WO2024024083A1 - Reconstituted tobacco for non-combustion heating-type flavor inhaler and method for manufacturing same, non-combustion heating-type flavor inhaler, and non-combustion heating-type flavor inhaling system - Google Patents
Reconstituted tobacco for non-combustion heating-type flavor inhaler and method for manufacturing same, non-combustion heating-type flavor inhaler, and non-combustion heating-type flavor inhaling system Download PDFInfo
- Publication number
- WO2024024083A1 WO2024024083A1 PCT/JP2022/029285 JP2022029285W WO2024024083A1 WO 2024024083 A1 WO2024024083 A1 WO 2024024083A1 JP 2022029285 W JP2022029285 W JP 2022029285W WO 2024024083 A1 WO2024024083 A1 WO 2024024083A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- tobacco
- recycled
- flavor inhaler
- regenerated
- combustion
- Prior art date
Links
- 241000208125 Nicotiana Species 0.000 title claims abstract description 344
- 235000002637 Nicotiana tabacum Nutrition 0.000 title claims abstract description 344
- 239000000796 flavoring agent Substances 0.000 title claims abstract description 97
- 235000019634 flavors Nutrition 0.000 title claims abstract description 95
- 238000002485 combustion reaction Methods 0.000 title claims abstract description 85
- 238000000034 method Methods 0.000 title claims description 46
- 238000004519 manufacturing process Methods 0.000 title claims description 13
- 239000000463 material Substances 0.000 claims abstract description 88
- 238000002835 absorbance Methods 0.000 claims abstract description 21
- 238000005033 Fourier transform infrared spectroscopy Methods 0.000 claims abstract description 18
- 238000010438 heat treatment Methods 0.000 claims description 76
- 239000002994 raw material Substances 0.000 claims description 41
- 238000011282 treatment Methods 0.000 claims description 25
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 24
- 238000010411 cooking Methods 0.000 claims description 23
- 239000011230 binding agent Substances 0.000 claims description 14
- 238000010521 absorption reaction Methods 0.000 claims description 13
- 239000002657 fibrous material Substances 0.000 claims description 12
- 238000005520 cutting process Methods 0.000 claims description 5
- 238000010979 pH adjustment Methods 0.000 claims description 4
- 150000008044 alkali metal hydroxides Chemical class 0.000 claims description 3
- PEDCQBHIVMGVHV-UHFFFAOYSA-N Glycerine Chemical compound OCC(O)CO PEDCQBHIVMGVHV-UHFFFAOYSA-N 0.000 description 32
- 239000000443 aerosol Substances 0.000 description 19
- 238000005259 measurement Methods 0.000 description 17
- SNICXCGAKADSCV-JTQLQIEISA-N (-)-Nicotine Chemical compound CN1CCC[C@H]1C1=CC=CN=C1 SNICXCGAKADSCV-JTQLQIEISA-N 0.000 description 16
- 238000001816 cooling Methods 0.000 description 16
- 235000011187 glycerol Nutrition 0.000 description 16
- 229960002715 nicotine Drugs 0.000 description 16
- SNICXCGAKADSCV-UHFFFAOYSA-N nicotine Natural products CN1CCCC1C1=CC=CN=C1 SNICXCGAKADSCV-UHFFFAOYSA-N 0.000 description 16
- 239000000123 paper Substances 0.000 description 16
- 238000011049 filling Methods 0.000 description 14
- 239000002585 base Substances 0.000 description 13
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 12
- 230000000052 comparative effect Effects 0.000 description 12
- 239000000126 substance Substances 0.000 description 11
- 238000011156 evaluation Methods 0.000 description 10
- 239000003513 alkali Substances 0.000 description 8
- 239000000779 smoke Substances 0.000 description 8
- 238000009423 ventilation Methods 0.000 description 8
- 238000000605 extraction Methods 0.000 description 7
- 239000000835 fiber Substances 0.000 description 7
- 239000000243 solution Substances 0.000 description 7
- 238000012546 transfer Methods 0.000 description 7
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 6
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 6
- DNIAPMSPPWPWGF-UHFFFAOYSA-N Propylene glycol Chemical compound CC(O)CO DNIAPMSPPWPWGF-UHFFFAOYSA-N 0.000 description 6
- 229920002301 cellulose acetate Polymers 0.000 description 6
- 235000019504 cigarettes Nutrition 0.000 description 6
- KRKNYBCHXYNGOX-UHFFFAOYSA-N citric acid Chemical compound OC(=O)CC(O)(C(O)=O)CC(O)=O KRKNYBCHXYNGOX-UHFFFAOYSA-N 0.000 description 6
- 229910052751 metal Inorganic materials 0.000 description 6
- 239000002184 metal Substances 0.000 description 6
- 239000002904 solvent Substances 0.000 description 6
- 125000002887 hydroxy group Chemical group [H]O* 0.000 description 5
- 239000000203 mixture Substances 0.000 description 5
- 238000000113 differential scanning calorimetry Methods 0.000 description 4
- 239000003205 fragrance Substances 0.000 description 4
- URAYPUMNDPQOKB-UHFFFAOYSA-N triacetin Chemical compound CC(=O)OCC(OC(C)=O)COC(C)=O URAYPUMNDPQOKB-UHFFFAOYSA-N 0.000 description 4
- XEKOWRVHYACXOJ-UHFFFAOYSA-N Ethyl acetate Chemical compound CCOC(C)=O XEKOWRVHYACXOJ-UHFFFAOYSA-N 0.000 description 3
- 229920002907 Guar gum Polymers 0.000 description 3
- KFZMGEQAYNKOFK-UHFFFAOYSA-N Isopropanol Chemical compound CC(C)O KFZMGEQAYNKOFK-UHFFFAOYSA-N 0.000 description 3
- 238000005266 casting Methods 0.000 description 3
- 230000007613 environmental effect Effects 0.000 description 3
- 239000000945 filler Substances 0.000 description 3
- 239000007789 gas Substances 0.000 description 3
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- 235000010417 guar gum Nutrition 0.000 description 3
- 229960002154 guar gum Drugs 0.000 description 3
- 238000000465 moulding Methods 0.000 description 3
- VLKZOEOYAKHREP-UHFFFAOYSA-N n-Hexane Chemical compound CCCCCC VLKZOEOYAKHREP-UHFFFAOYSA-N 0.000 description 3
- 238000006386 neutralization reaction Methods 0.000 description 3
- BDERNNFJNOPAEC-UHFFFAOYSA-N propan-1-ol Chemical compound CCCO BDERNNFJNOPAEC-UHFFFAOYSA-N 0.000 description 3
- 239000011122 softwood Substances 0.000 description 3
- PUPZLCDOIYMWBV-UHFFFAOYSA-N (+/-)-1,3-Butanediol Chemical compound CC(O)CCO PUPZLCDOIYMWBV-UHFFFAOYSA-N 0.000 description 2
- 229910018072 Al 2 O 3 Inorganic materials 0.000 description 2
- LSNNMFCWUKXFEE-UHFFFAOYSA-M Bisulfite Chemical compound OS([O-])=O LSNNMFCWUKXFEE-UHFFFAOYSA-M 0.000 description 2
- 229920002134 Carboxymethyl cellulose Polymers 0.000 description 2
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 2
- 229920001131 Pulp (paper) Polymers 0.000 description 2
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 2
- LSNNMFCWUKXFEE-UHFFFAOYSA-N Sulfurous acid Chemical compound OS(O)=O LSNNMFCWUKXFEE-UHFFFAOYSA-N 0.000 description 2
- RAHZWNYVWXNFOC-UHFFFAOYSA-N Sulphur dioxide Chemical compound O=S=O RAHZWNYVWXNFOC-UHFFFAOYSA-N 0.000 description 2
- 238000000862 absorption spectrum Methods 0.000 description 2
- 239000007864 aqueous solution Substances 0.000 description 2
- 230000004323 axial length Effects 0.000 description 2
- 239000001768 carboxy methyl cellulose Substances 0.000 description 2
- 235000010948 carboxy methyl cellulose Nutrition 0.000 description 2
- 239000008112 carboxymethyl-cellulose Substances 0.000 description 2
- 239000003795 chemical substances by application Substances 0.000 description 2
- 239000013078 crystal Substances 0.000 description 2
- 230000007423 decrease Effects 0.000 description 2
- 229910003460 diamond Inorganic materials 0.000 description 2
- 239000010432 diamond Substances 0.000 description 2
- 235000013355 food flavoring agent Nutrition 0.000 description 2
- 239000003292 glue Substances 0.000 description 2
- 239000001087 glyceryl triacetate Substances 0.000 description 2
- 235000013773 glyceryl triacetate Nutrition 0.000 description 2
- 239000004615 ingredient Substances 0.000 description 2
- 230000010354 integration Effects 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 238000000691 measurement method Methods 0.000 description 2
- 238000002156 mixing Methods 0.000 description 2
- 238000012856 packing Methods 0.000 description 2
- 235000013772 propylene glycol Nutrition 0.000 description 2
- 239000011734 sodium Substances 0.000 description 2
- 229910001220 stainless steel Inorganic materials 0.000 description 2
- 239000010935 stainless steel Substances 0.000 description 2
- 239000008399 tap water Substances 0.000 description 2
- 235000020679 tap water Nutrition 0.000 description 2
- 229960002622 triacetin Drugs 0.000 description 2
- 238000004804 winding Methods 0.000 description 2
- NOOLISFMXDJSKH-UTLUCORTSA-N (+)-Neomenthol Chemical compound CC(C)[C@@H]1CC[C@@H](C)C[C@@H]1O NOOLISFMXDJSKH-UTLUCORTSA-N 0.000 description 1
- 244000198134 Agave sisalana Species 0.000 description 1
- 229920002261 Corn starch Polymers 0.000 description 1
- FBPFZTCFMRRESA-FSIIMWSLSA-N D-Glucitol Natural products OC[C@H](O)[C@H](O)[C@@H](O)[C@H](O)CO FBPFZTCFMRRESA-FSIIMWSLSA-N 0.000 description 1
- FBPFZTCFMRRESA-JGWLITMVSA-N D-glucitol Chemical compound OC[C@H](O)[C@@H](O)[C@H](O)[C@H](O)CO FBPFZTCFMRRESA-JGWLITMVSA-N 0.000 description 1
- NOOLISFMXDJSKH-UHFFFAOYSA-N DL-menthol Natural products CC(C)C1CCC(C)CC1O NOOLISFMXDJSKH-UHFFFAOYSA-N 0.000 description 1
- 239000004386 Erythritol Substances 0.000 description 1
- UNXHWFMMPAWVPI-UHFFFAOYSA-N Erythritol Natural products OCC(O)C(O)CO UNXHWFMMPAWVPI-UHFFFAOYSA-N 0.000 description 1
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 description 1
- 240000006240 Linum usitatissimum Species 0.000 description 1
- 235000004431 Linum usitatissimum Nutrition 0.000 description 1
- 241001144488 Nicotiana occidentalis Species 0.000 description 1
- GRYLNZFGIOXLOG-UHFFFAOYSA-N Nitric acid Chemical compound O[N+]([O-])=O GRYLNZFGIOXLOG-UHFFFAOYSA-N 0.000 description 1
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical compound [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 description 1
- PMZURENOXWZQFD-UHFFFAOYSA-L Sodium Sulfate Chemical compound [Na+].[Na+].[O-]S([O-])(=O)=O PMZURENOXWZQFD-UHFFFAOYSA-L 0.000 description 1
- 244000061456 Solanum tuberosum Species 0.000 description 1
- 235000002595 Solanum tuberosum Nutrition 0.000 description 1
- XTXRWKRVRITETP-UHFFFAOYSA-N Vinyl acetate Chemical compound CC(=O)OC=C XTXRWKRVRITETP-UHFFFAOYSA-N 0.000 description 1
- TVXBFESIOXBWNM-UHFFFAOYSA-N Xylitol Natural products OCCC(O)C(O)C(O)CCO TVXBFESIOXBWNM-UHFFFAOYSA-N 0.000 description 1
- DPXJVFZANSGRMM-UHFFFAOYSA-N acetic acid;2,3,4,5,6-pentahydroxyhexanal;sodium Chemical compound [Na].CC(O)=O.OCC(O)C(O)C(O)C(O)C=O DPXJVFZANSGRMM-UHFFFAOYSA-N 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 239000003463 adsorbent Substances 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 239000011324 bead Substances 0.000 description 1
- 235000019437 butane-1,3-diol Nutrition 0.000 description 1
- 239000002775 capsule Substances 0.000 description 1
- 229940105329 carboxymethylcellulose Drugs 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 239000003245 coal Substances 0.000 description 1
- 239000000306 component Substances 0.000 description 1
- 239000004035 construction material Substances 0.000 description 1
- 239000008120 corn starch Substances 0.000 description 1
- 238000010790 dilution Methods 0.000 description 1
- 239000012895 dilution Substances 0.000 description 1
- 239000012153 distilled water Substances 0.000 description 1
- -1 during suction Substances 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- UNXHWFMMPAWVPI-ZXZARUISSA-N erythritol Chemical compound OC[C@H](O)[C@H](O)CO UNXHWFMMPAWVPI-ZXZARUISSA-N 0.000 description 1
- 235000019414 erythritol Nutrition 0.000 description 1
- 229940009714 erythritol Drugs 0.000 description 1
- 238000000769 gas chromatography-flame ionisation detection Methods 0.000 description 1
- 229960005150 glycerol Drugs 0.000 description 1
- 239000011121 hardwood Substances 0.000 description 1
- 239000002655 kraft paper Substances 0.000 description 1
- 229940041616 menthol Drugs 0.000 description 1
- HEBKCHPVOIAQTA-UHFFFAOYSA-N meso ribitol Natural products OCC(O)C(O)C(O)CO HEBKCHPVOIAQTA-UHFFFAOYSA-N 0.000 description 1
- CDBRNDSHEYLDJV-FVGYRXGTSA-M naproxen sodium Chemical compound [Na+].C1=C([C@H](C)C([O-])=O)C=CC2=CC(OC)=CC=C21 CDBRNDSHEYLDJV-FVGYRXGTSA-M 0.000 description 1
- 230000007935 neutral effect Effects 0.000 description 1
- 230000003472 neutralizing effect Effects 0.000 description 1
- 229910017604 nitric acid Inorganic materials 0.000 description 1
- 239000004745 nonwoven fabric Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 239000003002 pH adjusting agent Substances 0.000 description 1
- 230000000704 physical effect Effects 0.000 description 1
- 239000004014 plasticizer Substances 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 229960004063 propylene glycol Drugs 0.000 description 1
- 230000001007 puffing effect Effects 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 238000005096 rolling process Methods 0.000 description 1
- 229910052708 sodium Inorganic materials 0.000 description 1
- 235000019812 sodium carboxymethyl cellulose Nutrition 0.000 description 1
- 229910052938 sodium sulfate Inorganic materials 0.000 description 1
- 235000011152 sodium sulphate Nutrition 0.000 description 1
- 239000000600 sorbitol Substances 0.000 description 1
- 229960002920 sorbitol Drugs 0.000 description 1
- 235000010356 sorbitol Nutrition 0.000 description 1
- 150000005846 sugar alcohols Polymers 0.000 description 1
- 238000012360 testing method Methods 0.000 description 1
- 238000003856 thermoforming Methods 0.000 description 1
- 235000019505 tobacco product Nutrition 0.000 description 1
- 229910021642 ultra pure water Inorganic materials 0.000 description 1
- 239000012498 ultrapure water Substances 0.000 description 1
- MWOOGOJBHIARFG-UHFFFAOYSA-N vanillin Chemical compound COC1=CC(C=O)=CC=C1O MWOOGOJBHIARFG-UHFFFAOYSA-N 0.000 description 1
- FGQOOHJZONJGDT-UHFFFAOYSA-N vanillin Natural products COC1=CC(O)=CC(C=O)=C1 FGQOOHJZONJGDT-UHFFFAOYSA-N 0.000 description 1
- 235000012141 vanillin Nutrition 0.000 description 1
- 210000003462 vein Anatomy 0.000 description 1
- 238000003466 welding Methods 0.000 description 1
- 239000000230 xanthan gum Substances 0.000 description 1
- 229920001285 xanthan gum Polymers 0.000 description 1
- 235000010493 xanthan gum Nutrition 0.000 description 1
- 229940082509 xanthan gum Drugs 0.000 description 1
- 239000000811 xylitol Substances 0.000 description 1
- 235000010447 xylitol Nutrition 0.000 description 1
- HEBKCHPVOIAQTA-SCDXWVJYSA-N xylitol Chemical compound OC[C@H](O)[C@@H](O)[C@H](O)CO HEBKCHPVOIAQTA-SCDXWVJYSA-N 0.000 description 1
- 229960002675 xylitol Drugs 0.000 description 1
Classifications
-
- A—HUMAN NECESSITIES
- A24—TOBACCO; CIGARS; CIGARETTES; SIMULATED SMOKING DEVICES; SMOKERS' REQUISITES
- A24B—MANUFACTURE OR PREPARATION OF TOBACCO FOR SMOKING OR CHEWING; TOBACCO; SNUFF
- A24B3/00—Preparing tobacco in the factory
- A24B3/14—Forming reconstituted tobacco products, e.g. wrapper materials, sheets, imitation leaves, rods, cakes; Forms of such products
-
- A—HUMAN NECESSITIES
- A24—TOBACCO; CIGARS; CIGARETTES; SIMULATED SMOKING DEVICES; SMOKERS' REQUISITES
- A24B—MANUFACTURE OR PREPARATION OF TOBACCO FOR SMOKING OR CHEWING; TOBACCO; SNUFF
- A24B5/00—Stripping tobacco; Treatment of stems or ribs
- A24B5/12—Auxiliary devices for stripping
-
- A—HUMAN NECESSITIES
- A24—TOBACCO; CIGARS; CIGARETTES; SIMULATED SMOKING DEVICES; SMOKERS' REQUISITES
- A24D—CIGARS; CIGARETTES; TOBACCO SMOKE FILTERS; MOUTHPIECES FOR CIGARS OR CIGARETTES; MANUFACTURE OF TOBACCO SMOKE FILTERS OR MOUTHPIECES
- A24D1/00—Cigars; Cigarettes
- A24D1/20—Cigarettes specially adapted for simulated smoking devices
Definitions
- the present invention relates to a regenerated tobacco for use in a non-combustion heating type flavor inhaler, a method for manufacturing the same, a non-combustion heating type flavor inhaler, and a non-combustion heating type flavor inhaler system.
- combustion-type flavor inhalers cigarettes
- flavor is obtained by burning tobacco filler containing leaf tobacco.
- a non-combustion heating type flavor inhaler has been proposed, which obtains flavor by heating the tobacco filling instead of burning it.
- the heating temperature of the non-combustion heating type flavor inhaler is lower than the combustion temperature of the combustion type flavor inhaler, for example, about 400° C. or less.
- an aerosol generating agent such as glycerin is added to the tobacco filling in the non-combustion heating type flavor inhaler from the viewpoint of increasing the amount of smoke.
- the aerosol generator is vaporized by heating and generates an aerosol. Since the aerosol is supplied to the user along with a flavor component such as a tobacco component, the user can obtain a sufficient flavor.
- a non-combustion heated flavor inhaler can be used by heating a tobacco-containing segment filled with tobacco filler, for example, with a heater of a heating device.
- the heating device usually has a battery unit, and the heater is heated by supplying electric power from the battery unit. From the viewpoint of user convenience, when using a non-combustion heated flavor inhaler using a heating device, it is desirable to suppress power consumption and increase the usable time and number of usable flavor inhalers.
- Patent Document 1 discloses that black liquor with a high vanillin content can be obtained by cooking tobacco raw materials under alkaline conditions.
- One way to reduce power consumption without changing the size of the product is to improve the tobacco materials contained in non-combustion heated flavor inhalers, thereby reducing the amount of electricity consumed per non-combustion heated flavor inhaler. It is possible to suppress consumption.
- An object of the present invention is to provide a regenerated cigarette, a non-combustion heating flavor suction device, and a non-combustion heating flavor suction system that can suppress power consumption per non-combustion heating flavor suction device during use. shall be.
- the present invention includes the following embodiments.
- Regenerated tobacco for use in a non-combustion heating flavor inhaler, which includes a tobacco material and a tobacco component,
- the tobacco material has a maximum absorbance of 0.40 or more at a wavelength of 3200 to 3600 cm ⁇ 1 in FT-IR analysis, Regenerated tobacco, wherein the tobacco material has a specific heat of 5 mJ/mg ⁇ °C or less.
- a non-combustion heated flavor inhaler comprising a tobacco-containing segment filled with the recycled tobacco according to any one of [1] to [7].
- [10] The method for producing recycled tobacco according to any one of [1] to [7], a step of extracting tobacco components from tobacco raw materials to obtain tobacco extract and tobacco residue; After subjecting the tobacco residue to alkaline cooking treatment, adjusting the pH to 4.0 to 6.5; Sprinkling the tobacco extract back onto the tobacco residue after pH adjustment; including methods.
- the present invention it is possible to provide a recycled tobacco, a non-combustion heating flavor suction device, and a non-combustion heating flavor suction system that can suppress power consumption per non-combustion heating flavor suction device during use. Can be done.
- FIG. 3 is a cross-sectional view showing a state in which the device is inserted into the device and heated.
- 2 is a graph showing the amount of nicotine delivered in each puff in Example 1, Comparative Example 1, and Comparative Example 3.
- 2 is a graph showing the amount of glycerin delivered in each puff in Example 1, Comparative Example 1, and Comparative Example 3.
- 2 is a graph showing the nicotine transfer rate to mainstream smoke per power consumption (energy) with respect to the specific heat of the base material of recycled cigarettes in Example 1, Comparative Example 1, and Comparative Example 3.
- the regenerated tobacco according to the present embodiment is a regenerated tobacco for use in a non-combustion heating type flavor inhaler that includes a tobacco material and a tobacco component.
- the tobacco material has a maximum absorbance of 0.40 or more at a wavelength of 3200 to 3600 cm ⁇ 1 as determined by FT-IR analysis.
- the specific heat of the tobacco material is 5 mJ/mg ⁇ °C or less.
- the present inventors have found that by using a tobacco material with a low specific heat as the tobacco material contained in a non-combustion heated flavor inhaler, the heating efficiency is improved, and as a result, the We thought that it would be possible to suppress power consumption.
- the present inventors have found that tobacco materials with a maximum absorbance of 0.40 or more at a wavelength of 3200 to 3600 cm -1 in FT-IR analysis and a specific heat of 5 mJ/mg ⁇ °C or less, and tobacco It has been found that by using recycled tobacco containing these ingredients as the tobacco material for a non-combustion heating flavor inhaler, it is possible to suppress the power consumption per non-combustion heating flavor inhaler.
