JPH02273171A - Treatment of japanese rice wine - Google Patents

Treatment of japanese rice wine

Info

Publication number
JPH02273171A
JPH02273171A JP1094448A JP9444889A JPH02273171A JP H02273171 A JPH02273171 A JP H02273171A JP 1094448 A JP1094448 A JP 1094448A JP 9444889 A JP9444889 A JP 9444889A JP H02273171 A JPH02273171 A JP H02273171A
Authority
JP
Japan
Prior art keywords
sake
exchange resin
acid
anion exchange
type
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.)
Granted
Application number
JP1094448A
Other languages
Japanese (ja)
Other versions
JP2836842B2 (en
Inventor
Ikuo Toyoda
豊田 伊久雄
Shiro Nakanishi
中西 志郎
Tsuguaki Tomonaga
鞆永 継明
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.)
TOYODA SYUZO KK
Organo Corp
Original Assignee
TOYODA SYUZO KK
Organo Corp
Japan Organo Co Ltd
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Filing date
Publication date
Application filed by TOYODA SYUZO KK, Organo Corp, Japan Organo Co Ltd filed Critical TOYODA SYUZO KK
Priority to JP9444889A priority Critical patent/JP2836842B2/en
Publication of JPH02273171A publication Critical patent/JPH02273171A/en
Application granted granted Critical
Publication of JP2836842B2 publication Critical patent/JP2836842B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Abstract

PURPOSE:To accomplish the distribution at normal temperature of fresh raw Japanese rice wine retaining its inherent flavor with its putrefaction prevented, by treating Japanese wine with an OH-type anion exchange resin and an organic acid-type anionic resin to remove the mevalonic acid in the wine. CONSTITUTION:Japanese rice wine is brought into contact with an OH-type anion exchange resin and an organic acid-type anionic resin (the organic acid being at least one selected from citric acid, malic acid, succinic acid and lactic acid) either simultaneously or in any order, and, when appropriate, further brought into contact with a H-type cation exchange resin.

Description

【発明の詳細な説明】 (産業上の利用分野) 本発明は、清酒(生酒、火入殺菌酒)の精製処理方法に
関するものである。
DETAILED DESCRIPTION OF THE INVENTION (Industrial Field of Application) The present invention relates to a method for refining sake (raw sake, sterilized pasteurized sake).

(従来の技術) 清酒には、上槽後、前処理しないで製品とされるものと
、活性炭やr通則で粗処理する前処理を行なうものと、
更に所謂「火入」と称される加熱殺菌を行なって製品と
するものがあり、前2者は「火入」を行なわないために
通常生酒と呼ばれ後者は火入酒と呼ばれる。
(Prior art) There are two types of sake: sake that is made into a product without any pretreatment after the upper tank, and sake that is pretreated with rough treatment using activated carbon or R general rules.
Furthermore, there are products that undergo heat sterilization called ``hiiri''; the former two are usually called namazake because ``hiiri'' is not performed, and the latter is called hiiri.

前記火入酒における加熱殺菌は清酒が腐敗するのを防止
する目的で腐敗の原因となる火落菌を加熱(60〜65
℃)により滅菌して除去することを内容とする。なお加
熱処理の後に火落菌が再び清酒に混入することがあれば
火入酒であっても腐敗の問題は避けられないので、一般
に火落菌が繁殖し易い環境にある清酒処理工場等におい
ては瓶詰段階等について無菌化雰囲気が必要とされてい
る。
Heat sterilization in the above-mentioned sake is done by heating the hiochi bacteria that cause spoilage (60 to 65
℃) and then removed. Furthermore, if Hiotchi bacteria re-enters the sake after heat treatment, the problem of spoilage is unavoidable even if the sake is heated. A sterile atmosphere is required for the steps, etc.

