JPH0115276B2 - - Google Patents
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- Publication number
- JPH0115276B2 JPH0115276B2 JP61104345A JP10434586A JPH0115276B2 JP H0115276 B2 JPH0115276 B2 JP H0115276B2 JP 61104345 A JP61104345 A JP 61104345A JP 10434586 A JP10434586 A JP 10434586A JP H0115276 B2 JPH0115276 B2 JP H0115276B2
- Authority
- JP
- Japan
- Prior art keywords
- distillation
- heating
- steam
- cylinder
- shochu
- 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
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- Alcoholic Beverages (AREA)
- Distillation Of Fermentation Liquor, Processing Of Alcohols, Vinegar And Beer (AREA)
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Description
【発明の詳細な説明】
[産業上の利用分野]
本発明は、焼酎醪(モロミ)等の酒成分を含む
原液を減圧状態にして煮沸し蒸溜する焼酎等の減
圧単式蒸溜装置に関するものである。[Detailed Description of the Invention] [Industrial Application Field] The present invention relates to a vacuum single-type distillation device for shochu, etc., which distills a stock solution containing liquor components, such as shochu moromi, under reduced pressure by boiling it. .
[従来の技術]
焼酎等の蒸溜に使用する減圧単式蒸溜装置とし
ては、煮沸用の蒸溜缶の周囲部に周壁を被うジヤ
ケツト部を設け、このジヤケツト部に加熱蒸気を
供給して蒸溜缶内の焼酎醪等の原液を間接蒸煮し
沸騰させるようにしたジヤケツト型の外部加熱方
式の蒸溜装置(例えば特開昭52−34991号公報)、
あるいは蒸溜缶内に加熱蒸気を導入する内部加熱
方式の蒸溜装置(例えば特公昭60−22905号公報)
がある。[Prior Art] A vacuum single distillation device used for distilling shochu, etc., is equipped with a jacket part that covers the peripheral wall of a distillation can for boiling, and heated steam is supplied to this jacket part to heat the inside of the distillation can. A jacket-type external heating distillation device that indirectly steams and boils a stock solution such as shochu moromi (for example, Japanese Patent Application Laid-Open No. 1983-34991);
Alternatively, an internal heating type distillation device that introduces heated steam into the distillation can (for example, Japanese Patent Publication No. 60-22905)
There is.
[発明が解決しようとする問題点]
上記のような減圧単式蒸溜装置においては、加
熱方式が蒸気による間接加熱によるものであるた
め、内部の原液が充分に撹拌されなかつたり、加
熱伝熱面積が小さいと、蒸発時間が長くなり、蒸
溜効率が悪くなるので、加熱伝熱面積をできるだ
け大きくしてかつ原液を適度に撹拌しつつ加熱す
ることが望まれる。[Problems to be solved by the invention] In the vacuum single distillation apparatus as described above, the heating method is indirect heating using steam, so the stock solution inside may not be sufficiently stirred, or the heating heat transfer area may be insufficient. If it is small, the evaporation time will be long and the distillation efficiency will be poor, so it is desirable to make the heating heat transfer area as large as possible and to heat the stock solution while stirring it appropriately.