- absorption at wavelengths of 3200 to 3600 cm ⁇ 1 is derived from stretching vibrations of hydroxyl groups.
- the amount of hydroxyl groups in the resulting tobacco material increases, and the maximum absorbance can be increased.
- the increase in maximum absorbance is not derived from free OH but from hydroxyl groups covalently bonded to the tobacco material.
- regenerated tobacco refers to tobacco materials that are reconstituted by mixing tobacco components and other materials.
- the recycled tobacco according to the present embodiment can contain, for example, a binder, a fiber material, an aerosol generator, etc. in addition to the tobacco material and tobacco components.
- the tobacco material according to this embodiment has a maximum absorbance of 0.40 or more at a wavelength of 3200 to 3600 cm ⁇ 1 in FT-IR analysis.
- the maximum absorbance at the wavelength of 3200 to 3600 cm ⁇ 1 is preferably 0.42 or more, more preferably 0.45 or more.
- the upper limit of the range of maximum absorbance at wavelengths of 3200 to 3600 cm ⁇ 1 is not particularly limited, but may be, for example, 1.0 or less.
- FT-IR analysis of tobacco materials can be performed by the following method.
- a sample of tobacco material is brought into close contact with a diamond crystal for ATR measurement, and an infrared absorption spectrum is measured.
- a Fourier transform infrared spectrometer (trade name: Thermo Scientific Nicolet iS50, manufactured by Thermo Scientific) can be used.
- a method for making the maximum absorbance of the tobacco material 0.40 or more for example, a method of subjecting the tobacco raw material to an alkaline cooking treatment and then neutralizing it can be mentioned.
- tobacco raw materials include leaf tobacco, tobacco leaf veins, stems, roots, and flowers, which may be shredded or powdered.
- the type of leaf tobacco is not particularly limited, and any variety can be used, but examples include yellow tobacco, burley tobacco, native tobacco, orient leaf, and fermented leaves thereof.
- One type of these tobacco raw materials may be used, or two or more types may be used in combination.
- the tobacco raw material to be subjected to the alkaline cooking treatment is preferably tobacco residue after extracting a tobacco extract containing tobacco components from the tobacco raw material.
- the obtained tobacco extract can be used as a tobacco component of recycled tobacco.
- the alkali cooking treatment and neutralization method include the alkali cooking treatment and neutralization method in the method for producing recycled tobacco according to the present embodiment, which will be described later.
- the specific heat of the tobacco material is 5 mJ/mg ⁇ °C or less.
- the specific heat is preferably 4 mJ/mg ⁇ °C or less, more preferably 3 mJ/mg ⁇ °C or less, and even more preferably 2 mJ/mg ⁇ °C or less.
- the specific heat of the tobacco material can be reduced to 5 mJ/mg ⁇ ° C. or less by, for example, setting the maximum absorbance at a wavelength of 3200 to 3600 cm ⁇ 1 to 0.40 or more in FT-IR analysis.
- the specific heat of the tobacco material is indicated by the maximum specific heat capacity (mJ/mg ⁇ ° C.) up to 300° C., measured by DSC (differential scanning calorimetry). For example, it can be measured using a differential scanning calorimeter (trade name: DSC7020, manufactured by Hitachi High-Tech Science Co., Ltd.) under the following conditions. Temperature increase rate: 10° C./min, holding time: 2 minutes, pan: Al, sample mass: 10 mg, reference: Al 2 O 3 .
- the amount of water absorbed when the tobacco material is immersed in water at 23° C. for 900 seconds is preferably 4.0 to 6.0 g/g.
- the water absorption amount is more preferably 4.2 to 5.8 g/g, and even more preferably 4.5 to 5.5 g/g.
- the water absorption amount of the tobacco material can be measured by the following method.
- a cylindrical container with 19 holes of 1 mm diameter in a stainless steel tube of ⁇ 55 ⁇ 80 mm is prepared.
- a filter paper is placed in the cylindrical container, and 3 to 6 g of the tobacco material sample is placed thereon.
- Fill a vat with tap water place the cylindrical container in the vat, measure the mass after 900 seconds, and measure the amount of water absorbed per 1 g. This measurement is carried out three times, and the average value is taken as the water absorption amount.
- the angle of repose of the tobacco material is preferably 40° or less. When the angle of repose is 40° or less, it becomes easier to input the raw material when inputting the raw material in the production of recycled tobacco, which is preferable in terms of production.
- the angle of repose is more preferably 10 to 40°, and even more preferably 20 to 30°.
- the angle of repose of tobacco materials can be measured by the following method. A sample of tobacco material was dropped using a funnel from 4 cm above a 25 mm x 25 mm measuring table (peak material). Once the sample is dropped from the measuring table to the extent that it spills, a photograph is taken and the angle is measured using image analysis software (Keyence Microscope). This measurement is carried out three times, and the average value is taken as the value of the angle of repose.
- the amount of tobacco material contained in the recycled tobacco is preferably 20 to 80% by mass, more preferably 20 to 65% by mass, and 30 to 50% by mass when the mass of the recycled tobacco is 100% by mass. % is more preferable.
- the tobacco component is a tobacco-derived component contained in the tobacco raw material, and main components include components that contribute to aroma and taste.
- the recycled tobacco according to the present embodiment may contain the tobacco component alone, it is preferably contained as a tobacco extract obtained by extracting the tobacco component from the tobacco raw material.
- the tobacco residue after extracting the tobacco extract can be used as a raw material for tobacco materials, which reduces environmental impact and is also advantageous in terms of cost.
- the amount of tobacco components contained in the recycled tobacco can be appropriately set depending on the desired flavor.
- the recycled tobacco according to this embodiment preferably contains a binder. Since the recycled tobacco contains a binder, each raw material can be bonded together, and the recycled tobacco can be suitably molded into a desired shape.
- the type of binder is not particularly limited, but examples include guar gum, xanthan gum, CMC (carboxymethylcellulose), CMC-Na (sodium salt of carboxymethylcellulose), waxy corn starch, and potato. These may be used alone or in combination of two or more.
- the amount of binder contained in the recycled tobacco is preferably 1 to 10% by mass, more preferably 3 to 6% by mass, when the mass of the recycled tobacco is 100% by mass.
- the recycled tobacco according to this embodiment preferably contains a fiber material. Since the recycled tobacco contains the fiber material, the recycled tobacco can be easily formed and its shape can be maintained.
- the type of fiber material is not particularly limited, an example thereof is pulp.
- As the pulp in addition to wood pulp such as softwood pulp and hardwood pulp, non-wood pulps such as flax pulp, sisal pulp, and espart, which are generally used for wrapping paper for tobacco products, may be used in combination.
- the amount of fiber material contained in the recycled tobacco is preferably 1 to 15% by mass, more preferably 3 to 10% by mass, when the mass of the recycled tobacco is 100% by mass.
- the recycled tobacco according to this embodiment can contain an aerosol generator.
- the aerosol generator refers to a material that generates an aerosol by being heated and then cooled.
- Examples of the aerosol generator include polyhydric alcohols such as glycerin, propylene glycol, sorbitol, xylitol, and erythritol, triacetin, and 1,3-butanediol. These may be used alone or in combination of two or more.
- the amount of the aerosol generating agent contained in the recycled tobacco is preferably 5 to 40% by mass, more preferably 10 to 25% by mass, when the mass of the recycled tobacco is 100% by mass.
- the regenerated tobacco according to the present embodiment can contain other materials such as a flavoring agent.
- the type of flavoring agent is not particularly limited, and from the viewpoint of imparting good flavor, menthol is particularly preferred.
- one type of fragrance may be used alone, or two or more types may be used in combination.
- the amount of other materials contained in the recycled tobacco is preferably 10% by mass or less, more preferably 5% by mass or less, when the mass of the recycled tobacco is 100% by mass.
- the recycled tobacco according to this embodiment does not need to contain any other materials.
- the recycled tobacco according to the present embodiment is preferably a sheet-shaped recycled tobacco, or a sheet-shaped recycled tobacco obtained by cutting the sheet-shaped recycled tobacco. Because recycled tobacco is in sheet form, each component such as tobacco material, tobacco components, binder, and aerosol generator can be homogenized, and when heated, the aerosol generator and flavor components are efficiently heated and atomized. be able to. Further, by cutting the sheet into pieces, it is possible to obtain manufacturing suitability such as increased efficiency during winding.
- the recycled tobacco is in the form of a sheet, the length and width of the sheet are not particularly limited and can be adjusted as appropriate depending on the manner of filling.
- the width of the cut sheets can be 0.4 to 1.5 mm, and the length of the cut sheets can be 5 to 15 mm, for example.
- the thickness of the sheet or sheet cut is preferably 50 to 800 ⁇ m, more preferably 100 to 600 ⁇ m, in view of the balance between heat transfer efficiency and strength.
- the recycled tobacco according to this embodiment may be a nonwoven tobacco sheet (laminate sheet).
- a laminate sheet is obtained by sandwiching a mixture containing a tobacco material, a tobacco component, and a binder between nonwoven fabrics, and molding the resulting laminate into a certain shape by heat welding.
- the method for producing recycled tobacco according to this embodiment includes the following steps. Step of extracting tobacco components from tobacco raw materials to obtain tobacco extract and tobacco residue (hereinafter also referred to as “extraction step”); After subjecting the tobacco residue to an alkali cooking treatment, the pH is adjusted to 4.0 to 6.5. (hereinafter also referred to as “alkaline cooking treatment step”); step of applying the tobacco extract back onto the tobacco residue after pH adjustment (hereinafter also referred to as "returning step”).
- the recycled tobacco according to the present embodiment can be manufactured simply and efficiently. Moreover, environmental load and costs can be reduced.
- the method according to the present embodiment may include other steps, such as a molding step, in addition to the extraction step, the alkali cooking treatment step, and the feeding back step.
- tobacco components are extracted from tobacco raw materials to obtain tobacco extract and tobacco residue.
- the method for extracting tobacco components from tobacco raw materials is not particularly limited, but for example, tobacco components can be extracted by immersing tobacco raw materials in a solvent. Alternatively, tobacco components may be volatilized from the tobacco raw material by heating the tobacco raw material, and the vapor may be recovered.
- the solvent When tobacco components are extracted by immersing tobacco raw materials in a solvent, examples of the solvent include water, alcohol such as ethanol, and ethyl acetate.
- the extraction temperature and extraction time depend on the extraction solvent, but can be, for example, 10 to 60°C for 1 to 3 hours.
- the heating temperature of the tobacco materials can be, for example, 150 to 300°C.
- the steam recovery method is not particularly limited, but for example, the generated steam may be cooled and recovered, or the generated vapor may be passed through a solvent such as distilled water, ethanol, hexane, 2-propanol, 1-propanol, propylene glycol, or glycerin. Examples include methods such as collecting the product in the solvent, collecting the product using an adsorbent, column, filter, etc., and then eluting it.
- Alkali cooking process In this step, the tobacco residue obtained in the extraction step is subjected to an alkali cooking treatment, and then the pH is adjusted to 4.0 to 6.5.
- Alkaline cooking treatment refers to adding an alkaline substance to raw materials and heat-treating them. Alkaline cooking treatments include the kraft pulp method using a mixture of sodium hydroxide and sodium sulfate, the soda pulp method using an aqueous sodium hydroxide solution, the acid sulfite method using bisulfite and sulfur dioxide gas, etc. Examples include the neutral sulfite method using sodium and bisulfite.
- the alkaline substance is not particularly limited, but alkali metal hydroxides are preferred, such as sodium hydroxide.
- the alkaline substance may be added as an aqueous solution of the alkaline substance.
- an alkaline substance is added as an aqueous solution (chemical solution) of an alkaline substance
- the amount of the chemical solution added depends on the pH of the chemical solution, but for example, the ratio of tobacco residue (g) to the chemical solution (mL) is 1:2 to 2.
- the ratio is preferably 1:100, more preferably 1:3 to 1:100, even more preferably 1:3 to 1:50, even more preferably 1:5 to 1:50. , 1:10 to 1:50 is particularly preferred.
- Alkaline cooking treatment is generally performed at 120 to 180°C. In this embodiment as well, it is possible to carry out the reaction at the above-mentioned general temperature, but the temperature is preferably 130 to 230°C, more preferably 150 to 180°C. Further, the treatment time of the alkaline cooking treatment is not particularly limited as long as it is a time that allows the tobacco residue to be sufficiently digested. Although it varies depending on the pH of the chemical solution used, etc., for example, it is preferably from 5 minutes to 6 hours, more preferably from 30 minutes to 6 hours, and even more preferably from 1 hour to 6 hours.
- the pH of the tobacco residue is adjusted to 4.0 to 6.5.
- the pH can be adjusted using a pH adjuster such as citric acid, hydrochloric acid, sulfuric acid, or nitric acid.
- the pH is preferably 4.5 to 6.0, more preferably 5.0 to 6.0.
- the pH of tobacco residue can be measured by the following method. Add 10 mL of ultrapure water to 1 g of tobacco residue sample, and shake at 200 rpm for 10 minutes. The pH of the obtained liquid is measured with a tabletop pH meter (trade name: SS211, manufactured by HORIBA).
- the tobacco extract liquid is poured back onto the tobacco residue after pH adjustment.
- the tobacco components previously removed from the tobacco raw material are returned to tobacco residue.
- Regenerated tobacco with a low specific heat can be obtained by using tobacco residue with a low specific heat as a base material and returning tobacco components to the base material.
- the method of applying the tobacco extract back onto the tobacco residue is not particularly limited.
- the tobacco residue can be recombined by adding and mixing a tobacco extract to the tobacco residue and allowing the tobacco extract to soak into the tobacco residue. After recoating, the tobacco residue containing the tobacco extract may be dried.
- the obtained recycled tobacco may be formed into a sheet shape, shredded sheet shape, or the like.
- a known method such as a papermaking method, a casting method, or a rolling method.
- a rolling method such as a papermaking method, a casting method, or a rolling method.
- cutting recycled tobacco that has been formed into a sheet it can be formed into a shredded sheet.
- the non-combustion heated flavor inhaler according to the present embodiment includes a tobacco-containing segment filled with the recycled tobacco according to the present embodiment. Since the non-combustion heated flavor inhaler according to the present embodiment includes the tobacco-containing segment filled with the recycled tobacco according to the present embodiment, when heating the tobacco-containing segment, the temperature of the tobacco-containing segment can be increased with less electric power. can be raised. Therefore, the power consumption per non-combustion heated flavor inhaler can be suppressed.
- FIG. 1 shows an example of the non-combustion heating type flavor inhaler according to this embodiment.
- a non-combustion heated flavor inhaler 1 shown in FIG. 1 includes a tobacco-containing segment 2 filled with recycled tobacco according to the present embodiment, a cylindrical cooling segment 3 having perforations 8 on the circumference, and a center hole segment. 4 and a filter segment 5.
- the non-combustion heated flavor inhaler according to the present embodiment may have other segments in addition to the tobacco-containing segment, the cooling segment, the center hole segment, and the filter segment.
- the axial length of the non-combustion heated flavor inhaler according to this embodiment is not particularly limited, but is preferably 40 mm or more and 90 mm or less, more preferably 50 mm or more and 75 mm or less, 50 mm or more, More preferably, it is 60 mm or less.
- the circumferential length of the non-combustion heating type flavor inhaler is preferably 16 mm or more and 25 mm or less, more preferably 20 mm or more and 24 mm or less, and even more preferably 21 mm or more and 23 mm or less.
- the tobacco-containing segment has a length of 20 mm
- the cooling segment has a length of 20 mm
- the center hole segment has a length of 8 mm
- the filter segment has a length of 7 mm.
- the length of the filter segment can be selected within the range of 4 mm or more and 10 mm or less.
- the ventilation resistance of the filter segment at this time can be selected to be 15 mmH 2 O/seg or more and 60 mmH 2 O/seg or less per segment.
- recycled tobacco In the tobacco-containing segment 2, recycled tobacco according to the present embodiment is filled in a wrapping paper (hereinafter also referred to as a wrapper).
- the method of filling the recycled tobacco into the paper is not particularly limited, but for example, the recycled tobacco may be wrapped in a wrapper, or the recycled tobacco may be filled in a cylindrical wrapper.
- the shape of the recycled tobacco has a longitudinal direction such as a rectangular shape, the recycled tobacco may be packed so that the longitudinal direction is in an unspecified direction within the wrapper, and the recycled tobacco may be packed in the axial direction of the tobacco-containing segment 2 or They may be packed in alignment in a direction perpendicular to the axial direction.
- the cooling segment 3 may include a cylindrical member 7.
- the cylindrical member 7 may be, for example, a paper tube made of cardboard processed into a cylindrical shape.
- the cylindrical member 7 and the mouthpiece lining paper 12, which will be described later, are provided with perforations 8 that pass through them both. Due to the presence of the perforations 8, outside air is introduced into the cooling segment 3 during suction. As a result, the vaporized aerosol component generated by heating the tobacco-containing segment 2 comes into contact with the outside air, and as its temperature decreases, it liquefies and forms an aerosol.
- the diameter (cross-length) of the perforation 8 is not particularly limited, but may be, for example, 0.5 mm or more and 1.5 mm or less.
- the number of perforations 8 is not particularly limited, and may be one or two or more. For example, a plurality of perforations 8 may be provided around the circumference of the cooling segment 3.
- the amount of outside air introduced through the perforations 8 is preferably 85% by volume or less, more preferably 80% by volume or less, based on the volume of the entire gas sucked by the user.
- the ratio of the amount of outside air is 85% by volume or less, reduction in flavor due to dilution by outside air can be sufficiently suppressed.
- this is also called the ventilation ratio in another way.
- the lower limit of the ventilation ratio range is preferably 55% by volume or more, more preferably 60% by volume or more.
- the cooling segment may also be a segment comprising a sheet of suitable construction material that is crimped, pleated, gathered, or folded.
- the cross-sectional profile of such elements may exhibit randomly oriented channels.
- the cooling segment may also include a bundle of longitudinally extending tubes.
- Such cooling segments may be formed, for example, from pleated, gathered, or folded sheet material wrapped in a paper wrapper.
- the axial length of the cooling segment can be, for example, 7 mm or more and 28 mm or less, and can be, for example, 18 mm.
- the cooling segment may also be substantially circular in its axial cross-sectional shape, and its diameter may be, for example, greater than or equal to 5 mm and less than or equal to 10 mm, such as about 7 mm.
- the center hole segment is composed of a filling layer having one or more hollow portions and an inner plug wrapper covering the filling layer.
- the center hole segment 4 includes a first filling layer 9 having a hollow portion and a first inner plug wrapper 10 covering the first filling layer 9.
- the center hole segment 4 has the function of increasing the strength of the mouthpiece segment 6.
- the first packed layer 9 has an inner diameter of 1.0 mm, for example, filled with cellulose acetate fibers at high density and hardened by adding a plasticizer containing triacetin from 6% by mass to 20% by mass based on the mass of cellulose acetate.
- the rod can have a diameter of 5.0 mm or less.
- the first packed layer 9 has a high packing density of fibers, during suction, air and aerosol flow only through the hollow portion, and hardly flow inside the first packed layer 9. Since the first filling layer 9 inside the center hole segment 4 is a fiber filling layer, the feel of the device from the outside during use is less likely to cause discomfort to the user. Note that the center hole segment 4 may not have the first inner plug wrapper 10 and its shape may be maintained by thermoforming.
- the structure of the filter segment 5 is not particularly limited, but may be composed of a single or plural filling layers. The outside of the packed layer may be wrapped with one or more wrapping papers.
- the ventilation resistance per segment of the filter segment 5 can be changed as appropriate depending on the amount of filler filled in the filter segment 5, the material, etc. For example, if the filling is cellulose acetate fibers, increasing the amount of cellulose acetate fibers filled into the filter segment 5 can increase the ventilation resistance. When the filling is cellulose acetate fibers, the packing density of the cellulose acetate fibers can be 0.13-0.18 g/cm 3 .
- the ventilation resistance is a value measured by a ventilation resistance measuring device (trade name: SODIMAX, manufactured by SODIM).
- the circumferential length of the filter segment 5 is not particularly limited, but is preferably 16 to 25 mm, more preferably 20 to 24 mm, and even more preferably 21 to 23 mm.
- the length of the filter segment 5 in the axial direction can be selected from 4 to 10 mm, and is selected so that its ventilation resistance is 15 to 60 mmH 2 O/seg.
- the length of the filter segment 5 in the axial direction is preferably 5 to 9 mm, more preferably 6 to 8 mm.
- the cross-sectional shape of the filter segment 5 is not particularly limited, but may be, for example, circular, elliptical, polygonal, or the like. Further, a rupturable capsule containing a fragrance, fragrance beads, or a fragrance may be directly added to the filter segment 5.
- the center hole segment 4 and the filter segment 5 can be connected with an outer plug wrapper (outer wrapping paper) 11.
- the outer plug wrapper 11 can be, for example, cylindrical paper.
- the tobacco-containing segment 2, the cooling segment 3, and the connected center hole segment 4 and filter segment 5 can be connected by a mouthpiece lining paper 12. These connections can be made, for example, by applying glue such as vinyl acetate glue to the inner surface of the mouthpiece lining paper 12, inserting the three segments, and winding the paper. Note that these segments may be connected multiple times using multiple lining papers.
- the non-combustion heating type flavor inhaler system according to the present embodiment includes the non-combustion heating type flavor inhaler according to the present embodiment, and a heating device that heats the tobacco-containing segment of the non-combustion heating type flavor inhaler. Since the non-combustion heated flavor suction system according to the present embodiment includes the non-combustion heated flavor suction device according to the present embodiment, it is possible to suppress power consumption per non-combustion heated flavor suction device. .
- the non-combustion heating type flavor suction system according to this embodiment may have other configurations in addition to the non-combustion heating type flavor inhaler and the heating device according to this embodiment.
- the non-combustion heated flavor suction system shown in FIG. 2 includes a non-combustion heated flavor suction device 1 according to the present embodiment, and a heating device 13 that heats the tobacco-containing segment of the non-combustion heated flavor suction device 1 from the outside. Equipped with.
- FIG. 2(a) shows the state before the non-combustion heating type flavor inhaler 1 is inserted into the heating device 13
- FIG. 2(b) shows the state before the non-combustion heating type flavor inhaler 1 is inserted into the heating device 13 and heated.
- the heating device 13 shown in FIG. 2 includes a body 14, a heater 15, a metal tube 16, a battery unit 17, and a control unit 18.
- the body 14 has a cylindrical recess 19, and a heater 15 and a metal tube are placed on the inner side surface of the recess 19 at a position corresponding to the tobacco-containing segment of the non-combustion heated flavor inhaler 1 inserted into the recess 19. 16 are arranged.
