TWI634847B - Method for producing shred tobacco for formulating smoking products - Google Patents

Method for producing shred tobacco for formulating smoking products Download PDF

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TWI634847B
TWI634847B TW105128614A TW105128614A TWI634847B TW I634847 B TWI634847 B TW I634847B TW 105128614 A TW105128614 A TW 105128614A TW 105128614 A TW105128614 A TW 105128614A TW I634847 B TWI634847 B TW I634847B
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tobacco
yarn
reaction
smoking article
reaction mixture
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TW105128614A
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TW201811204A (en
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佐藤梨保
井上康信
勝岡恵
田口秀
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日本煙草產業股份有限公司
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Abstract

本發明之吸煙物品調配用煙草絲之製造方法,係包含:以可獲得具有3.5以下pH的反應混合液之方式,將選自含有煙草絲所含有之成分的煙草萃取液及煙草絲之反應對象、與選自具有磺酸基之固體酸觸媒及硫酸之反應參與物質進行混合,而使前述煙草絲所含有之成分的反應產生。 The method for producing a tobacco yarn for blending a smoking article according to the present invention comprises: a reaction product selected from the group consisting of tobacco extract containing tobacco silk and tobacco silk, in a manner of obtaining a reaction mixture having a pH of 3.5 or less And reacting with a reaction substance selected from a solid acid catalyst having a sulfonic acid group and sulfuric acid to produce a reaction of a component contained in the tobacco yarn.

Description

吸煙物品調配用煙草絲的製造方法  Method for producing tobacco yarn for smoking article preparation  

本發明係關於吸煙物品調配用煙草絲之製造方法。 The present invention relates to a method of producing tobacco yarn for smoking article formulation.

香煙等吸煙物品之吸煙時,會從吸煙物品產生:經由吸煙物品本體而被吸煙者抽吸之主流煙、及特別是在自然燃燒時從吸煙物品之先端部升起之副流煙。在該技術領域中,已報告有降低副流煙之各種技術,例如專利文獻1係報告使用二層卷紙之香煙。 When smoking articles such as cigarettes are smoked, they are generated from smoking articles: mainstream smoke smoked by smokers through the body of the smoking article, and sidestream smoke rising from the tip end of the smoking article, particularly during natural combustion. In the technical field, various techniques for reducing sidestream smoke have been reported. For example, Patent Document 1 reports the use of a cigarette of a two-layer roll paper.

[先前技術文獻]  [Previous Technical Literature]   [專利文獻]  [Patent Literature]  

[專利文獻1]國際公開第99/35923號 [Patent Document 1] International Publication No. 99/35923

在專利文獻1中由於卷紙為二層且內側之卷紙為難通氣性,故香煙在燃燒時,卷紙之內部容易存積熱,且難以釋出至外部,藉此而容易使燃燒部之溫度上昇。 其結果,專利文獻1之香煙係相較於具有通常卷紙之香煙,有燃燒速度增加、香煙之吸煙次數(亦即,吸煙至成為特定煙頭長度所需之次數)減少之傾向。香煙之吸煙係可使吸煙者放輕鬆,並且提供悠閒之時間。因此,吸煙次數對吸煙者而言為重要之香煙性能之一。 In Patent Document 1, since the roll paper is two-layered and the inner roll paper is difficult to ventilate, when the cigarette is burned, heat is easily accumulated inside the roll paper, and it is difficult to release it to the outside, thereby facilitating the combustion portion. The temperature rises. As a result, the cigarette of Patent Document 1 tends to decrease in the burning speed and the number of cigarettes to be smoked (that is, the number of times the cigarette is required to become a specific length of the cigarette) is reduced as compared with a cigarette having a normal roll paper. Cigarette smoking allows smokers to relax and provide leisure time. Therefore, the number of cigarettes is one of the important cigarette properties for smokers.

因此,本發明之目的在於提供一種煙草絲,其係被調配於吸煙物品時,不減少吸煙次數,而且可減少自吸煙物品所生成之副流煙。 Accordingly, it is an object of the present invention to provide a tobacco yarn which, when formulated in a smoking article, does not reduce the number of smoking, and which reduces sidestream smoke generated from smoking articles.

依據本發明之一態樣,係提供一種吸煙物品調配用煙草絲之製造方法,係包含:以可獲得具有3.5以下之pH的反應混合液之方式,將選自含有煙草絲所含有之成分的煙草萃取液及煙草絲之反應對象、與選自具有磺酸基之固體酸觸媒及硫酸之反應參與物質進行混合,使前述煙草絲所含有之成分的反應產生。 According to an aspect of the present invention, a method for producing a tobacco yarn for smoking article formulation comprises: selecting a reaction mixture having a pH of 3.5 or less, and selecting a component selected from the group consisting of tobacco silk containing ingredients The reaction object of the tobacco extract and the tobacco silk is mixed with a reaction-participating substance selected from the group consisting of a solid acid catalyst having a sulfonic acid group and sulfuric acid to produce a reaction of the components contained in the tobacco yarn.

依據另一態樣,提供藉由前述方法所得之吸煙物品調配用煙草絲。 According to another aspect, a tobacco yarn for smoking article preparation obtained by the aforementioned method is provided.

依據再另一態樣,提供含有前述吸煙物品調配用煙草絲之吸煙物品。 According to still another aspect, a smoking article comprising the tobacco yarn for dispensing the aforementioned smoking article is provided.

依據本發明,可提供一種煙草絲,其係被調配於吸煙物品時,可一邊維持吸煙次數,一邊降低自吸煙物品生成之副流煙。 According to the present invention, it is possible to provide a tobacco yarn which, when formulated in a smoking article, can reduce the sidestream smoke generated from the smoking article while maintaining the number of times of smoking.

1‧‧‧煙草絲 1‧‧‧Tobacco

2、5c‧‧‧水 2, 5c‧‧‧ water

3‧‧‧煙草萃取液 3‧‧‧Tobacco extract

4‧‧‧萃取殘渣 4‧‧‧ Extraction residue

5a‧‧‧具有磺基之固體酸觸媒 5a‧‧‧Solid acid catalyst with sulfo group

5b‧‧‧硫酸 5b‧‧‧sulfuric acid

6‧‧‧ph3.5以下之反應混合液 6‧‧‧pH3.5 below reaction mixture

7‧‧‧反應後之反應混合液 7‧‧‧Reaction mixture after reaction

8、8b‧‧‧反應後之煙草萃取液 8, 8b‧‧‧ tobacco extract after reaction

9‧‧‧處理液 9‧‧‧Processing fluid

10‧‧‧混合物 10‧‧‧Mixture

11‧‧‧吸煙物品調配用煙草絲 11‧‧‧Tobacco wire for smoking articles

第1圖係表示第1實施形態之方法的流程圖。 Fig. 1 is a flow chart showing the method of the first embodiment.

第2圖係表示第2實施形態之方法的流程圖。 Fig. 2 is a flow chart showing the method of the second embodiment.

第3圖係表示第3實施形態之方法的流程圖。 Fig. 3 is a flow chart showing the method of the third embodiment.

第4圖係表示第4實施形態之方法的流程圖。 Fig. 4 is a flow chart showing the method of the fourth embodiment.

1.吸煙物品調配用煙草絲之製造方法  1. Method for manufacturing tobacco wire for smoking article preparation  

本發明之吸煙物品調配用煙草絲的製造方法,係包含:以可獲得具有3.5以下之pH的反應混合液之方式,將選自含有煙草絲所含有之成分的煙草萃取液及煙草絲之反應對象、與選自具有磺酸基之固體酸觸媒及硫酸之反應參與物質進行混合,使前述煙草絲所含有之成分的反應產生。 The method for producing a tobacco yarn for blending a smoking article of the present invention comprises: reacting a tobacco extract liquid and tobacco silk selected from the group consisting of tobacco silk containing a reaction mixture having a pH of 3.5 or less The object is mixed with a reaction-participating substance selected from a solid acid catalyst having a sulfonic acid group and sulfuric acid to cause a reaction of components contained in the tobacco yarn.

在下述說明中,反應對象為含有煙草絲所含有之成分的煙草萃取液,反應參與物質為具有磺酸基之固體酸觸媒之前述方法稱為第1實施形態;反應對象為含有煙草絲所含有之成分的煙草萃取液,反應參與物質為硫酸之前述方法稱為第2實施形態;反應對象為煙草絲,反應參與物質為具有磺酸基之固體酸觸媒之前述方法稱為第3實施形態;反應對象為煙草絲,反應參與物質為硫酸之前述方法稱為第4實施形態。 In the following description, the reaction object is a tobacco extract containing a component contained in tobacco silk, and the above-mentioned method in which the reaction-participating substance is a solid acid catalyst having a sulfonic acid group is referred to as a first embodiment; The tobacco extract containing the component, the reaction-involved substance is sulfuric acid, and the above-mentioned method is called the second embodiment; the reaction target is tobacco silk, and the reaction-involved substance is a solid acid catalyst having a sulfonic acid group. The above-mentioned method is called the third embodiment. The above-mentioned method in which the reaction target is tobacco silk and the reaction-participating substance is sulfuric acid is referred to as a fourth embodiment.

以下,針對各實施形態進行說明,但以下 之說明的目的係詳細地說明本發明,並非用以限定本發明。 In the following, the embodiments are described in detail, but the following description is intended to describe the invention in detail and not to limit the invention.

[第1實施形態]  [First Embodiment]  

參照第1圖而說明第1實施形態。 The first embodiment will be described with reference to Fig. 1 .

第1實施形態之方法係包含:以可獲得具有3.5以下pH的反應混合液之方式,將含有煙草絲所含有之成分的煙草萃取液、與具有磺酸基之固體酸觸媒進行混合,使前述煙草絲所含有之成分產生反應。 The method according to the first embodiment includes mixing a tobacco extract containing a component contained in tobacco silk with a solid acid catalyst having a sulfonic acid group so that a reaction mixture having a pH of 3.5 or less is obtained. The components contained in the tobacco yarn described above react.

具體而言,第1實施形態之方法係包含:將煙草絲1所含有之成分以水2進行萃取,生成含有前述成分與前述水之煙草萃取液3、及含有前述成分經萃取後之前述煙草絲的萃取殘渣4之混合物;從前述萃取殘渣4分離前述煙草萃取液3;以可獲得具有3.5以下pH的反應混合液6之方式將經分離之前述煙草萃取液3、與具有磺酸基之固體酸觸媒5a進行混合,使前述成分之反應產生;從反應後之反應混合液7去除前述固體酸觸媒5a,獲得反應後之煙草萃取液8;藉由濃縮所得之煙草萃取液8,而從煙草萃取液8去除水2,獲得處理液9;將所得之處理液9與前述萃取殘渣4混合,獲得混合物10;使前述混合物10乾燥,而製造吸煙物品調配用煙草絲11。 Specifically, the method according to the first embodiment includes extracting a component contained in the tobacco yarn 1 with water 2 to produce a tobacco extract 3 containing the component and the water, and the tobacco after extracting the component a mixture of silk extraction residue 4; separating the tobacco extract 3 from the extraction residue 4; separating the tobacco extract 3 and having a sulfonic acid group in such a manner that a reaction mixture 6 having a pH of 3.5 or less can be obtained. The solid acid catalyst 5a is mixed to produce a reaction of the above components; the solid acid catalyst 5a is removed from the reaction mixture 7 after the reaction to obtain the tobacco extract 8 after the reaction; and the obtained tobacco extract 8 is concentrated. The water 2 is removed from the tobacco extract 8 to obtain a treatment liquid 9; the obtained treatment liquid 9 is mixed with the extraction residue 4 to obtain a mixture 10; and the mixture 10 is dried to produce a tobacco yarn 11 for smoking article preparation.

