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JPH0341151B2 - - Google Patents
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JPH0341151B2 - - Google Patents

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Publication number
JPH0341151B2
JPH0341151B2 JP59125335A JP12533584A JPH0341151B2 JP H0341151 B2 JPH0341151 B2 JP H0341151B2 JP 59125335 A JP59125335 A JP 59125335A JP 12533584 A JP12533584 A JP 12533584A JP H0341151 B2 JPH0341151 B2 JP H0341151B2
Authority
JP
Japan
Prior art keywords
distillation
hot water
moromi
temperature
wall
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
Application number
JP59125335A
Other languages
Japanese (ja)
Other versions
JPS615773A (en
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 filed Critical
Priority to JP59125335A priority Critical patent/JPS615773A/en
Publication of JPS615773A publication Critical patent/JPS615773A/en
Publication of JPH0341151B2 publication Critical patent/JPH0341151B2/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]

[産業上の利用分野] 本発明は蒸留酒の製造方法に関し、更に詳しく
は発酵後の醪を本来の香味を損わずに減圧蒸留す
る方法に関する。 [従来の技術] 蒸留酒、代表的には焼酎は米、麦等の原料を糖
化、発酵させ、これを蒸留して製造される。焼酎
乙類と呼ばれているものは、原料に由来する香味
を製品に付与するために単式蒸留によつて製造さ
れるもので、従来は常圧下において主に蒸留が行
なわれていたが、近年、効率的でしかも低温で行
なえる減圧下での蒸留が行なわれるようになつて
きた。従来、この種の蒸留においては105〜120℃
(0.2〜1.0Kg/cm2G)程度のスチームが直接的あ
るいは間接的に加熱源として用いられており、減
圧蒸留においても間接熱交換によつて同様にスチ
ームが加熱媒体として用いられているのが現状で
ある。 しかしながら、間接熱交換による減圧蒸留にお
いてスチームを用いると、特に原料として芋、大
豆、酒粕を用いた醪のように粘稠性が高い醪の場
合にはジヤケツト等の加熱面において過熱され易
く、製品の焼酎に異臭が付与され、また、本来の
ふくらみのある味がなくなり極めて辛口になつて
しまうという問題があつた。 [発明が解決しようとする問題点] 本発明は、発酵後の醪を減圧蒸留するにあたつ
て、原料に由来する本来の香味を損わずに蒸留酒
を製造することのできる方法を提供することを目
的とする。 [問題点を解決するための手段] 本発明はこの目的を達成するために、蒸留工程
において、蒸発缶内の醪への熱の供給を、スチー
ムを用いず、100℃以下、好ましくは60乃至100℃
の液体状熱媒体を蒸発缶に循環供給して行なうよ
うにした。すなわち、できるだけ熱媒体の温度を
醪の蒸発温度に近づけ、必要な熱量は液体状態媒
体の蒸発缶への循環量を多くすることによつて補
なうようにしたものである。 液体状熱媒体としては通常、温水が用いられ
る。 蒸留工程以外の処理は従来からの常法を用いる
ことができる。すなわち、焼酎の製造において
は、麹、酵母、水からなる一次醪に主原料及び水
を加えて二次醪として発酵させ、蒸留した後、熟
成、割水、その他必要な処理を行なう。 [実施例の説明] 以下、本発明の方法を添付図面に示した実施例
を基づいて説明する。 添付図面は本発明の方法を実施するための減圧
蒸留装置の系統図である。 図中、符号10はジヤケツト型蒸留缶で、その
周壁は内壁12と外壁14により二重構造となつ
ている。発酵工程を終えた醪16を蒸留缶10内
に仕込み、蒸留缶10内を真空ポンプ18で減圧
にするとともに、蒸留缶10の内壁12を外壁1
4との間の外側室20へ温水を循環供給して醪1
6を加熱しながら蒸留を行なう。この間、醪16
を撹拌機22で撹拌する。温水は温水制御槽24
で、蒸留缶10への供給時の温度が60乃至100℃
になるように導管26から導入されるスチームに
より加熱される。温水の供給温度を加圧状態で
100℃以上にすると粘稠性のある醪の場合に異臭
が付与されるので好ましくなく、また、60℃以下
では蒸留の時間的効率が悪くなるので好ましくな
い。温水制御槽24で加熱された温水は温水循環
ポンプ28により導管30を介して蒸留缶10の
外側室20へ供給され、醪16に熱を供給した
後、外側室20の上部から排出され、導管32を
介して温水制御槽24へと戻される。醪への熱供
給量は蒸留缶10へ供給される温水の温度及び供
給量で調節可能であり、温水の温度は温水制御槽
24へ導入されるスチーム量を調節することによ
り制御され、また、温水の蒸留缶10への供給量
は循環ポンプ28の温水吐出量によつて制御され
る。 アルコール分を多く含んだ留出物は冷却塔34
で冷却され、留液槽36に溜められ、その下部の
弁38から製品として抜き出される。 次にこの装置を用いた具体的実施例を示す。 実験例 甘藷を主原料として前記常法により発酵させた
醪1000(アルコール分14.5V/V%)を蒸留缶
10内に仕込み、真空度−700mmHg(60Torr)で
60乃至100℃の温水を循環させて蒸留を行なつた。
蒸留は3時間で完了した。370(アルコール分
38.2V/V%)の製品芋焼酎が得られた。 比較のために加熱源として温水の代わりに従来
通りスチーム(105℃、0.2Kg/cm2G)を用いて同
様に実験を行なつた。 その結果、スチームを用いた場合は、製品に焦
臭が付与され、蒸留缶の内壁表面には付着物が多
く見られたが、温水を用いた場合は原料本来の香
りが損われず、発酵に伴なう芳香と軽快な香りと
が付与されており、また、蒸留缶の内壁表面にも
付着物は見られなかつた。 上記本発明品と従来品の官能検査(〓酒)の結
果を第1表に示した。この官能検査は102名のパ
ネルに素性が判らないようにして常法により10回
繰返して検査を行なつた結果である。
[Industrial Field of Application] The present invention relates to a method for producing distilled spirits, and more particularly to a method for distilling fermented moromi under reduced pressure without impairing its original flavor. [Prior Art] Distilled spirits, typically shochu, are produced by saccharifying and fermenting raw materials such as rice and barley, and then distilling the resulting product. Shochu Otsu-type is produced by single distillation in order to impart the flavor derived from the raw materials to the product. Traditionally, distillation was mainly carried out under normal pressure, but in recent years Distillation under reduced pressure, which is efficient and can be carried out at low temperatures, has come to be carried out. Conventionally, in this type of distillation, the temperature is 105-120℃.
(0.2 to 1.0 Kg/cm 2 G) is used directly or indirectly as a heating source, and steam is similarly used as a heating medium in vacuum distillation through indirect heat exchange. is the current situation. However, when steam is used in vacuum distillation using indirect heat exchange, especially in the case of highly viscous moromi such as moromi made from potatoes, soybeans, or sake lees, the product is easily overheated on a heating surface such as a jacket. There were problems in that the shochu had a strange odor and lost its original full-bodied taste, becoming extremely dry. [Problems to be Solved by the Invention] The present invention provides a method for producing distilled liquor without impairing the original flavor derived from raw materials when fermented moromi is distilled under reduced pressure. The purpose is to [Means for Solving the Problems] In order to achieve this object, the present invention supplies heat to the moromi in the evaporator in the distillation process at 100°C or lower, preferably at 60°C or lower, without using steam. 100℃
