JPH0659199B2 - How to puff tobacco material - Google Patents
How to puff tobacco materialInfo
- Publication number
- JPH0659199B2 JPH0659199B2 JP4670587A JP4670587A JPH0659199B2 JP H0659199 B2 JPH0659199 B2 JP H0659199B2 JP 4670587 A JP4670587 A JP 4670587A JP 4670587 A JP4670587 A JP 4670587A JP H0659199 B2 JPH0659199 B2 JP H0659199B2
- Authority
- JP
- Japan
- Prior art keywords
- raw material
- carbon dioxide
- tobacco raw
- ethanol
- dioxide gas
- 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.)
- Expired - Lifetime
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- Manufacture Of Tobacco Products (AREA)
Description
【発明の詳細な説明】 〔産業上の利用分野〕 この発明は、たばこ原料の膨化方法に関する。TECHNICAL FIELD The present invention relates to a method for expanding a tobacco raw material.
たばこの膨化は、巻たばこ等のたばこ製品におけるたば
こ原料の使用量を節減し、またたばこ製品の香喫味の緩
和化等を目的とし、乾燥・収縮したたばこ組織を、生葉
の状態に近い状態まで膨張させる技術であり、たばこ製
品の製造において重要な技術をなしている。Tobacco puffing reduces the amount of tobacco raw materials used in tobacco products such as cigarettes, and also reduces the flavor and taste of tobacco products. It is an inflating technology and is an important technology in the manufacture of tobacco products.
乾燥たばこ原料を膨化させるための方法は、基本的に、
乾燥たばこ組織内に膨化助剤を浸透させ、加熱により膨
化助剤をたばこ組織内から瞬時に追い出すことを含む。
加熱により体積膨張した膨化助剤は、たばこ原料を膨張
させる。The method for expanding the dry tobacco material is basically
Including a puffing aid in the dry tobacco tissue and instantaneously expelling the puffing aid from the tobacco tissue by heating.
The swelling aid, which has been expanded in volume by heating, expands the tobacco raw material.
このようなたばこ原料の膨化方法として、たばこ原料に
膨化助剤として有機溶媒を液状またはガス状で含浸さ
せ、たばこ組織内に浸透した有機溶媒を加熱・蒸発させ
る方法が知られている(例えば、特公昭47−2280
0号公報、同49−1879号公報、同52−3060
0号公報、特開昭61−15676号公報等)。これら
方法は、たばこの膨化率については満足できるものであ
るが、使用する溶媒によっては、コストが高くなり、ま
たたばこの香喫味に悪影響を及ぼす恐れがある。As a method for expanding the tobacco raw material, a method is known in which the tobacco raw material is impregnated with an organic solvent as a expansion aid in a liquid or gaseous state, and the organic solvent permeated into the tobacco tissue is heated and evaporated (for example, Japanese Patent Publication No. 47-2280
No. 0, No. 49-1879, No. 52-3060.
No. 0, JP 61-15676, etc.). These methods are satisfactory with respect to the swelling rate of cigarettes, but they are costly depending on the solvent used and may adversely affect the flavor and taste of cigarettes.
膨化助剤として液化二酸化炭素を用いる方法も知られて
いる(特公昭53−29000号公報、同56−302
1号公報、同56−50830号公報、特開昭55−1
65793号公報等)が、この方法は、たばこ組織に液
状二酸化炭素をかなり高い圧力の下で含浸させ、含浸し
た液状二酸化炭素を固体二酸化炭素に変換した後、固体
二酸化炭素を蒸発させる工程を含むものであるので、た
ばこ原料中の溶解性成分の流出をきたし、また加熱膨化
時の温度も高く、香喫味に悪影響を及ぼすという問題が
ある。A method using liquefied carbon dioxide as a swelling aid is also known (Japanese Patent Publication Nos. 53-29000 and 56-302).
1, JP-A-56-50830, JP-A-55-1.
No. 65793), this method includes a step of impregnating a tobacco tissue with liquid carbon dioxide under a considerably high pressure, converting the impregnated liquid carbon dioxide into solid carbon dioxide, and then evaporating the solid carbon dioxide. Therefore, there is a problem that the soluble components in the tobacco raw material flow out and the temperature at the time of heat expansion is high, which adversely affects the flavor and taste.
