JPH036787B2 - - Google Patents

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Publication number
JPH036787B2
JPH036787B2 JP11560082A JP11560082A JPH036787B2 JP H036787 B2 JPH036787 B2 JP H036787B2 JP 11560082 A JP11560082 A JP 11560082A JP 11560082 A JP11560082 A JP 11560082A JP H036787 B2 JPH036787 B2 JP H036787B2
Authority
JP
Japan
Prior art keywords
fruit
concentration
fruit juice
wine
fermentation
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
JP11560082A
Other languages
Japanese (ja)
Other versions
JPS596879A (en
Inventor
Masaichi Sodeyama
Hidekazu Soma
Yoshizumi Iino
Hideo Myaji
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.)
Sapporo Breweries Ltd
Original Assignee
Sapporo Breweries 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 Sapporo Breweries Ltd filed Critical Sapporo Breweries Ltd
Priority to JP57115600A priority Critical patent/JPS596879A/en
Publication of JPS596879A publication Critical patent/JPS596879A/en
Publication of JPH036787B2 publication Critical patent/JPH036787B2/ja
Granted legal-status Critical Current

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Description

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

本発明は果実酒の製造法に関し、詳しくは果実
酒の製造工程において特定の逆浸透膜を用いて果
実搾汁液、発酵醪および果実酒の中の少なくとも
1種を濃縮する工程を加えた果実酒の製造法に関
する。 従来、香味の豊かな高級果実酒を製造する場
合、原料果実は厳選され、しかも仕込、発酵およ
び貯蔵の各工程において適切な方法を採用するこ
とにより行なわれていた。たとえばブドウにおい
ては、優良品種であること、栽培の適地であるこ
と、栽培時の天候が良好であること、栽培方法や
収穫時期が適正であること等の条件が揃い、ブド
ウが完熟あるいは過熟し、糖度や酸度も充分にあ
り、香味の豊かなものを原料として使用すること
が必要である。また、果実酒の製造工程において
も優良な酵母を用い、低温で発酵させ、適正な温
度で貯蔵することが必要である。 ところで、天候の不順や栽培方法の失敗などに
よつて収穫時期になつても完熟しない場合があ
る。このようなブドウは糖度が不充分で酸とのバ
ランスに欠けており、香味成分の少ない淡白なも
のであるため、このブドウから高級ワインを製造
することは出来ないものとされている。また、我
国における醸造用ブドウ中で最も使用量の多い品
種である甲州種は品種の特性、気候条件等により
淡白で糖度の低いものとなり易く、原料果実とし
ては欠点があり、高級ワインの原料としては不満
足なものであつた。 そこで、このような糖度が低く、香味成分の少
ないブドウを原料として香味の豊かなワインを製
造するために、果実あるいは果汁を濃縮すること
が従来から検討されている。たとえばブドウの乾
燥濃縮法、凍結濃縮法や果汁の減圧濃縮法、凍結
濃縮法等が提案されている。 しかしいずれの場合も香味の損傷が大きい、す
なわち加熱することによつてフルーテイーな香り
が損なわれ、凍結することによつて味の重要部分
である酸度が減少してしまう。 一方、果実酒そのものを濃縮して香味の豊かな
ものにしようとする試みは殆んど行なわれていな
い。その理由は、従来の加熱濃縮法あるいは減圧
濃縮法では揮発性香気成分やアルコールが飛散し
てしまい、得られる濃縮液は果実酒としての特徴
を欠いたものとなつてしまうからである。 最近、逆浸透膜や限外過膜を使用して果汁も
しくは発酵終了後の発酵液を濃縮する方法が提案
されている(特開昭50−129797号、同50−154494
号、同52−15898号)。しかし、これらの方法では
有機酸やアミノ酸の一部が透過してしまうため、
コク味がボデイー感が不充分であり香味の豊かな
ものが得られなかつた。 そこで本発明者は、上記欠点を解消して香味の
濃厚な果実酒を製造すべく鋭意検討した結果、食
塩と酒石酸の排除率が高い膜を使用し逆浸透法に
より製造工程中の適当な段階で濃縮処理を行なう
ことによつて目的を達成出来ることを見出し、か
かる知見に基いて本発明を完成するに至つた。 本発明は、果実酒の製造において、果実搾汁液
の濃縮工程、発酵醪の濃縮工程および果実酒の濃
縮工程の中の少なくとも1つの濃縮工程を加え、
かつ該濃縮工程をNaCl排除率90%以上、酒石酸
排除率90%以上の逆浸透膜を使用して行なうこと
を特徴とする果実酒の製造法である。 本発明に使用する逆浸透膜はNaCl排除率が90
%以上で、酸やアルコール等についても可及的に
排除率の高いものを選択する。特に、果実酒の酸
の主成分である酒石酸はその排除率が90%以上、
望ましくは100%に近いものを選択する。ここで、
排除率とは透過液側への対象成分の移行割合を下
記の式 排除率 =(1−透過液側の対象成分の全量/初発原液中の対象
成分の全量)x100(%) で計算したものである。膜の材質については特別
な制限はないが、一般に酢酸セルロース系の膜は
有機酸の排除率が低いので好ましくなく、芳香族
系ポリマー(たとえば芳香族ナイロン、芳香族ポ
リイミダゾロン)などには本発明の目的に適合す
るものがある。また、逆浸透膜濃縮装置はその構
造が耐圧板型、管状型、中空繊維型など任意の形
状のものを用いることができる。 果実酒の製造方法としては、通常行なわれてい
る方法を採用すればよく、また原料果実について
も制限がなく、ブドウ、リンゴ、イチゴ等種々の
ものを使用できる。果実酒の香味の特徴の1つは
果実に由来する独特の酸味を有することにある
が、本発明は酸味のバランスを保つことに配慮し
