JPH035280Y2 - - Google Patents
Info
- Publication number
- JPH035280Y2 JPH035280Y2 JP1987162680U JP16268087U JPH035280Y2 JP H035280 Y2 JPH035280 Y2 JP H035280Y2 JP 1987162680 U JP1987162680 U JP 1987162680U JP 16268087 U JP16268087 U JP 16268087U JP H035280 Y2 JPH035280 Y2 JP H035280Y2
- Authority
- JP
- Japan
- Prior art keywords
- distillation
- collector
- components
- boiling
- vapor
- 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
Links
Description
[産業上の利用分野]
本考案は、焼酎、ウイスキー、ブランデー等の
蒸溜酒の醗酵醪において、この醗酵醪を蒸溜缶内
部で煮沸して得られた酒精蒸気中に含まれるイソ
アミルアルコール、プロパノール、ブタノール、
フルフラール等の高沸点成分を除去する装置を有
する蒸溜酒の単式蒸溜装置に関するものである。
[従来の技術とその問題点]
醗酵醪を煮沸させて発生した酒精蒸気には、酒
の味覚や香りを悪くする、沸点が97℃〜132℃前
後のイソアミルアルコール、プロパノール、ブタ
ノール、フルフラール等の高沸点成分が含まれて
いる。
しかし、従来の単式蒸溜装置は、蒸溜缶で発生
した酒精蒸気を直接擬縮器へ送り込んで冷却し原
酒を得ているため、高沸点成分の除去がされず味
覚や香りのよい製品を得難かつた。
そこで、単式蒸溜装置を用いて高沸点成分の除
去した品質のよい製品を得るために、種々工夫さ
れている。
例えば、その一つの装置としては、蒸溜缶の上
部に精溜棚を設けて、酒精蒸気を精溜棚を経由さ
せて凝縮器へ送ることにより、精溜棚において高
沸点成分を除去する単式蒸溜装置がよく知られて
いる。
しかし、この方法であると装置の構造が複雑に
なるとともに、高沸点成分が精溜棚に残留する傾
向があり、この残留した高沸点成分が次に蒸溜し
た酒精蒸気へ混入して、製品の品質を悪くする場
合が多い。さらに、単式蒸溜装置は、蒸溜缶の内
部に一定量の醗酵醪を収納して煮沸するため、煮
沸とともに醗酵醪より蒸発する酒精蒸気の成分が
変化し、この酒精蒸気中の高沸点成分の量も変化
する。このためこの変化とともに除去する高沸点
成分の量も変化させないと、蒸溜酒の品質が一定
にならないという欠点がある。
[問題点を解決するための手段]
本考案は、上記問題点を解決するために考案さ
れたものであつて、酒成分を含む醗酵醪の原液を
煮沸して酒精蒸気を発生させる蒸溜缶と、酒精蒸
気を冷却して原酒を得る凝縮器とを備えた蒸溜酒
の単式蒸溜装置において、周壁の一部に冷却水が
供給されるジヤケツト部を有し、酒精蒸気中に含
まれる高沸点成分を凝縮して除去するサイクロン
型の補集器を、蒸溜缶から凝縮器に至る経路の途
中に設けるとともに、この補集器から蒸溜缶へ前
記高沸点成分を還流させる経路を設けてなるもの
である。
[作用]
上記構成の単式蒸溜装置において、醗酵醪を蒸
溜缶内部で煮沸して発生した酒精蒸気は補集器内
部に至る。補集器のジヤケツト部内部へ供給され
ている冷却水によつてこの酒精蒸気が冷却される
ことにより、酒精蒸気中の高沸点成分が分離すな
わち液化して、酒精蒸気より除去される。除去さ
れた高沸点成分は、蒸溜缶へ還流経路を経て還流
される。高沸点成分が除去された酒精蒸気は凝縮
器において冷却され原酒となる。
[実施例]
以下、本考案の一実施例を図面に基づいて説明
する。
本考案の減圧式単式蒸溜装置10は以下の構造
を有している。
12は醗酵醪の酒成分を含む原液Aを煮沸して
酒精蒸気を発生させる蒸溜缶、16は酒精蒸気中
の高沸点成分を除去するサイクロン型の補集器、
18は酒精蒸気を凝縮して蒸溜酒を得る凝縮器で
ある。蒸溜缶12と補集器16はスワンネツク状
の蒸気排出路14aによつて接続され、補集器1
6と凝縮器18は蒸気排出路14bによつて接続
されている。
蒸溜缶12の上部には、醗酵醪の原液Aを供給
する給入口26を設けている。蒸溜缶12の周壁
の構造を二重にすることによりジヤケツト加熱部
28を設け、蒸気給入管30より高温に加熱した
水蒸気をジヤケツト加熱部28へ送り込んで蒸溜
缶12内部を加熱する。また、加熱水蒸気が循環
するコイル式の加熱管32を蒸溜缶12の内部に
設けている。そして、これらジヤケツト加熱部2
8と加熱管32により醗酵醪の原液Aを万遍なく
煮沸する。なお、ジヤケツト加熱部28を循環し
た水蒸気は、蒸気ドレーン34より排出される。
補集器16の周壁を二重構造にしてジヤケツト
冷却部36を設けている。このジヤケツト冷却部
36の内部へ、給水管38より冷却水を供給して
循環させ、これにより補集器16の内部を冷却す
る構造となつている。この冷却水は排水管40よ
り排出できる。また、底部には、酒精蒸気から凝
縮した液体を蒸溜缶12内部へ戻す還流経路42
を設けている。
凝縮器18内部には、冷却管20を設け、酒精
蒸気がこの冷却管20内部を流通する間に冷却水
によつて冷却され凝縮される。また、前記凝縮器
18には、製品タンク22が接続され、凝縮器1
8により凝縮された蒸溜酒はこの製品タンク22
に貯留される。
蒸溜缶12から凝縮器18を経て製品タンク2
2に至る蒸溜経路の一部、例えば、図示の場合に
は製品タンク22の部分に真空ポンプ24を接続
することにより、蒸溜経路を減圧状態にして蒸溜
できるようになつている。
以下、上記の構成を有する蒸溜装置10を用い
ての蒸溜作業を説明する。
蒸溜缶12に所要量の焼酎醪の原液Aを収納し
た状態で加熱源である加熱管32とジヤケツト加
熱部28にゲージ圧力0.3Kg/cm2〜3Kg/cm2の水
蒸気を供給して加熱し、前記原液Aを万遍なく煮
沸する。
煮沸によつて発生した酒精蒸気は蒸気排出路1
4aを通つて補集器16に入る。補集器16内部
はジヤケツト冷却部36内部を流通する冷却水に
よつて冷却されているため、まず、酒精蒸気中の
高沸点成分が凝縮して、酒精蒸気より分縮され
る。高沸点成分としては、沸点が97℃〜132℃前
後のイソアミルアルコール、プロパノール、ブタ
ノール、フルフラール等が主なものである。ま
た、エステル類の中沸点成分、アセトアルデヒド
等の低沸点成分も分縮される。さらに、蒸溜缶1
2より上昇した飛抹も凝縮される。
本考案は単式蒸溜装置であることにより、蒸溜
缶12の内部に一定量の醗酵醪Aを収納して煮沸
している。そのため、煮沸する時間とともに蒸発
する酒精蒸気の成分が変化し、高沸点成分の量も
変化する。このため、除去する高沸点成分の量も
変化させないと得られた焼酎の品質が一定になら
ないので、ジヤケツト冷却部36内部を粒通する