これに対し、ガス状二酸化炭素を膨化助剤として用いる
方法が、特公昭56−50952号に開示されている。
この方法は、たばこ原料に高圧条件の下でガス状二酸化
炭素を含浸させ、圧力を開放した後、急速加熱してたば
こ原料を膨化させるものである。ガス状二酸化炭素含浸
時の圧力は、17.6kg/cm2以上と記載されている
が、実用的には、28〜56kg/cm2程度特に40kg/c
m2を越える圧力を用いないと効果がないことが判明して
いる。また、加熱膨化時の温度も100〜370℃とさ
れているが、実際的には、250℃を越える温度を用い
ないと充分な膨化率が得られないことも判明している。
このような高い温度でたばこ原料を処理すると、短時間
であっても、たばこ原料がこげたり、たばこ製品の香喫
味に悪影響を及ぼす。On the other hand, a method of using gaseous carbon dioxide as a swelling aid is disclosed in JP-B-56-50952.
According to this method, a tobacco raw material is impregnated with gaseous carbon dioxide under a high pressure condition, the pressure is released, and then the tobacco raw material is rapidly heated to expand the tobacco raw material. The pressure when impregnating gaseous carbon dioxide is described as 17.6 kg / cm 2 or more, but practically, it is about 28 to 56 kg / cm 2, especially 40 kg / c 2.
It has been found to be ineffective without using pressures above m 2 . Further, the temperature at the time of heat expansion is set to 100 to 370 ° C., but it has been found that a sufficient expansion rate cannot be obtained unless a temperature exceeding 250 ° C. is actually used.
When the tobacco raw material is treated at such a high temperature, the tobacco raw material burns and the aroma and flavor of the tobacco product are adversely affected even in a short time.
したがって、この発明の主目的は、加熱膨化時の温度が
比較的低い条件下においても充分に高い膨化率を得るこ
とができ、しかもたばこの香喫味に悪影響を与えずにた
ばこ原料を膨化するための方法を提供することにある。Therefore, the main object of the present invention is to obtain a sufficiently high expansion rate even under conditions where the temperature during heat expansion is relatively low, and to expand the tobacco raw material without adversely affecting the flavor and taste of the tobacco. Is to provide a method.
また、この発明の他の目的は、ガス状二酸化炭素含浸時
の圧力が比較的低く、その時間を短縮することができる
たばこ原料の膨化方法を提供することにある。Another object of the present invention is to provide a method for expanding a tobacco raw material, in which the pressure during impregnation of gaseous carbon dioxide is relatively low and the time can be shortened.
この発明においては、たばこ原料にまずエタノールを含
浸させ、しかる後圧力容器内で二酸化炭素ガスをたばこ
原料に含浸させる。ついで、圧力容器の圧力を開放し、
得られたエタノール−二酸化炭素ガス含浸たばこ原料を
熱処理に供してエタノールおよび二酸化炭素を除去する
とたばこ原料が膨化する。In the present invention, the tobacco raw material is first impregnated with ethanol, and thereafter the carbon dioxide gas is impregnated with the carbon dioxide gas in the pressure vessel. Then release the pressure in the pressure vessel,
When the obtained ethanol-carbon dioxide gas-impregnated tobacco raw material is subjected to heat treatment to remove ethanol and carbon dioxide, the tobacco raw material swells.
本発明者らは、比較的低い二酸化炭素ガス含浸圧力、比
較的短い二酸化炭素ガス含浸時間、および(または)比
較的低い加熱膨化および温度条件下においても充分に高
い膨化率を得ることができ、たばこの香喫味に悪影響を
与えずにたばこ原料を膨化するための方法を開発すべく
鋭意研究した。その結果、たばこ原料を、まず、水との
親和性がよく水より二酸化炭素ガスの溶解度の高いエタ
ノールで処理すると、たばこ組織内のエタノールに溶解
し含浸される二酸化炭素ガスのため、後の二酸化炭素ガ
ス含浸を低い圧力で短時間おこないおよび(または)そ
の後の加熱膨化処理を低い温度でおこなってもエタノー
ル単独または二酸化炭素ガス単独では得られない高い膨
化率を達成でき、たばこ原料の香喫味に悪影響を及ぼす
ことがないように膨化をおこなうことができることを見
出してこの発明を完成するに至った。We can obtain a sufficiently high expansion rate even under relatively low carbon dioxide gas impregnation pressure, relatively short carbon dioxide gas impregnation time, and / or relatively low heat expansion and temperature conditions, An intensive study was conducted to develop a method for expanding a tobacco raw material without adversely affecting the flavor and taste of tobacco. As a result, if the tobacco raw material is first treated with ethanol, which has a good affinity for water and a higher solubility of carbon dioxide gas than water, it is dissolved in ethanol in the tobacco tissue and impregnated with carbon dioxide gas. Even if carbon gas impregnation is carried out at low pressure for a short time and / or subsequent heat expansion treatment at low temperature, it is possible to achieve a high expansion rate that cannot be obtained with ethanol alone or carbon dioxide gas alone. The inventors have completed the present invention by finding that they can be expanded without adversely affecting them.