他方生酒は、発酵槽で熟成されたもろみを上槽した後、
殺菌及び発酵停止を目的とした火入加熱を行なわないも
のであるために通常の状態では清酒を長く保存すると腐
敗するという問題が顕著にあり、例えば清酒を一21℃
以下に一旦凍結させて酒質を変化をさせないでチルド流
通させ、清酒の腐敗を防ぐ流通方法が考えられ実際に行
なわれている。しかしこの方法は流通コストが嵩むとい
う問題がある。
On the other hand, Namazake is made by fermenting mash that has been aged in a fermentation tank.
Because sake does not undergo pasteurization for the purpose of sterilization and stopping fermentation, under normal conditions there is a noticeable problem that sake will spoil if stored for a long time.
The following distribution methods have been devised and are actually used to prevent sake from spoiling, by first freezing the sake and distributing it chilled without changing the quality of the sake. However, this method has the problem of increased distribution costs.

そこで従来から生酒の腐敗防止処理についていくつかの
提案がされている。例えば精密r過膜やミクロフィルタ
ー(以下MFという)を用いて精製処理する方法、ある
いはMFや他の前処理に限外♂A膜(以下UFという)
を用いた後処理を組合せる方法等である。
Therefore, several proposals have been made to prevent spoilage of raw sake. For example, a method of purification using a precision r-filtration membrane or a micro filter (hereinafter referred to as MF), or an ultra-A membrane (hereinafter referred to as UF) for MF or other pretreatment.
For example, a method that combines post-processing using

なおアミノ酸の分解を防止する目的で酵素吸着剤を用い
て酸性カルボオキシペプチダーゼ等の酵素を除去するこ
とも行なわれているが、この方法では清酒腐敗の問題は
解決されない。
In order to prevent the decomposition of amino acids, enzyme adsorbents have been used to remove enzymes such as acid carboxypeptidase, but this method does not solve the problem of sake spoilage.

(発明が解決しようとする課題) ところで上記のような精密r過膜等の膜を用いて火落菌
を除去し腐敗防止を図る方法では、火落菌の除去率が十
分でないために酒質の長期安定化は難かしいという問題
がある。またOF等を用いて処理を行なう場合には火落
菌の除去率は相当程度達成できるが、設備投資が莫大な
ものとなるため清酒製造の一工程の設備として汎用され
るには至っていない。
(Problems to be Solved by the Invention) However, with the above-mentioned method of removing hiochi bacteria and preventing spoilage using a membrane such as a precision r-filter membrane, the removal rate of hiochi bacteria is not sufficient, resulting in long-term problems with sake quality. The problem is that stabilization is difficult. In addition, when treatment is carried out using OF or the like, a considerable removal rate of Hiotachi bacteria can be achieved, but the equipment investment is enormous, so it has not been widely used as equipment for one process of sake production.

このように、火入処理した清酒と異なった独特の風味を
もつ「生酒」についての有効な腐敗対策は未だ提供され
ていないことから、生酒の広範囲な流通には問題が伴な
い、従来−射的には蔵元近郊にその流通販売が限定され
て広範囲に渡る流通は困難とされていた。
As described above, since no effective anti-corruption measures have yet been provided for ``namazake'', which has a unique flavor different from pasteurized sake, the wide distribution of namazake is fraught with problems, and conventional As a result, distribution and sales were limited to the vicinity of the brewery, making widespread distribution difficult.

以上のような現状を改善するために本発明者等は主に「
生酒」の腐敗を防止することができる方法について検討
を重ね、本発明をなすに至ったものである。
In order to improve the current situation as described above, the present inventors mainly
The present invention was developed after repeated studies on a method for preventing the spoilage of raw sake.

すなわち、「生酒」における腐敗の原因は火落菌の存在
によフて清酒中で蛋白質等の有機物の分解が進行するた
めであり、従来は、このような火落菌の死滅、除去法が
種々検討され、実施されてきていたのであるが、火落菌
が存在しても、その増殖に必要な発育素がなければ生酒
の腐敗は問題とならないことに注目し、この発育素とし
ての、清酒中に存在するメバロン酸の除去をもって腐敗
防止を図る本発明をなすに至ったものである。
In other words, the cause of spoilage in Namazake is the decomposition of organic matter such as proteins in the sake due to the presence of Hiotchi bacteria, and conventionally, various methods for killing and removing such Hiotchi bacteria have been studied. However, even if hiochi bacteria were present, spoilage of raw sake would not be a problem if there was no growth factor necessary for its proliferation. This invention has been made to prevent spoilage by removing existing mevalonic acid.

