CA3074591C - Tobacco material - Google Patents
Tobacco material Download PDFInfo
- Publication number
- CA3074591C CA3074591C CA3074591A CA3074591A CA3074591C CA 3074591 C CA3074591 C CA 3074591C CA 3074591 A CA3074591 A CA 3074591A CA 3074591 A CA3074591 A CA 3074591A CA 3074591 C CA3074591 C CA 3074591C
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- CA
- Canada
- Prior art keywords
- tobacco
- particles
- dispersion medium
- tobacco material
- weight
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
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Classifications
-
- A—HUMAN NECESSITIES
- A24—TOBACCO; CIGARS; CIGARETTES; SIMULATED SMOKING DEVICES; SMOKERS' REQUISITES
- A24B—MANUFACTURE OR PREPARATION OF TOBACCO FOR SMOKING OR CHEWING; TOBACCO; SNUFF
- A24B15/00—Chemical features or treatment of tobacco; Tobacco substitutes, e.g. in liquid form
- A24B15/18—Treatment of tobacco products or tobacco substitutes
- A24B15/28—Treatment of tobacco products or tobacco substitutes by chemical substances
- A24B15/30—Treatment of tobacco products or tobacco substitutes by chemical substances by organic substances
- A24B15/32—Treatment of tobacco products or tobacco substitutes by chemical substances by organic substances by acyclic compounds
-
- A—HUMAN NECESSITIES
- A24—TOBACCO; CIGARS; CIGARETTES; SIMULATED SMOKING DEVICES; SMOKERS' REQUISITES
- A24B—MANUFACTURE OR PREPARATION OF TOBACCO FOR SMOKING OR CHEWING; TOBACCO; SNUFF
- A24B15/00—Chemical features or treatment of tobacco; Tobacco substitutes, e.g. in liquid form
- A24B15/18—Treatment of tobacco products or tobacco substitutes
-
- A—HUMAN NECESSITIES
- A24—TOBACCO; CIGARS; CIGARETTES; SIMULATED SMOKING DEVICES; SMOKERS' REQUISITES
- A24B—MANUFACTURE OR PREPARATION OF TOBACCO FOR SMOKING OR CHEWING; TOBACCO; SNUFF
- A24B15/00—Chemical features or treatment of tobacco; Tobacco substitutes, e.g. in liquid form
- A24B15/18—Treatment of tobacco products or tobacco substitutes
- A24B15/24—Treatment of tobacco products or tobacco substitutes by extraction; Tobacco extracts
-
- A—HUMAN NECESSITIES
- A24—TOBACCO; CIGARS; CIGARETTES; SIMULATED SMOKING DEVICES; SMOKERS' REQUISITES
- A24B—MANUFACTURE OR PREPARATION OF TOBACCO FOR SMOKING OR CHEWING; TOBACCO; SNUFF
- A24B3/00—Preparing tobacco in the factory
- A24B3/12—Steaming, curing, or flavouring tobacco
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Health & Medical Sciences (AREA)
- General Health & Medical Sciences (AREA)
- Toxicology (AREA)
- Manufacture Of Tobacco Products (AREA)
Abstract
Description
TOBACCO MATERIAL
TECHNICAL FIELD
[0001] The present invention relates to a tobacco material and a tobacco product comprising the tobacco material.
BACKGROUND ART
Moreover, PTL 2 discloses a method of improving flavor through heating of a suspension of tobacco particles by utilizing the Maillard reaction or the like (PTL 2, paragraph [0013]).
Such tobacco particles are smaller than 40 mesh (PTL 2, paragraph [0024]), in other words, smaller than 400 pm. Meanwhile, a suspension of tobacco particles is also known as a raw material for a reconstituted tobacco sheet, and PTL 3 discloses that a suspension of tobacco particles with 60 to 400 mesh is heated to 80 F to 180 F (26.7 C to 82.2 C) (PTL 3, paragraph [0056]). The particle size of these tobacco particles is 38 to 250 lam.
CITATION LIST
PATENT LITERATURE
TECHNICAL PROBLEM
Accordingly, the above-mentioned problem is a problem peculiar to the use of fine particles with an average particle size of 30 p.m or less and is thus a novel problem found by the present inventors.
SOLUTION TO PROBLEM
(1) A tobacco material comprising an aqueous dispersion medium and tobacco particles that are dispersed in the dispersion medium and have an average particle size of 30 i_tm or less, where a hemicellulose content in the tobacco material is 0.8% by weight or less based on bone-dry tobacco particles.
(2) The tobacco material according to (1), where a pH is 4.8 or less.