この発明の方法によって膨化されるべきたばこ原料は、
黄色種、バーレーその他の種類のたばこ葉、中骨などで
あり、これらは、膨化処理後に刻む必要がないように予
め刻んだ状態にしておくのが望ましい。たばこ原料は、
通常、5重量%ないし30重量%の割合で水分を含んで
いる。以後述べる膨化条件にもよるが、実用的には、た
ばこ原料の含水量は、8重量%ないし23重量%である
ことが好ましい。The tobacco raw material to be puffed by the method of the present invention,
These include yellow varieties, burley and other types of tobacco leaves, middle bones and the like, which are preferably pre-cut so that they do not need to be cut after the expansion process. Tobacco ingredients are
It usually contains water in a proportion of 5% to 30% by weight. Practically, the water content of the tobacco raw material is preferably 8% by weight to 23% by weight, although it depends on the expansion conditions described below.
この発明の方法においては、たばこ原料に、まず、エタ
ノールを含浸透させる。このエタノール含浸透は、たば
こ原料をエタノール中に浸漬するか、またはたばこ原料
にエタノールを噴霧することによっておこなうことがで
きる。エタノール浸漬または噴霧後、たばこ原料を浸漬
浴から取り出しあるいは噴霧を停止し、エタノールがな
るべく蒸発しない温度および雰囲気の下で例えば1分な
いし数時間好ましくは1時間以内放置してエタノールを
たばこ組織内に浸透させる。この放置時間は、1時間以
内で充分である。エタノールは乾燥たばこ原料重量に対
して4%DB(ドライベース)以上100%DBまでの
割合、経済性を考慮すると好ましくは8%DBないし3
0%DBの割合で含浸されていることが好ましい。この
エタノール含浸濃度は、たばこ原料に対するエタノール
の添加量にほぼ対応し得る。In the method of the present invention, the tobacco raw material is first impregnated with ethanol. This ethanol impregnation can be performed by immersing the tobacco raw material in ethanol or by spraying the tobacco raw material with ethanol. After dipping or spraying with ethanol, the tobacco raw material is taken out of the dipping bath or spraying is stopped, and the ethanol is allowed to stand in the tobacco tissue for 1 minute to several hours, preferably within 1 hour under a temperature and an atmosphere in which ethanol does not evaporate as much as possible. Infiltrate. This leaving time of 1 hour or less is sufficient. Ethanol is preferably 8% DB to 3 in consideration of the ratio of 4% DB (dry base) to 100% DB based on the weight of the dry tobacco raw material, and economical efficiency.
It is preferably impregnated at a rate of 0% DB. This ethanol impregnation concentration can roughly correspond to the amount of ethanol added to the tobacco raw material.
エタノール含浸たばこ原料は、ついで、これを二酸化炭
素ガスの含浸工程に移行させる。その際、エタノール含
浸たばこ原料を、外側にジャケットを有する圧力容器内
に仕込む。二酸化炭素ガスの含浸に際しては、圧力容器
のジャケット内に熱交換媒体を循環させ、二酸化炭素を
ガス状に維持するに充分な圧力、温度条件(エタノール
含浸濃度が低い場合には、望ましくは、ガス圧を飽和点
またはその近くに保持し得る温度条件)の下に圧力容器
に二酸化炭素ガスを供給し、上記条件にエタノール含浸
たばこ原料を15秒ないし30分間置くことによって所
望の含浸が達成できる。二酸化炭素ガス含浸時の温度と
しては、通常、−55℃ないし50℃好ましくは−25
℃ないし50℃の温度を用いることができる。二酸化炭
素ガスはたばこ原料に1重量%以上の割合で含浸されて
いることが好ましい。The ethanol-impregnated tobacco raw material is then transferred to the carbon dioxide gas impregnation step. At that time, the ethanol-impregnated tobacco raw material is charged in a pressure vessel having an outer jacket. When impregnating carbon dioxide gas, a heat exchange medium is circulated in the jacket of the pressure vessel, and pressure and temperature conditions sufficient to maintain carbon dioxide in a gaseous state (when the ethanol impregnation concentration is low, preferably gas The desired impregnation can be achieved by supplying carbon dioxide gas to the pressure vessel under a temperature condition where the pressure can be maintained at or near the saturation point) and placing the ethanol-impregnated tobacco raw material for 15 seconds to 30 minutes under the above conditions. The temperature for impregnating carbon dioxide gas is usually -55 ° C to 50 ° C, preferably -25.
