JPH07173A - Deaeration device for producing liquor - Google Patents

Deaeration device for producing liquor

Info

Publication number
JPH07173A
JPH07173A JP16855993A JP16855993A JPH07173A JP H07173 A JPH07173 A JP H07173A JP 16855993 A JP16855993 A JP 16855993A JP 16855993 A JP16855993 A JP 16855993A JP H07173 A JPH07173 A JP H07173A
Authority
JP
Japan
Prior art keywords
deaerator
liquor
sake
deaeration device
degassing
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.)
Pending
Application number
JP16855993A
Other languages
Japanese (ja)
Inventor
Katsuhisa Honda
克久 本田
Masazumi Yamashita
正純 山下
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.)
Miura Co Ltd
Original Assignee
Miura Co Ltd
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 Miura Co Ltd filed Critical Miura Co Ltd
Priority to JP16855993A priority Critical patent/JPH07173A/en
Publication of JPH07173A publication Critical patent/JPH07173A/en
Pending legal-status Critical Current

Links

Landscapes

  • Alcoholic Beverages (AREA)
  • Distillation Of Fermentation Liquor, Processing Of Alcohols, Vinegar And Beer (AREA)

Abstract

PURPOSE:To provide a simple and low cost deaeration device used for producing liquors, capable of removing troublesomeness for the addition of chemical agents and for the management of goods in production and distribution processes and enabling to prevent the deterioration of the liquors CONSTITUTION:This deaeration device used in a line for producing a liquor comprises a deaeration device main body (10) for vacuum-sucking off dissolved gases from the liquor and a condensation device (20) connected to the course of a dissolved gas-discharging line (19), and volatile components are condensed and recovered from the dissolved gases discharged from the deaeration device main body with the concentration device (20).

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】この発明は、揮発成分を含有する
溶媒の製造ライン、例えば、高級アルコール類、エステ
ル類などの揮発性の芳香成分を含む清酒,ワイン等の酒
類の製造ラインにおいて用いられる酒造用脱気装置に関
するものである。
FIELD OF THE INVENTION The present invention is used in a production line for a solvent containing a volatile component, for example, in a production line for alcoholic beverages such as sake and wine containing a volatile aromatic component such as higher alcohols and esters. The present invention relates to a deaerator for sake brewing.

【0002】[0002]

【従来の技術】酒類、特に、清酒,ワイン等の醸造酒類
においては、酒中に溶存する酸素の影響による風味の劣
化、変色等が著しい。
2. Description of the Related Art Alcoholic beverages, particularly brewed alcoholic beverages such as sake and wine, are significantly deteriorated in flavor and discolored by the influence of oxygen dissolved in the alcoholic beverage.

【0003】例えば、清酒は、直射日光下では、溶存酸
素と酒中の成分との反応により、2〜3時間で著しい着
色や、異臭が発生する。また、清酒を貯蔵し、熟成させ
る熟成工程においても、貯蔵温度や酸素の混入により、
ヒネ臭や、風味の劣化が生じることがある。更に、工場
出荷後の流通過程においても上記のような劣化は進行す
ることが有り、流通末端においての不良品発生や不良在
庫が生じる場合がある。
For example, in sake, in the direct sunlight, due to the reaction between dissolved oxygen and components in the sake, remarkable coloring and off-flavor occur in 2 to 3 hours. Also, in the aging process of storing and aging sake, due to the storage temperature and the mixing of oxygen,
There may be a fin odor or deterioration of flavor. Further, the above deterioration may progress even in the distribution process after factory shipment, and defective products or defective inventory may occur at the distribution end.

【0004】そこで、このような問題を回避するために
酸化防止剤、合成保存料等を添加することがある。しか
し、上記のような酸化防止剤や合成保存料の添加は、製
造コストを上昇させるだけでなく、酒類の風味を劣化さ
せる要因ともなり、このような品質変化は、昨今のグル
メ志向、本物志向の風潮の中、消費者に対するイメージ
も悪く、購買動機の妨げになってしまう。更に近年の店
頭ディスプレー様式の変化から、明るい場所に陳列され
ることが多く、この点においても劣化に対する防止策が
要望されていた。
Therefore, in order to avoid such problems, antioxidants, synthetic preservatives, etc. may be added. However, the addition of the above-mentioned antioxidants and synthetic preservatives not only increases the manufacturing cost but also deteriorates the flavor of alcoholic beverages, and such quality changes are due to recent gourmet-oriented and genuine-oriented orientations. In the midst of this trend, the image of consumers is bad, which hinders purchasing motives. Further, due to recent changes in store display formats, they are often displayed in bright places, and in this respect also, measures to prevent deterioration have been demanded.