- the heater 15 can be an electric resistance heater, and electric power is supplied from the battery unit 17 according to instructions from a control unit 18 that performs temperature control, and the heater 15 is heated. Heat emitted from the heater 15 is transferred to the tobacco-containing segment of the non-combustion heated flavor inhaler 1 through a metal tube 16 with high thermal conductivity.
- FIG. 2(b) since it is schematically illustrated, there is a gap between the outer periphery of the non-combustion heating type flavor inhaler 1 and the inner periphery of the metal tube 16, but in reality, heat can be efficiently dissipated.
- the heating device 13 heats the tobacco-containing segment of the non-combustion heating flavor inhaler 1 from the outside, it may also heat the tobacco-containing segment from the inside.
- the heating temperature by the heating device is not particularly limited, but is preferably 400°C or less, more preferably 150°C or more and 400°C or less, and even more preferably 200°C or more and 350°C or less. Note that the heating temperature refers to the temperature of the heater of the heating device.
- the water absorption amount of the tobacco material was measured by the following method.
- a cylindrical container with 19 holes of 1 mm in diameter was prepared in a stainless steel tube of ⁇ 55 ⁇ 80 mm.
- a filter paper was placed in the cylindrical container, and 3 to 6 g of the tobacco material sample was placed thereon.
- a vat was filled with tap water, the cylindrical container was placed in the vat, and the mass was measured after 900 seconds to measure the amount of water absorbed per 1 g. The measurement was carried out three times, and the average value was taken as the amount of water absorbed at each time.
- the angle of repose of tobacco materials was measured by the following method. A sample of tobacco material was dropped using a funnel from 4 cm above a 25 mm x 25 mm measuring table (peak material). When the sample was dropped from the measuring table to the extent that it spilled, a photograph was taken and the angle was measured using image analysis software (Keyence Microscope). This measurement was carried out three times, and the average value was taken as the value of the angle of repose.
- the specific heat of the tobacco material As the specific heat of the tobacco material, the maximum specific heat capacity (mJ/mg ⁇ °C) up to 300°C was measured by DSC (differential scanning calorimetry). Specifically, the measurement was performed using a differential scanning calorimeter (trade name: DSC7020, manufactured by Hitachi High-Tech Science Co., Ltd.) under the following conditions. Temperature increase rate: 10° C./min, holding time: 2 minutes, pan: Al, sample mass: 10 mg, reference: Al 2 O 3 .
- Example 1 (Preparation of recycled tobacco) Yellow leaves were prepared as tobacco raw material. Water in an amount 12 times the mass of the raw material was added to the tobacco raw material, and the mixture was stirred at 50° C. and 300 rpm for 1 hour. Thereafter, the extract was collected by hand squeezing. Thereby, tobacco components were extracted from the tobacco raw material, and tobacco extract and tobacco residue were obtained. Next, 100 g/L of a 2 mol/L aqueous sodium hydroxide solution was added to the tobacco residue and heated at 180° C. for 3 hours. Thereafter, citric acid was added to adjust the pH to 5.6 to obtain a tobacco material. Regarding the tobacco material, the maximum absorbance at a wavelength of 3200 to 3600 cm -1 in FT-IR analysis, water absorption, angle of repose, and specific heat were measured, and stickiness was evaluated using the above method. The results are shown in Table 1.
- the tobacco extract was poured back onto the tobacco material.
- 100 parts by mass of tobacco material on which tobacco extract has been applied 3.7 parts by mass of guar gum as a binder, 3.7 parts by mass of softwood pulp as a fiber material, and 14 parts of glycerin as an aerosol generator. 6 parts by mass were mixed and formed into a sheet by a casting method.
- a sheet-shaped recycled tobacco was prepared. The thickness of the recycled tobacco was 428 ⁇ m, the density was 0.67 mg WB/mm 3 , the basis weight was 285 g WB/m 2 , the glycerin content was 12.7 mass % WB, and the water content was 12.1 mass % WB.
- the sheet-shaped recycled tobacco was filled into the tobacco-containing segment 2 of the non-combustion heating type flavor inhaler 1 shown in FIG. 1 to obtain a non-combustion heating type flavor inhaler.
- a heating test was conducted on the non-combustion heated flavor inhaler, and the amount of nicotine delivered and the amount of glycerin delivered were measured.
- the non-combustion heating type flavor inhaler 1 was inserted into the heating device 13 shown in FIG. 2, and the tobacco-containing segment was heated to 200°C. After preheating for 30 seconds, the amount of nicotine and glycerin contained in the inhaled mainstream smoke was measured by inhaling from the mouthpiece of the non-combustion heating type flavor inhaler 1.
- a suction machine (trade name: RM-20, manufactured by Borgwaldt) was used for suction. Suction (puffing) was performed once every 30 seconds with 55 ml for 2 seconds, a total of 10 times, and the amount of nicotine and glycerin was measured for each puff. The nicotine amount and glycerin amount were measured using GC-FID. The amount of nicotine delivered in each puff is shown in FIG. 3, and the amount of glycerin delivered in each puff is shown in FIG. 4. Furthermore, Table 1 shows the nicotine transfer rate to mainstream smoke per unit of power consumption (energy). However, nicotine and glycerin are shown as indicators of components from among a plurality of components contained in the recycled tobacco in this embodiment, and nicotine and glycerin are not particularly easily delivered.
- the tobacco extract was poured back onto the carbonized tobacco.
- 100 parts by mass of carbonized tobacco on which tobacco extract has been applied 3.7 parts by mass of guar gum as a binder, 3.7 parts by mass of softwood pulp as a fiber material, and 14 parts of glycerin as an aerosol generator. 6 parts by mass were mixed and molded into a sheet by a casting method.
- a sheet-shaped recycled tobacco was prepared.
- a non-combustion heated flavor inhaler was produced using the recycled tobacco in the same manner as in Example 1, and evaluated. The results are shown in FIG. 3, FIG. 4, and Table 1.
- Example 2 The tobacco extract obtained in Example 1 was added to activated carbon (trade name: Kuraray Coal, manufactured by Kuraray Co., Ltd.). A sheet-shaped regenerated tobacco was prepared in the same manner as in Example 1, except that the activated carbon was used in place of the tobacco residue on which the tobacco extract had been applied. Table 1 shows the measurement results of the specific heat and water absorption of the activated carbon itself, and the evaluation results of stickiness.
- activated carbon trade name: Kuraray Coal, manufactured by Kuraray Co., Ltd.
- Example 3 A tobacco extract and tobacco residue were obtained in the same manner as in Example 1. Thereafter, the tobacco extract was poured back onto the tobacco residue without subjecting the tobacco residue to an alkali cooking treatment. Other than that, a sheet-shaped recycled tobacco was prepared and evaluated in the same manner as in Example 1. Table 1 shows the measurement results of each physical property of the tobacco residue itself. Furthermore, the evaluation results of the non-combustion heating type flavor inhaler are shown in FIGS. 3, 4, and Table 1.
- the tobacco material is based on FT-IR analysis which shows a maximum absorbance of 0.40 or more at a wavelength of 3200 to 3600 cm -1 and a specific heat of 5 mJ/mg ⁇ °C or less.
- Example 1 in which regenerated tobacco was prepared using the regenerated tobacco, it was found in the evaluation of the non-combustion heated flavor inhaler containing the regenerated tobacco that the amount of nicotine and glycerin delivered was particularly large when the number of puffs increased. Additionally, the rate of nicotine transfer to mainstream smoke per unit of power consumption (energy) was also high (Table 1).
- Example 1 which shows the nicotine transfer rate to mainstream smoke per power consumption (energy) with respect to the specific heat of the base material of recycled cigarettes, in Example 1, the maximum It can be understood that by having an absorbance of 0.40 or more and a specific heat of 5 mJ/mg ⁇ ° C. or less, the nicotine transfer rate to mainstream smoke per unit of power consumption (energy) was improved. Further, from Table 1, it was found that the base material of Example 1 had a lower angle of repose than the base materials of Comparative Examples 1 and 3, making it easier to input the raw material at the time of inputting the raw material, and having excellent manufacturing suitability.
- Example 1 exhibited water absorption equivalent to that of the base materials of Comparative Examples 1 and 3, and the evaluation of stickiness was equivalent to that of the base materials of Comparative Examples 1 and 3. From this, it was found that there was no major change in the stickiness of the base material even if the alkali cooking treatment was performed, and the handling property was similarly excellent, and the raw material was easy to input.
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- Manufacture Of Tobacco Products (AREA)
Abstract
Provided is a reconstituted tobacco enabling control of power consumption per one non-combustion heating-type flavor inhaler during use. The reconstituted tobacco for a non-combustion heating-type flavor inhaler contains a tobacco material and a tobacco component, wherein the tobacco material has a maximum absorbance of 0.40 or more in the wavelength range of 3200 to 3600 cm-1 in a FT-IR analysis, and the specific heat of the tobacco material is 5 mJ / mg ・℃ or less.
Description
本発明は、非燃焼加熱型香味吸引器用再生たばこ及びその製造方法、非燃焼加熱型香味吸引器、並びに非燃焼加熱型香味吸引システムに関する。
The present invention relates to a regenerated tobacco for use in a non-combustion heating type flavor inhaler, a method for manufacturing the same, a non-combustion heating type flavor inhaler, and a non-combustion heating type flavor inhaler system.
燃焼型香味吸引器(シガレット)では、葉たばこを含むたばこ充填物を燃焼して香味を得る。該燃焼型香味吸引器の代替として、たばこ充填物を燃焼する代わりに加熱して香味を得る非燃焼加熱型香味吸引器が提案されている。非燃焼加熱型香味吸引器の加熱温度は、燃焼型香味吸引器の燃焼温度より低く、例えば約400℃以下である。このように、非燃焼加熱型香味吸引器の加熱温度は低いため、煙量を増加させる観点から、非燃焼加熱型香味吸引器ではたばこ充填物にグリセリン等のエアロゾル発生剤が添加される。エアロゾル発生剤は加熱により気化し、エアロゾルを発生する。該エアロゾルはたばこ成分等の香味成分を伴い使用者に供給されるため、使用者は十分な香味を得ることができる。
In combustion-type flavor inhalers (cigarettes), flavor is obtained by burning tobacco filler containing leaf tobacco. As an alternative to the combustion type flavor inhaler, a non-combustion heating type flavor inhaler has been proposed, which obtains flavor by heating the tobacco filling instead of burning it. The heating temperature of the non-combustion heating type flavor inhaler is lower than the combustion temperature of the combustion type flavor inhaler, for example, about 400° C. or less. As described above, since the heating temperature of the non-combustion heating type flavor inhaler is low, an aerosol generating agent such as glycerin is added to the tobacco filling in the non-combustion heating type flavor inhaler from the viewpoint of increasing the amount of smoke. The aerosol generator is vaporized by heating and generates an aerosol. Since the aerosol is supplied to the user along with a flavor component such as a tobacco component, the user can obtain a sufficient flavor.
非燃焼加熱型香味吸引器は、たばこ充填物が充填されたたばこ含有セグメントを例えば加熱装置のヒーターによって加熱することで使用することができる。加熱装置は通常電池ユニットを有し、該電池ユニットより電力が供給されることで、ヒーターの加熱が行われる。使用者の利便性の観点から、加熱装置を用いて非燃焼加熱型香味吸引器を使用する際に、電力消費量を抑制して、使用可能時間や使用可能本数を増加させることが望まれる。
A non-combustion heated flavor inhaler can be used by heating a tobacco-containing segment filled with tobacco filler, for example, with a heater of a heating device. The heating device usually has a battery unit, and the heater is heated by supplying electric power from the battery unit. From the viewpoint of user convenience, when using a non-combustion heated flavor inhaler using a heating device, it is desirable to suppress power consumption and increase the usable time and number of usable flavor inhalers.
一方、特許文献1には、たばこ原料をアルカリ性条件下で蒸解することにより、バニリン含有量が多い黒液が得られることが開示されている。
On the other hand, Patent Document 1 discloses that black liquor with a high vanillin content can be obtained by cooking tobacco raw materials under alkaline conditions.
製品のサイズを変更せずに電力消費量を抑制する方法の一つとして、非燃焼加熱型香味吸引器に含まれるたばこ材料を工夫することで、非燃焼加熱型香味吸引器1本あたりの電力消費量を抑制することが考えられる。
One way to reduce power consumption without changing the size of the product is to improve the tobacco materials contained in non-combustion heated flavor inhalers, thereby reducing the amount of electricity consumed per non-combustion heated flavor inhaler. It is possible to suppress consumption.
本発明は、使用時に、非燃焼加熱型香味吸引器1本あたりの電力消費量を抑制可能な再生たばこ、非燃焼加熱型香味吸引器、及び非燃焼加熱型香味吸引システムを提供することを目的とする。
An object of the present invention is to provide a regenerated cigarette, a non-combustion heating flavor suction device, and a non-combustion heating flavor suction system that can suppress power consumption per non-combustion heating flavor suction device during use. shall be.
本発明は以下の実施態様を含む。
The present invention includes the following embodiments.
[1]たばこ材料と、たばこ成分と、を含む非燃焼加熱型香味吸引器用の再生たばこであって、
前記たばこ材料はFT-IR分析にて波長3200~3600cm-1の最大吸光度が0.40以上であり、
前記たばこ材料の比熱が5mJ/mg・℃以下である、再生たばこ。 [1] Regenerated tobacco for use in a non-combustion heating flavor inhaler, which includes a tobacco material and a tobacco component,
The tobacco material has a maximum absorbance of 0.40 or more at a wavelength of 3200 to 3600 cm −1 in FT-IR analysis,
Regenerated tobacco, wherein the tobacco material has a specific heat of 5 mJ/mg·°C or less.
前記たばこ材料はFT-IR分析にて波長3200~3600cm-1の最大吸光度が0.40以上であり、
前記たばこ材料の比熱が5mJ/mg・℃以下である、再生たばこ。 [1] Regenerated tobacco for use in a non-combustion heating flavor inhaler, which includes a tobacco material and a tobacco component,
The tobacco material has a maximum absorbance of 0.40 or more at a wavelength of 3200 to 3600 cm −1 in FT-IR analysis,
Regenerated tobacco, wherein the tobacco material has a specific heat of 5 mJ/mg·°C or less.
[2]前記たばこ材料を23℃の水中に900秒浸漬した際の吸水量が4.0~6.0g/gである、[1]に記載の再生たばこ。
[2] The recycled tobacco according to [1], wherein the tobacco material has a water absorption amount of 4.0 to 6.0 g/g when immersed in water at 23° C. for 900 seconds.
[3]前記たばこ材料の安息角が40°以下である、[1]又は[2]に記載の再生たばこ。
[3] The recycled tobacco according to [1] or [2], wherein the tobacco material has an angle of repose of 40° or less.
[4]たばこ原料からたばこ成分を抽出して得られるたばこ抽出液を含む、[1]~[3]のいずれかに記載の再生たばこ。
[4] The regenerated tobacco according to any one of [1] to [3], which contains a tobacco extract obtained by extracting tobacco components from tobacco raw materials.
[5]さらにバインダを含む、[1]~[4]のいずれかに記載の再生たばこ。
[5] The recycled tobacco according to any one of [1] to [4], further comprising a binder.
[6]さらに繊維材料を含む、[1]~[5]のいずれかに記載の再生たばこ。
[6] The recycled tobacco according to any one of [1] to [5], further comprising a fiber material.
[7]シート状の再生たばこ、又は該シート状の再生たばこを裁断したシート刻状の再生たばこである、[1]~[6]のいずれかに記載の再生たばこ。
[7] The recycled tobacco according to any one of [1] to [6], which is a sheet-shaped recycled tobacco or a shredded sheet-shaped recycled tobacco obtained by cutting the sheet-shaped recycled tobacco.
[8][1]~[7]のいずれかに記載の再生たばこが充填された、たばこ含有セグメントを備える非燃焼加熱型香味吸引器。
[8] A non-combustion heated flavor inhaler comprising a tobacco-containing segment filled with the recycled tobacco according to any one of [1] to [7].
[9][8]に記載の非燃焼加熱型香味吸引器と、
前記たばこ含有セグメントを加熱する加熱装置と、
を備える非燃焼加熱型香味吸引システム。 [9] The non-combustion heated flavor inhaler according to [8],
a heating device for heating the tobacco-containing segment;
A non-combustion heated flavor suction system.
前記たばこ含有セグメントを加熱する加熱装置と、
を備える非燃焼加熱型香味吸引システム。 [9] The non-combustion heated flavor inhaler according to [8],
a heating device for heating the tobacco-containing segment;
A non-combustion heated flavor suction system.
[10][1]~[7]のいずれかに記載の再生たばこの製造方法であって、
たばこ原料からたばこ成分を抽出して、たばこ抽出液とたばこ残渣を得る工程と、
前記たばこ残渣をアルカリ蒸解処理した後、pHを4.0~6.5に調整する工程と、
pH調整後の前記たばこ残渣に前記たばこ抽出液をかけ戻す工程と、
を含む、方法。 [10] The method for producing recycled tobacco according to any one of [1] to [7],
a step of extracting tobacco components from tobacco raw materials to obtain tobacco extract and tobacco residue;
After subjecting the tobacco residue to alkaline cooking treatment, adjusting the pH to 4.0 to 6.5;
Sprinkling the tobacco extract back onto the tobacco residue after pH adjustment;
including methods.
たばこ原料からたばこ成分を抽出して、たばこ抽出液とたばこ残渣を得る工程と、
前記たばこ残渣をアルカリ蒸解処理した後、pHを4.0~6.5に調整する工程と、
pH調整後の前記たばこ残渣に前記たばこ抽出液をかけ戻す工程と、
を含む、方法。 [10] The method for producing recycled tobacco according to any one of [1] to [7],
a step of extracting tobacco components from tobacco raw materials to obtain tobacco extract and tobacco residue;
After subjecting the tobacco residue to alkaline cooking treatment, adjusting the pH to 4.0 to 6.5;
Sprinkling the tobacco extract back onto the tobacco residue after pH adjustment;
including methods.
[11]前記アルカリ蒸解処理が、前記たばこ残渣にアルカリ金属の水酸化物を添加し、130~230℃で5分間~6時間加熱する処理である、[10]に記載の方法。
[11] The method according to [10], wherein the alkaline cooking treatment is a treatment in which an alkali metal hydroxide is added to the tobacco residue and heated at 130 to 230°C for 5 minutes to 6 hours.
本発明によれば、使用時に、非燃焼加熱型香味吸引器1本あたりの電力消費量を抑制可能な再生たばこ、非燃焼加熱型香味吸引器、及び非燃焼加熱型香味吸引システムを提供することができる。
According to the present invention, it is possible to provide a recycled tobacco, a non-combustion heating flavor suction device, and a non-combustion heating flavor suction system that can suppress power consumption per non-combustion heating flavor suction device during use. Can be done.
本実施形態に係る再生たばこは、たばこ材料と、たばこ成分と、を含む非燃焼加熱型香味吸引器用の再生たばこである。ここで、前記たばこ材料はFT-IR分析にて波長3200~3600cm-1の最大吸光度が0.40以上である。また、前記たばこ材料の比熱は5mJ/mg・℃以下である。
The regenerated tobacco according to the present embodiment is a regenerated tobacco for use in a non-combustion heating type flavor inhaler that includes a tobacco material and a tobacco component. Here, the tobacco material has a maximum absorbance of 0.40 or more at a wavelength of 3200 to 3600 cm −1 as determined by FT-IR analysis. Further, the specific heat of the tobacco material is 5 mJ/mg·°C or less.
本発明者等は、非燃焼加熱型香味吸引器に含まれるたばこ材料として、低比熱のたばこ材料を使用することで、加熱効率が向上し、結果として非燃焼加熱型香味吸引器1本あたりの電力消費量を抑制できると考えた。本発明者等は鋭意検討した結果、FT-IR分析にて波長3200~3600cm-1の最大吸光度が0.40以上であり、かつ、比熱が5mJ/mg・℃以下であるたばこ材料と、たばこ成分と、を含む再生たばこを、非燃焼加熱型香味吸引器のたばこ材料として使用することで、非燃焼加熱型香味吸引器1本あたりの電力消費量を抑制できることを見出した。FT-IR分析にて波長3200~3600cm-1の吸収は水酸基の伸縮振動に由来する。例えばたばこ原料がアルカリ蒸解処理され、中和処理されることで、得られるたばこ材料の水酸基量が増加し、前記最大吸光度を増加させることができる。なお、この場合、たばこ原料はアルカリ蒸解処理後に中和されるため、前記最大吸光度の増加は遊離しているOH由来ではなく、たばこ材料に共有結合する水酸基に由来する。このように、たばこ材料の水酸基量がある一定以上になると、たばこ材料の比熱が低くなることを見出した。該たばこ材料を再生たばこの基材として用いることで、再生たばこの比熱を低減することができ、該再生たばこを加熱する際に、少ない電力で再生たばこの温度を上昇させることができる。したがって、非燃焼加熱型香味吸引器1本あたりの電力消費量を抑制することができる。なお、「再生たばこ」とは、たばこ成分と他の材料とが混合され、再構成されたたばこ材料を示す。
The present inventors have found that by using a tobacco material with a low specific heat as the tobacco material contained in a non-combustion heated flavor inhaler, the heating efficiency is improved, and as a result, the We thought that it would be possible to suppress power consumption. As a result of intensive studies, the present inventors have found that tobacco materials with a maximum absorbance of 0.40 or more at a wavelength of 3200 to 3600 cm -1 in FT-IR analysis and a specific heat of 5 mJ/mg・℃ or less, and tobacco It has been found that by using recycled tobacco containing these ingredients as the tobacco material for a non-combustion heating flavor inhaler, it is possible to suppress the power consumption per non-combustion heating flavor inhaler. In FT-IR analysis, absorption at wavelengths of 3200 to 3600 cm −1 is derived from stretching vibrations of hydroxyl groups. For example, by subjecting the tobacco raw material to an alkaline cooking treatment and neutralization treatment, the amount of hydroxyl groups in the resulting tobacco material increases, and the maximum absorbance can be increased. In this case, since the tobacco raw material is neutralized after the alkaline cooking treatment, the increase in maximum absorbance is not derived from free OH but from hydroxyl groups covalently bonded to the tobacco material. Thus, it has been found that when the amount of hydroxyl groups in the tobacco material exceeds a certain level, the specific heat of the tobacco material decreases. By using the tobacco material as a base material for recycled tobacco, the specific heat of the recycled tobacco can be reduced, and when heating the recycled tobacco, the temperature of the recycled tobacco can be increased with less electric power. Therefore, the power consumption per non-combustion heated flavor inhaler can be suppressed. Note that "regenerated tobacco" refers to tobacco materials that are reconstituted by mixing tobacco components and other materials.