上記従来例の外部加熱方式の蒸溜装置の場合合
には、蒸溜缶内の原液が外周部分から加熱される
ため、内部の原液を撹拌しないと内方部分が充分
に加熱されないことになり、だからといつて撹拌
装置を装備するのは真空度保持等の関係でその構
造が複雑化し、設備費が高くなる。しかも、蒸溜
が進むに伴つて製品が蒸溜物として溜出し、蒸溜
缶内の原液が漸次減少して蒸溜缶内の液面が低下
し、ジヤケツト部上端より低位の位置に来ると、
原液と上部気体の境界付近いおいて焦げ付き現象
が生じ、その結果蒸溜製品に焦臭が付き、製品不
良が生じることになる。またジヤケツト部におい
てその内壁である蒸溜缶内に吹き込み蒸気のため
の外圧力が作用するとともに蒸溜缶内の減圧によ
る内方への引張力が働き、あまり高圧の蒸気をジ
ヤケツト部に吹き込むことが因難である。そのた
め従来はゲージ圧力2Kg/cm2の蒸気が実用上の最
大のものとされており、操作上の手違い等でこれ
以上の高圧蒸気が吹き込まれて、蒸溜缶が破損す
るような事故も起つている。 In the case of the above-mentioned conventional external heating type distillation apparatus, the stock solution inside the still is heated from the outer circumference, so unless the stock solution inside is stirred, the inner part will not be heated sufficiently. However, the provision of a stirring device complicates the structure due to the need to maintain the degree of vacuum, and increases equipment costs. Moreover, as the distillation progresses, the product is distilled out as a distillate, and the stock solution in the distiller gradually decreases, causing the liquid level in the still to drop to a position lower than the top of the jacket.
A scorching phenomenon occurs near the boundary between the raw solution and the upper gas, resulting in a burnt odor in the distilled product and product defects. In addition, external pressure for the steam blown into the jacket acts on the inner wall of the still can, and an inward tensile force acts due to the reduced pressure inside the still can, causing too much high-pressure steam to be blown into the jacket. It is difficult. For this reason, steam with a gauge pressure of 2 kg/cm 2 has traditionally been considered the maximum in practical use, and accidents such as higher pressure steam being blown into the still can occur due to operational errors. There is.
また上記従来例の内部加熱方式の場合には、蒸
溜缶の内部に導入した蒸気管の周囲に上下が閉塞
された蒸気室が設けられるとともに、この蒸気室
にはこれを上下に貫通する原液の導通管が配設さ
れ、この導通管内を原液が流通することにより加
熱されるものであるが、前記導通管が比較的細く
かつ導通管以外の部分では対流が充分に行なわれ
ない結果となつており、そのため原液の煮沸蒸発
に時間がかかり、蒸溜効率が低くなつている。 In addition, in the case of the conventional internal heating method described above, a steam chamber is provided around the steam pipe introduced into the still can, and the steam chamber is closed at the top and bottom. A conduit is provided, and the raw solution is heated by flowing through the conduit, but the conduit is relatively thin and convection is not sufficient in areas other than the conduit. Therefore, it takes time to boil and evaporate the stock solution, resulting in low distillation efficiency.
特に蒸溜缶の容量が大きくなればなるほど、蒸
溜缶内に収容される原液の量も多く、蒸溜缶内の
外壁側の液が加熱され難く、均等な煮沸が行なえ
ず、醪中の夾雑物が蒸溜缶底部に沈澱すること等
もあつて、効率的な蒸溜が行なわれないことにな
り、酒成分が残液として蒸溜管内に残ることにな
る。 In particular, the larger the capacity of the distillation can, the larger the amount of stock liquid stored in the still, making it difficult to heat the liquid on the outer wall of the still, making it difficult to boil evenly, and contaminants in the moromi. It may also settle at the bottom of the still, preventing efficient distillation, and the liquor components will remain in the distillation tube as a residual liquid.
なお内部加熱方式のものとして、蒸気が流通す
る蛇管を蒸溜缶内に装備したものもあるにはある
が、この蛇管に原液中の夾雑物が付着し易く、ま
たこの蛇管自体のみでは充分な対流撹拌効果が得
られないものである。殊にこの種の単式蒸溜にお
いては、通常、良質の製品を得るために、あるい
は繰返し使用による加熱効率の低下を防ぐため
に、1回の蒸溜毎に缶内を清掃することとことと
されているが、前記のような蛇管よりなるもので
あると、その清掃作業が行ない難く、特に蛇管表
面に付着等が生じた場合の除去作業がきわめて面
倒なものとなつている。 Although some internal heating systems are equipped with a coiled tube inside the can through which steam flows, contaminants in the stock solution tend to adhere to this coil, and the coil itself does not provide sufficient convection. The stirring effect cannot be obtained. Especially in this type of pot distillation, the inside of the can is usually cleaned after each distillation in order to obtain a high-quality product or to prevent a decrease in heating efficiency due to repeated use. However, if it is made of a corrugated tube as described above, it is difficult to clean it, and in particular, when there is adhesion on the surface of the corrugated tube, it is extremely troublesome to remove it.