在第1實施形態中,首先將煙草絲1曝露於以水2之萃取步驟,將煙草絲1所含有之成分(以下,亦稱為煙草成分)以水2進行萃取。藉此生成含有煙草成分與水之煙草萃取液3、以及含有煙草成分經萃取後之煙草絲的萃取殘渣4。 In the first embodiment, the tobacco yarn 1 is first exposed to the extraction step of water 2, and the components (hereinafter also referred to as tobacco components) contained in the tobacco yarn 1 are extracted with water 2. Thereby, the tobacco extract 3 containing the tobacco component and water, and the extraction residue 4 containing the extracted tobacco filament of the tobacco component are produced.

煙草絲1可使用經整備為調配於吸煙物品之煙草絲。煙草絲1可使用任意之品種者,可使用例如黄色種、柏利種、東方種等之類。煙草絲1可使用單一品種者,亦可使用不同品種之混合物。煙草絲1係可含有除骨葉、中骨、及由此等原料所構成之再生煙草(亦即,將工廠之作業步驟所產生之葉屑、絲屑、中骨屑、細粉等加工成可再使用之形状的煙草材料)等。所謂「整備為調配於吸煙物品之煙草絲」係指經過在農家之乾燥步驟、其後在原料工場的1年至數年之長期熟成步驟、以及其後在製造工場的摻混及裁絲等各種加工處理,而整備為將調配於吸煙物品之煙草絲。吸煙物品為香煙時,「整備為調配於吸煙物品之煙草絲」係「整備為使用在香煙卷起步驟之煙草絲」。 Tobacco silk 1 can be used to prepare tobacco yarn that is formulated into a smoking article. As the tobacco yarn 1, any of various varieties can be used, and for example, yellow species, bailey species, oriental species, and the like can be used. Tobacco silk 1 can be used in a single variety, or a mixture of different varieties can be used. The tobacco silk 1 system may contain regenerated tobacco consisting of bone leaves, medium bones, and the like (that is, the leaf chips, silk chips, medium bone chips, fine powder, etc. produced by the working steps of the factory are processed into Reusable shape of tobacco material) and the like. The so-called "tobacco wire blended with smoking articles" refers to the long-term ripening step in the drying process of the farmer, the one-year to several years in the raw material workshop, and the subsequent blending and cutting of the manufacturing workshop. Various processing treatments are prepared for the tobacco yarn to be blended in smoking articles. When the smoking article is a cigarette, "the whole is a tobacco yarn that is blended in a smoking article" is "prepared to be a tobacco yarn used in the cigarette rolling step".

萃取係可藉由將煙草絲1浸漬於15至100℃之水中0.5至2小時來進行。萃取時,相對於作為萃取溶劑之水2,煙草絲1可使用例如10質量%之量。 The extraction system can be carried out by immersing the tobacco yarn 1 in water at 15 to 100 ° C for 0.5 to 2 hours. In the extraction, the tobacco yarn 1 can be used in an amount of, for example, 10% by mass based on the water 2 as the extraction solvent.

萃取後,將煙草萃取液3從萃取殘渣4分離。分離係例如可將煙草萃取液3從萃取殘渣4使用可分離之篩網來進行。 After the extraction, the tobacco extract 3 is separated from the extraction residue 4. The separation system can, for example, carry out the tobacco extract 3 from the extraction residue 4 using a separable screen.

以獲得具有3.5以下pH的反應混合液6之 方式將所分離之煙草萃取液3與具有磺酸基之固體酸觸媒5a進行混合。在此,具有磺酸基之固體酸觸媒5a係指在固體表面上存在磺酸基,且磺酸基作用為觸媒活性點之觸媒。具有磺酸基之固體酸觸媒5a較佳為具有粒子之形態。作為磺酸基之固體酸觸媒5a,可使用例如TAYCACURE SAC-6(TAYCA股份有限公司,平均粒徑:200μm、比表面積:450m2/g)。具有磺酸基之固體酸觸媒5a係以可獲得具有3.5以下pH的反應混合液6之量,添加於煙草萃取液3。具有磺酸基之固體酸觸媒5a較佳為以可獲得具有1.0至3.5之pH的反應混合液6之量,添加於煙草萃取液3。具有磺酸基之固體酸觸媒5a更佳為以可獲得具有1.7至3.5的pH,又更佳為1.7至2.5之pH的反應混合液6之量,添加於煙草萃取液3。例如,相對於煙草萃取液3,具有磺酸基之固體酸觸媒5a可使用1至20質量%之量。如後述之實施例證實,若所調製之反應混合液6之pH超過3.5時,使用此反應混合液6所製造之煙草絲11係無法充分地達成副流煙之降低效果。 The separated tobacco extract 3 is mixed with a solid acid catalyst 5a having a sulfonic acid group in such a manner as to obtain a reaction mixture 6 having a pH of 3.5 or less. Here, the solid acid catalyst 5a having a sulfonic acid group means a catalyst having a sulfonic acid group present on a solid surface and having a sulfonic acid group acting as a catalytic active site. The solid acid catalyst 5a having a sulfonic acid group preferably has a form of particles. 5a as a solid acid catalyst of a sulfonic acid group, may be used, for example TAYCACURE SAC-6 (TAYCA Co., Ltd., average particle diameter: 200μm, specific surface area: 450m 2 / g). The solid acid catalyst 5a having a sulfonic acid group is added to the tobacco extract 3 in an amount to obtain a reaction mixture 6 having a pH of 3.5 or less. The solid acid catalyst 5a having a sulfonic acid group is preferably added to the tobacco extract 3 in an amount to obtain a reaction mixture 6 having a pH of 1.0 to 3.5. The solid acid catalyst 5a having a sulfonic acid group is more preferably added to the tobacco extract 3 in an amount to obtain a reaction mixture 6 having a pH of 1.7 to 3.5, more preferably 1.7 to 2.5. For example, the solid acid catalyst 5a having a sulfonic acid group can be used in an amount of from 1 to 20% by mass based on the tobacco extract 3. As will be described later, when the pH of the prepared reaction mixture 6 exceeds 3.5, the tobacco yarn 11 produced by using the reaction mixture 6 cannot sufficiently reduce the sidestream smoke.

此外,在本發明中,反應混合液6係調製成為具有3.5以下之pH,但反應後之反應混合液7未必需要具有3.5以下之pH。 Further, in the present invention, the reaction mixture 6 is prepared to have a pH of 3.5 or less, but the reaction mixture 7 after the reaction does not necessarily have to have a pH of 3.5 or less.

藉由將所調製之反應混合液6放置特定之時間,可使在反應混合液6中所含有之煙草成分的反應產生。反應可藉由將反應混合液6在15至40℃靜置0.5至4小時來進行,亦可將反應混合液6在15至40℃攪拌並且 放置0.5至4小時來進行。在此反應,為煙草絲所含有之成分的多糖類、胺基酸等被預測會藉由具有磺酸基之固體酸觸媒5a進行脫水縮合。 The reaction of the tobacco mixture contained in the reaction mixture 6 can be produced by allowing the prepared reaction mixture 6 to stand for a specific period of time. The reaction can be carried out by allowing the reaction mixture 6 to stand at 15 to 40 ° C for 0.5 to 4 hours, or the reaction mixture 6 can be stirred at 15 to 40 ° C and allowed to stand for 0.5 to 4 hours. In this reaction, a polysaccharide, an amino acid or the like which is a component contained in the tobacco yarn is predicted to be subjected to dehydration condensation by a solid acid catalyst 5a having a sulfonic acid group.

從反應後之反應混合液7去除固體酸觸媒5a,獲得反應後之煙草萃取液8。固體酸觸媒5a之去除可藉例如抽吸過濾來進行。 The solid acid catalyst 5a is removed from the reaction mixture 7 after the reaction, and the tobacco extract 8 after the reaction is obtained. Removal of the solid acid catalyst 5a can be carried out, for example, by suction filtration.

藉由濃縮所得之煙草萃取液8,而從煙草萃取液8去除水2。藉由濃縮而去除水2之步驟,可進行至反應後之煙草萃取液8的液量成為例如100分之1至4分之1之程度為止。此步驟,一般係從煙草萃取液8去除大量之水2,但並不能去除水2之全部量。 Water 2 is removed from tobacco extract 8 by concentrating the resulting tobacco extract 8. The step of removing the water 2 by concentration can be carried out until the liquid amount of the tobacco extract 8 after the reaction becomes, for example, 1 to 1/1 of a degree. This step generally removes a large amount of water 2 from the tobacco extract 8, but does not remove the entire amount of water 2.

將藉由濃縮而去除水2之煙草萃取液(處理液9)與在萃取步驟所得之萃取殘渣4進行混合。處理液9可與相對於處理液9為40至100質量%之量的萃取殘渣4混合。但,在此混合步驟中,處理液9之量較佳為不超過與萃取殘渣4同時從所得之煙草萃取液3中得到之處理液9的量。 The tobacco extract (treatment liquid 9) from which water 2 is removed by concentration is mixed with the extraction residue 4 obtained in the extraction step. The treatment liquid 9 can be mixed with the extraction residue 4 in an amount of 40 to 100% by mass with respect to the treatment liquid 9. However, in this mixing step, the amount of the treatment liquid 9 is preferably not more than the amount of the treatment liquid 9 obtained from the obtained tobacco extract 3 at the same time as the extraction residue 4.

使所得之混合物10乾燥,而製造吸煙物品調配用煙草絲11。乾燥係使煙草絲具有的水分含量成為與在該技術領域一般被使用於吸煙物品之煙草絲為同程度為止之方式進行。乾燥係一般進行至乾燥後之煙草絲11的水分含量成為6至14質量%為止。例如,乾燥係藉由在20至25℃之溫度及60至70%之濕度的條件下將混合物10靜置2日來進行。 The resulting mixture 10 is dried to produce a tobacco yarn 11 for smoking article formulation. The drying system is such that the moisture content of the tobacco yarn is the same as that of the tobacco yarn generally used in smoking articles in the technical field. The drying system is generally carried out until the moisture content of the tobacco yarn 11 after drying is 6 to 14% by mass. For example, drying is carried out by allowing the mixture 10 to stand for 2 days under the conditions of a temperature of 20 to 25 ° C and a humidity of 60 to 70%.

[第2實施形態]  [Second Embodiment]  

參照第2圖說明第2實施形態。第2實施形態之說明係記載與第1實施形態相異之點,省略與第1實施形態重複之點。 The second embodiment will be described with reference to Fig. 2 . The description of the second embodiment is different from that of the first embodiment, and the point of repetition of the first embodiment is omitted.