【0005】特に、清酒,ワイン等においては、製造過
程のみならず、工場から出荷後の流通過程での管理も非
常に重要であり、細心の注意が必要で、商品管理が煩わ
しく、管理面での簡便化が要望されている。
In particular, for sake, wine, etc., not only the manufacturing process but also the management in the distribution process after shipment from the factory is very important. There is a demand for simplification.

【0006】[0006]

【発明が解決しようとする課題】そこで、出願人は、以
上のような問題を解消するものとして、酒類を含む液体
飲料を脱気することにより、主に、劣化の原因となる溶
存酸素を除去することを提案している(特開平4−36
178号公報参照)。
Therefore, in order to solve the above problems, the applicant mainly removes dissolved oxygen, which causes deterioration, by degassing a liquid beverage containing alcoholic beverages. Has been proposed (Japanese Patent Laid-Open No. 4-36).
178).

【0007】この方法では、溶存酸素に起因する上述の
各種の問題は解決されるが、この脱気に際して、酒類中
に含まれているエステル、高級アルコール類等の芳香成
分も同時に除去され、商品価値を決定する重要な要素で
ある芳香が減少するという新たな問題を生じていた。
This method solves the above-mentioned various problems caused by dissolved oxygen, but during this deaeration, aromatic components such as esters and higher alcohols contained in alcoholic beverages are also removed at the same time. It created a new problem of reducing fragrance, which is an important factor in determining value.

【0008】即ち、この発明の目的は、酒類から溶存気
体を除去する際に、芳香を有する揮発成分も除去されて
しまうのを防止することである。
That is, an object of the present invention is to prevent the removal of volatile components having an aroma when removing dissolved gas from alcoholic beverages.

【0009】[0009]

【課題を解決するための手段】この発明は、上述の課題
に鑑みてなされたもので、酒類の製造ラインに用いられ
る脱気装置であって、真空吸引によって酒類から溶存気
体を除去する脱気装置本体と、溶存気体の排出ラインの
途中に接続された凝縮装置とから成り、前記脱気装置本
体によって除去された溶存気体から凝縮装置によって揮
発成分を凝縮して回収することを特徴とする。
The present invention has been made in view of the above problems, and is a deaerator used in a liquor production line, which removes dissolved gas from liquor by vacuum suction. The apparatus is characterized by comprising a device main body and a condenser connected in the middle of a dissolved gas discharge line, wherein a volatile component is condensed and recovered from the dissolved gas removed by the degasser main body by a condenser.

【0010】[0010]

【作用】この発明によれば、酒類から溶存酸素を除去
し、酸素の混入を防止することができ、これにより、酸
化による酒類の品質の劣化を防止し、更に、この際に溶
存気体と同時に分離・除去される芳香成分を回収でき
る。
According to the present invention, dissolved oxygen can be removed from liquor and oxygen can be prevented from being mixed, whereby deterioration of liquor quality due to oxidation can be prevented. Aroma components that are separated and removed can be collected.

【0011】[0011]

【実施例】以下、この発明に係る脱気装置の一実施例
を、酒類の製造ラインに適用した場合について、図面を
参照しながら説明する。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENT An embodiment of the deaerator according to the present invention will be described below with reference to the drawings when applied to a liquor production line.