冷却水の量と温度を変化させて除去する高沸点成
分の量を変化させる。この場合、冷却水の量と温
度は簡単に制御できるため、容易に品質のよい焼
酎を得ることができる。
凝縮された液体状の高沸点成分等は、補集器1
6の底部に設けられた還流経路42を経て蒸溜缶
12内部の焼酎醪の原液Aに戻される。そして、
これら高沸点成分等のうち有効酒成分は、再び蒸
溜缶12内部で煮沸され酒精蒸気となることによ
り、焼酎醪の原液Aを無駄なく効率よく蒸溜でき
る。
除去した高沸点成分等は、還流されて補集器1
6に残留せず、次に蒸溜する酒精蒸気に混入して
焼酎の品質を悪くすることがない。
高沸点成分が分縮された酒精蒸気は蒸気排出路
14bを経て凝縮器18に入り、ここで冷却され
て凝縮され蒸溜液、すなわち、焼酎の製品とな
る。
この焼酎の製品は、製品タンク22内に送られ
貯溜される。
この蒸溜経路は真空ポンプ24により真空に近
い減圧状態に保持されていることにより蒸溜缶1
2内部の原液Aは45℃〜60℃の加熱温度で煮沸す
れば蒸溜は良好に行なわれる。
上記補集器16を接続した本考案の蒸溜装置1
0を使用して製造した焼酎と、補集器16を接続
せず蒸気排出器14a,14bとを直接接続した
従来の蒸溜装置によつて製造した焼酎とにおい
て、これら焼酎に含まれる高沸点成分、中沸点成
分とをそれぞれ比較分析した結果を第1表に示
す。
[Industrial Field of Application] The present invention is used for fermentation of distilled spirits such as shochu, whiskey, brandy, etc., and isoamyl alcohol, propanol, butanol,
The present invention relates to a single distillation device for distilled spirits that includes a device for removing high-boiling components such as furfural. [Conventional technology and its problems] Alcohol vapor generated by boiling fermented mash contains substances such as isoamyl alcohol, propanol, butanol, and furfural, which have a boiling point of around 97°C to 132°C, and which deteriorate the taste and aroma of alcoholic beverages. Contains high boiling point components. However, in conventional single distillation equipment, the alcohol vapor generated in the still can is sent directly to the pseudo-condenser and cooled to obtain unprocessed sake, which does not remove high-boiling components and makes it difficult to obtain products with good taste and aroma. It was. Therefore, various efforts have been made to obtain high-quality products from which high-boiling components have been removed using single distillation equipment. For example, one such device is a single distillation system in which high-boiling components are removed in the distillation shelf by installing a rectification shelf above the distillation can and sending the alcohol vapor through the distillation shelf to the condenser. The device is well known. However, with this method, the structure of the equipment becomes complicated, and high-boiling components tend to remain in the rectifying shelf, and these remaining high-boiling components mix into the next distilled alcoholic vapor, resulting in the product being contaminated. This often results in poor quality. Furthermore, in a single distillation device, a certain amount of fermentation mash is stored inside the still can and boiled, so the components of the alcoholic spirit vapor that evaporates from the fermentation mash change as it boils, and the amount of high boiling point components in this alcoholic vapor changes. also changes. Therefore, unless the amount of high-boiling components removed is also changed along with this change, there is a drawback that the quality of the distilled liquor will not be constant. [Means for Solving the Problems] The present invention was devised to solve the above problems, and includes a distillation can that generates alcoholic vapor by boiling a stock solution