第2實施形態之方法係包含:以獲得具有3.5以下pH的反應混合液之方式,將含有煙草絲所含有之成分的煙草萃取液與硫酸進行混合,使前述煙草絲所含有之成分的反應產生。 The method according to the second embodiment includes mixing a tobacco extract containing a component contained in tobacco silk with sulfuric acid to obtain a reaction mixture having a pH of 3.5 or less, and reacting the components contained in the tobacco yarn. .

具體而言,第2實施形態之方法係包含:將煙草絲1所含有之成分以水2進行萃取,生成含有前述成分與前述水之煙草萃取液3、及含有前述成分經萃取後之前述煙草絲的萃取殘渣4之混合物;從前述萃取殘渣3分離前述煙草萃取液4;以可獲得具有3.5以下pH的反應混合液6之方式將被分離之前述煙草萃取液3、與硫酸5b進行混合,使前述成分之反應產生;藉由濃縮反應後之反應混合液7而從反應混合液7去除水2,獲得處理液9;將所得之處理液9與前述萃取殘渣4混合,獲得混合物10;使前述混合物10乾燥,而製造吸煙物品調配用煙草絲11。 Specifically, the method according to the second embodiment includes extracting a component contained in the tobacco yarn 1 with water 2 to produce a tobacco extract 3 containing the component and the water, and the tobacco after the extraction of the component. a mixture of silk extraction residue 4; separating the tobacco extract 4 from the extraction residue 3; mixing the separated tobacco extract 3 with sulfuric acid 5b in such a manner that a reaction mixture 6 having a pH of 3.5 or less is obtained. The reaction of the above components is produced; the water mixture 2 is removed from the reaction mixture 7 by concentrating the reaction mixture 7 after the reaction to obtain a treatment liquid 9; and the obtained treatment liquid 9 is mixed with the extraction residue 4 to obtain a mixture 10; The aforementioned mixture 10 is dried to produce a tobacco yarn 11 for smoking article formulation.

又,在此一連串步驟中,可更包含從反應後之反應混 合液7去除硫酸離子之步驟。硫酸離子之去除可以例如於反應後之反應混合液7中添加陰離子交換樹脂,使其充分反應,而去除硫酸離子來進行。 Further, in this series of steps, the step of removing sulfate ions from the reaction mixture 7 after the reaction may be further included. The removal of the sulfate ion can be carried out, for example, by adding an anion exchange resin to the reaction mixture 7 after the reaction to sufficiently react it and removing the sulfate ion.

第2實施形態中,首先根據與第1實施形態同樣之方法而獲得煙草萃取液3。 In the second embodiment, first, the tobacco extract 3 is obtained by the same method as in the first embodiment.

以獲得具有3.5以下之pH的反應混合液6之方式將所得之煙草萃取液3與硫酸5b進行混合。硫酸5b係以可獲得具有3.5以下pH的反應混合液6之量添加於煙草萃取液3。硫酸5b較佳為以可獲得具有1.0至3.5之pH的反應混合液6之量添加於煙草萃取液3。硫酸5b更佳為以可獲得具有1.7至3.5的pH,又更佳為1.7至2.5之pH的反應混合液6之量,添加於煙草萃取液3。被添加之硫酸5b例如可使用具有濃度為0.1至98質量%者。例如相對於煙草萃取液3,具有濃度為21質量%之硫酸5b可使用1至10質量%之量。如後述之實施例證實,若所調製之反應混合液6之pH超過3.5,使用此反應混合液6所製造之煙草絲11係無法充分地達成副流煙之降低效果。 The obtained tobacco extract 3 was mixed with sulfuric acid 5b in such a manner as to obtain a reaction mixture 6 having a pH of 3.5 or less. The sulfuric acid 5b is added to the tobacco extract 3 in an amount to obtain a reaction mixture 6 having a pH of 3.5 or less. The sulfuric acid 5b is preferably added to the tobacco extract 3 in an amount to obtain a reaction mixture 6 having a pH of 1.0 to 3.5. More preferably, the sulfuric acid 5b is added to the tobacco extract 3 in an amount to obtain a reaction mixture 6 having a pH of 1.7 to 3.5, more preferably 1.7 to 2.5. The sulfuric acid 5b to be added can be used, for example, in a concentration of from 0.1 to 98% by mass. For example, the sulfuric acid 5b having a concentration of 21% by mass can be used in an amount of from 1 to 10% by mass based on the tobacco extract 3. As will be described later, when the pH of the prepared reaction mixture 6 exceeds 3.5, the tobacco yarn 11 produced by using the reaction mixture 6 cannot sufficiently reduce the sidestream smoke.

藉由將所調製之反應混合液6放置特定之時間,可使在反應混合液6中所含有之煙草成分的反應產生。反應可藉由將反應混合液6在15至40℃靜置0.5至4小時來進行,亦可將反應混合液6在15至40℃攪拌並且放置0.5至4小時來進行。在此反應,為煙草絲所含有之成分的多糖類、胺基酸等被預測會藉由硫酸5b進行脫水縮合。 The reaction of the tobacco mixture contained in the reaction mixture 6 can be produced by allowing the prepared reaction mixture 6 to stand for a specific period of time. The reaction can be carried out by allowing the reaction mixture 6 to stand at 15 to 40 ° C for 0.5 to 4 hours, or the reaction mixture 6 can be stirred at 15 to 40 ° C and allowed to stand for 0.5 to 4 hours. In this reaction, a polysaccharide, an amino acid or the like which is a component contained in the tobacco yarn is predicted to be subjected to dehydration condensation by sulfuric acid 5b.

藉由濃縮反應後之反應混合液7,而從反應混合液7去除水2。藉由濃縮去除水2之步驟,可進行至反應後之反應混合液7的液量成為例如100分之1至4分之1為止之程度。此步驟,一般係從反應混合液7去除大量之水2,但並不能去除水2之全部量。 Water 2 is removed from the reaction mixture 7 by concentrating the reaction mixture 7 after the reaction. By the step of concentrating and removing the water 2, the amount of the liquid of the reaction mixture 7 after the reaction can be, for example, 1 to 1/1 of the range. This step generally removes a large amount of water 2 from the reaction mixture 7, but does not remove the entire amount of water 2.

將藉由濃縮而去除水2之反應混合液(處理液9)與在萃取步驟所得之萃取殘渣4進行混合。處理液9可與相對於處理液9為40至100質量%之量的萃取殘渣4混合。但,在此混合步驟中,處理液9之量較佳為不超過與萃取殘渣4同時從所得之煙草萃取液3中得到之處理液9的量。 The reaction mixture (treatment liquid 9) from which water 2 was removed by concentration was mixed with the extraction residue 4 obtained in the extraction step. The treatment liquid 9 can be mixed with the extraction residue 4 in an amount of 40 to 100% by mass with respect to the treatment liquid 9. However, in this mixing step, the amount of the treatment liquid 9 is preferably not more than the amount of the treatment liquid 9 obtained from the obtained tobacco extract 3 at the same time as the extraction residue 4.

根據與第1實施形態同樣之方法史所得之混合物10乾燥,而製造吸煙物品調配用煙草絲11。 The mixture 10 obtained by the same method as in the first embodiment is dried to produce a tobacco yarn 11 for smoking article preparation.

[第3實施形態]  [Third embodiment]  

參照第3圖說明第3實施形態。第3實施形態之說明係記載與第1及第2實施形態相異之點,省略與第1及第2實施形態重複之點。 The third embodiment will be described with reference to Fig. 3 . The description of the third embodiment is different from the first and second embodiments, and the points overlapping with the first and second embodiments are omitted.

第3實施形態之方法係包含:以可獲得具有3.5以下pH的反應混合液之方式,將煙草絲、與具有磺酸基之固體酸觸媒進行混合,使前述煙草絲所含有之成分的反應產生。 The method according to the third embodiment includes mixing a tobacco yarn with a solid acid catalyst having a sulfonic acid group so as to obtain a reaction mixture having a pH of 3.5 or less, and reacting the components contained in the tobacco yarn. produce.

具體而言,第3實施形態之方法係包含:以可獲得具有3.5以下pH的反應混合液6之方式,將 煙草絲1、與具有磺酸基之固體酸觸媒5a及水5c進行混合,而使前述煙草絲1所含有之成分的反應產生;從反應後之反應混合液7去除前述固體酸觸媒5a及水5c,獲得反應後之煙草絲8b;使所得之煙草絲8b乾燥,而製造吸煙物品調配用煙草絲11。 Specifically, the method according to the third embodiment includes mixing the tobacco yarn 1 with the solid acid catalyst 5a having a sulfonic acid group and water 5c so that the reaction mixture 6 having a pH of 3.5 or less can be obtained. The reaction of the components contained in the tobacco yarn 1 is generated; the solid acid catalyst 5a and the water 5c are removed from the reaction mixture 7 after the reaction to obtain the tobacco yarn 8b after the reaction; and the obtained tobacco yarn 8b is dried. Tobacco wire 11 for the manufacture of smoking articles.

在第3實施形態所使用之「煙草絲」係與第1實施形態同樣,可使用整備為調配在吸煙物品之煙草絲。 In the same manner as in the first embodiment, the "tobacco yarn" used in the third embodiment can be used as a tobacco yarn to be blended in a smoking article.

在第3實施形態,首先以獲得具有3.5以下pH的反應混合液6之方式將煙草絲1、與具有磺酸基之固體酸觸媒5a及水5c進行混合。具有磺酸基之固體酸觸媒5a可使用在第1實施形態說明者。具有磺酸基之固體酸觸媒5a及水5c以可獲得具有3.5以下pH的反應混合液6之量,與煙草絲1混合。具有磺酸基之固體酸觸媒5a及水5c較佳為以可獲得具有1.0至3.5之pH的反應混合液6之量與煙草絲1混合。具有磺酸基之固體酸觸媒5a及水5c更佳為以可獲得具有1.7至3.5之pH,又更佳為1.7至2.5的pH之反應混合液6之量與煙草絲1混合。例如,相對於煙草絲1,具有磺酸基之固體酸觸媒5a可使用1至20質量%之量。如後述之實施例證實,若所調製之反應混合液6之pH超過3.5,使用此反應混合液6所製造之煙草絲11係無法充分地達成副流煙之降低效果。 In the third embodiment, first, the tobacco yarn 1 is mixed with a solid acid catalyst 5a having a sulfonic acid group and water 5c so as to obtain a reaction mixture liquid 6 having a pH of 3.5 or less. The solid acid catalyst 5a having a sulfonic acid group can be used in the first embodiment. The solid acid catalyst 5a having a sulfonic acid group and water 5c are mixed with the tobacco yarn 1 in an amount to obtain a reaction mixture 6 having a pH of 3.5 or less. The solid acid catalyst 5a having a sulfonic acid group and water 5c are preferably mixed with the tobacco yarn 1 in an amount to obtain a reaction mixture 6 having a pH of 1.0 to 3.5. The solid acid catalyst 5a having a sulfonic acid group and water 5c are more preferably mixed with the tobacco yarn 1 in an amount to obtain a reaction mixture 6 having a pH of 1.7 to 3.5, more preferably 1.7 to 2.5. For example, the solid acid catalyst 5a having a sulfonic acid group can be used in an amount of from 1 to 20% by mass based on the tobacco yarn 1. As will be described later, when the pH of the prepared reaction mixture 6 exceeds 3.5, the tobacco yarn 11 produced by using the reaction mixture 6 cannot sufficiently reduce the sidestream smoke.

