WO2024079809A1 - Tobacco formulation, tobacco sheet, tobacco filling material, smoking article, tobacco formulation production method, and tobacco sheet production method - Google Patents
Tobacco formulation, tobacco sheet, tobacco filling material, smoking article, tobacco formulation production method, and tobacco sheet production method Download PDFInfo
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- WO2024079809A1 WO2024079809A1 PCT/JP2022/038001 JP2022038001W WO2024079809A1 WO 2024079809 A1 WO2024079809 A1 WO 2024079809A1 JP 2022038001 W JP2022038001 W JP 2022038001W WO 2024079809 A1 WO2024079809 A1 WO 2024079809A1
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- tobacco
- starch
- sheet
- weight
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Classifications
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- 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
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- 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
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- 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
- A24B15/16—Chemical features of tobacco products or tobacco substitutes of tobacco substitutes
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- 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
- A24B15/30—Treatment of tobacco products or tobacco substitutes by chemical substances by organic substances
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- 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
- A24B15/30—Treatment of tobacco products or tobacco substitutes by chemical substances by organic substances
- A24B15/302—Treatment of tobacco products or tobacco substitutes by chemical substances by organic substances by natural substances obtained from animals or plants
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- 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
- A24B15/30—Treatment of tobacco products or tobacco substitutes by chemical substances by organic substances
- A24B15/32—Treatment of tobacco products or tobacco substitutes by chemical substances by organic substances by acyclic compounds
Definitions
- the present invention relates to tobacco preparations, tobacco sheets, tobacco fillers, smoking articles, methods for producing tobacco preparations, and methods for producing tobacco sheets.
- Imitation tobacco is a tobacco material made by artificially forming tobacco leaves into a paper-like form, and is also called tobacco sheet.
- Known methods for manufacturing such tobacco sheets include, for example, a papermaking process, a slurry (cast) process, a rolling (rolling) process, and an extrusion molding process.
- Patent Document 1 discloses that the smaller the particle size of the tobacco, the greater the surface area that bonds the tobacco particles together, improving the strength of the tobacco sheet, and that a uniform sheet can be created by using a particle size of 60 mesh to 400 mesh (56 ⁇ m to 375 ⁇ m).
- Patent Documents 2 and 3 also disclose that tobacco powder with a particle size of 30 to 120 ⁇ m is used, because the strength of the tobacco web decreases when the particle size of the tobacco is 150 ⁇ m or more when homogenized.
- Patent Documents 4 and 5 there is also technology for reducing the particle size of tobacco to nano size and using it as a raw material for the sheet.
- Patent Document 6 in the mixing process before sheet molding, a cellulose material with a particle size of 200 ⁇ m to 4000 ⁇ m is added and mixed with tobacco raw material with a particle size of 30 ⁇ m to 120 ⁇ m, and in this mixture, the above two types of substances with different particle sizes become entangled, allowing the sheet structure to be stably maintained.
- An object of the present invention is to provide a tobacco preparation that uses tobacco raw materials and is capable of forming a tobacco sheet without externally adding raw materials of poorly water-soluble substances, and said tobacco sheet.
- [1] Poorly water-soluble substances derived from tobacco raw materials, (2) a starch extracted from said tobacco material or from other tobacco materials; and (3) a vehicle.
- a tobacco sheet comprising: (1') a poorly water-soluble substance derived from a tobacco raw material; and (2') a starch extracted from the tobacco raw material or another tobacco raw material.
- [15] The tobacco sheet according to any one of [2 to [14], which is a molded product of the tobacco formulation according to [1].
- a tobacco filler comprising the tobacco sheet according to any one of [2] to [15].
- a smoking article comprising the tobacco filler described in [16].
- the smoking article according to [17] which is a non-combustion heating smoking article.
- a method for producing a tobacco sheet according to any one of [2] to [15] comprising: preparing the tobacco formulation by the method according to [19]; and spreading the tobacco formulation on a substrate and drying it.
- the present invention provides a tobacco preparation that uses tobacco raw materials and can be used to form a tobacco sheet without the external addition of other poorly water-soluble substance raw materials, and the tobacco sheet.
- FIG. 1 is a schematic cross-sectional view showing an example of a non-combustion heating smoking system.
- FIG. 2 is a schematic cross-sectional view showing an example of a non-combustion heat smoking article.
- X to Y includes the end values X and Y.
- the tobacco formulation of the present invention comprises: (1) Poorly water-soluble substances derived from tobacco raw materials, (2) a starch extracted from said tobacco material or from another tobacco material; and (3) a vehicle.
- the poorly water-soluble substance of the present invention is derived from tobacco raw materials.
- the poorly water-soluble substance refers to a substance that has a solubility in water of less than 20 ⁇ g/mL at 85° C., and can be obtained as a residue after subjecting tobacco raw materials to boiling and extraction treatments.
- the poorly water-soluble substance can be obtained as a residue of tobacco raw materials by subjecting tobacco raw materials to boiling and extraction treatments under specific conditions and extracting starch from the tobacco raw materials, for example, as shown in [Example 1] or [Example 2] (Preparation of tobacco formulation and tobacco sheet) described below.
- Whether or not a poorly water-soluble substance is derived from a tobacco raw material can be determined, for example, by performing isotope analysis of the poorly water-soluble substance and measuring the 13C/12C ratio.
- the poorly water soluble material may comprise or consist of poorly water soluble fibres.
- the shape of the poorly water-soluble substance in the tobacco formulation is not limited, but it is preferably in the form of particles.
- the lower limit of the primary particle diameter (D90) of the poorly water-soluble substance is not particularly limited, but from the viewpoint of maintaining the sheet structure, it is preferably 20 ⁇ m or more, more preferably 50 ⁇ m or more, and most preferably 100 ⁇ m or more.
- the lower limit of the primary particle diameter (D90) of the poorly water-soluble substance can be 5 ⁇ m or more or 10 ⁇ m or more.
- the upper limit of the primary particle diameter (D90) of the poorly water-soluble substance is not particularly limited, but from the viewpoint of uniformity of the sheet structure, it is preferably 500 ⁇ m or less, more preferably 250 ⁇ m or less, and most preferably 100 ⁇ m or less.
- the upper limit of the primary particle diameter (D90) of the poorly water-soluble substance can also be 80 ⁇ m or less, 50 ⁇ m or less, or 30 ⁇ m or less.
- the upper and lower limits of the primary particle diameter of the poorly water-soluble substance described above can be arbitrarily combined.
- the primary particle diameter (D90) of the poorly water-soluble substance can be measured according to the procedure and conditions described in "(1) Measurement of particle diameter of poorly water-soluble substance" in [Examples] described later. By reducing the primary particle size of the poorly water-soluble substance, the surface area for bonding tobacco particles together increases, and the strength of the tobacco sheet can be improved.
- the lower limit of the content of the poorly water-soluble substance in the tobacco formulation is not particularly limited, but from the viewpoint of functioning as a base material, it is preferably 5% by weight or more, more preferably 10% by weight or more, most preferably 15% by weight or more, and can also be 20% by weight or more, 75% by weight or more, or 90% by weight or more.
- the upper limit of the content of the poorly water-soluble substance in the tobacco formulation is not particularly limited, but can be 95% by weight or less, 80% by weight or less, 70% by weight or less, 50% by weight or less, or 35% by weight or less.
- the upper and lower limits of the content of the poorly water-soluble substance in the tobacco formulation can be combined in any manner.
- the content of the poorly water-soluble substance in the tobacco formulation can be expressed as a value calculated based on the solid content excluding the medium.
- the content of the poorly water-soluble substance in the tobacco formulation can be measured according to the procedures and conditions described in "(3) Measurement of the content of poorly water-soluble substance" in [Examples] below, and calculated as the ratio (wt%) of the weight of the obtained dry matter to the weight of the solid content of the tobacco formulation.
- the content of poorly water-soluble substances in tobacco preparations can also be calculated by the Prosky method. That is, after taking a sample of the tobacco preparation, the starch contained in the sample is randomly decomposed by heat-stable ⁇ -amylase until a small amount of glucose is linked to it. Next, the peptide bonds of the proteins contained in the sample are decomposed by protease. Finally, the sugar chains decomposed by heat-stable ⁇ -amylase are decomposed into one glucose molecule by amyloglucosidase. Then, ethanol is added to the sample to generate a precipitate, and the precipitate is collected by suction filtration and washed with ethanol and acetone.
- the filtration residue obtained by the above suction filtration contains the protein derived from the sample that was not decomposed, the protein derived from the enzyme, and inorganic matter (ash). Therefore, the amount of poorly water-soluble substances is calculated by separately quantifying the protein and ash and subtracting them from the above dry weight.
- the above protein content is calculated by the BSA assay method, which is based on a two-step reaction.
- the divalent copper ions (Cu 2+ ) contained in the kit are reduced to monovalent copper ions (Cu + ) by peptide bonds in the protein solution.
- the amount of Cu 2+ reduced is proportional to the amount of protein in the solution.
- two molecules of bicinchoninic acid (BCA) coordinate with Cu + to form a blue-purple complex that has strong absorption at 562 nm. This is measured with a spectrophotometer and colorimetrically quantified to calculate the protein mass.
- the ash content is calculated from the weight of a certain amount of the protein incinerated at a temperature of 550-600°C.
- tobacco raw materials are raw materials derived from Nicotiana plants, and examples thereof include tobacco raw materials such as tobacco leaves, aged tobacco leaves, tobacco shreds, tobacco powder, parts other than leaves such as midribs and stems, and processed products or waste products obtained by subjecting tobacco raw materials to processing.
- tobacco leaves are a general term for harvested tobacco leaves before they are aged.
- One form of aging includes curing.
- Tobacco shreds are aged tobacco leaves, etc. that have been chopped into a specified size.
- Tobacco powder is pulverized tobacco leaves, etc.
- tobacco varieties can be used as the tobacco raw material.
- examples of tobacco varieties include flue-cured, burley, orient, native, other Nicotiana tabacum varieties, and Nicotiana rustica varieties. These varieties can be used alone, but in order to obtain the desired flavor, they can also be blended during the process from tobacco leaf harvest to the processing of aged tobacco leaves into various forms (i.e., processed tobacco leaves) used in non-combustion heated tobacco products. Details of the tobacco varieties are disclosed in "Encyclopedia of Tobacco, Tobacco Research Center, March 31, 2009."
- the tobacco raw material from which the poorly water-soluble substance is derived may contain alkaloids from the standpoint of palatability quality.
- alkaloids from the standpoint of palatability quality.
- the type of alkaloid is not particularly limited, but nicotine, nornicotine, or a mixture thereof can be used.
- the starch may be extracted from a tobacco raw material contained in a tobacco formulation, or may be extracted from another tobacco raw material not contained in a tobacco formulation. That is, the tobacco formulation in one embodiment contains tobacco raw material X and starch extracted from X, in another embodiment contains tobacco raw material X and starch extracted from tobacco raw material Y other than X, and in yet another embodiment contains tobacco raw material X, starch extracted from X, and starch extracted from tobacco raw material Y other than X.
- the above starch is present inside the cells of the tobacco raw material. Therefore, the extraction conditions are adjusted so that the starch can be released outside the cells.
- the extraction conditions are described below.
- the starch functions as a binder that bonds poorly water-soluble substances together. Therefore, among the tobacco varieties mentioned above, those that contain a large amount of starch are preferred.
- the tobacco raw material is preferably tobacco leaves that contain 0.1 to 20% by weight of starch, and more preferably tobacco leaves that contain 0.1 to 2% by weight of starch. Examples of such tobacco leaves include flue-cured and burley varieties.
- the former contain about 2 to 5% by weight of starch in the tobacco leaves.
- the latter contain about 0.1 to 0.5% by weight of starch in the tobacco leaves.
- the tobacco formulation can be made free of binders other than starch.
- "free of" a specific component means that the component is not added intentionally, and the component may be included as an impurity. Even if a binder other than starch is included as an impurity, the content of the binder other than starch in the tobacco formulation can be 2% by weight or less, 1% by weight or less, or 0.5% by weight or less.
- the type of starch is not particularly limited, but soluble starch, insoluble starch, or a mixture thereof can be used. Among these, it is preferable to use soluble starch, as its water solubility allows for uniform mixing.
- the lower limit of the content of starch in the tobacco formulation is not particularly limited, but is preferably 1% by weight or more, more preferably 2% by weight or more, and most preferably 2.5% by weight or more.
- the upper limit of the content of starch in the tobacco formulation is not particularly limited, but is preferably 50% by weight or less, more preferably 40% by weight or less, and most preferably 25% by weight or less.
- the upper limit of the content of starch in the tobacco formulation can be 20% by weight or less, 15% by weight or less, 10% by weight or less, 5% by weight or less, or 4% by weight or less.
- the upper and lower limits of the content of starch in the tobacco formulation can be arbitrarily combined. When the content of starch is 1% by weight or more, the strength of the tobacco sheet can be increased.
- the binder function is unlikely to be improved.
- the starch content in the tobacco formulation is within the numerical range between the above lower and upper limits, the amount of starch functioning as a binder is appropriate, and the structure of the resulting tobacco sheet can be maintained.
- the starch content in the tobacco formulation can be expressed as a value calculated based on the solid content excluding the medium.
- the starch content in the tobacco formulation can be measured according to the procedures and conditions described in "(4) Measurement of starch content” in the [Examples] below, and calculated as the ratio (wt%) of the weight of starch to the weight of the solid content of the tobacco formulation.
- the medium is preferably a liquid at room temperature (about 23° C.), and specific examples thereof include water or a water-soluble organic solvent.
- the water-soluble organic solvent include linear or branched alcohols having 1 to 3 carbon atoms, and ethers having 4 to 7 carbon atoms. These can be used alone or in combination as the medium.
- the medium is preferably water or a mixed solvent of water and a water-soluble organic solvent, and more preferably water.
- the content of the medium in the tobacco formulation is not particularly limited, but from the viewpoint of thermal energy efficiency during heating, it is preferably 20 to 80% by weight, more preferably 30 to 75% by weight, and most preferably 50 to 70% by weight.
- the content of the medium in the tobacco formulation can be calculated based on the dry weight method using an IR moisture measuring device.
- the tobacco formulation of the present invention can be produced, for example, as shown in Example 1 or Example 2 (Preparation of Tobacco Formulation and Tobacco Sheet) described below, by mixing tobacco raw materials with a medium to obtain a mixture, and then subjecting the mixture to a boiling treatment and extraction treatment to extract starch from the tobacco raw materials.
- the tobacco raw material can be used as a reinforcing material.
- the tobacco raw material is preferably tobacco leaves containing 4 to 15% by weight of cellulose, more preferably tobacco leaves containing 5 to 13% by weight of cellulose.
- Examples of such varieties include flue-cured and burley varieties.
- the former contain about 6 to 8% by weight of cellulose in the tobacco leaves, and the latter contain about 10 to 12% by weight of cellulose in the tobacco leaves.
- the poorly water-soluble substance may include the cellulose.
- the tobacco preparation of the present invention is useful as a tobacco material.
- starch When starch is derived from a tobacco raw material, it has a high affinity with a poorly water-soluble substance derived from the same tobacco raw material.
- a poorly water-soluble substance is formed by removing part or all of the starch from tobacco raw material X, so that the medium or other components can be retained in the part of the poorly water-soluble substance from which the starch has been removed. Therefore, it is considered that the affinity between the poorly water-soluble substance and starch is particularly high. Therefore, the poorly water-soluble substance derived from the tobacco raw material has a high affinity with starch, etc., and additives added separately, etc. For this reason, the tobacco preparation of the present invention can form, for example, a tobacco sheet with excellent strength.
- the tobacco sheet of the present invention is (1') a poorly water-soluble substance derived from a tobacco raw material; and (2') a starch extracted from the tobacco raw material or from other tobacco raw materials.
- the type, shape, primary particle size, and other configurations of the poorly water-soluble substance contained in the tobacco sheet are not particularly limited, but may be the same as the configurations described in "(1) Poorly Water-Soluble Substances Derived from Tobacco Raw Materials" in "1. Tobacco Preparations" above.
- the lower limit of the content of the poorly water-soluble substance in the tobacco sheet is not particularly limited, but from the viewpoint of functioning as a substrate, it is preferably 5% by weight or more, more preferably 10% by weight or more, most preferably 15% by weight or more, and can also be 20% by weight or more, 75% by weight or more, or 90% by weight or more.
- the upper limit of the content of the poorly water-soluble substance in the tobacco sheet is not particularly limited, but can be 95% by weight or less, 80% by weight or less, 70% by weight or less, 50% by weight or less, or 35% by weight or less.
- the upper and lower limits of the content of the poorly water-soluble substance in the tobacco sheet can be combined in any manner.
- a tobacco sheet can be formed by removing the medium from the tobacco formulation.
- the content (wt%) of the poorly water-soluble substance in the tobacco formulation can be considered to be equal to the content (wt%) of the poorly water-soluble substance in the tobacco sheet.
- the content of poorly water-soluble substances in a tobacco sheet can also be calculated based on the above-mentioned Prosky method.
- the tobacco raw material from which the poorly water-soluble substance is derived is not particularly limited, but can be the same as the tobacco raw material described in "(Tobacco raw materials)" in “1. Tobacco preparations" above.
- (2') Starch extracted from tobacco raw materials or other tobacco raw materials The types of starch and other components contained in the tobacco sheet are not particularly limited, but may be the same as the components described in "(2) Starch extracted from tobacco raw materials or other tobacco raw materials” in "1. Tobacco preparations" above.
- the lower limit of the starch content in the tobacco sheet is not particularly limited, but is preferably 1% by weight or more, more preferably 2% by weight or more, and most preferably 2.5% by weight or more.
- the upper limit of the starch content in the tobacco sheet is not particularly limited, but is preferably 50% by weight or less, more preferably 40% by weight or less, and most preferably 25% by weight or less.
- the upper limit of the starch content in the tobacco sheet can be 20% by weight or less, 15% by weight or less, 10% by weight or less, 5% by weight or less, or 4% by weight or less.
- the upper and lower limits of the starch content in the tobacco sheet can be arbitrarily combined. When the starch content is 1% by weight or more, the strength of the tobacco sheet can be increased.
- the starch content in the tobacco sheet is within the numerical range between the above-mentioned lower and upper limits, the amount of starch functioning as a binder is appropriate, and the structure of the obtained tobacco sheet can be maintained.
- a tobacco sheet can be formed by removing the medium from the tobacco formulation.
- the starch content (wt%) in the above-mentioned tobacco formulation (converted into solid content) can be considered to be equal to the starch content (wt%) in the tobacco sheet.
- the tobacco sheet may include a component derived from a tobacco raw material.
- the component derived from a tobacco raw material may include a poorly water-soluble substance derived from the tobacco raw material described above, and starch extracted from the tobacco raw material described above.
- the lower limit of the content of components derived from tobacco raw materials in the tobacco sheet is not particularly limited, but from the viewpoint of functioning as a base material, it is preferably 10% by weight or more, more preferably 15% by weight or more, most preferably 20% by weight or more, and can also be 75% by weight or more or 90% by weight or more.
- the upper limit of the content of components derived from tobacco raw materials in the tobacco sheet is not particularly limited, but can be 80% by weight or less, 70% by weight or less, or 50% by weight or less.
- the upper and lower limits of the content of components derived from tobacco raw materials in the tobacco sheet can be combined in any manner.
- the content of components derived from the tobacco raw materials in the tobacco sheet can be calculated as the ratio of the weight of the tobacco raw materials to the total weight of the tobacco raw materials used and the externally added components.