(3) The tobacco material according to (1) or (2), where the aqueous dispersion medium contains an aqueous organic compound.
(4) The tobacco material according to (3), where the aqueous organic compound is selected from the group consisting of monohydric alcohols, polyhydric alcohols, sugar alcohols, sugars, polyhydric alcohol esters, and combinations thereof.
(5) The tobacco material according to any one of (1) to (4), where a water content in the aqueous dispersion medium exceeds 50% by weight.
ADVANTAGEOUS EFFECTS OF INVENTION
[0006] According to the present invention, it is possible to provide a low-viscosity tobacco material in which tobacco particles are dispersed in an aqueous dispersion medium.
BRIEF DESCRIPTION OF DRAWINGS
[0007] Fig. lA shows the viscosity of tobacco materials.
Fig. 1B shows the viscosity of tobacco materials.
Fig. 1C shows the viscosity of tobacco materials.
Fig. 2 shows the results of a storage test.
Fig. 3 shows the pH of tobacco materials.
DESCRIPTION OF EMBODIMENTS
[0008] Hereinafter, the present invention will be described in detail. In the present invention, the wording "X to Y" includes the lower and the upper limits of X
and Y.
[0009] 1. Tobacco Material A tobacco material of the present invention comprises an aqueous dispersion medium and tobacco particles that are dispersed in the dispersion medium and have an average particle size of 301.1,m or less.
[0010] (1) Tobacco Particles Tobacco particles may be derived from a tobacco raw material, a fermented tobacco raw material, or a heat-treated tobacco raw material. The tobacco raw material herein means whole tobacco or parts of tobacco. As such parts, leaves, veins, stems, roots, flowers, and mixtures thereof may be used. The variety of tobacco is not particularly limited, and examples include flue-cured, barley, domestic, and oriental. A
tobacco raw material to be used may be in the state of fresh leaves immediately after the harvest without being subjected to drying or the like, leaves that have been subjected to drying treatment after the harvest, or combinations thereof. In addition, tobacco stems and veins, expanded tobacco, and sheet tobacco obtained by processing these tobacco raw materials may also be used. These materials may be used alone or in combination of a plurality of varieties or parts.
[0011] Tobacco particles can be prepared by any suitable method but is preferably prepared by subjecting a tobacco raw material to common drying treatment, then coarse grinding with a common coarse grinder, followed by fine grinding. The drying treatment and coarse grinding may be performed in any publicly known manner, and the average particle size of coarsely ground tobacco particles preferably falls within a range from several hundred micrometers to several millimeters. A method for fine grinding is also not limited, and either method of wet grinding and dry grinding may be employed. The wet grinding can be performed by adding a liquid dispersion medium to coarsely ground tobacco particles, mixing, and processing the resulting mixture in a wet milling machine (MIC-2:
from Nara Machinery Co., Ltd., for example). The milling machine is preferably set to the rotation number of typical 1,100 to 1,300 rpm and milling time of about 5 to 100 minutes.
Meanwhile, dry grinding can be performed by processing coarsely ground tobacco particles in a dry fine grinder, such as a jet mill.
[0012] The thus-obtained tobacco particles have an average particle size of 30 gm or less and preferably 20 pm or less. By having such average particle sizes, clogging of a nozzle is less likely to occur during spraying of a dispersion; and tobacco particles are readily and uniformly dispersed in the tobacco material. Accordingly, smoking flavor can be evenly imparted to smoking articles. The lower limit of the average particle size of tobacco particles is 5 gm or more in one embodiment and 8 pm or more in another embodiment.
The average particle size of tobacco particles is adjustable by grinding conditions. For example, the average particle size can be increased by shortening the time for fine grinding, reducing the viscosity of a dispersion medium, and so forth.
[0013] The average particle size of the present invention can be determined by a laser diffraction/scattering method. Specifically, the average particle size of the present invention is measured by using a laser diffraction particle size analyzer (SALD-2100 nano particle size analyzer from Shimadzu Corporation) at a diffractive index of 1.60 to 0.101.
The aqueous dispersion medium may be water alone or may contain a specific organic compound. The organic compound is preferably water soluble, and such an aqueous organic compound is preferably selected from the group consisting of monohydric alcohols, polyhydric alcohols, sugar alcohols, sugars, polyhydric alcohol esters, and combinations thereof. When the organic compound is insoluble in water, the organic compound can be dissolved in an aqueous dispersion medium by using in combination with an amphiphilic organic compound, such as methanol.
Examples of the sugar alcohols include sorbitol, maltitol, xylitol, erythritol, lactitol, sorbitan, xylose, arabinose, mannose, and trehalose.