藉由將所調製之反應混合液6放置特定之時間,可使煙草絲1含有之煙草成分的反應產生。反應可 藉由將反應混合液6在15至40℃靜置0.5至4小時來進行,亦可將反應混合液6在15至40℃攪拌並且放置0.5至4小時來進行。在此反應,為煙草絲含有之成分的多糖類、胺基酸等被預測會藉由具有磺酸基之固體酸觸媒5a進行脫水縮合。 The reaction of the tobacco mixture contained in the tobacco yarn 1 can be produced by placing the prepared reaction mixture 6 for a specific period of time. The reaction can be carried out by allowing the reaction mixture 6 to stand at 15 to 40 ° C for 0.5 to 4 hours, or the reaction mixture 6 can be stirred at 15 to 40 ° C and allowed to stand for 0.5 to 4 hours. In this reaction, a polysaccharide, an amino acid or the like which is a component contained in the tobacco yarn is predicted to be subjected to dehydration condensation by a solid acid catalyst 5a having a sulfonic acid group.

從反應後之反應混合液7去除固體酸觸媒5a及水5c,獲得反應後之煙草絲8b。固體酸觸媒5a及水5c之去除係例如可將反應後之煙草絲8b從固體酸觸媒5a及水5c使用可分離之篩網來進行。此處所去除之水5c係可包含煙草絲1含有之成分。 The solid acid catalyst 5a and the water 5c are removed from the reaction mixture 7 after the reaction to obtain the tobacco yarn 8b after the reaction. The removal of the solid acid catalyst 5a and the water 5c can be carried out, for example, by using the separable screen from the solid acid catalyst 5a and the water 5c after the reaction. The water 5c removed here may contain the components contained in the tobacco yarn 1.

根據與第1實施形態同樣之方法使所得之煙草絲8b乾燥,而製造吸煙物品調配用煙草絲11。 The obtained tobacco yarn 8b is dried in the same manner as in the first embodiment to produce a tobacco yarn 11 for smoking article preparation.

[第4實施形態]  [Fourth embodiment]  

參照第4圖說明第4實施形態。第4實施形態之說明係記載與第1至第3實施形態相異之點,省略與第1至第3實施形態重複之點。 The fourth embodiment will be described with reference to Fig. 4 . The description of the fourth embodiment is different from the first to third embodiments, and the points overlapping with the first to third embodiments are omitted.

第4實施形態之方法係包含:以可獲得具有3.5以下pH的反應混合液之方式,將煙草絲、與硫酸進行混合,而使前述煙草絲含有之成分的反應產生。 The method according to the fourth embodiment includes a method of mixing a tobacco yarn with sulfuric acid so as to obtain a reaction mixture having a pH of 3.5 or less, and generating a reaction of a component contained in the tobacco yarn.

具體而言,第4實施形態之方法係包含:以可獲得具有3.5以下pH的反應混合液6之方式,將煙草絲1、與硫酸5b進行混合,使前述煙草絲1含有之成 分的反應產生;將反應後之反應混合液7與反應後之煙草絲8b及硫酸5b分離;使所得之煙草絲8b乾燥,而製造吸煙物品調配用煙草絲11。 Specifically, in the method of the fourth embodiment, the tobacco yarn 1 and the sulfuric acid 5b are mixed so that the reaction mixture 6 having a pH of 3.5 or less is obtained, and the reaction of the component contained in the tobacco yarn 1 is produced. The reaction mixture 7 after the reaction is separated from the tobacco silk 8b and the sulfuric acid 5b after the reaction; the obtained tobacco yarn 8b is dried to prepare a tobacco yarn 11 for smoking article preparation.

又,在此一連串之步驟中,可更含有從反應後之反應混合液7去除硫酸離子之步驟。 Further, in this series of steps, the step of removing sulfate ions from the reaction mixture 7 after the reaction may be further included.

在第4實施形態,首先以獲得具有3.5以下pH的反應混合液6之方式將煙草絲1、與硫酸5b進行混合。硫酸5b係可使用例如具有濃度為0.1至98質量%者。硫酸5b以可獲得具有3.5以下pH的反應混合液6之量,與煙草絲1混合。硫酸5b較佳為以可獲得具有1.0至3.5之pH的反應混合液6之量,與煙草絲1混合。硫酸5b更佳為以可獲得具有1.7至3.5之pH,又更佳為1.7至2.5的pH之反應混合液6之量,與煙草絲1混合。例如,相對於煙草絲1,具有濃度為0.1至98質量%之硫酸5b可使用1至20質量%之量。如後述之實施例證實,若所調製之反應混合液6之pH超過3.5,使用此反應混合液6所製造之煙草絲11係無法充分地達成副流煙之降低效果。 In the fourth embodiment, first, the tobacco yarn 1 and the sulfuric acid 5b are mixed so as to obtain the reaction mixture 6 having a pH of 3.5 or less. The sulfuric acid 5b system can be used, for example, having a concentration of 0.1 to 98% by mass. The sulfuric acid 5b is mixed with the tobacco yarn 1 in an amount to obtain a reaction mixture 6 having a pH of 3.5 or less. The sulfuric acid 5b is preferably mixed with the tobacco yarn 1 in an amount to obtain a reaction mixture 6 having a pH of 1.0 to 3.5. More preferably, the sulfuric acid 5b is mixed with the tobacco yarn 1 in an amount to obtain a reaction mixture 6 having a pH of from 1.7 to 3.5, more preferably from 1.7 to 2.5. For example, with respect to the tobacco yarn 1, the sulfuric acid 5b having a concentration of 0.1 to 98% by mass may be used in an amount of 1 to 20% by mass. As will be described later, when the pH of the prepared reaction mixture 6 exceeds 3.5, the tobacco yarn 11 produced by using the reaction mixture 6 cannot sufficiently reduce the sidestream smoke.

藉由將所調製之反應混合液6放置特定之時間,可使煙草絲1含有之煙草成分的反應產生。反應可藉由將反應混合液6在15至40℃靜置0.5至4小時來進行,亦可將反應混合液6在15至40℃攪拌並且放置0.5至4小時來進行。吾人係預測,在此反應中,煙草絲含有 之成分的多糖類、胺基酸等會藉由硫酸5b進行脫水縮合。 The reaction of the tobacco mixture contained in the tobacco yarn 1 can be produced by placing the prepared reaction mixture 6 for a specific period of time. The reaction can be carried out by allowing the reaction mixture 6 to stand at 15 to 40 ° C for 0.5 to 4 hours, or the reaction mixture 6 can be stirred at 15 to 40 ° C and allowed to stand for 0.5 to 4 hours. It is predicted that in this reaction, the polysaccharide, the amino acid or the like of the component containing the tobacco filament is dehydrated and condensed by the sulfuric acid 5b.

將反應後之反應混合液7分離成反應後之煙草絲8b(固體部分)及硫酸5b(液體部分)。該分離例如將反應後之煙草絲8b(固體部分)從硫酸5b(液體部分)使用可分離之篩網來進行。 The reaction mixture 7 after the reaction was separated into a tobacco silk 8b (solid portion) and a sulfuric acid 5b (liquid portion) after the reaction. This separation is carried out, for example, by using the tobacco wire 8b (solid portion) after the reaction from the sulfuric acid 5b (liquid portion) using a separable sieve.

在該分離之前,亦可從反應後之反應混合液7去除硫酸離子。硫酸離子之去除係例如於反應後之反應混合液7中加入陰離子交換樹脂,使其充分反應,再去除硫酸離子。在此所去除之硫酸離子係可包含煙草絲1含有之成分。 Sulfate ions may also be removed from the reaction mixture 7 after the reaction before the separation. The removal of the sulfate ion is carried out, for example, by adding an anion exchange resin to the reaction mixture 7 after the reaction to sufficiently react the sulfate ion. The sulfate ion removed here may contain a component contained in the tobacco yarn 1.

根據與第1實施形態同樣之方法使所得之煙草絲8b乾燥,而製造吸煙物品調配用煙草絲11。 The obtained tobacco yarn 8b is dried in the same manner as in the first embodiment to produce a tobacco yarn 11 for smoking article preparation.

2.吸煙物品調配用煙草絲  2. Tobacco wire for smoking articles  

一般而言,本發明之吸煙物品調配用煙草絲,其特徵為煙草絲中之含碳比例未達0.50,且藉由在氮環境下、500℃中加熱煙草絲10分鐘,其後冷卻,並且以22℃維持0.5小時而得之碳化物中含碳比例(以下,亦稱為「碳化物中之含碳比例」)為0.50以上。 In general, the tobacco yarn for smoking articles of the present invention is characterized in that the carbon content in the tobacco yarn is less than 0.50, and the tobacco yarn is heated for 10 minutes in a nitrogen atmosphere at 500 ° C, and then cooled, and The proportion of carbon contained in the carbide (hereinafter also referred to as "the proportion of carbon in the carbide") obtained by maintaining at 22 ° C for 0.5 hour is 0.50 or more.

在較佳之態樣中,本發明之吸煙物品調配用煙草絲,其特徵為「煙草絲中之含碳比例」為0.30以上、未達0.50,且「碳化物中之含碳比例」為0.50以上、未達0.58。 In a preferred aspect, the tobacco yarn for blending smoking articles of the present invention is characterized in that the "carbon content in the tobacco yarn" is 0.30 or more, less than 0.50, and the "carbon content in the carbide" is 0.50 or more. It did not reach 0.58.

另一方面,通常之煙草絲一般而言其特徵 為煙草絲中含碳比例為0.30以上、未達0.50,且藉由在氮環境下500℃中加熱煙草絲10分鐘,其後冷卻,並且以22℃維持0.5小時而得之碳化物中之含碳比例(「碳化物中含碳比例」)為0.40以上、未達0.50。在本說明書中,「通常之煙草絲」係指作為本發明方法的起始材料所使用之煙草絲,亦即未以本發明方法處理之煙草絲。 On the other hand, the usual tobacco yarn is generally characterized in that the tobacco yarn has a carbon content of 0.30 or more and less than 0.50, and the tobacco yarn is heated for 10 minutes at 500 ° C in a nitrogen atmosphere, followed by cooling, and The carbon content ("carbon content in the carbide") of the carbide obtained at 22 ° C for 0.5 hours was 0.40 or more and less than 0.50. In the present specification, "normal tobacco yarn" means a tobacco yarn used as a starting material for the method of the present invention, that is, tobacco yarn which is not treated by the method of the present invention.

因此,一般而言,本發明之吸煙物品調配用煙草絲其特徵係具有與通常之煙草絲為相同程度之「煙草絲中含碳比例」,且具有較從通常之煙草絲所得之碳化物更高的「碳化物中含碳比例」。 Therefore, in general, the tobacco yarn for smoking article formulation of the present invention is characterized by having the same degree of "carbon content in tobacco silk" as the usual tobacco yarn, and having more carbides than those obtained from ordinary tobacco yarn. High "carbon content in carbides".