- the tobacco sheet may further include an aerosol generating agent.
- the aerosol generating agent may include, but is not limited to, glycerin, 1,2-propanediol, 1,3-propanediol, or a mixture of two or more thereof.
- the content of the aerosol generating agent in the tobacco sheet is not particularly limited, but from the viewpoint of the amount of smoke produced when smoking, it is preferably 10 to 50% by weight, more preferably 15 to 45% by weight, and most preferably 20 to 25% by weight.
- the tobacco sheet may further contain glucan, which is a type of binder described below.
- the glucan may include, but is not limited to, tamarind gum, guar gum, locust bean gum, gellan gum, pullulan, or a mixture of two or more of these.
- the glucan content in the tobacco sheet is not particularly limited, but from the viewpoint of moldability, it is preferably 0.1 to 5% by weight, more preferably 0.5 to 2% by weight, and most preferably 1.0 to 1.5% by weight.
- the tobacco sheet may contain a binder.
- the tobacco sheet by using starch that functions as a binder, the tobacco sheet can be free of binders other than starch. Even if the tobacco sheet contains the binder as an impurity, the content of binders other than starch in the tobacco sheet can be 3% by weight or less, 1% by weight or less, or 0.5% by weight or less.
- the tobacco sheet may be pulp-free. Even if the tobacco sheet contains pulp as an impurity, the pulp content in the tobacco sheet may be 3% by weight or less, 1% by weight or less, or 0.5% by weight or less.
- the form of the tobacco sheet of the present invention is not particularly limited, and a paper-formed sheet, a cast sheet, or the like can be adopted. From the viewpoint of providing a low-density sheet, a cast sheet is preferable. Details of the various types of tobacco sheets mentioned above are disclosed in "Encyclopedia of Tobacco, Tobacco Research Center, March 31, 2009."
- the tobacco sheet of the present invention can be, but is not limited to, a molded product of the tobacco formulation described in the above section "1. Tobacco formulation.”
- the tobacco formulation of the present invention is preferably produced by a method including a step of heating a tobacco raw material in a medium to extract the above-mentioned starch.
- the tobacco formulation may be one described in the above section "1. Tobacco formulation.”
- the starch in the tobacco formulation is contained within the cell walls of the tobacco raw material. Therefore, a certain degree of high temperature is required to release the starch from within the cells. From this perspective, the temperature during extraction is preferably 100 to 125°C, more preferably 105 to 120°C, and most preferably 110 to 119°C. Furthermore, at this temperature, the above-mentioned cellulose can also be efficiently released outside the cells.
- the average pressure during extraction is preferably 20 to 117 kPa, more preferably 50 to 110 kPa, and most preferably 85 to 95 kPa.
- the maximum pressure during extraction is preferably 70 to 117 kPa, more preferably 80 to 116.5 kPa, and most preferably 90 to 116.5 kPa.
- the extraction treatment time is preferably 20 to 90 minutes, more preferably 60 to 80 minutes, and most preferably 65 to 70 minutes. Furthermore, when the extraction treatment time is within the above numerical range, the above-mentioned cellulose can also be efficiently released outside the cells.
- the number of times of the extraction process can be 1 to 2 times, 3 to 4 times, or 5 to 10 times, and the more times the number of times, the more efficiently the starch can be released. Furthermore, when the number of times of the extraction process is within the above numerical range, the above-mentioned cellulose can also be efficiently released outside the cells.
- Atmosphere It is preferable to carry out the extraction of starch from tobacco raw materials in a closed system, since this can prevent a reduction in the flavor components contained in the tobacco raw materials.
- the surface area of the tobacco raw material to be extracted is large. Therefore, a step of grinding the tobacco raw material in advance may be provided, and the powdered tobacco raw material may be subjected to extraction. In this case, dry grinding is preferable. A known machine may be used for dry grinding.
- the particle size distribution of the powdered tobacco raw material is not limited, but it is preferable that it has a D90 of less than 500 ⁇ m, and more preferably a D90 of less than 100 ⁇ m.
- the lower limit of D90 is not limited, but is practically 5 ⁇ m or more.
- the tobacco raw material may be ground simultaneously with the extraction. That is, the extraction can be carried out while the tobacco raw material is wet-ground.
- the wet-grinding is preferably carried out in a closed system.
- the particle size distribution of the wet-ground tobacco raw material is as described above.
- the method for producing a tobacco formulation may further include a step of adding ingredients including an aerosol generating agent, a binder, or a combination thereof.
- the aerosol generating agent or binder may be those described in "(Other ingredients)" in "2. Tobacco Sheet” above.
- the manufacturing method of the tobacco formulation may not include a step of adding other poorly water-soluble substances, including pulp.
- the other poorly water-soluble substances are poorly water-soluble substances other than the poorly water-soluble substances derived from the tobacco raw materials described above.
- tobacco sheets can be formed without externally adding raw materials of other poorly water-soluble substances to the tobacco formulation.
- the method for producing the tobacco sheet of the present invention is not particularly limited, and any known method such as a papermaking method, a casting method, etc. Of these methods, the casting method is preferred from the viewpoint of uniformity of the obtained sheet.
- a method for producing a tobacco sheet of the present invention may comprise the steps of preparing a tobacco formulation by the method described above, and spreading and drying the tobacco formulation on a substrate.
- the method of producing a tobacco sheet does not need to include a step of pulverizing the tobacco formulation.
- ⁇ Tobacco sheet molding method (casting method)>
- An example of a method for forming a tobacco sheet by a casting method includes a method including the following steps. (1) A step of mixing ground aged tobacco with water, an optional pulp, and an optional binder to obtain a mixture (homogenization step). (2) The mixture is spread (cast) into a thin sheet and dried to form a tobacco sheet.
- a step may be added in which a slurry of water, pulp, binder, and crushed tobacco leaves is mixed with ultraviolet light or X-rays to remove some of the components such as nitrosamines.
- the shape of the tobacco sheet can be adjusted as appropriate, but in one embodiment, the thickness is 50 to 500 ⁇ m.
- the tobacco sheet can be chopped to produce shreds or strands.
- the tobacco sheet can also be pulverized to produce powder.
- the tobacco filler of the present invention comprises the tobacco sheet described above. Furthermore, the smoking article of the present invention includes the above tobacco filler. The smoking article of the present invention may be a non-combustion heating smoking article.
- smoking article means an inhalation article that allows the user to enjoy a flavor by inhaling.
- Smoking articles can be broadly divided into combustion-type smoking articles, such as conventional cigarettes, and non-combustion heat-type smoking articles.
- Examples of combustible smoking articles include cigarettes, pipes, pipes, cigars, and cigarillos.
- a non-combustion heated smoking article may be heated by a heating device separate from the article, or by a heating device integrated into the article.
- the non-combustion heated smoking article and the heating device are collectively referred to as a "non-combustion heated smoking system.”
- An example of a non-combustion heated smoking system is described below with reference to Figures 1 and 2.
- FIG. 1 is a schematic cross-sectional view showing an example of a non-combustion heat smoking system, showing the state before a heater 12 is inserted into the smoking segment 20A of a non-combustion heat smoking article 20. When in use, the heater 12 is inserted into the smoking segment 20A.
- FIG. 2 is a cross-sectional view of a non-combustion heat smoking article 20.
- the non-combustion heat smoking system includes a non-combustion heat smoking article 20 and a heating device 10 that heats the smoking segment 20A from the inside.
- the non-combustion heat smoking system is not limited to the configuration shown in FIG. 1.
- the heating device 10 shown in FIG. 1 includes a body 11 and a heater 12.
- the body 11 may include a battery unit and a control unit.
- the heater 12 may be an electric resistance heater, and is inserted into the smoking segment 20A to heat the smoking segment 20A.
- the smoking segment 20A is heated from the inside, but the embodiment of the non-combustion heating smoking article 20 is not limited to this, and in another embodiment, the smoking segment 20A is heated from the outside.
- the heating temperature by the heating device 10 is not particularly limited, but is preferably 400°C or less, more preferably 50 to 400°C, and even more preferably 150 to 350°C.
- the heating temperature refers to the temperature of the heater 12 of the heating device 10.
- the non-combustion heat smoking article 20 (hereinafter simply referred to as "smoking article 20") has a cylindrical shape.
- the circumferential length of the smoking article 20 is preferably 16 mm to 27 mm, more preferably 20 mm to 26 mm, and even more preferably 21 mm to 25 mm.
- the overall length (horizontal length) of the smoking article 20 is not particularly limited, but is preferably 40 mm to 90 mm, more preferably 50 mm to 75 mm, and even more preferably 50 mm to 60 mm.
- the smoking article 20 is composed of a smoking segment 20A, a filter portion 20C that forms the mouthpiece, and a connecting portion 20B that connects these.
- the smoking segment 20A is cylindrical, and its overall length (length in the axial direction) is, for example, preferably 5 to 100 mm, more preferably 10 to 50 mm, and even more preferably 10 to 25 mm.
- the cross-sectional shape of the smoking segment 20A is not particularly limited, but can be, for example, circular, elliptical, polygonal, etc.
- the smoking segment 20A has a smoking composition sheet or material derived therefrom 21 and a wrapper 22 wrapped around it.
- the filter section 20C has a cylindrical shape.
- the filter section 20C has a rod-shaped first segment 25 filled with cellulose acetate fiber and a rod-shaped second segment 26 similarly filled with cellulose acetate fiber.
- the first segment 25 is located on the smoking segment 20A side.
- the first segment 25 may have a hollow portion.
- the second segment 26 is located on the mouthpiece side.
- the second segment 26 is solid.
- the first segment 25 is composed of a first filling layer (cellulose acetate fiber) 25a and an inner plug wrapper 25b wrapped around the first filling layer 25a.
- the second segment 26 is composed of a second filling layer (cellulose acetate fiber) 26a and an inner plug wrapper 26b wrapped around the second filling layer 26a.
- the first segment 25 and the second segment 26 are connected by an outer plug wrapper 27.
- the outer plug wrapper 27 is adhered to the first segment 25 and the second segment 26 with a vinyl acetate emulsion adhesive or the like.
- the length of the filter portion 20C can be, for example, 10 to 30 mm
- the length of the connecting portion 20B can be, for example, 10 to 30 mm
- the length of the first segment 25 can be, for example, 5 to 15 mm
- the length of the second segment 26 can be, for example, 5 to 15 mm.
- the first segment 25 (center hole segment) is composed of a first filling layer 25a having one or more hollow portions, and an inner plug wrapper 25b that covers the first filling layer 25a.
- the first segment 25 has the function of increasing the strength of the second segment 26.
- the first filling layer 25a of the first segment 25 is densely packed with, for example, cellulose acetate fibers.
- a plasticizer containing triacetin is added to the cellulose acetate fibers in an amount of, for example, 6 to 20% by mass relative to the mass of the cellulose acetate, and the fibers are hardened.
- the hollow portion of the first segment 25 has an inner diameter of, for example, ⁇ 1.0 to ⁇ 5.0 mm.
- the first filling layer 25a of the first segment 25 may be constructed with, for example, a relatively high fiber packing density, or may be equivalent to the fiber packing density of the second filling layer 26a of the second segment 26 described below. Therefore, during inhalation, air and aerosol flow only through the hollow portion, and almost no air or aerosol flows through the first filling layer 25a. For example, if it is desired to reduce the loss of aerosol components due to filtration in the second segment 26, the length of the second segment 26 can be shortened and the first segment 25 can be lengthened accordingly.
- Replacing the shortened second segment 26 with the first segment 25 is effective in increasing the amount of aerosol components delivered. Because the first filling layer 25a of the first segment 25 is a fiber-filled layer, the feel from the outside during use does not cause discomfort to the user.
- the second segment 26 is composed of a second packed layer 26a and an inner plug wrapper 26b that covers the second packed layer 26a.
- the second segment 26 (filter segment) is packed with cellulose acetate fibers at a typical density and has typical filtering performance for filtering aerosol components.
- the filtering performance for filtering the aerosol (mainstream smoke) emitted from the smoking segment 20A may be different between the first segment 25 and the second segment 26. At least one of the first segment 25 and the second segment 26 may contain a flavoring.
- the structure of the filter portion 20C is arbitrary, and may be a structure having multiple segments as described above, or may be composed of a single segment.
- the filter portion 20C may also be composed of one segment. In this case, the filter portion 20C may be composed of either the first segment or the second segment.
- the connecting part 20B is cylindrical.
- the connecting part 20B has a cardboard tube 23 formed into a cylindrical shape, for example, from cardboard.
- the connecting part 20B may be filled with a cooling material for cooling the aerosol.
- An example of the cooling material is a sheet of a polymer such as polylactic acid, which can be folded and filled.
- a support part may be provided between the smoking segment 20A and the connecting part 20B to prevent the position of the smoking segment 20A from fluctuating.
- the support part may be made of a known material, such as a center hole filter like the first segment 25.
- the wrapper 28 is wrapped around the outside of the smoking segment 20A, the connecting portion 20B, and the filter portion 20C in a cylindrical shape, connecting them together.
- One side (inner surface) of the wrapper 28 is coated entirely or almost entirely with a vinyl acetate emulsion adhesive, except for the area near the ventilation hole portion 24.
- the multiple ventilation hole portions 24 are formed by laser processing from the outside after the smoking segment 20A, the connecting portion 20B, and the filter portion 20C are integrated by the wrapper 28.
- the ventilation hole section 24 has two or more through holes penetrating the connecting section 20B in the thickness direction.
- the two or more through holes are formed so as to be arranged radially when viewed from an extension of the central axis of the smoking article 20.
- the ventilation hole section 24 is provided in the connecting section 20B, but may be provided in the filter section 20C.
- the two or more through holes of the ventilation hole section 24 are arranged in one row at a fixed interval on one ring, but may be arranged in two rows at a fixed interval on two rings, or one or two rows of the ventilation hole section 24 may be arranged discontinuously or irregularly.
- Example 1 Preparation of tobacco formulations and tobacco sheets
- 1000 g of flue-cured tobacco was processed in a small grinder (High Speed Mill, manufactured by LabNect Co., Ltd.) to obtain a flue-cured tobacco coarsely ground product (hereinafter referred to as "tobacco sample”).
- tobacco sample a flue-cured tobacco coarsely ground product
- 300 g of the obtained tobacco sample and 1000 g of water were put into a switchable pressure cooker (Quick Eco, manufactured by Pearl Metal Co., Ltd.) and mixed, and the obtained mixture was then boiled under the following conditions.
- Pressure Maximum pressure 90 kPa, average pressure 80 kPa
- Temperature 119°C Time: 30 minutes
- the mixture after the second boiling treatment was cooled to 35°C, and the moisture content of the mixture was measured using an IR moisture meter (MB45, OHAUS) based on the IR moisture measurement method, which was 80% by weight.
- guar gum After measuring the moisture content in the pressure cooker, 15 g of guar gum, 6 g of CMC (carboxymethylcellulose), and 43.5 g of glycerin were added and mixed to obtain a mixed liquid. 800 g of the resulting mixed liquid was sampled, and while adding 800 g of water, it was treated with a defibrator (high-speed dispersion high shear mixer, manufactured by Silverson) to carry out wet pulverization and extraction processing.
- the wet pulverization conditions were as follows. Rotational speed: 7000 rpm Time: 10 minutes * Slowly add 800g of water to the above mixture over a period of 10 minutes.
- the above wet grinding and extraction process produced a suspension (tobacco preparation) containing poorly water-soluble substances derived from flue-cured tobacco, starch extracted from flue-cured tobacco, and water as a medium.
- the suspension obtained as described above was spread on a stainless steel plate and naturally dried at room temperature to produce a slurry sheet (tobacco sheet) (thickness: 1 mm).
- the content of components derived from the tobacco raw materials in the tobacco sheet of Example 1 was calculated as the percentage of the weight of the tobacco raw materials to the total weight of the tobacco raw materials used (tobacco sample) and the externally added components (guar gum, CMC, and glycerin), and was found to be 82.3% by weight.
- Example 2 (Preparation of tobacco formulations and tobacco sheets) 300 g of the tobacco sample described in [Example 1] above and 1000 g of water were mixed in a pressure cooker (Quick Eco, manufactured by Pearl Metal Co., Ltd.), and the resulting mixture was boiled under the following conditions. The boiling process was repeated twice. Pressure: Maximum pressure 90 kPa, average pressure 80 kPa Temperature: 119°C Time: 30 minutes
- the mixture after the third boiling treatment was cooled to 25°C, and the moisture content of the mixture was measured using an IR moisture meter (MB45, OHAUS) based on the IR moisture measurement method, which was 80% by weight.
- guar gum After measuring the moisture content in the pressure cooker, 15 g of guar gum, 6 g of CMC (carboxymethylcellulose), and 43.5 g of glycerin were added and mixed to obtain a mixed liquid. 800 g of the resulting mixed liquid was sampled, and while adding 800 g of water, it was treated with a defibrator (high-speed dispersion high shear mixer, manufactured by Silverson) to carry out wet grinding and extraction processing. The wet grinding conditions were as follows. Rotational speed: 4500 rpm Time: 20 minutes * Slowly add 800g of water to the above mixture over a period of 20 minutes.
- defibrator high-speed dispersion high shear mixer, manufactured by Silverson
- the above wet grinding and extraction process produced a suspension (tobacco preparation) containing poorly water-soluble substances derived from flue-cured tobacco, starch extracted from flue-cured tobacco, and water as a medium.
- the suspension obtained as described above was spread on a stainless steel plate and naturally dried at room temperature to produce a slurry sheet (tobacco sheet) (thickness: 1 mm).
- the content of components derived from the tobacco raw materials in the tobacco sheet of Example 2 was calculated as the ratio of the weight of the tobacco raw materials to the total weight of the tobacco raw materials used (tobacco sample) and the externally added components (guar gum, CMC, and glycerin), and was found to be 82.3% by weight.
- the obtained suspension was spread on a stainless steel plate and naturally dried at room temperature to produce a slurry sheet (tobacco sheet) (thickness: 1 mm).
- the content of components derived from the tobacco raw materials in the tobacco sheet of the comparative example was calculated as the percentage of the weight of the tobacco raw materials to the total weight of the tobacco raw materials used (tobacco sample) and the externally added components (glycerin, pulp, and guar gum), and was found to be 86.9% by weight.
- the mixture was centrifuged at 5530 G for 5 minutes using a centrifuge (refrigerated centrifuge, manufactured by KUBOTA Corporation), and the supernatant was removed to obtain 0.5 g of precipitate.
- a centrifuge refrigerated centrifuge, manufactured by KUBOTA Corporation
- 40 ml of water was added, and the mixture was heated at 80° C. for 30 minutes to obtain a mixture.
- the mixture was centrifuged at 5530 G for 5 minutes using a centrifuge (refrigerated centrifuge, manufactured by KUBOTA) and the supernatant was removed to obtain 0.4 g of precipitate.
- the steps of adding water, heating and mixing, centrifugation, and removing the supernatant were repeated twice more in the same manner as above to obtain 0.3 g of precipitate.
- the content (wt %) of the poorly water-soluble substance in the suspension obtained as described above (converted into solids content) can be regarded as equal to the content (wt %) of the poorly water-soluble substance in the slurry sheet.