Examples of the sugars include lactose, table sugar, coupling sugar, glucose, enzyme-converted syrup, acid-converted syrup, maltose syrup, maltose, high-fructose corn syrup, fructose, hydrogenated maltose, hydrogenated starch syrup, and honey.
Examples of the polyhydric alcohol esters include fatty acid polyhydric alcohol esters, such as fatty acid triglycerides.
by weight or less, further preferably 10% by weight or less, and particularly preferably 9% by weight or less based on bone-dry tobacco particles.
Meanwhile, a tobacco material of the present invention with the above-mentioned pH ranges is also characterized by suppressed proliferation of microorganisms and capability of maintaining the quality. The pH of a tobacco material can be determined by measuring a hydrogen ion concentration in the tobacco material by using a pH meter.
and a tobacco particle concentration of 16.7% by weight is preferably 10 to 500 cP and more preferably 10 to 200 cP. The viscosity is measured with a B-type viscometer.
= CA 03074591 2020-03-02
Examples of the additives include food ingredients for designing flavor, such as spearmint leaves, peppermint leaves, green tea and other tea leaves, coffee, cocoa, cardamom, menthol, and sugar; polysaccharide thickeners for enhancing dispersibility through viscosity adjustment, such as glucans and pectin; food additives, such as various emulsifiers; glues, such as carboxymethyl cellulose (CMC); and curing agents for enhancing handling properties after addition to tobacco. The timing of adding such additives is not limited, and additives may be added before fine grinding of a tobacco raw material and finely ground together or may be added to a tobacco material. The proportions of additives may also be set suitably.
However, when additives are contained, the total amount of tobacco particles and a dispersion medium in a tobacco material of the present invention is preferably 90% by weight or more and more preferably 95% by weight or more based on the total amount of the tobacco material.
or lower. Heating is preferably performed under pressure by using an apparatus, such as a pressure cooker. The pressure is preferably 1.8 MPa or higher. A tobacco material of the present invention produced under these conditions also exerts an effect of remarkably = CA 03074591 2020-03-02 suppressing proliferation of microorganisms.
Examples of the auxiliary members include cigarette paper, filters, and tipping paper.
Examples of the method of adding a tobacco material to a base material include, but are not particularly limited to, dropwise addition, spraying, coating, and impregnation.
by weight based on the weight of the tobacco shreds in view of efficiency in imparting smoking flavor. When tobacco with strong flavor is used for a tobacco material, the above-mentioned proportion may be reduced to 0.01 to 0.1% by weight, for example.
EXAMPLES
Tobacco particles with an average particle size of 30 .1.1n were prepared as in the following by using a leaf tobacco raw material (Brazilian flue-cured raw material).
The leaf tobacco raw material was coarsely ground to 10 mm or less by using a cutter mill from Tokyo Atomizer M. F. G. Co., Ltd. Subsequently, the coarsely ground leaf -tobacco raw material was coarsely ground further to an average particle size of 100 pm or less by using a CONDUX impact mill from NETZSCH Group and then finely ground by using a CSM impact classifier mill from NETZSCH Group to yield tobacco particles with an average particle size of 30 pm or less.
The suspended state of the tobacco particles did not change even after the high-temperature high-pressure treatment.
A: 160 C-10 min B: 180 C-10 min C: 180 C-30 min D: 180 C-60 min
by using a B-type viscometer (rotor No. 1, rotation number of 0.3 to 100 rpm).
1) A slurry was washed with water and subjected to centrifugation (8,000 rpm, min) to collect a settled residue. This procedure was repeated twice.
2) The collected residue was rinsed with ethanol and subjected to centrifugation (8,000 rpm, 10 min) to collect a settled residue. This procedure was repeated twice.
3) The resulting residue was dried in a constant-temperature apparatus (100 C-2 hrs).
4) The dried residue was weighed, and quantification of cellulose and hemicellulose by the Van Soest method was outsourced to Japan Food Research Laboratories to obtain cellulose and hemicellulose contents based on the weight of bone-dry tobacco particles.
A tobacco material of the present invention was produced and evaluated in the same manner as Example 1 except for changing the content of tobacco particles (bone dry) to 14.3% by weight and performing only high-temperature high-pressure treatment D
above.
A tobacco material of the present invention was produced and evaluated in the same manner as Example 1 except for changing the content of tobacco particles (bone dry) to 20.0% by weight and performing only high-temperature high-pressure treatment D
above.
A tobacco material for comparison was produced and evaluated in the same manner as Example 1 except for changing the high-temperature high-pressure treatment to the following.