本発明は、上記従来の欠点に鑑み、内部加熱方
式のものにおいて、構造簡単にしてしかも対流作
用および加熱、蒸発速度を良好になし、蒸溜効率
の非常に優れた焼酎等の減圧単式蒸溜装置を提供
しようとするものである。 In view of the above-mentioned conventional drawbacks, the present invention provides a single vacuum distillation device for distilling shochu, etc., which uses an internal heating type, has a simple structure, has good convection action, good heating and evaporation rates, and has very high distillation efficiency. This is what we are trying to provide.
[問題点を解決するための手段]
本発明は、原液を煮沸する蒸溜缶から製品タン
クに到る蒸溜経路を減圧状態にして焼酎等を蒸溜
する減圧単式蒸溜装置であつて、特に上記の問題
点を解決するために、前記蒸溜缶内の下方部に、
上下に開口した内筒とこれよりやや径大の外筒と
を上下端部で連接した2重筒構造をなしかつ両筒
間の上下端部を閉塞してその内部空間に加熱蒸気
を供給できるようにした加熱筒を、底部よりやや
上方位置に装備してなるものであり、内外2重筒
構造の加熱筒が対流筒を兼ねるようにしたことを
特徴とするものである。[Means for Solving the Problems] The present invention is a vacuum distillation device for distilling shochu and the like by reducing the pressure of the distillation path from the distillation can for boiling the stock solution to the product tank, and particularly solves the above-mentioned problems. In order to solve the problem, in the lower part of the distillation can,
It has a double cylinder structure in which an inner cylinder with an open top and bottom and an outer cylinder with a slightly larger diameter are connected at the upper and lower ends, and heating steam can be supplied to the internal space by closing the upper and lower ends between the two cylinders. This heating cylinder is installed at a position slightly above the bottom, and is characterized in that the heating cylinder with a double inner and outer cylinder structure also serves as a convection cylinder.
[作用]
上記の本発明の蒸溜装置においては、蒸溜缶の
内部において、蒸溜缶内の中央部に加熱源として
装備した加熱筒により焼酎醪等の原液を加熱する
もので、特に前記加熱筒は上下端部で連設した内
外2重筒よりなり、その両筒間の空間に蒸気が吹
き込まれる結果、内外両筒が原液に対する加熱伝
熱面となり、蒸溜缶内の原液は前記加熱筒の内外
両筒の双方により加熱されることになり、内部加
熱方式であつても加熱伝熱面積がかなり大きくな
る。しかも前記加熱筒はその軸心を上下方向にし
て底部よりやや上方位置に配してあるため、これ
により加熱される原液は加熱筒内部においては加
熱されて上昇し、加熱筒外方部分では蒸溜缶外壁
側からは加熱されないために下降することにな
り、これによつて図面矢印に示す方向の対流作用
が生じることになる。しかも原液が前記のように
常に対流作用を行なつているから、原液中の夾雑
物が加熱筒等の表面に付着したり、焦げ付きが生
じたりすることがない。[Function] In the above-mentioned distillation apparatus of the present invention, the undiluted liquid such as shochu moromi is heated inside the distillation can by a heating cylinder installed as a heating source in the center of the distillation can. It consists of double inner and outer cylinders connected at the upper and lower ends, and as a result of the steam being blown into the space between the two cylinders, both the inner and outer cylinders become a heating heat transfer surface for the concentrate, and the concentrate in the still is heated between the inside and outside of the heating cylinder. Heating is done by both cylinders, and even if it is an internal heating method, the heating heat transfer area becomes quite large. Moreover, since the heating cylinder is placed slightly above the bottom with its axis in the vertical direction, the stock solution heated by this is heated and rises inside the heating cylinder, and distills in the outside part of the heating cylinder. Since it is not heated from the outer wall of the can, it descends, resulting in a convection action in the direction shown by the arrow in the figure. Moreover, since the stock solution is constantly undergoing convection as described above, there is no possibility that impurities in the stock solution will adhere to the surface of the heating cylinder or the like, or that it will become scorched.
