JPS6216635B2 - - Google Patents

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Publication number
JPS6216635B2
JPS6216635B2 JP16179578A JP16179578A JPS6216635B2 JP S6216635 B2 JPS6216635 B2 JP S6216635B2 JP 16179578 A JP16179578 A JP 16179578A JP 16179578 A JP16179578 A JP 16179578A JP S6216635 B2 JPS6216635 B2 JP S6216635B2
Authority
JP
Japan
Prior art keywords
shochu
distillation
distillate
components
otsu
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
Application number
JP16179578A
Other languages
Japanese (ja)
Other versions
JPS5592684A (en
Inventor
Masaaki Yamamoto
Masahiro Yamamoto
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.)
Individual
Original Assignee
Individual
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 Individual filed Critical Individual
Priority to JP16179578A priority Critical patent/JPS5592684A/en
Publication of JPS5592684A publication Critical patent/JPS5592684A/en
Publication of JPS6216635B2 publication Critical patent/JPS6216635B2/ja
Granted legal-status Critical Current

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  • Alcoholic Beverages (AREA)

Description

【発明の詳細な説明】[Detailed description of the invention]

醪取り本格焼酎は、酒税法上乙類焼酎と呼ば
れ、その蒸留法は連続式でなく、単式の一定量ず
つ完結させるいわゆるバツチ式蒸留法でなければ
ならない。そして、その蒸留装置は、第1図に示
すとおり、もろみを加熱して蒸発させる加熱用蒸
気管1a及び間接加熱用蒸気管1bを備え更に排
液排出管1cを有するもろみ蒸発罐1とその蒸発
罐1から蒸発した焼酎蒸気を冷却して凝縮する冷
却装置2と凝縮した焼酎液をためて検定する貯槽
3とから成り立つている。アルコールメーターボ
ツクス4は凝縮してくる焼酎のアルコール度数を
計測する酒精計をセツトしている。 乙類焼酎の蒸留は、蒸発罐1に所定量のもろみ
を入れて、加熱用蒸気管1aによる吹込み、間接
加熱用蒸気管1bによる加熱等により加熱して、
アルコールを主成分とする揮発成分を蒸発させ
て、冷却装置2により30℃前後に冷却して凝縮し
てくる焼酎を貯槽3に導き、アルコール度数が0
に近づく終り近くまで蒸留を行うのが普通であ
る。一定量ずつ蒸留を行う単式蒸留においては、
貯槽3に流入する焼酎は、はじめアルコール度数
が高く(約50〜60%)留液の時間分毎のアルコー
ル%を示す、第2図に示すとおり時間の経過と共
にアルコール度数は低くなり、やがて0となり蒸
留は終る。 アルコール以外の揮発成分、すなわち乙類焼酎
に含まれる微量成分はその種類により溜出するピ
ークが初期であつたり、或は後期であつたり、又
全期に亘つて少しづつ溜出するものもある。そし
てこれ等の微量成分が乙類焼酎の独特の風味を形
成するが、風味的に良い成分のみを得ることはむ
ずかしく、風味的に悪成分も混在するのが普通で
ある。そして、風味的に良成分を残し、悪成分だ
けをいかにして除去するかが、乙類焼酎品質向上
の最大の問題となつている。 乙類焼酎の蒸留では第2図に示すとおり、蒸留
初期の留分を初留、中期を中留、後期を後留と呼
んでいるが、後留になる程アルコール度数は低く
なり、フルフラール等の風味的にすぐれない成分
の留出が多くなる。それで後留分は早目に切りす
て、悪風味成分を除きたいところであるが、アル
コールも同時に切り捨てる結果、極端に早目に切
りすてることは、アルコール収率を悪くすること
になるので限度があり、普通アルコール%10%〜
8%位までとり入れている。 又、後留部分だけを別の貯槽に移して、後留部
分のみを集めて、再蒸留するとか、吸着過を行
うとかの方法も行われているが、作業工程を一つ
或は二つ増加させることで手間がかかり、必ずし
も最善の策ではない。 現在は大半のメーカーは全留液を一緒に集め
て、再過とか、吸着剤による過等を行つて、
雑成分を除去しているが、悪成分を徹底的に取り
除こうとすれば、良成分も除去されて、乙類焼酎
らしい風格が失われるので、どの程度の過や吸
着を行うかが仲々むずかしい課題となつている。 本発明は、乙類焼酎の風格向上のために、もろ
みを加熱して蒸発し、蒸発した焼酎蒸気を冷却し
こうして凝結した留液を一定量すつ完結させる乙
類焼酎の単式蒸留法において、吸着過工程を蒸
留工程中に組入れ、留液の経時的な留出成分の変
化に応じ吸着過の度合を調整し、蒸留中適宜の
時期に凝結する焼酎の悪成分のみを厳格に過吸
着することを特徴とするものである。 次に本発明を実施する装置を第1図について説
明する。 上記装置は蒸留缶1を有する蒸留装置中の冷却
タンク2から凝縮してくる焼酎をアルコールメー
ターボツクス4を経て貯槽3に導く前に、吸着、
過装置5を設けて、蒸留液が出てくる途中で吸
着過等を行うことができるようにしたものであ
る。 このようにすることによつて、蒸留途中の焼酎
の流れの蒸留工程において吸着過工程を併設す
るもので、蒸留中の適宜の時期例えば、後留区分
の悪成分のみを厳格に過吸着させて、アルコー
ルはそのままで悪成分をとり除くことができる
し、又風味の比較的すぐれた初留区分はそのまま
過装置5を素通りさせて、芳香成分は何ら失う
ことなく蒸留できる。 本発明の方法による焼酎と在来法による焼酎と
のフルフラール(悪成分の一つ)の分析値と利酒
結果を示すと次のとおりである。
Under the Liquor Tax Law, Moritori Honkaku Shochu is called Otsu-type shochu, and its distillation method is not a continuous method, but rather a so-called batch distillation method that completes the distillation in single batches. As shown in Fig. 1, the distillation apparatus includes a heating steam pipe 1a for heating and evaporating mash and an indirect heating steam pipe 1b, and a mash evaporating can 1 having a drain liquid discharge pipe 1c, It consists of a cooling device 2 that cools and condenses the shochu vapor evaporated from a can 1, and a storage tank 3 that collects and tests the condensed shochu liquid. Alcohol meter box 4 is equipped with a spirit meter that measures the alcohol content of condensed shochu. To distill Otsu-class shochu, put a predetermined amount of mash into the evaporator can 1, and heat it by blowing through the heating steam pipe 1a, heating through the indirect heating steam pipe 1b, etc.
Volatile components, mainly alcohol, are evaporated, and the shochu is cooled to around 30°C by the cooling device 2, and the condensed shochu is led to the storage tank 3, where the alcohol content is 0.