- 100 mg of the obtained powdery product was weighed and placed in a 15 ml centrifuge tube (SUMILON (registered trademark), manufactured by Sumitomo Bakelite Co., Ltd.), and 10 ml of MilliQ water at room temperature was added, and then ultrasonic waves were applied for 10 minutes at room temperature using an ultrasonic device (BRANSONIC, manufactured by Emerson Japan Co., Ltd.) to perform extraction processing, and a mixed liquid was obtained.
- the obtained mixed liquid was centrifuged for 5 minutes at 4 ° C. and 8000 rpm using a centrifuge (cooled centrifuge, manufactured by KUBOTA Co., Ltd.). After centrifugation, the supernatant was removed to obtain a precipitate.
- the precipitate was mixed with 7 ml of dimethyl sulfoxide (DMSO) and stirred with a vortex mixer to obtain a suspension.
- DMSO dimethyl sulfoxide
- the resulting suspension was heated (extracted) at 100°C for 5 minutes to dissolve the starch in the precipitate into DMSO.
- the suspension after the extraction was quenched with ice water, and then centrifuged at 3000G for 5 minutes using the above-mentioned centrifuge. After centrifugation, 5 ml of the supernatant was collected and placed in a 50 ml measuring flask.
- the supernatant in the measuring flask was then subjected to the same process as above, including extraction at 100°C for 5 minutes, quenching with ice water, centrifugation at 3000G for 5 minutes, and collection and introduction of 5 ml of the supernatant into a 50 ml measuring flask, which were repeated three times to obtain DMSO in which starch was dissolved (in a measuring flask). MilliQ water was added to the obtained DMSO: 20 ml, and the mixture was made up to 100 ml and stirred, and then 100 ml of the obtained sample was transferred to a glass test tube.
- the glucose concentrations were 0 ⁇ g/ml, 10 ⁇ g/ml, 20 ⁇ g/ml, 50 ⁇ g/ml, and 100 ⁇ g/ml, respectively. Based on the obtained absorbance measurements and the calibration curve, the ratio (wt%) of the weight of starch to the weight (1 g) of the solid content of the suspension used was calculated, and this was taken as the starch content (wt%). The results are shown in Table 1. Since the slurry sheet is formed by removing only the water medium from the suspension, the starch content (wt %) (solid content equivalent) in the suspension obtained as described above can be considered to be equal to the starch content (wt %) in the slurry sheet.
- the tobacco formulations of Examples 1 and 2 can be used to produce tobacco sheets without adding other poorly water-soluble raw materials such as pulp.
- poorly water-soluble raw materials such as pulp.
- starch contained in the tobacco raw materials is extracted by boiling treatment, and poorly water-soluble substances are obtained as residues of the tobacco raw materials.
- the poorly water-soluble substances derived from the tobacco raw materials obtained in this manner improve the moldability and strength of the tobacco sheet in place of other poorly water-soluble substances, so that the tobacco sheet can be formed without adding other poorly water-soluble substances.
- the tobacco formulations of Examples 1 and 2 do not require the external addition of other poorly water-soluble raw materials such as pulp, it is possible to increase the amount of tobacco raw materials and glycerin added, which increases the freedom of design of the tobacco formulation and tobacco sheet.
- the particle size ( ⁇ m) of the poorly water-soluble substance was measured to be 22.4 ⁇ m for the suspension in Example 1 and 24.2 ⁇ m for the slurry sheet, indicating that the particle size was extremely small after the grinding and extraction process.
- the particle size of the poorly water-soluble substance was thus small, which is believed to increase the surface area that bonds tobacco particles together and improve the strength of the slurry sheet.
- the tobacco formulation of the comparative example has pulp, a poorly water-soluble substance, added to it in order to produce a tobacco sheet. If pulp were not added to the tobacco formulation of the comparative example, the sheet shape would not be able to be maintained, and tobacco sheet would not be able to be produced.
- the particle size of the poorly water-soluble substance derived from the tobacco raw materials is large because the product does not go through the crushing and extraction process. As a result, the surface area for bonding the tobacco particles together is insufficient, and pulp must be added to improve the strength of the slurry sheet.
- the results in Table 1 also show that the content of poorly water-soluble substances in the suspension of Example 2 (12% by weight) is lower than the content of poorly water-soluble substances in the suspension of Example 1 (30% by weight).
- the boiling treatment was performed more times in Example 2 than in Example 1, more components such as starch could be extracted from the tobacco raw material, and as a result, the amount measured as poorly water-soluble substances decreased accordingly.
- the results of Examples 1 and 2 show that the amount of extracted components such as starch can be controlled by changing the conditions of the boiling treatment.
- the starch content in the suspension of Example 1 was 3.04% by weight, which is higher than the starch content in the suspension of the Comparative Example, which was 2.47% by weight. This is thought to be because, compared to the suspension of the Comparative Example, which was not subjected to a boiling treatment, the suspension of Example 1 was subjected to a boiling treatment, and therefore more starch was extracted from the tobacco raw material and released into the suspension.
- the suspension contains a large amount of starch, as in Example 1, the starch functions as a binder that bonds poorly water-soluble substances together, making it possible to produce a tobacco sheet with greater strength.
- the tobacco formulation of the present invention uses tobacco raw materials and can produce tobacco sheets without the external addition of other poorly water-soluble substance raw materials.
- heating device 11 body 12 heater 20 Non-combustion heating smoking article 20A Smoking segment 20B Connecting part 20C Filter part 21 Smoking composition sheet or material derived therefrom 22 Wrapper 23 Paper tube 24 Ventilation hole portion 25 First segment 25a First filling layer 25b Inner plug wrapper 26 Second segment 26a Second filling layer 26b Inner plug wrapper 27 Outer plug wrapper 28 Wrapper
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Abstract
Description
本発明は、たばこ製剤、たばこシート、たばこ充填物、喫煙物品、たばこ製剤の製造方法、及びたばこシートの製造方法に関する。 The present invention relates to tobacco preparations, tobacco sheets, tobacco fillers, smoking articles, methods for producing tobacco preparations, and methods for producing tobacco sheets.
模造たばこは、葉たばこを原料として人工的に紙状に成形したたばこ材料であり、たばこシートとも呼ばれる。当該たばこシートの製造方法としては、例えば、抄造(製紙)プロセスにより製造する方法、スラリー(キャスト)プロセスにより製造する方法、圧延(口ール)プロセスにより製造する方法、押出成形プロセスにより製造する方法等が知られている。 Imitation tobacco is a tobacco material made by artificially forming tobacco leaves into a paper-like form, and is also called tobacco sheet. Known methods for manufacturing such tobacco sheets include, for example, a papermaking process, a slurry (cast) process, a rolling (rolling) process, and an extrusion molding process.
所定の強度のたばこシートを得るために、原料となるたばこの粒径を所定の範囲内とすることが知られている。例えば、特許文献1においては、たばこの粒径サイズが小さいほど、たばこの粒子同士を接着する表面積が増加してたばこシートの強度を向上できること、特に60メッシュ~400メッシュ(56μm~375μm)にすることで均一なシートを作成できることが開示されている。また、特許文献2や特許文献3においては、たばこの粒径が150μm以上であると均一化した場合のたばこウェブの強度が低下するため、30~120μmのたばこ粉体を使用することが記載されている。さらに、ナノサイズにまでたばこの粒径を細かくしてシートの原料として使用する技術もある(特許文献4及び5並びに非特許文献1)。 It is known that in order to obtain a tobacco sheet with a specified strength, the particle size of the tobacco raw material is set within a specified range. For example, Patent Document 1 discloses that the smaller the particle size of the tobacco, the greater the surface area that bonds the tobacco particles together, improving the strength of the tobacco sheet, and that a uniform sheet can be created by using a particle size of 60 mesh to 400 mesh (56 μm to 375 μm). Patent Documents 2 and 3 also disclose that tobacco powder with a particle size of 30 to 120 μm is used, because the strength of the tobacco web decreases when the particle size of the tobacco is 150 μm or more when homogenized. Furthermore, there is also technology for reducing the particle size of tobacco to nano size and using it as a raw material for the sheet (Patent Documents 4 and 5, and Non-Patent Document 1).
また、たばこシートの成形性や強度を向上させるために、たばこ以外の植物繊維などの難水溶性物質を添加することも多い。特許文献6では、シート成形前の混合工程において、粒径30μm~120μmのたばこ原料へ200μm~4000μmのセルロース材料を添加して混合しており、このような混合物中で上記2種類の異なる粒径の物質が絡み合い、シートとしての構造を安定的に保持することができる。 Furthermore, in order to improve the moldability and strength of tobacco sheets, water-insoluble substances such as plant fibers other than tobacco are often added. In Patent Document 6, in the mixing process before sheet molding, a cellulose material with a particle size of 200 μm to 4000 μm is added and mixed with tobacco raw material with a particle size of 30 μm to 120 μm, and in this mixture, the above two types of substances with different particle sizes become entangled, allowing the sheet structure to be stably maintained.
さらに、加熱式タバコ(非燃焼加熱喫煙物品)に使用するためのたばこシートの需要も高まっている。加熱式タバコ用たばこシートの製造においては、たばこ原料、エアロゾル形成剤、バインダーなどを混合した上でたばこシートに成形する。このようなたばこシートの製造において、シートの成形性や強度を向上させるために、難水溶性のセルロースパルプを添加する(特許文献7)、たばこ粒子の粒径を規定する(特許文献8)などの工夫がなされている。また、当該たばこシートの製造において、加熱時の熱伝導性を向上させるために難水溶性の金属類や炭酸カルシウムを添加することも行われている(特許文献9及び10)。 Furthermore, the demand for tobacco sheets for use in heated tobacco products (non-combustion heated smoking articles) is also increasing. In the manufacture of tobacco sheets for heated tobacco products, tobacco raw materials, aerosol forming agents, binders, etc. are mixed and then molded into a tobacco sheet. In the manufacture of such tobacco sheets, ingenuity has been employed to improve the moldability and strength of the sheets, such as adding water-insoluble cellulose pulp (Patent Document 7) and specifying the particle size of tobacco particles (Patent Document 8). In addition, in the manufacture of such tobacco sheets, water-insoluble metals and calcium carbonate have also been added to improve thermal conductivity during heating (Patent Documents 9 and 10).
特許文献6及び7に開示されているように、たばこ原料にたばこ以外の植物繊維などの難水溶性物質を添加する場合、当該難水溶性物質を準備する分だけ余分にコストがかかり、また、当該難水溶性物質を配合する工程の分だけ作業の時間及び労力が余分にかかってしまう。
かかる事情に鑑み、本願の発明者らが鋭意検討を行った結果、植物としてのたばこ原料を使用して、ファイバー素材などの難水溶性物質の原料を外添しないでも、粒径に依存しないたばこシートが作成可能であることを見出した。本発明は、たばこ原料を使用し、他の難水溶性物質の原料を外添しないでもたばこシートが形成可能なたばこ製剤、及び当該たばこシートを提供することを課題とする。
As disclosed in Patent Documents 6 and 7, when a poorly water-soluble substance such as plant fibers other than tobacco is added to tobacco raw materials, extra costs are incurred for preparing the poorly water-soluble substance, and the process of blending the poorly water-soluble substance requires extra work time and effort.
In view of the above circumstances, the inventors of the present application conducted intensive research and found that it is possible to prepare a tobacco sheet that is not dependent on particle size by using tobacco raw materials as plants, without externally adding raw materials of poorly water-soluble substances such as fiber materials. An object of the present invention is to provide a tobacco preparation that uses tobacco raw materials and is capable of forming a tobacco sheet without externally adding raw materials of poorly water-soluble substances, and said tobacco sheet.
前記課題は以下の本発明によって解決される。
[1]
(1)たばこ原料に由来する難水溶性物質、
(2)前記たばこ原料又は他のたばこ原料から抽出されたデンプン、及び
(3)媒体
を含むたばこ製剤。
[2]
(1’)たばこ原料に由来する難水溶性物質、及び
(2’)前記たばこ原料又は他のたばこ原料から抽出されたデンプン
を含むたばこシート。
[3] 前記デンプンが、前記たばこ原料から抽出されたデンプンである、[2]に記載のたばこシート。
[4] 前記デンプンが可溶性デンプンである、[2]又は[3]に記載のたばこシート。
[5] 前記難水溶性物質の一次粒子径が100μm以下である、[2]~[4]のいずれか1つに記載のたばこシート。
[6] 前記たばこシート中の前記デンプンの含有量が10重量%以下である、[2]~[5]のいずれか1つに記載のたばこシート。
[7] 前記難水溶性物質の由来となる前記たばこ原料が葉たばこを含む、[2]~[6]のいずれか1つに記載のたばこシート。
[8] 前記難水溶性物質の由来となる前記たばこ原料がアルカロイドを含む、[2]~[7]のいずれか1つに記載のたばこシート。
[9] エアロゾル発生剤を更に含む、[2]~[8]のいずれか1つに記載のたばこシート。
[10] 前記エアロゾル発生剤が、グリセリン、1,2-プロパンジオール、1,3-プロパンジオール、又はこれらの混合物を含む、[9]に記載のたばこシート。
[11] グルカンを更に含む、[2]~[10]のいずれか1つに記載のたばこシート。
[12] 前記グルカンが、タマリンドガム、グアーガム、ローカストビーンガム、ジェランガム、プルラン、又はこれらの混合物を含む、[11]に記載のたばこシート。
[13] パルプを含まない、[2]~[12]のいずれか1つに記載のたばこシート。
[14] キャストシートである、[2]~[13]のいずれか1つに記載のたばこシート。
[15] [1]に記載のたばこ製剤の成形体である、[2~[14]のいずれか1つに記載のたばこシート。
[16] [2]~[15]のいずれか1つに記載のたばこシートを含むたばこ充填物。
[17] [16]に記載のたばこ充填物を含む喫煙物品。
[18] 非燃焼加熱喫煙物品である、[17]に記載の喫煙物品。
[19] 前記たばこ原料を前記媒体中で加熱して、前記デンプンを抽出する工程を備える、[1]に記載のたばこ製剤の製造方法。
[20]
[19]に記載の方法で前記たばこ製剤を調製する工程、及び
前記たばこ製剤を基材の上に展開し、そして乾燥させる工程を備える、[2]~[15]のいずれか1つに記載のたばこシートの製造方法。
The above problems are solved by the present invention described below.
[1]
(1) Poorly water-soluble substances derived from tobacco raw materials,
(2) a starch extracted from said tobacco material or from other tobacco materials; and (3) a vehicle.
[2]
A tobacco sheet comprising: (1') a poorly water-soluble substance derived from a tobacco raw material; and (2') a starch extracted from the tobacco raw material or another tobacco raw material.
[3] The tobacco sheet according to [2], wherein the starch is a starch extracted from the tobacco raw material.
[4] The tobacco sheet according to [2] or [3], wherein the starch is a soluble starch.
[5] The tobacco sheet according to any one of [2] to [4], wherein the primary particle size of the poorly water-soluble substance is 100 μm or less.
[6] The tobacco sheet according to any one of [2] to [5], wherein the starch content in the tobacco sheet is 10% by weight or less.
[7] The tobacco sheet according to any one of [2] to [6], wherein the tobacco raw material from which the poorly water-soluble substance is derived contains tobacco leaves.
[8] The tobacco sheet according to any one of [2] to [7], wherein the tobacco raw material from which the poorly water-soluble substance is derived contains an alkaloid.
[9] The tobacco sheet according to any one of [2] to [8], further comprising an aerosol generating agent.
[10] The tobacco sheet according to [9], wherein the aerosol generating agent comprises glycerin, 1,2-propanediol, 1,3-propanediol, or a mixture thereof.
[11] The tobacco sheet according to any one of [2] to [10], further comprising glucan.
[12] The tobacco sheet according to [11], wherein the glucan comprises tamarind gum, guar gum, locust bean gum, gellan gum, pullulan, or a mixture thereof.
[13] The tobacco sheet according to any one of [2] to [12], which does not contain pulp.
[14] The tobacco sheet according to any one of [2] to [13], which is a cast sheet.
[15] The tobacco sheet according to any one of [2 to [14], which is a molded product of the tobacco formulation according to [1].
[16] A tobacco filler comprising the tobacco sheet according to any one of [2] to [15].
[17] A smoking article comprising the tobacco filler described in [16].
[18] The smoking article according to [17], which is a non-combustion heating smoking article.
[19] A method for producing a tobacco formulation according to [1], comprising a step of heating the tobacco raw material in the medium to extract the starch.
[20]
A method for producing a tobacco sheet according to any one of [2] to [15], comprising: preparing the tobacco formulation by the method according to [19]; and spreading the tobacco formulation on a substrate and drying it.
本発明によって、たばこ原料を使用し、他の難水溶性物質の原料を外添しないでもたばこシートが形成可能なたばこ製剤、及び当該たばこシートを提供できる。 The present invention provides a tobacco preparation that uses tobacco raw materials and can be used to form a tobacco sheet without the external addition of other poorly water-soluble substance raw materials, and the tobacco sheet.
以下、本発明を詳細に説明する。本発明において「X~Y」はその端値であるX及びYを含む。 The present invention will be described in detail below. In this invention, "X to Y" includes the end values X and Y.
1.たばこ製剤
本発明のたばこ製剤は、
(1)たばこ原料に由来する難水溶性物質、
(2)前記たばこ原料又は他のたばこ原料から抽出されたデンプン、及び
(3)媒体
を含む。
1. Tobacco formulation The tobacco formulation of the present invention comprises:
(1) Poorly water-soluble substances derived from tobacco raw materials,
(2) a starch extracted from said tobacco material or from another tobacco material; and (3) a vehicle.
(1)たばこ原料に由来する難水溶性物質
本発明の難水溶性物質は、たばこ原料に由来する。本願において、難水溶性物質は、85℃において水に対する溶解度が20μg/mL未満である物質を意味し、たばこ原料に対して煮沸処理及び抽出処理を行った後の残渣として得ることができる。難水溶性物質は、例えば、後述の[実施例1]又は[実施例2]の(たばこ製剤及びたばこシートの調製)に示すように、たばこ原料に対して特定の条件下で煮沸処理及び抽出処理を行い、たばこ原料からデンプンを抽出することにより、たばこ原料の残渣として得ることができる。
難水溶性物質がたばこ原料に由来するか否かは、例えば、難水溶性物質のアイソトープ分性を行い13C/12Cの比を測定することにより判別することが可能である。
難水溶性物質は、難水溶性繊維を含むことができ、又は難水溶性繊維からなることができる。
(1) Poorly Water-Soluble Substances Derived from Tobacco Raw Materials The poorly water-soluble substance of the present invention is derived from tobacco raw materials. In this application, the poorly water-soluble substance refers to a substance that has a solubility in water of less than 20 μg/mL at 85° C., and can be obtained as a residue after subjecting tobacco raw materials to boiling and extraction treatments. The poorly water-soluble substance can be obtained as a residue of tobacco raw materials by subjecting tobacco raw materials to boiling and extraction treatments under specific conditions and extracting starch from the tobacco raw materials, for example, as shown in [Example 1] or [Example 2] (Preparation of tobacco formulation and tobacco sheet) described below.
Whether or not a poorly water-soluble substance is derived from a tobacco raw material can be determined, for example, by performing isotope analysis of the poorly water-soluble substance and measuring the 13C/12C ratio.
The poorly water soluble material may comprise or consist of poorly water soluble fibres.