Temperatures between 0 ° C and 50 ° C can be used. Carbon dioxide gas is preferably impregnated in the tobacco raw material at a ratio of 1% by weight or more.
二酸化炭素ガスによる含浸が終ったら、圧力を開放し、
エタノール−二酸化炭素ガス含浸たばこ原料を取り出
す。圧力の開放は、圧力容器の容積および圧力にもよる
が、通常おこなわれているバルブ操作による排気によっ
て、1秒ないし10分間でおこなうことができる。When the impregnation with carbon dioxide gas is complete, release the pressure,
Take out the tobacco raw material impregnated with ethanol-carbon dioxide gas. The pressure can be released in 1 second to 10 minutes by exhausting the valve operation which is usually performed, though it depends on the volume and pressure of the pressure vessel.
取り出したエタノール−二酸化炭素ガス含浸たばこ原料
を、熱処理に供することによってエタノールおよび二酸
化炭素ガスを除去してたばこ原料を膨化させる工程に移
行する。この膨化工程への移行は、エタノールや二酸化
炭素ガスがたばこ原料からできるだけ散逸しないように
短時間の内におこなうことが好ましい。たばこ原料の膨
化熱処理は、通常100℃以上、好ましくは125℃な
いし225℃の温度に加熱された空気、水蒸気またはそ
の混合物からなる気流にエタノール−二酸化炭素ガス含
浸たばこ原料を、エタノールおよび二酸化炭素ガスの除
去によりたばこ原料が膨化するに充分な時間さらすこと
(気流乾燥)によって最も都合よくおこなうことができ
る。この膨化熱処理は、通常、1秒ないし30秒間で達
成できる。The extracted ethanol-carbon dioxide gas-impregnated tobacco raw material is subjected to a heat treatment to remove ethanol and carbon dioxide gas, and the tobacco raw material is expanded. The transition to the expansion step is preferably performed within a short time so that ethanol and carbon dioxide gas are not scattered as much as possible from the tobacco raw material. The puffing heat treatment of the tobacco raw material is carried out by heating the tobacco raw material impregnated with ethanol-carbon dioxide gas into a stream of air, steam or a mixture thereof heated to a temperature of usually 100 ° C. or higher, preferably 125 ° C. to 225 ° C. This can be most conveniently carried out by exposing the tobacco material to a time sufficient for the tobacco material to swell by removal of (gas stream drying). This swelling heat treatment can usually be accomplished in 1 to 30 seconds.
上記のようにたばこ原料にまずエタノールを含浸させる
と、二酸化炭素ガス含浸時の圧力が15〜30kg/cm2
と低くしかも膨化熱処理時の気流温度がたばこ原料の香
喫味に影響を及ぼさない温度である200℃以下とい
う、二酸化炭素ガスのみの含浸では充分に膨化できない
条件であっても充分に高い膨化率(以後定義する)を達
成でき、しかもたばこ原料の香喫味に悪影響を及ぼすこ
とがない。加えて、用いるエタノールおよび二酸化炭素
ガスは、たばこ原料の香喫味になんら悪影響を及ぼさな
い。なお、膨化率だけの観点からみれば、熱処理温度は
もっと高い方(例えば、350℃までの温度)が効果的
であるが、既に述べたように、温度が高すぎると、処理
時間が短くてもこげ臭等が生じてたばこ原料の香喫味に
悪影響を与える。また、二酸化炭素含浸圧力は30kg/
cm2以上であっても同様に高い膨化率を示す。さらに、
エタノールの代りに他の低級脂肪族アルコール、アセト
ン酢酸、ベンゼン、四塩化炭素を用いることもできる
が、これら物質はたばこ原料の香喫味等に悪影響を及ぼ
すのでここでは用いない。When the tobacco raw material is first impregnated with ethanol as described above, the pressure during carbon dioxide gas impregnation is 15 to 30 kg / cm 2.
It is low and the swelling rate is sufficiently high even under the condition that the temperature of the airflow during the swelling heat treatment is 200 ° C. or lower, which is a temperature at which the flavor and taste of the tobacco raw material is not affected, that is, the swelling cannot be sufficiently swelled by only carbon dioxide gas impregnation ( (To be defined hereinafter) can be achieved, and the flavor and taste of the tobacco raw material is not adversely affected. In addition, the ethanol and carbon dioxide gas used do not have any adverse effect on the flavor and taste of the tobacco raw material. From the viewpoint of the expansion rate alone, it is effective to use a higher heat treatment temperature (for example, a temperature up to 350 ° C.), but as described above, if the temperature is too high, the treatment time is short. A smoky odor is produced, which adversely affects the flavor and taste of the tobacco raw material. The carbon dioxide impregnation pressure is 30 kg /
Even if it is cm 2 or more, it also shows a high swelling rate. further,
Other lower aliphatic alcohols, acetone acetic acid, benzene and carbon tetrachloride can be used in place of ethanol, but these substances are not used here because they adversely affect the flavor and taste of the tobacco raw material.