【0012】図1において、(10)は脱気装置本体、(20)
は凝縮装置を示す。上記脱気装置本体(10)は、所謂膜式
脱気装置であって、中空糸状やフィルム状の気体透過膜
を備えた脱気モジュール(11)と、水封式真空ポンプ等の
真空吸引手段(12)とで構成されている。上記の脱気モジ
ュール(11)には、気体透過膜によって仕切られる一方側
の空間に未脱気の清酒(以下、未脱気酒と称する。)の
供給口(13)と、脱気処理後の清酒(以下、脱気清酒と称
する。)の取出口(14)とを接続し、また、他方側の空間
に上記真空吸引手段(12)から延びる真空吸引ライン(18)
を接続してある。そして、上記脱気モジュール(11)内の
気体透過膜によって区画される一方の側に処理液(この
場合は未脱気酒)を流し、他方の側を上記真空吸引手段
(12)によって減圧状態とすることにより、この気体透過
膜を通じて処理液中の溶存気体が吸引除去される構成と
なっている。
In FIG. 1, (10) is the deaerator body, and (20)
Indicates a condenser. The deaerator body (10) is a so-called membrane deaerator, which is a deaerator module (11) including a hollow fiber-shaped or film-shaped gas permeable membrane, and a vacuum suction means such as a water-sealed vacuum pump. It is composed of (12) and. The degassing module (11) has a supply port (13) for undegassed sake (hereinafter referred to as undegassed sake) in a space on one side partitioned by a gas permeable membrane, and a degassing-treated product. Vacuum suction line (18) connected to the take-out port (14) of the sake (hereinafter referred to as deaerated sake) and extending from the vacuum suction means (12) to the space on the other side.
Are connected. Then, the treatment liquid (in this case, undegassed liquor) is flown to one side partitioned by the gas permeable membrane in the degassing module (11), and the other side is the vacuum suction means.
When the pressure is reduced by (12), the dissolved gas in the treatment liquid is sucked and removed through the gas permeable membrane.

【0013】ここで、この実施例において脱気装置とし
て膜式脱気装置を用いたのは、加熱することなく、常温
下で脱気処理可能であり、酒類の品質の劣化が無いから
である。この脱気装置の選定にあっては、溶存酸素濃度
約 3ppm 以下(より好ましくは、約0.5ppm 以下)とな
るような脱気性能のものが好ましい。
Here, the reason why the membrane type deaerator is used as the deaerator in this embodiment is that the deaerating process can be carried out at room temperature without heating and the quality of alcoholic beverages does not deteriorate. . In selecting the deaerator, a deaerator having a dissolved oxygen concentration of about 3 ppm or less (more preferably about 0.5 ppm or less) is preferable.

【0014】尚、脱気度合として溶存酸素濃度を用いる
のは、上記脱気法では、窒素,酸素,炭酸ガス等の溶存
気体が略同一比率で除去されるため、一般的には測定の
容易な溶存酸素量で表示する。
It should be noted that the dissolved oxygen concentration is used as the degree of degassing because, in the above degassing method, dissolved gases such as nitrogen, oxygen and carbon dioxide are removed at substantially the same ratio, so that it is generally easy to measure. The amount of dissolved oxygen is displayed.

【0015】上記凝縮装置(20)は、脱気装置本体(10)か
らの溶存気体の排出ライン(19)の途中に接続される。
尚、この実施例においては、溶存気体排出ライン(19)
は、上記の脱気モジュール(11)と真空吸引手段(12)との
間の真空吸引ライン(18)を兼ねており、凝縮装置(20)
は、この真空吸引ライン(18)の途中に接続されている。
即ち、この排出ライン(19)の一部を成す真空吸引ライン
(18)の途中に接続したタンク(21)と、このタンク(21)の
周囲に配置された冷却ジャケット(22)、この冷却ジャケ
ット(22)に冷却媒体を循環供給するチラー(23)を備え、
上記タンク(21)の底部には揮発成分の取出口(24)を接続
してある。
The condensing device (20) is connected in the middle of the discharge line (19) for the dissolved gas from the deaerator body (10).
In this embodiment, the dissolved gas discharge line (19)
Is also a vacuum suction line (18) between the degassing module (11) and the vacuum suction means (12), the condenser (20)
Is connected in the middle of this vacuum suction line (18).
That is, a vacuum suction line that forms a part of this discharge line (19)
A tank (21) connected in the middle of (18), a cooling jacket (22) arranged around the tank (21), and a chiller (23) for circulating a cooling medium to the cooling jacket (22). ,
A volatile component outlet (24) is connected to the bottom of the tank (21).