本実施形態に係る再生たばこは、前記たばこ材料、たばこ成分以外にも、例えばバインダ、繊維材料、エアロゾル発生剤等を含むことができる。
The recycled tobacco according to the present embodiment can contain, for example, a binder, a fiber material, an aerosol generator, etc. in addition to the tobacco material and tobacco components.
(たばこ材料)
本実施形態に係るたばこ材料は、FT-IR分析にて波長3200~3600cm-1の最大吸光度が0.40以上である。水酸基の伸縮振動に由来する、波長3200~3600cm-1の範囲の最大吸光度が0.40以上であることにより、たばこ材料の比熱を低減でき、再生たばこ全体の比熱を低減できるため、非燃焼加熱型香味吸引器1本あたりの電力消費量を抑制することができる。前記波長3200~3600cm-1の最大吸光度は0.42以上であることが好ましく、0.45以上であることがより好ましい。前記波長3200~3600cm-1の最大吸光度の範囲の上限は特に限定されないが、例えば1.0以下であることができる。 (Tobacco material)
The tobacco material according to this embodiment has a maximum absorbance of 0.40 or more at a wavelength of 3200 to 3600 cm −1 in FT-IR analysis. By having a maximum absorbance of 0.40 or more in the wavelength range of 3200 to 3600 cm -1 , which is derived from the stretching vibration of hydroxyl groups, the specific heat of the tobacco material can be reduced, and the specific heat of the entire recycled tobacco can be reduced, so non-combustion heating The power consumption per one type flavor inhaler can be suppressed. The maximum absorbance at the wavelength of 3200 to 3600 cm −1 is preferably 0.42 or more, more preferably 0.45 or more. The upper limit of the range of maximum absorbance at wavelengths of 3200 to 3600 cm −1 is not particularly limited, but may be, for example, 1.0 or less.
本実施形態に係るたばこ材料は、FT-IR分析にて波長3200~3600cm-1の最大吸光度が0.40以上である。水酸基の伸縮振動に由来する、波長3200~3600cm-1の範囲の最大吸光度が0.40以上であることにより、たばこ材料の比熱を低減でき、再生たばこ全体の比熱を低減できるため、非燃焼加熱型香味吸引器1本あたりの電力消費量を抑制することができる。前記波長3200~3600cm-1の最大吸光度は0.42以上であることが好ましく、0.45以上であることがより好ましい。前記波長3200~3600cm-1の最大吸光度の範囲の上限は特に限定されないが、例えば1.0以下であることができる。 (Tobacco material)
The tobacco material according to this embodiment has a maximum absorbance of 0.40 or more at a wavelength of 3200 to 3600 cm −1 in FT-IR analysis. By having a maximum absorbance of 0.40 or more in the wavelength range of 3200 to 3600 cm -1 , which is derived from the stretching vibration of hydroxyl groups, the specific heat of the tobacco material can be reduced, and the specific heat of the entire recycled tobacco can be reduced, so non-combustion heating The power consumption per one type flavor inhaler can be suppressed. The maximum absorbance at the wavelength of 3200 to 3600 cm −1 is preferably 0.42 or more, more preferably 0.45 or more. The upper limit of the range of maximum absorbance at wavelengths of 3200 to 3600 cm −1 is not particularly limited, but may be, for example, 1.0 or less.
たばこ材料のFT-IR分析は、以下の方法により実施することができる。たばこ材料のサンプルをATR測定用ダイヤモンドクリスタルに密着させ、赤外吸収スペクトルを測定する。測定装置としては、フーリエ変換赤外分光装置(商品名:Thermo Scientific Nicolet iS50、Thermo Scientific社製)を用いることができる。測定方法:ATR法、分解能:4cm-1、積算回数:32回(n=2)の条件で測定を実施することができる。
FT-IR analysis of tobacco materials can be performed by the following method. A sample of tobacco material is brought into close contact with a diamond crystal for ATR measurement, and an infrared absorption spectrum is measured. As the measuring device, a Fourier transform infrared spectrometer (trade name: Thermo Scientific Nicolet iS50, manufactured by Thermo Scientific) can be used. Measurement method: ATR method, resolution: 4 cm −1 , number of integrations: 32 times (n=2).
たばこ材料の前記最大吸光度を0.40以上とする方法としては、例えばたばこ原料をアルカリ蒸解処理した後、中和する方法が挙げられる。たばこ原料としては、例えば葉たばこ、たばこの葉脈部、幹部、根、花等が挙げられ、これらは裁刻されていてもよく、粉末状であってもよい。前記葉たばこの種類は特に限定されず、どの品種も適用可能であるが、例えば黄色種、バーレー種、在来種、オリエント葉等や、それらの発酵葉等であることができる。これらのたばこ原料は一種を用いてもよく、二種以上を併用してもよい。特に、アルカリ蒸解処理を行うたばこ原料としては、たばこ原料からたばこ成分を含むたばこ抽出液を抽出した後のたばこ残渣であることが好ましい。通常は廃棄されるたばこ残渣を再利用できるため、環境負荷を低減でき、またコスト面でも有利なためである。さらに、得られるたばこ抽出液は、再生たばこのたばこ成分として使用することができる。アルカリ蒸解処理及び中和の方法としては、例えば後述する本実施形態に係る再生たばこの製造方法におけるアルカリ蒸解処理及び中和の方法が挙げられる。
As a method for making the maximum absorbance of the tobacco material 0.40 or more, for example, a method of subjecting the tobacco raw material to an alkaline cooking treatment and then neutralizing it can be mentioned. Examples of tobacco raw materials include leaf tobacco, tobacco leaf veins, stems, roots, and flowers, which may be shredded or powdered. The type of leaf tobacco is not particularly limited, and any variety can be used, but examples include yellow tobacco, burley tobacco, native tobacco, orient leaf, and fermented leaves thereof. One type of these tobacco raw materials may be used, or two or more types may be used in combination. In particular, the tobacco raw material to be subjected to the alkaline cooking treatment is preferably tobacco residue after extracting a tobacco extract containing tobacco components from the tobacco raw material. This is because tobacco residue, which would normally be discarded, can be reused, reducing environmental impact and being cost-effective. Furthermore, the obtained tobacco extract can be used as a tobacco component of recycled tobacco. Examples of the alkali cooking treatment and neutralization method include the alkali cooking treatment and neutralization method in the method for producing recycled tobacco according to the present embodiment, which will be described later.
前記たばこ材料の比熱は、5mJ/mg・℃以下である。該比熱が5mJ/mg・℃以下であることにより、再生たばこ全体の比熱を十分に低減でき、非燃焼加熱型香味吸引器1本あたりの電力消費量を抑制することができる。該比熱は4mJ/mg・℃以下であることが好ましく、3mJ/mg・℃以下であることがより好ましく、2mJ/mg・℃以下であることがさらに好ましい。該比熱は低ければ低い方が好ましく、該比熱の範囲の下限は特に限定されないが、例えば0.1mJ/mg・℃以上であることができる。なお、たばこ材料の比熱は、例えばFT-IR分析にて波長3200~3600cm-1の最大吸光度を0.40以上にすることにより、5mJ/mg・℃以下とすることができる。
The specific heat of the tobacco material is 5 mJ/mg·°C or less. When the specific heat is 5 mJ/mg·° C. or less, the specific heat of the entire recycled tobacco can be sufficiently reduced, and the power consumption per non-combustion heating flavor inhaler can be suppressed. The specific heat is preferably 4 mJ/mg·°C or less, more preferably 3 mJ/mg·°C or less, and even more preferably 2 mJ/mg·°C or less. The lower the specific heat is, the more preferable it is, and the lower limit of the range of the specific heat is not particularly limited, but can be, for example, 0.1 mJ/mg·°C or more. Note that the specific heat of the tobacco material can be reduced to 5 mJ/mg·° C. or less by, for example, setting the maximum absorbance at a wavelength of 3200 to 3600 cm −1 to 0.40 or more in FT-IR analysis.
たばこ材料の比熱は、DSC(示差走査熱量測定)により測定される、300℃までの最大比熱容量(mJ/mg・℃)で示される。例えば、示差走査熱量計(商品名:DSC7020、(株)日立ハイテクサイエンス製)を用いて、以下の条件により測定することができる。昇温速度:10℃/min、保持時間:2分、パン:Al、サンプル質量:10mg、リファレンス:Al2O3。
The specific heat of the tobacco material is indicated by the maximum specific heat capacity (mJ/mg·° C.) up to 300° C., measured by DSC (differential scanning calorimetry). For example, it can be measured using a differential scanning calorimeter (trade name: DSC7020, manufactured by Hitachi High-Tech Science Co., Ltd.) under the following conditions. Temperature increase rate: 10° C./min, holding time: 2 minutes, pan: Al, sample mass: 10 mg, reference: Al 2 O 3 .
前記たばこ材料を23℃の水中に900秒浸漬した際の吸水量は、4.0~6.0g/gであることが好ましい。前記吸水量が4.0~6.0g/gであることにより、べたつきが少なくハンドリング性に優れ、原料投入時に原料が投入しやすくなる。また、非燃焼加熱型香味吸引器の製造の巻き上げの際に、巻き上げがしやすくなる。前記吸水量は、4.2~5.8g/gであることがより好ましく、4.5~5.5g/gであることがさらに好ましい。
The amount of water absorbed when the tobacco material is immersed in water at 23° C. for 900 seconds is preferably 4.0 to 6.0 g/g. When the water absorption amount is 4.0 to 6.0 g/g, there is little stickiness and excellent handling properties, making it easier to input the raw materials. Further, it becomes easier to roll up the product when manufacturing a non-combustion heated flavor inhaler. The water absorption amount is more preferably 4.2 to 5.8 g/g, and even more preferably 4.5 to 5.5 g/g.
たばこ材料の前記吸水量は、以下の方法により測定することができる。φ55×80mmのステンレス管に1mm径の穴19個が開いた円筒容器を用意する。ろ紙を該円筒容器内に設置し、その上にたばこ材料のサンプルを3~6g入れる。バットに水道水を張り、バット内に該円筒容器を入れ、900秒後の質量を測定し、1g当たりの吸水量を測定する。該測定を3回実施し、その平均値を吸水量とする。
The water absorption amount of the tobacco material can be measured by the following method. A cylindrical container with 19 holes of 1 mm diameter in a stainless steel tube of φ55×80 mm is prepared. A filter paper is placed in the cylindrical container, and 3 to 6 g of the tobacco material sample is placed thereon. Fill a vat with tap water, place the cylindrical container in the vat, measure the mass after 900 seconds, and measure the amount of water absorbed per 1 g. This measurement is carried out three times, and the average value is taken as the water absorption amount.
前記たばこ材料の安息角は、40°以下であることが好ましい。該安息角が40°以下であることにより、再生たばこの製造において、原料投入時に原料が投入しやすくなり、製造上好ましい。該安息角は10~40°であることがより好ましく、20~30°であることがさらに好ましい。
The angle of repose of the tobacco material is preferably 40° or less. When the angle of repose is 40° or less, it becomes easier to input the raw material when inputting the raw material in the production of recycled tobacco, which is preferable in terms of production. The angle of repose is more preferably 10 to 40°, and even more preferably 20 to 30°.
たばこ材料の安息角は、以下の方法により測定することができる。25mm×25mmの計測台(ピーク材)の4cm上から漏斗にてたばこ材料のサンプルを落とす。計測台からサンプルがこぼれる程度まで落としたら写真を撮影し、画像解析ソフト(キーエンス社製顕微鏡)にて角度を測定する。この測定を3回実施し、その平均値を安息角の値とする。
The angle of repose of tobacco materials can be measured by the following method. A sample of tobacco material was dropped using a funnel from 4 cm above a 25 mm x 25 mm measuring table (peak material). Once the sample is dropped from the measuring table to the extent that it spills, a photograph is taken and the angle is measured using image analysis software (Keyence Microscope). This measurement is carried out three times, and the average value is taken as the value of the angle of repose.
再生たばこに含まれるたばこ材料の量は、再生たばこの質量を100質量%とするとき、20~80質量%であることが好ましく、20~65質量%であることがより好ましく、30~50質量%であることがさらに好ましい。
The amount of tobacco material contained in the recycled tobacco is preferably 20 to 80% by mass, more preferably 20 to 65% by mass, and 30 to 50% by mass when the mass of the recycled tobacco is 100% by mass. % is more preferable.
(たばこ成分)
たばこ成分は、前記たばこ原料に含まれるたばこ由来の成分であり、主な成分としては香喫味に寄与する成分が挙げられる。本実施形態に係る再生たばこは、たばこ成分を単体として含んでもよいが、たばこ原料からたばこ成分を抽出して得られるたばこ抽出液として含むことが好ましい。この場合、たばこ抽出液を抽出した後のたばこ残渣は、たばこ材料の原料として使用することができるため、環境負荷を低減でき、またコスト面でも有利である。再生たばこに含まれるたばこ成分の量は、目的とする香味に応じて適宜設定することができる。 (Tobacco ingredient)
The tobacco component is a tobacco-derived component contained in the tobacco raw material, and main components include components that contribute to aroma and taste. Although the recycled tobacco according to the present embodiment may contain the tobacco component alone, it is preferably contained as a tobacco extract obtained by extracting the tobacco component from the tobacco raw material. In this case, the tobacco residue after extracting the tobacco extract can be used as a raw material for tobacco materials, which reduces environmental impact and is also advantageous in terms of cost. The amount of tobacco components contained in the recycled tobacco can be appropriately set depending on the desired flavor.
たばこ成分は、前記たばこ原料に含まれるたばこ由来の成分であり、主な成分としては香喫味に寄与する成分が挙げられる。本実施形態に係る再生たばこは、たばこ成分を単体として含んでもよいが、たばこ原料からたばこ成分を抽出して得られるたばこ抽出液として含むことが好ましい。この場合、たばこ抽出液を抽出した後のたばこ残渣は、たばこ材料の原料として使用することができるため、環境負荷を低減でき、またコスト面でも有利である。再生たばこに含まれるたばこ成分の量は、目的とする香味に応じて適宜設定することができる。 (Tobacco ingredient)
The tobacco component is a tobacco-derived component contained in the tobacco raw material, and main components include components that contribute to aroma and taste. Although the recycled tobacco according to the present embodiment may contain the tobacco component alone, it is preferably contained as a tobacco extract obtained by extracting the tobacco component from the tobacco raw material. In this case, the tobacco residue after extracting the tobacco extract can be used as a raw material for tobacco materials, which reduces environmental impact and is also advantageous in terms of cost. The amount of tobacco components contained in the recycled tobacco can be appropriately set depending on the desired flavor.
(バインダ)
本実施形態に係る再生たばこは、バインダを含むことが好ましい。再生たばこがバインダを含むことで、各原料を結合することができ、所望の形状に好適に成形することができる。バインダの種類は特に限定されないが、例えばグアーガム、キサンタンガム、CMC(カルボキシメチルセルロース)、CMC-Na(カルボキシメチルセルロースのナトリウム塩)、ワキシーコーンスターチ、馬鈴薯等が挙げられる。これらは一種を用いてもよく、二種以上を併用してもよい。再生たばこに含まれるバインダの量は、再生たばこの質量を100質量%とするとき、1~10質量%であることが好ましく、3~6質量%であることがより好ましい。 (binder)
The recycled tobacco according to this embodiment preferably contains a binder. Since the recycled tobacco contains a binder, each raw material can be bonded together, and the recycled tobacco can be suitably molded into a desired shape. The type of binder is not particularly limited, but examples include guar gum, xanthan gum, CMC (carboxymethylcellulose), CMC-Na (sodium salt of carboxymethylcellulose), waxy corn starch, and potato. These may be used alone or in combination of two or more. The amount of binder contained in the recycled tobacco is preferably 1 to 10% by mass, more preferably 3 to 6% by mass, when the mass of the recycled tobacco is 100% by mass.
本実施形態に係る再生たばこは、バインダを含むことが好ましい。再生たばこがバインダを含むことで、各原料を結合することができ、所望の形状に好適に成形することができる。バインダの種類は特に限定されないが、例えばグアーガム、キサンタンガム、CMC(カルボキシメチルセルロース)、CMC-Na(カルボキシメチルセルロースのナトリウム塩)、ワキシーコーンスターチ、馬鈴薯等が挙げられる。これらは一種を用いてもよく、二種以上を併用してもよい。再生たばこに含まれるバインダの量は、再生たばこの質量を100質量%とするとき、1~10質量%であることが好ましく、3~6質量%であることがより好ましい。 (binder)
The recycled tobacco according to this embodiment preferably contains a binder. Since the recycled tobacco contains a binder, each raw material can be bonded together, and the recycled tobacco can be suitably molded into a desired shape. The type of binder is not particularly limited, but examples include guar gum, xanthan gum, CMC (carboxymethylcellulose), CMC-Na (sodium salt of carboxymethylcellulose), waxy corn starch, and potato. These may be used alone or in combination of two or more. The amount of binder contained in the recycled tobacco is preferably 1 to 10% by mass, more preferably 3 to 6% by mass, when the mass of the recycled tobacco is 100% by mass.
(繊維材料)
本実施形態に係る再生たばこは、繊維材料を含むことが好ましい。再生たばこが繊維材料を含むことで、再生たばこを成形する際に形成しやすく、またその形状を維持することができる。繊維材料の種類は特に限定されないが、例えばパルプが挙げられる。パルプとしては、針葉樹パルプや広葉樹パルプ等の木材パルプ以外にも、亜麻パルプ、サイザル麻パルプ、エスパルトなど一般的にたばこ製品用の巻紙に使用される非木材パルプを併用してもよい。再生たばこに含まれる繊維材料の量は、再生たばこの質量を100質量%とするとき、1~15質量%であることが好ましく、3~10質量%であることがより好ましい。 (fiber material)
The recycled tobacco according to this embodiment preferably contains a fiber material. Since the recycled tobacco contains the fiber material, the recycled tobacco can be easily formed and its shape can be maintained. Although the type of fiber material is not particularly limited, an example thereof is pulp. As the pulp, in addition to wood pulp such as softwood pulp and hardwood pulp, non-wood pulps such as flax pulp, sisal pulp, and espart, which are generally used for wrapping paper for tobacco products, may be used in combination. The amount of fiber material contained in the recycled tobacco is preferably 1 to 15% by mass, more preferably 3 to 10% by mass, when the mass of the recycled tobacco is 100% by mass.
本実施形態に係る再生たばこは、繊維材料を含むことが好ましい。再生たばこが繊維材料を含むことで、再生たばこを成形する際に形成しやすく、またその形状を維持することができる。繊維材料の種類は特に限定されないが、例えばパルプが挙げられる。パルプとしては、針葉樹パルプや広葉樹パルプ等の木材パルプ以外にも、亜麻パルプ、サイザル麻パルプ、エスパルトなど一般的にたばこ製品用の巻紙に使用される非木材パルプを併用してもよい。再生たばこに含まれる繊維材料の量は、再生たばこの質量を100質量%とするとき、1~15質量%であることが好ましく、3~10質量%であることがより好ましい。 (fiber material)
The recycled tobacco according to this embodiment preferably contains a fiber material. Since the recycled tobacco contains the fiber material, the recycled tobacco can be easily formed and its shape can be maintained. Although the type of fiber material is not particularly limited, an example thereof is pulp. As the pulp, in addition to wood pulp such as softwood pulp and hardwood pulp, non-wood pulps such as flax pulp, sisal pulp, and espart, which are generally used for wrapping paper for tobacco products, may be used in combination. The amount of fiber material contained in the recycled tobacco is preferably 1 to 15% by mass, more preferably 3 to 10% by mass, when the mass of the recycled tobacco is 100% by mass.
(エアロゾル発生剤)
本実施形態に係る再生たばこは、エアロゾル発生剤を含むことができる。エアロゾル発生剤とは、加熱後、冷却されることによりエアロゾルを生成する材料を示す。エアロゾル発生剤としては、例えばグリセリン、プロピレングリコール、ソルビトール、キシリトール、エリスリトール等の多価アルコール、トリアセチン、1,3-ブタンジオール等が挙げられる。これらは一種を用いてもよく、二種以上を併用してもよい。再生たばこに含まれるエアロゾル発生剤の量は、再生たばこの質量を100質量%とするとき、5~40質量%であることが好ましく、10~25質量%であることがより好ましい。 (aerosol generator)
The recycled tobacco according to this embodiment can contain an aerosol generator. The aerosol generator refers to a material that generates an aerosol by being heated and then cooled. Examples of the aerosol generator include polyhydric alcohols such as glycerin, propylene glycol, sorbitol, xylitol, and erythritol, triacetin, and 1,3-butanediol. These may be used alone or in combination of two or more. The amount of the aerosol generating agent contained in the recycled tobacco is preferably 5 to 40% by mass, more preferably 10 to 25% by mass, when the mass of the recycled tobacco is 100% by mass.
本実施形態に係る再生たばこは、エアロゾル発生剤を含むことができる。エアロゾル発生剤とは、加熱後、冷却されることによりエアロゾルを生成する材料を示す。エアロゾル発生剤としては、例えばグリセリン、プロピレングリコール、ソルビトール、キシリトール、エリスリトール等の多価アルコール、トリアセチン、1,3-ブタンジオール等が挙げられる。これらは一種を用いてもよく、二種以上を併用してもよい。再生たばこに含まれるエアロゾル発生剤の量は、再生たばこの質量を100質量%とするとき、5~40質量%であることが好ましく、10~25質量%であることがより好ましい。 (aerosol generator)
The recycled tobacco according to this embodiment can contain an aerosol generator. The aerosol generator refers to a material that generates an aerosol by being heated and then cooled. Examples of the aerosol generator include polyhydric alcohols such as glycerin, propylene glycol, sorbitol, xylitol, and erythritol, triacetin, and 1,3-butanediol. These may be used alone or in combination of two or more. The amount of the aerosol generating agent contained in the recycled tobacco is preferably 5 to 40% by mass, more preferably 10 to 25% by mass, when the mass of the recycled tobacco is 100% by mass.