本発明は以上の観点に基づいて、清酒中に含まれるメバ
ロン酸を除去することにより清酒の腐敗を防止する処理
方法を提供するところにある。
Based on the above viewpoint, the present invention provides a processing method for preventing sake from spoiling by removing mevalonic acid contained in the sake.

また本発明の他の目的は、常温で流通可能でかつ新鮮な
風味を維持した生酒を製造することができる処理方法を
提供するところにある。
Another object of the present invention is to provide a processing method that can produce raw sake that can be distributed at room temperature and maintains a fresh flavor.

又本発明の更に他の目的は火入酒への火落菌の混入を防
止するために従来必要とされている無菌化設備の負担を
軽減させることができる処理方法を提供することにある
Still another object of the present invention is to provide a processing method that can reduce the burden on sterilization equipment conventionally required to prevent the contamination of hiochi bacteria into hot sake.

(課題を解決するための手段) 本発明者等は、上記目的を達成するために鋭意研究を重
ねた結果、メバロン酸はアニオン交換樹脂、特にOH型
のアニオン交換樹脂によって効果的に吸着、除去できる
こと、しかしながらOH型アニオン交換樹脂にはメバロ
ン酸だけでなく、清酒中に含まれているクエン酸、リン
ゴ酸等の清酒の風味にかかせない有機酸も一部吸着され
、従って清酒をOH型のアニオン交換樹脂のみで処理し
た場合は、風味の点で好ましくない清酒となってしまう
ことを見い出した。
(Means for Solving the Problem) As a result of intensive research to achieve the above object, the present inventors have found that mevalonic acid can be effectively adsorbed and removed by anion exchange resin, especially OH type anion exchange resin. However, OH-type anion exchange resins adsorb not only mevalonic acid, but also some of the organic acids that are essential to the flavor of sake, such as citric acid and malic acid, which are contained in sake. It has been found that when treated with only an anion exchange resin, the result is a sake that is undesirable in terms of flavor.

本発明はかかる知見に基づいてなされたものである。す
なわち本発明よりなる清酒の処理方法の特徴は、清酒の
風味を損なうことなく清酒中に含有されるメバロン酸を
除去する目的で、OH型のアニオン交換樹脂、及びクエ
ン酸。
The present invention has been made based on this knowledge. That is, the feature of the sake processing method according to the present invention is that an OH type anion exchange resin and citric acid are used for the purpose of removing mevalonic acid contained in sake without impairing the flavor of the sake.

リンゴ酸、コハク酸、乳酸から選択される一つまたは二
つ以上の有機酸型アニオン交換樹脂に清酒を接触させる
ところにある。
Sake is brought into contact with one or more organic acid type anion exchange resins selected from malic acid, succinic acid, and lactic acid.

