WO2014175399A1 - 香喫味成分を含む嗜好品の構成要素の製造方法及び香喫味成分を含む嗜好品の構成要素 - Google Patents
香喫味成分を含む嗜好品の構成要素の製造方法及び香喫味成分を含む嗜好品の構成要素 Download PDFInfo
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- WO2014175399A1 WO2014175399A1 PCT/JP2014/061617 JP2014061617W WO2014175399A1 WO 2014175399 A1 WO2014175399 A1 WO 2014175399A1 JP 2014061617 W JP2014061617 W JP 2014061617W WO 2014175399 A1 WO2014175399 A1 WO 2014175399A1
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- WIPO (PCT)
- Prior art keywords
- tobacco
- tobacco source
- component
- flavor
- predetermined solvent
- Prior art date
Links
- 239000004615 ingredient Substances 0.000 title claims abstract description 17
- 239000000470 constituent Substances 0.000 title claims abstract description 7
- 238000000034 method Methods 0.000 title claims description 25
- 241000208125 Nicotiana Species 0.000 claims abstract description 166
- 235000002637 Nicotiana tabacum Nutrition 0.000 claims abstract description 166
- 239000002904 solvent Substances 0.000 claims abstract description 111
- 239000003513 alkali Substances 0.000 claims abstract description 21
- 238000004519 manufacturing process Methods 0.000 claims abstract description 21
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- 235000019634 flavors Nutrition 0.000 claims description 117
- 238000011282 treatment Methods 0.000 claims description 36
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- SNICXCGAKADSCV-JTQLQIEISA-N (-)-Nicotine Chemical compound CN1CCC[C@H]1C1=CC=CN=C1 SNICXCGAKADSCV-JTQLQIEISA-N 0.000 description 32
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- KRKNYBCHXYNGOX-UHFFFAOYSA-N citric acid Chemical compound OC(=O)CC(O)(C(O)=O)CC(O)=O KRKNYBCHXYNGOX-UHFFFAOYSA-N 0.000 description 6
- 239000003571 electronic cigarette Substances 0.000 description 6
- QGZKDVFQNNGYKY-UHFFFAOYSA-O Ammonium Chemical compound [NH4+] QGZKDVFQNNGYKY-UHFFFAOYSA-O 0.000 description 4
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 4
- 229910052799 carbon Inorganic materials 0.000 description 4
- 238000000605 extraction Methods 0.000 description 4
- 150000007857 hydrazones Chemical class 0.000 description 4
- 239000012535 impurity Substances 0.000 description 4
- 230000001965 increasing effect Effects 0.000 description 4
- WEVYAHXRMPXWCK-UHFFFAOYSA-N Acetonitrile Chemical compound CC#N WEVYAHXRMPXWCK-UHFFFAOYSA-N 0.000 description 3
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 3
- 238000011276 addition treatment Methods 0.000 description 3
- 229930013930 alkaloid Natural products 0.000 description 3
- 150000003797 alkaloid derivatives Chemical class 0.000 description 3
- 238000005185 salting out Methods 0.000 description 3
- LENZDBCJOHFCAS-UHFFFAOYSA-N tris Chemical compound OCC(N)(CO)CO LENZDBCJOHFCAS-UHFFFAOYSA-N 0.000 description 3
- 238000009423 ventilation Methods 0.000 description 3
- UOXGDFZIBNLXMV-UHFFFAOYSA-N 2-(2,4-dinitrophenyl)pyrazine Chemical compound [N+](=O)([O-])C1=C(C=CC(=C1)[N+](=O)[O-])C1=NC=CN=C1 UOXGDFZIBNLXMV-UHFFFAOYSA-N 0.000 description 2
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 2
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- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- PEDCQBHIVMGVHV-UHFFFAOYSA-N Glycerine Chemical compound OCC(O)CO PEDCQBHIVMGVHV-UHFFFAOYSA-N 0.000 description 2
- 235000005135 Micromeria juliana Nutrition 0.000 description 2
- NBIIXXVUZAFLBC-UHFFFAOYSA-N Phosphoric acid Chemical compound OP(O)(O)=O NBIIXXVUZAFLBC-UHFFFAOYSA-N 0.000 description 2
- 241000246354 Satureja Species 0.000 description 2
- 235000007315 Satureja hortensis Nutrition 0.000 description 2
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 2
- IKHGUXGNUITLKF-XPULMUKRSA-N acetaldehyde Chemical compound [14CH]([14CH3])=O IKHGUXGNUITLKF-XPULMUKRSA-N 0.000 description 2
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- BWHMMNNQKKPAPP-UHFFFAOYSA-L potassium carbonate Chemical compound [K+].[K+].[O-]C([O-])=O BWHMMNNQKKPAPP-UHFFFAOYSA-L 0.000 description 2
- TYJJADVDDVDEDZ-UHFFFAOYSA-M potassium hydrogencarbonate Chemical compound [K+].OC([O-])=O TYJJADVDDVDEDZ-UHFFFAOYSA-M 0.000 description 2
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- UFTFJSFQGQCHQW-UHFFFAOYSA-N triformin Chemical compound O=COCC(OC=O)COC=O UFTFJSFQGQCHQW-UHFFFAOYSA-N 0.000 description 2
- BJEPYKJPYRNKOW-REOHCLBHSA-N (S)-malic acid Chemical compound OC(=O)[C@@H](O)CC(O)=O BJEPYKJPYRNKOW-REOHCLBHSA-N 0.000 description 1
