JPS6360994B2 - - Google Patents
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- Publication number
- JPS6360994B2 JPS6360994B2 JP9264379A JP9264379A JPS6360994B2 JP S6360994 B2 JPS6360994 B2 JP S6360994B2 JP 9264379 A JP9264379 A JP 9264379A JP 9264379 A JP9264379 A JP 9264379A JP S6360994 B2 JPS6360994 B2 JP S6360994B2
- Authority
- JP
- Japan
- Prior art keywords
- shochu
- distillation
- alcohol
- mash
- conduit
- 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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- 235000020083 shōchū Nutrition 0.000 claims description 68
- 238000004821 distillation Methods 0.000 claims description 45
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims description 39
- 238000010438 heat treatment Methods 0.000 claims description 12
- 238000001816 cooling Methods 0.000 claims description 11
- 239000000796 flavoring agent Substances 0.000 claims description 10
- 235000019634 flavors Nutrition 0.000 claims description 10
- 241000209219 Hordeum Species 0.000 description 12
- 235000007340 Hordeum vulgare Nutrition 0.000 description 12
- 238000010992 reflux Methods 0.000 description 12
- 238000000034 method Methods 0.000 description 8
- 238000010793 Steam injection (oil industry) Methods 0.000 description 5
- 238000000746 purification Methods 0.000 description 5
- 238000010586 diagram Methods 0.000 description 4
- 244000061456 Solanum tuberosum Species 0.000 description 3
- 235000002595 Solanum tuberosum Nutrition 0.000 description 3
- 238000011156 evaluation Methods 0.000 description 3
- 238000000855 fermentation Methods 0.000 description 3
- 230000004151 fermentation Effects 0.000 description 3
- 239000004615 ingredient Substances 0.000 description 3
- 238000007670 refining Methods 0.000 description 3
- 230000001953 sensory effect Effects 0.000 description 3
- 206010013911 Dysgeusia Diseases 0.000 description 2
- 238000013459 approach Methods 0.000 description 2
- 238000007664 blowing Methods 0.000 description 2
- 230000007423 decrease Effects 0.000 description 2
- 230000006866 deterioration Effects 0.000 description 2
- HYBBIBNJHNGZAN-UHFFFAOYSA-N furfural Chemical compound O=CC1=CC=CO1 HYBBIBNJHNGZAN-UHFFFAOYSA-N 0.000 description 2
- 235000019640 taste Nutrition 0.000 description 2
- 244000017020 Ipomoea batatas Species 0.000 description 1
- 235000002678 Ipomoea batatas Nutrition 0.000 description 1
- 240000007594 Oryza sativa Species 0.000 description 1
- 235000007164 Oryza sativa Nutrition 0.000 description 1
- 230000002159 abnormal effect Effects 0.000 description 1
- 150000001298 alcohols Chemical class 0.000 description 1
- 150000001299 aldehydes Chemical class 0.000 description 1
- 235000009508 confectionery Nutrition 0.000 description 1
- 238000001944 continuous distillation Methods 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 150000002148 esters Chemical class 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 238000005360 mashing Methods 0.000 description 1
- 150000007524 organic acids Chemical class 0.000 description 1
- 235000005985 organic acids Nutrition 0.000 description 1