て原料の仕込、発酵、貯蔵等を行なうものであ
る。 前述した如く、本発明では果実酒の製造工程に
おいて、果実搾汁液の濃縮工程、発酵醪の濃縮工
程および果実酒の濃縮工程の中の少なくとも1つ
の濃縮工程を加えるのであるが、品質の良好な製
品を得るためには、果実搾汁液または果実酒ある
いはこれら両者について濃縮を行なうことが好ま
しい。なお、こゝで濃縮の対象とされる果実酒と
は発酵を終了した発酵液を過した後の液体から
貯蔵された該液体までを意味する。 果実搾汁液、すなわち果汁の濃縮についてブド
ウを例として説明する。原料ブドウは除梗、破
砕、圧搾され、フリーラン果汁およびプレス果汁
にし、これらを単独で、あるいは混合したものを
原果汁として用いる。この果汁はそのまゝ用いて
もよく、清澄処理してから用いることもできる。
清澄処理は濃縮効果の向上、果汁の保存性の向上
等を目的として必要に応じて行なうものであり、
この処理はたとえば原果汁を冷却静置あるいは遠
心分離によつて滓部と清澄部に分画し、該清澄部
をさらに過するものである。 次に、果汁を逆浸透濃縮装置にかける場合、そ
の温度は果汁が凍結あるいは沸騰することがない
範囲で、望ましくは0〜50℃に調整して香りの飛
散や酸化の促進等が起らないようにして行なう。
また、逆浸透を起させるための圧力については、
使用する膜の耐圧性なども考慮しなければならな
いが、可及的に高圧とする方が水の透過が早く、
濃縮効率が良い。果汁の濃縮倍率については原果
汁の浸透圧や使用圧力により異なり、たとえば果
汁糖度15度で使用圧力60Kg/cm2の場合、濃縮倍率
は約2倍が最大であり、また果汁糖度8度で使用
圧力80Kg/cm2の場合は約5倍が最大である。 原果汁もしくは上記の如く濃縮された果汁はそ
のまゝあるいは補糖、稀釈等の果汁調整を行なつ
てから発酵させる。発酵はサツカロミセス・セレ
ビシエIAM−4274などのブドウ酒酵母を使用し、
通常の方法によつて培養することにより行なう。
たとえばブドウ酒酵母を常法により培養した培養
液を上記果汁に対し1〜10%(v/v)の割合で
接種し、5〜35℃の温度、PH2〜5の条件でアル
コール発酵を行なう。そして目標とするアルコー
ル分、残糖分に到達した時点を発酵終了時期とす
る。 発酵が終了した後、常法により滓引き、貯蔵、
熟成、過等を行なつて果実酒を得る。この間、
必要に応じて酸化防止剤として亜硫酸類(亜硫酸
ガス、メタ重亜硫酸カリウム)をSO2として10〜
350mg/添加する。貯蔵、熟成は果実酒に過度
の酸化が生起しないような容器を用いて行なうこ
とが望ましい。本発明によれば、ブドウの仕込
後、数ケ月〜1年で香味の豊かな酸味の強い、し
かもボデイーの重厚なワインが得られる。貯蔵、
熟成をさらに続けてもこの特徴は消失せず、一層
香味の熟成が行なわれる。 次に、発酵醪の濃縮工程を採用する場合につい
て説明する。発酵醪は果汁に酵母を添加して発酵
中のものであり、発酵期間中の任意の時期のもの
を対象とすることができる。また、赤ワインなど
の場合は果実が混入している。この発酵醪を一部
取出し、必要に応じて遠心分離、過などの処理
をしたのち濃縮する。濃縮の条件は前述と同様で
ある。発酵醪には水、糖分、アルコール分、エキ
ス分、香気成分などが含まれているが、逆浸透膜
を用いて濃縮を行なうと水およびアルコールの一
部が該膜を透過する。しかし、後述するように濃
縮処理の条件を適切に設定すれば、アルコールの
透過量を抑制することができる。濃縮された発酵
醪は元の発酵中の醪に戻して発酵を続ける。 発酵終了後は前記の如く常法により滓引き、貯
蔵、熟成、過等を行なつて果実酒を得る。この
場合も、香味が豊かで酸味の強いボデイーの重厚
なワインが得られる。なお、発酵醪の濃縮は、発
酵期間中の任意の時期に行なえるほか1回の処理
量を適宜に決定できる等の利点がある。 果実酒について濃縮を行なう場合、発酵を終了
した発酵液を過した後の液体から該液体を貯蔵
して1年以内の新酒が主に対象とされ、必要に応
じて過処理、低温化処理を行なつてから濃縮す
る。濃縮の条件は前述の同様である。果実酒の濃
縮を行なうと、発酵醪の場合と同様に水とアルコ
ールの一部が透過液として流出し、アルコール、
酸、糖、エキス分、香気成分などが濃縮される。
アルコールの透過は果実酒の濃縮時の温度を低
温、たとえば0〜10℃に保つことによつてほとん
ど抑制することができる。高温で濃縮を行なうと
アルコールの透過量が増大するので好ましくな
い。また、濃縮倍率については液量比で5倍程度
までの濃度が可能であるが、糖、酸、香味のバラ
ンスを保つためには2倍以内とするのが好まし
い。このようにして得られる濃縮果実酒は香味が
豊かで、コク味やボデイー感が重厚である。 本発明によれば、たとえば甲州種の如く糖度の
低い淡白なブドウを原料とした場合でも香りが高
く、酸味の強い果実酒が得られ、酸味は熟成する
ことによつて丸味を帯び重厚なボデイー感を与え
高級酒になる。また、赤ワインの製造の場合は果
皮から色素を抽出するため一般に果粒を漬したま
ま発酵に供するので、果汁の段階での濃縮は適切
でない。しかし、本発明によれば色素も他の成分
と同様に濃縮されるので良質の赤ワインを得るこ
とができる。 次に、本発明の実施例を示す。 実施例 1 甲州種ブドウを常法により除梗、破砕、圧搾
し、フリーラン果汁(搾汁率60%)を得た。この
果汁にメタ重亜硫酸カリウムをSO2として
100ppmになる様に添加し、1日5〜10℃の温度
で静置後、清澄部と滓部(液量で10%)に分画し
た。この清澄部をケイソウ土過し、清澄果汁
100を調整した。この果汁を逆浸透装置で濃縮
した。逆浸透膜はポリベンズイミダゾロン系膜
で、NaCl阻止率98%、酒石酸阻止率99%のもの
を使用した。ここで、阻止率とは濃縮液側に残存
する対象成分の割合を下記の式 阻止率 =(濃縮液側の対象成分の全量/初発原液中の対象成分
の全量)x100(%) で計算したものである。また、その装置は膜面積
1.26m2の管状膜構造のものを用いた。温度は室温
(15℃)で行なつたが、操作中7〜23.5℃までの
温度上昇がみられた。使用圧は55Kg/cm2とした。
透過液はほとんど無味無臭の水であつた。濃縮倍
率1.49倍のもの(濃縮液)を40、濃縮倍率
1.83倍のもの(濃縮液)を22得た。 それぞれの濃縮液および濃縮前の原果汁の3種
類についての果汁分析値を第1表に示した。
