JPS6140777A - Earth and sand separation in sheet tobacco producing process - Google Patents

Earth and sand separation in sheet tobacco producing process

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Publication number
JPS6140777A
JPS6140777A JP12203384A JP12203384A JPS6140777A JP S6140777 A JPS6140777 A JP S6140777A JP 12203384 A JP12203384 A JP 12203384A JP 12203384 A JP12203384 A JP 12203384A JP S6140777 A JPS6140777 A JP S6140777A
Authority
JP
Japan
Prior art keywords
sand
tobacco powder
fine
powder
earth
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.)
Granted
Application number
JP12203384A
Other languages
Japanese (ja)
Other versions
JPS6221507B2 (en
Inventor
富沢 茂
片岡 悟
久保田 誠一
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Japan Tobacco Inc
Original Assignee
Japan Tobacco Inc
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Japan Tobacco Inc filed Critical Japan Tobacco Inc
Priority to JP12203384A priority Critical patent/JPS6140777A/en
Publication of JPS6140777A publication Critical patent/JPS6140777A/en
Publication of JPS6221507B2 publication Critical patent/JPS6221507B2/ja
Granted legal-status Critical Current

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Abstract

(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。
(57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.

Description

【発明の詳細な説明】 本発明は、シートたばこ製造工程における土砂分離方法
に関するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for separating soil and sand in a sheet tobacco manufacturing process.

シートたばこの製造工程にあっては、原料としてたばこ
製造工程で注出したくずであるたばこ細粉や、あるいは
着葉位置の異なる数十種の葉たばこを細(刻んでブレン
ドしてなるたばこ細粉が使用されるが、いずれももとの
葉たばこに付着した土砂等が混入しており、このため粉
砕工程、成形工程での゛装置の一摩耗を防止し、また製
品品質を一定に保持する目的でこれら工程の前に原料の
たばこ細粉中に混入している土砂等を分離する分離工程
を設けている。
In the manufacturing process of sheet cigarettes, the raw materials are either fine tobacco powder, which is the waste poured out during the tobacco manufacturing process, or fine tobacco powder, which is made by chopping and blending dozens of types of leaf tobacco with different leaf positions. However, all of them are contaminated with dirt, etc. that adhered to the original leaf tobacco, so the purpose is to prevent wear of the equipment during the crushing and molding processes, and to maintain a constant product quality. Before these steps, a separation step is carried out to separate dirt and sand mixed into the fine tobacco powder, which is the raw material.

従来の分離工程では、篩目の異なる複数の篩を使用し、
まず大きい篩目の第1篩で篩別、この後篩目以下の篩下
たばこ細粉を小さい篩目の第2篩で篩別している。
In the conventional separation process, multiple sieves with different mesh sizes are used.
First, the tobacco is sieved using a first sieve with a large sieve size, and then the fine tobacco powder below the sieve size is sieved using a second sieve with a small sieve size.

しかし、たばこ細粉と土砂等の粒径があまり変わらない
ものについては、たばこ細粉と土砂等を篩で分離するこ
とはできない。
However, if the particle sizes of fine tobacco powder and sand and the like do not differ much, it is not possible to separate the fine tobacco powder and sand and the like using a sieve.

土砂等の粒径が成形工程での成形ロール間の間隙(はぼ
0.1鶴程度)よりも小さい場合については、成形ロー
ルを傷つけることがなく、また粉砕工程で粉砕する必要
がなく、さらにある程度の土砂等の混入がタール分の減
少に役立つこと等から問題がないものの、粒径が成形ロ
ール間の間隙付近の場合には成形ロールを傷つける問題
がある。
When the particle size of the earth and sand is smaller than the gap between the forming rolls in the forming process (approximately 0.1 crane), the forming rolls will not be damaged, and there is no need to crush them in the crushing process. Although there is no problem with the inclusion of a certain amount of earth and sand because it helps to reduce the tar content, there is a problem of damaging the forming rolls if the particle size is close to the gap between the forming rolls.

本発明は上記事情に鑑みてなされたもので、その目的と
するところは、粉砕工程、成形工程でトラブルが生じな
いようにたばこ細粉から土砂等を分離するシートたばこ
製造工程における土砂分離方法を提供することである。
The present invention has been made in view of the above circumstances, and its purpose is to provide a method for separating soil and sand in the sheet tobacco manufacturing process, which separates soil and the like from fine tobacco powder so as to prevent troubles from occurring during the crushing and molding processes. It is to provide.