- XVMSFILGAMDHEY-UHFFFAOYSA-N 6-(4-aminophenyl)sulfonylpyridin-3-amine Chemical compound C1=CC(N)=CC=C1S(=O)(=O)C1=CC=C(N)C=N1 XVMSFILGAMDHEY-UHFFFAOYSA-N 0.000 description 1
- 241000208134 Nicotiana rustica Species 0.000 description 1
- 244000061176 Nicotiana tabacum Species 0.000 description 1
- PQVFSULCPVMPFH-UHFFFAOYSA-N [N+](=O)([O-])C1=C(C=CC(=C1)[N+](=O)[O-])C=1C(=NC=CN1)CC#N Chemical compound [N+](=O)([O-])C1=C(C=CC(=C1)[N+](=O)[O-])C=1C(=NC=CN1)CC#N PQVFSULCPVMPFH-UHFFFAOYSA-N 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 230000002411 adverse Effects 0.000 description 1
- BJEPYKJPYRNKOW-UHFFFAOYSA-N alpha-hydroxysuccinic acid Natural products OC(=O)C(O)CC(O)=O BJEPYKJPYRNKOW-UHFFFAOYSA-N 0.000 description 1
- 229910000147 aluminium phosphate Inorganic materials 0.000 description 1
- 229910021529 ammonia Inorganic materials 0.000 description 1
- 229910052786 argon Inorganic materials 0.000 description 1
- 238000006757 chemical reactions by type Methods 0.000 description 1
- 238000002485 combustion reaction Methods 0.000 description 1
- 235000009508 confectionery Nutrition 0.000 description 1
- 238000011109 contamination Methods 0.000 description 1
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- 125000004185 ester group Chemical group 0.000 description 1
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- 210000000214 mouth Anatomy 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- XKLJHFLUAHKGGU-UHFFFAOYSA-N nitrous amide Chemical compound ON=N XKLJHFLUAHKGGU-UHFFFAOYSA-N 0.000 description 1
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Images
Classifications
-
- A—HUMAN NECESSITIES
- A24—TOBACCO; CIGARS; CIGARETTES; SIMULATED SMOKING DEVICES; SMOKERS' REQUISITES
- A24B—MANUFACTURE OR PREPARATION OF TOBACCO FOR SMOKING OR CHEWING; TOBACCO; SNUFF
- A24B15/00—Chemical features or treatment of tobacco; Tobacco substitutes, e.g. in liquid form
- A24B15/18—Treatment of tobacco products or tobacco substitutes
- A24B15/24—Treatment of tobacco products or tobacco substitutes by extraction; Tobacco extracts
-
- A—HUMAN NECESSITIES
- A24—TOBACCO; CIGARS; CIGARETTES; SIMULATED SMOKING DEVICES; SMOKERS' REQUISITES
- A24B—MANUFACTURE OR PREPARATION OF TOBACCO FOR SMOKING OR CHEWING; TOBACCO; SNUFF
- A24B13/00—Tobacco for pipes, for cigars, e.g. cigar inserts, or for cigarettes; Chewing tobacco; Snuff
-
- 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
- A24B15/167—Chemical features of tobacco products or tobacco substitutes of tobacco substitutes in liquid or vaporisable form, e.g. liquid compositions for electronic cigarettes
-
- 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
- A24B15/24—Treatment of tobacco products or tobacco substitutes by extraction; Tobacco extracts
- A24B15/241—Extraction of specific substances
-
- 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
- A24B15/24—Treatment of tobacco products or tobacco substitutes by extraction; Tobacco extracts
- A24B15/26—Use of organic solvents for extraction
Definitions
- the present invention relates to a method for producing a component of a luxury product including a flavor ingredient and a component of the luxury product including a flavor component.
- a technique for containing a flavor ingredient for example, an alkaloid containing a nicotine ingredient
- a technique for utilizing the tobacco source itself as a flavor source, or extracting a flavor ingredient from the tobacco source to obtain a flavor source Techniques for supporting a substrate are known.
- a first feature of the present invention is a method for producing a component of a luxury product containing a flavor component, wherein the flavor component is released from an alkali-treated tobacco source into the gas phase; Step B for capturing the flavor component in the predetermined solvent by bringing the flavor component released into the liquid into contact with the predetermined solvent, which is a liquid substance at room temperature, and adding the predetermined solvent to the component
- the gist is to include the step C.
- the gist of the second feature of the present invention is that it is a component of a luxury product containing a flavor ingredient produced by the above-described production method.
- FIG. 1 is a diagram illustrating an example of a luxury product (tobacco product) manufactured by the manufacturing method according to the first embodiment.