たばこ製剤における難水溶性物質の形状は限定されないが、粒状であることが好ましい。
難水溶性物質の一次粒子径(D90)の下限は、特に限定されないが、シート構造を維持する観点より、20μm以上が好ましく、50μm以上がより好ましく、100μm以上が最も好ましい。難水溶性物質の一次粒子径(D90)の下限は、5μm以上又は10μm以上とすることもできる。難水溶性物質の一次粒子径(D90)の上限は、特に限定されないが、シート構造の均一性の観点より、500μm以下が好ましく、250μm以下がより好ましく、100μm以下が最も好ましい。難水溶性物質の一次粒子径(D90)の上限は、80μm以下、50μm以下、又は30μm以下とすることもできる。上述の難水溶性物質の一次粒子径の上限及び下限は、任意に組み合わせることができる。難水溶性物質の一次粒子径(D90)は、後述の[実施例]の「(1)難水溶性物質の粒子径の測定」に記載の手順及び条件に沿って測定を行うことができる。
難水溶性物質の一次粒子径を小さくすることにより、たばこの粒子同士を接着する表面積が増加し、たばこシートの強度を向上できる。
The shape of the poorly water-soluble substance in the tobacco formulation is not limited, but it is preferably in the form of particles.
The lower limit of the primary particle diameter (D90) of the poorly water-soluble substance is not particularly limited, but from the viewpoint of maintaining the sheet structure, it is preferably 20 μm or more, more preferably 50 μm or more, and most preferably 100 μm or more. The lower limit of the primary particle diameter (D90) of the poorly water-soluble substance can be 5 μm or more or 10 μm or more. The upper limit of the primary particle diameter (D90) of the poorly water-soluble substance is not particularly limited, but from the viewpoint of uniformity of the sheet structure, it is preferably 500 μm or less, more preferably 250 μm or less, and most preferably 100 μm or less. The upper limit of the primary particle diameter (D90) of the poorly water-soluble substance can also be 80 μm or less, 50 μm or less, or 30 μm or less. The upper and lower limits of the primary particle diameter of the poorly water-soluble substance described above can be arbitrarily combined. The primary particle diameter (D90) of the poorly water-soluble substance can be measured according to the procedure and conditions described in "(1) Measurement of particle diameter of poorly water-soluble substance" in [Examples] described later.
By reducing the primary particle size of the poorly water-soluble substance, the surface area for bonding tobacco particles together increases, and the strength of the tobacco sheet can be improved.
たばこ製剤中の難水溶性物質の含有量の下限は、特に限定されないが、基材として機能させる観点より、5重量%以上が好ましく、10重量%以上がより好ましく、15重量%以上が最も好ましく、また、20重量%以上、75重量%以上、又は90重量%以上とすることもできる。たばこ製剤中の難水溶性物質の含有量の上限は、特に限定されないが、95重量%以下、80重量%以下、70重量%以下、50重量%以下、又は35重量%以下とすることができる。たばこ製剤中の難水溶性物質の含有量の上限及び下限は、任意に組み合わせることができる。
たばこ製剤中の難水溶性物質の含有量は、媒体を除いた固形分換算の値とすることができる。たばこ製剤中の難水溶性物質の含有量は、後述の[実施例]の「(3)難水溶性物質の含有量の測定」に記載の手順及び条件に沿って測定を行い、たばこの製剤の固形分重量に対する、得られた乾燥物の重量の割合(重量%)として算出することができる。
The lower limit of the content of the poorly water-soluble substance in the tobacco formulation is not particularly limited, but from the viewpoint of functioning as a base material, it is preferably 5% by weight or more, more preferably 10% by weight or more, most preferably 15% by weight or more, and can also be 20% by weight or more, 75% by weight or more, or 90% by weight or more. The upper limit of the content of the poorly water-soluble substance in the tobacco formulation is not particularly limited, but can be 95% by weight or less, 80% by weight or less, 70% by weight or less, 50% by weight or less, or 35% by weight or less. The upper and lower limits of the content of the poorly water-soluble substance in the tobacco formulation can be combined in any manner.
The content of the poorly water-soluble substance in the tobacco formulation can be expressed as a value calculated based on the solid content excluding the medium. The content of the poorly water-soluble substance in the tobacco formulation can be measured according to the procedures and conditions described in "(3) Measurement of the content of poorly water-soluble substance" in [Examples] below, and calculated as the ratio (wt%) of the weight of the obtained dry matter to the weight of the solid content of the tobacco formulation.
たばこ製剤中の難水溶性物質の含有量は、プロスキー法によって算出することもできる。すなわち、たばこ製剤の試料を採取後、熱安定α-アミラーゼによって、当該試料に含まれるデンプンをブドウ糖が少量つながった状態にまでランダムに分解する。次に、プロテアーゼによって、当該試料に含まれるたんぱく質のペプチド結合を分解する。最後に、アミログルコシダーゼによって、熱安定α-アミラーゼによって分解された糖鎖をブドウ糖1分子にまで分解する。その後、当該試料にエタノールを加えて沈殿を生成させた後、吸引ろ過を行い沈殿物を回収し、得られた沈殿物をエタノール及びアセトンで洗浄する。エタノール及びアセトンで洗浄することで、酵素分解されなかった沈殿物中の脂質を洗い流す。洗浄後の沈殿物は、一晩乾燥して乾燥重量を測定する。一方、上記の吸引ろ過により得られるろ過残渣中には、分解されずに残った試料由来のたんぱく質や酵素由来のたんぱく質、無機物(灰分)が含まれる。このため、別途、たんぱく質と灰分を定量して、上記の乾燥重量から差し引くことで難水溶性物質の量が算出される。
なお、上記のたんぱく質はBSA assay法により、算出され、これは主に2段階の反応に基づいている。第1段階では、たんぱく質溶液中のペプチド結合によって、キットに含まれる二価銅イオン(Cu2+)が一価銅イオン(Cu+)に還元される。還元されるCu2+の量は、溶液に含まれるたんぱく質の量に比例する。第2段階では、2分子のbicinchoninic acid(BCA)がCu+に配位して、562 nmに強い吸収を示す青紫色の錯体を形成する。これを分光光度計で測定して比色定量することでたんぱく質量を算出する。灰分は一定量を550~600℃の温度で灰化した重量から算出される。
The content of poorly water-soluble substances in tobacco preparations can also be calculated by the Prosky method. That is, after taking a sample of the tobacco preparation, the starch contained in the sample is randomly decomposed by heat-stable α-amylase until a small amount of glucose is linked to it. Next, the peptide bonds of the proteins contained in the sample are decomposed by protease. Finally, the sugar chains decomposed by heat-stable α-amylase are decomposed into one glucose molecule by amyloglucosidase. Then, ethanol is added to the sample to generate a precipitate, and the precipitate is collected by suction filtration and washed with ethanol and acetone. By washing with ethanol and acetone, lipids in the precipitate that were not enzymatically decomposed are washed away. The washed precipitate is dried overnight and the dry weight is measured. Meanwhile, the filtration residue obtained by the above suction filtration contains the protein derived from the sample that was not decomposed, the protein derived from the enzyme, and inorganic matter (ash). Therefore, the amount of poorly water-soluble substances is calculated by separately quantifying the protein and ash and subtracting them from the above dry weight.
The above protein content is calculated by the BSA assay method, which is based on a two-step reaction. In the first step, the divalent copper ions (Cu 2+ ) contained in the kit are reduced to monovalent copper ions (Cu + ) by peptide bonds in the protein solution. The amount of Cu 2+ reduced is proportional to the amount of protein in the solution. In the second step, two molecules of bicinchoninic acid (BCA) coordinate with Cu + to form a blue-purple complex that has strong absorption at 562 nm. This is measured with a spectrophotometer and colorimetrically quantified to calculate the protein mass. The ash content is calculated from the weight of a certain amount of the protein incinerated at a temperature of 550-600°C.
(たばこ原料)
上述のたばこ原料とは、タバコ属植物由来の原料であり、例えば、たばこ葉、熟成済みたばこ葉、たばこ刻、たばこ粉末、中骨や残幹等の葉以外の部位等のたばこ原料、およびたばこ原料を処理に供して得た処理物または排出物が挙げられる。たばこ葉とは、収穫されたたばこの葉が、熟成を経る前のものの総称である。熟成の一態様にはキュアリングが含まれる。たばこ刻は、熟成済たばこ葉等が、所定の大きさに刻まれたものである。たばこ粉末はたばこ葉等を粉砕したものである。
(Tobacco raw materials)
The tobacco raw materials mentioned above are raw materials derived from Nicotiana plants, and examples thereof include tobacco raw materials such as tobacco leaves, aged tobacco leaves, tobacco shreds, tobacco powder, parts other than leaves such as midribs and stems, and processed products or waste products obtained by subjecting tobacco raw materials to processing. Tobacco leaves are a general term for harvested tobacco leaves before they are aged. One form of aging includes curing. Tobacco shreds are aged tobacco leaves, etc. that have been chopped into a specified size. Tobacco powder is pulverized tobacco leaves, etc.
たばこ原料におけるたばこの品種としては、種々のものを用いることができる。例えば、タバコの品種として、黄色種、バーレー種、オリエント種、在来種、その他のニコチアナ-タバカム系品種、ニコチアナ-ルスチカ系品種を挙げることができる。これらの品種は、単独で用いることもできるが、目的とする香味を得るために、たばこ葉の収穫から、熟成済たばこ葉を非燃焼加熱式たばこ製品で利用される種々の形態(すなわち、加工済たばこ葉)とするまでの過程でブレンドして用いることもできる。前記たばこの品種の詳細は、「たばこの事典、たばこ総合研究センター、2009.3.31」に開示されている。 Various tobacco varieties can be used as the tobacco raw material. For example, examples of tobacco varieties include flue-cured, burley, orient, native, other Nicotiana tabacum varieties, and Nicotiana rustica varieties. These varieties can be used alone, but in order to obtain the desired flavor, they can also be blended during the process from tobacco leaf harvest to the processing of aged tobacco leaves into various forms (i.e., processed tobacco leaves) used in non-combustion heated tobacco products. Details of the tobacco varieties are disclosed in "Encyclopedia of Tobacco, Tobacco Research Center, March 31, 2009."
難水溶性物質の由来となるたばこ原料は、嗜好性品質の観点より、アルカロイドを含むことができる。
アルカロイドの種類は、特に限定されないが、ニコチン、ノルニコチン、又はこれらの混合物を使用できる。
The tobacco raw material from which the poorly water-soluble substance is derived may contain alkaloids from the standpoint of palatability quality.
The type of alkaloid is not particularly limited, but nicotine, nornicotine, or a mixture thereof can be used.
(2)たばこ原料又は他のたばこ原料から抽出されたデンプン
本発明において、デンプンは、たばこ製剤に含まれるたばこ原料から抽出されたものであってもよいし、たばこ製剤に含まれない別のたばこ原料から抽出されたものであってもよい。すなわち、たばこ製剤は、一態様においてたばこ原料Xと、当該Xから抽出されたデンプンとを含み、別態様としてたばこ原料Xと、X以外のたばこ原料Yから抽出されたデンプンとを含み、さらに別態様としてたばこ原料Xと、当該Xから抽出されたデンプンと、X以外のたばこ原料Yから抽出されたデンプンとを含む。
(2) Starch extracted from tobacco raw materials or other tobacco raw materials In the present invention, the starch may be extracted from a tobacco raw material contained in a tobacco formulation, or may be extracted from another tobacco raw material not contained in a tobacco formulation. That is, the tobacco formulation in one embodiment contains tobacco raw material X and starch extracted from X, in another embodiment contains tobacco raw material X and starch extracted from tobacco raw material Y other than X, and in yet another embodiment contains tobacco raw material X, starch extracted from X, and starch extracted from tobacco raw material Y other than X.
上記デンプンはたばこ原料の細胞内に存在している。したがって、抽出条件は、デンプンを細胞外へリリースできるように調整される。抽出条件については後述する。 The above starch is present inside the cells of the tobacco raw material. Therefore, the extraction conditions are adjusted so that the starch can be released outside the cells. The extraction conditions are described below.
本発明において、上記のデンプンは、難水溶性物質同士を接合するバインダーとして機能する。したがって、上述のたばこ品種の中において、デンプンを多く含むものが好ましい。よって、一態様においてたばこ原料は、デンプンを0.1~20重量%含むたばこ葉が好ましく、デンプンを0.1~2重量%含むたばこ葉がより好ましい。このようなたばこ葉としては、黄色種またはバーレー種が挙げられる。前者は、たばこ葉中に2~5重量%程度のデンプンを含む。また後者は、たばこ葉中に0.1~0.5重量%程度のデンプンを含む。 In the present invention, the starch functions as a binder that bonds poorly water-soluble substances together. Therefore, among the tobacco varieties mentioned above, those that contain a large amount of starch are preferred. Thus, in one embodiment, the tobacco raw material is preferably tobacco leaves that contain 0.1 to 20% by weight of starch, and more preferably tobacco leaves that contain 0.1 to 2% by weight of starch. Examples of such tobacco leaves include flue-cured and burley varieties. The former contain about 2 to 5% by weight of starch in the tobacco leaves. The latter contain about 0.1 to 0.5% by weight of starch in the tobacco leaves.
バインダーとして機能するデンプンを使用することで、たばこ製剤を、デンプン以外のバインダーを含まないものとすることができる。ここで、本願において、特定の成分を「含まない」とは、当該成分を意図的に添加しないことを意味しており、不純物としては当該成分が含まれ得る。デンプン以外のバインダーが不純物として含まれる場合でも、たばこ製剤中のデンプン以外のバインダーの含有量は、2重量%以下、1重量%以下、又は0.5重量%以下とすることができる。 By using starch that functions as a binder, the tobacco formulation can be made free of binders other than starch. Here, in this application, "free of" a specific component means that the component is not added intentionally, and the component may be included as an impurity. Even if a binder other than starch is included as an impurity, the content of the binder other than starch in the tobacco formulation can be 2% by weight or less, 1% by weight or less, or 0.5% by weight or less.
上記のデンプンの種類は、特に限定されないが、可溶性デンプン、不溶性デンプン、又はこれらの混合物を使用でき、これらの中でも、水溶性により均一な混合が可能となるという観点により、可溶性デンプンを使用することが好ましい。 The type of starch is not particularly limited, but soluble starch, insoluble starch, or a mixture thereof can be used. Among these, it is preferable to use soluble starch, as its water solubility allows for uniform mixing.
たばこ製剤中のデンプンの含有量の下限は、特に限定されないが、1重量%以上が好ましく、2重量%以上がより好ましく、2.5重量%以上が最も好ましい。たばこ製剤中のデンプンの含有量の上限は、特に限定されないが、50重量%以下が好ましく、40重量%以下がより好ましく、25重量%以下が最も好ましい。たばこ製剤中のデンプンの含有量の上限は、20重量%以下、15重量%以下、10重量%以下、5重量%以下、又は4重量%以下とすることもできる。たばこ製剤中のデンプンの含有量の上限及び下限は、任意に組み合わせることができる。デンプンの含有量が1重量%以上であると、たばこシートの強度を大きくすることができる。また、デンプンの含有量の上限(50重量%以下)に関して、粘性物でありバインダーとして機能するデンプンが50重量%で十分な量となり、これ以上に量が増えてもバインダーの機能が向上しにくい。また、たばこ製剤中のデンプンの含有量が上記の下限と上限との間の数値範囲内であることにより、バインダーとして機能するデンプンが適切な量となり、得られるたばこシートの構造を維持することができる。
たばこ製剤中のデンプンの含有量は、媒体を除いた固形分換算の値とすることができる。たばこ製剤中のデンプンの含有量は、後述の[実施例]の「(4)デンプンの含有量の測定」に記載の手順及び条件に沿って測定を行い、たばこの製剤の固形分重量に対するデンプンの重量の割合(重量%)として算出することができる。
The lower limit of the content of starch in the tobacco formulation is not particularly limited, but is preferably 1% by weight or more, more preferably 2% by weight or more, and most preferably 2.5% by weight or more. The upper limit of the content of starch in the tobacco formulation is not particularly limited, but is preferably 50% by weight or less, more preferably 40% by weight or less, and most preferably 25% by weight or less. The upper limit of the content of starch in the tobacco formulation can be 20% by weight or less, 15% by weight or less, 10% by weight or less, 5% by weight or less, or 4% by weight or less. The upper and lower limits of the content of starch in the tobacco formulation can be arbitrarily combined. When the content of starch is 1% by weight or more, the strength of the tobacco sheet can be increased. In addition, with regard to the upper limit of the content of starch (50% by weight or less), 50% by weight of starch, which is a viscous substance and functions as a binder, is sufficient, and even if the amount increases beyond this, the binder function is unlikely to be improved. Furthermore, by ensuring that the starch content in the tobacco formulation is within the numerical range between the above lower and upper limits, the amount of starch functioning as a binder is appropriate, and the structure of the resulting tobacco sheet can be maintained.
The starch content in the tobacco formulation can be expressed as a value calculated based on the solid content excluding the medium. The starch content in the tobacco formulation can be measured according to the procedures and conditions described in "(4) Measurement of starch content" in the [Examples] below, and calculated as the ratio (wt%) of the weight of starch to the weight of the solid content of the tobacco formulation.
(3)媒体
媒体は室温(23℃程度)で液体であることが好ましく、その具体例として水または水溶性有機溶媒が挙げられる。水溶性有機溶媒としては、炭素数が1~3である鎖状または分岐状アルコール、あるいは炭素数が4~7であるエーテル等が挙げられる。媒体としてはこれらを単独または組合せて使用できる。取扱性の観点からは、媒体としては水または水と水溶性有機溶媒との混合溶媒が好ましく、水がより好ましい。
(3) Medium The medium is preferably a liquid at room temperature (about 23° C.), and specific examples thereof include water or a water-soluble organic solvent. Examples of the water-soluble organic solvent include linear or branched alcohols having 1 to 3 carbon atoms, and ethers having 4 to 7 carbon atoms. These can be used alone or in combination as the medium. From the viewpoint of ease of handling, the medium is preferably water or a mixed solvent of water and a water-soluble organic solvent, and more preferably water.
たばこ製剤中の媒体の含有量は、特に限定されないが、加熱時の熱エネルギー効率の観点より、20~80重量%が好ましく、30~75重量%がより好ましく、50~70重量%が最も好ましい。たばこ製剤中の媒体の含有量は、IR水分測定装置を使用した乾燥重量法に基づいて算出することができる。 The content of the medium in the tobacco formulation is not particularly limited, but from the viewpoint of thermal energy efficiency during heating, it is preferably 20 to 80% by weight, more preferably 30 to 75% by weight, and most preferably 50 to 70% by weight. The content of the medium in the tobacco formulation can be calculated based on the dry weight method using an IR moisture measuring device.
本発明のたばこ製剤は、例えば、後述の[実施例1]又は[実施例2]の(たばこ製剤及びたばこシートの調製)に示すように、たばこ原料と媒体とを混合して混合物を得た後、当該混合物に対して煮沸処理及び抽出処理を行い当該たばこ原料からデンプンを抽出することにより製造することができる。 The tobacco formulation of the present invention can be produced, for example, as shown in Example 1 or Example 2 (Preparation of Tobacco Formulation and Tobacco Sheet) described below, by mixing tobacco raw materials with a medium to obtain a mixture, and then subjecting the mixture to a boiling treatment and extraction treatment to extract starch from the tobacco raw materials.