(その他材料)
本実施形態に係る再生たばこは、前記たばこ材料、前記たばこ成分、前記バインダ、前記繊維材料、前記エアロゾル発生剤以外にも、例えば香料等のその他材料を含むことができる。香料の種類は、特に限定されず、良好な香味の付与の観点から、特に好ましくはメンソールである。また、香料は1種を単独で用いても良いし、2種以上を併用しても良い。再生たばこに含まれるその他材料の量は、再生たばこの質量を100質量%とするとき、10質量%以下であることが好ましく、5質量%以下であることがより好ましい。本実施形態に係る再生たばこは、その他材料を含まなくてもよい。 (Other materials)
In addition to the tobacco material, the tobacco component, the binder, the fiber material, and the aerosol generator, the regenerated tobacco according to the present embodiment can contain other materials such as a flavoring agent. The type of flavoring agent is not particularly limited, and from the viewpoint of imparting good flavor, menthol is particularly preferred. Moreover, one type of fragrance may be used alone, or two or more types may be used in combination. The amount of other materials contained in the recycled tobacco is preferably 10% by mass or less, more preferably 5% by mass or less, when the mass of the recycled tobacco is 100% by mass. The recycled tobacco according to this embodiment does not need to contain any other materials.
本実施形態に係る再生たばこは、前記たばこ材料、前記たばこ成分、前記バインダ、前記繊維材料、前記エアロゾル発生剤以外にも、例えば香料等のその他材料を含むことができる。香料の種類は、特に限定されず、良好な香味の付与の観点から、特に好ましくはメンソールである。また、香料は1種を単独で用いても良いし、2種以上を併用しても良い。再生たばこに含まれるその他材料の量は、再生たばこの質量を100質量%とするとき、10質量%以下であることが好ましく、5質量%以下であることがより好ましい。本実施形態に係る再生たばこは、その他材料を含まなくてもよい。 (Other materials)
In addition to the tobacco material, the tobacco component, the binder, the fiber material, and the aerosol generator, the regenerated tobacco according to the present embodiment can contain other materials such as a flavoring agent. The type of flavoring agent is not particularly limited, and from the viewpoint of imparting good flavor, menthol is particularly preferred. Moreover, one type of fragrance may be used alone, or two or more types may be used in combination. The amount of other materials contained in the recycled tobacco is preferably 10% by mass or less, more preferably 5% by mass or less, when the mass of the recycled tobacco is 100% by mass. The recycled tobacco according to this embodiment does not need to contain any other materials.
(再生たばこの形状)
本実施形態に係る再生たばこは、シート状の再生たばこ、又は該シート状の再生たばこを裁断したシート刻状の再生たばこであることが好ましい。再生たばこがシート状であることにより、たばこ材料、たばこ成分、バインダ、エアロゾル発生剤等の各成分を均質化することができ、加熱時に効率的にエアロゾル発生剤や香味成分を加熱し霧化することができる。また、シート刻みにすることによって巻き上げ時の効率化などの製造適正を得ることができる。再生たばこがシート状である場合、シートの長さ及び幅は、特段制限されることはなく、充填する態様に合わせて適宜調整できる。再生たばこがシート刻状である場合、例えばシート刻の幅は0.4~1.5mm、シート刻の長さは5~15mmであることができる。シート又はシート刻の厚さは、伝熱効率と強度の兼ね合いから、50~800μmが好ましく、100~600μmがより好ましい。 (Shape of recycled cigarettes)
The recycled tobacco according to the present embodiment is preferably a sheet-shaped recycled tobacco, or a sheet-shaped recycled tobacco obtained by cutting the sheet-shaped recycled tobacco. Because recycled tobacco is in sheet form, each component such as tobacco material, tobacco components, binder, and aerosol generator can be homogenized, and when heated, the aerosol generator and flavor components are efficiently heated and atomized. be able to. Further, by cutting the sheet into pieces, it is possible to obtain manufacturing suitability such as increased efficiency during winding. When the recycled tobacco is in the form of a sheet, the length and width of the sheet are not particularly limited and can be adjusted as appropriate depending on the manner of filling. When the recycled tobacco is cut into sheets, the width of the cut sheets can be 0.4 to 1.5 mm, and the length of the cut sheets can be 5 to 15 mm, for example. The thickness of the sheet or sheet cut is preferably 50 to 800 μm, more preferably 100 to 600 μm, in view of the balance between heat transfer efficiency and strength.
本実施形態に係る再生たばこは、シート状の再生たばこ、又は該シート状の再生たばこを裁断したシート刻状の再生たばこであることが好ましい。再生たばこがシート状であることにより、たばこ材料、たばこ成分、バインダ、エアロゾル発生剤等の各成分を均質化することができ、加熱時に効率的にエアロゾル発生剤や香味成分を加熱し霧化することができる。また、シート刻みにすることによって巻き上げ時の効率化などの製造適正を得ることができる。再生たばこがシート状である場合、シートの長さ及び幅は、特段制限されることはなく、充填する態様に合わせて適宜調整できる。再生たばこがシート刻状である場合、例えばシート刻の幅は0.4~1.5mm、シート刻の長さは5~15mmであることができる。シート又はシート刻の厚さは、伝熱効率と強度の兼ね合いから、50~800μmが好ましく、100~600μmがより好ましい。 (Shape of recycled cigarettes)
The recycled tobacco according to the present embodiment is preferably a sheet-shaped recycled tobacco, or a sheet-shaped recycled tobacco obtained by cutting the sheet-shaped recycled tobacco. Because recycled tobacco is in sheet form, each component such as tobacco material, tobacco components, binder, and aerosol generator can be homogenized, and when heated, the aerosol generator and flavor components are efficiently heated and atomized. be able to. Further, by cutting the sheet into pieces, it is possible to obtain manufacturing suitability such as increased efficiency during winding. When the recycled tobacco is in the form of a sheet, the length and width of the sheet are not particularly limited and can be adjusted as appropriate depending on the manner of filling. When the recycled tobacco is cut into sheets, the width of the cut sheets can be 0.4 to 1.5 mm, and the length of the cut sheets can be 5 to 15 mm, for example. The thickness of the sheet or sheet cut is preferably 50 to 800 μm, more preferably 100 to 600 μm, in view of the balance between heat transfer efficiency and strength.
また、本実施形態に係る再生たばこは、不織布状のたばこシート(ラミネートシート)であってもよい。ラミネートシートは、たばこ材料と、たばこ成分と、バインダとを含む混合物を不織布によって挟み、得られる積層物を熱溶着によって一定形状に成形して得られる。
Furthermore, the recycled tobacco according to this embodiment may be a nonwoven tobacco sheet (laminate sheet). A laminate sheet is obtained by sandwiching a mixture containing a tobacco material, a tobacco component, and a binder between nonwoven fabrics, and molding the resulting laminate into a certain shape by heat welding.
[再生たばこの製造方法]
本実施形態に係る再生たばこの製造方法は、以下の工程を含む。たばこ原料からたばこ成分を抽出して、たばこ抽出液とたばこ残渣を得る工程(以下、「抽出工程」ともいう。);前記たばこ残渣をアルカリ蒸解処理した後、pHを4.0~6.5に調整する工程(以下、「アルカリ蒸解処理工程」ともいう。);pH調整後の前記たばこ残渣に前記たばこ抽出液をかけ戻す工程(以下、「かけ戻し工程」ともいう。)。前記方法によれば、本実施形態に係る再生たばこを簡便に、効率よく製造することができる。また、環境負荷及びコストを低減することができる。本実施形態に係る方法は、抽出工程、アルカリ蒸解処理工程、かけ戻し工程以外にも、例えば成形工程等の他の工程を含んでもよい。 [Method for manufacturing recycled cigarettes]
The method for producing recycled tobacco according to this embodiment includes the following steps. Step of extracting tobacco components from tobacco raw materials to obtain tobacco extract and tobacco residue (hereinafter also referred to as "extraction step"); After subjecting the tobacco residue to an alkali cooking treatment, the pH is adjusted to 4.0 to 6.5. (hereinafter also referred to as "alkaline cooking treatment step"); step of applying the tobacco extract back onto the tobacco residue after pH adjustment (hereinafter also referred to as "returning step"). According to the method, the recycled tobacco according to the present embodiment can be manufactured simply and efficiently. Moreover, environmental load and costs can be reduced. The method according to the present embodiment may include other steps, such as a molding step, in addition to the extraction step, the alkali cooking treatment step, and the feeding back step.
本実施形態に係る再生たばこの製造方法は、以下の工程を含む。たばこ原料からたばこ成分を抽出して、たばこ抽出液とたばこ残渣を得る工程(以下、「抽出工程」ともいう。);前記たばこ残渣をアルカリ蒸解処理した後、pHを4.0~6.5に調整する工程(以下、「アルカリ蒸解処理工程」ともいう。);pH調整後の前記たばこ残渣に前記たばこ抽出液をかけ戻す工程(以下、「かけ戻し工程」ともいう。)。前記方法によれば、本実施形態に係る再生たばこを簡便に、効率よく製造することができる。また、環境負荷及びコストを低減することができる。本実施形態に係る方法は、抽出工程、アルカリ蒸解処理工程、かけ戻し工程以外にも、例えば成形工程等の他の工程を含んでもよい。 [Method for manufacturing recycled cigarettes]
The method for producing recycled tobacco according to this embodiment includes the following steps. Step of extracting tobacco components from tobacco raw materials to obtain tobacco extract and tobacco residue (hereinafter also referred to as "extraction step"); After subjecting the tobacco residue to an alkali cooking treatment, the pH is adjusted to 4.0 to 6.5. (hereinafter also referred to as "alkaline cooking treatment step"); step of applying the tobacco extract back onto the tobacco residue after pH adjustment (hereinafter also referred to as "returning step"). According to the method, the recycled tobacco according to the present embodiment can be manufactured simply and efficiently. Moreover, environmental load and costs can be reduced. The method according to the present embodiment may include other steps, such as a molding step, in addition to the extraction step, the alkali cooking treatment step, and the feeding back step.
(抽出工程)
本工程では、たばこ原料からたばこ成分を抽出して、たばこ抽出液とたばこ残渣を得る。たばこ原料からたばこ成分を抽出する方法は特に限定されないが、例えばたばこ原料を溶媒に浸漬してたばこ成分を抽出することができる。また、たばこ原料を加熱してたばこ原料からたばこ成分を揮発させ、その蒸気を回収してもよい。 (Extraction process)
In this step, tobacco components are extracted from tobacco raw materials to obtain tobacco extract and tobacco residue. The method for extracting tobacco components from tobacco raw materials is not particularly limited, but for example, tobacco components can be extracted by immersing tobacco raw materials in a solvent. Alternatively, tobacco components may be volatilized from the tobacco raw material by heating the tobacco raw material, and the vapor may be recovered.
本工程では、たばこ原料からたばこ成分を抽出して、たばこ抽出液とたばこ残渣を得る。たばこ原料からたばこ成分を抽出する方法は特に限定されないが、例えばたばこ原料を溶媒に浸漬してたばこ成分を抽出することができる。また、たばこ原料を加熱してたばこ原料からたばこ成分を揮発させ、その蒸気を回収してもよい。 (Extraction process)
In this step, tobacco components are extracted from tobacco raw materials to obtain tobacco extract and tobacco residue. The method for extracting tobacco components from tobacco raw materials is not particularly limited, but for example, tobacco components can be extracted by immersing tobacco raw materials in a solvent. Alternatively, tobacco components may be volatilized from the tobacco raw material by heating the tobacco raw material, and the vapor may be recovered.
たばこ原料を溶媒に浸漬してたばこ成分を抽出する場合、該溶媒としては、例えば水、エタノール等のアルコール、酢酸エチル等が挙げられる。抽出温度、抽出時間は抽出溶媒にもよるが、例えば10~60℃で1~3時間であることができる。たばこ原料を加熱してたばこ原料からたばこ成分を揮発させ、その蒸気を回収する場合、たばこ材料の加熱温度は例えば150~300℃であることができる。蒸気の回収方法は特に限定されないが、例えば生成する蒸気を冷却して回収する、生成する蒸気を蒸留水、エタノール、ヘキサン、2-プロパノール、1-プロパノール、プロピレングリコール、グリセリン等の溶媒中に通過させて該溶媒中に捕集する、吸着剤やカラム、フィルター等を用いて捕集しその後溶出させる等の方法が挙げられる。
When tobacco components are extracted by immersing tobacco raw materials in a solvent, examples of the solvent include water, alcohol such as ethanol, and ethyl acetate. The extraction temperature and extraction time depend on the extraction solvent, but can be, for example, 10 to 60°C for 1 to 3 hours. When heating tobacco raw materials to volatilize tobacco components from the tobacco raw materials and recovering the vapor, the heating temperature of the tobacco materials can be, for example, 150 to 300°C. The steam recovery method is not particularly limited, but for example, the generated steam may be cooled and recovered, or the generated vapor may be passed through a solvent such as distilled water, ethanol, hexane, 2-propanol, 1-propanol, propylene glycol, or glycerin. Examples include methods such as collecting the product in the solvent, collecting the product using an adsorbent, column, filter, etc., and then eluting it.
(アルカリ蒸解処理工程)
本工程では、前記抽出工程で得られたたばこ残渣をアルカリ蒸解処理した後、pHを4.0~6.5に調整する。アルカリ蒸解処理とは、原料にアルカリ性物質を添加し、加熱処理することを示す。アルカリ蒸解処理としては、水酸化ナトリウムと硫酸ナトリウムの混合液を使用するクラフトパルプ法、水酸化ナトリウム水溶液を使用するソーダパルプ法、重亜硫酸塩および亜硫酸ガス等を使用する酸性亜硫酸塩法、水酸化ナトリウムと重亜硫酸塩を使用する中性亜硫酸塩法等が挙げられる。アルカリ性物質としては特に限定されないが、アルカリ金属の水酸化物が好ましく、例えば水酸化ナトリウム等が挙げられる。アルカリ性物質はアルカリ性物質の水溶液として添加してもよい。アルカリ性物質をアルカリ性物質の水溶液(薬液)として添加する場合、薬液の添加量としては、薬液のpHにもよるが、例えばたばこ残渣(g)と薬液(mL)との比が、1:2~1:100であることが好ましく、1:3~1:100であることがより好ましく、1:3~1:50であることが更に好ましく、1:5~1:50であることが更に好ましく、1:10~1:50であることが特に好ましい。 (Alkali cooking process)
In this step, the tobacco residue obtained in the extraction step is subjected to an alkali cooking treatment, and then the pH is adjusted to 4.0 to 6.5. Alkaline cooking treatment refers to adding an alkaline substance to raw materials and heat-treating them. Alkaline cooking treatments include the kraft pulp method using a mixture of sodium hydroxide and sodium sulfate, the soda pulp method using an aqueous sodium hydroxide solution, the acid sulfite method using bisulfite and sulfur dioxide gas, etc. Examples include the neutral sulfite method using sodium and bisulfite. The alkaline substance is not particularly limited, but alkali metal hydroxides are preferred, such as sodium hydroxide. The alkaline substance may be added as an aqueous solution of the alkaline substance. When an alkaline substance is added as an aqueous solution (chemical solution) of an alkaline substance, the amount of the chemical solution added depends on the pH of the chemical solution, but for example, the ratio of tobacco residue (g) to the chemical solution (mL) is 1:2 to 2. The ratio is preferably 1:100, more preferably 1:3 to 1:100, even more preferably 1:3 to 1:50, even more preferably 1:5 to 1:50. , 1:10 to 1:50 is particularly preferred.
本工程では、前記抽出工程で得られたたばこ残渣をアルカリ蒸解処理した後、pHを4.0~6.5に調整する。アルカリ蒸解処理とは、原料にアルカリ性物質を添加し、加熱処理することを示す。アルカリ蒸解処理としては、水酸化ナトリウムと硫酸ナトリウムの混合液を使用するクラフトパルプ法、水酸化ナトリウム水溶液を使用するソーダパルプ法、重亜硫酸塩および亜硫酸ガス等を使用する酸性亜硫酸塩法、水酸化ナトリウムと重亜硫酸塩を使用する中性亜硫酸塩法等が挙げられる。アルカリ性物質としては特に限定されないが、アルカリ金属の水酸化物が好ましく、例えば水酸化ナトリウム等が挙げられる。アルカリ性物質はアルカリ性物質の水溶液として添加してもよい。アルカリ性物質をアルカリ性物質の水溶液(薬液)として添加する場合、薬液の添加量としては、薬液のpHにもよるが、例えばたばこ残渣(g)と薬液(mL)との比が、1:2~1:100であることが好ましく、1:3~1:100であることがより好ましく、1:3~1:50であることが更に好ましく、1:5~1:50であることが更に好ましく、1:10~1:50であることが特に好ましい。 (Alkali cooking process)
In this step, the tobacco residue obtained in the extraction step is subjected to an alkali cooking treatment, and then the pH is adjusted to 4.0 to 6.5. Alkaline cooking treatment refers to adding an alkaline substance to raw materials and heat-treating them. Alkaline cooking treatments include the kraft pulp method using a mixture of sodium hydroxide and sodium sulfate, the soda pulp method using an aqueous sodium hydroxide solution, the acid sulfite method using bisulfite and sulfur dioxide gas, etc. Examples include the neutral sulfite method using sodium and bisulfite. The alkaline substance is not particularly limited, but alkali metal hydroxides are preferred, such as sodium hydroxide. The alkaline substance may be added as an aqueous solution of the alkaline substance. When an alkaline substance is added as an aqueous solution (chemical solution) of an alkaline substance, the amount of the chemical solution added depends on the pH of the chemical solution, but for example, the ratio of tobacco residue (g) to the chemical solution (mL) is 1:2 to 2. The ratio is preferably 1:100, more preferably 1:3 to 1:100, even more preferably 1:3 to 1:50, even more preferably 1:5 to 1:50. , 1:10 to 1:50 is particularly preferred.
アルカリ蒸解処理は、一般的に、120~180℃で行われる。本実施形態でも、前記一般的な温度で行うことが可能であるが、好ましくは130~230℃、より好ましくは150~180℃である。また、アルカリ蒸解処理の処理時間は、たばこ残渣が十分に蒸解される時間であれば特に限定されない。使用する薬液のpH等によっても異なるが、例えば、5分間~6時間が好ましく、30分間~6時間がより好ましく、1時間~6時間がさらに好ましい。
Alkaline cooking treatment is generally performed at 120 to 180°C. In this embodiment as well, it is possible to carry out the reaction at the above-mentioned general temperature, but the temperature is preferably 130 to 230°C, more preferably 150 to 180°C. Further, the treatment time of the alkaline cooking treatment is not particularly limited as long as it is a time that allows the tobacco residue to be sufficiently digested. Although it varies depending on the pH of the chemical solution used, etc., for example, it is preferably from 5 minutes to 6 hours, more preferably from 30 minutes to 6 hours, and even more preferably from 1 hour to 6 hours.
アルカリ蒸解処理後、たばこ残渣のpHを4.0~6.5に調整する。pHの調整は、クエン酸、塩酸、硫酸、硝酸等のpH調整剤を用いることで行うことができる。前記pHは、4.5~6.0であることが好ましく、5.0~6.0であることがより好ましい。なお、たばこ残渣のpHは、以下の方法で測定することができる。たばこ残渣のサンプル1gに対して超純水10mLを添加し、200rpmで10分間震盪する。得られた液のpHを、卓上型pHメーター(商品名:SS211、HORIBA社製)で測定する。
After the alkaline cooking treatment, the pH of the tobacco residue is adjusted to 4.0 to 6.5. The pH can be adjusted using a pH adjuster such as citric acid, hydrochloric acid, sulfuric acid, or nitric acid. The pH is preferably 4.5 to 6.0, more preferably 5.0 to 6.0. Note that the pH of tobacco residue can be measured by the following method. Add 10 mL of ultrapure water to 1 g of tobacco residue sample, and shake at 200 rpm for 10 minutes. The pH of the obtained liquid is measured with a tabletop pH meter (trade name: SS211, manufactured by HORIBA).
(かけ戻し工程)
本工程では、pH調整後の前記たばこ残渣に前記たばこ抽出液をかけ戻す。本工程により、予めたばこ原料から取り出していたたばこ成分をたばこ残渣に戻す。低比熱化されたたばこ残渣を基材として、該基材にたばこ成分を戻すことで、比熱の低い再生たばこを得ることができる。たばこ残渣にたばこ抽出液をかけ戻す方法は特に限定されない。例えば、たばこ残渣にたばこ抽出液を添加して混合し、たばこ残渣にたばこ抽出液を染み込ませることでかけ戻すことができる。かけ戻した後でたばこ抽出液を含むたばこ残渣を乾燥してもよい。 (Returning process)
In this step, the tobacco extract liquid is poured back onto the tobacco residue after pH adjustment. Through this step, the tobacco components previously removed from the tobacco raw material are returned to tobacco residue. Regenerated tobacco with a low specific heat can be obtained by using tobacco residue with a low specific heat as a base material and returning tobacco components to the base material. The method of applying the tobacco extract back onto the tobacco residue is not particularly limited. For example, the tobacco residue can be recombined by adding and mixing a tobacco extract to the tobacco residue and allowing the tobacco extract to soak into the tobacco residue. After recoating, the tobacco residue containing the tobacco extract may be dried.
本工程では、pH調整後の前記たばこ残渣に前記たばこ抽出液をかけ戻す。本工程により、予めたばこ原料から取り出していたたばこ成分をたばこ残渣に戻す。低比熱化されたたばこ残渣を基材として、該基材にたばこ成分を戻すことで、比熱の低い再生たばこを得ることができる。たばこ残渣にたばこ抽出液をかけ戻す方法は特に限定されない。例えば、たばこ残渣にたばこ抽出液を添加して混合し、たばこ残渣にたばこ抽出液を染み込ませることでかけ戻すことができる。かけ戻した後でたばこ抽出液を含むたばこ残渣を乾燥してもよい。 (Returning process)
In this step, the tobacco extract liquid is poured back onto the tobacco residue after pH adjustment. Through this step, the tobacco components previously removed from the tobacco raw material are returned to tobacco residue. Regenerated tobacco with a low specific heat can be obtained by using tobacco residue with a low specific heat as a base material and returning tobacco components to the base material. The method of applying the tobacco extract back onto the tobacco residue is not particularly limited. For example, the tobacco residue can be recombined by adding and mixing a tobacco extract to the tobacco residue and allowing the tobacco extract to soak into the tobacco residue. After recoating, the tobacco residue containing the tobacco extract may be dried.
(成形工程)
本実施形態に係る方法では、得られた再生たばこをシート状、シート刻状等に成形してもよい。例えば、かけ戻し工程により得られたたばこ成分を含むたばこ残渣と、前記バインダと、前記繊維材料とを混合し、抄造法、キャスト法、圧延法等の公知の方法でシート状に成形することができる。また、シート状に成形された再生たばこを裁刻することで、シート刻状に成形することができる。 (molding process)
In the method according to the present embodiment, the obtained recycled tobacco may be formed into a sheet shape, shredded sheet shape, or the like. For example, it is possible to mix tobacco residue containing tobacco components obtained by the re-feeding process, the binder, and the fiber material, and form the mixture into a sheet by a known method such as a papermaking method, a casting method, or a rolling method. can. Furthermore, by cutting recycled tobacco that has been formed into a sheet, it can be formed into a shredded sheet.