上記方法は、例えばOH型のアニオン交換樹脂及び有機
酸型アニオン交換樹脂の混床に清酒を通す方法、−塔の
内部にOH型のアニオン交換樹脂と有機酸型アニオン交
換樹脂を二層に分離配置した所謂複層床に、清酒をOH
型アニオン交換樹脂、次で有機酸型アニオン交換樹脂の
順に接触させるように通す方法、2塔以上に分割されて
いる所謂複床槽のイオン交換樹脂塔に上記順序で順次に
清酒を通す方法のいずれであってもよい。また更にこれ
らの処理を行なった清酒を9H調整のためにH型カチオ
ン交換樹脂に通してもよい、前記有機酸型アニオン交換
樹脂はクエン酸、リンゴ酸、コハク酸、乳酸のイオン型
のものであり、これらを単独でも併用してもよい。併用
の場合には有機酸型アニオン交換樹脂を使用する樹脂塔
を混酸型として使用する他、別々に別けた樹脂塔に順次
に通すようにしてもよい。
The above method includes, for example, passing sake through a mixed bed of an OH type anion exchange resin and an organic acid type anion exchange resin, - separating an OH type anion exchange resin and an organic acid type anion exchange resin into two layers inside a column; Sake is poured OH on the so-called multi-layered floor.
A method in which the sake is brought into contact with a type anion exchange resin, then an organic acid type anion exchange resin, and a method in which sake is passed sequentially in the above order through an ion exchange resin tower in a so-called multi-bed tank that is divided into two or more towers. It may be either. Furthermore, the sake subjected to these treatments may be passed through an H-type cation exchange resin for 9H adjustment, and the organic acid type anion exchange resin is an ionic type of citric acid, malic acid, succinic acid, or lactic acid. These may be used alone or in combination. In the case of combined use, a resin tower using an organic acid type anion exchange resin may be used as a mixed acid type, or the resin may be sequentially passed through separate resin towers.

また本発明方法は、OH型アニオン交換樹脂及びH型カ
チオン交換樹脂に接触させた清酒に、上述した有機酸を
単独または併用添加するようにしてもよい。この場合の
処理には、樹脂塔として混床式、2床式、複層式のいず
れを採用することもできる。なお、この処理に先立って
酸性亜硫酸型アニオン交換樹脂に清酒を接触させる前処
理を行なうことが特に好ましく、これにより清酒中に含
まれていて悪酔いの原因となるアルデヒドを効果的に除
去できる利点がある。
Further, in the method of the present invention, the above-mentioned organic acids may be added alone or in combination to the sake that has been brought into contact with the OH type anion exchange resin and the H type cation exchange resin. In this case, any of a mixed bed type, two bed type, and multilayer type can be adopted as the resin column. In addition, it is particularly preferable to carry out a pretreatment in which the sake is brought into contact with an acidic sulfite-type anion exchange resin prior to this treatment.This has the advantage that aldehydes contained in the sake and which cause nausea can be effectively removed. be.

(作用) 本発明は前記の構成をなすことによって、清酒中に存在
するメバロン酸が除去でき、生酒においては従来にない
腐敗防止の有効な対策となり、火入酒については火入加
熱処理後における火落菌混入に伴なう腐敗防止に有効な
対策となる。
(Function) By having the above-mentioned structure, the present invention can remove mevalonic acid present in sake, and it is an effective measure to prevent spoilage that has not been seen before in raw sake. This is an effective measure to prevent rot caused by contamination with hiochi bacteria.

以下本発明の詳細な説明する。The present invention will be explained in detail below.

清酒を、OH型のアニオン交換樹脂、及び有機酸型のア
ニオン交換樹脂に接触させる構成とした本発明によれば
、清酒中に存在するメバロン酸をOH型のアニオン交換
樹脂によって完全に除去することができるとともに、当
該アニオン交換樹脂によって一部除去されてしまう清酒
の風味にかかせない有機酸を、有機酸型のアニオン交換
樹脂によって補充することができ、従って清酒の風味を
損なうことなく、従来より腐敗し難くい生酒、あるいは
火入酒を得ることができる。
According to the present invention, in which sake is brought into contact with an OH type anion exchange resin and an organic acid type anion exchange resin, mevalonic acid present in sake can be completely removed by the OH type anion exchange resin. At the same time, the organic acid-type anion exchange resin can replenish the organic acids that are essential to the flavor of sake, which are partially removed by the anion exchange resin. You can obtain raw sake or hot sake that is less likely to spoil.

なお上記方法によりた場合は、得られる清酒のpHが、
清酒本来のpH(pH4,2〜4.5)より若干アルカ
リ性となる場合もあり、その場合は上記方法で処理した
清酒を、更にH型のカチオン交換樹脂に接触させること
もよってpH調整を行なうことができる。
In addition, when using the above method, the pH of the resulting sake is
In some cases, the pH of sake is slightly more alkaline than the original pH (pH 4.2 to 4.5), and in that case, the sake treated with the above method is further brought into contact with an H-type cation exchange resin to adjust the pH. be able to.