「含碳比例」被認為是不易燃燒程度之指標。又,用以得到碳化物所使用之500℃的加熱溫度係與自然燃燒時香煙之燃燒溫度幾乎相同程度之溫度。因此,「碳化物中含碳比例」較高表示煙草絲在自然燃燒時不易燃燒。 The "carbon content ratio" is considered to be an indicator of the degree of non-flammability. Further, the heating temperature at 500 ° C used for obtaining the carbide is almost the same as the combustion temperature of the cigarette at the time of natural combustion. Therefore, a higher "carbon content in the carbide" means that the tobacco filament is not easily burned when it is naturally burned.

從以上可知,煙草絲中含碳比例未達0.50且碳化物中含碳比例為0.50以上之特徴,意指煙草絲自然燃燒時不易燃燒,並且由吸煙物品所生成之副流煙的量少。 As can be seen from the above, the tobacco fiber has a carbon content of less than 0.50 and a carbon content of the carbide of 0.50 or more, which means that the tobacco yarn is not easily burned when it is naturally burned, and the amount of sidestream smoke generated by the smoking article is small.

「煙草絲中含碳比例」及「碳化物中含碳比例」可使用元素分析裝置測定。例如,可使用元素分析裝置SUMIGRAPH NCH-22F(住化分析中心股份有限公司製)進行測定。 The "carbon content in tobacco silk" and "carbon content in carbide" can be measured using an elemental analyzer. For example, the measurement can be carried out using an elemental analysis device SUMIGRAPH NCH-22F (manufactured by Sumitomo Chemical Co., Ltd.).

「含碳比例」具體而言可如下述般進行測定。將煙草絲或碳化物在調和環境下(22℃、60%相對濕度) 藏置24小時以上,秤量0.01g之煙草絲或碳化物,在氧化環境下加熱至800℃,以元素分析裝置分析所得之燃燒生成物並且求出元素組成。使用結晶纖維素作為碳與氫之參考組。藉由使用參考組,可直接測定燃燒生成物之碳比例。 The "carbon content ratio" can be specifically measured as follows. The tobacco silk or carbide was stored in a blending environment (22 ° C, 60% relative humidity) for more than 24 hours, weighed 0.01 g of tobacco silk or carbide, heated to 800 ° C in an oxidizing environment, and analyzed by an elemental analysis device. The product is burned and the elemental composition is determined. Crystalline cellulose was used as a reference group for carbon and hydrogen. By using the reference group, the carbon ratio of the combustion product can be directly determined.

3.吸煙物品  3. Smoking items  

本發明之吸煙物品調配用煙草絲係可使用於任意之吸煙物品,一般為燃燒型之吸煙物品,例如香煙、煙斗、煙袋、捲葉、雪茄等。 The tobacco yarn for smoking article formulation of the present invention can be used for any smoking article, generally a smoking type smoking article such as a cigarette, a pipe, a cigarette bag, a rolled leaf, a cigar or the like.

調配比例係無限定,惟本發明之吸煙物品調配用煙草絲可以佔吸煙物品所含之全煙草絲(以下,亦稱為煙草填充材料)之全體(100質量%)之方式調配,亦可以佔煙草填充材料之一部分例如煙草填充材料之50至75質量%之方式調配。 The blending ratio is not limited, but the tobacco yarn for the distribution of the smoking articles of the present invention may be formulated in such a manner that the total amount of tobacco (hereinafter referred to as tobacco filler) contained in the smoking article is 100% by mass. One portion of the tobacco filling material is formulated in a manner such as 50 to 75% by mass of the tobacco filling material.

前者之情形,煙草填充材料在自然燃燒時極難以燃燒,可顯著地降低副流煙明顯。但,此情形,煙草填充材料亦難以於吸煙燃燒時燃燒,其結果,吸煙次數有較通常之煙草絲多少增加之可能性。另一方面,後者之情形,由於本發明之吸煙物品調配用煙草絲與通常之煙草絲混合,故可一併具有煙草填充材料自然燃燒時難以燃燒,並且降低副流煙之效果,以及保證可與通常之煙草絲在吸煙燃燒時具有同樣的燃燒效果。 In the former case, the tobacco filling material is extremely difficult to burn when naturally burned, and the sidestream smoke is remarkably reduced. However, in this case, the tobacco filling material is also difficult to burn when the smoking is burned, and as a result, the number of times of smoking is increased more than the usual amount of tobacco. On the other hand, in the latter case, since the tobacco yarn for smoking articles of the present invention is mixed with the usual tobacco yarn, it is possible to have the tobacco filler material hard to burn when it is naturally burned, and to reduce the effect of the sidestream smoke, and to ensure that it can be It has the same burning effect as a normal tobacco filament when it is burned.

從以上可知,本發明之吸煙物品可發揮不使吸煙次數減少,且可降低從吸煙物品所生成之副流煙的 效果。 As apparent from the above, the smoking article of the present invention can exhibit an effect of not reducing the number of times of smoking and reducing the sidestream smoke generated from the smoking article.

4.較佳之實施形態  4. Preferred embodiment  

如上述,第1實施形態之方法係包含:以可獲得具有3.5以下之pH的反應混合液之方式將含有煙草絲含有之成分的煙草萃取液、及具有磺酸基之固體酸觸媒進行混合,使前述煙草絲含有之成分的反應產生。 As described above, the method according to the first embodiment includes mixing a tobacco extract containing a tobacco silk-containing component and a solid acid catalyst having a sulfonic acid group so that a reaction mixture having a pH of 3.5 or less can be obtained. The reaction of the components contained in the tobacco yarn described above is produced.

具體而言,第1實施形態之方法係包含:將煙草絲1含有之成分以水2進行萃取,生成含有前述成分與前述水之煙草萃取液3、及含有前述成分經萃取後之前述煙草絲的萃取殘渣4之混合物;從前述萃取殘渣4分離前述煙草萃取液3;以可獲得具有3.5以下pH的反應混合液6之方式將經分離之前述煙草萃取液3、與具有磺酸基之固體酸觸媒5a進行混合,使前述成分之反應產生;從反應後之反應混合液7去除前述固體酸觸媒5a,獲得反應後之煙草萃取液8;藉由濃縮所得之煙草萃取液8,而從煙草萃取液8去除水2,獲得處理液9;將所得之處理液9與前述萃取殘渣4混合,獲得混合物10;使前述混合物10乾燥,而製造吸煙物品調配用煙草絲11。 Specifically, the method according to the first embodiment includes extracting a component contained in the tobacco yarn 1 with water 2, and producing a tobacco extract 3 containing the component and the water, and the tobacco yarn containing the component after extraction. a mixture of the extraction residue 4; separating the tobacco extract 3 from the extraction residue 4; and separating the tobacco extract 3 and the solid having a sulfonic acid group in such a manner that a reaction mixture 6 having a pH of 3.5 or less can be obtained. The acid catalyst 5a is mixed to produce a reaction of the above components; the solid acid catalyst 5a is removed from the reaction mixture 7 after the reaction to obtain the tobacco extract 8 after the reaction; and the obtained tobacco extract 8 is concentrated by using Water 2 is removed from the tobacco extract 8 to obtain a treatment liquid 9; the obtained treatment liquid 9 is mixed with the above-mentioned extraction residue 4 to obtain a mixture 10; and the above mixture 10 is dried to produce a tobacco yarn 11 for smoking article preparation.

又,如上述,第2實施形態之方法係包含: 以可獲得具有3.5以下pH的反應混合液之方式,將含有煙草絲含有之成分的煙草萃取液及硫酸進行混合,使前述煙草絲含有之成分的反應產生。 Further, as described above, the method according to the second embodiment includes: mixing a tobacco extract containing a component containing tobacco silk and sulfuric acid so as to obtain a reaction mixture having a pH of 3.5 or less, and mixing the tobacco yarn The reaction of the ingredients is produced.

具體而言,第2實施形態之方法係包含:將煙草絲1含有之成分以水2進行萃取,生成含有前述成分與前述水之煙草萃取液3、及含有前述成分經萃取後之前述煙草絲的萃取殘渣4之混合物;從前述萃取殘渣3分離前述煙草萃取液4;以可獲得具有3.5以下pH的反應混合液6之方式將經分離之前述煙草萃取液3、與硫酸5b進行混合,使前述成分之反應產生;藉由濃縮反應後之反應混合液7而從反應混合液7去除水2,獲得處理液9;將所得之處理液9與前述萃取殘渣4混合,獲得混合物10;使前述混合物10乾燥,製造吸煙物品調配用煙草絲11。 Specifically, the method according to the second embodiment includes extracting the component contained in the tobacco yarn 1 with water 2, and producing the tobacco extract 3 containing the component and the water, and the tobacco yarn containing the component after extraction. a mixture of the extraction residue 4; separating the tobacco extract 4 from the extraction residue 3; mixing the separated tobacco extract 3 with sulfuric acid 5b so as to obtain a reaction mixture 6 having a pH of 3.5 or less. The reaction of the above components is produced; the water mixture 2 is removed from the reaction mixture 7 by concentrating the reaction mixture 7 after the reaction to obtain a treatment liquid 9; and the obtained treatment liquid 9 is mixed with the extraction residue 4 to obtain a mixture 10; The mixture 10 is dried to produce a tobacco yarn 11 for smoking article preparation.

又,如上述,第3實施形態之方法係包含:以可獲得具有3.5以下pH的反應混合液之方式,將煙草絲、與具有磺酸基之固體酸觸媒進行混合,使前述煙草絲含有之成分的反應產生。 Further, as described above, the method according to the third embodiment includes mixing the tobacco yarn with a solid acid catalyst having a sulfonic acid group so as to obtain a reaction mixture having a pH of 3.5 or less, and the tobacco yarn is contained. The reaction of the components is produced.

具體而言,第3實施形態之方法係包含:以可獲得具有3.5以下pH的反應混合液6之方式,將煙草絲1、與具有磺酸基之固體酸觸媒5a及水5c進行混 合,使前述煙草絲1含有之成分的反應產生;從反應後之反應混合液7去除前述固體酸觸媒5a及水5c,獲得反應後之煙草絲8b;使所得之煙草絲8b乾燥,製造吸煙物品調配用煙草絲11。 Specifically, the method according to the third embodiment includes mixing the tobacco yarn 1 with the solid acid catalyst 5a having a sulfonic acid group and water 5c so that the reaction mixture 6 having a pH of 3.5 or less can be obtained. The reaction of the components contained in the tobacco yarn 1 is generated; the solid acid catalyst 5a and the water 5c are removed from the reaction mixture 7 after the reaction to obtain the tobacco yarn 8b after the reaction; and the obtained tobacco yarn 8b is dried to produce a smoking article. The tobacco yarn 11 is blended.

又,如上述,第4實施形態之方法係包含:以可獲得具有3.5以下pH的反應混合液之方式,將煙草絲、與硫酸進行混合,使前述煙草絲含有之成分的反應產生。 Further, as described above, the method according to the fourth embodiment includes mixing the tobacco yarn with sulfuric acid so as to obtain a reaction mixture having a pH of 3.5 or less, and generating a reaction of the components contained in the tobacco yarn.