[実施例] 次に本発明の実施例を図面に基いて説明する。[Example] Next, embodiments of the present invention will be described based on the drawings.
1は焼酎醪等の酒成分を含む原液を煮沸する蒸
溜缶、2は前記蒸溜缶1の上部に接続されたスワ
ンネツク状の蒸気排出路3を介して接続された冷
却器であつて、蒸溜缶1より排出される蒸気がこ
の冷却器2内に有する蛇管4を流通する間に冷却
水によつて冷却され凝縮されるようになつてい
る。5は前記冷却器2に接続された製品タンクで
あつて、前記の冷却器2により凝縮されて排出さ
れる蒸溜物である焼酎等の製品はこの製品タンク
5に貯留される。また前記の蒸溜缶1から冷却器
2を経て製品タンク5に到る蒸溜経路6の一部、
例えば製品タンク5の部分には真空ポンプ7が接
続されており、蒸溜経路6を減圧状態にして蒸溜
できるようになつている。 Reference numeral 1 denotes a distillation can for boiling a stock solution containing liquor components such as shochu moromi, and 2 a cooler connected to the upper part of the distillation can 1 via a swanneck-shaped steam exhaust passage 3. Steam discharged from the cooler 2 is cooled and condensed by cooling water while flowing through a flexible pipe 4 included in the cooler 2. Reference numeral 5 denotes a product tank connected to the cooler 2, and products such as shochu, which is a distillate condensed and discharged by the cooler 2, are stored in the product tank 5. Also, a part of the distillation route 6 from the distillation can 1 to the product tank 5 via the cooler 2,
For example, a vacuum pump 7 is connected to the product tank 5 so that the distillation path 6 can be brought into a reduced pressure state for distillation.
10は上記の蒸溜缶1内の下方中央部に装備し
た内外2重筒構造の加熱筒であつて、上下に開口
した内管11と外筒12とが両筒間に通常10〜30
mm程度の間隔を存して上下端部で端板により連接
されるとともに、内外両筒11,12間の上下が
閉塞されてその内部空間が蒸気室13として形成
されており、この蒸気室13に蒸気供給管14が
接続され、加熱蒸気を吹き込めるように構成され
ている。またこの加熱筒10は上下方向に開口さ
せて蒸溜缶1の底部15との間に焼酎醪等の原液
の対流作用を許容する間隔を存するように底部1
5よりやや上方位置に配置されており、原液がこ
の加熱筒10を中心として対流作用を行なえるよ
うになつている。この加熱筒10の直径は普通蒸
溜缶1の約1/2〜1/3が対流作用および加熱効果上
好適である。16は加熱筒10に接続されたガス
抜き孔、17はドレーン管である。 Reference numeral 10 denotes a heating cylinder having a double inner and outer cylinder structure installed in the lower central part of the distillation can 1, with an inner tube 11 and an outer tube 12 that are open at the top and bottom.
The upper and lower ends of the cylinders 11 and 12 are connected by end plates with a distance of about mm, and the upper and lower ends of the inner and outer cylinders 11 and 12 are closed to form a steam chamber 13. A steam supply pipe 14 is connected to the steam supply pipe 14 so that heated steam can be blown thereinto. The heating cylinder 10 is opened in the vertical direction so that there is a gap between the bottom 15 of the distillation can 1 and the bottom 15 to allow convection of the stock solution such as shochu moromi.