上記目的を達成するため、本発明は、土砂等が混入して
いるたばこ細粉を篩で篩別し、次いで篩別された篩下た
ばこ細粉を流動層に送り、該流動層で気体流によりたば
こ細粉を飛散させ、この後流動層で飛散せず残留したた
ばこ細粉を回転分離機に送り、該回転分離機で遠心力と
求心力を利用して土砂等とたばこ細粉とを分離すること
を特徴としている。
In order to achieve the above object, the present invention sieves fine tobacco powder mixed with earth and sand, etc., sends the sieved fine tobacco powder under the sieve to a fluidized bed, and in the fluidized bed, a gas flow is generated. The fine tobacco powder is scattered by the fluidized bed, and the remaining tobacco fine powder that is not scattered in the fluidized bed is sent to a rotary separator, and the rotary separator uses centrifugal force and centripetal force to separate the fine tobacco powder from earth and sand. It is characterized by

以下本発明の一実施例を図面を参照して説明する。An embodiment of the present invention will be described below with reference to the drawings.

第1図は本発明の土砂分離方法を採用したシートたばこ
製造工程の全体の概要を示している0図中符号1は土砂
分離工程、2,3は粉砕工程、4は配合工程、5は成形
工程、6は乾燥工程、7は裁断工程である。
Figure 1 shows an overview of the entire sheet tobacco manufacturing process employing the sand separation method of the present invention. Step 6 is a drying step, and 7 is a cutting step.

原料としては、たばこ製造工程で注出したくずであるた
ばこ細粉、あるいは若葉位置の異なる数十種の葉たばこ
を細く刻んでブレンドしてなるたばこ細粉が使用される
The raw material used is fine tobacco powder, which is the waste poured out during the tobacco manufacturing process, or fine tobacco powder, which is made by finely chopping and blending dozens of types of leaf tobacco with different young leaf positions.

たばこ細粉は、まず土砂分離工程1で土砂等が分離され
た後、粉砕工程2で粉砕される。この粉砕工程2では、
粉砕工程3で粉砕された粉末添加物、すなわち結合剤と
してのセルロース誘導体や天然の各種ガム、耐破壊性を
賦与するための繊維状物が粉砕混合されて、均一な粉末
混合物となる。
The fine tobacco powder is first separated from sand and the like in a sand separation step 1, and then pulverized in a pulverization step 2. In this crushing step 2,
The powder additives pulverized in the pulverization step 3, that is, cellulose derivatives and various natural gums as binders, and fibrous materials for imparting fracture resistance, are pulverized and mixed to form a uniform powder mixture.

粉末混合物は配合工程4に送られ、ここで可塑剤および
香料として各種グリコールやツルピントなどとともに湿
潤強度剤としての各種ジ・アルデヒドが水に?8WIし
て添加されて、均一に湿潤した粉粒体となる。
The powder mixture is sent to compounding step 4, where various di-aldehydes as wet strength agents are added to water along with various glycols and turpinto as plasticizers and fragrances. It is added at 8WI to form a uniformly wet powder.

10%〜80%の水分範囲の湿潤粉粒体は、成形工程5
に送られて、ここで2本のロールにより連続的に圧延さ
れてシート状となってトゲターナイフによりロールから
剥離される。
Wet powder with a moisture content of 10% to 80% is formed in the molding step 5.
There, it is continuously rolled by two rolls to form a sheet and peeled off from the rolls by a thorn knife.

ロールから剥されたシート状たばこは乾燥工程6で水分
8〜15%に調湿された後、裁断工程7で所定寸法に裁
断される。
The sheet-shaped tobacco peeled from the roll is conditioned to have a moisture content of 8 to 15% in a drying step 6, and then cut into predetermined sizes in a cutting step 7.

以上がシートたばこ製造工程の概要である0次に土砂分
離工程1を詳細に説明する。たばこ細粉は、まず篩目0
.3fiのWa8に送られて篩別される。
The above is an overview of the sheet tobacco manufacturing process, and the soil separation process 1 will be explained in detail. Tobacco fine powder is first sieved to 0
.. It is sent to Wa8 of 3fi and is screened.

0.3fi以上のたばこ細粉は粉砕工程2に送られる。Fine tobacco powder of 0.3fi or more is sent to the crushing step 2.