of fermented moromi containing alcoholic ingredients. , a single distillation device for distilled spirits equipped with a condenser that cools alcohol vapor to obtain raw liquor, which has a jacket part on a part of the peripheral wall to which cooling water is supplied, and high boiling point components contained in alcohol vapor. A cyclone-type collector for condensing and removing the high-boiling components is provided in the middle of the path from the still to the condenser, and a path is provided for refluxing the high-boiling components from the collector to the still. be. [Function] In the single distillation apparatus configured as described above, the alcoholic spirit vapor generated by boiling the fermented mash inside the still reaches the inside of the collector. By cooling this alcohol vapor with the cooling water supplied into the jacket portion of the collector, high boiling point components in the alcohol vapor are separated, that is, liquefied, and removed from the alcohol vapor. The removed high-boiling components are refluxed to the still via a reflux route. Alcohol vapor from which high-boiling components have been removed is cooled in a condenser and becomes unprocessed sake. [Example] Hereinafter, an example of the present invention will be described based on the drawings. The vacuum type single distillation apparatus 10 of the present invention has the following structure. 12 is a distiller that boils the stock solution A containing the alcohol components of the fermented moromi to generate alcohol vapor; 16 is a cyclone-type collector that removes high-boiling components from the alcohol vapor;
18 is a condenser that condenses alcohol vapor to obtain distilled liquor. The distillation can 12 and the collector 16 are connected by a swan neck-shaped steam discharge passage 14a, and the collector 1
6 and the condenser 18 are connected by a steam exhaust path 14b. At the top of the distillation can 12, there is provided an inlet 26 for supplying the stock solution A of fermentation mash. A jacket heating section 28 is provided by duplicating the structure of the peripheral wall of the distillation can 12, and steam heated to a high temperature is sent to the jacket heating section 28 from a steam supply pipe 30 to heat the inside of the distillation can 12. Further, a coil-type heating pipe 32 through which heated steam circulates is provided inside the distiller 12. And these jacket heating parts 2
8 and a heating tube 32 to evenly boil the fermentation mash stock solution A. Note that the water vapor that has circulated through the jacket heating section 28 is discharged from the steam drain 34. The circumferential wall of the collector 16 has a double structure and a jacket cooling section 36 is provided. Cooling water is supplied into the jacket cooling section 36 from a water supply pipe 38 and circulated, thereby cooling the inside of the collector 16. This cooling water can be discharged from the drain pipe 40. In addition, at the bottom, there is a reflux path 42 for returning liquid condensed from alcohol vapor to the inside of the distillation can 12.