当該方法を用いるアニオン交換樹脂の種類としては、強
塩基性1弱塩基性、あるいは中塩基性と称されるアニオ
ン交換樹脂のいずれも用いることができるが、得られる
清酒の風味の点において弱塩基性あるいは中塩基性アニ
オン交換樹脂を用いるのが好ましい。
As for the type of anion exchange resin used in this method, any of the anion exchange resins called strong basic, weak basic, or medium basic can be used, but in terms of the flavor of the resulting sake, weak basic It is preferable to use a neutral or medium basic anion exchange resin.

上記有機酸型のアニオン交換樹脂は、通常、アニオン交
換樹脂に、クエン酸、リンゴ酸、コハク酸乳酸のいずれ
か一つの有機酸を含む溶液、あるいは二つ以上の有機酸
を含む混酸溶液を接触させることによって得ることがで
きる。
The above-mentioned organic acid type anion exchange resin is usually prepared by contacting the anion exchange resin with a solution containing an organic acid such as citric acid, malic acid, or succinic acid or lactic acid, or a mixed acid solution containing two or more organic acids. It can be obtained by letting

また、上記pH調整のために用いるH型カチオン交換樹
脂としては強酸性カチオン交換樹脂1弱酸性カチオン交
換樹脂のいずれでもよいが、好ましくは強酸性カチオン
交換樹脂を用いるのがよい。
The H-type cation exchange resin used for the pH adjustment may be either a strongly acidic cation exchange resin or a weakly acidic cation exchange resin, but it is preferable to use a strongly acidic cation exchange resin.

次に、清酒をOH型アニオン交換樹脂及びH型カチオン
交換樹脂に接触させた後、有機酸を添加(補酸)する構
成とした本発明によれば、OH型アニオン交換樹脂によ
るメバロン酸の除去およびクエン酸等の有機酸を含む他
のアニオン成分の除去に加えて、H型カチオン交換樹脂
によるカチオン成分の除去も行なわれ、従って脱イオン
化された風味の乏しい酒が得られるが、この酒にあとか
ら必要量の有機酸を補酸し、pH調整を行なうことによ
って十分な風味を有する清酒を得ることができる。末法
は、有機酸型のアニオン交換樹脂を用いる前記方法に比
べて操作が簡単であり、又pH調整も容易であるという
利点を有する。
Next, according to the present invention, in which the sake is brought into contact with an OH type anion exchange resin and an H type cation exchange resin, an organic acid is added (supplementary acid).Mevalonic acid is removed by the OH type anion exchange resin. In addition to the removal of other anionic components, including organic acids such as citric acid and other anionic components, removal of cationic components by H-type cation exchange resins is also carried out, thus resulting in a deionized and flavorless sake; By later supplementing with a necessary amount of organic acid and adjusting the pH, sake with sufficient flavor can be obtained. The powder method has the advantage of being easier to operate and easier to adjust the pH than the above method using an organic acid type anion exchange resin.

なお当該方法に用いるイオン交換樹脂も前記方法の場合
と同様のものでよいが、好ましくは強塩基性アニオン交
換樹脂と強酸性カチオン交換樹脂の組合せが最適であり
、また清酒を接触させる順序は特に限定されない。
Note that the ion exchange resin used in this method may be the same as in the above method, but preferably a combination of a strongly basic anion exchange resin and a strongly acidic cation exchange resin is optimal, and the order in which the sake is brought into contact is particularly determined. Not limited.

(実施例) 以下本発明を図面に示す実施例に基づいて説明する。(Example) The present invention will be described below based on embodiments shown in the drawings.