The heating cylinder 10 is disposed at a position slightly above the heating cylinder 10 so that the raw solution can undergo convection around the heating cylinder 10. The diameter of the heating cylinder 10 is preferably about 1/2 to 1/3 of the diameter of the distiller 1 in terms of convection and heating effects. 16 is a gas vent connected to the heating cylinder 10, and 17 is a drain pipe.
また図示する実施例では、上記の加熱筒10の
下方部に円環状をなす蒸気吹き込み管18が配さ
れ、該蒸気吹き込み管18には蒸気を内方斜め下
向きに吹き出せる直径2mmからせいぜい10mm程度
の蒸気吹き出し用の小孔19が多数設けられて
り、この蒸気の吹き出し作用により上記の対流作
用が一層良好に行なえるようになつている。 In the illustrated embodiment, an annular steam blowing pipe 18 is disposed at the lower part of the heating cylinder 10, and the steam blowing pipe 18 has a diameter of about 2 mm to 10 mm at most, which can blow steam inward and diagonally downward. A large number of small holes 19 are provided for blowing out steam, and the blowing out of the steam allows the above-mentioned convection to be carried out even better.
図の20は蒸溜缶1の上部に設けた焼酎醪等の
原液の供給管、21は液面計、22は真空ポンプ
7と製品タンク5との接続管路23に設けたミス
トセパレータ、24は冷却器4の後続に配したガ
スセパレータ、25はテスターを示す。 In the figure, 20 is a supply pipe for stock liquid such as shochu moromi installed in the upper part of the distillation can 1, 21 is a liquid level gauge, 22 is a mist separator installed in the connection pipe 23 between the vacuum pump 7 and the product tank 5, and 24 is a A gas separator 25 is placed after the cooler 4 and a tester.
なお図示していないが、前記蒸気排出路3の竪
管部分には、通常煮沸されて発生した蒸気に含ま
れる不純物を除去する精溜柵等を備え、精溜作用
を行なえるようになつており、また横管部分は予
備的な冷却作用を行なうようになつている。 Although not shown, the vertical pipe portion of the steam exhaust passage 3 is usually equipped with a rectifying fence or the like for removing impurities contained in the steam generated by boiling, so that a rectifying action can be performed. In addition, the horizontal pipe section is designed to provide a preliminary cooling effect.
上記の構成を有する本発明の蒸溜装置による蒸
溜作業について説明すると、蒸溜缶1に所要量の
焼酎醪等の原液を収容した状態で、加熱源である
加熱筒20にゲージ圧0.3〜3Kg/cm2の蒸気を供
給して加熱し、前記原液を煮沸する。特に蒸溜缶
1内での煮沸においては、加熱筒10の内外両筒
11,12がいずれも吹き込まれる蒸気によつて
加熱伝熱面として作用するため、原液の加熱作用
が広い面積で行なわれ、しかもこの加熱作用によ
つて加熱筒10の内方部ではその周囲部から加熱
される原液が上昇し、また加熱筒10の外方部で
は蒸溜缶1の外壁側からは加熱されないために下
降流となり、その結果加熱筒10を中心とする図
面矢印方向の対流作用を促し、この対流作用と前
記加熱伝熱面積の大きいこととが相俟つて、原液
全体を万遍に効率よく加熱し得て煮沸を促進でき
る。 To explain the distillation operation using the distillation apparatus of the present invention having the above-mentioned configuration, with the distillation can 1 containing the required amount of stock solution such as shochu moromi, the heating tube 20 as the heating source is heated at a gauge pressure of 0.3 to 3 kg/cm. 2 steam is supplied and heated to boil the stock solution. Particularly during boiling in the distiller 1, both the inner and outer cylinders 11 and 12 of the heating cylinder 10 act as heating heat transfer surfaces by the steam blown in, so that the heating action of the stock solution is performed over a wide area. Moreover, due to this heating effect, the raw solution heated from the surrounding area rises in the inner part of the heating cylinder 10, and downwards in the outer part of the heating cylinder 10 because it is not heated from the outer wall side of the still can 1. As a result, the convection action in the direction of the arrow in the drawing is promoted around the heating cylinder 10, and this convection action and the large heating heat transfer area combine to efficiently heat the entire stock solution evenly. Boiling can be accelerated.