このたばこ細粉中に混入する土砂等はわずかであり、粉
砕工程2で粉砕される。0.3m以下の篩下たばこ細粉
(篩上たばこ細粉よりも土砂等の混入量が多い)は、第
2図に示すように、定量供給機9によ゛り撮動流動層1
0に送られる。
Only a small amount of earth and sand is mixed into this fine tobacco powder, and it is crushed in the crushing step 2. As shown in Fig. 2, the fine tobacco powder under the sieve of 0.3 m or less (containing more soil, etc. than the fine tobacco powder above the sieve) is fed to the moving fluidized bed 1 by the quantitative feeder 9, as shown in Fig. 2.
Sent to 0.

振動流動fftloは、入口lll110 aが高く出
口側10bが低くなるように傾斜していて、全体が振動
しつつ送風機11からの空気を網状の整流板12がら空
気吹出面風速20cm/mで吹き込んでたばこ細粉を飛
散させる。空気により飛散されたたばこ細粉は、サイク
ロン13に送られて空気と分離された後、粉砕工程2に
送られる。このたばこ細粉中には、空気流により吹き上
げられる程度の粒径の小さい土砂等(成形ロール間の間
隙よりも小さい)が混入しているが、これは前述の如く
問題がない。
The oscillating flow fftlo is inclined so that the inlet side 110a is high and the outlet side 10b is low, and the air from the blower 11 is blown at a wind speed of 20 cm/m on the air outlet surface through the mesh rectifier plate 12 while the whole body vibrates. Sprinkle fine tobacco powder. The fine tobacco powder scattered by the air is sent to the cyclone 13 and separated from the air, and then sent to the crushing step 2. This fine tobacco powder contains dirt and the like whose particle size is small enough to be blown up by the air flow (smaller than the gap between the forming rolls), but this is not a problem as described above.

飛散されずに振動流動層10に残留したたばこ細粉中に
は土砂等が多く混入しており、しかもここに混入してい
る土砂等はその粒径が成形ロール間の間隙付近のものが
多い、このたばこ細粉は回転分1iIt機14に送られ
、ここで遠心力と求心力を利用してたばこ細粉と土砂等
に分離される。なお、第2図中計4はエアーロッカ(ロ
ータリバルブ)である。
The fine tobacco powder remaining in the vibrating fluidized bed 10 without being scattered contains a lot of dirt, etc., and the particle size of the dirt, etc. mixed in here is often close to the gap between the forming rolls. This fine tobacco powder is sent to the rotating 1iIt machine 14, where it is separated into fine tobacco powder, dirt, etc. using centrifugal force and centripetal force. Note that 4 in Figure 2 is an air locker (rotary valve).

第3図〜第6図はこの回転分離機14を詳細に示してい
る0円筒状の本体15の上部には投入口16が設けられ
ていて、該投入口16から投入された上述のたばこ細粉
は投入口16のほぼ真下位置に設けられた原料分散板1
7により本体15内の空間内に分散される。
3 to 6 show this rotary separator 14 in detail. A cylindrical main body 15 is provided with an input port 16 in the upper part, and the above-mentioned tobacco fines are inputted from the input port 16. The powder is transferred to the raw material dispersion plate 1 located almost directly below the input port 16.
7 to be distributed within the space within the main body 15.

原料分散板17の下方位置には適宜間隔をおいてほぼ円
錐状の分離板18が設けられている。この分離板18の
斜面18aは傾斜角度θが3°程度に設定されている0
分離板18の中央部には原料落下口19が設けられ、ま
た分離板18の周縁と本体15の周壁との間には2〜3
謳程度の土砂落下間隙2−0が設けられている。
Substantially conical separating plates 18 are provided below the raw material distribution plate 17 at appropriate intervals. The slope 18a of this separation plate 18 has an inclination angle θ of about 3°.
A raw material falling port 19 is provided in the center of the separating plate 18, and two to three holes are provided between the peripheral edge of the separating plate 18 and the peripheral wall of the main body 15.
An earth and sand fall gap 2-0 is provided.

本体15を回転駆動する回動装置21は、クランク状の
駆動軸22と該駆動軸22に駆動力を与えるモータ(図
示せず)とから構成されている。
A rotating device 21 that rotationally drives the main body 15 is composed of a crank-shaped drive shaft 22 and a motor (not shown) that applies a driving force to the drive shaft 22.