本発明においてはたばこ原料中に内在するセルロースを補強材として利用できる。したがって、一態様においてたばこ原料は、セルロースを4~15重量%含むたばこ葉が好ましく、セルロースを5~13重量%含むたばこ葉がより好ましい。このような品種としては、黄色種またはバーレー種が挙げられる。前者は、たばこ葉中に6~8重量%程度のセルロースを含む。また後者は、たばこ葉中に10~12重量%程度のセルロースを含む。
上述の難水溶性物質は、上記セルロースを含むものとすることができる。
In the present invention, cellulose contained in the tobacco raw material can be used as a reinforcing material. Thus, in one embodiment, the tobacco raw material is preferably tobacco leaves containing 4 to 15% by weight of cellulose, more preferably tobacco leaves containing 5 to 13% by weight of cellulose. Examples of such varieties include flue-cured and burley varieties. The former contain about 6 to 8% by weight of cellulose in the tobacco leaves, and the latter contain about 10 to 12% by weight of cellulose in the tobacco leaves.
The poorly water-soluble substance may include the cellulose.
(たばこ製剤の特性)
後述するとおり、本発明のたばこ製剤はたばこ材料として有用である。デンプンがたばこ原料に由来する場合、同じたばこ原料に由来する難水溶性物質との親和性が高い。特に、たばこ原料Xに由来する難水溶性物質と、当該Xから抽出されたデンプンとを含む態様においては、たばこ原料Xの中から一部または全部のデンプンが除去されて難水溶性物質が形成されているため、難水溶性物質中のデンプンが除去された部位に媒体または他の成分を保持できる。そのため、難水溶性物質とデンプンとの親和性が特に高いと考えられる。したがって、たばこ原料に由来する難水溶性物質は、デンプン等や、別途添加された添加剤等と高い親和性を有する。このため、本発明のたばこ製剤は、例えば強度に優れたたばこシートを形成できる。
(Characteristics of tobacco preparations)
As described below, the tobacco preparation of the present invention is useful as a tobacco material. When starch is derived from a tobacco raw material, it has a high affinity with a poorly water-soluble substance derived from the same tobacco raw material. In particular, in an embodiment containing a poorly water-soluble substance derived from tobacco raw material X and starch extracted from the X, a poorly water-soluble substance is formed by removing part or all of the starch from tobacco raw material X, so that the medium or other components can be retained in the part of the poorly water-soluble substance from which the starch has been removed. Therefore, it is considered that the affinity between the poorly water-soluble substance and starch is particularly high. Therefore, the poorly water-soluble substance derived from the tobacco raw material has a high affinity with starch, etc., and additives added separately, etc. For this reason, the tobacco preparation of the present invention can form, for example, a tobacco sheet with excellent strength.
2.たばこシート
本発明のたばこシートは、
(1’)たばこ原料に由来する難水溶性物質、及び
(2’)前記たばこ原料又は他のたばこ原料から抽出されたデンプン
を含む。
2. Tobacco Sheet The tobacco sheet of the present invention is
(1') a poorly water-soluble substance derived from a tobacco raw material; and (2') a starch extracted from the tobacco raw material or from other tobacco raw materials.
(1’)たばこ原料に由来する難水溶性物質
たばこシートに含まれる難水溶性物質の種類、形状、一次粒子径等の各構成は、特に限定されないが、上記「1.たばこ製剤」の「(1)たばこ原料に由来する難水溶性物質」に記載の各構成と同様とすることができる。
(1') Poorly Water-Soluble Substances Derived from Tobacco Raw Materials The type, shape, primary particle size, and other configurations of the poorly water-soluble substance contained in the tobacco sheet are not particularly limited, but may be the same as the configurations described in "(1) Poorly Water-Soluble Substances Derived from Tobacco Raw Materials" in "1. Tobacco Preparations" above.
たばこシート中の難水溶性物質の含有量の下限は、特に限定されないが、基材として機能させる観点より、5重量%以上が好ましく、10重量%以上がより好ましく、15重量%以上が最も好ましく、また、20重量%以上、75重量%以上、又は90重量%以上とすることもできる。たばこシート中の難水溶性物質の含有量の上限は、特に限定されないが、95重量%以下、80重量%以下、70重量%以下、50重量%以下、又は35重量%以下とすることができる。たばこシート中の難水溶性物質の含有量の上限及び下限は、任意に組み合わせることができる。
たばこ製剤から媒体を除くことによりたばこシートを形成することができる。そのため、後述の[実施例]の「(3)難水溶性物質の含有量の測定」に記載したように、上述のたばこ製剤中の難水溶性物質の含有量(重量%)(固形分換算)を、たばこシート中の難水溶性物質の含有量(重量%)に等しいとみなすことができる。
また、たばこシート中の難水溶性物質の含有量は、前述のプロスキー法に基づいて算出することもできる。
The lower limit of the content of the poorly water-soluble substance in the tobacco sheet is not particularly limited, but from the viewpoint of functioning as a substrate, it is preferably 5% by weight or more, more preferably 10% by weight or more, most preferably 15% by weight or more, and can also be 20% by weight or more, 75% by weight or more, or 90% by weight or more. The upper limit of the content of the poorly water-soluble substance in the tobacco sheet is not particularly limited, but can be 95% by weight or less, 80% by weight or less, 70% by weight or less, 50% by weight or less, or 35% by weight or less. The upper and lower limits of the content of the poorly water-soluble substance in the tobacco sheet can be combined in any manner.
A tobacco sheet can be formed by removing the medium from the tobacco formulation. Therefore, as described in "(3) Measurement of the content of poorly water-soluble substance" in the Examples below, the content (wt%) of the poorly water-soluble substance in the tobacco formulation (converted into solid content) can be considered to be equal to the content (wt%) of the poorly water-soluble substance in the tobacco sheet.
The content of poorly water-soluble substances in a tobacco sheet can also be calculated based on the above-mentioned Prosky method.
難水溶性物質の原料となるたばこ原料は、特に限定されないが、上記「1.たばこ製剤」の「(たばこ原料)」に記載のたばこ原料と同様のものとすることができる。 The tobacco raw material from which the poorly water-soluble substance is derived is not particularly limited, but can be the same as the tobacco raw material described in "(Tobacco raw materials)" in "1. Tobacco preparations" above.
(2’)たばこ原料又は他のたばこ原料から抽出されたデンプン
たばこシートに含まれるデンプンの種類等の各構成は、特に限定されないが、上記「1.たばこ製剤」の「(2)たばこ原料又は他のたばこ原料から抽出されたデンプン」に記載の各構成と同様とすることができる。
(2') Starch extracted from tobacco raw materials or other tobacco raw materials The types of starch and other components contained in the tobacco sheet are not particularly limited, but may be the same as the components described in "(2) Starch extracted from tobacco raw materials or other tobacco raw materials" in "1. Tobacco preparations" above.
たばこシート中のデンプンの含有量の下限は、特に限定されないが、1重量%以上が好ましく、2重量%以上がより好ましく、2.5重量%以上が最も好ましい。たばこシート中のデンプンの含有量の上限は、特に限定されないが、50重量%以下が好ましく、40重量%以下がより好ましく、25重量%以下が最も好ましい。たばこシート中のデンプンの含有量の上限は、20重量%以下、15重量%以下、10重量%以下、5重量%以下、又は4重量%以下とすることもできる。たばこシート中のデンプンの含有量の上限及び下限は、任意に組み合わせることができる。デンプンの含有量が1重量%以上であると、たばこシートの強度を大きくすることができる。また、デンプンの含有量の上限(50重量%以下)に関して、粘性物でありバインダーとして機能するデンプンが50重量%で十分な量となり、これ以上に量が増えてもバインダーの機能が向上しにくい。また、たばこシート中のデンプンの含有量が上記の下限と上限との間の数値範囲内であることにより、バインダーとして機能するデンプンが適切な量となり、得られるたばこシートの構造を維持することができる。
たばこ製剤から媒体を除くことによりたばこシートを形成することができる。そのため、後述の[実施例]の「(4)デンプンの含有量の測定」に記載したように、上述のたばこ製剤中のデンプンの含有量(重量%)(固形分換算)を、たばこシート中のデンプンの含有量(重量%)に等しいとみなすことができる。
The lower limit of the starch content in the tobacco sheet is not particularly limited, but is preferably 1% by weight or more, more preferably 2% by weight or more, and most preferably 2.5% by weight or more. The upper limit of the starch content in the tobacco sheet is not particularly limited, but is preferably 50% by weight or less, more preferably 40% by weight or less, and most preferably 25% by weight or less. The upper limit of the starch content in the tobacco sheet can be 20% by weight or less, 15% by weight or less, 10% by weight or less, 5% by weight or less, or 4% by weight or less. The upper and lower limits of the starch content in the tobacco sheet can be arbitrarily combined. When the starch content is 1% by weight or more, the strength of the tobacco sheet can be increased. In addition, with regard to the upper limit of the starch content (50% by weight or less), 50% by weight of starch, which is a viscous substance and functions as a binder, is sufficient, and even if the amount increases beyond this, the binder function is unlikely to be improved. Furthermore, by having the starch content in the tobacco sheet be within the numerical range between the above-mentioned lower and upper limits, the amount of starch functioning as a binder is appropriate, and the structure of the obtained tobacco sheet can be maintained.
A tobacco sheet can be formed by removing the medium from the tobacco formulation. Therefore, as described in "(4) Measurement of starch content" in the Examples below, the starch content (wt%) in the above-mentioned tobacco formulation (converted into solid content) can be considered to be equal to the starch content (wt%) in the tobacco sheet.
たばこシートは、たばこ原料に由来する成分を含むことができる。たばこ原料に由来する成分は、上述のたばこ原料に由来する難水溶性物質、及び上述のたばこ原料から抽出されたデンプンを含むことができる。
たばこシート中のたばこ原料に由来する成分の含有量の下限は、特に限定されないが、基材として機能させる観点より、10重量%以上が好ましく、15重量%以上がより好ましく、20重量%以上が最も好ましく、また、75重量%以上又は90重量%以上とすることもできる。たばこシート中のたばこ原料に由来する成分の含有量の上限は、特に限定されないが、80重量%以下、70重量%以下、又は50重量%以下とすることができる。たばこシート中のたばこ原料に由来する成分の含有量の上限及び下限は、任意に組み合わせることができる。
たばこシート中のたばこ原料に由来する成分の含有量は、使用したたばこ原料と外添した成分との合計の重量に対する、当該たばこ原料の重量の割合として算出することができる。
The tobacco sheet may include a component derived from a tobacco raw material. The component derived from a tobacco raw material may include a poorly water-soluble substance derived from the tobacco raw material described above, and starch extracted from the tobacco raw material described above.
The lower limit of the content of components derived from tobacco raw materials in the tobacco sheet is not particularly limited, but from the viewpoint of functioning as a base material, it is preferably 10% by weight or more, more preferably 15% by weight or more, most preferably 20% by weight or more, and can also be 75% by weight or more or 90% by weight or more. The upper limit of the content of components derived from tobacco raw materials in the tobacco sheet is not particularly limited, but can be 80% by weight or less, 70% by weight or less, or 50% by weight or less. The upper and lower limits of the content of components derived from tobacco raw materials in the tobacco sheet can be combined in any manner.
The content of components derived from the tobacco raw materials in the tobacco sheet can be calculated as the ratio of the weight of the tobacco raw materials to the total weight of the tobacco raw materials used and the externally added components.
(その他の成分)
たばこシートは、エアロゾル発生剤を更に含むことができる。
エアロゾル発生剤は、特に限定されないが、グリセリン、1,2-プロパンジオール、1,3-プロパンジオール、又はこれらのうちの2種以上の混合物を含むことができる。
たばこシート中のエアロゾル発生剤の含有量は、特に限定されないが、喫煙時の煙量の観点より、10~50重量%が好ましく、15~45重量%がより好ましく、20~25重量%が最も好ましい。
(Other ingredients)
The tobacco sheet may further include an aerosol generating agent.
The aerosol generating agent may include, but is not limited to, glycerin, 1,2-propanediol, 1,3-propanediol, or a mixture of two or more thereof.
The content of the aerosol generating agent in the tobacco sheet is not particularly limited, but from the viewpoint of the amount of smoke produced when smoking, it is preferably 10 to 50% by weight, more preferably 15 to 45% by weight, and most preferably 20 to 25% by weight.
たばこシートは、グルカンを更に含むことができる。グルカンは、後述するバインダーの一種である。
グルカンは、特に限定されないが、タマリンドガム、グアーガム、ローカストビーンガム、ジェランガム、プルラン、又はこれらのうちの2種以上の混合物を含むことができる。
たばこシート中のグルカンの含有量は、特に限定されないが、成形性の観点より、0.1~5重量%が好ましく、0.5~2重量%がより好ましく、1.0~1.5重量%が最も好ましい。
The tobacco sheet may further contain glucan, which is a type of binder described below.
The glucan may include, but is not limited to, tamarind gum, guar gum, locust bean gum, gellan gum, pullulan, or a mixture of two or more of these.
The glucan content in the tobacco sheet is not particularly limited, but from the viewpoint of moldability, it is preferably 0.1 to 5% by weight, more preferably 0.5 to 2% by weight, and most preferably 1.0 to 1.5% by weight.
たばこシートは、バインダーを含むことができる。一方で、本発明では、バインダーとして機能するデンプンを使用することで、たばこシートを、デンプン以外のバインダーを含まないものとすることができる。仮に、たばこシートが当該バインダーを不純物として含む場合であっても、たばこシート中のデンプン以外のバインダーの含有量は、3重量%以下、1重量%以下、又は0.5重量%以下とすることができる。 The tobacco sheet may contain a binder. However, in the present invention, by using starch that functions as a binder, the tobacco sheet can be free of binders other than starch. Even if the tobacco sheet contains the binder as an impurity, the content of binders other than starch in the tobacco sheet can be 3% by weight or less, 1% by weight or less, or 0.5% by weight or less.
無添加とすることが望ましい場合は、たばこシートをパルプを含まないものとすることができる。仮に、たばこシートがパルプを不純物として含む場合であっても、たばこシート中のパルプの含有量は、3重量%以下、1重量%以下、又は0.5重量%以下とすることができる If it is desirable to have no additives, the tobacco sheet may be pulp-free. Even if the tobacco sheet contains pulp as an impurity, the pulp content in the tobacco sheet may be 3% by weight or less, 1% by weight or less, or 0.5% by weight or less.
本発明のたばこシートの形態は、特に限定されず、抄造シート、キャストシート等を採用することができるが、低密度のシートとする観点より、キャストシートであることが好ましい。
上記の各種たばこシートについては、「たばこの事典、たばこ総合研究センター、2009.3.31」に詳細が開示されている。
The form of the tobacco sheet of the present invention is not particularly limited, and a paper-formed sheet, a cast sheet, or the like can be adopted. From the viewpoint of providing a low-density sheet, a cast sheet is preferable.
Details of the various types of tobacco sheets mentioned above are disclosed in "Encyclopedia of Tobacco, Tobacco Research Center, March 31, 2009."
本発明のたばこシートは、特に限定されないが、上述の「1.たばこ製剤」の項目に記載のたばこ製剤の成形体とすることができる。 The tobacco sheet of the present invention can be, but is not limited to, a molded product of the tobacco formulation described in the above section "1. Tobacco formulation."
3.製造方法
(たばこ製剤の製造方法)
本発明のたばこ製剤は、たばこ原料を媒体中で加熱して、上述のデンプンを抽出する工程を備える方法で製造されることが好ましい。たばこ製剤は、上記「1.たばこ製剤」の項目に記載したものとすることができる。
3. Manufacturing method (Manufacturing method of tobacco formulation)
The tobacco formulation of the present invention is preferably produced by a method including a step of heating a tobacco raw material in a medium to extract the above-mentioned starch. The tobacco formulation may be one described in the above section "1. Tobacco formulation."
(1)温度
たばこ製剤中のデンプンはたばこ原料の細胞壁内に含まれている。よって、細胞内からデンプンをリリースするためにはある程度の高い温度が必要となる。このような観点から、抽出時の温度は、好ましくは100~125℃であり、より好ましくは105~120℃であり、最も好ましくは110~119℃である。またこの温度であると、上述のセルロースも効率よく細胞外へリリースすることができる。
(1) Temperature The starch in the tobacco formulation is contained within the cell walls of the tobacco raw material. Therefore, a certain degree of high temperature is required to release the starch from within the cells. From this perspective, the temperature during extraction is preferably 100 to 125°C, more preferably 105 to 120°C, and most preferably 110 to 119°C. Furthermore, at this temperature, the above-mentioned cellulose can also be efficiently released outside the cells.
(2)圧力
細胞内からデンプンをリリースするためにはある程度の高い圧力が必要となる。このような観点から、抽出時の平均圧力は、好ましくは20~117kPaであり、より好ましくは50~110kPaであり、最も好ましくは85~95kPaである。また、抽出時の最大圧力は、好ましくは70~117kPaであり、より好ましくは80~116.5kPaであり、最も好ましくは90~116.5kPaである。また、平均圧力又は最大圧力が上記数値範囲内であると、上述のセルロースも効率よく細胞外へリリースすることができる。
(2) Pressure A certain level of high pressure is required to release starch from within the cells. From this viewpoint, the average pressure during extraction is preferably 20 to 117 kPa, more preferably 50 to 110 kPa, and most preferably 85 to 95 kPa. The maximum pressure during extraction is preferably 70 to 117 kPa, more preferably 80 to 116.5 kPa, and most preferably 90 to 116.5 kPa. When the average pressure or maximum pressure is within the above numerical range, the above-mentioned cellulose can also be efficiently released outside the cells.
(3)時間
細胞内からデンプンをリリースするためにはある程度の長い時間が必要となる。このような観点から、抽出処理の時間は、好ましくは20~90分であり、より好ましくは60~80分であり、最も好ましくは65~70分である。また、抽出処理の時間が上記数値範囲内であると、上述のセルロースも効率よく細胞外へリリースすることができる。
(3) Time A relatively long time is required to release starch from within the cells. From this viewpoint, the extraction treatment time is preferably 20 to 90 minutes, more preferably 60 to 80 minutes, and most preferably 65 to 70 minutes. Furthermore, when the extraction treatment time is within the above numerical range, the above-mentioned cellulose can also be efficiently released outside the cells.
(4)回数
抽出処理を繰り返すことにより、細胞内からデンプンをよりリリースすることができる。このような観点から、抽出処理の回数は、1~2回、3~4回、又は5~10回とすることができ、回数が多い程、デンプンをより効率よくリリースすることができる。また、抽出処理の回数が上記数値範囲内であると、上述のセルロースも効率よく細胞外へリリースすることができる。
(4) Number of times By repeating the extraction process, more starch can be released from inside the cells. From this viewpoint, the number of times of the extraction process can be 1 to 2 times, 3 to 4 times, or 5 to 10 times, and the more times the number of times, the more efficiently the starch can be released. Furthermore, when the number of times of the extraction process is within the above numerical range, the above-mentioned cellulose can also be efficiently released outside the cells.
(5)雰囲気
たばこ原料からのデンプンの抽出は閉鎖系で行うことが好ましい。たばこ原料が有する香味成分が低減することを回避できるからである。
(5) Atmosphere It is preferable to carry out the extraction of starch from tobacco raw materials in a closed system, since this can prevent a reduction in the flavor components contained in the tobacco raw materials.