The present invention relates to a method for producing fruit wine, and more specifically to a fruit wine that includes a step of concentrating at least one of fruit juice, fermented mortar, and fruit wine using a specific reverse osmosis membrane in the fruit wine manufacturing process. Concerning the manufacturing method. Conventionally, when producing high-quality fruit liquors with rich flavors, raw materials have been carefully selected, and appropriate methods have been adopted in each step of preparation, fermentation, and storage. For example, when it comes to grapes, conditions such as being a good variety, being in a suitable place for cultivation, having good weather during cultivation, and using appropriate cultivation methods and harvesting times are all met to ensure that the grapes are fully ripe or overripe. It is necessary to use raw materials that have sufficient sugar content and acidity, and are rich in flavor. In addition, in the process of producing fruit wine, it is necessary to use high-quality yeast, ferment at low temperatures, and store at appropriate temperatures. By the way, due to unfavorable weather or faulty cultivation methods, the fruit may not fully ripen even at harvest time. Such grapes have insufficient sugar content, lack balance with acid, and are bland with few flavor components, so it is said that it is impossible to produce high-quality wine from these grapes. In addition, the Koshu variety, which is the most commonly used variety of grapes for winemaking in Japan, tends to be bland and low in sugar content due to the characteristics of the variety, climate conditions, etc., and has drawbacks as a raw material fruit, so it is not suitable as a raw material for high-quality wine. was unsatisfactory. Therefore, in order to produce wine with rich flavor using grapes with low sugar content and few flavor components as raw materials, concentrating the fruit or fruit juice has been considered. For example, methods such as a grape dry concentration method, a freeze concentration method, a fruit juice concentration method under reduced pressure, and a freeze concentration method have been proposed. However, in either case, the flavor is severely damaged; heating destroys the fruity aroma, and freezing reduces the acidity, which is an important part of taste. On the other hand, almost no attempts have been made to concentrate fruit wine itself to make it rich in flavor. The reason for this is that in the conventional heating concentration method or vacuum concentration method, volatile aroma components and alcohol scatter, and the resulting concentrated liquid lacks the characteristics of a fruit liquor. Recently, methods have been proposed for concentrating fruit juice or fermented liquid after fermentation using reverse osmosis membranes or ultrafiltration membranes (Japanese Patent Application Laid-open Nos. 50-129797 and 50-154494).
No. 52-15898). However, with these methods, some organic acids and amino acids pass through, so