本実施形態に係る方法では、得られた再生たばこをシート状、シート刻状等に成形してもよい。例えば、かけ戻し工程により得られたたばこ成分を含むたばこ残渣と、前記バインダと、前記繊維材料とを混合し、抄造法、キャスト法、圧延法等の公知の方法でシート状に成形することができる。また、シート状に成形された再生たばこを裁刻することで、シート刻状に成形することができる。 (molding process)
In the method according to the present embodiment, the obtained recycled tobacco may be formed into a sheet shape, shredded sheet shape, or the like. For example, it is possible to mix tobacco residue containing tobacco components obtained by the re-feeding process, the binder, and the fiber material, and form the mixture into a sheet by a known method such as a papermaking method, a casting method, or a rolling method. can. Furthermore, by cutting recycled tobacco that has been formed into a sheet, it can be formed into a shredded sheet.
[非燃焼加熱型香味吸引器]
本実施形態に係る非燃焼加熱型香味吸引器は、本実施形態に係る再生たばこが充填された、たばこ含有セグメントを備える。本実施形態に係る非燃焼加熱型香味吸引器は、本実施形態に係る再生たばこが充填されたたばこ含有セグメントを備えるため、該たばこ含有セグメントを加熱する際に、少ない電力でたばこ含有セグメントの温度を上昇させることができる。したがって、非燃焼加熱型香味吸引器1本あたりの電力消費量を抑制することができる。 [Non-combustion heated flavor inhaler]
The non-combustion heated flavor inhaler according to the present embodiment includes a tobacco-containing segment filled with the recycled tobacco according to the present embodiment. Since the non-combustion heated flavor inhaler according to the present embodiment includes the tobacco-containing segment filled with the recycled tobacco according to the present embodiment, when heating the tobacco-containing segment, the temperature of the tobacco-containing segment can be increased with less electric power. can be raised. Therefore, the power consumption per non-combustion heated flavor inhaler can be suppressed.
本実施形態に係る非燃焼加熱型香味吸引器は、本実施形態に係る再生たばこが充填された、たばこ含有セグメントを備える。本実施形態に係る非燃焼加熱型香味吸引器は、本実施形態に係る再生たばこが充填されたたばこ含有セグメントを備えるため、該たばこ含有セグメントを加熱する際に、少ない電力でたばこ含有セグメントの温度を上昇させることができる。したがって、非燃焼加熱型香味吸引器1本あたりの電力消費量を抑制することができる。 [Non-combustion heated flavor inhaler]
The non-combustion heated flavor inhaler according to the present embodiment includes a tobacco-containing segment filled with the recycled tobacco according to the present embodiment. Since the non-combustion heated flavor inhaler according to the present embodiment includes the tobacco-containing segment filled with the recycled tobacco according to the present embodiment, when heating the tobacco-containing segment, the temperature of the tobacco-containing segment can be increased with less electric power. can be raised. Therefore, the power consumption per non-combustion heated flavor inhaler can be suppressed.
本実施形態に係る非燃焼加熱型香味吸引器の一例を図1に示す。図1に示される非燃焼加熱型香味吸引器1は、本実施形態に係る再生たばこが充填されたたばこ含有セグメント2と、周上に穿孔8を有する筒状の冷却セグメント3と、センターホールセグメント4と、フィルターセグメント5と、を備える。本実施形態に係る非燃焼加熱型香味吸引器は、たばこ含有セグメント、冷却セグメント、センターホールセグメント及びフィルターセグメント以外にも、他のセグメントを有していてもよい。
FIG. 1 shows an example of the non-combustion heating type flavor inhaler according to this embodiment. A non-combustion heated flavor inhaler 1 shown in FIG. 1 includes a tobacco-containing segment 2 filled with recycled tobacco according to the present embodiment, a cylindrical cooling segment 3 having perforations 8 on the circumference, and a center hole segment. 4 and a filter segment 5. The non-combustion heated flavor inhaler according to the present embodiment may have other segments in addition to the tobacco-containing segment, the cooling segment, the center hole segment, and the filter segment.
本実施形態に係る非燃焼加熱型香味吸引器の軸方向の長さは特に限定されないが、40mm以上、90mm以下であることが好ましく、50mm以上、75mm以下であることがより好ましく、50mm以上、60mm以下であることがさらに好ましい。また、非燃焼加熱型香味吸引器の周の長さは16mm以上、25mm以下であることが好ましく、20mm以上、24mm以下であることがより好ましく、21mm以上、23mm以下であることがさらに好ましい。例えば、たばこ含有セグメントの長さは20mm、冷却セグメントの長さは20mm、センターホールセグメントの長さは8mm、フィルターセグメントの長さは7mmである態様を挙げることができる。なお、フィルターセグメントの長さは4mm以上、10mm以下の範囲内で選択可能である。また、その際のフィルターセグメントの通気抵抗は、セグメント当たり15mmH2O/seg以上、60mmH2O/seg以下であるように選択できる。これら個々のセグメント長さは、製造適性、要求品質等に応じて、適宜変更できる。さらには、センターホールセグメントを用いずに、冷却セグメントの下流側にフィルターセグメントのみを配置しても、非燃焼加熱型香味吸引器として機能させることができる。
The axial length of the non-combustion heated flavor inhaler according to this embodiment is not particularly limited, but is preferably 40 mm or more and 90 mm or less, more preferably 50 mm or more and 75 mm or less, 50 mm or more, More preferably, it is 60 mm or less. Further, the circumferential length of the non-combustion heating type flavor inhaler is preferably 16 mm or more and 25 mm or less, more preferably 20 mm or more and 24 mm or less, and even more preferably 21 mm or more and 23 mm or less. For example, an embodiment may be mentioned in which the tobacco-containing segment has a length of 20 mm, the cooling segment has a length of 20 mm, the center hole segment has a length of 8 mm, and the filter segment has a length of 7 mm. Note that the length of the filter segment can be selected within the range of 4 mm or more and 10 mm or less. Further, the ventilation resistance of the filter segment at this time can be selected to be 15 mmH 2 O/seg or more and 60 mmH 2 O/seg or less per segment. These individual segment lengths can be changed as appropriate depending on manufacturing suitability, required quality, etc. Furthermore, even if only the filter segment is disposed downstream of the cooling segment without using the center hole segment, it is possible to function as a non-combustion heated flavor inhaler.
(たばこ含有セグメント)
たばこ含有セグメント2は、本実施形態に係る再生たばこが巻紙(以下、ラッパーともいう)内に充填されている。再生たばこを巻紙内に充填する方法は特に限定されないが、例えば再生たばこをラッパーで包んでもよく、筒状のラッパー内に再生たばこを充填してもよい。再生たばこの形状が矩形状のように長手方向を有する場合、再生たばこは該長手方向がラッパー内でそれぞれ不特定の方向となるように充填されていてもよく、たばこ含有セグメント2の軸方向又は該軸方向に対して垂直な方向となるように整列させて充填されていてもよい。 (Tobacco-containing segment)
In the tobacco-containing segment 2, recycled tobacco according to the present embodiment is filled in a wrapping paper (hereinafter also referred to as a wrapper). The method of filling the recycled tobacco into the paper is not particularly limited, but for example, the recycled tobacco may be wrapped in a wrapper, or the recycled tobacco may be filled in a cylindrical wrapper. When the shape of the recycled tobacco has a longitudinal direction such as a rectangular shape, the recycled tobacco may be packed so that the longitudinal direction is in an unspecified direction within the wrapper, and the recycled tobacco may be packed in the axial direction of the tobacco-containing segment 2 or They may be packed in alignment in a direction perpendicular to the axial direction.
たばこ含有セグメント2は、本実施形態に係る再生たばこが巻紙(以下、ラッパーともいう)内に充填されている。再生たばこを巻紙内に充填する方法は特に限定されないが、例えば再生たばこをラッパーで包んでもよく、筒状のラッパー内に再生たばこを充填してもよい。再生たばこの形状が矩形状のように長手方向を有する場合、再生たばこは該長手方向がラッパー内でそれぞれ不特定の方向となるように充填されていてもよく、たばこ含有セグメント2の軸方向又は該軸方向に対して垂直な方向となるように整列させて充填されていてもよい。 (Tobacco-containing segment)
In the tobacco-containing segment 2, recycled tobacco according to the present embodiment is filled in a wrapping paper (hereinafter also referred to as a wrapper). The method of filling the recycled tobacco into the paper is not particularly limited, but for example, the recycled tobacco may be wrapped in a wrapper, or the recycled tobacco may be filled in a cylindrical wrapper. When the shape of the recycled tobacco has a longitudinal direction such as a rectangular shape, the recycled tobacco may be packed so that the longitudinal direction is in an unspecified direction within the wrapper, and the recycled tobacco may be packed in the axial direction of the tobacco-containing segment 2 or They may be packed in alignment in a direction perpendicular to the axial direction.
(冷却セグメント)
図1に示されるように、冷却セグメント3は筒状部材7で構成される態様を挙げることができる。筒状部材7は例えば厚紙を円筒状に加工した紙管であってもよい。 (cooling segment)
As shown in FIG. 1, the cooling segment 3 may include a cylindrical member 7. The cylindrical member 7 may be, for example, a paper tube made of cardboard processed into a cylindrical shape.
図1に示されるように、冷却セグメント3は筒状部材7で構成される態様を挙げることができる。筒状部材7は例えば厚紙を円筒状に加工した紙管であってもよい。 (cooling segment)
As shown in FIG. 1, the cooling segment 3 may include a cylindrical member 7. The cylindrical member 7 may be, for example, a paper tube made of cardboard processed into a cylindrical shape.
筒状部材7及び後述するマウスピースライニングペーパー12には、両者を貫通する穿孔8が設けられている。穿孔8の存在により、吸引時に外気が冷却セグメント3内に導入される。これにより、たばこ含有セグメント2が加熱されることで生成したエアロゾル気化成分が外気と接触し、その温度が低下するため液化し、エアロゾルが形成される。穿孔8の径(差し渡し長さ)は特に限定されないが、例えば0.5mm以上、1.5mm以下であってもよい。穿孔8の数は特に限定されず、1つでも2つ以上でもよい。例えば穿孔8は冷却セグメント3の周上に複数設けられていてもよい。
The cylindrical member 7 and the mouthpiece lining paper 12, which will be described later, are provided with perforations 8 that pass through them both. Due to the presence of the perforations 8, outside air is introduced into the cooling segment 3 during suction. As a result, the vaporized aerosol component generated by heating the tobacco-containing segment 2 comes into contact with the outside air, and as its temperature decreases, it liquefies and forms an aerosol. The diameter (cross-length) of the perforation 8 is not particularly limited, but may be, for example, 0.5 mm or more and 1.5 mm or less. The number of perforations 8 is not particularly limited, and may be one or two or more. For example, a plurality of perforations 8 may be provided around the circumference of the cooling segment 3.
穿孔8から導入される外気量は、使用者により吸引される気体全体の体積に対して85体積%以下が好ましく、80体積%以下がより好ましい。前記外気量の割合が85体積%以下であることにより、外気によって希釈されることによる香味の低減を十分に抑制することができる。なお、これを別の言い方ではベンチレーション割合ともいう。ベンチレーション割合の範囲の下限は、冷却性の観点から、55体積%以上が好ましく、60体積%以上がより好ましい。
The amount of outside air introduced through the perforations 8 is preferably 85% by volume or less, more preferably 80% by volume or less, based on the volume of the entire gas sucked by the user. When the ratio of the amount of outside air is 85% by volume or less, reduction in flavor due to dilution by outside air can be sufficiently suppressed. Note that this is also called the ventilation ratio in another way. From the viewpoint of cooling performance, the lower limit of the ventilation ratio range is preferably 55% by volume or more, more preferably 60% by volume or more.
また、冷却セグメントは、しわ付けされた、ひだ付けされた、ギャザー加工された、又は折り畳まれた適切な構成材料のシートを含むセグメントであってもよい。そのような要素の断面プロフィールは、ランダムに向いたチャネルを示す場合がある。また、冷却セグメントは、縦方向延在チューブの束を含んでいてもよい。このような冷却セグメントは、例えば、ひだ付け、ギャザー付け、又は折り畳まれたシート材料を巻紙で巻装して形成することができる。
The cooling segment may also be a segment comprising a sheet of suitable construction material that is crimped, pleated, gathered, or folded. The cross-sectional profile of such elements may exhibit randomly oriented channels. The cooling segment may also include a bundle of longitudinally extending tubes. Such cooling segments may be formed, for example, from pleated, gathered, or folded sheet material wrapped in a paper wrapper.
冷却セグメントの軸方向の長さは、例えば7mm以上、28mm以下であることができ、例えば18mmであることができる。また、冷却セグメントは、その軸方向断面形状として実質的に円形であることができ、その直径は例えば5mm以上、10mm以下であることができ、例えば約7mmであることができる。
The axial length of the cooling segment can be, for example, 7 mm or more and 28 mm or less, and can be, for example, 18 mm. The cooling segment may also be substantially circular in its axial cross-sectional shape, and its diameter may be, for example, greater than or equal to 5 mm and less than or equal to 10 mm, such as about 7 mm.
(センターホールセグメント)
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充填層と、該充填層を覆うインナープラグラッパー(内側巻紙)とで構成される。例えば、図1に示されるように、センターホールセグメント4は、中空部を有する第一の充填層9と、第一の充填層9を覆う第一のインナープラグラッパー10とで構成される。センターホールセグメント4は、マウスピースセグメント6の強度を高める機能を有する。第一の充填層9は、例えば酢酸セルロース繊維が高密度で充填されトリアセチンを含む可塑剤が酢酸セルロース質量に対して、6質量%以上、20質量%以下添加されて硬化された内径φ1.0mm以上、φ5.0mm以下のロッドとすることができる。第一の充填層9は繊維の充填密度が高いため、吸引時は、空気やエアロゾルは中空部のみを流れることになり、第一の充填層9内はほとんど流れない。センターホールセグメント4内部の第一の充填層9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少ない。なお、センターホールセグメント4が第一のインナープラグラッパー10を持たず、熱成型によってその形が保たれていてもよい。 (center hole segment)
The center hole segment is composed of a filling layer having one or more hollow portions and an inner plug wrapper covering the filling layer. For example, as shown in FIG. 1, the center hole segment 4 includes a first filling layer 9 having a hollow portion and a first inner plug wrapper 10 covering the first filling layer 9. The center hole segment 4 has the function of increasing the strength of the mouthpiece segment 6. The first packed layer 9 has an inner diameter of 1.0 mm, for example, filled with cellulose acetate fibers at high density and hardened by adding a plasticizer containing triacetin from 6% by mass to 20% by mass based on the mass of cellulose acetate. As described above, the rod can have a diameter of 5.0 mm or less. Since the first packed layer 9 has a high packing density of fibers, during suction, air and aerosol flow only through the hollow portion, and hardly flow inside the first packed layer 9. Since the first filling layer 9 inside the center hole segment 4 is a fiber filling layer, the feel of the device from the outside during use is less likely to cause discomfort to the user. Note that the center hole segment 4 may not have the first inner plug wrapper 10 and its shape may be maintained by thermoforming.
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充填層と、該充填層を覆うインナープラグラッパー(内側巻紙)とで構成される。例えば、図1に示されるように、センターホールセグメント4は、中空部を有する第一の充填層9と、第一の充填層9を覆う第一のインナープラグラッパー10とで構成される。センターホールセグメント4は、マウスピースセグメント6の強度を高める機能を有する。第一の充填層9は、例えば酢酸セルロース繊維が高密度で充填されトリアセチンを含む可塑剤が酢酸セルロース質量に対して、6質量%以上、20質量%以下添加されて硬化された内径φ1.0mm以上、φ5.0mm以下のロッドとすることができる。第一の充填層9は繊維の充填密度が高いため、吸引時は、空気やエアロゾルは中空部のみを流れることになり、第一の充填層9内はほとんど流れない。センターホールセグメント4内部の第一の充填層9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少ない。なお、センターホールセグメント4が第一のインナープラグラッパー10を持たず、熱成型によってその形が保たれていてもよい。 (center hole segment)
The center hole segment is composed of a filling layer having one or more hollow portions and an inner plug wrapper covering the filling layer. For example, as shown in FIG. 1, the center hole segment 4 includes a first filling layer 9 having a hollow portion and a first inner plug wrapper 10 covering the first filling layer 9. The center hole segment 4 has the function of increasing the strength of the mouthpiece segment 6. The first packed layer 9 has an inner diameter of 1.0 mm, for example, filled with cellulose acetate fibers at high density and hardened by adding a plasticizer containing triacetin from 6% by mass to 20% by mass based on the mass of cellulose acetate. As described above, the rod can have a diameter of 5.0 mm or less. Since the first packed layer 9 has a high packing density of fibers, during suction, air and aerosol flow only through the hollow portion, and hardly flow inside the first packed layer 9. Since the first filling layer 9 inside the center hole segment 4 is a fiber filling layer, the feel of the device from the outside during use is less likely to cause discomfort to the user. Note that the center hole segment 4 may not have the first inner plug wrapper 10 and its shape may be maintained by thermoforming.
(フィルターセグメント)
フィルターセグメント5の構成は特に限定されないが、単数または複数の充填層から構成されてよい。充填層の外側は一枚または複数枚の巻紙で巻装されてよい。フィルターセグメント5のセグメント当たりの通気抵抗は、フィルターセグメント5に充填される充填物の量、材料等により適宜変更することができる。例えば、充填物が酢酸セルロース繊維である場合、フィルターセグメント5に充填される酢酸セルロース繊維の量を増加させれば、通気抵抗を増加させることができる。充填物が酢酸セルロース繊維である場合、酢酸セルロース繊維の充填密度は0.13~0.18g/cm3であることができる。なお、通気抵抗は通気抵抗測定器(商品名:SODIMAX、SODIM製)により測定される値である。 (filter segment)
The structure of the filter segment 5 is not particularly limited, but may be composed of a single or plural filling layers. The outside of the packed layer may be wrapped with one or more wrapping papers. The ventilation resistance per segment of the filter segment 5 can be changed as appropriate depending on the amount of filler filled in the filter segment 5, the material, etc. For example, if the filling is cellulose acetate fibers, increasing the amount of cellulose acetate fibers filled into the filter segment 5 can increase the ventilation resistance. When the filling is cellulose acetate fibers, the packing density of the cellulose acetate fibers can be 0.13-0.18 g/cm 3 . Note that the ventilation resistance is a value measured by a ventilation resistance measuring device (trade name: SODIMAX, manufactured by SODIM).
フィルターセグメント5の構成は特に限定されないが、単数または複数の充填層から構成されてよい。充填層の外側は一枚または複数枚の巻紙で巻装されてよい。フィルターセグメント5のセグメント当たりの通気抵抗は、フィルターセグメント5に充填される充填物の量、材料等により適宜変更することができる。例えば、充填物が酢酸セルロース繊維である場合、フィルターセグメント5に充填される酢酸セルロース繊維の量を増加させれば、通気抵抗を増加させることができる。充填物が酢酸セルロース繊維である場合、酢酸セルロース繊維の充填密度は0.13~0.18g/cm3であることができる。なお、通気抵抗は通気抵抗測定器(商品名:SODIMAX、SODIM製)により測定される値である。 (filter segment)
The structure of the filter segment 5 is not particularly limited, but may be composed of a single or plural filling layers. The outside of the packed layer may be wrapped with one or more wrapping papers. The ventilation resistance per segment of the filter segment 5 can be changed as appropriate depending on the amount of filler filled in the filter segment 5, the material, etc. For example, if the filling is cellulose acetate fibers, increasing the amount of cellulose acetate fibers filled into the filter segment 5 can increase the ventilation resistance. When the filling is cellulose acetate fibers, the packing density of the cellulose acetate fibers can be 0.13-0.18 g/cm 3 . Note that the ventilation resistance is a value measured by a ventilation resistance measuring device (trade name: SODIMAX, manufactured by SODIM).
フィルターセグメント5の周の長さは特に限定されないが、16~25mmであることが好ましく、20~24mmであることがより好ましく、21~23mmであることがさらに好ましい。フィルターセグメント5の軸方向の長さは4~10mmを選択可能であり、その通気抵抗が15~60mmH2O/segとなるように選択される。フィルターセグメント5の軸方向の長さは5~9mmが好ましく、6~8mmがより好ましい。フィルターセグメント5の断面の形状は特に限定されないが、例えば円形、楕円形、多角形等であることができる。また、フィルターセグメント5には香料を含んだ破壊性カプセル、香料ビーズ、香料を直接添加していてもよい。
The circumferential length of the filter segment 5 is not particularly limited, but is preferably 16 to 25 mm, more preferably 20 to 24 mm, and even more preferably 21 to 23 mm. The length of the filter segment 5 in the axial direction can be selected from 4 to 10 mm, and is selected so that its ventilation resistance is 15 to 60 mmH 2 O/seg. The length of the filter segment 5 in the axial direction is preferably 5 to 9 mm, more preferably 6 to 8 mm. The cross-sectional shape of the filter segment 5 is not particularly limited, but may be, for example, circular, elliptical, polygonal, or the like. Further, a rupturable capsule containing a fragrance, fragrance beads, or a fragrance may be directly added to the filter segment 5.
図1に示されるように、センターホールセグメント4と、フィルターセグメント5とはアウタープラグラッパー(外側巻紙)11で接続できる。アウタープラグラッパー11は、例えば円筒状の紙であることができる。また、たばこ含有セグメント2と、冷却セグメント3と、接続済みのセンターホールセグメント4及びフィルターセグメント5とは、マウスピースライニングペーパー12により接続できる。これらの接続は、例えばマウスピースライニングペーパー12の内側面に酢酸ビニル系糊等の糊を塗り、前記3つのセグメントを入れて巻くことで接続することができる。なお、これらのセグメントは複数のライニングペーパーで複数回に分けて接続されていてもよい。
As shown in FIG. 1, the center hole segment 4 and the filter segment 5 can be connected with an outer plug wrapper (outer wrapping paper) 11. The outer plug wrapper 11 can be, for example, cylindrical paper. Further, the tobacco-containing segment 2, the cooling segment 3, and the connected center hole segment 4 and filter segment 5 can be connected by a mouthpiece lining paper 12. These connections can be made, for example, by applying glue such as vinyl acetate glue to the inner surface of the mouthpiece lining paper 12, inserting the three segments, and winding the paper. Note that these segments may be connected multiple times using multiple lining papers.