【0016】尚、図面において、参照番号(15)は電磁
弁、(16)は流量計、(17)はプレフィルタを示す。
In the drawings, reference numeral (15) is a solenoid valve, (16) is a flow meter, and (17) is a prefilter.

【0017】上記の構成において、その作用を以下に説
明する。まず、醸造工程によって発酵して生成された未
脱気酒を供給口(13)から脱気装置本体(10)に供給し、真
空吸引手段(12)によって減圧状態の脱気モジュール(11)
を通過させることにより、脱気処理を行い、脱気酒の取
出口(14)から取出す。この際、この脱気度合は、溶存酸
素濃度で測定して約 0.5ppm 程度にまで脱気する。この
脱気処理により、清酒中の溶存酸素を極限まで低減させ
ることができ、上記の酸化等品質劣化を有効に防止でき
る。
The operation of the above structure will be described below. First, undeaerated liquor produced by fermentation in the brewing process is supplied from the supply port (13) to the deaerator body (10), and the degassing module (11) is in a depressurized state by the vacuum suction means (12).
Is passed through to degas, and is taken out from the degassing liquor outlet (14). At this time, the degree of degassing should be degassed to about 0.5 ppm as measured by the dissolved oxygen concentration. By this deaeration treatment, the dissolved oxygen in sake can be reduced to the utmost limit, and the above-mentioned quality deterioration such as oxidation can be effectively prevented.

【0018】この脱気処理の際には、清酒中の溶存気体
の他、エステル、高級アルコール類等の芳香成分も脱気
モジュール(11)の気体透過膜を通過し、清酒から分離さ
れ、上記の真空吸引ライン(18)内に流入するが、これら
の芳香成分は沸点が低く、上記の凝縮装置(20)のタンク
(21)内に流入した時点で冷却され、液化してタンク(21)
内に貯溜される。従って、この凝縮装置(20)からは、酸
素、窒素,二酸化炭素等の溶存気体のみが溶存気体排出
ライン(19)を介して排出される。
During this degassing process, in addition to the dissolved gas in sake, aromatic components such as esters and higher alcohols also pass through the gas permeable membrane of the degassing module (11) and are separated from the sake. It flows into the vacuum suction line (18), but these aroma components have low boiling points, and the tank of the above-mentioned condenser (20) is
When it flows into (21), it is cooled, liquefied, and then the tank (21)
It is stored inside. Therefore, only the dissolved gas such as oxygen, nitrogen and carbon dioxide is discharged from the condenser (20) through the dissolved gas discharge line (19).

【0019】このようにして取出された芳香成分は、脱
気後の清酒に添加し、元来の香のよい製品とするのに利
用でき、また、他の食品、調味料の添加物としても利用
できる。
The thus-obtained aroma component can be added to sake after deaeration to be used as a product with an original fragrance, and also as an additive for other foods and seasonings. Available.

【0020】この脱気装置による脱気処理の後は、周知
のように、酵素活性を停止させる火入れ工程、熟成のた
めの熟成工程、割水や他の樽の酒とを調合して風味、ア
ルコール濃度などを調整する調整工程、所定の容器に瓶
詰する瓶詰工程等を経て、製品として出荷する。
After the degassing treatment by the degassing device, as is well known, a burning step for stopping enzyme activity, an aging step for aging, blending with water and other barrel liquor to taste, The product is shipped as a product through an adjustment process of adjusting the alcohol concentration and the like, a bottling process of bottling in a predetermined container, and the like.

【0021】上記の各工程においても、酸素等の混入に
よって着色する可能性をより減少させるために上記脱気
装置による脱気処理を施すのが好ましい。また、上記の
調整工程において使用する割水は、脱気装置によって脱
気された所謂脱気水を用いるとよい。このように脱気水
を用いると、前工程までの溶存酸素の除去効果に加え、
割水の混合の際に溶存酸素の混入を防止することができ
る。また、この割水の脱気度合は、上述同様溶存酸素濃
度で測定して約 0.5ppm 程度とする。
In each of the above steps, it is preferable to carry out a degassing process by the degassing device in order to further reduce the possibility of coloring due to the mixing of oxygen and the like. Moreover, it is good to use what is called deaerated water deaerated by the deaeration device as the split water used in the above adjusting step. By using degassed water in this way, in addition to the effect of removing dissolved oxygen up to the previous step,
It is possible to prevent dissolved oxygen from being mixed in when the divided water is mixed. The degree of degassing of this split water shall be about 0.5 ppm as measured by the dissolved oxygen concentration as above.