- FIG. 2 is a flowchart showing the manufacturing method according to the first embodiment.
- FIG. 3 is a diagram illustrating an example of a bubbling apparatus for performing bubbling into a predetermined solvent performed for the manufacturing method according to the first embodiment.
- FIG. 4 is a flowchart illustrating the manufacturing method according to the first modification.
- FIG. 5 is a diagram for explaining the first experiment.
- FIG. 6 is a diagram for explaining the first experiment.
- FIG. 7 is a diagram for explaining the first experiment.
- FIG. 8 is a diagram for explaining the first experiment.
- FIG. 9 is a diagram for explaining the second experiment.
- FIG. 10 is a diagram for explaining the second experiment.
- Such a flavor suction tool may be a carbon heat source type flavor suction tool 1 as shown in FIG. 1, an electronic cigarette type flavor suction tool, or a chemical reaction type flavor suction tool. May be.
- a nicotine component is taken as an example of a flavor component that contributes to tobacco flavor.
- the nicotine component is used as an indicator of the flavor component.
- the flavor suction tool 1 includes a carbon heat source 3, a flavor generation source 4, a filter 5, a paper tube holder 2 that holds the carbon heat source 3, the flavor generation source 4, and the filter 5. May be provided.
- the flavor suction tool 1 As a constituent element of the flavor suction tool 1, a case where at least one of cellulose constituting the carbon heat source 3, the flavor generating source 4, the filter 5, and the paper tube holder 2 is manufactured will be exemplified.
- step S101 the tobacco source is subjected to an alkali treatment (alkali addition treatment) to release a flavor component from the tobacco source into the gas phase.
- alkali treatment alkali addition treatment
- the tobacco source that has been subjected to alkali treatment is heated to release the flavor component from the tobacco source into the gas phase. According to such a configuration, it is possible to improve the emission efficiency of the flavor component into the gas phase.
- the heating temperature of the tobacco source may be any temperature from room temperature to the thermal decomposition temperature of the tobacco source, and the higher the heating temperature, the higher the efficiency of releasing the flavor components into the gas phase. However, if the heating temperature is too high, the amount of contaminant components released into the gas phase may increase. Considering these points, for example, the heating temperature may be in the range of 60 ° C. to 150 ° C. When the heating temperature of the tobacco source is 60 ° C. or higher, the timing at which a sufficient flavor component is released from the tobacco source can be advanced. On the other hand, when the heating temperature of the tobacco source is less than 150 ° C., the timing at which a contaminant component (for example, tobacco-specific nitrosamine: TSNA) is released from the tobacco source can be delayed.
- a contaminant component for example, tobacco-specific nitrosamine: TSNA
- step S101 it is preferable to perform the process of step S101 in the sealed space.
- the “sealing” is a state in which solid foreign matters can be prevented from being mixed and loss of contents can be prevented in a normal handling, transportation or storage state. According to such a configuration, it is possible to prevent a situation in which the savory component is volatilized out of the system.
- a tobacco raw material or a tobacco extract adjusted to an alkaline pH may be used as such a tobacco source.
- a tobacco raw material or tobacco extract whose pH is adjusted to 8.0 or more, more preferably 9.0 or more may be used as such a tobacco source.
- the tobacco source may be a tobacco raw material such as chopped powder, granule or molded body, or a tobacco extract such as a sheet to which an extract containing a flavor component is added or a freeze-dried powder or gel. Also good.
- tobacco source for example, raw materials of the genus Tobacco such as Nicotiana tabacum and Nicotiana rustica can be used.
- Nicotiana tabacam for example, varieties such as Burley species and yellow species may be used.
- the content of the flavor component in the tobacco source is not particularly limited, but from the viewpoint of the amount of the flavor component released into the gas phase, the content of the flavor component in the tobacco source is preferably as large as possible.
- the particle size of the tobacco source can be any particle size, but the use of a tobacco source having a particle size as small as possible has a higher efficiency of releasing flavor components into the gas phase. If the particle size of the tobacco source is too small, it becomes difficult to handle the tobacco source in the manufacturing process. Considering these points, for example, a tobacco source having a particle diameter of about 0.5 mm to 1.18 mm may be used.
- a tobacco source a product that has been dried after harvesting (Cured tobacco) may be used, or a product that has not been subjected to a drying process (Green tobacco) may be used. Also good.
- a substance added to the tobacco source in the above alkali addition treatment for example, a basic substance such as an aqueous potassium carbonate solution may be sprayed.
- the basic substance to be added has weak basicity.
- the pH of the tobacco source after the alkali addition treatment is preferably alkaline, more preferably 8.0 or more, and within the range of 8.9 to 9.7. More preferably. Therefore, it is preferable to determine the amount of a basic substance such as potassium carbonate to be added to the tobacco source so as to satisfy such a condition.
- step S101 it is preferable to subject the tobacco source to a water treatment. According to such a configuration, it is possible to improve the emission efficiency of the flavor component into the gas phase.