具體而言,第4實施形態之方法係包含:以可獲得具有3.5以下pH的反應混合液6之方式,將煙草絲1、與硫酸5b進行混合,使前述煙草絲1含有之成分的反應產生;從反應後之反應混合液7分離反應後之煙草絲8b及硫酸5b;使所得之煙草絲8b乾燥,製造吸煙物品調配用煙草絲11。 Specifically, in the method of the fourth embodiment, the tobacco yarn 1 and the sulfuric acid 5b are mixed so that the reaction mixture 6 having a pH of 3.5 or less is obtained, and the reaction of the component contained in the tobacco yarn 1 is produced. The reacted tobacco mixture 8b and the sulfuric acid 5b are separated from the reaction mixture 7 after the reaction; the obtained tobacco yarn 8b is dried to prepare a tobacco yarn 11 for smoking article preparation.

若依據較佳之實施形態,上述第1至第4實施形態中之任一者,前述反應混合液具有1.0至3.5之pH,較佳為具有1.7至3.5之pH,更佳為具有1.7至2.5之pH。 According to a preferred embodiment, in any one of the first to fourth embodiments, the reaction mixture has a pH of 1.0 to 3.5, preferably a pH of 1.7 to 3.5, more preferably 1.7 to 2.5. pH.

若依據其他較佳之實施形態,上述第1至第4實施形態及上述較佳之實施形態中之任一者,使煙草絲含有之成分的反應產生之前述步驟,係藉由將前述反應混 合液在15至40℃放置0.5至4小時來進行。 According to another preferred embodiment, in any one of the first to fourth embodiments and the preferred embodiment described above, the step of reacting the components contained in the tobacco yarn is carried out by subjecting the reaction mixture to It is allowed to stand at 15 to 40 ° C for 0.5 to 4 hours.

若依據其他較佳之實施形態,上述第1及第3實施形態及上述較佳之實施形態中之任一者,前述固體酸觸媒係於載體粒子之表面具有磺酸基之粒子。 According to another preferred embodiment, in any one of the first and third embodiments and the preferred embodiment, the solid acid catalyst is a particle having a sulfonic acid group on the surface of the carrier particle.

若依據其他較佳之實施形態,上述第1至第4實施形態及上述較佳之實施形態中之任一者,使煙草絲乾燥之前述步驟,係進行至使乾燥後之前述煙草絲之水分含量成為6至14質量%為止。 According to another preferred embodiment, in any one of the first to fourth embodiments and the preferred embodiment described above, the step of drying the tobacco yarn is performed until the moisture content of the tobacco yarn after drying is changed 6 to 14% by mass.

若依據其他較佳之實施形態,上述第1至第4實施形態及上述較佳之實施形態中之任一者,前述煙草絲係經整備為調配於吸煙物品之煙草絲,具體而言,係經過包含:在農家之乾燥步驟、其後在原料工廠之1年乃至數年之長期熟成步驟、及其後在製造工廠之摻混及裁刻之加工處理步驟,而經整備為調配於吸煙物品之煙草絲。 According to another preferred embodiment, in any one of the first to fourth embodiments and the preferred embodiment, the tobacco yarn is prepared as a tobacco yarn blended in a smoking article, specifically, including : Tobacco formulated in smoking articles in the drying step of the farmhouse, the long-term ripening step in the raw material factory for one year or even years, and the subsequent processing steps of blending and cutting in the manufacturing plant. wire.

若依據其他較佳之實施形態,上述第1及第2實施形態及上述較佳之實施形態中之任一者,以水萃取於煙草絲含有之成分的前述步驟,係藉由將前述煙草絲於15至100℃之水中浸漬0.5至2小時來進行。 According to another preferred embodiment, in any one of the first and second embodiments and the preferred embodiment described above, the step of extracting the component contained in the tobacco yarn with water is performed by using the tobacco yarn as described above. It is immersed in water of 100 ° C for 0.5 to 2 hours.

若依據其他較佳之實施形態,上述第2及第4實施形態及上述較佳之實施形態中之任一者,前述方法更包含從反應後之前述反應混合液去除硫酸離子之步驟。 According to another preferred embodiment, in any one of the second and fourth embodiments and the preferred embodiment, the method further comprises the step of removing sulfate ions from the reaction mixture after the reaction.

[實施例]  [Examples]   [1]香煙調配用煙草絲之調製  [1] Modulation of Tobacco Filament for Cigarette Blending   實施例1-1  Example 1-1  

將含水比例經調整為12質量%之煙草絲(3R4F參考香煙)25g浸漬於250mL之熱水(60℃)中2小時,萃取煙草絲含有之成分(煙草成分)。其後,使用篩目0.15mm之篩網,分成過篩之煙草萃取液及殘留於篩網上之萃取殘渣。 25 g of tobacco silk (3R4F reference cigarette) having a water content adjusted to 12% by mass was immersed in 250 mL of hot water (60 ° C) for 2 hours to extract a component (tobacco component) contained in the tobacco yarn. Thereafter, a sieve having a mesh size of 0.15 mm was used, and the sieved tobacco extract and the residue remaining on the sieve were separated.

於所得之煙草萃取液250mL中添加具有磺酸基之固體酸觸媒(TAYCACURE SAC-6、TAYCA股份有限公司製)40g,獲得pH1.7之反應混合液。使用桌上型pH計F-72(HORIBA製)作為pH測定器。將所得之反應混合液在22℃靜置4小時,產生煙草成分之反應。將反應後之反應混合液使用濾紙(Advantech 4號)藉由抽氣機抽吸過濾,從反應混合液去除固體酸觸媒。 40 g of a solid acid catalyst (TAYCACURE SAC-6, manufactured by TAYCA Co., Ltd.) having a sulfonic acid group was added to 250 mL of the obtained tobacco extract to obtain a reaction mixture of pH 1.7. A tabletop pH meter F-72 (manufactured by HORIBA) was used as a pH meter. The resulting reaction mixture was allowed to stand at 22 ° C for 4 hours to produce a reaction of the tobacco component. The reaction mixture after the reaction was filtered by suction with a filter paper (Advantech No. 4) to remove a solid acid catalyst from the reaction mixture.

使用蒸發器將所得之液體(反應後之煙草萃取液)濃縮至液體之總量成為12.5g左右,以去除萃取溶劑(水)。將所得之處理液12.5g添加於萃取殘渣12.5g中。將所得之混合物在溫度22℃/相對濕度60%之室內乾燥2日,調整煙草絲之水分含有比例成為12質量%。藉此,調成香煙調配用煙草絲。 The obtained liquid (the tobacco extract after the reaction) was concentrated to a total amount of about 12.5 g using an evaporator to remove the extraction solvent (water). 12.5 g of the obtained treatment liquid was added to 12.5 g of the extraction residue. The obtained mixture was dried in a room at a temperature of 22 ° C / a relative humidity of 60% for 2 days, and the moisture content ratio of the tobacco yarn was adjusted to 12% by mass. Thereby, the tobacco yarn for cigarette preparation is adjusted.

實施例1-2  Example 1-2  

依據與實施例1-1同樣之方法調製煙草絲。所調製之煙草絲及3R4F參考香煙之煙草絲分別以75質量%及25質量%之比例進行混合,成為香煙調配用煙草絲。 The tobacco yarn was prepared in the same manner as in Example 1-1. The tobacco silk of the prepared tobacco silk and the 3R4F reference cigarette were mixed at a ratio of 75 mass% and 25 mass%, respectively, and became tobacco yarn for cigarette blending.

實施例1-3  Examples 1-3  

依據與實施例1-1同樣之方法調製煙草絲。所調製之煙草絲及3R4F參考香煙之煙草絲分別以50質量%及50質量%之比例進行混合,成為香煙調配用煙草絲。 The tobacco yarn was prepared in the same manner as in Example 1-1. The tobacco silk of the prepared tobacco yarn and the 3R4F reference cigarette were mixed at a ratio of 50% by mass and 50% by mass, respectively, to form a tobacco yarn for cigarette blending.

實施例1-4  Examples 1-4  

除了於煙草萃取液250mL中添加具有磺酸基之固體酸觸媒13g,製得pH3.4之反應混合液以外,其餘係依據與實施例1-1同樣之方法而調製香煙調配用煙草絲。 Tobacco yarn for cigarette preparation was prepared in the same manner as in Example 1-1, except that 13 g of a solid acid catalyst having a sulfonic acid group was added to 250 mL of the tobacco extract to prepare a reaction mixture of pH 3.4.

比較例1-1  Comparative Example 1-1  

除了於煙草萃取液250mL中添加具有磺酸基之固體酸觸媒7.5g,製得pH2.5之反應混合液以外,其餘係依據與實施例1-1同樣之方法而調製香煙調配用煙草絲。 Tobacco blending tobacco was prepared in the same manner as in Example 1-1, except that 7.5 g of a solid acid catalyst having a sulfonic acid group was added to 250 mL of the tobacco extract to prepare a reaction mixture of pH 2.5. .

比較例1-2  Comparative Example 1-2  

除了未添加具有磺酸基之固體酸觸媒以外,其餘係依據與實施例1-1同樣之方法而調製香煙調配用煙草絲。 The tobacco yarn for cigarette preparation was prepared in the same manner as in Example 1-1, except that the solid acid catalyst having a sulfonic acid group was not added.

實施例2-1  Example 2-1  

於含水比例經調整為12質量%之煙草絲(3R4F參考香煙)25g中添加pH經調整為-1.0之硫酸5mL,製得pH3.5之反應混合液。將所得之反應混合液在22℃下靜置4小時,使煙草絲含有之成分(煙草成分)之反應產生。將反應 後之反應混合液分離成反應後之煙草絲(固體部分)及硫酸(液體部分)。 To 5 g of tobacco silk (3R4F reference cigarette) having a water content ratio adjusted to 12% by mass, 5 mL of sulfuric acid adjusted to -1.0 was added to prepare a reaction mixture of pH 3.5. The obtained reaction mixture was allowed to stand at 22 ° C for 4 hours to cause a reaction of a component (tobacco component) contained in the tobacco yarn. The reaction mixture after the reaction was separated into a tobacco silk (solid portion) and sulfuric acid (liquid portion) after the reaction.

將所得之煙草絲在溫度22℃/相對濕度60%之室內乾燥2日,調整煙草絲之水分含有比例成為12質量%。藉此調製成香煙調配用煙草絲。 The obtained tobacco yarn was dried in a room at a temperature of 22 ° C / 60% relative humidity for 2 days, and the moisture content ratio of the tobacco yarn was adjusted to 12% by mass. Thereby, the tobacco yarn for cigarette preparation is prepared.

比較例2-1  Comparative Example 2-1  

除了於煙草絲中添加pH經調整為1.7之硫酸,製得pH5.1之反應混合液以外,其餘係依據與實施例2-1同樣之方法而調製香煙調配用煙草絲。 The tobacco yarn for cigarette preparation was prepared in the same manner as in Example 2-1, except that a reaction mixture having a pH adjusted to 1.7 was added to the tobacco yarn to prepare a reaction mixture of pH 5.1.