実施例1 第1図に示したフロー図に従って、上槽後の日本酒の原
酒(アルコール含有量19〜20%)を、0.45μの
孔径のMFにて処理し、この処理酒を、酸性亜硫酸型の
アニオン交換樹脂(強塩基性アニオン交換樹脂、アンバ
ーライト(登録商標、以下同じ) I RA−401を
酸性亜硫酸型に調整したもの)101を充填した車床式
樹脂塔(SB塔)に流速5V=4にて通液し、この処理
酒を更に、H型カチオン交換樹脂(強酸性カチオン交換
樹脂、アンバーライトI R−120)1容(7℃)と
、OH型アニオン交換樹脂(強塩基性アニオン交換樹脂
アンバーライトIRA−402) 2容(141)との
混合樹脂を充填した混床式樹脂塔(MB塔)に5V=4
にて通液した。
Example 1 According to the flowchart shown in Figure 1, the raw Japanese sake (alcohol content 19-20%) after the upper tank was treated with MF with a pore size of 0.45μ, and the treated sake was treated with acidic sulfite. A flow rate of 5 V was applied to a car floor type resin tower (SB tower) filled with anion exchange resin (strongly basic anion exchange resin, Amberlite (registered trademark, hereinafter the same) I RA-401 adjusted to acidic sulfite type) 101. = 4, and this treated sake was further mixed with 1 volume (7°C) of H-type cation exchange resin (strongly acidic cation exchange resin, Amberlite I R-120) and OH-type anion exchange resin (strongly basic 5V = 4 in a mixed bed resin tower (MB tower) filled with a mixed resin with 2 volumes (141) of anion exchange resin Amberlite IRA-402)
The liquid was passed through.

得られた生酒にpH調整のためにクエン酸。Add citric acid to the resulting raw sake to adjust the pH.

リンゴ酸を補酸してpHを4.3にした。Malic acid was supplemented to adjust the pH to 4.3.

これを更に活性炭にて仕上げ処理し製品とした。This was further finished with activated carbon and made into a product.

以上の処理を行なつた清酒中の各処理段階での成分変化
を下記表1に示した。
Table 1 below shows the changes in the components of the sake treated as described above at each treatment stage.

表      1 埋酒を更に、クエン酸型及びリンゴ酸型のアニオン交換
樹脂の混合樹脂(アンバーライトI RA−68)25
1を充填した混酸型樹脂塔(SB−2塔)に通液して製
品を得た。
Table 1 Mixed resin of citric acid type and malic acid type anion exchange resin (Amberlite I RA-68) 25
A product was obtained by passing the solution through a mixed acid type resin tower (SB-2 tower) filled with 1.

本実施例における清酒中の各処理段階での成分変化を下
記表2に示した。
Table 2 below shows the changes in the components of sake at each processing stage in this example.

末法によれば、処理後に補酸を行なう必要がなく、しか
も腐敗の心配のないフルーティーな生酒が得られた。
According to the final method, it was not necessary to add acid after processing, and fruity raw sake was obtained that was free from spoilage.

表       ま ただし酵素類の測定値は u/i 実施例2 第2図に示したフロー図に従って、上槽後の原酒(MF
処理後)を、MR型のOH型アニオン交換樹脂(中塩基
性アニオン交換樹脂、アンバーライトIRA−68)2
51を充填した樹脂塔(SR−1塔)に5V−4にて通
液し、この処国税庁醸造試験所法による ただし酵素類の測定値は u/f 腐敗についての評価試験 実施例1.2について次により清酒の腐敗試験を行なっ
た。
Table Measured values of dashi enzymes are u/i Example 2 According to the flow diagram shown in Figure 2, the raw sake after the upper tank (MF
After treatment), MR type OH type anion exchange resin (medium basic anion exchange resin, Amberlite IRA-68) 2
The liquid was passed through a resin tower (SR-1 tower) filled with SR-1 at 5V-4, and the measured values of enzymes were U/F according to the National Tax Agency Brewing Laboratory method. We conducted a spoilage test on sake using the following method.