- the tobacco source in the stage before being subjected to step S101, the tobacco source may be subjected to water treatment to increase the moisture content of the tobacco source, and then step S101 may be performed.
- a base such as an aqueous potassium carbonate solution may be used.
- An alkali treatment and a hydration treatment may be performed at the same time by adding an aqueous solution of an organic substance.
- the higher the amount of moisture contained in the tobacco source the higher the efficiency of releasing the flavor components into the gas phase.
- the efficiency of releasing the flavor components into the gas phase is significantly reduced.
- the moisture content of the tobacco source after spraying the alkaline substance is preferably 10% by weight or more, and 30% by weight or more. More preferably it is.
- the upper limit of the moisture content of the tobacco source is not particularly limited. For example, it is preferably 50% by weight or less in order to efficiently heat the tobacco source.
- a cigarette source may be ventilated.
- the aeration time in such aeration treatment varies depending on the apparatus for treating the tobacco source and the amount of the tobacco source, and therefore cannot be specified in general.
- the tobacco source is a 500 g tobacco material
- the ventilation time is Within about 300 minutes.
- the total aeration amount in such aeration treatment cannot be specified because it differs depending on the amount of the cigarette source and the apparatus that treats the cigarette source.
- the ratio of the total ventilation rate to the weight of the tobacco source is about 10 L / g.
- the aeration time is about 300 minutes or less, and the total aeration amount in the aeration treatment is about 4.9 to 5.3 L / g.
- humidified air having a water content of about 80% or saturated water vapor at 80 ° C. may be brought into contact with the tobacco source.
- the air used in the ventilation process may not be saturated water vapor.
- the moisture content of the air used in the aeration treatment does not particularly require humidification of the tobacco raw material 50, for example, so that the moisture contained in the tobacco raw material 50 to which the heat treatment and the aeration treatment are applied falls within a range of less than 50%. May be adjusted.
- the gas used in the aeration process is not limited to air, and may be an inert gas such as nitrogen or argon.
- step S102 the flavor component released in the gas phase is captured by contacting with a predetermined solvent.
- the flavor component released in the gas phase is dissolved in a predetermined solvent, the flavor component released in the gas phase is absorbed in the predetermined solvent, or the flavor flavor released in the gas phase.
- the component is adsorbed in a predetermined solvent.
- the flavor component in the predetermined solvent it is preferable to capture the flavor component in the predetermined solvent by bubbling the flavor component released into the gas phase into the predetermined solvent. Thereby, a sufficient amount of flavor components can be transferred to the predetermined solvent while suppressing the transfer of unnecessary contaminants contained in the tobacco raw material as the tobacco source to the predetermined solvent.
- the predetermined solvent a substance that is liquid at room temperature, for example, glycerin, water, ethanol, polyol, aqueous citric acid solution, oil such as medium chain fatty acid triglyceride, or the like can be used. According to such a configuration, the flavor component can be dissolved in the predetermined solvent.
- the temperature of the predetermined solvent at the start of bubbling is room temperature.
- the lower limit of the normal temperature is, for example, a temperature at which the predetermined solvent does not solidify, preferably 10 ° C.
- the upper limit of normal temperature is 40 degrees C or less, for example.
- the pressure in the container of the alkali treatment apparatus is equal to or lower than normal pressure.
- the upper limit of the pressure inside the container of the alkali treatment apparatus is +0.1 MPa or less in gauge pressure.
- the inside of the container of an alkali treatment apparatus may be a reduced pressure atmosphere. That is, in step S101 and step S102, in a state where a pressure equal to or lower than normal pressure is applied to the tobacco source, the flavor component is released from the tobacco source into the gas phase, and the flavor released into the gas phase by the predetermined solvent. Capture ingredients.
- the pH of the predetermined solvent is preferably lower than the pH of the tobacco source. According to this configuration, the flavor component in the gas phase can be more distributed to the predetermined solvent than the tobacco source.
- FIG. 3 shows an example of a bubbling device 100 for bubbling flavor components released in the gas phase into a predetermined solvent.
- the gas 10 containing the flavor component released in the gas phase in step S ⁇ b> 101 is released into the predetermined solvent 20 through the hole 30 provided in the bubbling device 100, and the gas 10 The flavor component is captured by the predetermined solvent 20.
- the gas 40 containing contaminant components not captured by the predetermined solvent 20 is exhausted outside the bubbling device 100. That is, the pressure applied to the predetermined solvent 20 in step S102 is equal to or lower than normal pressure.
- the contact area between the gas 10 and the predetermined solvent 20 can be increased, and the capture efficiency of flavor components by the predetermined solvent can be improved.
- the predetermined solvent may be cooled in order to suppress an increase in the temperature of the predetermined solvent.
- acquisition efficiency of the flavor component by a predetermined solvent can be improved.
- the lower limit of the normal temperature is, for example, a temperature at which the predetermined solvent does not solidify, preferably 10 ° C. as described above.
- the upper limit of normal temperature is 40 degrees C or less as mentioned above, for example.
- Raschig rings may be arranged to increase the contact area of the flavor component released in the gas phase with respect to the predetermined solvent.