Distillation is usually carried out until near the end, which approaches . In single distillation, in which distillation is carried out in fixed amounts,
The shochu flowing into the storage tank 3 initially has a high alcohol content (approximately 50 to 60%), and as shown in Figure 2, which shows the alcohol percentage per hour of distillate, the alcohol content decreases over time and eventually reaches 0. Then the distillation ends. Volatile components other than alcohol, that is, trace components contained in Otsu-type shochu, may peak at the early stage or at the later stage depending on the type of shochu, and some may distill out little by little over the entire period. . These trace components form the unique flavor of Otsu-class shochu, but it is difficult to obtain only the components that are good for flavor, and it is common for components that are bad for flavor to be mixed in as well. The biggest problem in improving the quality of Otsu-type shochu is how to leave only the good flavor components and remove only the bad ones. In the distillation of Otsu-type shochu, as shown in Figure 2, the initial distillation fraction is called the first distillation, the middle distillation is called the middle distillation, and the latter distillation is called the rear distillation. This increases the distillation of components that are not good in terms of flavor. Therefore, it is desirable to cut off the residual distillate as soon as possible to remove the bad flavor components, but alcohol is also cut off at the same time, so there is a limit to cutting off the remaining distillate too early as this will reduce the alcohol yield. There is, normal alcohol% 10% ~
It has been incorporated up to about 8%. Other methods include transferring only the residual fraction to another storage tank, collecting only the residual fraction, and re-distilling or performing adsorption, but these methods require only one or two steps. Increasing the number takes time and effort, and is not necessarily the best solution. Currently, most manufacturers collect all the distillate together and perform refiltration or filtration with an adsorbent.
Miscellaneous ingredients are removed, but if you try to thoroughly remove the bad ingredients, the good ingredients will also be removed and you will lose the distinctive character of Otsu-type shochu, so it is difficult to decide how much to remove and absorb. It is becoming. In order to improve the personality of Otsu-class shochu, the present invention is a single distillation method for Otsu-class shochu, in which mash is heated and evaporated, the evaporated shochu vapor is cooled, and a fixed amount of condensed distillate is produced. An over-adsorption step is incorporated into the distillation process, and the degree of over-adsorption is adjusted according to changes in the distillate components of the distillate over time, strictly over-adsorbing only the harmful components of shochu that condense at appropriate times during distillation. It is characterized by this. Next, an apparatus for carrying out the present invention will be described with reference to FIG. The above device adsorbs shochu condensed from a cooling tank 2 in a distillation apparatus having a distillation can 1 before guiding it to a storage tank 3 via an alcohol meter box 4.
A filtration device 5 is provided so that adsorption and filtration can be carried out while the distillate is coming out. By doing this, an over-adsorption step is added to the distillation process of the shochu stream during distillation, and at an appropriate time during distillation, for example, only the bad components in the trailing distillate are strictly over-adsorbed. Bad components can be removed from the alcohol as it is, and the initial distillation fraction with a relatively good flavor can be passed through the filtration device 5 as it is and distilled without losing any aromatic components. The analysis values of furfural (one of the harmful ingredients) and the alcohol yield results of shochu produced by the method of the present invention and shochu produced by the conventional method are as follows.