【0022】以上のように、本発明装置によれば、酒類
の賞味期限の延長や、変質等によるクレーム・不良在庫
の減少を達成できるうえ、従来、減少してた吟醸香等の
芳香を損なうのを防止できる。
As described above, according to the apparatus of the present invention, it is possible to extend the expiration date of alcoholic beverages, reduce complaints and defective stocks due to alteration, etc., and spoil the fragrance such as ginjo aroma, which has been reduced in the past. Can be prevented.

【0023】尚、以上の説明では、この発明を清酒に適
用した場合について説明したが、清酒以外にも、その他
の酒類、醤油等の液体調味料等の醸造製品の製造ライン
中において適用することができる。
In the above description, the case where the present invention is applied to sake is explained. However, in addition to sake, it should be applied in the production line of brewed products such as other alcoholic beverages and liquid seasonings such as soy sauce. You can

【0024】また、本発明装置によって得られる芳香成
分は、脱気の対象とした酒類に添加する他、他の食品、
調味料、飲料等に添加することもできる。
The aroma component obtained by the device of the present invention is added to alcoholic beverages to be degassed, other foods,
It can also be added to seasonings, beverages and the like.

【0025】更に、脱気膜を、アルコール蒸気を透過し
得る性能のものを選択しておけば、上記の様な高級アル
コール、高級エステル類のほか、各種揮発成分を回収す
ることができるため、簡易的な蒸留装置としての利用も
可能である。
Further, if the degassing membrane is selected so that it can permeate alcohol vapor, various volatile components can be recovered in addition to the higher alcohols and higher esters as described above. It can also be used as a simple distillation device.

【0026】[0026]

【発明の効果】この発明は、以上のような構成であるの
で、清酒,ワイン等の醸造酒類を含む醸造製品中の溶存
酸素の除去、並びに、酸素の再溶存防止が達成できるた
め、その酸化を防止することができ、酒類の風味の劣化
が変色を防止し、初期の良好な風味や色を長期間にわた
って維持することができ、製品の賞味期限の延長や、変
質等によるクレーム・不良在庫の減少を達成できる。
EFFECTS OF THE INVENTION Since the present invention has the above-mentioned constitution, it is possible to remove dissolved oxygen in brewed products including brewed liquors such as sake and wine, and to prevent re-dissolution of oxygen. It is possible to prevent the deterioration of the flavor of alcoholic beverages from discoloring, maintain the initial good flavor and color for a long time, extend the shelf life of the product, claim complaints due to deterioration, etc. Can be achieved.

【0027】又、従来の窒素曝気法や加熱脱気法におけ
る、不純物の混入や熱による成分変化などの不具合を解
消でき、脱酸素剤,酸化防止剤等の薬品を使用しないの
で、安全性に優れ、しかもランニングコストが低い。
Further, in the conventional nitrogen aeration method and thermal deaeration method, problems such as mixing of impurities and component changes due to heat can be solved, and chemicals such as oxygen scavengers and antioxidants are not used, so safety is improved. Excellent and low running cost.

【0028】しかも、従来、上記のような効果を得るた
めに損なわれていた揮発性の芳香成分を回収することが
できるため、この芳香成分をもとの溶媒に添加すること
により、香のよい製品とすることができ、また、この芳
香成分を他の食品、調味料、飲料等の添加物としても利
用できる。
Moreover, since the volatile aroma component, which has been impaired in order to obtain the above-mentioned effects, can be recovered in the past, by adding the aroma component to the original solvent, the fragrance is improved. It can be used as a product, and the aromatic component can be used as an additive for other foods, seasonings, beverages and the like.

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

【図1】この発明に係る酒類用脱気装置の一実施例を示
す概略構成図である。
FIG. 1 is a schematic configuration diagram showing an embodiment of an alcoholic degassing apparatus according to the present invention.