- an arbitrary acid such as malic acid or citric acid may be added to the predetermined solvent in order to suppress re-evaporation of the flavor components supplemented by the predetermined solvent.
- a vacuum concentration treatment, a heat concentration treatment, a salting-out treatment, or the like may be performed.
- a solvent having a lower vapor pressure than the component (for example, water) to be removed it is preferable to use a solvent having a lower vapor pressure than the component (for example, water) to be removed as the predetermined solvent.
- vacuum concentration treatment is performed in a sealed space, there is little contact with air, and there is no need to increase the temperature of the predetermined solvent, so there is little concern about component changes. Therefore, the use of vacuum concentration increases the types of predetermined solvents that can be used.
- the kind of the predetermined solvent that can be used is reduced as compared with the vacuum concentration.
- a predetermined solvent having an ester structure such as MCT (Medium Chain Triglyceride) may not be used.
- salting-out treatment it is possible to separate the flavor components more efficiently than the vacuum concentration treatment.
- the yield of flavor components is about half of the flavor components in the liquid solvent phase / water phase. Is bad.
- salting-out may not occur depending on the ratio of the predetermined solvent, water and flavor components.
- step S103 a predetermined solvent in a state where the flavor component is captured is added to the constituent elements of the flavor suction tool 1 described above.
- a sufficient amount of flavor components are transferred to a predetermined solvent without transferring unnecessary impurities in the tobacco raw material as a tobacco source by a very simple method.
- a predetermined solvent for example, a filter
- the constituent elements for example, a filter
- the flavor component is captured with respect to the tobacco raw material (tobacco raw material residue) after the flavor component is released.
- the predetermined solvent in a state of being present may be applied back.
- the amount of the flavor component (here, nicotine component) contained in the tobacco material after multiplying the tobacco material residue by the predetermined solvent is the tobacco before the flavor component is released. It should be noted that the amount of flavor components contained in the raw material (here, the nicotine component) or less.
- step S103 shown in FIG. 2 the step of adding a predetermined solvent in a state where the flavor component is captured includes step S103A and step S103B.
- Step S103A a tobacco raw material (tobacco raw material residue) after releasing the flavor component in Step S101 is prepared.
- step S103B the predetermined solvent in the state where the flavor component is captured in step S102 is multiplied by the tobacco raw material residue. That is, in the first modification, the component of the luxury product including the flavor ingredient is the tobacco raw material (tobacco raw material residue) after releasing the flavor ingredient in step S101.
- the predetermined solvent to be returned to the tobacco raw material residue may be neutralized.
- the moisture content of the tobacco material before performing the heat treatment is 30% by weight or more, preferably 40% by weight or more, and the moisture content of the tobacco material after the heat treatment is almost completely dry, Specifically, it is preferable to heat the tobacco source until the moisture content of the tobacco source is less than 5% by weight.
- the contaminated component for example, ammonium ions
- impurities such as ammonium ions can be sufficiently removed from the tobacco source. Details of such heat treatment methods are described in the specification of WO2013 / 146592, which is incorporated herein by reference.
- tobacco that suppresses the loss of flavor components while removing impurities (such as ammonium ions) contained in the tobacco material.
- Raw materials can be manufactured.
- the present invention may be applied to a flavor source base material of a luxury product that can be consumed in the oral cavity, such as a gum base, a tablet, an edible film, and a candy, as a component of a luxury product containing a flavor component. Good.
- the present invention produces other suction devices, for example, an electronic cigarette aerosol source (so-called E-liquid), instead of the above-described flavor suction device components, as a component of a luxury product containing a flavor ingredient.
- E-liquid electronic cigarette aerosol source
- the non-volatile component contained in the cigarette source does not move to the predetermined solvent and only the component that volatilizes at about 120 ° C. can be collected in the predetermined solvent, the component collected by the predetermined solvent can be collected from the electronic cigarette. It is effective when used as an aerosol source.
- the term “electronic cigarette” as used herein includes a liquid aerosol source and an electric heater for heating and atomizing the aerosol source, and a non-combustion flavor inhaler or aerosol suction for delivering the aerosol to the user. (For example, aerosol inhaler described in Japanese Patent No. 5196673, aerosol electronic cigarette described in Japanese Patent No. 5385418, etc.).
- the flavor components were captured by a cold trap without using a predetermined solvent.
- the flavor component was supplemented using what connected the Liebig cooling pipe and the Graham cooling pipe.
- the Liebig cooling pipe and the Graham cooling pipe each used tap water as a refrigerant, and the temperature inside the pipe was maintained at about 20 ° C.
- the components released from the cigarette source into the gas phase are cooled while passing through the Liebig and Graham cooling tubes in this order, and the condensed liquid components are collected in the beaker at the outlet of the Graham cooling tube to capture the flavor components. Went.