The body taste was insufficient and a rich flavor could not be obtained. Therefore, the inventor of the present invention made extensive studies to eliminate the above drawbacks and produce a fruit wine with a rich flavor.As a result, the inventors of the present invention determined that the appropriate stage of the production process using a membrane with a high rejection rate of salt and tartaric acid and reverse osmosis. The inventors have discovered that the objective can be achieved by carrying out a concentration treatment, and have completed the present invention based on this knowledge. In the production of fruit wine, the present invention adds at least one concentration step of a fruit juice concentration step, a fermentation moromi concentration step, and a fruit wine concentration step,
The method for producing fruit wine is characterized in that the concentration step is carried out using a reverse osmosis membrane with a NaCl rejection rate of 90% or more and a tartaric acid rejection rate of 90% or more. The reverse osmosis membrane used in the present invention has a NaCl rejection rate of 90
% or more, and select one that has the highest possible exclusion rate for acids, alcohols, etc. In particular, the removal rate of tartaric acid, which is the main acidic component of fruit wine, is over 90%.
Preferably, select one close to 100%. here,
Rejection rate is the transfer rate of the target component to the permeate side, calculated using the following formula: Rejection rate = (1 - total amount of target component on permeate side / total amount of target component in the initial stock solution) x 100 (%) It is. There are no particular restrictions on the material of the membrane, but cellulose acetate-based membranes are generally undesirable due to their low organic acid rejection rate, and aromatic polymers (e.g., aromatic nylon, aromatic polyimidazolone) are not recommended. There is something that meets the purpose of the invention. Further, the reverse osmosis membrane concentrator may have any shape such as a pressure plate type, a tubular type, or a hollow fiber type. As a method for producing fruit wine, a commonly used method may be adopted, and there are no restrictions on the raw material fruit, and various fruits such as grapes, apples, and strawberries can be used. One of the characteristics of the flavor of fruit wine is that it has a unique sour taste derived from fruits, but the present invention takes into account the preparation, fermentation, storage, etc. of raw materials in order to maintain the balance of sour taste. . As mentioned above, in the present invention, at least one concentration step among the fruit juice concentration step, the fermentation moromi concentration step, and the fruit wine concentration step is added in the fruit wine manufacturing process. In order to obtain the product, it is preferable to concentrate the fruit juice or the fruit wine or both. Note that the fruit wine to be concentrated here refers to the liquid from the fermented liquid after fermentation to the stored liquid. Concentration of fruit juice, that is, fruit juice, will be explained using grapes as an example. The raw material grapes are destemmed, crushed, and pressed to produce free-run fruit juice and pressed fruit juice, which are used alone or in a mixture as the original fruit juice. This fruit juice may be used as is or after clarification.