ここで、膨化率は、膨化させようとするたばこ原料の見
掛け密度(ρ0)を、膨化後のたばこ原料の見掛け密度
(ρ)で除した商(ρ0/ρ)と定義される。この発明
によれば、上記のような低圧・低温条件下でも、エタノ
ール単独または二酸化炭素ガス単独では得られない2.
0以上の膨化率を達成できる。Here, the expansion rate is defined as the quotient (ρ 0 / ρ) obtained by dividing the apparent density (ρ 0 ) of the tobacco raw material to be expanded by the apparent density (ρ) of the tobacco raw material after expansion. According to the present invention, ethanol cannot be obtained alone or carbon dioxide gas alone cannot be obtained even under the above-mentioned low pressure and low temperature conditions.
A swelling rate of 0 or more can be achieved.
実施例 1 水分が14%で、水銀圧入法(測定圧力250kg/cm2a
bs)で測定した見掛け密度ρ0が0.887g/cm3の黄
色種の刻みたばこ原料300gにエタノールを9.5g
重量%または30g重量%噴霧し30分間蔵置した。こ
のエタノール含浸たばこ原料を、外側ジャケット内に熱
交換媒体を循環させて約0℃に保持した内容積4リット
ルの圧力容器に仕込み、二酸化炭素ガスを導入して25
kg/cm2に加圧した。この条件の下で10分間二酸化炭
素ガスの含浸をおこなった。しかる後、圧力を開放し
た。圧力開放時間は約30秒であった。エタノール−二
酸化炭素ガス含浸たばこ原料を圧力容器から取り出し、
これを直ちに、下記表1に示す温度の加熱空気が20m
/秒の流速で流れる気流乾燥機に入れ、5秒間で取り出
すことによって膨化させた。Example 1 With a water content of 14%, mercury porosimetry (measurement pressure 250 kg / cm 2 a
9.5 g of ethanol was added to 300 g of yellow-cut tobacco material having an apparent density ρ 0 of 0.887 g / cm 3 measured in bs).
It was sprayed with 30% by weight or 30% by weight and stored for 30 minutes. The ethanol-impregnated tobacco raw material was charged into a pressure vessel having an internal volume of 4 liters, which was maintained at about 0 ° C. by circulating a heat exchange medium in the outer jacket, and carbon dioxide gas was introduced into the pressure vessel.
Pressurized to kg / cm 2 . Under this condition, carbon dioxide gas was impregnated for 10 minutes. Then, the pressure was released. The pressure release time was about 30 seconds. Remove the ethanol-carbon dioxide gas impregnated tobacco raw material from the pressure vessel,
Immediately, 20m of heated air at the temperature shown in Table 1 below
It was swelled by putting it in an air flow dryer flowing at a flow rate of / sec and taking it out for 5 seconds.
こうして得た各たばこ原料を22℃、相対湿度60%の
恒温恒湿室に1週間蔵置して調和した。これら膨化たば
この見掛け密度ρを水銀圧入法により測定し、膨化率
(ρ0/ρ)を算出した。The respective tobacco raw materials thus obtained were stored for 1 week in a constant temperature and constant humidity chamber at 22 ° C. and a relative humidity of 60% for harmonization. The apparent density ρ of these expanded cigarettes was measured by the mercury intrusion method, and the expansion rate (ρ 0 / ρ) was calculated.
また、上記調和した各膨化たばこ原料を巻上げ、紙巻た
ばことし、10人の特に訓練された専門パネルにより香
喫味評価をおこなった。この官能試験においては、エタ
ノールも二酸化炭素ガスも含浸させず、温度150℃で
加熱膨化させた後、相対湿度60%に調和して巻上げ、
紙巻たばことしたものを対照品とした。香喫味は、対照
品と同等のものを0、やや優れているものを+1、かな
り優れているものを+2、極めて優れているものを+
3、やや劣っているものを−1、かなり劣っているもの
を−2、極めて劣っているものを−3として評価してあ
る。In addition, each of the harmonized tobacco raw materials was rolled up, cigarettes were wrapped, and the flavor and taste was evaluated by a specially trained expert panel of 10 people. In this sensory test, neither ethanol nor carbon dioxide gas was impregnated, heated and expanded at a temperature of 150 ° C., and then rolled up in harmony with a relative humidity of 60%,
A cigarette was used as a control. The flavor and aroma are the same as the control product, 0, slightly superior, +1, considerably superior, +2, extremely superior, +
3 is evaluated as being slightly inferior, -1 is considerably inferior, and -2 is extremely inferior.