(6)粉砕
抽出効率の観点から、抽出に供するたばこ原料の表面積は大きいことが好ましい。したがって、予めたばこ原料を粉砕する工程を設け、粉末のたばこ原料を抽出に供してもよい。この場合は乾式粉砕を行うことが好ましい。乾式粉砕には公知の機械を用いることができる。粉末のたばこ原料の粒度分布は限定されないが、500μm未満のD90を有することが好ましく、100μm未満のD90を有することがより好ましい。D90の下限は限定されないが、実質的には5μm以上が下限となる。
(6) Grinding From the viewpoint of extraction efficiency, it is preferable that the surface area of the tobacco raw material to be extracted is large. Therefore, a step of grinding the tobacco raw material in advance may be provided, and the powdered tobacco raw material may be subjected to extraction. In this case, dry grinding is preferable. A known machine may be used for dry grinding. The particle size distribution of the powdered tobacco raw material is not limited, but it is preferable that it has a D90 of less than 500 μm, and more preferably a D90 of less than 100 μm. The lower limit of D90 is not limited, but is practically 5 μm or more.
あるいは、抽出と同時にたばこ原料を粉砕してもよい。すなわち、たばこ原料を湿式粉砕しながら前記抽出を行うことができる。当該湿式粉砕は閉鎖系で処理を行うことが好ましい。湿式粉砕されたたばこ原料の粒度分布は前述のとおりである。 Alternatively, the tobacco raw material may be ground simultaneously with the extraction. That is, the extraction can be carried out while the tobacco raw material is wet-ground. The wet-grinding is preferably carried out in a closed system. The particle size distribution of the wet-ground tobacco raw material is as described above.
たばこ製剤の製造方法は、エアロゾル発生剤、バインダー、又はこれらの組み合わせを含む成分を添加する工程を更に含むことができる。エアロゾル発生剤又はバインダーは、上記「2.たばこシート」の「(その他の成分)」に記載したものを使用できる。 The method for producing a tobacco formulation may further include a step of adding ingredients including an aerosol generating agent, a binder, or a combination thereof. The aerosol generating agent or binder may be those described in "(Other ingredients)" in "2. Tobacco Sheet" above.
たばこ製剤の製造方法は、パルプを含む他の難水溶性物質を添加する工程を含まないものとすることができる。他の難水溶性物質は、上述のたばこ原料に由来する難水溶性物質以外の難水溶性物質である。本願では、たばこ製剤に他の難水溶性物質の原料を外添しないでもたばこシートが形成可能である。 The manufacturing method of the tobacco formulation may not include a step of adding other poorly water-soluble substances, including pulp. The other poorly water-soluble substances are poorly water-soluble substances other than the poorly water-soluble substances derived from the tobacco raw materials described above. In the present application, tobacco sheets can be formed without externally adding raw materials of other poorly water-soluble substances to the tobacco formulation.
(たばこシートの製造方法)
本発明のたばこシートを製造する方法の種類は、特に限定されず、抄造法、キャスト法等の公知の方法を採用することができる。これらの方法のうち、得られるシートの均一性の観点より、キャスト法が好ましい。
(Production method of tobacco sheet)
The method for producing the tobacco sheet of the present invention is not particularly limited, and any known method such as a papermaking method, a casting method, etc. Of these methods, the casting method is preferred from the viewpoint of uniformity of the obtained sheet.
本発明のたばこシートを製造する方法は、上述の方法でたばこ製剤を調製する工程、及び前記たばこ製剤を基材の上に展開し、そして乾燥させる工程を備えることができる。
上述のたばこ製剤を調製する工程においてたばこ原料の粉砕が行われている場合、たばこシートを製造する方法は、たばこ製剤を粉砕する工程を含まなくてもよい。
A method for producing a tobacco sheet of the present invention may comprise the steps of preparing a tobacco formulation by the method described above, and spreading and drying the tobacco formulation on a substrate.
When the tobacco raw material is pulverized in the step of preparing the above-mentioned tobacco formulation, the method of producing a tobacco sheet does not need to include a step of pulverizing the tobacco formulation.
<たばこシートの成形方法(キャスト法)>
キャスト法(スラリー法)によりたばこシートを成形する方法としては、例えば、以下の工程を含む方法を挙げることができる。
(1)水、任意のパルプ及び任意のバインダーと、熟成済たばこの粉砕物を混合して混合物を得る工程(均質化工程)。
(2)当該混合物を薄く延ばして(キャストして)乾燥し、たばこシートとする工程。
この方法でたばこシートを成形する場合、水、パルプ及びバインダーと、砕いたたばこ葉を混合したスラリーに対して紫外線照射もしくはX線照射することでニトロソアミン等の一部の成分を除去する工程を加えてもよい。
<Tobacco sheet molding method (casting method)>
An example of a method for forming a tobacco sheet by a casting method (slurry method) includes a method including the following steps.
(1) A step of mixing ground aged tobacco with water, an optional pulp, and an optional binder to obtain a mixture (homogenization step).
(2) The mixture is spread (cast) into a thin sheet and dried to form a tobacco sheet.
When forming a tobacco sheet by this method, a step may be added in which a slurry of water, pulp, binder, and crushed tobacco leaves is mixed with ultraviolet light or X-rays to remove some of the components such as nitrosamines.
たばこシートの形状は適宜調整できるが、一態様において厚さは50~500μmである。当該たばこシートを裁刻することで、刻またはストランドを製造できる。また、当該たばこシートを粉砕することで、粉末を製造できる。 The shape of the tobacco sheet can be adjusted as appropriate, but in one embodiment, the thickness is 50 to 500 μm. The tobacco sheet can be chopped to produce shreds or strands. The tobacco sheet can also be pulverized to produce powder.
4.たばこ充填物及び喫煙物品
本発明のたばこ充填物は、上述のたばこシートを含む。
また、本発明の喫煙物品は、上記たばこ充填物を含む。
本発明の喫煙物品は、非燃焼加熱喫煙物品とすることができる。
4. Tobacco Filler and Smoking Article The tobacco filler of the present invention comprises the tobacco sheet described above.
Furthermore, the smoking article of the present invention includes the above tobacco filler.
The smoking article of the present invention may be a non-combustion heating smoking article.
本願において「喫煙物品」は、ユーザが吸引により香味を味わう吸引物品を意味する。喫煙物品は、従来のシガレットを代表とする燃焼型喫煙物品と非燃焼加熱喫煙物品とに大別できる。 In this application, "smoking article" means an inhalation article that allows the user to enjoy a flavor by inhaling. Smoking articles can be broadly divided into combustion-type smoking articles, such as conventional cigarettes, and non-combustion heat-type smoking articles.
燃焼型喫煙物品としては、例えば、シガレット、パイプ、キセル、葉巻、またはシガリロなどが挙げられる。 Examples of combustible smoking articles include cigarettes, pipes, pipes, cigars, and cigarillos.
非燃焼加熱喫煙物品(加熱喫煙物品)は、当該物品と別体型の加熱装置により加熱されてもよいし、当該物品と一体型の加熱装置により加熱されてもよい。前者の喫煙物品(別体型)において、非燃焼加熱喫煙物品と加熱装置とをまとめて、「非燃焼加熱喫煙システム」とも称する。以下に非燃焼加熱喫煙システムの一例を、図1および図2を参照して説明する。 A non-combustion heated smoking article (heated smoking article) may be heated by a heating device separate from the article, or by a heating device integrated into the article. In the former smoking article (separate type), the non-combustion heated smoking article and the heating device are collectively referred to as a "non-combustion heated smoking system." An example of a non-combustion heated smoking system is described below with reference to Figures 1 and 2.
図1は、非燃焼加熱喫煙システムの一例を示す断面模式図であり、非燃焼加熱喫煙物品20の喫煙用セグメント20A内に、ヒータ12を挿入する前の状態を示す。使用時には、喫煙用セグメント20A内に、ヒータ12が挿入される。図2は、非燃焼加熱喫煙物品20の断面図である。 FIG. 1 is a schematic cross-sectional view showing an example of a non-combustion heat smoking system, showing the state before a heater 12 is inserted into the smoking segment 20A of a non-combustion heat smoking article 20. When in use, the heater 12 is inserted into the smoking segment 20A. FIG. 2 is a cross-sectional view of a non-combustion heat smoking article 20.
図1に示すとおり、非燃焼加熱喫煙システムは、非燃焼加熱喫煙物品20と、喫煙用セグメント20Aを内側から加熱する加熱装置10とを備える。ただし非燃焼加熱喫煙システムは、図1の構成に限定されない。 As shown in FIG. 1, the non-combustion heat smoking system includes a non-combustion heat smoking article 20 and a heating device 10 that heats the smoking segment 20A from the inside. However, the non-combustion heat smoking system is not limited to the configuration shown in FIG. 1.
図1に示される加熱装置10は、ボディ11と、ヒータ12とを備える。図示していないが、ボディ11は電池ユニットと制御ユニットを備えていてもよい。ヒータ12は電気抵抗によるヒータであることができ、喫煙用セグメント20A内に挿入されて、喫煙用セグメント20Aを加熱する。 The heating device 10 shown in FIG. 1 includes a body 11 and a heater 12. Although not shown, the body 11 may include a battery unit and a control unit. The heater 12 may be an electric resistance heater, and is inserted into the smoking segment 20A to heat the smoking segment 20A.
図1においては喫煙用セグメント20Aが内側から加熱されているが、非燃焼加熱喫煙物品20の態様はこれに限定されず、別態様において喫煙用セグメント20Aは外側から加熱される。 In FIG. 1, the smoking segment 20A is heated from the inside, but the embodiment of the non-combustion heating smoking article 20 is not limited to this, and in another embodiment, the smoking segment 20A is heated from the outside.
加熱装置10による加熱温度は特に限定されないが、400℃以下であることが好ましく、50~400℃であることがより好ましく、150~350℃であることがさらに好ましい。加熱温度とは加熱装置10のヒータ12の温度を指す。 The heating temperature by the heating device 10 is not particularly limited, but is preferably 400°C or less, more preferably 50 to 400°C, and even more preferably 150 to 350°C. The heating temperature refers to the temperature of the heater 12 of the heating device 10.
図2に示すとおり、非燃焼加熱喫煙物品20(以下、単に「喫煙物品20」と称する)は、円柱形状を有する。喫煙物品20の円周の長さは、16mm~27mmであることが好ましく、20mm~26mmであることがより好ましく、21mm~25mmであることがさらに好ましい。喫煙物品20の全長(水平方向の長さ)は特に限定されないが、40mm~90mmであることが好ましく、50mm~75mmであることがより好ましく、50mm~60mmであることがさらに好ましい。 As shown in FIG. 2, the non-combustion heat smoking article 20 (hereinafter simply referred to as "smoking article 20") has a cylindrical shape. The circumferential length of the smoking article 20 is preferably 16 mm to 27 mm, more preferably 20 mm to 26 mm, and even more preferably 21 mm to 25 mm. The overall length (horizontal length) of the smoking article 20 is not particularly limited, but is preferably 40 mm to 90 mm, more preferably 50 mm to 75 mm, and even more preferably 50 mm to 60 mm.
喫煙物品20は、喫煙用セグメント20Aと、吸口を構成するフィルター部20Cと、これらを連結する連結部20Bとから構成される。 The smoking article 20 is composed of a smoking segment 20A, a filter portion 20C that forms the mouthpiece, and a connecting portion 20B that connects these.
喫煙用セグメント20Aは、円柱状であり、その全長(軸方向の長さ)は、例えば、5~100mmであることが好ましく、10~50mmであることがより好ましく、10~25mmであることがさらに好ましい。喫煙用セグメント20Aの断面の形状は特に限定されないが、例えば円形、楕円形、多角形等とすることができる。 The smoking segment 20A is cylindrical, and its overall length (length in the axial direction) is, for example, preferably 5 to 100 mm, more preferably 10 to 50 mm, and even more preferably 10 to 25 mm. The cross-sectional shape of the smoking segment 20A is not particularly limited, but can be, for example, circular, elliptical, polygonal, etc.
喫煙用セグメント20Aは、喫煙用組成物シートまたはこれに由来する材料21と、その周囲に巻かれたラッパー22とを有する。 The smoking segment 20A has a smoking composition sheet or material derived therefrom 21 and a wrapper 22 wrapped around it.
フィルター部20Cは、円柱形をなしている。フィルター部20Cは、酢酸セルロースアセテート繊維が充填されて構成されたロッド状の第1セグメント25と、同じく酢酸セルロースアセテート繊維が充填されて構成されたロッド状の第2セグメント26とを有する。第1セグメント25は、喫煙用セグメント20A側に位置している。第1セグメント25は、中空部を有していてもよい。第2セグメント26は、吸口側に位置している。第2セグメント26は、中実である。第1セグメント25は、第1充填層(酢酸セルロースアセテート繊維)25aと、第1充填層25aの周囲に巻かれたインナープラグラッパー25bとにより構成される。第2セグメント26は、第2充填層(酢酸セルロースアセテート繊維)26aと、第2充填層26aの周囲に巻かれたインナープラグラッパー26bとにより構成される。第1セグメント25および第2セグメント26は、アウタープラグラッパー27によって連結されている。アウタープラグラッパー27は、酢酸ビニルエマルジョン系接着剤等によって第1セグメント25および第2セグメント26に接着されている。 The filter section 20C has a cylindrical shape. The filter section 20C has a rod-shaped first segment 25 filled with cellulose acetate fiber and a rod-shaped second segment 26 similarly filled with cellulose acetate fiber. The first segment 25 is located on the smoking segment 20A side. The first segment 25 may have a hollow portion. The second segment 26 is located on the mouthpiece side. The second segment 26 is solid. The first segment 25 is composed of a first filling layer (cellulose acetate fiber) 25a and an inner plug wrapper 25b wrapped around the first filling layer 25a. The second segment 26 is composed of a second filling layer (cellulose acetate fiber) 26a and an inner plug wrapper 26b wrapped around the second filling layer 26a. The first segment 25 and the second segment 26 are connected by an outer plug wrapper 27. The outer plug wrapper 27 is adhered to the first segment 25 and the second segment 26 with a vinyl acetate emulsion adhesive or the like.
フィルター部20Cの長さを例えば10~30mm、連結部20Bの長さを例えば10~30mm、第1セグメント25の長さを例えば5~15mm、第2セグメント26の長さを例えば5~15mmとすることができる。これら個々のセグメントの長さは、一例であり、製造適性、要求品質、喫煙用セグメント20Aの長さ等に応じて、適宜変更できる。 The length of the filter portion 20C can be, for example, 10 to 30 mm, the length of the connecting portion 20B can be, for example, 10 to 30 mm, the length of the first segment 25 can be, for example, 5 to 15 mm, and the length of the second segment 26 can be, for example, 5 to 15 mm. These lengths of each segment are just examples and can be changed as appropriate depending on manufacturing suitability, required quality, the length of the smoking segment 20A, etc.
例えば、第1セグメント25(センターホールセグメント)は、1つまたは複数の中空部を有する第1充填層25aと、第1充填層25aを覆うインナープラグラッパー25bとで構成される。第1セグメント25は、第2セグメント26の強度を高める機能を有する。第1セグメント25の第1充填層25aは、例えば酢酸セルロース繊維が高密度で充填されている。この酢酸セルロース繊維には、トリアセチンを含む可塑剤が酢酸セルロースの質量に対して、例えば6~20質量%添加されて硬化されている。第1セグメント25の中空部は、例えば内径φ1.0~φ5.0mmである。 For example, the first segment 25 (center hole segment) is composed of a first filling layer 25a having one or more hollow portions, and an inner plug wrapper 25b that covers the first filling layer 25a. The first segment 25 has the function of increasing the strength of the second segment 26. The first filling layer 25a of the first segment 25 is densely packed with, for example, cellulose acetate fibers. A plasticizer containing triacetin is added to the cellulose acetate fibers in an amount of, for example, 6 to 20% by mass relative to the mass of the cellulose acetate, and the fibers are hardened. The hollow portion of the first segment 25 has an inner diameter of, for example, φ1.0 to φ5.0 mm.
第1セグメント25の第1充填層25aは、例えば、比較的に高い繊維充填密度で構成されてもよく、あるいは後述する第2セグメント26の第2充填層26aの繊維充填密度と同等であってもよい。このため、吸引時には、空気やエアロゾルが中空部のみを流れることになり、第1充填層25aには空気やエアロゾルがほとんど流れない。例えば、第2セグメント26において、エアロゾル成分の濾過による減少を少なくしたい場合には、例えば第2セグメント26の長さを短くして、その分だけ第1セグメント25を長くすることもできる。 The first filling layer 25a of the first segment 25 may be constructed with, for example, a relatively high fiber packing density, or may be equivalent to the fiber packing density of the second filling layer 26a of the second segment 26 described below. Therefore, during inhalation, air and aerosol flow only through the hollow portion, and almost no air or aerosol flows through the first filling layer 25a. For example, if it is desired to reduce the loss of aerosol components due to filtration in the second segment 26, the length of the second segment 26 can be shortened and the first segment 25 can be lengthened accordingly.
短縮した第2セグメント26を第1セグメント25で置き換えることは、エアロゾル成分のデリバリー量を増大させるために有効である。第1セグメント25の第1充填層25aが繊維充填層であることから、使用時の外側からの触り心地は、使用者に違和感を生じさせることがない。 Replacing the shortened second segment 26 with the first segment 25 is effective in increasing the amount of aerosol components delivered. Because the first filling layer 25a of the first segment 25 is a fiber-filled layer, the feel from the outside during use does not cause discomfort to the user.
第2セグメント26は、第2充填層26aと、第2充填層26aを覆うインナープラグラッパー26bとで構成される。第2セグメント26(フィルターセグメント)は、酢酸セルロース繊維が一般的な密度で充填されており、一般的なエアロゾル成分の濾過性能を有する。 The second segment 26 is composed of a second packed layer 26a and an inner plug wrapper 26b that covers the second packed layer 26a. The second segment 26 (filter segment) is packed with cellulose acetate fibers at a typical density and has typical filtering performance for filtering aerosol components.
第1セグメント25と第2セグメント26との間で、喫煙用セグメント20Aから放出されるエアロゾル(主流煙)をろ過するろ過性能を異ならせてもよい。第1セグメント25および第2セグメント26の少なくとも一方に、香料を含ませてもよい。フィルター部20Cの構造は任意であり、上記のような複数のセグメントを有する構造であってもよいし、単一のセグメントによって構成されていてもよい。またフィルター部20Cは、1つのセグメントで構成されてもよい。この場合、フィルター部20Cは、第1セグメントまたは第2セグメントのいずれで構成されていてもよい。 The filtering performance for filtering the aerosol (mainstream smoke) emitted from the smoking segment 20A may be different between the first segment 25 and the second segment 26. At least one of the first segment 25 and the second segment 26 may contain a flavoring. The structure of the filter portion 20C is arbitrary, and may be a structure having multiple segments as described above, or may be composed of a single segment. The filter portion 20C may also be composed of one segment. In this case, the filter portion 20C may be composed of either the first segment or the second segment.
連結部20Bは、円筒形をなしている。連結部20Bは、例えば厚紙等によって円筒形に形成された紙管23を有する。連結部20Bには、エアロゾルを冷却するための冷却部材が充填されていてもよい。冷却部材としては、ポリ乳酸等のポリマーのシートが挙げられ、当該シートを折り畳んで充填することができる。さらに、喫煙用セグメント20Aと連結部20Bの間には、喫煙用セグメント20Aの位置が変動することを抑制する支持部が設けられていてもよい。支持部は、第1セグメント25のようなセンタホールフィルター等の公知の材料で構成できる。 The connecting part 20B is cylindrical. The connecting part 20B has a cardboard tube 23 formed into a cylindrical shape, for example, from cardboard. The connecting part 20B may be filled with a cooling material for cooling the aerosol. An example of the cooling material is a sheet of a polymer such as polylactic acid, which can be folded and filled. Furthermore, a support part may be provided between the smoking segment 20A and the connecting part 20B to prevent the position of the smoking segment 20A from fluctuating. The support part may be made of a known material, such as a center hole filter like the first segment 25.