has been established. A cooling pipe 20 is provided inside the condenser 18, and while alcohol vapor flows through the cooling pipe 20, it is cooled by cooling water and condensed. Further, a product tank 22 is connected to the condenser 18, and a product tank 22 is connected to the condenser 18.
The distilled liquor condensed by 8 is transferred to this product tank 22.
is stored in From the distillation can 12 to the product tank 2 via the condenser 18
By connecting a vacuum pump 24 to a part of the distillation route leading to the product tank 22, for example, in the illustrated case, a part of the product tank 22, the distillation route can be brought into a reduced pressure state and distillation can be carried out. Hereinafter, a distillation operation using the distillation apparatus 10 having the above configuration will be explained. With the required amount of undiluted shochu liquor A stored in the still can 12, water vapor at a gauge pressure of 0.3 kg/cm 2 to 3 kg/cm 2 is supplied to the heating tube 32 and the jacket heating section 28, which are heating sources, to heat it. , Boil the stock solution A evenly. Alcohol vapor generated by boiling is passed through steam exhaust path 1.
It enters the collector 16 through 4a. Since the inside of the collector 16 is cooled by the cooling water flowing inside the jacket cooling section 36, first, high boiling point components in the alcoholic spirit vapor are condensed and fractionated from the alcoholic vapor. The main high-boiling components are isoamyl alcohol, propanol, butanol, furfural, etc., each having a boiling point of about 97°C to 132°C. In addition, medium-boiling components such as esters and low-boiling components such as acetaldehyde are also fractionated. In addition, distillation can 1
The air that increased from 2 is also condensed. Since the present invention is a single distillation device, a certain amount of fermented mash A is stored inside the still can 12 and boiled. Therefore, the components of the alcohol vapor that evaporate change with the boiling time, and the amount of high-boiling components also changes. For this reason, the quality of the obtained shochu will not be constant unless the amount of high-boiling components to be removed is changed. change the amount of In this case, since the amount and temperature of the cooling water can be easily controlled, high quality shochu can be easily obtained. Condensed liquid high-boiling components, etc. are collected in the collector 1.
It is returned to the stock solution A of shochu moromi inside the distillation can 12 through a reflux path 42 provided at the bottom of the shochu moromi 6. and,
Among these high boiling point components, the effective liquor components are boiled again inside the still can 12 and turned into liquor vapor, so that the undiluted solution A of shochu moromi can be efficiently distilled without waste. The removed high-boiling components are refluxed and sent to the collector 1.