Clarification treatment is carried out as necessary to improve the concentration effect and the preservation of fruit juice.
This treatment involves, for example, fractionating raw fruit juice into a dregs portion and a clarified portion by cooling and standing or centrifuging, and then filtering the clarified portion. Next, when applying the fruit juice to a reverse osmosis concentrator, the temperature should be adjusted within a range that does not allow the fruit juice to freeze or boil, preferably between 0 and 50 degrees Celsius, so that aroma dispersion and acceleration of oxidation do not occur. Do it like this.
Also, regarding the pressure to cause reverse osmosis,
The pressure resistance of the membrane used must also be taken into account, but water permeates faster if the pressure is as high as possible.
Good concentration efficiency. The concentration ratio of fruit juice varies depending on the osmotic pressure of the original fruit juice and the working pressure. For example, when the sugar content of fruit juice is 15 degrees and the working pressure is 60 kg/ cm2 , the maximum concentration ratio is about 2 times, and when the sugar content of fruit juice is 8 degrees. When the pressure is 80Kg/cm 2 , the maximum value is about 5 times. The raw fruit juice or the fruit juice concentrated as described above is fermented as is or after fruit juice adjustment such as adding sugar or dilution. Fermentation uses grape wine yeast such as Satucharomyces cerevisiae IAM-4274,
This is done by culturing using a conventional method.
For example, a culture solution obtained by culturing grape wine yeast in a conventional manner is inoculated into the above fruit juice at a ratio of 1 to 10% (v/v), and alcoholic fermentation is carried out at a temperature of 5 to 35°C and a pH of 2 to 5. The fermentation ends when the target alcohol content and residual sugar content are reached. After fermentation is completed, the slag is removed, stored, and
Fruit wine is obtained by aging and aging. During this time,
If necessary, add sulfites (sulfur dioxide gas, potassium metabisulfite) as an antioxidant as SO2 for 10~
Add 350mg/. It is desirable to store and ripen the fruit wine in a container that will not cause excessive oxidation. According to the present invention, wine with rich flavor, strong acidity, and heavy body can be obtained within several months to a year after grapes are harvested. storage,
Even if the wine is aged further, this characteristic does not disappear, and the flavor matures even further. Next, a case will be described in which a fermentation moromi concentrating step is employed. Fermented moromi is one that is being fermented by adding yeast to fruit juice, and can be used at any time during the fermentation period. Also, in the case of red wine, fruits are mixed in. A portion of this fermented moromi is taken out and, if necessary, subjected to treatments such as centrifugation and filtration, and then concentrated. The conditions for concentration are the same as described above. Fermented moromi contains water, sugar, alcohol, extract, aroma components, etc., but when it is concentrated using a reverse osmosis membrane, some of the water and alcohol permeate through the membrane. However, as will be described later, if the conditions for the concentration treatment are appropriately set, the amount of permeation of alcohol can be suppressed. The concentrated fermented moromi is returned to the original fermented moromi to continue fermentation. After the fermentation is completed, the fruit liquor is obtained by sloughing, storing, maturing, fermenting, etc. in the usual manner as described above. In this case as well, the result is a heavy-bodied wine with rich flavor and strong acidity. In addition, the fermentation mash can be concentrated at any time during the fermentation period, and the amount to be processed at one time can be appropriately determined. When concentrating fruit wine, it is mainly targeted at new sake that has been stored for less than a year, starting from the liquid after the fermentation process has finished fermentation. After that, concentrate it. The conditions for concentration are the same as described above. When fruit liquor is concentrated, some of the water and alcohol flow out as a permeate, similar to the case of fermented moromi, and alcohol,
Acid, sugar, extract, aroma components, etc. are concentrated.