なお、エタノール含浸処理をしない以外は全く同様の処
理により得た膨化たばこ原料についても同様に試験し
た。In addition, a puffed tobacco raw material obtained by the completely same treatment except that the ethanol impregnation treatment was not carried out was similarly tested.
以上の結果を表1に併記する。The above results are also shown in Table 1.
表1の結果から明らかなように、いずれの加熱膨化温度
においてもエタノール−二酸化炭素ガス含浸たばこ原料
は、二酸化炭素ガスのみの含浸たばこ原料と比較して優
れた膨化率を示している。二酸化炭素ガスのみの含浸た
ばこ原料は、表1に示す条件では高い膨化率を示さない
が、比較的高い膨化率を示す加熱膨化温度条件において
は香喫味にこげ臭が発現する。これに対し、エタノール
−二酸化炭素ガス含浸たばこ原料は、比較的低い加熱膨
化温度においても高い膨化率を示し、かつこげ臭の発現
もみられなかった。また、加熱膨化温度200℃から2
25℃では二酸化炭素ガスのみの含浸たばこ原料にはこ
げ臭が発現したのに対し、エタノール−二酸化炭素含浸
たばこ原料ではこげ臭の発現はみられなかった。これは
エタノールの蒸発潜熱により二酸化炭素ガスのみの含浸
たばこに比較して品温を低くできるためであると考えら
れる。 As is clear from the results of Table 1, the ethanol-carbon dioxide gas-impregnated tobacco raw material exhibits an excellent expansion rate at any heating and expansion temperature as compared with the carbon dioxide gas-impregnated tobacco raw material. The tobacco raw material impregnated only with carbon dioxide gas does not show a high expansion rate under the conditions shown in Table 1, but under the heating expansion temperature conditions showing a relatively high expansion rate, a fragrant taste and a dark odor are developed. On the other hand, the tobacco raw material impregnated with ethanol-carbon dioxide gas exhibited a high expansion rate even at a relatively low heating expansion temperature, and did not exhibit a burning odor. Also, the heating and swelling temperature of 200 ° C. to 2
At 25 ° C., a burning odor was exhibited in the tobacco raw material impregnated with carbon dioxide gas only, whereas no burning odor was observed in the ethanol raw material impregnated with carbon dioxide. It is considered that this is because the product temperature can be lowered by the latent heat of vaporization of ethanol as compared with a cigarette impregnated with only carbon dioxide gas.
実施例 2. 実施例1で用いたものと同様のたばこ原料を圧力容器に
仕込み、下記表2に示す圧力および温度条件で10分間
二酸化炭素ガス含浸をおこなった。しかる後、圧力を開
放し、たばこ原料を圧力容器から取り出し、これを直ち
に150℃の加熱空気が20m/秒の流速で流れる気流
乾燥機に入れ、5秒間で取り出した。こうして得た各膨
化たばこ原料の膨化率を実施例1と同様に算出した。結
果を表2に併記する。Example 2. The same tobacco raw material as that used in Example 1 was charged into a pressure vessel, and carbon dioxide gas impregnation was performed for 10 minutes under the pressure and temperature conditions shown in Table 2 below. Thereafter, the pressure was released, the tobacco raw material was taken out of the pressure vessel, immediately put in an air flow dryer in which heated air at 150 ° C. at a flow rate of 20 m / sec, and taken out for 5 seconds. The expansion rate of each expanded tobacco raw material thus obtained was calculated in the same manner as in Example 1. The results are also shown in Table 2.
表2から明らかなように、いずれの含浸条件においても
エタノール−二酸化炭素ガス含浸たばこは、二酸化炭素
ガスのみの含浸たばこと比較して優れた膨化率を示し
た。また、含浸圧力が30kg/cm2以下の低い圧力条件
でも充分に満足できる膨化率を示した。 As is clear from Table 2, the cigarettes impregnated with ethanol-carbon dioxide gas showed excellent expansion rates under all impregnation conditions as compared with the cigarettes impregnated with carbon dioxide gas only. Further, the swelling rate was sufficiently satisfactory even under a low pressure condition of the impregnation pressure of 30 kg / cm 2 or less.