比較例2-2  Comparative Example 2-2  

除了於煙草絲中添加pH經調整為2.5之硫酸,製得pH5.2之反應混合液以外,其餘係依據與實施例2-1同樣之方法而調製香煙調配用煙草絲。 The tobacco blending tobacco yarn was prepared in the same manner as in Example 2-1, except that a sulfuric acid adjusted to pH 2.5 was added to the tobacco yarn to prepare a reaction mixture of pH 5.2.

比較例2-3  Comparative Example 2-3  

除了於煙草絲中添加pH經調整為3.0之硫酸,製得pH5.2之反應混合液以外,其餘係依據與實施例2-1同樣之方法而調製香煙調配用煙草絲。 The tobacco yarn for cigarette blending was prepared in the same manner as in Example 2-1, except that a reaction mixture having a pH adjusted to 3.0 was added to the tobacco yarn to prepare a reaction mixture of pH 5.2.

比較例2-4  Comparative Example 2-4  

除了於煙草絲中添加超純水(pH7.0)取代硫酸,製得pH5.1之反應混合液以外,其餘係依據與實施例2-1同樣之 方法而調製香煙調配用煙草絲。 The tobacco yarn for cigarette preparation was prepared in the same manner as in Example 2-1 except that ultrafine water (pH 7.0) was added to the tobacco yarn instead of sulfuric acid to prepare a reaction mixture of pH 5.1.

實施例3-1  Example 3-1  

將含水比例經調整為12質量%之煙草絲(3R4F參考香煙)25g浸漬於250mL之熱水(60℃)中2小時,萃取煙草絲含有之成分(煙草成分)。其後,使用篩目0.15mm之篩網,分成過篩之煙草萃取液及殘留於篩網上之萃取殘渣。 25 g of tobacco silk (3R4F reference cigarette) having a water content adjusted to 12% by mass was immersed in 250 mL of hot water (60 ° C) for 2 hours to extract a component (tobacco component) contained in the tobacco yarn. Thereafter, a sieve having a mesh size of 0.15 mm was used, and the sieved tobacco extract and the residue remaining on the sieve were separated.

於所得之煙草萃取液250mL中添加pH經調整為-1.0之硫酸6mL,獲得pH1.7之反應混合液。將所得之反應混合液在22℃靜置4小時,使煙草成分之反應產生。 6 mL of sulfuric acid adjusted to -1.0 was added to 250 mL of the obtained tobacco extract to obtain a reaction mixture of pH 1.7. The resulting reaction mixture was allowed to stand at 22 ° C for 4 hours to cause a reaction of the tobacco component.

使用蒸發器將所得之液體濃縮至液體之總量為12.5g左右,以去除萃取溶劑(水)。將所得之處理液12.5g添加於萃取殘渣12.5g中。將所得之混合物在溫度22℃/相對濕度60%之室內乾燥2日,調整煙草絲之水分含有比例成為12質量%。藉此調製成香煙調配用煙草絲。 The resulting liquid was concentrated to a liquid amount of about 12.5 g using an evaporator to remove the extraction solvent (water). 12.5 g of the obtained treatment liquid was added to 12.5 g of the extraction residue. The obtained mixture was dried in a room at a temperature of 22 ° C / a relative humidity of 60% for 2 days, and the moisture content ratio of the tobacco yarn was adjusted to 12% by mass. Thereby, the tobacco yarn for cigarette preparation is prepared.

比較例4-1至4-5  Comparative Examples 4-1 to 4-5  

在比較例4-1至4-5中係除了使用硝酸取代硫酸以外,其餘係依據與實施例2-1同樣之方法而調製香煙調配用煙草絲。 In Comparative Examples 4-1 to 4-5, except for using nitric acid instead of sulfuric acid, the tobacco yarn for cigarette blending was prepared in the same manner as in Example 2-1.

在比較例4-1中,係除了於煙草絲中添加pH經調整為-1.0之硝酸,製得pH2.0之反應混合液以外,其餘係依據與實施例2-1同樣之方法而調製香煙調配用煙草絲。 In Comparative Example 4-1, a cigarette was prepared in the same manner as in Example 2-1 except that a nitric acid having a pH adjusted to -1.0 was added to the tobacco yarn to prepare a reaction mixture having a pH of 2.0. Tobacco yarn for blending.

在比較例4-2中,係除了於煙草絲中添加pH經調整為0.5之硝酸,製得pH4.9之反應混合液以外,其餘係依據與實施例2-1同樣之方法而調製香煙調配用煙草絲。 In Comparative Example 4-2, except that a reaction mixture having a pH adjusted to 0.5 was added to the tobacco yarn to prepare a reaction mixture of pH 4.9, the cigarette preparation was carried out in the same manner as in Example 2-1. Use tobacco silk.

在比較例4-3中,係除了於煙草絲中添加pH經調整為1.7之硝酸,製得pH5.0之反應混合液以外,其餘係依據與實施例2-1同樣之方法而調製香煙調配用煙草絲。 In Comparative Example 4-3, except that a reaction mixture having a pH adjusted to 1.7 was added to the tobacco yarn to prepare a reaction mixture of pH 5.0, the cigarette preparation was carried out in the same manner as in Example 2-1. Use tobacco silk.

在比較例4-4中,係除了於煙草絲中添加pH經調整為2.6之硝酸,製得pH5.1之反應混合液以外,其餘係依據與實施例2-1同樣之方法而調製香煙調配用煙草絲。 In Comparative Example 4-4, except that a reaction mixture having a pH adjusted to 2.6 was added to the tobacco yarn to prepare a reaction mixture of pH 5.1, the cigarette preparation was carried out in the same manner as in Example 2-1. Use tobacco silk.

在比較例4-5中,係除了於煙草絲中添加pH經調整為3.6之硝酸,製得pH5.1之反應混合液以外,其餘係依據與實施例2-1同樣之方法而調製香煙調配用煙草絲。 In Comparative Example 4-5, except that a reaction mixture having a pH adjusted to 3.6 was added to the tobacco yarn to prepare a reaction mixture of pH 5.1, the cigarette preparation was carried out in the same manner as in Example 2-1. Use tobacco silk.

參考例  Reference example  

在參考例中係使用3R4F參考香煙之煙草絲作為通常之煙草絲。 In the reference example, tobacco of 3R4F reference cigarette was used as a usual tobacco yarn.

[2]香煙之製作  [2] Production of cigarettes  

以捲紙包住所調製之煙草絲製作成長度57mm、捲周17mm、每支香煙之填充量300mg之煙草桿部。使用市售 之MEVIUS SUPER LIGHT所使用之捲紙作為卷紙。又,使與煙草桿部相同圓周之17mm紙管與上述煙草桿部連接,製作成測定用之香煙。 A tobacco rod portion having a length of 57 mm, a circumference of 17 mm, and a filling amount of 300 mg per cigarette was prepared by wrapping the tobacco yarn prepared by wrapping paper. Roll paper used in the commercially available MEVIUS SUPER LIGHT was used as the roll paper. Further, a 17 mm paper tube having the same circumference as the tobacco rod portion was connected to the tobacco rod portion to prepare a cigarette for measurement.

[3]測定  [3] Determination  

使用所調製之煙草絲及所製作之香煙,進行下述測定。 The following measurement was carried out using the prepared tobacco yarn and the produced cigarette.

a.煙草絲中之含碳比例  a. The proportion of carbon in tobacco silk  

將所調製之香煙調配用煙草絲在調和環境下(22℃、60%相對濕度)下儲藏24小時以上。儲藏後,秤量0.01g之煙草絲,在氧化環境下加熱至800℃。將所得之燃燒生成物以元素分析裝置SUMIGRAPH NCH-22F(住化分析中心股份有限公司製)分析而求得元素組成。使用結晶纖維素作為碳與氫之參考。 The prepared tobacco tobacco was prepared to be stored in a blending environment (22 ° C, 60% relative humidity) for 24 hours or more. After storage, 0.01 g of tobacco silk was weighed and heated to 800 ° C in an oxidizing atmosphere. The obtained combustion product was analyzed by an elemental analysis device SUMIGRAPH NCH-22F (manufactured by Sumitomo Chemical Co., Ltd.) to determine the elemental composition. Crystalline cellulose is used as a reference for carbon and hydrogen.

b.碳化物中之含碳比例  b. The proportion of carbon in the carbide  

將所調製之香煙調配用煙草絲在調和環境下(22℃、60%相對濕度)下儲藏24小時以上。儲藏後,將煙草絲0.2g放入坩堝,設置於高溫爐中,在氮環境下加熱至500℃,其後,以500℃保持10分鐘。高溫爐之溫度下降至50℃以下後,取出坩堝,置入於22℃之乾燥器中,靜置0.5小時,得到碳化物。秤量碳化物0.01g,在氧化環境下加熱至800℃。將所得之燃燒生成物以元素分析裝置SUMIGRAPH NCH-22F(住化分析中心股份有限公司製)分析而求得元素組成。使用結晶纖維素作為碳與氫之參考。 The prepared tobacco tobacco was prepared to be stored in a blending environment (22 ° C, 60% relative humidity) for 24 hours or more. After storage, 0.2 g of tobacco silk was placed in a crucible, placed in a high-temperature furnace, heated to 500 ° C in a nitrogen atmosphere, and then held at 500 ° C for 10 minutes. After the temperature of the high-temperature furnace was lowered to 50 ° C or lower, the crucible was taken out, placed in a desiccator at 22 ° C, and allowed to stand for 0.5 hour to obtain a carbide. Weigh 0.01 g of carbide and heat to 800 ° C in an oxidizing atmosphere. The obtained combustion product was analyzed by an elemental analysis device SUMIGRAPH NCH-22F (manufactured by Sumitomo Chemical Co., Ltd.) to determine the elemental composition. Crystalline cellulose is used as a reference for carbon and hydrogen.

c.副流煙量  c. sidestream smoke  

以日本國專利公開公報第2002-82053號記載之方法測定副流煙量。亦即,使測定用之香煙自然燃燒產生副流煙,於副流煙之上昇方向呈垂直的方向照射可見光束,測定於可見光束之照射方向呈垂直的方向散射之散亂光之強度(與副流煙量相關)。 The amount of sidestream smoke was measured by the method described in Japanese Laid-Open Patent Publication No. 2002-82053. That is, the cigarette for measurement is naturally burned to generate a sidestream smoke, and the visible light beam is irradiated in a direction perpendicular to the rising direction of the sidestream smoke, and the intensity of the scattered light scattered in a direction perpendicular to the direction in which the visible light beam is irradiated is measured (and The amount of sidestream smoke is related).

d.吸煙次數  d. Number of cigarettes  

僅使用煙草桿部(不含濾嘴部分)作為測定用之香煙。依據CIR法(流量:27.5mL/秒、吸煙時間:2秒/抽吸、吸煙頻率:2抽吸/分)進行吸煙,測定菸頭長度(Butt length)成為35mm為止之吸煙次數。 Only the tobacco rod portion (without the filter portion) was used as the cigarette for measurement. Smoking was carried out according to the CIR method (flow rate: 27.5 mL/sec, smoking time: 2 sec/suction, smoking frequency: 2 puff/min), and the number of cigarettes until the length of the butt length (Butt length) became 35 mm was measured.