そして、上記の煮沸によつて発生した蒸気は蒸
気排出路3を通つて冷却器2に入り、ここで冷却
されて凝縮された蒸溜液すなわち焼酎等の製品が
製品タンク5内に送られ貯留されるものであり、
この蒸溜経路6は真空ポンプ7により真空に近い
減圧状態に保持されているため、この真空度によ
つても異なるが、蒸溜缶1内の原液は45〜60℃程
度の加熱温度で沸騰し、蒸溜が良好に行なわれ
る。 The steam generated by the boiling described above enters the cooler 2 through the steam exhaust path 3, where it is cooled and condensed, and the distilled liquid, that is, a product such as shochu, is sent to the product tank 5 and stored there. It is
Since this distillation path 6 is maintained in a reduced pressure state close to vacuum by a vacuum pump 7, the stock solution in the distillation can 1 boils at a heating temperature of about 45 to 60°C, although it varies depending on the degree of vacuum. Distillation is carried out well.
[発明の効果]
上記したように本発明においては、蒸溜缶内部
に装備した加熱筒の内外両筒がその間に吹き込ま
れる蒸気によつて加熱伝熱面となり、蒸溜缶内の
原液を前記内外両筒によつて加熱でき、内部加熱
方式であつても加熱伝熱面積が大きく、その上、
蒸溜缶底部のやや上方位置に配された前記加熱筒
自体が対流筒を兼ね、その内方部分では上昇、外
方部分では下降する原液の対流を促し、これら加
熱伝熱面積の大なることと対流撹拌作用とが相俟
つて、加熱筒による加熱伝熱効率を高め、原液全
体を万遍に効率よく加熱煮沸できるので、蒸溜時
間を短縮化でき、蒸溜効率が高く、焼酎等の蒸溜
酒をコスト安価に得ることができる。しかも原液
が前記のように加熱筒を中心として常に対流作用
を行ない、かつ前記のように煮沸時間を短縮でき
るので、液中の夾雑物が加熱筒表面に付着するこ
とがなく、また溜出により液面が低下しても前記
加熱筒は底部やや上方位置にあつて常に液中に浸
漬しているために焦げ付き等が生じることがない
ので、焼酎等の蒸溜製品に焦臭が付く虞れもな
く、高品質の製品を得ることができる。また前記
焦げ付きや夾雑物の付着が生じないので、加熱筒
による加熱効果を長期にわたつて良好に保持でき
る。[Effects of the Invention] As described above, in the present invention, both the inner and outer cylinders of the heating cylinder installed inside the still can become heating heat transfer surfaces by the steam blown in between, and the raw liquid in the still can is transferred to both the inner and outer cylinders. It can be heated by a cylinder, and even if it is an internal heating method, the heating heat transfer area is large, and in addition,
The heating cylinder itself, which is placed slightly above the bottom of the distillation can, also serves as a convection cylinder, promoting convection of the concentrate rising in the inner part and descending in the outer part, and increasing the heating heat transfer area. Combined with the convection stirring action, the heating heat transfer efficiency of the heating cylinder is increased, and the entire stock solution can be efficiently heated and boiled evenly, so distillation time can be shortened, distillation efficiency is high, and distilled spirits such as shochu can be produced at a lower cost. It can be obtained cheaply. Moreover, as the raw solution constantly undergoes convection around the heating tube as described above, and the boiling time can be shortened as described above, impurities in the liquid do not adhere to the surface of the heating tube, and the distillation process Even if the liquid level drops, the heating cylinder is located slightly above the bottom and is always immersed in the liquid, so there is no chance of burning or the like, so there is no risk of burning odor in distilled products such as shochu. You can get a high quality product without any hassle. Furthermore, since the burning and foreign substances do not occur, the heating effect of the heating cylinder can be maintained well for a long period of time.