- Example 1- Experimental conditions according to Example 1- -Type of tobacco source: Tobacco raw material of Burley species-Nicotine content in tobacco source: 4.9% by weight per dry weight of tobacco source -Ammonium ion content in tobacco source: 4545 ⁇ g / g per dry weight of tobacco source ⁇ Amount of tobacco source: 500 g ⁇ Tobacco source particle size: 0.5mm to 1.18mm -PH of tobacco source after alkali treatment: 9.6 -Initial moisture content of tobacco source after alkali treatment: 39% ⁇ 2% -Heating temperature of tobacco source: 120 ° C ⁇ Processing time: 300 min ⁇ Air flow rate during bubbling: 15 L / min -Predetermined solvent type: Glycerin-Predetermined solvent amount: 61 g -Predetermined solvent temperature: 20 ° C
- Example 2- Experimental conditions according to Example 2- -Type of tobacco source: Tobacco raw material of Burley species-Amount of tobacco source: 55 g ⁇ Nicotine content in tobacco sources: 4.9% by weight per dry weight of tobacco sources -Ammonium ion content in tobacco source: 4545 ⁇ g / g per dry weight of tobacco source ⁇ Tobacco source particle size: 0.5mm to 1.18mm -PH of tobacco source after alkali treatment: 9.6 -Initial moisture content of tobacco source after alkali treatment: 39% ⁇ 2% -Heating temperature of tobacco source: 120 ° C ⁇ Processing time: 24 hours ⁇ Air flow rate during bubbling: 1.5 L / min -Predetermined solvent type: Glycerin-Predetermined solvent amount: 7.4 g
- the measurement result of the nicotine component recovery rate is as shown in FIG.
- the measurement results of acetaldehyde, ammonium ions, and pyridine captured by bubbling to a predetermined solvent or condensing by a cooling tube are as shown in FIGS.
- the nicotine component recovery rate is expressed as the weight percent of the nicotine component trapped by bubbling into a predetermined solvent or condensing by a cooling tube when the initial weight of the nicotine component contained in the tobacco source is 100% by weight. ing.
- the acetaldehyde concentration is the weight ratio of the captured nicotine weight, that is, the weight of acetaldehyde when the captured nicotine weight is 1. It is shown as a ratio.
- the ammonium ion concentration and the pyridine concentration are shown as a weight ratio with respect to the captured nicotine weight, that is, a weight ratio of ammonium ion and pyridine when the captured nicotine weight is 1.
- Example 1 had a nicotine recovery rate equal to or higher than that of the comparative example.
- Example 2 which is the same aeration flow rate and processing time as a comparative example can obtain the nicotine recovery rate substantially equivalent to a comparative example.
- Example 1 acetaldehyde and pyridine were substantially zero (less than the detection limit), and the weight ratio of ammonium ions when the weight of nicotine was 1 was less than 1/1000 of the comparative example.
- Example 2 pyridine is substantially zero (less than the detection limit), and the weight ratio of acetaldehyde when the nicotine weight is 1 is less than 1/45 of the comparative example, and the nicotine weight is 1.
- the weight ratio of ammonium ions in the case was less than 1/270 of the comparative example.
- the flavor component here, the nicotine component
- the contaminated components for example, acetaldehyde, ammonium ions and pyridine
- the temperature of the predetermined solvent is a set temperature of a chiller (a constant temperature bath) that controls the temperature of the container that stores the predetermined solvent. It should be noted that the temperature of a given solvent converges about 60 minutes after setting the container on the chiller and starting the temperature control.
- the method was performed in accordance with the German Standardization Organization DIN 10373. That is, 100 mg of a predetermined solvent was collected, 7.5 mL of an 11% aqueous sodium hydroxide solution and 10 mL of hexane were added, and the mixture was extracted by shaking for 60 minutes. After extraction, the supernatant hexane phase was subjected to a gas chromatograph mass spectrometer (GC / MS), and the weight of nicotine contained in the predetermined solvent was quantified.
- GC / MS gas chromatograph mass spectrometer
- Method for measuring acetaldehyde contained in a given solvent 0.05 mL of a predetermined solvent is collected, 0.4 mL of 6 mmol / L 2,4-dinitrophenylpyrazine solution is added to convert acetaldehyde in the predetermined solvent into a nonvolatile hydrazone derivative, and further 0.2 w / v% 0.55 mL of trizma base solution was added to stabilize the hydrazone derivative in the given solvent.
- the obtained liquid was subjected to a high performance liquid chromatography diode array detector, and the amount of hydrazone derivative contained in the predetermined solvent was quantified. Furthermore, the amount of acetaldehyde contained in the collection solvent was calculated from the amount of hydrazone derivative.
- a 6 mmol / L 2,4-dinitrophenylpyrazine solution was prepared by adding 992 mL water and 8 mL 80% phosphoric acid to 1 L of 12 mL of 2,4-dinitrophenylpyrazine-acetonitrile solution.
- a 2 w / v% Trizma base solution was prepared by adding 800 mL acetonitrile and 200 mL water to 2 g Trizma base.
- the weight of the tobacco raw material in the dry state is calculated by subtracting the above-described moisture content from the total weight of the tobacco raw material.