Permeation of alcohol can be largely suppressed by keeping the temperature during concentration of the fruit wine at a low temperature, for example, 0 to 10°C. Concentrating at high temperatures is not preferred because the amount of alcohol permeated increases. Regarding the concentration ratio, it is possible to achieve a concentration up to about 5 times the liquid volume ratio, but it is preferably within 2 times in order to maintain the balance of sugar, acid, and flavor. The concentrated fruit liquor obtained in this way is rich in flavor and has a strong body and body. According to the present invention, fruit wine with a high aroma and strong acidity can be obtained even when using light grapes with a low sugar content such as Koshu grapes as raw materials, and the acidity becomes rounder with ripening and has a heavy body. It gives a sense of taste and becomes a high-class sake. Furthermore, in the production of red wine, the fruit is generally fermented while still being soaked in order to extract pigments from the skins, so concentrating the fruit at the juice stage is not appropriate. However, according to the present invention, pigments are also concentrated like other components, so it is possible to obtain high-quality red wine. Next, examples of the present invention will be shown. Example 1 Koshu grapes were destemmed, crushed, and pressed in a conventional manner to obtain free-run fruit juice (juice yield: 60%). Add potassium metabisulfite to this fruit juice as SO 2
The solution was added to a concentration of 100 ppm, left to stand at a temperature of 5 to 10°C for one day, and then fractionated into a clear part and a dregs part (10% in liquid volume). This clarified portion is filtered through diatomaceous earth to produce clarified fruit juice.
Adjusted 100. This fruit juice was concentrated using a reverse osmosis device. The reverse osmosis membrane was a polybenzimidazolone membrane with a NaCl rejection rate of 98% and a tartaric acid rejection rate of 99%. Here, the rejection rate is the proportion of the target component remaining in the concentrate side, calculated using the following formula: Rejection rate = (Total amount of target component in the concentrate side / Total amount of target component in the initial stock solution) x 100 (%) It is something. In addition, the device has a membrane area
A 1.26 m 2 tubular membrane structure was used. Although the temperature was kept at room temperature (15°C), a rise in temperature from 7 to 23.5°C was observed during the operation. The working pressure was 55Kg/cm 2 .
The permeate was almost tasteless and odorless water. Concentration magnification 1.49 times (concentrated liquid) to 40, concentration magnification
22 1.83 times as concentrated solution (concentrated solution) was obtained. Table 1 shows the fruit juice analysis values for the three types of concentrated liquid and original fruit juice before concentration.

【表】 原果汁、濃縮液、の3種類の果汁からワイ
ンをつくり比較検討した。原果汁は糖度が14度で
あつたので、糖度22度を目標に上白糖で補糖し
た。濃縮液、はそのまま発酵醪とした。酒母
はサツカロミセス・セレビシエIAM−4274の発
酵醪をそれぞれ5%ずつ添加した。発酵温度は15
±1℃とした。 発酵状況はいずれも順調であり、原果汁および
濃縮液は10〜12日でアルコール発酵が終了し
た。濃縮液は14日目でアルコールが14度近くに
なつたので、冷却、SO2の添加で発酵を停止せさ
せた。発酵終了時にはSO2を100ppm添加し、5
℃まで冷却してケイソウ土過により酵母を分離
した。得られた果実酒はビン詰めし、10〜12℃で
貯蔵した。 果実酒の分析値を第2表に示す。また熟練者に
よる製品の試飲結果を第3表に示す。表から明ら
かなように、濃縮液を発酵させたものは香味が豊
かで重厚なワインである。果汁の濃縮倍率と水の
透過速度との関係を第1図に示す。
[Table] Wine was made from three types of fruit juice: raw fruit juice and concentrated liquid, and a comparative study was conducted. The original fruit juice had a sugar content of 14 degrees, so we supplemented it with white sugar, aiming for a sugar content of 22 degrees. The concentrate was used as fermented moromi. The fermented mash of Satucharomyces cerevisiae IAM-4274 was added at 5% each to the mash. Fermentation temperature is 15
The temperature was ±1°C. Fermentation progressed smoothly, and alcoholic fermentation of the original fruit juice and concentrate was completed in 10 to 12 days. The alcohol content of the concentrate reached nearly 14 degrees on the 14th day, so the fermentation was stopped by cooling and adding SO 2 . At the end of fermentation, add 100ppm of SO 2 ,
After cooling to ℃, yeast was separated by diatomaceous earth filtration. The resulting fruit wine was bottled and stored at 10-12°C. Table 2 shows the analytical values for the fruit wine. Table 3 also shows the results of product tasting by experts. As you can see from the table, fermented concentrate produces a rich and heavy wine. FIG. 1 shows the relationship between the concentration ratio of fruit juice and the water permeation rate.