- 235000012015 potatoes Nutrition 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 235000009566 rice Nutrition 0.000 description 1
- 238000001577 simple distillation Methods 0.000 description 1
- 235000019583 umami taste Nutrition 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Landscapes
- Alcoholic Beverages (AREA)
Description
芋焼酎、米焼酎、麦焼酎、黒糖焼酎等、本格焼
酎と呼ばれるものは、酒税法上乙類焼酎と規定さ
れており、その乙類焼酎は、連続式蒸留法であつ
てはならないとされている。すなわち或る所定量
を1回毎に完結させる単式蒸留法でなければなら
ない。
一般に乙類焼酎の蒸留装置は第1図に示すとお
り加熱用蒸気管Aあるいは間接加熱用蒸気管Bを
備え、廃液排出管Dを備えているもろみ加熱蒸発
缶Eと、加熱蒸発缶Eから発生した焼酎蒸気の除
滴、還流、濃縮等を行う装置Sを経て導管Gを通
して導く冷却装置Cと、冷却装置Cで凝縮した焼
酎留液のアルコール度数を検査するアルコールメ
ーターボツクスMと、焼酎の貯槽Tとから成つて
いる。
乙類焼酎の蒸留は加熱蒸発缶Eに適量の例えば
いも焼酎もろみ1000程度を入れて、加熱用蒸気
管Aで蒸気を吹きこんで加熱し、(約30分〜50分
で沸とうして来る)、発生して来る焼酎蒸気は除
滴、還流、濃縮等の装置S及び導管Gを通過し
て、冷却装置Cに至り、凝縮する焼酎留液をアル
コールメーターボツクスMにてアルコール度数
(%)を検定しつゝ貯槽Tにためる。蒸留の終点
近くになると焼酎中のアルコールがうすくなつて
来るので、アルコール度数5〜10%位になつたら
蒸留を打ち切つて終了する。蒸留終点に近づくと
品質の劣化が判然としてくるので、極端に悪くな
い限りはできるだけアルコール度数を低くまで蒸
留するのが普通である。通常焼酎が留出しはじめ
てから2〜3時間で終る。いももろみのとき貯槽
Tの中の焼酎のアルコール%は35%内外が標準で
ある。
単式蒸留においてはいも焼酎の一例の場合冷却
装置Cより凝縮してアルコールメーターボツクス
Mを通過する焼酎のアルコール含有%は第2図に
示すとおり、初め焼酎留液が留出し、高濃度のア
ルコール含有率を示し、時間の経過と共にアルコ
ール分は低くなり、やがて0に近づいて終了す
る。一般にアルコール分が低くなつて来た蒸留終
点近くの焼酎は後留部分すなわち(すえだれ)と
称し、アルコール含有%は少くて、風味的に劣悪
とされるものが相対的に多く留出して来ている。
導管は2個以上とすることができる。
一般に乙類焼酎の風格はアルコール分以外の揮
発性成分の種類と量によつて決まると云つても過
言ではない。乙類焼酎に含まれるアルコール以外
の成分としては、アルデヒド、高級アルコール、
エステル、有機酸、フルフラール等があるが、風
味的に優劣を決める決定的な成分や量は未だ確定
されていない。それ故に焼酎品質の優劣を競う権
威ある焼酎品評会、鑑評会においてはすべて人の
官能審査によつて決めているのが現状である。乙
類焼酎の蒸留において比較的初期に留出する留分
を初留(はなだれ)と称し、中間部分を中留と称
し、特に後留部分は風味的に劣つているが、これ
を早目に切り捨てることはアルコール収得率の低
下となるので、採算的に引き合う点までできる限
りアルコールをとり入れているのが現状である。
中には分割蒸留と称し風味的に優れている初留中
留部分を別貯槽に入れて、極くはじめの初留と後
留部分は別に集めて、再蒸留して悪成分を除く方
法も採用されている。しかしこの方法も悪成分は
少くなつても風味的良成分も少くなつている。こ
の外、乙類焼酎の蒸留装置としては現在アルコー
ル以外の成分を極力少くするための工夫として、
蒸発缶より発生した焼酎蒸気を精製、還流、濃縮
装置を通過させて、アルコール分以外の微量成分
を極力還流させてアルコールの純度を高める工夫
を施した装置もあるがこの装置では、蒸留のはじ
めから終りまですべて同一の還流、濃縮等の工程
を経なければならねい。それで余り精製や還流等
を必要としない時間例えば中留期も還流や濃縮を
行うので風味的良成分までも失つて、風味の少い
乙類焼酎の風格の乏しい焼酎に近づいてゆく。又
蒸留全工程にわたつて精製濃縮を行うので蒸留時
間が長びいて加熱時間が長く、蒸留経費がかさむ
ばなりでなく、加熱時間が長いことのために、異
常な熱変化をうけた微量成分の留出に由来する風
味の悪い性質が出現することも屡々である。
本発明においては、第3図に示すとおりもろみ
加熱蒸発缶1より発生した焼酎蒸気を精製、還
流、濃縮等の装置2、導管3A,3B,3Cを経
て冷却装置4に導く。導管3A,3B,3Cは並
列に設けられ、導管3Aは焼酎蒸気の精製、還
流、濃縮等の装置2を殆んどバイパスで抜けて冷
却装置4に導かれ、導管3Bは中程度の精製、還
流、濃縮等を行つて冷却装置4に導かれ、導管3
Cは精製、還流、濃縮を装置2を全部通つて冷却
装置4に導かれる。蒸留の時間の経過に応じて導
管3A,3B,3Cを適宜選択して使いわけてで
きるだけ風味的良成分をとり入れて悪成分を除い
て良質の焼酎を得ることができる。
例えば順調な醗酵を終えた熟成もろみや、アル
コール含有%の比較的高い優良もろみを蒸留する
時は大部分の蒸留を導管3Aか導管3Bのみを使
用し、終点に近い後留部分になつて導管3Cのみ
を使用すると、風味のよい旨味多い焼酎を得るこ
とができる。特に高濃度の焼酎を得たい時は初留
部分のみ導管3Aを使用し中留、後留は導管3
B,3Cを使用することによつて高いアルコール
含有%の焼酎が得られる。使用原料がやゝ粗悪で
あつたり、醗酵が順調でなく、もろみに不純不良
成分が多かつたり、アルコール含有%が比較的低
いもろみを蒸留する時は、はじめから導管3Aを
閉じて、導管3Bか導管3Cを使用すると精製、
還流、濃縮の工程を能力一杯は活用できて焼酎の
劣化を極力防ぐことができる。
ここで麦焼酎を製造した例を示すと次のとおり
である。