実施例 3 実施例1で用いた黄色種たばこ原料にエタノールを噴霧
して10分間蔵置し、下記表3に示す種種のエタノール
含浸量のたばこ原料を得た。各エタノール含浸たばこ原
料を、直ちに、圧力容器に仕込み、表3に示す含浸条件
で二酸化炭素ガスの含浸をおこなった。しかる後、圧力
を開放してエタノール−二酸化炭素ガス含浸たばこ原料
を圧力容器から取り出し、これを直ちに、150℃の加
熱空気が20m/秒の流速で流れる気流乾燥機に入れ、
5秒間で取り出すことによって膨化させた。こうして得
た各膨化たばこ原料の膨化率を実施例1と同様に算出し
た。結果を表3に併記する。Example 3 The yellow seed tobacco raw material used in Example 1 was sprayed with ethanol and stored for 10 minutes to obtain a tobacco raw material having ethanol impregnated amounts of the various seeds shown in Table 3 below. Each ethanol-impregnated tobacco raw material was immediately charged into a pressure vessel and impregnated with carbon dioxide gas under the impregnation conditions shown in Table 3. Then, the pressure was released, and the ethanol-carbon dioxide gas-impregnated tobacco raw material was taken out from the pressure vessel, and immediately put into a gas stream dryer in which heated air at 150 ° C flows at a flow rate of 20 m / sec.
It was swelled by taking it out for 5 seconds. The expansion rate of each expanded tobacco raw material thus obtained was calculated in the same manner as in Example 1. The results are also shown in Table 3.
表3の結果から明らかなように、エタノール−二酸化炭
素ガス含浸たばこ原料は、二酸化炭素ガスのみの含浸た
ばこと比較して、いずれのエタノール含浸量においても
優れた膨化率を示した。 As is clear from the results in Table 3, the ethanol-carbon dioxide gas-impregnated tobacco raw material exhibited an excellent expansion rate at any ethanol impregnation amount as compared with the carbon dioxide gas-impregnated tobacco raw material.
実施例 4 実施例1で用いたものと同様の黄色種たばこ原料に対
し、下記表4に示す条件でエタノール含浸および二酸化
炭素ガス含浸並びに加熱膨化をおこなった。得られた各
膨化たばこ原料の膨化率を表4に併記する。Example 4 The same yellow seed tobacco material as that used in Example 1 was impregnated with ethanol and carbon dioxide gas and heated and expanded under the conditions shown in Table 4 below. Table 4 also shows the expansion rates of the obtained expanded tobacco raw materials.
表4の結果から明らかなように、エタノールを含浸させ
たたばこ原料は、5分以上の二酸化炭素ガス含浸時間で
優れた膨化率を示すのに対し、エタノールを含浸させて
いないたばこ原料は、充分な膨化率を達成するためには
二酸化炭素ガス含浸時間に長時間を要する。 As is clear from the results shown in Table 4, the tobacco raw material impregnated with ethanol exhibits an excellent expansion rate at a carbon dioxide gas impregnation time of 5 minutes or more, whereas the tobacco raw material not impregnated with ethanol is sufficient. It takes a long time to impregnate carbon dioxide gas in order to achieve a high expansion rate.
実施例 5 バーレー種たばこ原料を用いて、下記表5に示す条件で
エタノール含浸および二酸化炭素ガス含浸並びに加熱膨
化をおこなった。各膨化たばこの膨化率を表5に併記す
る。Example 5 Using a Burley type tobacco raw material, ethanol impregnation and carbon dioxide gas impregnation and heat expansion were performed under the conditions shown in Table 5 below. The expansion rate of each expanded cigarette is also shown in Table 5.
表5の結果から明らかなように、この発明の方法は、バ
ーレー種に対しても優れた効果を奏する。 As is clear from the results in Table 5, the method of the present invention has excellent effects on Burley seeds.
実施例 6 含浸ガスとして空気または二酸化炭素ガスを用い、下記
表6に示す条件で膨化処理をおこなった。結果を表6に
併記する。Example 6 Using air or carbon dioxide gas as the impregnating gas, expansion treatment was performed under the conditions shown in Table 6 below. The results are also shown in Table 6.
表6の結果から明らかなように、まずエタノールを含浸
させ、しかる後二酸化炭素ガスを含浸させることによっ
てのみ優れた膨化率が達成できる。 As is clear from the results of Table 6, an excellent expansion rate can be achieved only by first impregnating with ethanol and then impregnating carbon dioxide gas.