すなわち、実施例1および実施例2で得た製品と原酒と
を、それぞれ室温(約25℃)で放置してその酒質変化
をみたところ、本発明製品は60日経過後においても火
落菌の増殖はほとんどなく、よって腐敗は全く認められ
なかった。
That is, when the products obtained in Examples 1 and 2 and the unprocessed sake were left at room temperature (approximately 25 degrees Celsius) and changes in alcohol quality were observed, it was found that the products of the present invention showed no growth of hiochi bacteria even after 60 days. There was almost no evidence of corruption.

原酒の場合は10日経過後において既に火落菌の増殖が
著しく、明らかに腐敗が生じていた。
In the case of unprocessed sake, after 10 days, Hiotchi bacteria had already grown significantly and spoilage had clearly occurred.

(発明の効果) 以上述べた通り本発明の処理方法によれば、清酒中り含
まれるメバロン酸を除去することで清酒腐敗の防止が有
効に行なわれ、新鮮で本来の風味を維持した生酒が常温
で流通可能になるという効果がある。
(Effects of the Invention) As described above, according to the processing method of the present invention, by removing mevalonic acid contained in sake, sake spoilage is effectively prevented, and raw sake that is fresh and retains its original flavor is produced. It has the effect of being able to be distributed at room temperature.

又火大酒について本発明の処理を行なうこともでき、こ
れにより火入加熱処理後における火大酒への火落菌の混
入防止が図られるため、無菌化設備の負担を軽減させる
ことができる効果がある。
In addition, it is possible to perform the treatment of the present invention on Hiotaizake, which prevents the contamination of Hiotoshi bacteria into Hiotaizake after pasteurization and heat treatment, which has the effect of reducing the burden on sterilization equipment. There is.

更に、酸性亜硫酸型アニオン交換樹脂による処理を併用
することによって、メバロン酸の除去と共に悪酔いの原
因となるアルデヒドの除去を行なうことができるという
効果がある。
Furthermore, by using a treatment with an acidic sulfite type anion exchange resin, it is possible to remove not only mevalonic acid but also aldehydes that cause nausea.

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

図面第1図は本発明の実施例1の生酒精製処理のシステ
ムフローを説明する図、第2図は実施例2の生酒精製処
理のシステムフローを説明する図である。 手続補正 書 平成2年 2 月 21日 l。 事件の表示 平成 / 年 特 許 願 第 ?火tり8号 3゜ 補正をする者 事件との関係 出 願 人 住 所 東京都千代田区九の内2丁目6番2号丸の内へ重洲ビル
3307゜ 補正の対象 補     正     書 本願明細書中下記事項を補正致します。 記 1、第3頁18〜19行目に 「精密FA膜やミクロフィルター(以下MFという)」
とあるを 「精密?Pi#HIi (ミクロフィルター、以下MF
という)」と訂正する。 2、第9頁下から3行目に 「接触させることもよって」とあるな 「接触させることによって」と訂正する。 3、第10頁7行目〜8行目に 「コハク酸乳酸」とあるな 「コハク酸、乳酸」と訂正する。
FIG. 1 is a diagram explaining the system flow of the raw sake refining process according to the first embodiment of the present invention, and FIG. 2 is a diagram explaining the system flow of the raw sake refining process according to the second embodiment. Procedural amendment February 21, 1990 l. Case display Heisei/year patent application number? Tue 8 No. 3  Person making the amendment Related to the case Applicant Address 3307 Shigesu Building, 2-6-2 Kunouchi, Chiyoda-ku, Tokyo 3307゜ Subject of amendment Amendment Document The following matters in the specification of the present application We will correct it. Note 1, page 3, lines 18-19, "Precision FA membrane or micro filter (hereinafter referred to as MF)"
It says "Precision? Pi#HIi (micro filter, hereinafter MF
)” is corrected. 2. On the 3rd line from the bottom of page 9, it says "by bringing it into contact". It should be corrected to "by bringing it into contact." 3. On page 10, lines 7 and 8, the text "succinic acid lactic acid" should be corrected to "succinic acid, lactic acid."