6, and will not mix with the alcoholic spirit vapor to be distilled next and deteriorate the quality of shochu. The alcohol vapor from which the high boiling point components have been fractionated enters the condenser 18 through the vapor discharge path 14b, where it is cooled and condensed to become a distillate, that is, a shochu product. This shochu product is sent to a product tank 22 and stored therein. This distillation path is maintained in a reduced pressure state close to vacuum by a vacuum pump 24, so that the distillation can 1
If the stock solution A inside No. 2 is boiled at a heating temperature of 45°C to 60°C, distillation will be carried out well. Distillation apparatus 1 of the present invention connected to the collector 16
0, and shochu produced by a conventional distillation apparatus in which the collector 16 is not connected and the steam dischargers 14a and 14b are directly connected, the high boiling point components contained in these shochu Table 1 shows the results of a comparative analysis of , medium-boiling point components, respectively.
【表】【table】
【表】
第1表において、イソアミルアルコール、プロ
パノール、ブタノールは、フーゼル油に含まれて
いることにより、これら高沸点成分は油脂酸化指
標値によつて示す。紫外部吸光度は、10m/m石
英セル、波長275nmにて測定し、また、油脂酸化
指標値は、2−チオバルピツール酸による発色を
10m/m石英セル、波長530nmにて測定されたも
のである。
第1表より本考案の酒精装置10の方が補集器
16を備えていない従来の蒸溜装置より酒精蒸気
中の高沸点成分、中沸点成分、低沸点成分をよく
除去でき、そのため、味覚と香りがよい焼酎を得
ることができる。
なお、本実施例では、真空ポンプ24を備えた
減圧式の単式蒸溜装置について説明したが、これ
に限らず本考案は、常圧式の単式蒸溜装置に用い
ても減圧式と同様に良好なる結果が得られる。こ
の場合、蒸溜缶内部の醗酵醪の原液Aを加熱する
手段は、前記実施例のジヤケツト加熱部28と加
熱管32に代えて、原液Aに加熱水蒸気を直接吹
き込む手段にする。
さらに、本実施例では焼酎の蒸溜装置について
説明したが、これに限らず、ウイスキー、ブラン
デー等の蒸溜酒の単式蒸溜装置に使用してもよ
い。
[考案の効果]
上記で説明したように、本考案の蒸溜酒の単式
蒸溜装置は、醗酵醪を煮沸して発生した酒精蒸気
より高沸点成分を補集器において効率よく取り除
いて、味覚と香りがよい原酒を得ることができ、
また、除去した高沸点成分等は、蒸溜缶へ還流さ
れて補集器には残留せず、次に蒸溜する酒精蒸気
に混入して焼酎の品質を悪くすることがない。
また、構造も蒸溜缶と凝縮器との間にジヤケツ
ト部を装備した補集器を設けるだけの簡単な構造
であるとともに、前記ジヤケツト部へ供給する冷
却水の温度と量により、簡単に高沸点成分を除去
する量を調節できる。[Table] In Table 1, since isoamyl alcohol, propanol, and butanol are contained in fusel oil, these high boiling point components are indicated by the fat oxidation index value. The ultraviolet absorbance was measured using a 10m/m quartz cell at a wavelength of 275nm, and the oil and fat oxidation index values were measured using 2-thiobalpituric acid.