The liquid heating medium was circulated and supplied to the evaporator. That is, the temperature of the heat medium is brought as close as possible to the evaporation temperature of the mash, and the necessary amount of heat is compensated for by increasing the amount of liquid medium that circulates to the evaporator. Warm water is usually used as the liquid heat medium. Conventional methods can be used for treatments other than the distillation step. That is, in the production of shochu, the main raw materials and water are added to a primary moromi consisting of koji, yeast, and water, fermented as a secondary moromi, distilled, and then subjected to aging, diluting, and other necessary treatments. [Description of Examples] Hereinafter, the method of the present invention will be described based on examples shown in the accompanying drawings. The accompanying drawing is a system diagram of a vacuum distillation apparatus for carrying out the method of the invention. In the figure, reference numeral 10 denotes a jacket-type distillation can, the peripheral wall of which has a double structure with an inner wall 12 and an outer wall 14. The moromi 16 that has completed the fermentation process is placed in the distillation can 10, and the inside of the distillation can 10 is reduced in pressure with the vacuum pump 18, and the inner wall 12 of the distillation can 10 is replaced with the outer wall 1.
The hot water is circulated and supplied to the outer chamber 20 between the moromi 1 and 4.
Distillation is carried out while heating 6. During this time, moromi 16
is stirred with a stirrer 22. Hot water is in the hot water control tank 24
The temperature at the time of supply to the distillation vessel 10 is 60 to 100℃.
It is heated by the steam introduced from the conduit 26 so that the temperature becomes . Hot water supply temperature under pressure
A temperature of 100°C or higher is undesirable because it imparts an off-flavor to a viscous mash, and a temperature of 60°C or lower is undesirable because the time efficiency of distillation becomes poor. The hot water heated in the hot water control tank 24 is supplied to the outer chamber 20 of the distillation can 10 via the conduit 30 by the hot water circulation pump 28, and after supplying heat to the moromi 16, is discharged from the upper part of the outer chamber 20, and is passed through the conduit. 32 and is returned to the hot water control tank 24. The amount of heat supplied to the moromi can be adjusted by the temperature and amount of hot water supplied to the still 10, and the temperature of the hot water is controlled by adjusting the amount of steam introduced into the hot water control tank 24. The amount of hot water supplied to the distiller 10 is controlled by the amount of hot water discharged from the circulation pump 28. The distillate containing a large amount of alcohol is sent to the cooling tower 34.
The liquid is cooled, stored in a distillate tank 36, and extracted as a product from a valve 38 at the bottom thereof. Next, a specific example using this device will be shown. Experimental example: 1000 mash (alcohol content: 14.5 V/V%) fermented using sweet potato as the main raw material by the above-mentioned conventional method was placed in a distillation can 10, and the mixture was heated at a vacuum level of -700 mmHg (60 Torr).
Distillation was carried out by circulating hot water at 60 to 100°C.
Distillation was completed in 3 hours. 370 (alcohol content
38.2V/V%) product potato shochu was obtained. For comparison, a similar experiment was conducted using conventional steam (105° C., 0.2 Kg/cm 2 G) instead of hot water as the heating source. As a result, when steam was used, the product had a burnt odor and many deposits were observed on the inner wall surface of the distillation can, but when hot water was used, the original aroma of the ingredients was not impaired and fermentation It had a light aroma and a light aroma associated with it, and no deposits were observed on the inner wall surface of the distillation can. The results of the sensory test (alcohol) for the above-mentioned products of the present invention and conventional products are shown in Table 1. This sensory test was conducted 10 times using conventional methods, with a panel of 102 people blinded to their identities.