駆動軸22は本体1の底部側の中心軸線(本体15の中
心軸線11と一致)がプーリ23を設けた側の中心軸線
12と距離dだけずれている。モータにより駆動軸2I
を駆動して本体I5を回転(250rpm+程度)させ
ると、この回転運動は、第6図に示すように、回転運動
径2d (25m程度)、回転運動外周2d+D(Dは
本体15の直径)で公転することになる。
In the drive shaft 22, the center axis on the bottom side of the main body 1 (coinciding with the center axis 11 of the main body 15) is shifted by a distance d from the center axis 12 on the side where the pulley 23 is provided. Drive shaft 2I by motor
When the main body I5 is rotated (approximately 250 rpm+) by driving the main body I5, as shown in FIG. It will revolve.

このため、分離板1B上に落下したたばこ細粉は上記回
転運動による遠心力と求心力とを受けて、比重の大きい
土砂等は斜面18aに沿って分離板18の周縁に寄せら
れ、比重の小さいたばこ細粉は斜面18aに沿って中央
側に寄せられる。
Therefore, the fine tobacco powder that has fallen onto the separating plate 1B is subjected to the centrifugal force and centripetal force caused by the above-mentioned rotational movement, and the earth and sand with a high specific gravity are gathered to the periphery of the separating plate 18 along the slope 18a, The fine tobacco powder is gathered toward the center along the slope 18a.

周縁側に寄せられた土砂等は土砂落下間隙2゜から落下
して排出口24から排出され、また中央側に寄せられた
たばこ細粉は原料落下口19から落下して取出口25か
ら取出される。
The earth and sand collected on the periphery side fall through the earth and sand falling gap 2° and are discharged from the discharge port 24, and the tobacco fine powder collected on the center side falls from the raw material fall port 19 and is taken out from the take-out port 25. Ru.

取出口25から取出されるたばこ細粉には若干土砂等が
混入しているものの、この土砂等は求心力を受けて分離
板18の中央側に寄せられるものであり、その粒径は成
形ロール間の間隙よりも小さく問題がない8間隙付近の
粒径の土砂等は遠心力により分離板18の周縁側に寄せ
られるため、このたばこ細粉中に混入しているようなこ
とばない、このたばこ細粉は粉砕工程2に送られる。排
出口24から排出された土砂等には若干たばこ細粉が混
入しているが、これは廃棄される。
Although the fine tobacco powder taken out from the outlet 25 contains some dirt and sand, this dirt is attracted to the center of the separation plate 18 by the centripetal force, and its particle size is smaller than that between the forming rolls. Sediment, etc. with a particle size near the 8-gap, which is smaller than the gap and poses no problem, is brought to the periphery of the separation plate 18 by centrifugal force, so that there is no such thing as being mixed in with this tobacco fine powder. The powder is sent to grinding step 2. Although some fine tobacco powder is mixed in the earth and sand discharged from the discharge port 24, this is discarded.

このように、0.3fi以上のたばこ細粉には土砂等が
わずかに混入しているが、これば粉砕工程2で粉砕され
てしまい、また振動流動層10で空気流により飛散され
たたばこ細粉や回転分離機14で分離されたたばこ細粉
に混入する土砂等の粒径は成形ロール間の間隙よりも小
さく、このため粉砕工程2で使用する粉砕機は従来より
も能力の小さいものですみ、また成形ロールを傷つける
おそれがなく、土砂等の分離効率が優れている。
As described above, fine tobacco powder of 0.3 fi or more contains a small amount of dirt, etc., but this is crushed in the crushing step 2, and the tobacco fine powder is scattered by the air flow in the vibrating fluidized bed 10. The particle size of the dust and dirt mixed in the fine tobacco powder separated by the rotary separator 14 is smaller than the gap between the forming rolls, so the capacity of the crusher used in crushing process 2 is smaller than conventional ones. Also, there is no risk of damaging the forming rolls, and the separation efficiency of dirt, etc. is excellent.

上記土砂分離方法で在来種と黄色種のたばこ細粉につい
て土砂等を分離したところ次の表に示す結果を得た。
When the soil and other substances were separated from fine powder of native and yellow tobacco using the above-mentioned method of separating tobacco, the results shown in the following table were obtained.

電l 各項の上段は元原料を100としたもの。Electricity The upper row of each item is based on the original raw material as 100.

〃 下段は土砂含有率(%)である。従−って両者の積
が土砂の量目であり他がたばこの量目を示す。
〃 The lower row shows the soil content (%). Therefore, the product of the two represents the amount of earth and sand, and the other represents the amount of tobacco.

x2 分離結果は回転分離機の排出口24の土砂等を廃
棄したもの。
x2 Separation results are the result of discarding the earth and sand from the discharge port 24 of the rotary separator.