Honkaku shochu, such as potato shochu, rice shochu, barley shochu, brown sugar shochu, etc., are defined as category O shochu under the Liquor Tax Act, and category 2 shochu must not be produced by continuous distillation. There is. In other words, it must be a simple distillation method in which a certain predetermined amount is completed each time. In general, distillation equipment for Otsu-class shochu is equipped with a heating steam pipe A or an indirect heating steam pipe B, and a mash heating evaporator E equipped with a waste liquid discharge pipe D, and a heating evaporator E as shown in Figure 1. A cooling device C that guides the shochu vapor through a conduit G through a device S that performs drip removal, reflux, concentration, etc., an alcohol meter box M that tests the alcohol content of the shochu distillate condensed in the cooling device C, and a shochu storage tank. It consists of T. To distill Otsu-type shochu, put an appropriate amount, for example, about 1,000 yam of sweet potato shochu mash, into a heating evaporator E, and heat it by blowing steam through the heating steam pipe A (it will boil in about 30 to 50 minutes). ), the generated shochu vapor passes through a device S for dripping, reflux, concentration, etc. and a conduit G, and reaches a cooling device C. The condensed shochu distillate is measured in an alcohol meter box M to measure the alcohol content (%). is stored in storage tank T. Near the end of distillation, the alcohol in the shochu becomes weaker, so when the alcohol content reaches around 5-10%, distillation is stopped. As the end point of distillation approaches, the deterioration in quality becomes obvious, so unless it is extremely bad, it is common practice to distill the alcohol content to as low as possible. Usually, the process ends within 2 to 3 hours after the shochu begins to distill. When mashing potatoes, the standard alcohol percentage of shochu in storage tank T is around 35%. In the case of potato shochu in single distillation, the alcohol content of the shochu condensed from the cooling device C and passed through the alcohol meter box M is as shown in Figure 2. Initially, the shochu distillate is distilled out, and the shochu contains a high concentration of alcohol. The alcohol content decreases over time and eventually approaches 0 and ends. In general, shochu near the end of distillation, where the alcohol content has decreased, is called the after-distillation part, or ``suedare''. ing.
There can be more than one conduit. Generally speaking, it is no exaggeration to say that the character of Otsu-class shochu is determined by the type and amount of volatile components other than alcohol. Components other than alcohol contained in Otsuru shochu include aldehydes, higher alcohols,
There are esters, organic acids, furfural, etc., but the decisive ingredients and amounts that determine the superiority and inferiority of flavor have not yet been determined. For this reason, the current situation is that the authoritative shochu competitions and competitions that compete to determine the quality of shochu are all decided based on human sensory evaluation. The fraction that is distilled relatively early in the distillation of Otsu-type shochu is called the first distillation (hanadare), and the middle fraction is called the middle distillation. Cutting it down to 100% lowers the alcohol yield rate, so the current situation is to incorporate as much alcohol as possible to the point where it is profitable.