【表】 なお、本実施例では、蒸留缶を二重構造のジヤ
ケツト型を採用したが、蒸留缶内に配設した蛇管
に液体状熱媒体を通すようにすることもできる。 [発明の効果] 以上説明したように本発明の方法は、発酵後の
醪を減圧蒸留するに際し、加熱媒体としてスチー
ムを用いず、100℃以下の液体状熱媒体を蒸留缶
に循環供給するようになしたので、得られた製品
に焦臭等の異臭や辛口でピリピリするような異味
が付与されず、原料本来の香りと発酵に伴なう芳
香とが融合された軽快でさわやかな香りを呈し、
マイルドで口当りが良く、のどごしのよい甘口タ
イプの蒸留酒が得られる。また、蒸留後の蒸留缶
の内壁に焦げ等の付着物がないので、保守が容易
となると共に、貯蔵熟成による品質向上効果も従
来法と比較して顕著なものである。 なお、本発明は特に粘稠性の醪に対して有効な
方法であるが、これに限定されるものでないこと
は勿論である。
[Table] In this embodiment, a jacket type distillation can with a double structure is adopted, but it is also possible to pass a liquid heat medium through a flexible pipe arranged inside the distillation can. [Effects of the Invention] As explained above, the method of the present invention does not use steam as a heating medium when distilling fermented moromi under reduced pressure, but instead circulates and supplies a liquid heating medium of 100°C or less to the distillation can. As a result, the resulting product does not have any unusual smells such as burnt odor or dry, tingling tastes, and has a light and refreshing aroma that combines the original aroma of the raw materials with the aroma associated with fermentation. present,
A sweet type of distilled liquor that is mild and pleasant to the touch is obtained. Furthermore, since there is no scorch or other deposits on the inner wall of the distillation can after distillation, maintenance is easy, and the quality improvement effect of storage aging is more remarkable than in conventional methods. Although the present invention is particularly effective for viscous mash, it is of course not limited thereto.

