2022-06-06 | 2023-06-23 | 福建中烟工业有限责任公司 | Method for preparing stem slices, cut stems and cut tobacco composition and application |
Family Cites Families (10)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB951485A (en) * | 1961-12-20 | 1964-03-04 | Desmond Walter Molins | Improvements in or relating to a method of manufacturing cigarettes |
GB1089361A (en) | 1964-01-22 | 1967-11-01 | Desmond Walter Molins | Improvements relating to tobacco processing |
US3411514A (en) * | 1966-12-21 | 1968-11-19 | Philip Morris Inc | Method of making improved shreds from rolled tobacco stems |
GB1284795A (en) * | 1969-05-09 | 1972-08-09 | Amf Inc | Wet processing of tobacco stems |
US3690328A (en) * | 1970-04-20 | 1972-09-12 | American Mach & Foundry | Wet processing of tobacco stems |
BE790758A (en) * | 1971-11-04 | 1973-02-15 | Philip Morris Inc | PROCESS FOR INCREASING THE VOLUME OF TOBACCO STEMS |
JPS53104797A (en) * | 1977-02-22 | 1978-09-12 | Japan Tobacco Inc | Preparation of expanded veins and stalks of tobacco leaves |
DE2913823A1 (en) * | 1979-04-06 | 1980-10-09 | Bat Cigarettenfab Gmbh | METHOD FOR PRODUCING A TOBACCOA CUT WITH IMPROVED FILLABILITY |
US4787402A (en) * | 1986-02-03 | 1988-11-29 | R. J. Reynolds Tobacco Company | Process and apparatus for providing roll reconstituted tobacco material |
EP0931464A1 (en) * | 1998-01-23 | 1999-07-28 | Fabriques De Tabac Reunies S.A. | A process for providing cut filler for cigarettes |
-
2008
- 2008-10-21 NZ NZ586254A patent/NZ586254A/en unknown
- 2008-10-21 AU AU2008338293A patent/AU2008338293B2/en active Active
- 2008-10-21 WO PCT/AU2008/001552 patent/WO2009076699A1/en active Application Filing
- 2008-10-21 EP EP08863262.5A patent/EP2230950B8/en active Active
Non-Patent Citations (1)
Title |
---|
None * |
Also Published As
Publication number | Publication date |
---|---|
NZ586254A (en) | 2012-07-27 |
EP2230950B8 (en) | 2020-01-01 |
EP2230950A4 (en) | 2018-01-10 |
AU2008338293A1 (en) | 2009-06-25 |
EP2230950A1 (en) | 2010-09-29 |
WO2009076699A1 (en) | 2009-06-25 |
AU2008338293B2 (en) | 2012-06-21 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
EP2230950B1 (en) | A process for producing tobacco products | |
RU2714782C2 (en) | Production line of homogenised tobacco material and method for in-line production of homogenised tobacco material | |
RU2714779C2 (en) | Production line of homogenised tobacco material and method for in-line production of homogenised tobacco material | |
EP3075268B1 (en) | Apparatus for forming an endless rod from a sticky tobacco material | |
JP6811616B2 (en) | Reconstructed tobacco sheet and related methods | |
RU2688385C1 (en) | Method for production of cast sheet of homogenised tobacco material | |
EP0651951B1 (en) | Method for producing blended cigarette filler | |
KR102526262B1 (en) | Method and apparatus for intermediately storing double-length semi-finished products | |
EP3223636B1 (en) | Oral pouched product | |
JP2022500043A (en) | Methods and plants for the production of reconstructed tobacco | |
US6782890B2 (en) | Apparatus for building tobacco rods in cigarette making machines | |
CN107072285A (en) | Method for producing the tobacco-containing material that homogenizes | |
JP5439490B2 (en) | Tobacco modular preparation including extraction | |
KR102453354B1 (en) | Process for the production of homogenized tobacco material | |
CN111093401B (en) | Device and method for manufacturing reconstituted tobacco shreds | |
CN113194759B (en) | Method and apparatus for producing alkaloid containing material sheet | |
US20080196731A1 (en) | Processing of Tobacco Materials Containing a High Proportion of Tobacco Fines | |
CN106263002B (en) | A kind of processing technology for lifting expanded cut stem raw material availability | |
US4449540A (en) | Separation of lamina from stems in baled tobacco | |
WO1994010864A1 (en) | Cigarette and process for preparing the cigarette | |
US11957156B2 (en) | Method for the preparation of a sheet including a homogenized material containing alkaloids and aerosol forming article comprising a component prepared from it | |
RU93226U1 (en) | CIGARETTE | |
CN114828662A (en) | Sheets of alkaloid containing material | |
CN114828664A (en) | Method for producing sheets of material containing alkaloids | |
CN109770414B (en) | Method and device for producing heating rods |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
PUAI | Public reference made under article 153(3) epc to a published international application that has entered the european phase |
Free format text: ORIGINAL CODE: 0009012 |
|
17P | Request for examination filed |
Effective date: 20100624 |
|
AK | Designated contracting states |
Kind code of ref document: A1 Designated state(s): AT BE BG CH CY CZ DE DK EE ES FI FR GB GR HR HU IE IS IT LI LT LU LV MC MT NL NO PL PT RO SE SI SK TR |
|
AX | Request for extension of the european patent |
Extension state: AL BA MK RS |
|
DAX | Request for extension of the european patent (deleted) | ||
RA4 | Supplementary search report drawn up and despatched (corrected) |
Effective date: 20171208 |
|
RIC1 | Information provided on ipc code assigned before grant |
Ipc: A24B 5/14 20060101ALI20171204BHEP Ipc: A24B 5/08 20060101AFI20171204BHEP Ipc: A24B 3/04 20060101ALI20171204BHEP Ipc: A24B 5/16 20060101ALI20171204BHEP Ipc: A24B 3/12 20060101ALI20171204BHEP |
|
STAA | Information on the status of an ep patent application or granted ep patent |
Free format text: STATUS: EXAMINATION IS IN PROGRESS |
|
17Q | First examination report despatched |
Effective date: 20181005 |
|
GRAP | Despatch of communication of intention to grant a patent |
Free format text: ORIGINAL CODE: EPIDOSNIGR1 |
|
STAA | Information on the status of an ep patent application or granted ep patent |
Free format text: STATUS: GRANT OF PATENT IS INTENDED |
|
INTG | Intention to grant announced |
Effective date: 20190515 |
|
GRAS | Grant fee paid |
Free format text: ORIGINAL CODE: EPIDOSNIGR3 |
|