- a method for producing a component of a luxury product including a flavor component capable of selectively reducing a contaminating component contained in a tobacco source, and a preference including a flavor component A component of the product can be provided.
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Abstract
Description
以下、図1乃至図3を参照して、本発明の第1の実施形態に係る香喫味成分を含む嗜好品の構成要素の製造方法について説明する。本実施形態では、かかる嗜好品の構成要素として、香味吸引具の構成要素を製造するケースについて例示するものとする。
第1実施形態に係る製造方法によれば、非常に簡便な方法で、たばこ源としてのたばこ原料中の不要な夾雑物質を移行させることなく、十分な量の香喫味成分を所定溶媒に移行させることができ、かかる所定溶媒を香味吸引具1の構成要素(例えば、フィルタ)に対して添加して香味発生源とすることで、夾雑物質のユーザへの送達を低減することができる。
以下において、第1実施形態の変更例1について説明する。以下においては、第1実施形態に対する相違点について主として説明する。
上述の第1の実施形態では、香喫味成分を含む嗜好品の構成要素として、上述の香味吸引具の構成要素を製造するケースについて説明したが、本発明は、かかるケースに限定されることはない。
(第1実験)
第1実験では、実施例及び比較例について、たばこ源に含まれるアルカロイド(ここでは、ニコチン成分)の回収率(以下、ニコチン成分回収率)、アセトアルデヒド濃度、アンモニウムイオン濃度、ピリジン濃度を測定した。実施例では、上述した第1実施形態に従って、バブリングによって香喫味成分を所定溶媒によって捕捉した(実施例1)。また、後述する比較例とステップS101におけるたばこ源の量、処理時間、通気流量を同一とするために実施例1よりも小スケールの装置を用いた点、捕集溶媒の温度制御を行わなかった点以外は実施例1と同様の条件で香喫味成分の捕捉を行った(実施例2)。
・たばこ源の種類:バーレー種のたばこ原料
・たばこ源に含まれるニコチン量:たばこ源の乾燥重量当たり4.9重量%
・たばこ源に含まれるアンモニウムイオン量:たばこ源の乾燥重量当たり4545μg/g
・たばこ源の量:500g
・たばこ源の粒径:0.5mm~1.18mm
・アルカリ処理後のたばこ源のpH:9.6
・アルカリ処理後のたばこ源の初期水分量:39%±2%
・たばこ源の加熱温度:120℃
・処理時間:300min
・バブリング時の空気流量:15L/min
・所定溶媒の種類:グリセリン
・所定溶媒の量:61g
・所定溶媒の温度:20℃
・たばこ源の種類:バーレー種のたばこ原料・たばこ源の量:55g
・たばこ源に含まれるニコチン量:たばこ源の乾燥重量当たり4.9重量%
・たばこ源に含まれるアンモニウムイオン量:たばこ源の乾燥重量当たり4545μg/g
・たばこ源の粒径:0.5mm~1.18mm
・アルカリ処理後のたばこ源のpH:9.6
・アルカリ処理後のたばこ源の初期水分量:39%±2%
・たばこ源の加熱温度:120℃
・処理時間:24Hr
・バブリング時の空気流量:1.5L/min
・所定溶媒の種類:グリセリン
・所定溶媒の量:7.4g
・たばこ源の種類:バーレー種のたばこ原料
・たばこ源に含まれるニコチン量:たばこ源の乾燥重量当たり4.9重量%
・たばこ源に含まれるアンモニウムイオン量:たばこ源の乾燥重量当たり4545μg/g
・たばこ源の量:55g
・たばこ源の粒径:0.5mm~1.18mm
・アルカリ処理後のたばこ源のpH:9.6
・アルカリ処理後のたばこ源の初期水分量:39%±2%
・たばこ源の加熱温度:120℃
・処理時間:24Hr
・コールドトラップ時の空気流量:1.5L/min
・冷媒の温度:20℃
第2実験では、以下の条件下において、所定溶媒の温度を変更することによって、所定溶液に含まれるアンモニウムイオン及びピリジンの重量を測定した。所定溶液に含まれるアンモニウムイオンの重量は、図9に示す通りである。所定溶液に含まれるピリジンの重量は、図10に示す通りである。
・たばこ源の種類;バーレー種
・たばこ源に含まれるニコチン量:たばこ源の乾燥重量当たり4.9重量%
・たばこ源に含まれるアンモニウムイオン量:たばこ源の乾燥重量当たり4545μg/g
・たばこ源の量:500g
・たばこ源の粒径:0.5mm~1.18mm
・たばこ源の加熱温度:120℃
・アルカリ処理後のたばこ源のpH:9.6
・アルカリ処理後のたばこ源の初期水分量:39%±2%・処理時間:300min
・バブリング時の空気流量:15L/min
・所定溶媒の種類:グリセリン
・所定溶媒の量:61g
(たばこ原料に含まれるニコチン成分の測定方法)