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

添付の図面は本発明の方法を実施するための減
圧蒸留装置の系統図である。 10……蒸留缶、12……内壁、14……外
壁、16……醪、18……真空ポンプ、20……
外側室、24……温水制御槽。
The accompanying drawing is a schematic diagram of a vacuum distillation apparatus for carrying out the method of the invention. 10... Distillation can, 12... Inner wall, 14... Outer wall, 16... Moromi, 18... Vacuum pump, 20...
Outer chamber, 24... hot water control tank.

【特許請求の範囲】[Claims]

1 筐体の前面に、培養槽と、該培養槽内の調整
のための調整液を貯蔵する貯槽と、該培養槽によ
る培養を操作するための操作機器とを有する培養
装置において、該筐体前面の下方に該培養槽を取
付け、該筐体前面の上方であつて中央より右側ま
たは左側に該貯槽を取付け、該筐体前面の上方で
該貯槽を取付けた側の反対側に該操作機器を取付
けたことを特徴とする培養装置。
1. In a culture device having a culture tank, a storage tank for storing a conditioning solution for adjusting the inside of the culture tank, and an operating device for operating culture in the culture tank on the front side of the case, the case The culture tank is installed below the front of the case, the storage tank is installed above the front of the case to the right or left of the center, and the operating device is installed above the front of the case on the opposite side to where the storage tank is installed. A culture device characterized by having a.

JP59125335A 1984-06-20 1984-06-20 Production of distilled liquor by vacuum distillation Granted JPS615773A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP59125335A JPS615773A (en) 1984-06-20 1984-06-20 Production of distilled liquor by vacuum distillation

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP59125335A JPS615773A (en) 1984-06-20 1984-06-20 Production of distilled liquor by vacuum distillation

Publications (2)

Publication Number Publication Date
JPS615773A JPS615773A (en) 1986-01-11
JPH0341151B2 true JPH0341151B2 (en) 1991-06-21

Family

ID=14907562

Family Applications (1)

Application Number Title Priority Date Filing Date
JP59125335A Granted JPS615773A (en) 1984-06-20 1984-06-20 Production of distilled liquor by vacuum distillation

Country Status (1)

Country Link
JP (1) JPS615773A (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP6611286B2 (en) * 2018-01-23 2019-11-27 三和酒類株式会社 Method for producing distilled liquor using microwave distillation
KR102850975B1 (en) * 2018-09-28 2025-08-26 산토리 홀딩스 가부시키가이샤 Sweet potato soju

Also Published As

Publication number Publication date
JPS615773A (en) 1986-01-11

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