GRAA | (expected) grant |
Free format text: ORIGINAL CODE: 0009210 |
|
STAA | Information on the status of an ep patent application or granted ep patent |
Free format text: STATUS: THE PATENT HAS BEEN GRANTED |
|
AK | Designated contracting states |
Kind code of ref document: B1 Designated state(s): AT BE BG CH CY CZ DE DK EE ES FI FR GB GR HR HU IE IS IT LI LT LU LV MC MT NL NO PL PT RO SE SI SK TR |
|
REG | Reference to a national code |
Ref country code: GB Ref legal event code: FG4D |
|
REG | Reference to a national code |
Ref country code: CH Ref legal event code: EP |
|
REG | Reference to a national code |
Ref country code: IE Ref legal event code: FG4D |
|
REG | Reference to a national code |
Ref country code: CH Ref legal event code: PK Free format text: BERICHTIGUNG B8 |
|
REG | Reference to a national code |
Ref country code: AT Ref legal event code: REF Ref document number: 1203142 Country of ref document: AT Kind code of ref document: T Effective date: 20191215 |
|
RAP2 | Party data changed (patent owner data changed or rights of a patent transferred) |
Owner name: BRITISH AMERICAN TOBACCO AUSTRALASIA LIMITED |
|
REG | Reference to a national code |
Ref country code: DE Ref legal event code: R096 Ref document number: 602008061690 Country of ref document: DE |
|
REG | Reference to a national code |
Ref country code: NL Ref legal event code: FP |
|
REG | Reference to a national code |
Ref country code: LT Ref legal event code: MG4D |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: BG Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20200220 Ref country code: GR Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20200221 Ref country code: LT Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20191120 Ref country code: FI Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20191120 Ref country code: ES Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20191120 Ref country code: SE Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20191120 Ref country code: LV Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20191120 Ref country code: NO Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20200220 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: IS Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20200320 Ref country code: HR Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20191120 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: CZ Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20191120 Ref country code: RO Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20191120 Ref country code: EE Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20191120 Ref country code: PT Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20200412 Ref country code: DK Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20191120 |
|
REG | Reference to a national code |
Ref country code: AT Ref legal event code: MK05 Ref document number: 1203142 Country of ref document: AT Kind code of ref document: T Effective date: 20191120 |
|
REG | Reference to a national code |
Ref country code: DE Ref legal event code: R097 Ref document number: 602008061690 Country of ref document: DE |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: SK Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20191120 |
|
PLBE | No opposition filed within time limit |
Free format text: ORIGINAL CODE: 0009261 |
|
STAA | Information on the status of an ep patent application or granted ep patent |
Free format text: STATUS: NO OPPOSITION FILED WITHIN TIME LIMIT |
|
REG | Reference to a national code |
Ref country code: DE Ref legal event code: R082 Ref document number: 602008061690 Country of ref document: DE Representative=s name: VENNER SHIPLEY GERMANY LLP, DE Ref country code: DE Ref legal event code: R082 Ref document number: 602008061690 Country of ref document: DE Representative=s name: VENNER SHIPLEY LLP, DE |
|
26N | No opposition filed |
Effective date: 20200821 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: AT Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20191120 Ref country code: PL Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20191120 Ref country code: SI Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20191120 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: IT Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20191120 |
|
REG | Reference to a national code |
Ref country code: CH Ref legal event code: PL |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: MC Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20191120 Ref country code: LU Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20201021 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: FR Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20201031 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: CH Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20201031 Ref country code: LI Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20201031 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: IE Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20201021 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: TR Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20191120 Ref country code: MT Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20191120 Ref country code: CY Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20191120 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: BE Payment date: 20221019 Year of fee payment: 15 |
|
P01 | Opt-out of the competence of the unified patent court (upc) registered |
Effective date: 20230504 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: NL Payment date: 20231019 Year of fee payment: 16 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: GB Payment date: 20231020 Year of fee payment: 16 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: DE Payment date: 20231020 Year of fee payment: 16 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: BE Payment date: 20231019 Year of fee payment: 16 |