[非燃焼加熱型香味吸引システム]
本実施形態に係る非燃焼加熱型香味吸引システムは、本実施形態に係る非燃焼加熱型香味吸引器と、該非燃焼加熱型香味吸引器のたばこ含有セグメントを加熱する加熱装置と、を備える。本実施形態に係る非燃焼加熱型香味吸引システムは、本実施形態に係る非燃焼加熱型香味吸引器を備えるため、非燃焼加熱型香味吸引器1本あたりの電力消費量を抑制することができる。本実施形態に係る非燃焼加熱型香味吸引システムは、本実施形態に係る非燃焼加熱型香味吸引器及び前記加熱装置以外に、他の構成を有していてもよい。 [Non-combustion heated flavor suction system]
The non-combustion heating type flavor inhaler system according to the present embodiment includes the non-combustion heating type flavor inhaler according to the present embodiment, and a heating device that heats the tobacco-containing segment of the non-combustion heating type flavor inhaler. Since the non-combustion heated flavor suction system according to the present embodiment includes the non-combustion heated flavor suction device according to the present embodiment, it is possible to suppress power consumption per non-combustion heated flavor suction device. . The non-combustion heating type flavor suction system according to this embodiment may have other configurations in addition to the non-combustion heating type flavor inhaler and the heating device according to this embodiment.
本実施形態に係る非燃焼加熱型香味吸引システムは、本実施形態に係る非燃焼加熱型香味吸引器と、該非燃焼加熱型香味吸引器のたばこ含有セグメントを加熱する加熱装置と、を備える。本実施形態に係る非燃焼加熱型香味吸引システムは、本実施形態に係る非燃焼加熱型香味吸引器を備えるため、非燃焼加熱型香味吸引器1本あたりの電力消費量を抑制することができる。本実施形態に係る非燃焼加熱型香味吸引システムは、本実施形態に係る非燃焼加熱型香味吸引器及び前記加熱装置以外に、他の構成を有していてもよい。 [Non-combustion heated flavor suction system]
The non-combustion heating type flavor inhaler system according to the present embodiment includes the non-combustion heating type flavor inhaler according to the present embodiment, and a heating device that heats the tobacco-containing segment of the non-combustion heating type flavor inhaler. Since the non-combustion heated flavor suction system according to the present embodiment includes the non-combustion heated flavor suction device according to the present embodiment, it is possible to suppress power consumption per non-combustion heated flavor suction device. . The non-combustion heating type flavor suction system according to this embodiment may have other configurations in addition to the non-combustion heating type flavor inhaler and the heating device according to this embodiment.
本実施形態に係る非燃焼加熱型香味吸引システムの一例を図2に示す。図2に示される非燃焼加熱型香味吸引システムは、本実施形態に係る非燃焼加熱型香味吸引器1と、非燃焼加熱型香味吸引器1のたばこ含有セグメントを外側から加熱する加熱装置13とを備える。
An example of the non-combustion heating type flavor suction system according to this embodiment is shown in FIG. 2. The non-combustion heated flavor suction system shown in FIG. 2 includes a non-combustion heated flavor suction device 1 according to the present embodiment, and a heating device 13 that heats the tobacco-containing segment of the non-combustion heated flavor suction device 1 from the outside. Equipped with.
図2(a)は非燃焼加熱型香味吸引器1を加熱装置13に挿入する前の状態を示し、図2(b)は非燃焼加熱型香味吸引器1を加熱装置13に挿入して加熱する状態を示す。図2に示される加熱装置13は、ボディ14と、ヒーター15と、金属管16と、電池ユニット17と、制御ユニット18とを備える。ボディ14は筒状の凹部19を有し、凹部19の内側側面であって、凹部19に挿入される非燃焼加熱型香味吸引器1のたばこ含有セグメントと対応する位置に、ヒーター15及び金属管16が配置されている。ヒーター15は電気抵抗によるヒーターであることができ、温度制御を行う制御ユニット18からの指示により電池ユニット17より電力が供給され、ヒーター15の加熱が行われる。ヒーター15から発せられた熱は、熱伝導度の高い金属管16を通じて非燃焼加熱型香味吸引器1のたばこ含有セグメントへ伝えられる。
FIG. 2(a) shows the state before the non-combustion heating type flavor inhaler 1 is inserted into the heating device 13, and FIG. 2(b) shows the state before the non-combustion heating type flavor inhaler 1 is inserted into the heating device 13 and heated. Indicates the state of The heating device 13 shown in FIG. 2 includes a body 14, a heater 15, a metal tube 16, a battery unit 17, and a control unit 18. The body 14 has a cylindrical recess 19, and a heater 15 and a metal tube are placed on the inner side surface of the recess 19 at a position corresponding to the tobacco-containing segment of the non-combustion heated flavor inhaler 1 inserted into the recess 19. 16 are arranged. The heater 15 can be an electric resistance heater, and electric power is supplied from the battery unit 17 according to instructions from a control unit 18 that performs temperature control, and the heater 15 is heated. Heat emitted from the heater 15 is transferred to the tobacco-containing segment of the non-combustion heated flavor inhaler 1 through a metal tube 16 with high thermal conductivity.
図2(b)においては、模式的に図示しているため、非燃焼加熱型香味吸引器1の外周と金属管16の内周との間に隙間があるが、実際は、熱を効率的に伝達する目的で非燃焼加熱型香味吸引器1の外周と金属管16の内周との間に隙間は無い方が望ましい。なお、加熱装置13は非燃焼加熱型香味吸引器1のたばこ含有セグメントを外側から加熱するが、内側から加熱するものであってもよい。
In FIG. 2(b), since it is schematically illustrated, there is a gap between the outer periphery of the non-combustion heating type flavor inhaler 1 and the inner periphery of the metal tube 16, but in reality, heat can be efficiently dissipated. For the purpose of transmitting flavor, it is preferable that there be no gap between the outer periphery of the non-combustion heating type flavor inhaler 1 and the inner periphery of the metal tube 16. Although the heating device 13 heats the tobacco-containing segment of the non-combustion heating flavor inhaler 1 from the outside, it may also heat the tobacco-containing segment from the inside.
加熱装置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、150℃以上400℃以下であることがより好ましく、200℃以上350℃以下であることがさらに好ましい。なお、加熱温度とは加熱装置のヒーターの温度を示す。
The heating temperature by the heating device is not particularly limited, but is preferably 400°C or less, more preferably 150°C or more and 400°C or less, and even more preferably 200°C or more and 350°C or less. Note that the heating temperature refers to the temperature of the heater of the heating device.
以下、本実施形態を実施例により詳細に説明するが、本実施形態はこれらの実施例に限定されない。なお、FT-IR分析における波長3200~3600cm-1の最大吸光度の測定、吸水量の測定、安息角の測定、比熱の測定、及びべたつきの評価は、以下の方法により実施した。
Hereinafter, the present embodiment will be described in detail with reference to examples, but the present embodiment is not limited to these examples. The measurement of the maximum absorbance at a wavelength of 3200 to 3600 cm -1 in the FT-IR analysis, the measurement of water absorption, the measurement of the angle of repose, the measurement of specific heat, and the evaluation of stickiness were carried out by the following methods.
[FT-IR分析における波長3200~3600cm-1の最大吸光度の測定]
たばこ材料のFT-IR分析における波長3200~3600cm-1の最大吸光度の測定は、以下の方法により行った。たばこ材料のサンプルをATR測定用ダイヤモンドクリスタルに密着させ、赤外吸収スペクトルを測定した。測定装置としては、フーリエ変換赤外分光装置(商品名:Thermo Scientific Nicolet iS50、Thermo Scientific社製)を用いた。測定方法:ATR法、分解能:4cm-1、積算回数:32回(n=2)の条件で測定を実施した。 [Measurement of maximum absorbance at wavelength 3200 to 3600 cm −1 in FT-IR analysis]
The maximum absorbance at a wavelength of 3200 to 3600 cm −1 in FT-IR analysis of tobacco materials was measured by the following method. A sample of tobacco material was brought into close contact with a diamond crystal for ATR measurement, and an infrared absorption spectrum was measured. As a measuring device, a Fourier transform infrared spectrometer (trade name: Thermo Scientific Nicolet iS50, manufactured by Thermo Scientific) was used. Measurement method: ATR method, resolution: 4 cm −1 , number of integrations: 32 times (n=2).
たばこ材料のFT-IR分析における波長3200~3600cm-1の最大吸光度の測定は、以下の方法により行った。たばこ材料のサンプルをATR測定用ダイヤモンドクリスタルに密着させ、赤外吸収スペクトルを測定した。測定装置としては、フーリエ変換赤外分光装置(商品名:Thermo Scientific Nicolet iS50、Thermo Scientific社製)を用いた。測定方法:ATR法、分解能:4cm-1、積算回数:32回(n=2)の条件で測定を実施した。 [Measurement of maximum absorbance at wavelength 3200 to 3600 cm −1 in FT-IR analysis]
The maximum absorbance at a wavelength of 3200 to 3600 cm −1 in FT-IR analysis of tobacco materials was measured by the following method. A sample of tobacco material was brought into close contact with a diamond crystal for ATR measurement, and an infrared absorption spectrum was measured. As a measuring device, a Fourier transform infrared spectrometer (trade name: Thermo Scientific Nicolet iS50, manufactured by Thermo Scientific) was used. Measurement method: ATR method, resolution: 4 cm −1 , number of integrations: 32 times (n=2).
[吸水量の測定]
たばこ材料の吸水量は、以下の方法により測定した。φ55×80mmのステンレス管に1mm径の穴19個が開いた円筒容器を用意した。ろ紙を該円筒容器内に設置し、その上にたばこ材料のサンプルを3~6g入れた。バットに水道水を張り、バット内に該円筒容器を入れ、900秒後の質量を測定し、1g当たりの吸水量を測定した。該測定を3回実施し、その平均値を各時間における吸水量とした。 [Measurement of water absorption]
The water absorption amount of the tobacco material was measured by the following method. A cylindrical container with 19 holes of 1 mm in diameter was prepared in a stainless steel tube of φ55×80 mm. A filter paper was placed in the cylindrical container, and 3 to 6 g of the tobacco material sample was placed thereon. A vat was filled with tap water, the cylindrical container was placed in the vat, and the mass was measured after 900 seconds to measure the amount of water absorbed per 1 g. The measurement was carried out three times, and the average value was taken as the amount of water absorbed at each time.
たばこ材料の吸水量は、以下の方法により測定した。φ55×80mmのステンレス管に1mm径の穴19個が開いた円筒容器を用意した。ろ紙を該円筒容器内に設置し、その上にたばこ材料のサンプルを3~6g入れた。バットに水道水を張り、バット内に該円筒容器を入れ、900秒後の質量を測定し、1g当たりの吸水量を測定した。該測定を3回実施し、その平均値を各時間における吸水量とした。 [Measurement of water absorption]
The water absorption amount of the tobacco material was measured by the following method. A cylindrical container with 19 holes of 1 mm in diameter was prepared in a stainless steel tube of φ55×80 mm. A filter paper was placed in the cylindrical container, and 3 to 6 g of the tobacco material sample was placed thereon. A vat was filled with tap water, the cylindrical container was placed in the vat, and the mass was measured after 900 seconds to measure the amount of water absorbed per 1 g. The measurement was carried out three times, and the average value was taken as the amount of water absorbed at each time.
[安息角の測定]
たばこ材料の安息角は、以下の方法により測定した。25mm×25mmの計測台(ピーク材)の4cm上から漏斗にてたばこ材料のサンプルを落とした。計測台からサンプルがこぼれる程度まで落としたら写真を撮影し、画像解析ソフト(キーエンス社製顕微鏡)にて角度を測定した。この測定を3回実施し、その平均値を安息角の値とした。 [Measurement of angle of repose]
The angle of repose of tobacco materials was measured by the following method. A sample of tobacco material was dropped using a funnel from 4 cm above a 25 mm x 25 mm measuring table (peak material). When the sample was dropped from the measuring table to the extent that it spilled, a photograph was taken and the angle was measured using image analysis software (Keyence Microscope). This measurement was carried out three times, and the average value was taken as the value of the angle of repose.
たばこ材料の安息角は、以下の方法により測定した。25mm×25mmの計測台(ピーク材)の4cm上から漏斗にてたばこ材料のサンプルを落とした。計測台からサンプルがこぼれる程度まで落としたら写真を撮影し、画像解析ソフト(キーエンス社製顕微鏡)にて角度を測定した。この測定を3回実施し、その平均値を安息角の値とした。 [Measurement of angle of repose]
The angle of repose of tobacco materials was measured by the following method. A sample of tobacco material was dropped using a funnel from 4 cm above a 25 mm x 25 mm measuring table (peak material). When the sample was dropped from the measuring table to the extent that it spilled, a photograph was taken and the angle was measured using image analysis software (Keyence Microscope). This measurement was carried out three times, and the average value was taken as the value of the angle of repose.
[比熱の測定]
たばこ材料の比熱として、DSC(示差走査熱量測定)により300℃までの最大比熱容量(mJ/mg・℃)を測定した。具体的には、示差走査熱量計(商品名:DSC7020、(株)日立ハイテクサイエンス製)を用いて、以下の条件により測定した。昇温速度:10℃/min、保持時間:2分、パン:Al、サンプル質量:10mg、リファレンス:Al2O3。 [Measurement of specific heat]
As the specific heat of the tobacco material, the maximum specific heat capacity (mJ/mg·°C) up to 300°C was measured by DSC (differential scanning calorimetry). Specifically, the measurement was performed using a differential scanning calorimeter (trade name: DSC7020, manufactured by Hitachi High-Tech Science Co., Ltd.) under the following conditions. Temperature increase rate: 10° C./min, holding time: 2 minutes, pan: Al, sample mass: 10 mg, reference: Al 2 O 3 .
たばこ材料の比熱として、DSC(示差走査熱量測定)により300℃までの最大比熱容量(mJ/mg・℃)を測定した。具体的には、示差走査熱量計(商品名:DSC7020、(株)日立ハイテクサイエンス製)を用いて、以下の条件により測定した。昇温速度:10℃/min、保持時間:2分、パン:Al、サンプル質量:10mg、リファレンス:Al2O3。 [Measurement of specific heat]
As the specific heat of the tobacco material, the maximum specific heat capacity (mJ/mg·°C) up to 300°C was measured by DSC (differential scanning calorimetry). Specifically, the measurement was performed using a differential scanning calorimeter (trade name: DSC7020, manufactured by Hitachi High-Tech Science Co., Ltd.) under the following conditions. Temperature increase rate: 10° C./min, holding time: 2 minutes, pan: Al, sample mass: 10 mg, reference: Al 2 O 3 .
[べたつきの評価]
たばこ材料のべたつきの評価は、パネラー5名がたばこ材料を手で触り、5件法にて評価した(n=1)。具体的には、「全くべたついていない」を0点、「非常にべたついている」を5点として、0~5点で評価した。なお、前記パネラーは訓練が十分に行われており、べたつきに関する評価の閾値が等しく、パネラー間で統一化されていることが確認されている。 [Evaluation of stickiness]
The stickiness of the tobacco material was evaluated by five panelists who touched the tobacco material with their hands and evaluated it using a five-point method (n=1). Specifically, the evaluation was made on a scale of 0 to 5, with 0 points being ``not sticky at all'' and 5 points being ``very sticky''. It has been confirmed that the panelists have been sufficiently trained and that the threshold values for evaluation regarding stickiness are the same and standardized among the panelists.
たばこ材料のべたつきの評価は、パネラー5名がたばこ材料を手で触り、5件法にて評価した(n=1)。具体的には、「全くべたついていない」を0点、「非常にべたついている」を5点として、0~5点で評価した。なお、前記パネラーは訓練が十分に行われており、べたつきに関する評価の閾値が等しく、パネラー間で統一化されていることが確認されている。 [Evaluation of stickiness]
The stickiness of the tobacco material was evaluated by five panelists who touched the tobacco material with their hands and evaluated it using a five-point method (n=1). Specifically, the evaluation was made on a scale of 0 to 5, with 0 points being ``not sticky at all'' and 5 points being ``very sticky''. It has been confirmed that the panelists have been sufficiently trained and that the threshold values for evaluation regarding stickiness are the same and standardized among the panelists.
[実施例1]
(再生たばこの調製)
たばこ原料として黄色葉を準備した。前記たばこ原料に対して原料質量の12倍の水を加え、50℃、300rpmで1時間攪拌した。その後、手絞りによって抽出液を回収した。これにより、前記たばこ原料からたばこ成分を抽出し、たばこ抽出液とたばこ残渣を得た。次に、前記たばこ残渣に2mol/Lの水酸化ナトリウム水溶液を100g/L投入し、180℃で3時間加熱した。その後、クエン酸を添加してpHを5.6に調整することで、たばこ材料を得た。該たばこ材料について、前記方法により、FT-IR分析における波長3200~3600cm-1の最大吸光度、吸水量、安息角、及び比熱の測定、並びにべたつきの評価を行った。結果を表1に示す。 [Example 1]
(Preparation of recycled tobacco)
Yellow leaves were prepared as tobacco raw material. Water in an amount 12 times the mass of the raw material was added to the tobacco raw material, and the mixture was stirred at 50° C. and 300 rpm for 1 hour. Thereafter, the extract was collected by hand squeezing. Thereby, tobacco components were extracted from the tobacco raw material, and tobacco extract and tobacco residue were obtained. Next, 100 g/L of a 2 mol/L aqueous sodium hydroxide solution was added to the tobacco residue and heated at 180° C. for 3 hours. Thereafter, citric acid was added to adjust the pH to 5.6 to obtain a tobacco material. Regarding the tobacco material, the maximum absorbance at a wavelength of 3200 to 3600 cm -1 in FT-IR analysis, water absorption, angle of repose, and specific heat were measured, and stickiness was evaluated using the above method. The results are shown in Table 1.
(再生たばこの調製)
たばこ原料として黄色葉を準備した。前記たばこ原料に対して原料質量の12倍の水を加え、50℃、300rpmで1時間攪拌した。その後、手絞りによって抽出液を回収した。これにより、前記たばこ原料からたばこ成分を抽出し、たばこ抽出液とたばこ残渣を得た。次に、前記たばこ残渣に2mol/Lの水酸化ナトリウム水溶液を100g/L投入し、180℃で3時間加熱した。その後、クエン酸を添加してpHを5.6に調整することで、たばこ材料を得た。該たばこ材料について、前記方法により、FT-IR分析における波長3200~3600cm-1の最大吸光度、吸水量、安息角、及び比熱の測定、並びにべたつきの評価を行った。結果を表1に示す。 [Example 1]
(Preparation of recycled tobacco)
Yellow leaves were prepared as tobacco raw material. Water in an amount 12 times the mass of the raw material was added to the tobacco raw material, and the mixture was stirred at 50° C. and 300 rpm for 1 hour. Thereafter, the extract was collected by hand squeezing. Thereby, tobacco components were extracted from the tobacco raw material, and tobacco extract and tobacco residue were obtained. Next, 100 g/L of a 2 mol/L aqueous sodium hydroxide solution was added to the tobacco residue and heated at 180° C. for 3 hours. Thereafter, citric acid was added to adjust the pH to 5.6 to obtain a tobacco material. Regarding the tobacco material, the maximum absorbance at a wavelength of 3200 to 3600 cm -1 in FT-IR analysis, water absorption, angle of repose, and specific heat were measured, and stickiness was evaluated using the above method. The results are shown in Table 1.
得られたたばこ材料を基材として、該たばこ材料に前記たばこ抽出液をかけ戻した。たばこ抽出液をかけ戻したたばこ材料を100質量部と、バインダとしてのグアーガムを3.7質量部と、繊維材料としての針葉樹パルプを3.7質量部と、エアロゾル発生剤としてのグリセリンを14.6質量部と、を混合し、キャスト法にてシート状に成形した。以上により、シート状の再生たばこを調製した。再生たばこの厚みは428μm、密度は0.67mgWB/mm3、坪量は285gWB/m2、グリセリン含有量は12.7質量%WB、水分含有量は12.1質量%WBであった。
Using the obtained tobacco material as a base material, the tobacco extract was poured back onto the tobacco material. 100 parts by mass of tobacco material on which tobacco extract has been applied, 3.7 parts by mass of guar gum as a binder, 3.7 parts by mass of softwood pulp as a fiber material, and 14 parts of glycerin as an aerosol generator. 6 parts by mass were mixed and formed into a sheet by a casting method. As described above, a sheet-shaped recycled tobacco was prepared. The thickness of the recycled tobacco was 428 μm, the density was 0.67 mg WB/mm 3 , the basis weight was 285 g WB/m 2 , the glycerin content was 12.7 mass % WB, and the water content was 12.1 mass % WB.
(評価)
前記シート状の再生たばこを、図1に示される非燃焼加熱型香味吸引器1のたばこ含有セグメント2内に充填し、非燃焼加熱型香味吸引器を得た。該非燃焼加熱型香味吸引器について加熱試験を実施し、ニコチンデリバリー量と、グリセリンデリバリー量を測定した。具体的には、図2に示される加熱装置13に非燃焼加熱型香味吸引器1を挿入し、たばこ含有セグメントを200℃に加熱した。30秒の予備加熱の後、非燃焼加熱型香味吸引器1の吸口部から吸引することで、吸引する主流煙中に含まれるニコチン及びグリセリンの量を測定した。吸引には吸引機(商品名:RM-20、Borgwaldt社製)を用いた。吸引(パフ)は、30秒に1回、1回あたり55mlを2秒間かけて、計10回行い、パフ毎にニコチン量及びグリセリン量の測定を行った。ニコチン量及びグリセリン量の測定は、GC-FIDを用いて行った。各パフにおけるニコチンデリバリー量を図3、各パフにおけるグリセリンデリバリー量を図4にそれぞれ示す。また、電力消費量(エネルギー)当りの主流煙へのニコチン移行率を表1に示す。ただし、ニコチンおよびグリセリンは本実施形態における再生たばこに含まれる複数の成分の中から成分の指標として示しており、特にニコチンやグリセリンを特異的にデリバリー容易としているものではない。 (evaluation)
The sheet-shaped recycled tobacco was filled into the tobacco-containing segment 2 of the non-combustion heating type flavor inhaler 1 shown in FIG. 1 to obtain a non-combustion heating type flavor inhaler. A heating test was conducted on the non-combustion heated flavor inhaler, and the amount of nicotine delivered and the amount of glycerin delivered were measured. Specifically, the non-combustion heating type flavor inhaler 1 was inserted into the heating device 13 shown in FIG. 2, and the tobacco-containing segment was heated to 200°C. After preheating for 30 seconds, the amount of nicotine and glycerin contained in the inhaled mainstream smoke was measured by inhaling from the mouthpiece of the non-combustion heating type flavor inhaler 1. A suction machine (trade name: RM-20, manufactured by Borgwaldt) was used for suction. Suction (puffing) was performed once every 30 seconds with 55 ml for 2 seconds, a total of 10 times, and the amount of nicotine and glycerin was measured for each puff. The nicotine amount and glycerin amount were measured using GC-FID. The amount of nicotine delivered in each puff is shown in FIG. 3, and the amount of glycerin delivered in each puff is shown in FIG. 4. Furthermore, Table 1 shows the nicotine transfer rate to mainstream smoke per unit of power consumption (energy). However, nicotine and glycerin are shown as indicators of components from among a plurality of components contained in the recycled tobacco in this embodiment, and nicotine and glycerin are not particularly easily delivered.