東8 比較例は回転分離機を使用せず、流動層の残留部
分を廃棄して分離結果を示した。
East 8 Comparative example did not use a rotary separator, and the remaining portion of the fluidized bed was discarded to show the separation results.

上記表から明らかなように、たばこの回収率が95%以
上と大幅に向上した。
As is clear from the table above, the cigarette recovery rate was significantly improved to over 95%.

以上説明したように本発明によれば、篩による分離手段
と流動層による分離手段と遠心力と求心力を利用した回
転分離による分離手段とを組み合わせて、まず篩で分離
し、次で流動層で分離し、この後回転分離機で分離する
ようにしているので、土砂分離効率が良く、粉砕工程で
の負担が少な(、また成形ロールを傷つけることがない
As explained above, according to the present invention, separation means using a sieve, separation means using a fluidized bed, and separation means using rotational separation using centrifugal force and centripetal force are combined, and separation is first performed using a sieve, and then separation is performed using a fluidized bed. Since it is separated and then separated using a rotary separator, the soil and sand separation efficiency is high, and the burden on the crushing process is small (and the forming rolls are not damaged).

【図面の簡単な説明】[Brief explanation of drawings]

図面は本発明の一実施例を示すもので、第1図はシート
たばこ製造工程全体の概略図、第2図は分離工程を詳細
に示す構成図、第3図〜第6図は回転分δU機を詳細に
示しており、第3図は全体の断面図、第4図は回動装置
の拡大断面図、第5図は本体の横断面図、第6図は回転
運動を説明する説明図である。 8・・・篩、10・・・流動層、14・・・回転分離機
。 特許出願人     日  本 専 売 公 社指定代
理人     日本専売公社研究開発部長中   山 
   道   夫
The drawings show one embodiment of the present invention, in which Fig. 1 is a schematic diagram of the entire sheet cigarette manufacturing process, Fig. 2 is a configuration diagram showing the separation process in detail, and Figs. 3 to 6 are diagrams showing the rotation amount δU. The machine is shown in detail, with Fig. 3 being an overall sectional view, Fig. 4 being an enlarged sectional view of the rotating device, Fig. 5 being a cross-sectional view of the main body, and Fig. 6 being an explanatory diagram explaining the rotational movement. It is. 8... Sieve, 10... Fluidized bed, 14... Rotary separator. Patent applicant: Japan Exclusive Public Corporation designated agent: Nakayama, Director of Research and Development, Japan Exclusive Public Corporation
Michi Husband

Claims (1)

【特許請求の範囲】[Claims] 土砂等が混入しているたばこ細粉を篩で篩別し、次いで
篩別された篩下たばこ細粉を流動層に送り、該流動層で
気体流によりたばこ細粉を飛散させ、この後流動層で飛
散せず残留したたばこ細粉を回転分離機に送り、該回転
分離機で遠心力と求心力とを利用して土砂等とたばこ細
粉とに分離することを特徴とするシートたばこ製造工程
における土砂分離方法。
Fine tobacco powder mixed with earth and sand is separated by a sieve, and then the sieved fine tobacco powder under the sieve is sent to a fluidized bed, where the fine tobacco powder is scattered by a gas flow, and then A sheet cigarette manufacturing process characterized by sending the fine tobacco powder remaining without being scattered in the layer to a rotary separator, and separating it into sand, etc. and fine tobacco powder using centrifugal force and centripetal force in the rotary separator. Sediment separation method.
JP12203384A 1984-06-15 1984-06-15 Earth and sand separation in sheet tobacco producing process Granted JPS6140777A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP12203384A JPS6140777A (en) 1984-06-15 1984-06-15 Earth and sand separation in sheet tobacco producing process

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP12203384A JPS6140777A (en) 1984-06-15 1984-06-15 Earth and sand separation in sheet tobacco producing process

Publications (2)

Publication Number Publication Date
JPS6140777A true JPS6140777A (en) 1986-02-27
JPS6221507B2 JPS6221507B2 (en) 1987-05-13

Family

ID=14825927

Family Applications (1)

Application Number Title Priority Date Filing Date
JP12203384A Granted JPS6140777A (en) 1984-06-15 1984-06-15 Earth and sand separation in sheet tobacco producing process

Country Status (1)

Country Link
JP (1) JPS6140777A (en)

Also Published As

Publication number Publication date
JPS6221507B2 (en) 1987-05-13

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