ドイツ標準化機構DIN 10373に準ずる方法で行った。すなわち、たばこ原料を250mg採取し、11%水酸化ナトリウム水溶液7.5mLとヘキサン10mLを加え、60分間振とう抽出した。抽出後、上澄みであるヘキサン相をガスクロマトグラフ質量分析計(GC/MS)に供し、たばこ原料に含まれるニコチン重量を定量した。
所定溶媒を50μL採取し、0.05Nの希硫酸水溶液950μLを添加することで希釈し、イオンクロマトグラフィーで分析し、所定溶媒に含まれるアンモニウムイオンを定量した。
ドイツ標準化機構DIN 10373に準ずる方法で行った。すなわち、所定溶媒を100mg採取し、11%水酸化ナトリウム水溶液7.5mLとヘキサン10mLを加え、60分間振とう抽出した。抽出後、上澄みであるヘキサン相をガスクロマトグラフ質量分析計(GC/MS)に供し、所定溶媒に含まれるニコチン重量を定量した。
所定溶媒を0.05mL採取し、6mmol/Lの2,4-ジニトロフェニルピラジン溶液を0.4mL加えて所定溶媒中のアセトアルデヒドを不揮発性のヒドラゾン誘導体に変換し、更に0.2w/v%のトリズマベース溶液を0.55mL加えて所定溶媒中のヒドラゾン誘導体を安定化した。得られた液を高速液体クロマトグラフィーダイオードアレイ検出器に供し、所定溶媒に含まれるヒドラゾン誘導体量を定量した。さらに、ヒドラゾン誘導体量から捕集溶媒に含まれるアセトアルデヒト量を算出した。
所定溶媒を1mL採取し、メタノール19mLを添加することで希釈し、ガスクロマトグラフ質量分析計にて所定溶媒中に含まれるピリジン量を定量した。
たばこ原料を250mg採取し、エタノール10mLを加え、60分間振とう抽出を行った。抽出後、抽出液を0.45μmのメンブレンフィルタでろ過し、熱伝導度検出器を備えたガスクロマトグラフ(GC/TCD)に供し、たばこ原料に含まれる水分量を定量した。
Claims (11)
- 香喫味成分を含む嗜好品の構成要素の製造方法であって、
アルカリ処理されたたばこ源を加熱して、前記たばこ源から気相中に香喫味成分を放出する工程Aと、
気相中に放出された前記香喫味成分を常温で液体の物質である所定溶媒に接触させることによって、前記所定溶媒に前記香喫味成分を捕捉させる工程Bと、
前記所定溶媒を前記構成要素に添加する工程Cとを有することを特徴とする製造方法。 - 前記工程Bにおいて、気相中に放出された前記香喫味成分を前記所定溶媒中に通気することによって、前記所定溶媒に前記香喫味成分を捕捉させることを特徴とする請求項1に記載の製造方法。
- 前記工程Aにおいて、常圧以下の圧力が前記たばこ源に印加された状態で、前記たばこ源から気相中に香喫味成分を放出することを特徴とする請求項1又は2に記載の製造方法。
- 前記工程Bにおいて、前記所定溶媒の温度は、10℃以上かつ40℃以下であることを特徴とする請求項1又は2に記載の製造方法。
- 前記工程Aにおいて、前記たばこ源に対して加水処理を施すことを特徴とする請求項1又は2に記載の製造方法。
- 前記工程Aにおいて、前記たばこ源を加熱する前において前記たばこ源の水分量は、前記加水処理によって30重量%以上であることを特徴とする請求項5に記載の製造方法。
- 前記構成要素として、ガムベース、タブレット、可食フィルム、基材、フィルタ、セルロースの少なくとも1つが用いられることを特徴とする請求項1又は2に記載の製造方法。
- 前記構成要素は、前記工程Aで前記香喫味成分を放出した後の前記たばこ源である残たばこ源であり、
前記工程Cは、前記所定溶媒を前記残たばこ源に掛け戻す工程を含むことを特徴とする請求項1又は2に記載の製造方法。 - 前記工程Aにおいて、前記たばこ源を加熱する前において前記たばこ源の水分量は、30重量%以上であり、前記たばこ源を加熱した後において前記たばこ源の水分量は、5重量%未満であることを特徴とする請求項8に記載の製造方法。
- 前記工程Bにおいて、前記所定溶媒の温度は、10℃以上かつ40℃以下であることを特徴とする請求項9に記載の製造方法。
- 請求項1乃至10のいずれか一項に記載の製造方法によって製造されたことを特徴とする香喫味成分を含む嗜好品の構成要素。
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CN105142430B (zh) | 2021-04-27 |
JPWO2014175399A1 (ja) | 2017-02-23 |
TW201509317A (zh) | 2015-03-16 |
EP2982252A1 (en) | 2016-02-10 |
US20160073678A1 (en) | 2016-03-17 |
US10390555B2 (en) | 2019-08-27 |
EP2982252A4 (en) | 2017-01-04 |
EP2982252B1 (en) | 2024-06-12 |
CA2910389A1 (en) | 2014-10-30 |
JP6034488B2 (ja) | 2016-11-30 |
CN105142430A (zh) | 2015-12-09 |
CA2910389C (en) | 2019-01-22 |
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