X: None Y: 150 C -5 min Z: 150 C-15 min
Tobacco materials for comparison were produced and evaluated in the same manner as Examples 2 and 3, respectively, except for omitting the high-temperature high-pressure treatment.
These results are shown in Figs. 1 and 2 as well as Tables 1 and 2.
Table 1 The amount of hemicellulose for Examples and Comparative Examples (weight %) Ex. 1 Ex. 2 Ex. 3 Comp.
Comp. Comp.
Ex. 1 Ex. 2 Ex. 3 A 160 C-10 min 0.0 B 180 C-10 min 0.0 C 180 C-30 min 0.0 D 180 C-60 min 0.0 0.0 0.0 Y 150 C -5 min 1.4 Z 150 C-15 min 0.9 X None 2.7 2.7 2.7
Table 2 The amount of cellulose for Examples and Comparative Examples (weight%) Ex. 1 Ex. 2 Ex. 3 Comp.
Comp. Comp.
Ex. 1 Ex. 2 Ex. 3 A 160 C-10 min 11.7 B 180 C-10 min 8.8 - -C 180 C-30 min 8.6 D 180 C-60 min 7.5 7.5 8.8 Y 150 C -5 min 13.5 Z 150 C-15 min 10.8 X None 12.2 12.2 12.2
and Z (hereinafter, referred to as "Comparative Example 1Y" and the like) in Comparative Example 1 tend to have an increased viscosity. This is presumably because a large amount of polysaccharides were extracted into an aqueous medium but were not decomposed by high-temperature high-pressure treatment under such conditions, thereby increasing interactions with water. Meanwhile, the tobacco materials of the present invention, such as Example 1A, are considered to achieve a lower viscosity through extraction of a large amount of polysaccharides and the like including hemicellulose into an aqueous medium, followed by decomposition. As described above, it is clear that the tobacco materials of the present invention with a certain content or less of hemicellulose exhibit a low viscosity.
A hydrogen ion concentration in a slurry was measured by using a pH meter from Mettler Toledo for the tobacco materials of the present invention treated under high-temperature high-pressure conditions A and C in Example 1 [the content of tobacco particles (bone dry): 16.7% by weight]. These tobacco materials were poured into 50 mL
vials and subjected to a storage test. The storage test was performed by placing the vials in a constant-temperature room at 35 C. A total viable count was measured for samples obtained immediately after the start of the storage test, after 72 hours, and after 120 hours.
The total viable count was measured in accordance with the method posted on the home = CA 03074591 2020-03-02 page of Japan Food Research Laboratories as in the following.
1) A sample was diluted with sterile water to prepare serial tenfold diluted samples.
2) Each of the samples diluted to the respective concentrations were inoculated on a standard agar medium and cultured at 35 C for two days. After the culture, the number of colonies was counted.
3) The initial viable count of the samples was calculated on the basis of differences in the number of colonies appeared for the respective dilutions.
The tobacco material for comparison that did not undergo high-temperature high-pressure treatment of Comparative Example 1 was subjected to a storage test in the same manner as Example 4.
Claims (13)
preparing a dispersion containing an aqueous dispersion medium and tobacco particles that are dispersed in the dispersion medium and have an average particle size of 30 gm or less; and heating the dispersion to 160 C or higher.