実施例 7 実施例1で用いたものと同様のたばこ原料に表7に示す
種々の濃度でエタノール(EtOH)を含浸させ、25kg/cm
2の圧力下で表7に示す温度にて10分間二酸化炭素を
含浸させた。各膨化たばこの膨化率を表7に併記する。Example 7 Tobacco raw materials similar to those used in Example 1 were impregnated with ethanol (EtOH) at various concentrations shown in Table 7, and 25 kg / cm
Carbon dioxide was impregnated under the pressure of 2 at the temperature shown in Table 7 for 10 minutes. Table 7 also shows the expansion rate of each expanded cigarette.
表7に示す結果から明らかなように、二酸化炭素の含浸
温度が飽和点に近い程、膨化率は優れているが、エタノ
ール含浸濃度が高くなるにしたがって二酸化炭素ガス含
浸温度が高くても二酸化炭素ガス含浸温度が飽和点に近
い条件と同じ膨化率を示す。これはエタノールに対する
二酸化炭素ガスの溶解度が高いためである。エタノール
含浸濃度が30%以上であれば20℃以下の温度で膨化
率はほぼ同じであり、またエタノール含浸濃度15〜2
0%ではほぼ同様の膨化傾向を示す。 As is clear from the results shown in Table 7, the closer the carbon dioxide impregnation temperature is to the saturation point, the better the swelling rate, but as the ethanol impregnation concentration increases, the carbon dioxide gas impregnation temperature increases even if the carbon dioxide impregnation temperature increases. It shows the same swelling rate as the gas impregnation temperature is close to the saturation point. This is because the carbon dioxide gas has a high solubility in ethanol. If the ethanol impregnation concentration is 30% or more, the swelling rate is almost the same at a temperature of 20 ° C. or less, and the ethanol impregnation concentration is 15 to 2
At 0%, almost the same swelling tendency is exhibited.
以上述べたように、この発明のたばこ原料の膨化方法に
よれば、比較的低い二酸化炭素ガス含浸圧力、比較的短
い二酸化炭素ガス含浸時間および(または)比較的低い
加熱膨化および温度条件下においても充分に高い膨化率
を得ることができ、したがってたばこの香喫味に悪影響
を与えずにたばこ原料を膨化させることができる。As described above, according to the method for expanding a tobacco raw material of the present invention, even under relatively low carbon dioxide gas impregnation pressure, relatively short carbon dioxide gas impregnation time and / or relatively low heat expansion and temperature conditions. A sufficiently high puffing rate can be obtained, and thus the tobacco raw material can be puffed without adversely affecting the flavor and taste of the cigarette.
Claims (1)
ルを含浸させ、このエタノール含浸たばこ原料を圧力容
器に仕込み、該圧力容器に二酸化炭素ガスを導入するこ
とによって加圧下に二酸化炭素ガスを該エタノール含浸
たばこ原料に含浸させ、しかる後該圧力容器の圧力を開
放し、得られたエタノール−二酸化炭素ガス含浸たばこ
原料を熱処理に供してたばこ原料からエタノールおよび
二酸化炭素ガスを除去することによりたばこ原料を膨化
させることを特徴とするたばこ原料の膨化方法。1. A tobacco raw material to be expanded is impregnated with ethanol, the ethanol-impregnated tobacco raw material is charged into a pressure vessel, and carbon dioxide gas is introduced into the pressure vessel to apply the carbon dioxide gas under pressure to the ethanol. The tobacco raw material is impregnated with the impregnated tobacco raw material, and then the pressure of the pressure vessel is released, and the obtained ethanol-carbon dioxide gas impregnated tobacco raw material is subjected to heat treatment to remove ethanol and carbon dioxide gas from the tobacco raw material to obtain a tobacco raw material. A method for expanding a tobacco raw material, which comprises expanding.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP4670587A JPH0659199B2 (en) | 1987-03-03 | 1987-03-03 | How to puff tobacco material |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP4670587A JPH0659199B2 (en) | 1987-03-03 | 1987-03-03 | How to puff tobacco material |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS63214172A JPS63214172A (en) | 1988-09-06 |
JPH0659199B2 true JPH0659199B2 (en) | 1994-08-10 |
Family
ID=12754779
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP4670587A Expired - Lifetime JPH0659199B2 (en) | 1987-03-03 | 1987-03-03 | How to puff tobacco material |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH0659199B2 (en) |
-
1987
- 1987-03-03 JP JP4670587A patent/JPH0659199B2/en not_active Expired - Lifetime
Also Published As
Publication number | Publication date |
---|---|
JPS63214172A (en) | 1988-09-06 |
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