Claims (1)

【特許請求の範囲】 1 清酒を、OH型のアニオン交換樹脂、及びクエン酸
、リンゴ酸、コハク酸、乳酸から選択される一つまたは
二つ以上の有機酸型とされた有機酸型アニオン交換樹脂
に接触させることを特徴とする清酒の処理方法。 2 清酒をOH型のアニオン交換樹脂及び有機酸型アニ
オン交換樹脂の混床に通すことを特徴とする請求項1に
記載の清酒の処理方法。 3 清酒をOH型のアニオン交換樹脂に接触させた後、
有機酸型アニオン交換樹脂に接触させることを特徴とす
る請求項1に記載の清酒の処理方法。 4 請求項1ないし3のいずれかの清酒の処理方法で処
理した清酒を、更にH型のカチオン交換樹脂に接触させ
ることを特徴とする清酒の処理方法。 5 清酒をOH型アニオン交換樹脂及びH型カチオン交
換樹脂に接触させた後、クエン酸、リンゴ酸、コハク酸
、乳酸から選択される一つまたは二つ以上の有機酸を添
加することを特徴とする清酒の処理方法。
[Scope of Claims] 1 An organic acid type anion exchange method in which sake is converted into an OH type anion exchange resin and one or more organic acid types selected from citric acid, malic acid, succinic acid, and lactic acid. A method for processing sake that involves bringing it into contact with resin. 2. The method for treating sake according to claim 1, characterized in that the sake is passed through a mixed bed of an OH type anion exchange resin and an organic acid type anion exchange resin. 3 After bringing the sake into contact with an OH type anion exchange resin,
The method for treating sake according to claim 1, characterized in that the sake is brought into contact with an organic acid type anion exchange resin. 4. A method for treating sake, which comprises further contacting the refined sake treated by the method for treating sake according to any one of claims 1 to 3 with an H-type cation exchange resin. 5. After bringing the sake into contact with an OH type anion exchange resin and an H type cation exchange resin, one or more organic acids selected from citric acid, malic acid, succinic acid, and lactic acid are added. How to process sake.
JP9444889A 1989-04-14 1989-04-14 How to process sake Expired - Fee Related JP2836842B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP9444889A JP2836842B2 (en) 1989-04-14 1989-04-14 How to process sake

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP9444889A JP2836842B2 (en) 1989-04-14 1989-04-14 How to process sake

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Publication Number Publication Date
JPH02273171A true JPH02273171A (en) 1990-11-07
JP2836842B2 JP2836842B2 (en) 1998-12-14

Family

ID=14110543

Family Applications (1)

Application Number Title Priority Date Filing Date
JP9444889A Expired - Fee Related JP2836842B2 (en) 1989-04-14 1989-04-14 How to process sake

Country Status (1)

Country Link
JP (1) JP2836842B2 (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2000184878A (en) * 1998-12-19 2000-07-04 Satoru Tabata Production of liquors and sweet food
JP2007061064A (en) * 2005-09-02 2007-03-15 Miwa Shuzo:Kk Method for producing japanese sake
JP2009247284A (en) * 2008-04-07 2009-10-29 Japan Organo Co Ltd Method and apparatus for removing aldehyde compound in alcohol-containing liquid
CN105331672A (en) * 2015-11-25 2016-02-17 江南大学 Culture medium for detecting ethanol-tolerance contaminant microorganism in yellow rice wine, and application of culture medium

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2000184878A (en) * 1998-12-19 2000-07-04 Satoru Tabata Production of liquors and sweet food
JP2007061064A (en) * 2005-09-02 2007-03-15 Miwa Shuzo:Kk Method for producing japanese sake
JP2009247284A (en) * 2008-04-07 2009-10-29 Japan Organo Co Ltd Method and apparatus for removing aldehyde compound in alcohol-containing liquid
CN105331672A (en) * 2015-11-25 2016-02-17 江南大学 Culture medium for detecting ethanol-tolerance contaminant microorganism in yellow rice wine, and application of culture medium

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