There is also a method known as split distillation, in which the first distillate and the middle distillate, which are superior in flavor, are placed in a separate storage tank, and the very first distillate and the last distillate are collected separately and re-distilled to remove bad components. It has been adopted. However, even though this method reduces the number of bad ingredients, the number of good flavor ingredients also decreases. In addition to this, the current distillation equipment for Otsu-type shochu is designed to reduce the amount of components other than alcohol as much as possible.
Some devices are designed to increase the purity of alcohol by purifying, refluxing, and concentrating the shochu vapor generated from the evaporator, refluxing trace components other than alcohol as much as possible. The process from beginning to end must be the same, such as refluxing and concentrating. Because reflux and concentration are carried out during periods when purification and reflux are not required, for example, during the middle fermentation period, even good flavor components are lost, resulting in a shochu that has little flavor and lacks the personality of Otsu-class shochu. In addition, since purification and concentration are carried out throughout the entire distillation process, the distillation time and heating time are long, which not only increases distillation costs, but also eliminates trace components that have undergone abnormal thermal changes due to the long heating time. It is also common for a bad flavor to appear due to the distillation of alcohol. In the present invention, as shown in FIG. 3, shochu vapor generated from the mash heating evaporator 1 is guided to a cooling device 4 through a device 2 for refining, refluxing, concentrating, etc., and conduits 3A, 3B, and 3C. The conduits 3A, 3B, and 3C are provided in parallel, and the conduit 3A mostly bypasses the device 2 for refining, refluxing, and concentrating shochu vapor and is led to the cooling device 4, and the conduit 3B is for medium purification, After refluxing, concentrating, etc., it is led to a cooling device 4, and then passed through a conduit 3.
C is purified, refluxed, and concentrated through the device 2 and led to the cooling device 4. By appropriately selecting and using the conduits 3A, 3B, and 3C according to the passage of distillation time, high-quality shochu can be obtained by incorporating as many good flavor components as possible and removing bad components. For example, when distilling aged mash that has completed smooth fermentation or high-quality mash with a relatively high alcohol content, most of the distillation is carried out using only conduit 3A or conduit 3B. By using only 3C, it is possible to obtain shochu with a good flavor and a lot of umami. When you want to obtain shochu with a particularly high concentration, use conduit 3A only for the first distillation part, and use conduit 3A for the middle distillation and rear distillation.
By using B and 3C, shochu with a high alcohol content can be obtained. If the raw materials used are of poor quality, the fermentation is not going well, the mash has many impurities, or the mash has a relatively low alcohol content, close conduit 3A from the beginning and replace conduit 3B. If you use conduit 3C, it will be purified.