[4]結果  [4] Results  

將測定結果表示於下述表。「煙草絲中之含碳比例」及「碳化物中之含碳比例」係分別表示3個煙草絲試樣之平均值,「副流煙量」及「吸煙次數」係分別表示3根香煙試樣之平均值。 The measurement results are shown in the following table. "Carbon content in tobacco silk" and "Carbon ratio in carbide" are the average values of three tobacco silk samples, respectively. "Sub-stream smoke" and "number of cigarettes" indicate three cigarette tests. The average value of the sample.

在實施例1-1至1-4、以及比較例1-1及1-2中,使用煙草萃取液作為反應對象,使用具有磺酸基之固體酸觸媒作為反應參與物質。從此等實驗結果,可知含有 煙草萃取液及固體酸觸媒之反應混合液之pH設為特定值(3.5)以下,並且使煙草絲含有之成分之反應產生時,所得之煙草絲不會使吸煙次數減少,而且可降低從香煙生成之副流煙。 In Examples 1-1 to 1-4, and Comparative Examples 1-1 and 1-2, a tobacco extract was used as a reaction target, and a solid acid catalyst having a sulfonic acid group was used as a reaction-participating substance. From the results of these experiments, it is understood that the pH of the reaction mixture containing the tobacco extract and the solid acid catalyst is set to a specific value (3.5) or less, and when the reaction of the components contained in the tobacco yarn is produced, the obtained tobacco yarn does not cause smoking. The number of times is reduced, and the sidestream smoke generated from the cigarette can be reduced.

在實施例2-1、及比較例2-1乃至2-3中,係使用煙草絲作為反應對象,使用硫酸作為反應參與物質。從此等實驗結果,亦顯示含有煙草絲及硫酸之反應混合液之pH設為特定值(3.5)以下,並且使煙草絲含有之成分之反應產生時,所得之煙草絲不會使吸煙次數減少,而且可降低從香煙生成之副流煙。 In Example 2-1 and Comparative Example 2-1 to 2-3, tobacco silk was used as a reaction target, and sulfuric acid was used as a reaction-participating substance. From the results of these experiments, it is also shown that when the pH of the reaction mixture containing tobacco silk and sulfuric acid is set to a specific value (3.5) or less, and the reaction of the components contained in the tobacco yarn is produced, the obtained tobacco yarn does not reduce the number of cigarettes to be smoked. Moreover, the sidestream smoke generated from the cigarette can be reduced.

在實施例3-1中,使用煙草萃取液作為反應對象,使用硫酸作為反應參與物質。從此實驗,亦顯示含有煙草萃取液及硫酸之反應混合液之pH設為特定值(3.5)以下,使煙草絲含有之成分之反應產生時,所得之煙草絲不會使吸煙次數減少,而且可降低從香煙所生成之副流煙。 In Example 3-1, a tobacco extract was used as a reaction object, and sulfuric acid was used as a reaction-participating substance. From this experiment, it is also shown that the pH of the reaction mixture containing the tobacco extract and sulfuric acid is set to a specific value (3.5) or less, and when the reaction of the components contained in the tobacco yarn is produced, the obtained tobacco yarn does not reduce the number of times of smoking, and Reduce the sidestream smoke generated from cigarettes.

又,從實施例1-1至1-3之結果,可知如下述。依據本發明之方法所得之煙草絲以100質量%之調配比例調配於香煙時,煙草絲於自然燃燒時極難以燃燒,而可顯著地降低副流煙。另一方面,將依據本發明之方法所得之煙草絲以50至75質量%之調配比例與通常之煙草絲混合並調配於香煙時,可一併具有煙草絲於自然燃燒時難以燃燒,而可降低副流煙之效果,以及於吸煙燃燒時以與通常之煙草絲具有同樣的容易燃燒程度進行燃燒的效果。 Further, from the results of Examples 1-1 to 1-3, it is as follows. When the tobacco yarn obtained by the method of the present invention is formulated in a ratio of 100% by mass to the cigarette, the tobacco yarn is extremely difficult to burn when it is naturally burned, and the sidestream smoke can be remarkably reduced. On the other hand, when the tobacco yarn obtained by the method of the present invention is mixed with a usual tobacco yarn in a blending ratio of 50 to 75% by mass and formulated in a cigarette, the tobacco yarn can be easily burned when naturally burned, but The effect of reducing the sidestream smoke and the effect of burning at the same degree of burning as the usual tobacco yarn when smoking is burned.

又,從比較例4-1至4-5之結果,可知使用 硝酸取代硫酸而使反應混合液之pH為特定值(3.5)以下,即使使煙草絲含有之成分產生反應,仍無法降低從香煙生成之副流煙。 Further, from the results of Comparative Examples 4-1 to 4-5, it was found that the pH of the reaction mixture was set to a specific value (3.5) or less by using nitric acid instead of sulfuric acid, and even if the components contained in the tobacco yarn were reacted, the cigarette could not be lowered. The sidestream smoke generated.

又,從實施例1-1至1-3、實施例2-1、實施例3-1、及參考例之結果,可知依據本發明方法所得之煙草絲,與通常之煙草絲相比,可不使吸煙次數減少,並且降低從香煙生成之副流煙。 Further, from the results of Examples 1-1 to 1-3, Example 2-1, Example 3-1, and Reference Examples, it is understood that the tobacco yarn obtained by the method of the present invention is comparable to the conventional tobacco yarn. The number of smoking is reduced, and the sidestream smoke generated from the cigarette is reduced.

Claims (15)

一種吸煙物品調配用煙草絲之製造方法,係包含:以可獲得具有3.5以下pH的反應混合液之方式,將選自含有煙草絲所含有之成分的煙草萃取液及煙草絲之反應對象、與選自具有磺酸基之固體酸觸媒及硫酸之反應參與物質進行混合,使前述煙草絲所含有之成分的反應產生。 A method for producing a tobacco yarn for blending a smoking article, comprising: reacting a tobacco extract and a tobacco yarn selected from the group consisting of tobacco silk containing a reaction mixture having a pH of 3.5 or less, and A reaction product selected from the group consisting of a solid acid catalyst having a sulfonic acid group and sulfuric acid is mixed to produce a reaction of a component contained in the tobacco yarn. 如申請專利範圍第1項所述之製造方法,其中,前述反應對象為含有煙草絲所含有之成分的煙草萃取液,前述反應參與物質為具有磺酸基之固體酸觸媒。 The production method according to the first aspect of the invention, wherein the reaction object is a tobacco extract containing a component contained in tobacco silk, and the reaction-participating substance is a solid acid catalyst having a sulfonic acid group. 如申請專利範圍第1項所述之製造方法,其中,前述反應對象為含有煙草絲所含有之成分的煙草萃取液,前述反應參與物質為硫酸。 The production method according to the first aspect of the invention, wherein the reaction object is a tobacco extract containing a component contained in tobacco silk, and the reaction-participating substance is sulfuric acid. 如申請專利範圍第1項所述之製造方法,其中,前述反應對象為煙草絲,前述反應參與物質為具有磺酸基之固體酸觸媒。 The production method according to claim 1, wherein the reaction target is tobacco yarn, and the reaction-participating substance is a solid acid catalyst having a sulfonic acid group. 如申請專利範圍第1項所述之製造方法,其中,前述反應對象為煙草絲,前述反應參與物質為硫酸。 The production method according to claim 1, wherein the reaction target is tobacco yarn, and the reaction participating substance is sulfuric acid. 如申請專利範圍第1至5項中任一項所述之製造方法,其中,前述反應混合液具有1.7至3.5之pH。 The production method according to any one of claims 1 to 5, wherein the reaction mixture has a pH of from 1.7 to 3.5. 如申請專利範圍第6項所述之製造方法,其中,前述反應混合液具有1.7至2.5之pH。 The production method according to claim 6, wherein the reaction mixture has a pH of from 1.7 to 2.5. 一種吸煙物品調配用煙草絲,係藉由申請專利範圍第1至7項中任一項所述之製造方法而得到者。 A tobacco yarn for use in the preparation of a smoking article is obtained by the production method according to any one of claims 1 to 7. 一種吸煙物品調配用煙草絲,係申請專利範圍第8項所述之吸煙物品調配用煙草絲,其中前述吸煙物品調配用煙草絲中之含碳比例為未達0.50,並且藉由在氮環境下、於500℃中加熱前述吸煙物品調配用煙草絲10分鐘,其後,以22℃維持0.5小時而得之碳化物中的含碳比例為0.50以上。 The invention relates to a tobacco yarn for blending smoking articles, which is a tobacco yarn for distributing smoking articles according to claim 8 of the patent application, wherein the proportion of carbon in the tobacco yarn for blending the aforementioned smoking articles is less than 0.50, and by using nitrogen in a nitrogen environment The tobacco yarn for tobacco preparation preparation was heated at 500 ° C for 10 minutes, and then the carbon content in the carbide was 0.50 or more at 22 ° C for 0.5 hour. 一種吸煙物品,係含有申請專利範圍第8項所述之吸煙物品調配用煙草絲。 A smoking article comprising the tobacco yarn for smoking article preparation according to item 8 of the patent application. 一種吸煙物品,係含有申請專利範圍第8項所述之吸煙物品調配用煙草絲之吸煙物品,其中前述吸煙物品調配用煙草絲佔前述吸煙物品所含有之全煙草絲的100質量%。 A smoking article is the smoking article of the tobacco yarn for smoking article preparation according to claim 8, wherein the tobacco material for the smoking article formulation accounts for 100% by mass of the whole tobacco yarn contained in the smoking article. 一種吸煙物品,係含有申請專利範圍第8項所述之吸煙物品調配用煙草絲之吸煙物品,其中前述吸煙物品調配用煙草絲佔前述吸煙物品所含有之全煙草絲的50至75質量%。 A smoking article is the smoking article of the tobacco material for smoking articles according to claim 8, wherein the tobacco material for the smoking article preparation comprises 50 to 75 mass% of the total tobacco yarn contained in the smoking article. 一種香煙,係含有申請專利範圍第8項所述之吸煙物品調配用煙草絲。 A cigarette comprising the tobacco yarn for smoking article preparation according to item 8 of the patent application. 一種香煙,係含有申請專利範圍第8項所述之吸煙物品調配用煙草絲,其中前述吸煙物品調配用煙草絲佔前述香煙所含有之全煙草絲的100質量%。 A cigarette comprising the tobacco yarn for smoking article preparation according to claim 8, wherein the tobacco material for the smoking article formulation accounts for 100% by mass of the whole tobacco yarn contained in the cigarette. 一種香煙,係含有申請專利範圍第8項所述之吸煙物品調配用煙草絲,其中前述吸煙物品調配用煙草絲佔前述香煙所含有之全煙草絲的50至75質量%。 A cigarette comprising the tobacco yarn for smoking article formulation according to claim 8, wherein the tobacco material for the smoking article formulation comprises 50 to 75 mass% of the whole tobacco yarn contained in the cigarette.
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