Measurements were taken using a 10m/m quartz cell and a wavelength of 530nm. Table 1 shows that the alcohol distillation device 10 of the present invention can remove high-boiling point components, medium-boiling point components, and low-boiling point components from alcohol vapor better than the conventional distillation device that is not equipped with a collector 16, and as a result, it improves the taste. You can get shochu with a good aroma. In this embodiment, a vacuum-type single distillation apparatus equipped with a vacuum pump 24 has been described, but the present invention is not limited to this, and the present invention can also be used in an ordinary-pressure single-type distillation apparatus with good results similar to the vacuum distillation apparatus. is obtained. In this case, the means for heating the stock solution A of the fermentation mash inside the still is a means for directly blowing heated steam into the stock solution A, instead of the jacket heating section 28 and the heating tube 32 of the previous embodiment. Further, in this embodiment, a shochu distillation apparatus has been described, but the present invention is not limited to this, and the present invention may be used in a single distillation apparatus for distilled spirits such as whiskey and brandy. [Effects of the invention] As explained above, the distilled liquor single distillation apparatus of the present invention efficiently removes high-boiling components from the alcohol vapor generated by boiling the fermented mash in the collector, improving the taste and aroma. You can get good unprocessed sake,
In addition, the removed high-boiling components are refluxed to the still and do not remain in the collector, and do not mix with the alcohol vapor to be distilled next and deteriorate the quality of the shochu. In addition, the structure is simple, just installing a collector equipped with a jacket between the distillation can and the condenser, and the temperature and amount of cooling water supplied to the jacket can easily be adjusted to a high boiling point. The amount of components removed can be adjusted.
図は本考案の蒸溜装置を示し、一部を断面にし
た略示図である。
符号の説明、A……醗酵醪の原液、10……単
式蒸溜装置、12……蒸溜缶、16……補集器、
18……凝縮器、20……ジヤケツト冷却部、4
2……還流経路。
The figure shows a distillation apparatus according to the present invention, and is a schematic diagram with a part cut away. Explanation of the symbols, A...Fermentation moromi stock solution, 10...Single distillation device, 12...Still can, 16...Collector,
18... Condenser, 20... Jacket cooling section, 4
2... Reflux route.
Claims (1)
を発生させる蒸溜缶と、酒精蒸気を冷却して原酒
を得る凝縮器とを備えた蒸溜酒の単式蒸溜装置に
おいて、 周壁の一部に冷却水が供給されるジヤケツト部
を有し、酒精蒸気中に含まれる高沸点成分を擬縮
して除去するサイクロン型の補集器を、蒸溜缶か
ら擬縮器に至る経路の途中に設けるとともに、こ
の補集器から蒸溜缶へ前記高沸点成分を還流させ
る経路を設けてなることを特徴とする蒸溜酒の単
式蒸溜装置。[Scope of Claim for Utility Model Registration] A single distillation device for distilled spirits, which is equipped with a distillation can that boils a stock solution of fermented moromi containing alcohol components to generate alcohol vapor, and a condenser that cools the alcohol vapor to obtain unprocessed sake. In this method, a cyclone-type collector, which has a jacket part on a part of the peripheral wall to which cooling water is supplied, and which pseudo-condenses and removes high-boiling components contained in alcohol vapor, is transferred from the distillation can to the pseudo-condenser. 1. A single-type distillation apparatus for distilled spirits, characterized in that a path is provided in the middle of a path to reach the collector, and a path is provided for refluxing the high-boiling components from the collector to the distillation can.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1987162680U JPH035280Y2 (en) | 1987-10-23 | 1987-10-23 |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1987162680U JPH035280Y2 (en) | 1987-10-23 | 1987-10-23 |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH0166899U JPH0166899U (en) | 1989-04-28 |
| JPH035280Y2 true JPH035280Y2 (en) | 1991-02-12 |
Family
ID=31446723
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP1987162680U Expired JPH035280Y2 (en) | 1987-10-23 | 1987-10-23 |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH035280Y2 (en) |
Family Cites Families (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS6137908A (en) * | 1984-07-27 | 1986-02-22 | Nippon Steel Corp | Operating method of converter |
| JPS62208266A (en) * | 1986-03-07 | 1987-09-12 | Chem Plant:Kk | Vacuum and continuous concentrating treatment apparatus for distillation waste liquor of shochu (low-class distilled spirit) |
-
1987
- 1987-10-23 JP JP1987162680U patent/JPH035280Y2/ja not_active Expired
Also Published As
| Publication number | Publication date |
|---|---|
| JPH0166899U (en) | 1989-04-28 |
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