The reflux and concentration processes can be utilized to their fullest potential, and deterioration of shochu can be prevented as much as possible. An example of producing barley shochu is as follows.
【表】
官能検査は10人で行い優良品に1点、普通品に
2点、やゝ劣るに3点の評点を付し、その評点を
合計したものが官能審査の得点である。従つて得
点の少いもの程優良の評価をうけたこととなる。
例 1
麦焼酎を本発明装置で蒸留した例(第4図参
照)
麦もろみアルコール分 17.8%
一回に使用したもろみ容量 1.050
蒸気吹きこみはじめより終了までの時間 3時間
35分
(イ) 蒸気吹きこみはじめより焼酎留液留出はじめ
まで 45分
(ロ) 留出はじめから50分までは導管3A,3B,
3C全開で蒸留する。
(ハ) 留出はじめから50分後から更に1時間経過時
までは導管3Aを全閉し、導管3B,3Cを全
開する。
(ニ) 留出はじめから1時間50分後から終了まで導
管3A,3Bを全閉し、導管3Cを全開で蒸留
する。
生成焼酎のアルコール% 44.2%
生成焼酎の容量 410
アルコール収取率(生成焼酎のアルコール/もろみ中
全アルコール
×100) 97%
製品の特長 いやな麦臭少く、甘味多く、口当り
のやわらかい後味のよい焼酎、麦焼酎によくみ
られる焦臭が殆んど感ぜられない。
例 2
麦焼酎を本発明装置で蒸留した別の例(第5図
参照)
麦もろみ例1と同じ 17.8%
一回に使用したもろみ容量 1.050
蒸気吹きこみはじめより終了までの時間 3時間
46分
(イ) 蒸気吹きこみはじめより焼酎留出はじめまで
45分。
(ロ) 留出はじめより50分までは導管3A全開、3
B,3C全閉。
(ハ) 留出はじめ50分後から更に1時間経過時まで
は導管3Aを全閉し、導管3B,3Cを全開。
(ニ) 留出はじめから1時間50分後から終点まで導
管3Cみの全開。
生成焼酎のアルコール% 42.1%
生成焼酎の容量 430
アルコール収得率 97%
製品の特長 軽いさわやかな麦臭あり、旨味多く
丸味のある焼酎、焦臭や末ダレ臭はない。
例 3
麦焼酎を在来の装置で蒸留した例(第6図参
照)
麦もろみ例1、2と同じ 17.8%アルコール度
一回に使用したもろみ容量 985
蒸気吹きこみはじめより終了までの時間 3時間
55分
(イ) 蒸気吹きこみはじめより焼酎留液出はじめま
で 53分
(ロ) 留出はじめてから蒸留終りまでの時間 3時
間2分
生成焼酎のアルコール% 39.7%
生成焼酎の容量 426.6
アルコール収得率 96%
製品の特長 麦臭と焦臭があり刺戟臭あり、味は
甘味はあるが雑味多く、後味に残るかんじ。
結局在来の蒸留装置では、
(1) 装置固有の蒸留法のみでもろみの状況の変化
に対応する幅が極めて少く、
(2) 焼酎の精製、濃縮は装置固有の型式だけであ
り幅がなく、
(3) 場合によつては再留を要することがあり、
(4) 装置固有のアルコール濃度しか得られない。
が本発明の装置によれば、
(1) 蒸留前のもろみのでき具合に応じて、最適の
蒸留法を選択でき、
(2) 設計する品質に応じて、精製、濃縮の程度を
選択できる幅が広く、
(3) 焼酎を再蒸留しなくても悪成分の除去ができ
るので蒸留手間と経費が少くてすみ、
(4) 在来のものよりも唯一回の蒸留で自由に高濃
度アルコールの焼酎ができる。[Table] The sensory test was conducted by 10 people, and a score of 1 point was given to an excellent product, 2 points to an average product, and 3 points to a slightly inferior product.The total of the scores was the sensory evaluation score. Therefore, the lower the score, the better the evaluation. Example 1 Example of distilling barley shochu using the device of the present invention (see Figure 4) Barley mash alcohol content 17.8% Volume of mash used at one time 1.050 Time from the beginning of steam injection to the end 3 hours
35 minutes (a) From the start of steam injection to the start of shochu distillate distillation 45 minutes (b) From the start of distillation until 50 minutes, pipes 3A, 3B,
Distill at 3C full throttle. (c) From 50 minutes after the start of distillation until one hour has passed, fully close conduit 3A and fully open conduits 3B and 3C. (d) Completely close conduits 3A and 3B and fully open conduit 3C for distillation from 1 hour and 50 minutes after the start of distillation until the end. Alcohol % of produced shochu 44.2% Volume of produced shochu 410 Alcohol collection rate (alcohol of produced shochu/total alcohol in mash x 100) 97% Product features A shochu with little unpleasant barley odor, lots of sweetness, and a soft texture with a good aftertaste. There is almost no burnt smell that is often found in barley shochu. Example 2 Another example of distilling barley shochu using the device of the present invention (see Figure 5) Same as barley mash example 1 17.8% Volume of mash used at one time 1.050 Time from the beginning of steam injection to the end 3 hours
46 minutes (a) From the beginning of steam blowing to the beginning of shochu distillation
45 minutes. (b) Conduit 3A is fully opened until 50 minutes from the beginning of distillation.