ラッパー28は、喫煙用セグメント20A、連結部20B、およびフィルター部20Cの外側に円筒形に巻かれて、これらを一体的に連結している。ラッパー28の一方の面(内面)には、通気孔部24の付近を除く全面または略全面に酢酸ビニルエマルジョン系接着剤が塗布されている。複数の通気孔部24は、ラッパー28によって、喫煙用セグメント20A、連結部20B、およびフィルター部20Cが一体にされた後に、外側からレーザ加工を施して形成される。 The wrapper 28 is wrapped around the outside of the smoking segment 20A, the connecting portion 20B, and the filter portion 20C in a cylindrical shape, connecting them together. One side (inner surface) of the wrapper 28 is coated entirely or almost entirely with a vinyl acetate emulsion adhesive, except for the area near the ventilation hole portion 24. The multiple ventilation hole portions 24 are formed by laser processing from the outside after the smoking segment 20A, the connecting portion 20B, and the filter portion 20C are integrated by the wrapper 28.
通気孔部24は、連結部20Bを厚み方向に貫通するように2以上の貫通孔を有する。2以上の貫通孔は、喫煙物品20の中心軸の延長線上から見て、放射状に配置するように形成される。本実施形態では、通気孔部24は、連結部20Bに設けられているが、フィルター部20Cに設けられていてもよい。また、本実施形態では、通気孔部24の2以上の貫通孔は、1つの円環上に一定間隔を空けて1列に並んで設けられるが、2つの円環上に一定の間隔を空けて2列に並んで設けられていてもよいし、1列または2列の通気孔部24が不連続または不規則に並んで設けられていてもよい。ユーザが吸口を咥えて吸引する際に、通気孔部24を介して主流煙中に外気が取り込まれる。ただし、通気孔部24は設けられていなくてもよい。 The ventilation hole section 24 has two or more through holes penetrating the connecting section 20B in the thickness direction. The two or more through holes are formed so as to be arranged radially when viewed from an extension of the central axis of the smoking article 20. In this embodiment, the ventilation hole section 24 is provided in the connecting section 20B, but may be provided in the filter section 20C. In addition, in this embodiment, the two or more through holes of the ventilation hole section 24 are arranged in one row at a fixed interval on one ring, but may be arranged in two rows at a fixed interval on two rings, or one or two rows of the ventilation hole section 24 may be arranged discontinuously or irregularly. When a user holds the mouthpiece in his/her mouth and inhales, outside air is taken into the mainstream smoke through the ventilation hole section 24. However, the ventilation hole section 24 does not have to be provided.
[実施例1]
(たばこ製剤及びたばこシートの調製)
1000gの黄色種たばこを小型式粉砕機(ハイスピードミル、ラボネクト株式会社製)で処理して黄色種たばこの粗砕品(以下「たばこサンプル」という)を得た。得られたたばこサンプル:300gと水:1000gとを切り替え式圧力鍋(クイックエコ、パール金属株式会社製)に投入して混合した後、得られた混合液について下記の条件で、煮沸処理を行った。
圧力:最大圧力90kPa、平均圧力80kPa
温度:119℃
時間:30分
[Example 1]
(Preparation of tobacco formulations and tobacco sheets)
1000 g of flue-cured tobacco was processed in a small grinder (High Speed Mill, manufactured by LabNect Co., Ltd.) to obtain a flue-cured tobacco coarsely ground product (hereinafter referred to as "tobacco sample"). 300 g of the obtained tobacco sample and 1000 g of water were put into a switchable pressure cooker (Quick Eco, manufactured by Pearl Metal Co., Ltd.) and mixed, and the obtained mixture was then boiled under the following conditions.
Pressure: Maximum pressure 90 kPa, average pressure 80 kPa
Temperature: 119°C
Time: 30 minutes
圧力鍋中の上記の煮沸処理後の混合物に対して、1000gの水を加えて混合した後、得られた混合液について下記の条件で、2回目の煮沸処理を行った。
圧力:最大圧力90kPa、平均圧力80kPa
温度:119℃
時間:30分
1000 g of water was added to the mixture after the boiling treatment in the pressure cooker and mixed, and the resulting mixture was then subjected to a second boiling treatment under the following conditions.
Pressure: Maximum pressure 90 kPa, average pressure 80 kPa
Temperature: 119°C
Time: 30 minutes
上記の2回目の煮沸処理後の混合物を35℃まで冷却し、IR水分計(MB45、OHAUS社製)を使用してIR水分測定法に基づいて当該混合物中の水分量を測定したところ、80重量%であった。 The mixture after the second boiling treatment was cooled to 35°C, and the moisture content of the mixture was measured using an IR moisture meter (MB45, OHAUS) based on the IR moisture measurement method, which was 80% by weight.
圧力鍋中の水分量測定後の混合物に対して、グアーガム:15g、CMC(カルボキシメチルセルロース):6g、及びグリセリン:43.5gを加えて混合し、混合液を得た。得られた混合液:800gを採取し、水:800gを加えながら解繊装置(高速分散ハイシアーミキサー、シルバーソン社製)で処理して湿式粉砕を行うとともに抽出処理を実施した。湿式粉砕条件は以下のとおりとした。
回転数:7000rpm
時間:10分
*上記混合液に対して、水:800gを10分間にわたってゆっくりと投入
After measuring the moisture content in the pressure cooker, 15 g of guar gum, 6 g of CMC (carboxymethylcellulose), and 43.5 g of glycerin were added and mixed to obtain a mixed liquid. 800 g of the resulting mixed liquid was sampled, and while adding 800 g of water, it was treated with a defibrator (high-speed dispersion high shear mixer, manufactured by Silverson) to carry out wet pulverization and extraction processing. The wet pulverization conditions were as follows.
Rotational speed: 7000 rpm
Time: 10 minutes * Slowly add 800g of water to the above mixture over a period of 10 minutes.
上記の湿式粉砕・抽出処理により、黄色種たばこに由来する難水溶性物質、黄色種たばこから抽出されたデンプン、及び媒体である水を含む懸濁液(たばこ製剤)が得られた。 The above wet grinding and extraction process produced a suspension (tobacco preparation) containing poorly water-soluble substances derived from flue-cured tobacco, starch extracted from flue-cured tobacco, and water as a medium.
次いで、上記のようにして得られた懸濁液をステンレス板の上に展開して室温にて自然乾燥し、スラリーシート(たばこシート)(厚み:1mm)を製造した。
実施例1のたばこシート中のたばこ原料に由来する成分の含有量として、使用したたばこ原料(たばこサンプル)と外添した成分(グアーガム、CMC、及びグリセリン)との合計の重量に対する、当該たばこ原料の重量の割合を算出したところ、82.3重量%であった。
Next, the suspension obtained as described above was spread on a stainless steel plate and naturally dried at room temperature to produce a slurry sheet (tobacco sheet) (thickness: 1 mm).
The content of components derived from the tobacco raw materials in the tobacco sheet of Example 1 was calculated as the percentage of the weight of the tobacco raw materials to the total weight of the tobacco raw materials used (tobacco sample) and the externally added components (guar gum, CMC, and glycerin), and was found to be 82.3% by weight.
[実施例2]
(たばこ製剤及びたばこシートの調製)
上記[実施例1]で述べたたばこサンプル:300gと水:1000gとを切り替え式圧力鍋(クイックエコ、パール金属株式会社製)に投入して混合した後、得られた混合液について下記の条件で、煮沸処理を行った。当該煮沸処理は2回繰り返して行った。
圧力:最大圧力90kPa、平均圧力80kPa
温度:119℃
時間:30分
[Example 2]
(Preparation of tobacco formulations and tobacco sheets)
300 g of the tobacco sample described in [Example 1] above and 1000 g of water were mixed in a pressure cooker (Quick Eco, manufactured by Pearl Metal Co., Ltd.), and the resulting mixture was boiled under the following conditions. The boiling process was repeated twice.
Pressure: Maximum pressure 90 kPa, average pressure 80 kPa
Temperature: 119°C
Time: 30 minutes
圧力鍋中の上記の煮沸処理後の混合物に対して、1000gの水を加えて混合した後、得られた混合液について下記の条件で、3回目の煮沸処理を行った。
圧力:最大圧力90kPa、平均圧力80kPa
温度:119℃
時間:30分
1000 g of water was added to the mixture after the boiling treatment in the pressure cooker and mixed, and the resulting mixture was then subjected to a third boiling treatment under the following conditions.
Pressure: Maximum pressure 90 kPa, average pressure 80 kPa
Temperature: 119°C
Time: 30 minutes
上記の3回目の煮沸処理後の混合物を25℃まで冷却し、IR水分計(MB45、OHAUS社製)を使用してIR水分測定法に基づいて当該混合物中の水分量を測定したところ、80重量%であった。 The mixture after the third boiling treatment was cooled to 25°C, and the moisture content of the mixture was measured using an IR moisture meter (MB45, OHAUS) based on the IR moisture measurement method, which was 80% by weight.
圧力鍋中の水分量測定後の混合物に対して、グアーガム:15g、CMC(カルボキシメチルセルロース):6g、及びグリセリン:43.5gを加えて混合し、混合液を得た。得られた混合液:800gを採取し、水:800gを加えながら解繊装置(高速分散ハイシアーミキサー、シルバーソン社製)で処理して湿式粉砕を行うとともに抽出処理を実施した。湿式粉砕条件は以下のとおりとした。
回転数:4500rpm
時間:20分
*上記混合液に対して、水:800gを20分間にわたってゆっくりと投入
After measuring the moisture content in the pressure cooker, 15 g of guar gum, 6 g of CMC (carboxymethylcellulose), and 43.5 g of glycerin were added and mixed to obtain a mixed liquid. 800 g of the resulting mixed liquid was sampled, and while adding 800 g of water, it was treated with a defibrator (high-speed dispersion high shear mixer, manufactured by Silverson) to carry out wet grinding and extraction processing. The wet grinding conditions were as follows.
Rotational speed: 4500 rpm
Time: 20 minutes * Slowly add 800g of water to the above mixture over a period of 20 minutes.
上記の湿式粉砕・抽出処理により、黄色種たばこに由来する難水溶性物質、黄色種たばこから抽出されたデンプン、及び媒体である水を含む懸濁液(たばこ製剤)が得られた。 The above wet grinding and extraction process produced a suspension (tobacco preparation) containing poorly water-soluble substances derived from flue-cured tobacco, starch extracted from flue-cured tobacco, and water as a medium.
次いで、上記のようにして得られた懸濁液をステンレス板の上に展開して室温にて自然乾燥し、スラリーシート(たばこシート)(厚み:1mm)を製造した。
実施例2のたばこシート中のたばこ原料に由来する成分の含有量として、使用したたばこ原料(たばこサンプル)と外添した成分(グアーガム、CMC、及びグリセリン)との合計の重量に対する、当該たばこ原料の重量の割合を算出したところ、82.3重量%であった。
Next, the suspension obtained as described above was spread on a stainless steel plate and naturally dried at room temperature to produce a slurry sheet (tobacco sheet) (thickness: 1 mm).
The content of components derived from the tobacco raw materials in the tobacco sheet of Example 2 was calculated as the ratio of the weight of the tobacco raw materials to the total weight of the tobacco raw materials used (tobacco sample) and the externally added components (guar gum, CMC, and glycerin), and was found to be 82.3% by weight.
[比較例]
(たばこ製剤及びたばこシートの調製)
上記[実施例1]で述べたたばこサンプル(粉砕品):300gと水:1000gとをホモジナイザー(ROBOMICS、特殊機化工業株式会社製)にかけてホモジナイズして混合物を得た。得られた混合物:1300gに対して、グリセリンを15g、パルプ(粒子径:900μm(加重平均粒径))):15g、バインダーとしてグアーガム:15gを加えて混合し、懸濁液(たばこ製剤)を得た。得られた懸濁液をステンレス板の上に展開して室温にて自然乾燥し、スラリーシート(たばこシート)(厚み:1mm)を製造した。
比較例のたばこシート中のたばこ原料に由来する成分の含有量として、使用したたばこ原料(たばこサンプル)と外添した成分(グリセリン、パルプ、及びグアーガム)との合計の重量に対する、当該たばこ原料の重量の割合を算出したところ、86.9重量%であった。
[Comparative Example]
(Preparation of tobacco formulations and tobacco sheets)
300 g of the tobacco sample (ground product) described in [Example 1] above and 1000 g of water were homogenized using a homogenizer (ROBOMICS, manufactured by Tokushu Kika Kogyo Co., Ltd.) to obtain a mixture. 15 g of glycerin, 15 g of pulp (particle size: 900 μm (weighted average particle size)), and 15 g of guar gum as a binder were added to 1300 g of the obtained mixture and mixed to obtain a suspension (tobacco preparation). The obtained suspension was spread on a stainless steel plate and naturally dried at room temperature to produce a slurry sheet (tobacco sheet) (thickness: 1 mm).
The content of components derived from the tobacco raw materials in the tobacco sheet of the comparative example was calculated as the percentage of the weight of the tobacco raw materials to the total weight of the tobacco raw materials used (tobacco sample) and the externally added components (glycerin, pulp, and guar gum), and was found to be 86.9% by weight.
(1)難水溶性物質の粒子径の測定
上記実施例1の(たばこ製剤及びたばこシートの調製)により得られた懸濁液:2.5g(固形分重量で1g)を秤量し、試料用懸濁液とした。また、上記実施例1及び比較例の(たばこ製剤及びたばこシートの調製)により得られた各スラリーシートの一部を切り取り、1gの試料用スラリーシートを得た。
これらの実施例1の試料用懸濁液:2.5g(固形分重量で1g)並びに実施例1及び比較例の試料用スラリーシート:1gそれぞれに対して、水を40ml加えた後、80℃下にて30分加熱して混合液を得た。得られた混合液を、遠心分離機(冷却遠心機、KUBOTA社製)により、5530G、5分の条件にて遠心分離し、上澄みを除去して沈殿物:0.5gを得た。
得られた0.5gの沈殿物に対して、水を40ml加えた後、80℃下にて30分加熱して混合液を得た。得られた混合液を、遠心分離機(冷却遠心機、KUBOTA社製)により、5530G、5分の条件にて遠心分離し、上澄みを除去して沈殿物:0.4gを得た。得られた0.4gの沈殿物に対して、上記と同様にして、水の添加、加熱・混合、遠心分離、及び上澄みの除去の各工程をさらに2回繰り返して行い、沈殿物:0.3gを得た。
得られた0.3gの沈殿物に対して、95%エタノール水溶液を40ml加えた後、混合して、当該沈殿物の分散液を得た。得られた分散液を湿式粒径測定装置(HORIBA Partica 960、株式会社堀場製作所)により測定し、得られた粒子径(D90)の値を難水溶性物質の粒子径(一次粒子径)の測定値とした。結果を表1に示す。
(1) Measurement of particle size of poorly water-soluble substance 2.5 g (1 g solids weight) of the suspension obtained in Example 1 (Preparation of tobacco formulation and tobacco sheet) was weighed out and used as a sample suspension. A part of each of the slurry sheets obtained in Example 1 and Comparative Example (Preparation of tobacco formulation and tobacco sheet) was cut out to obtain 1 g of sample slurry sheets.
40 ml of water was added to 2.5 g (1 g solids weight) of the sample suspension of Example 1 and 1 g of the sample slurry sheets of Example 1 and Comparative Example, and then the mixture was heated at 80° C. for 30 minutes to obtain a mixture. The mixture was centrifuged at 5530 G for 5 minutes using a centrifuge (refrigerated centrifuge, manufactured by KUBOTA Corporation), and the supernatant was removed to obtain 0.5 g of precipitate.
To the resulting 0.5 g of precipitate, 40 ml of water was added, and the mixture was heated at 80° C. for 30 minutes to obtain a mixture. The mixture was centrifuged at 5530 G for 5 minutes using a centrifuge (refrigerated centrifuge, manufactured by KUBOTA) and the supernatant was removed to obtain 0.4 g of precipitate. The steps of adding water, heating and mixing, centrifugation, and removing the supernatant were repeated twice more in the same manner as above to obtain 0.3 g of precipitate.
40 ml of 95% ethanol aqueous solution was added to 0.3 g of the precipitate obtained, and then mixed to obtain a dispersion of the precipitate. The resulting dispersion was measured using a wet particle size measuring device (HORIBA Partica 960, Horiba, Ltd.), and the obtained particle size (D90) value was taken as the measured particle size (primary particle size) of the poorly water-soluble substance. The results are shown in Table 1.
(2)水の含有量の測定
上記実施例1及び2の(たばこ製剤及びたばこシートの調製)により得られた懸濁液(たばこ製剤)について、IR水分計(MB45、OHAUS社製)を使用してIR水分測定法に基づいて、たばこ製剤中の水の含有量を測定した。結果を表1に示す。
(2) Measurement of water content The water content in the suspension (tobacco formulation) obtained in Examples 1 and 2 (Preparation of tobacco formulation and tobacco sheet) was measured using an IR moisture meter (MB45, OHAUS) based on the IR moisture measurement method. The results are shown in Table 1.
(3)難水溶性物質の含有量の測定
上記実施例1及び2の(たばこ製剤及びたばこシートの調製)により得られた懸濁液:25g(固形分重量で10g)を秤量し、試料用懸濁液とした。これらの実施例1及び2の各試料用懸濁液:2.5g(固形分重量で1g)に、80℃の温水を40ml加えて、30分撹拌し、遠心分離機(冷却遠心機、KUBOTA社製)により、5530G、5分の条件にて遠心処理を行った。遠心処理後、上澄みを除去して沈殿物:0.5gを得た。得られた0.5gの沈殿物に対して、上記と同様にして、温水の添加、混合、遠心分離、及び上澄みの除去の各工程をさらに3回繰り返して行い、沈殿物を取得し、得られた沈殿物を80℃の条件で30分間乾燥処理にかけ、得られた乾燥物の重量を測定した。そして、上記の使用した懸濁液の固形分重量(1g)に対する、得られた乾燥物の重量の割合(重量%)を算出し、得られた値を懸濁液中の難水溶性物質の含有量(重量%)(固形分換算)とした。結果を表1に示す。
懸濁液から媒体である水のみが除かれることによってスラリーシートが形成されるため、上記のようにして得られた懸濁液中の難水溶性物質の含有量(重量%)(固形分換算)は、スラリーシート中の難水溶性物質の含有量(重量%)に等しいとみなせる。
(3) Measurement of content of poorly water-soluble substances 25 g (10 g solids) of the suspension obtained by the above Examples 1 and 2 (preparation of tobacco formulation and tobacco sheet) was weighed and used as a sample suspension. 40 ml of 80°C hot water was added to 2.5 g (1 g solids) of each sample suspension of Examples 1 and 2, and the mixture was stirred for 30 minutes and centrifuged at 5530G for 5 minutes using a centrifuge (cooled centrifuge, manufactured by KUBOTA). After centrifugation, the supernatant was removed to obtain 0.5 g of precipitate. The steps of adding hot water, mixing, centrifugation, and removing the supernatant were repeated three more times for the obtained 0.5 g of precipitate in the same manner as above to obtain a precipitate, and the obtained precipitate was dried for 30 minutes at 80°C, and the weight of the obtained dried product was measured. The ratio (wt%) of the weight of the obtained dried material to the weight (1 g) of the solid content of the suspension used above was calculated, and the obtained value was taken as the content (wt%) of the poorly water-soluble substance in the suspension (converted into solid content). The results are shown in Table 1.