前記シート状の再生たばこを、図1に示される非燃焼加熱型香味吸引器1のたばこ含有セグメント2内に充填し、非燃焼加熱型香味吸引器を得た。該非燃焼加熱型香味吸引器について加熱試験を実施し、ニコチンデリバリー量と、グリセリンデリバリー量を測定した。具体的には、図2に示される加熱装置13に非燃焼加熱型香味吸引器1を挿入し、たばこ含有セグメントを200℃に加熱した。30秒の予備加熱の後、非燃焼加熱型香味吸引器1の吸口部から吸引することで、吸引する主流煙中に含まれるニコチン及びグリセリンの量を測定した。吸引には吸引機(商品名:RM-20、Borgwaldt社製)を用いた。吸引(パフ)は、30秒に1回、1回あたり55mlを2秒間かけて、計10回行い、パフ毎にニコチン量及びグリセリン量の測定を行った。ニコチン量及びグリセリン量の測定は、GC-FIDを用いて行った。各パフにおけるニコチンデリバリー量を図3、各パフにおけるグリセリンデリバリー量を図4にそれぞれ示す。また、電力消費量(エネルギー)当りの主流煙へのニコチン移行率を表1に示す。ただし、ニコチンおよびグリセリンは本実施形態における再生たばこに含まれる複数の成分の中から成分の指標として示しており、特にニコチンやグリセリンを特異的にデリバリー容易としているものではない。 (evaluation)
The sheet-shaped recycled tobacco was filled into the tobacco-containing segment 2 of the non-combustion heating type flavor inhaler 1 shown in FIG. 1 to obtain a non-combustion heating type flavor inhaler. A heating test was conducted on the non-combustion heated flavor inhaler, and the amount of nicotine delivered and the amount of glycerin delivered were measured. Specifically, the non-combustion heating type flavor inhaler 1 was inserted into the heating device 13 shown in FIG. 2, and the tobacco-containing segment was heated to 200°C. After preheating for 30 seconds, the amount of nicotine and glycerin contained in the inhaled mainstream smoke was measured by inhaling from the mouthpiece of the non-combustion heating type flavor inhaler 1. A suction machine (trade name: RM-20, manufactured by Borgwaldt) was used for suction. Suction (puffing) was performed once every 30 seconds with 55 ml for 2 seconds, a total of 10 times, and the amount of nicotine and glycerin was measured for each puff. The nicotine amount and glycerin amount were measured using GC-FID. The amount of nicotine delivered in each puff is shown in FIG. 3, and the amount of glycerin delivered in each puff is shown in FIG. 4. Furthermore, Table 1 shows the nicotine transfer rate to mainstream smoke per unit of power consumption (energy). However, nicotine and glycerin are shown as indicators of components from among a plurality of components contained in the recycled tobacco in this embodiment, and nicotine and glycerin are not particularly easily delivered.
[比較例1]
たばこ原料として黄色葉を準備した。前記たばこ原料に対して原料質量の12倍の水を加え、50℃、300rpmで1時間攪拌した。その後、手絞りによって抽出液を回収した。これにより、前記たばこ原料からたばこ成分を抽出し、たばこ抽出液とたばこ残渣を得た。次に、前記たばこ残渣をオーブン内に入れ、N2:Air=92%:8%(酸素濃度:1.7%)の混合気体を1L/分で流通させながら、前記たばこ残渣を230℃で1時間加熱した。これにより、前記たばこ残渣は炭化され、炭化たばこを得た。該炭化たばこについて、前記方法により、FT-IR分析における波長3200~3600cm-1の最大吸光度、安息角、及び比熱の測定、並びにべたつきの評価を行った。結果を表1に示す。 [Comparative example 1]
Yellow leaves were prepared as tobacco raw material. Water in an amount 12 times the weight of the raw material was added to the tobacco raw material, and the mixture was stirred at 50° C. and 300 rpm for 1 hour. Thereafter, the extract was collected by hand squeezing. As a result, tobacco components were extracted from the tobacco raw material, and tobacco extract and tobacco residue were obtained. Next, the tobacco residue was placed in an oven, and the tobacco residue was heated at 230° C. while flowing a mixed gas of N 2 :Air=92%:8% (oxygen concentration: 1.7%) at a rate of 1 L/min. Heated for 1 hour. As a result, the tobacco residue was carbonized to obtain carbonized tobacco. Regarding the carbonized tobacco, the maximum absorbance at a wavelength of 3200 to 3600 cm -1 in FT-IR analysis, the angle of repose, and the specific heat were measured, and the stickiness was evaluated using the above method. The results are shown in Table 1.
たばこ原料として黄色葉を準備した。前記たばこ原料に対して原料質量の12倍の水を加え、50℃、300rpmで1時間攪拌した。その後、手絞りによって抽出液を回収した。これにより、前記たばこ原料からたばこ成分を抽出し、たばこ抽出液とたばこ残渣を得た。次に、前記たばこ残渣をオーブン内に入れ、N2:Air=92%:8%(酸素濃度:1.7%)の混合気体を1L/分で流通させながら、前記たばこ残渣を230℃で1時間加熱した。これにより、前記たばこ残渣は炭化され、炭化たばこを得た。該炭化たばこについて、前記方法により、FT-IR分析における波長3200~3600cm-1の最大吸光度、安息角、及び比熱の測定、並びにべたつきの評価を行った。結果を表1に示す。 [Comparative example 1]
Yellow leaves were prepared as tobacco raw material. Water in an amount 12 times the weight of the raw material was added to the tobacco raw material, and the mixture was stirred at 50° C. and 300 rpm for 1 hour. Thereafter, the extract was collected by hand squeezing. As a result, tobacco components were extracted from the tobacco raw material, and tobacco extract and tobacco residue were obtained. Next, the tobacco residue was placed in an oven, and the tobacco residue was heated at 230° C. while flowing a mixed gas of N 2 :Air=92%:8% (oxygen concentration: 1.7%) at a rate of 1 L/min. Heated for 1 hour. As a result, the tobacco residue was carbonized to obtain carbonized tobacco. Regarding the carbonized tobacco, the maximum absorbance at a wavelength of 3200 to 3600 cm -1 in FT-IR analysis, the angle of repose, and the specific heat were measured, and the stickiness was evaluated using the above method. The results are shown in Table 1.
得られた炭化たばこを基材として、該炭化たばこに前記たばこ抽出液をかけ戻した。たばこ抽出液をかけ戻した炭化たばこを100質量部と、バインダとしてのグアーガムを3.7質量部と、繊維材料としての針葉樹パルプを3.7質量部と、エアロゾル発生剤としてのグリセリンを14.6質量部と、を混合し、キャスト法にてシート状に成形した。以上により、シート状の再生たばこを調製した。該再生たばこを用いて実施例1と同様に非燃焼加熱型香味吸引器を作製し、評価した。結果を図3、図4及び表1に示す。
Using the obtained carbonized tobacco as a base material, the tobacco extract was poured back onto the carbonized tobacco. 100 parts by mass of carbonized tobacco on which tobacco extract has been applied, 3.7 parts by mass of guar gum as a binder, 3.7 parts by mass of softwood pulp as a fiber material, and 14 parts of glycerin as an aerosol generator. 6 parts by mass were mixed and molded into a sheet by a casting method. As described above, a sheet-shaped recycled tobacco was prepared. A non-combustion heated flavor inhaler was produced using the recycled tobacco in the same manner as in Example 1, and evaluated. The results are shown in FIG. 3, FIG. 4, and Table 1.
[比較例2]
活性炭(商品名:クラレコール、(株)クラレ製)に、実施例1で得られたたばこ抽出液を添加した。該活性炭を、たばこ抽出液をかけ戻したたばこ残渣の代わりに用いた以外は、実施例1と同様にシート状の再生たばこを調製した。活性炭自体の比熱と吸水量の測定結果、及びべたつきの評価結果を表1に示す。 [Comparative example 2]
The tobacco extract obtained in Example 1 was added to activated carbon (trade name: Kuraray Coal, manufactured by Kuraray Co., Ltd.). A sheet-shaped regenerated tobacco was prepared in the same manner as in Example 1, except that the activated carbon was used in place of the tobacco residue on which the tobacco extract had been applied. Table 1 shows the measurement results of the specific heat and water absorption of the activated carbon itself, and the evaluation results of stickiness.
活性炭(商品名:クラレコール、(株)クラレ製)に、実施例1で得られたたばこ抽出液を添加した。該活性炭を、たばこ抽出液をかけ戻したたばこ残渣の代わりに用いた以外は、実施例1と同様にシート状の再生たばこを調製した。活性炭自体の比熱と吸水量の測定結果、及びべたつきの評価結果を表1に示す。 [Comparative example 2]
The tobacco extract obtained in Example 1 was added to activated carbon (trade name: Kuraray Coal, manufactured by Kuraray Co., Ltd.). A sheet-shaped regenerated tobacco was prepared in the same manner as in Example 1, except that the activated carbon was used in place of the tobacco residue on which the tobacco extract had been applied. Table 1 shows the measurement results of the specific heat and water absorption of the activated carbon itself, and the evaluation results of stickiness.
[比較例3]
実施例1と同様にたばこ抽出液とたばこ残渣を得た。その後、たばこ残渣のアルカリ蒸解処理を行わずに、該たばこ残渣に前記たばこ抽出液をかけ戻した。それ以外は実施例1と同様にシート状の再生たばこを調製し、評価した。たばこ残渣自体の各物性の測定結果を表1に示す。また、非燃焼加熱型香味吸引器の評価結果を図3、図4及び表1に示す。 [Comparative example 3]
A tobacco extract and tobacco residue were obtained in the same manner as in Example 1. Thereafter, the tobacco extract was poured back onto the tobacco residue without subjecting the tobacco residue to an alkali cooking treatment. Other than that, a sheet-shaped recycled tobacco was prepared and evaluated in the same manner as in Example 1. Table 1 shows the measurement results of each physical property of the tobacco residue itself. Furthermore, the evaluation results of the non-combustion heating type flavor inhaler are shown in FIGS. 3, 4, and Table 1.
実施例1と同様にたばこ抽出液とたばこ残渣を得た。その後、たばこ残渣のアルカリ蒸解処理を行わずに、該たばこ残渣に前記たばこ抽出液をかけ戻した。それ以外は実施例1と同様にシート状の再生たばこを調製し、評価した。たばこ残渣自体の各物性の測定結果を表1に示す。また、非燃焼加熱型香味吸引器の評価結果を図3、図4及び表1に示す。 [Comparative example 3]
A tobacco extract and tobacco residue were obtained in the same manner as in Example 1. Thereafter, the tobacco extract was poured back onto the tobacco residue without subjecting the tobacco residue to an alkali cooking treatment. Other than that, a sheet-shaped recycled tobacco was prepared and evaluated in the same manner as in Example 1. Table 1 shows the measurement results of each physical property of the tobacco residue itself. Furthermore, the evaluation results of the non-combustion heating type flavor inhaler are shown in FIGS. 3, 4, and Table 1.
図3及び図4に示されるように、FT-IR分析にて波長3200~3600cm-1の最大吸光度が0.40以上であり、かつ、比熱が5mJ/mg・℃以下であるたばこ材料を基材として用い、再生たばこを調製した実施例1では、該再生たばこを含む非燃焼加熱型香味吸引器の評価において、特にパフ数が増加した時にニコチン及びグリセリンデリバリー量が多いことが分かった。また、これに伴い電力消費量(エネルギー)当りの主流煙へのニコチン移行率が高かった(表1)。一方、FT-IR分析にて波長3200~3600cm-1の最大吸光度が0.40未満である、又は、比熱が5mJ/mg・℃を超えるたばこ材料を基材として用い、再生たばこを調製した比較例1及び3では、該再生たばこを含む非燃焼加熱型香味吸引器の評価において、ニコチン及びグリセリンデリバリー量が実施例1よりも少なかった(図3及び図4)。そのため、電力消費量(エネルギー)当りの主流煙へのニコチン移行率が実施例1よりも低かった(表1)。再生たばこの基材の比熱に対する電力消費量(エネルギー)当りの主流煙へのニコチン移行率を示した図5のグラフに示されるように、実施例1では、基材であるたばこ材料の前記最大吸光度が0.40以上であり、かつ比熱が5mJ/mg・℃以下であることにより、電力消費量(エネルギー)当りの主流煙へのニコチン移行率が向上したことが理解できる。また、表1より、実施例1の基材は比較例1及び3の基材よりも安息角が低く、原料投入時に原料が投入しやすくなり、製造適性に優れることが分かった。さらに、実施例1の基材は比較例1及び3の基材と同等の吸水量を示し、べたつきの評価はこれらと同等であった。これより、アルカリ蒸解処理を行っても基材のべたつきに大きな変化はなく、同様にハンドリング性に優れ、原料投入時に原料は投入しやすいことが分かった。
As shown in Figures 3 and 4, the tobacco material is based on FT-IR analysis which shows a maximum absorbance of 0.40 or more at a wavelength of 3200 to 3600 cm -1 and a specific heat of 5 mJ/mg・℃ or less. In Example 1, in which regenerated tobacco was prepared using the regenerated tobacco, it was found in the evaluation of the non-combustion heated flavor inhaler containing the regenerated tobacco that the amount of nicotine and glycerin delivered was particularly large when the number of puffs increased. Additionally, the rate of nicotine transfer to mainstream smoke per unit of power consumption (energy) was also high (Table 1). On the other hand, a comparison was made in which recycled tobacco was prepared using a tobacco material with a maximum absorbance of less than 0.40 at a wavelength of 3200 to 3600 cm -1 or a specific heat of more than 5 mJ/mg/°C as determined by FT-IR analysis. In Examples 1 and 3, the amounts of nicotine and glycerin delivered were smaller than in Example 1 in the evaluation of the non-combustion heated flavor inhaler containing the recycled tobacco (FIGS. 3 and 4). Therefore, the nicotine transfer rate to mainstream smoke per unit of power consumption (energy) was lower than in Example 1 (Table 1). As shown in the graph of FIG. 5, which shows the nicotine transfer rate to mainstream smoke per power consumption (energy) with respect to the specific heat of the base material of recycled cigarettes, in Example 1, the maximum It can be understood that by having an absorbance of 0.40 or more and a specific heat of 5 mJ/mg·° C. or less, the nicotine transfer rate to mainstream smoke per unit of power consumption (energy) was improved. Further, from Table 1, it was found that the base material of Example 1 had a lower angle of repose than the base materials of Comparative Examples 1 and 3, making it easier to input the raw material at the time of inputting the raw material, and having excellent manufacturing suitability. Furthermore, the base material of Example 1 exhibited water absorption equivalent to that of the base materials of Comparative Examples 1 and 3, and the evaluation of stickiness was equivalent to that of the base materials of Comparative Examples 1 and 3. From this, it was found that there was no major change in the stickiness of the base material even if the alkali cooking treatment was performed, and the handling property was similarly excellent, and the raw material was easy to input.
1 非燃焼加熱型香味吸引器
2 たばこ含有セグメント
3 冷却セグメント
4 センターホールセグメント
5 フィルターセグメント
6 マウスピースセグメント
7 筒状部材
8 穿孔
9 第一の充填層
10 第一のインナープラグラッパー
11 アウタープラグラッパー
12 マウスピースライニングペーパー
13 加熱装置
14 ボディ
15 ヒーター
16 金属管
17 電池ユニット
18 制御ユニット
19 凹部 1 Non-combustion heated flavor inhaler 2 Tobacco-containing segment 3 Cooling segment 4 Center hole segment 5 Filter segment 6 Mouthpiece segment 7 Cylindrical member 8 Perforation 9 First filling layer 10 First inner plug wrapper 11 Outer plug wrapper 12 Mouthpiece lining paper 13 Heating device 14 Body 15 Heater 16 Metal tube 17 Battery unit 18 Control unit 19 Recess
2 たばこ含有セグメント
3 冷却セグメント
4 センターホールセグメント
5 フィルターセグメント
6 マウスピースセグメント
7 筒状部材
8 穿孔
9 第一の充填層
10 第一のインナープラグラッパー
11 アウタープラグラッパー
12 マウスピースライニングペーパー
13 加熱装置
14 ボディ
15 ヒーター
16 金属管
17 電池ユニット
18 制御ユニット
19 凹部 1 Non-combustion heated flavor inhaler 2 Tobacco-containing segment 3 Cooling segment 4 Center hole segment 5 Filter segment 6 Mouthpiece segment 7 Cylindrical member 8 Perforation 9 First filling layer 10 First inner plug wrapper 11 Outer plug wrapper 12 Mouthpiece lining paper 13 Heating device 14 Body 15 Heater 16 Metal tube 17 Battery unit 18 Control unit 19 Recess
Claims (11)
- たばこ材料と、たばこ成分と、を含む非燃焼加熱型香味吸引器用の再生たばこであって、
前記たばこ材料はFT-IR分析にて波長3200~3600cm-1の最大吸光度が0.40以上であり、
前記たばこ材料の比熱が5mJ/mg・℃以下である、再生たばこ。 A recycled tobacco for use in a non-combustion heated flavor inhaler, which includes a tobacco material and a tobacco component,
The tobacco material has a maximum absorbance of 0.40 or more at a wavelength of 3200 to 3600 cm −1 in FT-IR analysis,
Regenerated tobacco, wherein the tobacco material has a specific heat of 5 mJ/mg·°C or less. - 前記たばこ材料を23℃の水中に900秒浸漬した際の吸水量が4.0~6.0g/gである、請求項1に記載の再生たばこ。 The regenerated tobacco according to claim 1, wherein the tobacco material has a water absorption amount of 4.0 to 6.0 g/g when immersed in water at 23° C. for 900 seconds.
- 前記たばこ材料の安息角が40°以下である、請求項1又は2に記載の再生たばこ。 The regenerated tobacco according to claim 1 or 2, wherein the tobacco material has an angle of repose of 40° or less.
- たばこ原料からたばこ成分を抽出して得られるたばこ抽出液を含む、請求項1~3のいずれか一項に記載の再生たばこ。 The regenerated tobacco according to any one of claims 1 to 3, comprising a tobacco extract obtained by extracting tobacco components from tobacco raw materials.
- さらにバインダを含む、請求項1~4のいずれか一項に記載の再生たばこ。 The recycled tobacco according to any one of claims 1 to 4, further comprising a binder.
- さらに繊維材料を含む、請求項1~5のいずれか一項に記載の再生たばこ。 The regenerated tobacco according to any one of claims 1 to 5, further comprising a fiber material.
- シート状の再生たばこ、又は該シート状の再生たばこを裁断したシート刻状の再生たばこである、請求項1~6のいずれか一項に記載の再生たばこ。 The regenerated tobacco according to any one of claims 1 to 6, which is a regenerated tobacco sheet or a shredded regenerated tobacco obtained by cutting the regenerated tobacco sheet.
- 請求項1~7のいずれか一項に記載の再生たばこが充填された、たばこ含有セグメントを備える非燃焼加熱型香味吸引器。 A non-combustion heated flavor inhaler comprising a tobacco-containing segment filled with the recycled tobacco according to any one of claims 1 to 7.
- 請求項8に記載の非燃焼加熱型香味吸引器と、
前記たばこ含有セグメントを加熱する加熱装置と、
を備える非燃焼加熱型香味吸引システム。 The non-combustion heated flavor inhaler according to claim 8;
a heating device for heating the tobacco-containing segment;
A non-combustion heated flavor suction system. - 請求項1~7のいずれか一項に記載の再生たばこの製造方法であって、
たばこ原料からたばこ成分を抽出して、たばこ抽出液とたばこ残渣を得る工程と、
前記たばこ残渣をアルカリ蒸解処理した後、pHを4.0~6.5に調整する工程と、
pH調整後の前記たばこ残渣に前記たばこ抽出液をかけ戻す工程と、
を含む、方法。 The method for producing recycled tobacco according to any one of claims 1 to 7, comprising:
a step of extracting tobacco components from tobacco raw materials to obtain tobacco extract and tobacco residue;
After subjecting the tobacco residue to alkaline cooking treatment, adjusting the pH to 4.0 to 6.5;
Sprinkling the tobacco extract back onto the tobacco residue after pH adjustment;
including methods. - 前記アルカリ蒸解処理が、前記たばこ残渣にアルカリ金属の水酸化物を添加し、130~230℃で5分間~6時間加熱する処理である、請求項10に記載の方法。 The method according to claim 10, wherein the alkaline cooking treatment is a treatment in which an alkali metal hydroxide is added to the tobacco residue and heated at 130 to 230°C for 5 minutes to 6 hours.
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JP6019216B2 (en) * | 2013-03-21 | 2016-11-02 | 日本たばこ産業株式会社 | Method for producing black liquor and method for producing flavor component-containing liquid |
WO2019097641A1 (en) * | 2017-11-16 | 2019-05-23 | 日本たばこ産業株式会社 | Method for manufacturing fragrance-carrying tobacco filler, fragrance-carrying tobacco filler, and heating type flavor inhaler |
CN112385890A (en) * | 2019-10-09 | 2021-02-23 | 湖北中烟工业有限责任公司 | Heating device for low-temperature cigarette |
WO2022138261A1 (en) * | 2020-12-24 | 2022-06-30 | 日本たばこ産業株式会社 | Tobacco composition, tobacco-containing segment, non-combustion heating-type flavor inhaler, and non-combustion heating-type flavor inhalation system |
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JP6019216B2 (en) * | 2013-03-21 | 2016-11-02 | 日本たばこ産業株式会社 | Method for producing black liquor and method for producing flavor component-containing liquid |
WO2019097641A1 (en) * | 2017-11-16 | 2019-05-23 | 日本たばこ産業株式会社 | Method for manufacturing fragrance-carrying tobacco filler, fragrance-carrying tobacco filler, and heating type flavor inhaler |
CN112385890A (en) * | 2019-10-09 | 2021-02-23 | 湖北中烟工业有限责任公司 | Heating device for low-temperature cigarette |
WO2022138261A1 (en) * | 2020-12-24 | 2022-06-30 | 日本たばこ産業株式会社 | Tobacco composition, tobacco-containing segment, non-combustion heating-type flavor inhaler, and non-combustion heating-type flavor inhalation system |
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