【符号の説明】[Explanation of symbols]

(10) 脱気装置本体 (11) 脱気モジュール (12) 真空吸引手段 (19) 溶存気体排出ライン (20) 凝縮装置 (21) タンク (22) 冷却ジャケット (23) チラー (10) Deaerator body (11) Deaerator module (12) Vacuum suction means (19) Dissolved gas discharge line (20) Condenser (21) Tank (22) Cooling jacket (23) Chiller

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 酒類の製造ラインに用いられる脱気装置
であって、真空吸引によって酒類から溶存気体を除去す
る脱気装置本体(10)と、溶存気体の排出ライン(19)の途
中に接続された凝縮装置(20)とから成り、前記脱気装置
本体によって除去された溶存気体から凝縮装置(20)によ
って揮発成分を凝縮して回収することを特徴とする酒造
用脱気装置。
1. A deaerator used in a liquor production line, which is connected between a deaerator body (10) for removing dissolved gas from liquor by vacuum suction and a dissolved gas discharge line (19). A deaerator for sake brewing, which comprises a condensed device (20) and which collects the volatile components from the dissolved gas removed by the deaerator body by condensing the volatile components by the condensing device (20).
JP16855993A 1993-06-14 1993-06-14 Deaeration device for producing liquor Pending JPH07173A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP16855993A JPH07173A (en) 1993-06-14 1993-06-14 Deaeration device for producing liquor

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP16855993A JPH07173A (en) 1993-06-14 1993-06-14 Deaeration device for producing liquor

Publications (1)

Publication Number Publication Date
JPH07173A true JPH07173A (en) 1995-01-06

Family

ID=15870279

Family Applications (1)

Application Number Title Priority Date Filing Date
JP16855993A Pending JPH07173A (en) 1993-06-14 1993-06-14 Deaeration device for producing liquor

Country Status (1)

Country Link
JP (1) JPH07173A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2012037535A2 (en) * 2010-09-19 2012-03-22 Kornacki Daniel C Method and apparatus for treating fermented liquids

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2012037535A2 (en) * 2010-09-19 2012-03-22 Kornacki Daniel C Method and apparatus for treating fermented liquids
WO2012037535A3 (en) * 2010-09-19 2012-07-12 Kornacki Daniel C Method and apparatus for treating fermented liquids

Similar Documents

Publication Publication Date Title
Catarino et al. Dealcoholizing wine by membrane separation processes
CA2119901C (en) Production of fermented malt beverages
JPS59125885A (en) Concentration fo alcohol benerage
JPH0760005A (en) Dearation of liquid product
IE56753B1 (en) Concentration of alcoholic beverages
JPH025849A (en) Method and apparatus for reducing alcohol content of alcoholic beverage
US20160097024A1 (en) Alcohol Reduction In Beverages
US5520943A (en) Method for modifying the quality of liquid foodstuff
CA1307471C (en) Process for partial or total dalcoholization of wine and/or cider and apparatus therefore
JPS61166388A (en) High concentration beer product and its production
De Francesco et al. Influence of the dealcoholisation by osmotic distillation on the sensory properties of different beer types
US5695795A (en) Methods for chill-treating non-distilled malted barley beverages
JPH07173A (en) Deaeration device for producing liquor
US20050069606A1 (en) Sparkling low alcoholic beverage sake and producing method thereof
US5869114A (en) Production of fermented malt beverages
JP3187442B2 (en) Production method of alcoholic beverages
JP2007289166A (en) Method for maturing liquor and matured liquor
JP2003230374A (en) Fruit juice-containing alcoholic beverage contained in vessel and method for producing the same
JP4697820B2 (en) Method for producing brewed sake
Bosco et al. Investigation of the effects of oxygen and other considerations on the shelf-life of craft beer
USRE36897E (en) Methods for chill treating non-distilled malted barley beverages
JP2002065238A (en) Method for producing liquors
CA3029441A1 (en) Draught beer with a high co2 content
US2088360A (en) Making alcoholic liquors
JP7128561B1 (en) Refined sake manufacturing method and refined sake