【表】 本発明の利点を特記すれば、 焼酎の矯正過工程を蒸留工程の中にくみ入
れられるから工程の簡略化となる。 焼酎留液の経時的な留出成分の変化に応じて
吸着過の度合を弱めたり、強めたり或は素通
りさせることができて、留出区分に応じた過
矯正ができるので、乙類焼酎の良い風味をでき
るだけ損わず、不良分を除去することが、容易
に然もほぼ完全に行うことができる。
[Table] The advantages of the present invention are as follows: The shochu distillation process can be incorporated into the distillation process, which simplifies the process. Depending on the change in the distillate components of the shochu distillate over time, the degree of over-adsorption can be weakened, strengthened, or allowed to pass through, and over-correction can be performed according to the distillate classification, so it is possible to Defects can be easily and almost completely removed without damaging the good flavor as much as possible.

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

第1図は本発明を実施する装置の説明図であ
り、第2図は留液の時間毎のアルコール度数を示
す図である。 1:蒸留法、2:冷却装置、3:貯槽、5:吸
着過装置。
FIG. 1 is an explanatory diagram of an apparatus for implementing the present invention, and FIG. 2 is a diagram showing the alcohol content of the distillate over time. 1: Distillation method, 2: Cooling device, 3: Storage tank, 5: Adsorption device.

Claims (1)

【特許請求の範囲】[Claims] 1 もろみを加熱して蒸発し、蒸発した焼酎蒸気
を冷却し、こうして凝結した留液を回収して一定
量ずつ完結させる乙類焼酎の単式蒸留法におい
て、吸着過工程を蒸留工程中に組入れ、留液の
経時的な留出成分の変化に応じて蒸留期間の一定
時期を選択して、焼酎にとつて風味不良成分が多
く出現する時期、即ちアルコール分が30%以下と
なる後留区分は、留出液を吸着過工程に通し、
風味不良成分を出来るだけ除去することを特徴と
する乙類焼酎の単式蒸留法。
1. In the single distillation method for type Otsu shochu, in which the mash is heated and evaporated, the evaporated shochu vapor is cooled, and the condensed distillate is collected and completed in fixed amounts, an adsorption step is incorporated into the distillation process, A certain period of the distillation period is selected according to the change in the distillate components of the distillate over time, and the period when many components with bad flavor appear in shochu, that is, the period when the alcohol content is less than 30%, is determined. , passing the distillate through an adsorption step;
A single distillation method for Otsu-type shochu that is characterized by removing as much of the flavor-poor components as possible.
JP16179578A 1978-12-29 1978-12-29 Simple distillation for preparation of low-class distilled spirits Granted JPS5592684A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP16179578A JPS5592684A (en) 1978-12-29 1978-12-29 Simple distillation for preparation of low-class distilled spirits

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP16179578A JPS5592684A (en) 1978-12-29 1978-12-29 Simple distillation for preparation of low-class distilled spirits

Publications (2)

Publication Number Publication Date
JPS5592684A JPS5592684A (en) 1980-07-14
JPS6216635B2 true JPS6216635B2 (en) 1987-04-14

Family

ID=15742047

Family Applications (1)

Application Number Title Priority Date Filing Date
JP16179578A Granted JPS5592684A (en) 1978-12-29 1978-12-29 Simple distillation for preparation of low-class distilled spirits

Country Status (1)

Country Link
JP (1) JPS5592684A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH035848U (en) * 1989-06-06 1991-01-21

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2015112050A (en) * 2013-12-10 2015-06-22 サッポロビール株式会社 Shochu and method of producing the same
CN104046553A (en) * 2014-06-18 2014-09-17 王明跃 Heating distillation device of steamer pot of white spirits
CN105368681B (en) * 2015-12-17 2018-06-12 乌毡帽酒业有限公司 A kind of alembic cover pipe connecting structure

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH035848U (en) * 1989-06-06 1991-01-21

Also Published As

Publication number Publication date
JPS5592684A (en) 1980-07-14

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