殊に本発明の場合、前記のように夾雑物の付着
等が生じ難い上、加熱筒表面に付着等が生じて
も、該表面の付着物の除去作業が行ない易く、1
回の蒸溜毎の缶内清掃がきわめて容易に行なえ、
以て長期に渡り良好な品質および加熱効率を維持
できる。 In particular, in the case of the present invention, not only is it difficult for foreign matter to adhere as described above, but even if adhesion occurs on the surface of the heating cylinder, it is easy to remove the foreign matter from the surface.
It is extremely easy to clean the inside of the can after each distillation.
As a result, good quality and heating efficiency can be maintained over a long period of time.
さらに内外2重筒の加熱筒は従来よりも高圧の
蒸気を吹き込んでも表面に凹凸を生じることがな
い。 Furthermore, the dual heating cylinder (inside and outside) does not cause unevenness on the surface even when high-pressure steam is blown into it compared to conventional heating cylinders.
第1図は本発明の実施例を示す一部欠截正面
図、第2図は一部の拡大縦断面図、第3図は前図
−線における断面図である。
1……蒸溜缶、2……冷却器、3……蒸気排出
路、4……蛇管、5……製品タンク、6……蒸溜
経路、7……真空ポンプ、10……加熱筒、11
……内筒、12……外筒、13……蒸気室、14
……蒸気供給管、15……底部。
FIG. 1 is a partially cutaway front view showing an embodiment of the present invention, FIG. 2 is a partially enlarged longitudinal sectional view, and FIG. 3 is a sectional view taken along the line taken from the front figure. 1... Distillation can, 2... Cooler, 3... Steam exhaust path, 4... Serpentine pipe, 5... Product tank, 6... Distillation route, 7... Vacuum pump, 10... Heating cylinder, 11
... Inner cylinder, 12 ... Outer cylinder, 13 ... Steam chamber, 14
...Steam supply pipe, 15...bottom.
Claims (1)
ンクに到る蒸溜経路を減圧状態にして焼酎等の原
酒を蒸溜する減圧単式蒸溜装置において、上下に
開口した内筒とこれよりやや径大の外筒とを上下
端部で連接した2重筒構造をなしかつ内外両筒間
の上下端部を閉塞してその内部空間に加熱蒸気を
送給できるようにした加熱筒を、前記蒸溜缶内の
下方部における底部よりやや上方位置に装備して
なることを特徴とする焼酎等の減圧単式蒸溜装
置。1. In a vacuum single distillation device that distills unprocessed liquor such as shochu by reducing the pressure in the distillation path from the distillation can that boils the stock solution such as shochu moromi to the product tank, there is an inner cylinder that opens at the top and bottom and a slightly larger diameter one. A heating cylinder, which has a double cylinder structure in which the outer cylinder is connected at the upper and lower ends, and which closes the upper and lower ends between the inner and outer cylinders so that heated steam can be delivered to the internal space, is placed inside the distillation can. A reduced-pressure single-type distillation apparatus for distilling shochu, etc., characterized in that it is installed at a position slightly above the bottom of the lower part of the apparatus.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP61104345A JPS62259575A (en) | 1986-05-06 | 1986-05-06 | Vacuum pot still for shochu or the like |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP61104345A JPS62259575A (en) | 1986-05-06 | 1986-05-06 | Vacuum pot still for shochu or the like |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS62259575A JPS62259575A (en) | 1987-11-11 |
| JPH0115276B2 true JPH0115276B2 (en) | 1989-03-16 |
Family
ID=14378311
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP61104345A Granted JPS62259575A (en) | 1986-05-06 | 1986-05-06 | Vacuum pot still for shochu or the like |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS62259575A (en) |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS4825095U (en) * | 1971-07-30 | 1973-03-24 |
-
1986
- 1986-05-06 JP JP61104345A patent/JPS62259575A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS62259575A (en) | 1987-11-11 |
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