B, 3C fully closed. (c) From 50 minutes after the start of distillation until one hour has passed, pipe 3A is fully closed, and pipes 3B and 3C are fully opened. (d) Fully open conduit 3C from 1 hour and 50 minutes after the start of distillation to the end point. Alcohol% of produced shochu: 42.1% Volume of produced shochu: 430 Alcohol yield: 97% Product Features: Shochu with a light and refreshing barley odor, rich flavor and roundness, no burnt odor or runny odor. Example 3 An example of distilling barley shochu using a conventional device (see Figure 6) Same as barley mash examples 1 and 2 Volume of mash used for one 17.8% alcohol content 985 Time from the start of steam injection to the end 3 hours
55 minutes (a) From the start of steam injection to the start of shochu distillate coming out 53 minutes (b) Time from the start of distillation to the end of distillation 3 hours 2 minutes Alcohol% of shochu produced 39.7% Volume of shochu produced 426.6 Alcohol yield 96 % Product Features It has a barley odor, a burnt odor, and a pungent odor.The taste is sweet but has a lot of unpleasant taste, which leaves a lingering aftertaste. In the end, with conventional distillation equipment, (1) there is very little scope for responding to changes in the situation of the mash using only the distillation method unique to the device, and (2) there is no scope for refining and concentrating shochu, as only the type unique to the device can handle. , (3) Re-distillation may be required in some cases, and (4) only the alcohol concentration specific to the device can be obtained. However, according to the apparatus of the present invention, (1) the optimum distillation method can be selected according to the condition of the mash before distillation, and (2) the degree of purification and concentration can be selected according to the quality to be designed. (3) Since harmful components can be removed without re-distilling the shochu, distillation time and costs are reduced; (4) Compared to conventional shochu, it is possible to freely produce high-concentration alcohol in just one distillation. You can make shochu.
第1図は従来の乙類焼酎の蒸留装置の概略説明
図である。第2図は蒸留中の留液のアルコール含
有%の経過を示す線図である。第3図は本発明に
よる焼酎の蒸留装置の概略説明図である。第4,
5,6図はそれぞれ例1、例2、例3の蒸留中の
留液のアルコール濃度の変化を示す線図である。
1:加熱蒸発缶、2:精製、還流、濃縮装置、
3A,3B,3C:導管、4:冷却装置。
FIG. 1 is a schematic explanatory diagram of a conventional distillation apparatus for Otsu-class shochu. FIG. 2 is a diagram showing the course of the alcohol content percentage of the distillate during distillation. FIG. 3 is a schematic explanatory diagram of a shochu distillation apparatus according to the present invention. Fourth,
Figures 5 and 6 are diagrams showing changes in the alcohol concentration of the distillate during distillation in Examples 1, 2, and 3, respectively. 1: heating evaporator, 2: purification, reflux, concentrator,
3A, 3B, 3C: conduit, 4: cooling device.
Claims (1)
ール含有焼酎蒸気を並列に設けた2個以上の導管
により冷却装置へ導くよう配置し、それらの導管
が加熱蒸発缶より発生した焼酎蒸気を、そのまま
直ちに冷却装置へ導く導管、精留、還流、濃縮の
度合の異る装置を通過させて冷却装置へ導く導管
より成り、1回の蒸留中に時期をえらんで、焼酎
蒸気の精留、還流、濃縮の度合を変えて、風味の
悪い成分の少い焼酎を留出させる焼酎の蒸留装
置。1 Arranged so that the alcohol-containing shochu vapor generated from one mash heating evaporator is led to a cooling device through two or more conduits installed in parallel, and these conduits immediately direct the shochu vapor generated from the mash heating evaporator to the cooling device. The shochu vapor is rectified, refluxed, and concentrated at selected times during one distillation. A shochu distillation device that changes the degree of shochu and distills shochu with fewer components that have a bad flavor.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP9264379A JPS5618585A (en) | 1979-07-23 | 1979-07-23 | Distillation apparatus of low-class distilled alcoholic beverage (shochu) |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP9264379A JPS5618585A (en) | 1979-07-23 | 1979-07-23 | Distillation apparatus of low-class distilled alcoholic beverage (shochu) |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5618585A JPS5618585A (en) | 1981-02-21 |
| JPS6360994B2 true JPS6360994B2 (en) | 1988-11-28 |
Family
ID=14060125
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP9264379A Granted JPS5618585A (en) | 1979-07-23 | 1979-07-23 | Distillation apparatus of low-class distilled alcoholic beverage (shochu) |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5618585A (en) |
-
1979
- 1979-07-23 JP JP9264379A patent/JPS5618585A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5618585A (en) | 1981-02-21 |
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