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| PCT/JP2017/031947 WO2019049207A1 (en) | 2017-09-05 | 2017-09-05 | Tobacco material |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CA3074591A1 CA3074591A1 (en) | 2019-03-14 |
| CA3074591C true CA3074591C (en) | 2022-07-12 |
Family
ID=65634894
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CA3074591A Active CA3074591C (en) | 2017-09-05 | 2017-09-05 | Tobacco material |
Country Status (8)
| Country | Link |
|---|---|
| US (1) | US20200196657A1 (en) |
| EP (1) | EP3662765B1 (en) |
| JP (1) | JP6945635B2 (en) |
| KR (1) | KR102425798B1 (en) |
| CN (1) | CN111050572A (en) |
| CA (1) | CA3074591C (en) |
| RU (1) | RU2745863C1 (en) |
| WO (1) | WO2019049207A1 (en) |
Families Citing this family (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP3984379B1 (en) * | 2020-10-15 | 2023-07-05 | JT International SA | Method for manufacturing an rtb sheet comprising a tobacco product |
| JP7617950B2 (en) * | 2020-12-24 | 2025-01-20 | 日本たばこ産業株式会社 | Manufacturing method of tobacco material |
| KR102790355B1 (en) * | 2021-04-08 | 2025-04-04 | 주식회사 케이티앤지 | Tobacco material comprising flavor material and method of manufacturing the same |
| KR102790354B1 (en) * | 2021-04-08 | 2025-04-04 | 주식회사 케이티앤지 | Tobacco material comprising natural flavor material and method of manufacturing the same |
| JP2024147831A (en) * | 2021-06-11 | 2024-10-17 | 日本たばこ産業株式会社 | Tobacco preparations |
| JPWO2024209684A1 (en) | 2023-04-07 | 2024-10-10 |
Family Cites Families (16)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB573191A (en) * | 1942-08-13 | 1945-11-09 | American Mach & Foundry | Improvements in or relating to cigars cigarettes and the like |
| JPS6167469A (en) * | 1984-09-11 | 1986-04-07 | 日本たばこ産業株式会社 | Production of fragrance for tobacco |
| EP0283672B1 (en) * | 1987-02-10 | 1993-09-22 | R.J. Reynolds Tobacco Company | Cigarette |
| JP3681410B2 (en) | 1992-04-09 | 2005-08-10 | フィリップ・モーリス・プロダクツ・インコーポレイテッド | Reconstituted tobacco sheet and method for producing and using the same |
| EP0821886A3 (en) * | 1996-08-01 | 1998-08-19 | R.J. Reynolds Tobacco Company | Method of providing aromatic compounds from tobacco |
| CN101273796B (en) * | 2008-05-07 | 2010-06-02 | 广东省金叶烟草薄片技术开发有限公司 | Composite papermaking method reconstituted tobacco and producing method thereof |
| US9167847B2 (en) * | 2009-03-16 | 2015-10-27 | Philip Morris Usa Inc. | Production of coated tobacco particles suitable for usage in a smokeless tobacoo product |
| CN102429319B (en) * | 2011-08-26 | 2013-11-27 | 重庆恒远晋通科技有限公司 | Continuous extracting method for tobacco |
| JP2013215187A (en) * | 2012-03-15 | 2013-10-24 | Kao Corp | Method for producing saccharide |
| JP2014185103A (en) | 2013-03-22 | 2014-10-02 | L'oreal Sa | Persistent coloration of hair using condensation agent |
| EP2783585A1 (en) * | 2013-03-28 | 2014-10-01 | Philip Morris Products S.A. | Tobacco based casing |
| WO2014185103A1 (en) * | 2013-05-13 | 2014-11-20 | 日本たばこ産業株式会社 | Tobacco material, tobacco product to which tobacco material is added, and method for producing tobacco material |
| JP2015200056A (en) * | 2014-03-31 | 2015-11-12 | 日本製紙株式会社 | Method of producing dissolved craft pulp continuously |
| WO2016156598A1 (en) * | 2015-04-01 | 2016-10-06 | Philip Morris Products S.A. | Homogenized tobacco material and method of production of homogenized tobacco material |
| PL3324759T3 (en) * | 2015-07-21 | 2026-01-26 | Philip Morris Products S.A. | Method of making tobacco products |
| US10869497B2 (en) * | 2015-09-08 | 2020-12-22 | R.J. Reynolds Tobacco Company | High-pressure cold pasteurization of tobacco material |
-
2017
- 2017-09-05 RU RU2020112537A patent/RU2745863C1/en active
- 2017-09-05 WO PCT/JP2017/031947 patent/WO2019049207A1/en not_active Ceased
- 2017-09-05 EP EP17924586.5A patent/EP3662765B1/en active Active
- 2017-09-05 JP JP2019540157A patent/JP6945635B2/en active Active
- 2017-09-05 CN CN201780094636.9A patent/CN111050572A/en active Pending
- 2017-09-05 CA CA3074591A patent/CA3074591C/en active Active
- 2017-09-05 KR KR1020207009086A patent/KR102425798B1/en active Active
-
2020
- 2020-03-04 US US16/809,322 patent/US20200196657A1/en not_active Abandoned
Also Published As
| Publication number | Publication date |
|---|---|
| EP3662765A4 (en) | 2021-04-07 |
| RU2745863C1 (en) | 2021-04-02 |
| KR102425798B1 (en) | 2022-07-28 |
| JP6945635B2 (en) | 2021-10-06 |
| CN111050572A (en) | 2020-04-21 |
| WO2019049207A1 (en) | 2019-03-14 |
| EP3662765B1 (en) | 2022-08-17 |
| US20200196657A1 (en) | 2020-06-25 |
| KR20200044925A (en) | 2020-04-29 |
| EP3662765A1 (en) | 2020-06-10 |
| CA3074591A1 (en) | 2019-03-14 |
| JPWO2019049207A1 (en) | 2020-10-01 |
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