Since the slurry sheet is formed by removing only the water medium from the suspension, the content (wt %) of the poorly water-soluble substance in the suspension obtained as described above (converted into solids content) can be regarded as equal to the content (wt %) of the poorly water-soluble substance in the slurry sheet.
(4)デンプンの含有量の測定
上記実施例1及び比較例の(たばこ製剤及びたばこシートの調製)により得られた懸濁液:2.5g(固形分重量で1g)を秤量し、試料用懸濁液とした。これらの実施例1及び比較例の各試料用懸濁液:2.5g(固形分重量で1g)を、ホモジナイザー(ROBOMICS、特殊機化工業株式会社製)にかけてホモジナイズして粉砕して粉状物を得た。得られた粉状物を100mg測り取り、15ml容遠心管(SUMILON(登録商標)、住友ベークライト株式会社製)の中に入れ、常温のMilliQ水:10mlを添加した後、常温下にて超音波装置(BRANSONIC、日本エマソン株式会社製)を使用して10分間超音波をかけて抽出処理を行い、混合液を得た。得られた混合液を、遠心分離機(冷却遠心機、KUBOTA社製)により、4℃、8000rpmの条件で5分間、遠心処理を行った。遠心処理後、上澄みを除去して沈殿物を得た。得られた沈殿物へジメチルスルホキシド(DMSO)7mlを加えてボルテックスミキサーにて撹拌し、懸濁液を得た。得られた懸濁液に対して、100℃で5分間加熱処理(抽出処理)を行うことで沈殿物中のデンプンをDMSO中に溶出させた。抽出処理後の懸濁液を氷水で急冷した後、上述の遠心分離機により、3000G、5分間、遠心処理を行った。遠心処理後、上澄みを5ml採取し、50mlメスフラスコに入れた。そして、メスフラスコ中の上澄み液に対して、上記と同様にして、100℃での5分間の抽出処理、氷水による急冷、3000Gでの5分間の遠心処理、及び上澄み5mlの採取・50mlメスフラスコへの投入の各工程をさらに3回繰り返して行い、デンプンが溶解したDMSO:20ml(メスフラスコに入った状態)を得た。
得られたDMSO:20mlに対してMilliQ水を加えて100mlにメスアップして撹拌した後、得られたサンプル100mlをガラス製の試験管へ移した。試験管中のサンプルに対して、5%フェノール溶液:500μlを入れた後、濃硫酸:2.5mlをゆっくりと投入することにより、サンプル中のデンプンを単糖へ分解させた。その後、得られた溶液をボルテックスミキサーにて撹拌した後、20分間静置した。静置後の試験管中の溶液について、分光光度計(SP-300、株式会社オプティマ製)を使用して波長490nmにて吸光度を測定した。検量線にはグルコースを5%フェノール溶液に溶解させたものを用い、同様に吸光度を分析した。当該グルコースの濃度は各々、0μg/ml、10μg/ml、20μg/ml、50μg/ml、100μg/mlとした。得られた吸光度の測定値及び検量線に基づいて、使用した懸濁液の固形分重量(1g)に対するデンプンの重量の割合(重量%)を算出し、デンプンの含有量(重量%)とした。結果を表1に示す。
懸濁液から媒体である水のみが除かれることによってスラリーシートが形成されるため、上記のようにして得られた懸濁液中のデンプンの含有量(重量%)(固形分換算)は、スラリーシート中のデンプンの含有量(重量%)に等しいとみなせる。
(4) Measurement of starch content The suspension obtained by the above Example 1 and Comparative Example (preparation of tobacco formulation and tobacco sheet): 2.5 g (1 g in solid weight) was weighed and used as a sample suspension. Each sample suspension: 2.5 g (1 g in solid weight) of these Example 1 and Comparative Example was homogenized and pulverized using a homogenizer (ROBOMICS, manufactured by Tokushu Kika Kogyo Co., Ltd.) to obtain a powdery product. 100 mg of the obtained powdery product was weighed and placed in a 15 ml centrifuge tube (SUMILON (registered trademark), manufactured by Sumitomo Bakelite Co., Ltd.), and 10 ml of MilliQ water at room temperature was added, and then ultrasonic waves were applied for 10 minutes at room temperature using an ultrasonic device (BRANSONIC, manufactured by Emerson Japan Co., Ltd.) to perform extraction processing, and a mixed liquid was obtained. The obtained mixed liquid was centrifuged for 5 minutes at 4 ° C. and 8000 rpm using a centrifuge (cooled centrifuge, manufactured by KUBOTA Co., Ltd.). After centrifugation, the supernatant was removed to obtain a precipitate. The precipitate was mixed with 7 ml of dimethyl sulfoxide (DMSO) and stirred with a vortex mixer to obtain a suspension. The resulting suspension was heated (extracted) at 100°C for 5 minutes to dissolve the starch in the precipitate into DMSO. The suspension after the extraction was quenched with ice water, and then centrifuged at 3000G for 5 minutes using the above-mentioned centrifuge. After centrifugation, 5 ml of the supernatant was collected and placed in a 50 ml measuring flask. The supernatant in the measuring flask was then subjected to the same process as above, including extraction at 100°C for 5 minutes, quenching with ice water, centrifugation at 3000G for 5 minutes, and collection and introduction of 5 ml of the supernatant into a 50 ml measuring flask, which were repeated three times to obtain DMSO in which starch was dissolved (in a measuring flask).
MilliQ water was added to the obtained DMSO: 20 ml, and the mixture was made up to 100 ml and stirred, and then 100 ml of the obtained sample was transferred to a glass test tube. 500 μl of 5% phenol solution was added to the sample in the test tube, and then 2.5 ml of concentrated sulfuric acid was slowly added to decompose the starch in the sample into monosaccharides. The obtained solution was then stirred with a vortex mixer and allowed to stand for 20 minutes. The absorbance of the solution in the test tube after standing was measured at a wavelength of 490 nm using a spectrophotometer (SP-300, manufactured by Optima Co., Ltd.). For the calibration curve, glucose was dissolved in 5% phenol solution, and the absorbance was analyzed in the same manner. The glucose concentrations were 0 μg/ml, 10 μg/ml, 20 μg/ml, 50 μg/ml, and 100 μg/ml, respectively. Based on the obtained absorbance measurements and the calibration curve, the ratio (wt%) of the weight of starch to the weight (1 g) of the solid content of the suspension used was calculated, and this was taken as the starch content (wt%). The results are shown in Table 1.
Since the slurry sheet is formed by removing only the water medium from the suspension, the starch content (wt %) (solid content equivalent) in the suspension obtained as described above can be considered to be equal to the starch content (wt %) in the slurry sheet.
上記[実施例1]及び[実施例2]の結果より、実施例1及び2のたばこ製剤により、パルプ等の他の難水溶性物質の原料を外添しないでもたばこシートを製造できることがわかった。実施例1及び2のたばこ製剤を得る際には、煮沸処理によりたばこ原料に含まれていたデンプンが抽出され、たばこ原料の残渣として難水溶性物質が得られる。このようにして得られたたばこ原料に由来する難水溶性物質が、他の難水溶性物質の代わりにたばこシートの成形性や強度を向上させるため、他の難水溶性物質を外添しないでもたばこシートを形成することができる。実施例1及び2のたばこ製剤では、パルプ等の他の難水溶性物質の原料を外添する必要がないため、その分だけ、たばこ原料やグリセリンの添加量を増やすことが可能となり、たばこ製剤及びたばこシートの設計の自由度が増す。
また、表1に示すように、難水溶性物質の粒子径(μm)について、実施例1の懸濁液では22.4μm、スラリーシートでは24.2μmの測定結果となり、粉砕・抽出処理を経て極めて小さくなっていることがわかった。実施例1では、このように難水溶性物質の粒子径が小さくなっているため、たばこの粒子同士を接着する表面積が増加してスラリーシートの強度を向上できていると考えられる。
From the results of [Example 1] and [Example 2] above, it was found that the tobacco formulations of Examples 1 and 2 can be used to produce tobacco sheets without adding other poorly water-soluble raw materials such as pulp. When obtaining the tobacco formulations of Examples 1 and 2, starch contained in the tobacco raw materials is extracted by boiling treatment, and poorly water-soluble substances are obtained as residues of the tobacco raw materials. The poorly water-soluble substances derived from the tobacco raw materials obtained in this manner improve the moldability and strength of the tobacco sheet in place of other poorly water-soluble substances, so that the tobacco sheet can be formed without adding other poorly water-soluble substances. Since the tobacco formulations of Examples 1 and 2 do not require the external addition of other poorly water-soluble raw materials such as pulp, it is possible to increase the amount of tobacco raw materials and glycerin added, which increases the freedom of design of the tobacco formulation and tobacco sheet.
In addition, as shown in Table 1, the particle size (μm) of the poorly water-soluble substance was measured to be 22.4 μm for the suspension in Example 1 and 24.2 μm for the slurry sheet, indicating that the particle size was extremely small after the grinding and extraction process. In Example 1, the particle size of the poorly water-soluble substance was thus small, which is believed to increase the surface area that bonds tobacco particles together and improve the strength of the slurry sheet.
一方、比較例のたばこ製剤は、たばこシートを製造するために難水溶性物質であるパルプが外添されている。仮に比較例のたばこ製剤にパルプを外添しなかった場合、シート形状を維持できないため、たばこシートを製造できない。比較例では、粉砕・抽出処理を経ていないためにたばこ原料に由来する難水溶性物質の粒子径が大きくなる。そのために、たばこの粒子同士を接着する表面積が十分ではなく、パルプを添加してスラリーシートの強度を向上させる必要がある。 On the other hand, the tobacco formulation of the comparative example has pulp, a poorly water-soluble substance, added to it in order to produce a tobacco sheet. If pulp were not added to the tobacco formulation of the comparative example, the sheet shape would not be able to be maintained, and tobacco sheet would not be able to be produced. In the comparative example, the particle size of the poorly water-soluble substance derived from the tobacco raw materials is large because the product does not go through the crushing and extraction process. As a result, the surface area for bonding the tobacco particles together is insufficient, and pulp must be added to improve the strength of the slurry sheet.
また、表1の結果より、実施例2の懸濁液中の難水溶性物質の含有量(12重量%)は、実施例1の懸濁液中の難水溶性物質の含有量(30重量%)より小さくなっていることがわかった。この点について、実施例2では実施例1よりも煮沸処理の回数が多いため、たばこ原料からデンプン等の成分をより多く抽出でき、その結果、多く抽出された分だけ難水溶性物質として測定される量が減ったと考えられる。実施例1及び2の結果より、煮沸処理の条件を変更することにより、抽出されるデンプン等の成分の量を制御できることがわかった。 The results in Table 1 also show that the content of poorly water-soluble substances in the suspension of Example 2 (12% by weight) is lower than the content of poorly water-soluble substances in the suspension of Example 1 (30% by weight). In this regard, it is believed that because the boiling treatment was performed more times in Example 2 than in Example 1, more components such as starch could be extracted from the tobacco raw material, and as a result, the amount measured as poorly water-soluble substances decreased accordingly. The results of Examples 1 and 2 show that the amount of extracted components such as starch can be controlled by changing the conditions of the boiling treatment.
さらに、表1の結果より、実施例1の懸濁液中のデンプンの含有量は3.04重量%であり、比較例の懸濁液中のデンプンの含有量:2.47重量%より高い値となっていることが確認できた。これは、煮沸処理を行っていない比較例の懸濁液に比べて、実施例1の懸濁液は、煮沸処理を行っている分だけより多くのデンプンがたばこ原料から抽出され懸濁液中に放出されたためと思われる。実施例1のように懸濁液中に含まれるデンプンの量が多いと、当該デンプンが難水溶性物質同士を接合するバインダーとして機能するために、より強度に優れたたばこシートを製造することができる。 Furthermore, from the results in Table 1, it was confirmed that the starch content in the suspension of Example 1 was 3.04% by weight, which is higher than the starch content in the suspension of the Comparative Example, which was 2.47% by weight. This is thought to be because, compared to the suspension of the Comparative Example, which was not subjected to a boiling treatment, the suspension of Example 1 was subjected to a boiling treatment, and therefore more starch was extracted from the tobacco raw material and released into the suspension. When the suspension contains a large amount of starch, as in Example 1, the starch functions as a binder that bonds poorly water-soluble substances together, making it possible to produce a tobacco sheet with greater strength.
以上のように、本発明のたばこ製剤は、たばこ原料を使用し、他の難水溶性物質の原料を外添しないでもたばこシートを製造できる。 As described above, the tobacco formulation of the present invention uses tobacco raw materials and can produce tobacco sheets without the external addition of other poorly water-soluble substance raw materials.
10 加熱装置
11 ボディ
12 ヒータ
20 非燃焼加熱喫煙物品
20A 喫煙用セグメント
20B 連結部
20C フィルター部
21 喫煙用組成物シートまたはこれに由来する材料
22 ラッパー
23 紙管
24 通気孔部
25 第1セグメント
25a 第1充填層
25b インナープラグラッパー
26 第2セグメント
26a 第2充填層
26b インナープラグラッパー
27 アウタープラグラッパー
28 ラッパー
10 heating device 11 body 12 heater
20 Non-combustion heating smoking article 20A Smoking segment 20B Connecting part 20C Filter part
21 Smoking composition sheet or material derived therefrom 22 Wrapper 23 Paper tube 24 Ventilation hole portion 25 First segment 25a First filling layer 25b Inner plug wrapper 26 Second segment 26a Second filling layer 26b Inner plug wrapper 27 Outer plug wrapper 28 Wrapper
Claims (20)
(2)前記たばこ原料又は他のたばこ原料から抽出されたデンプン、及び
(3)媒体
を含むたばこ製剤。 (1) Poorly water-soluble substances derived from tobacco raw materials,
(2) a starch extracted from said tobacco material or from other tobacco materials; and (3) a vehicle.
(2’)前記たばこ原料又は他のたばこ原料から抽出されたデンプン
を含むたばこシート。 A tobacco sheet comprising: (1') a poorly water-soluble substance derived from a tobacco raw material; and (2') a starch extracted from the tobacco raw material or another tobacco raw material.
前記たばこ製剤を基材の上に展開し、そして乾燥させる工程を備える、請求項2~15のいずれか1つに記載のたばこシートの製造方法。 A method for producing a tobacco sheet according to any one of claims 2 to 15, comprising the steps of: preparing the tobacco formulation by the method according to claim 19; and spreading the tobacco formulation on a substrate and drying it.
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| JP2024550962A JPWO2024079809A1 (en) | 2022-10-12 | 2022-10-12 | |
| EP22962029.9A EP4602930A1 (en) | 2022-10-12 | 2022-10-12 | Tobacco formulation, tobacco sheet, tobacco filling material, smoking article, tobacco formulation production method, and tobacco sheet production method |
| PCT/JP2022/038001 WO2024079809A1 (en) | 2022-10-12 | 2022-10-12 | Tobacco formulation, tobacco sheet, tobacco filling material, smoking article, tobacco formulation production method, and tobacco sheet production method |
| KR1020257014479A KR20250074675A (en) | 2022-10-12 | 2022-10-12 | Tobacco preparations, tobacco sheets, tobacco fillers, smoking products, methods for making tobacco preparations, and methods for making tobacco sheets |
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| PCT/JP2022/038001 WO2024079809A1 (en) | 2022-10-12 | 2022-10-12 | Tobacco formulation, tobacco sheet, tobacco filling material, smoking article, tobacco formulation production method, and tobacco sheet production method |
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| EP (1) | EP4602930A1 (en) |
| JP (1) | JPWO2024079809A1 (en) |
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Citations (7)
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| EP0565360A2 (en) | 1992-04-09 | 1993-10-13 | Philip Morris Products Inc. | Reconstituted tabacco sheets and methods for producing and using the same |
| JP2015506711A (en) * | 2012-02-10 | 2015-03-05 | アール・ジエイ・レイノルズ・タバコ・カンパニー | Multi-layer smokeless tobacco composition |
| WO2016013946A1 (en) | 2014-07-23 | 2016-01-28 | Instytut Biopolimerow I Włokien Chemicznych | Method of preparing cellulose nano-fibres from stalks of annual plants |
| WO2016050471A1 (en) | 2014-09-30 | 2016-04-07 | Philip Morris Products S.A. | Homogenized tobacco material and method of production of homogenized tobacco material |
| US20170079325A1 (en) | 2014-05-21 | 2017-03-23 | Philip Morris Products S.A. | Inductively heatable tobacco product |
| WO2017089589A1 (en) | 2015-11-27 | 2017-06-01 | Philip Morris Products S.A. | Homogenized tobacco material production line and method for inline production of homogenized tobacco material |
| JP2021509270A (en) * | 2017-12-29 | 2021-03-25 | フィリップ・モーリス・プロダクツ・ソシエテ・アノニム | Methods for the preparation of sheets containing homogenized alkaloid-containing materials, and aerosol-forming articles containing components prepared from this method. |
Family Cites Families (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| ES2545532T3 (en) | 2005-01-06 | 2015-09-11 | Japan Tobacco Inc. | Composition of carbonaceous heat source for a non-combustible type smoking article |
| CN110236218B (en) | 2014-09-30 | 2022-01-11 | 菲利普莫里斯生产公司 | Method for producing homogenized tobacco material |
| US10196778B2 (en) | 2017-03-20 | 2019-02-05 | R.J. Reynolds Tobacco Company | Tobacco-derived nanocellulose material |
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2022
- 2022-10-12 JP JP2024550962A patent/JPWO2024079809A1/ja active Pending
- 2022-10-12 WO PCT/JP2022/038001 patent/WO2024079809A1/en not_active Ceased
- 2022-10-12 KR KR1020257014479A patent/KR20250074675A/en active Pending
- 2022-10-12 EP EP22962029.9A patent/EP4602930A1/en active Pending
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| EP0565360A2 (en) | 1992-04-09 | 1993-10-13 | Philip Morris Products Inc. | Reconstituted tabacco sheets and methods for producing and using the same |
| JP2015506711A (en) * | 2012-02-10 | 2015-03-05 | アール・ジエイ・レイノルズ・タバコ・カンパニー | Multi-layer smokeless tobacco composition |
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| WO2016013946A1 (en) | 2014-07-23 | 2016-01-28 | Instytut Biopolimerow I Włokien Chemicznych | Method of preparing cellulose nano-fibres from stalks of annual plants |
| WO2016050471A1 (en) | 2014-09-30 | 2016-04-07 | Philip Morris Products S.A. | Homogenized tobacco material and method of production of homogenized tobacco material |
| WO2017089589A1 (en) | 2015-11-27 | 2017-06-01 | Philip Morris Products S.A. | Homogenized tobacco material production line and method for inline production of homogenized tobacco material |
| JP2021509270A (en) * | 2017-12-29 | 2021-03-25 | フィリップ・モーリス・プロダクツ・ソシエテ・アノニム | Methods for the preparation of sheets containing homogenized alkaloid-containing materials, and aerosol-forming articles containing components prepared from this method. |
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| EP4602930A1 (en) | 2025-08-20 |
| JPWO2024079809A1 (en) | 2024-04-18 |
| KR20250074675A (en) | 2025-05-27 |
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