【表】【table】

【表】 実施例 2 リンゴ100Kgを常法により破砕、圧搾し、リン
ゴ果汁70(糖度14度)を得た。このリンゴ果汁
にメタ重亜硫酸カリウムをSO2として100ppmと
なるように添加し、3日間冷温静置後、清澄過
処理し、清澄果汁60を得た。この果汁を原果汁
とし、その40を逆浸透装置を使つて濃縮した。
逆浸透膜およびその装置は実施例1と同一のもの
を使用した。濃縮により透過液12を得、濃縮率
を1.43倍とした。この透過液は無味無臭であつた
が、その揮発性香気成分をガスクロマトグラフイ
ーを用いて検討した。原果汁にはエチル−2−メ
チルブチレイト、ヘキサノール、2−ヘキサナル
等のリンゴの特徴を示す物質がみられたが、透過
液ではほとんど検出されなかつた。 この濃縮液および原果汁を常法により発酵さ
せ、果実酒を得た。原果汁は糖度が14度であつた
ので、砂糖で糖度20度まで補糖し、濃縮液の糖度
と同一にした。発酵状況はいずれも正常であり、
12日で主発酵を終了した。主発酵終了と同時にメ
タ重亜硫酸カリウムをSO2として100ppm添加し、
過処理してビン詰め貯蔵した。仕込後4ケ月目
での分析値および試飲結果を第4表および第5表
に示す。果実酒のアルコール分、エキス分および
総酸の分析は国税庁所定分析法注解に従つて行な
つた。また、〓酒は〓酒パネル10名により香、味
について5点満点法で行ない、優れた品質のもの
5点、良い品質のもの4点、平均的品質のもの3
点、多少欠点のある品質のもの2点、劣つた品質
のもの1点とし、その平均点で示した。濃縮リン
ゴ酒は特に芳香が強く、特徴のある酒となつた。
[Table] Example 2 100 kg of apples were crushed and squeezed by a conventional method to obtain apple juice 70 (sugar content 14 degrees). Potassium metabisulfite was added to this apple juice at a concentration of 100 ppm as SO 2 , and after being allowed to stand in the cold for 3 days, it was subjected to clarification and filtration treatment to obtain clarified fruit juice 60. This fruit juice was used as the original fruit juice, and 40% of it was concentrated using a reverse osmosis device.
The same reverse osmosis membrane and equipment as in Example 1 were used. Permeate 12 was obtained by concentration, and the concentration ratio was 1.43 times. Although this permeate was tasteless and odorless, its volatile aroma components were investigated using gas chromatography. Substances characteristic of apples, such as ethyl-2-methylbutyrate, hexanol, and 2-hexanal, were found in the raw fruit juice, but they were hardly detected in the permeate. This concentrate and raw fruit juice were fermented by a conventional method to obtain fruit wine. The original fruit juice had a sugar content of 14 degrees, so it was supplemented with sugar to bring the sugar content to 20 degrees, making it the same as the sugar content of the concentrate. All fermentation conditions are normal.
Main fermentation was completed in 12 days. At the same time as the main fermentation was completed, 100 ppm of potassium metabisulfite was added as SO 2 .
It was overtreated and stored in bottles. Tables 4 and 5 show the analytical values and tasting results 4 months after preparation. The alcohol content, extract content, and total acid content of the fruit wine were analyzed in accordance with the commentary on analytical methods specified by the National Tax Agency. In addition, sake was evaluated by a panel of 10 people using a 5-point scale for aroma and taste, with 5 points for excellent quality, 4 points for good quality, and 3 points for average quality.
2 points were given to those with somewhat defective quality, and 1 point was given to those with inferior quality, and the average score was given. Concentrated cider has a particularly strong aroma and has become a distinctive drink.

【表】【table】

【表】 実施例 3 甲州種ブドウから得た果汁を濃縮することなく
実施例1と同様にして発酵させ果実酒を得た。仕
込後4ケ月でケイソウ土過し、逆浸透濃縮処理
した。使用した逆浸透膜はポリベンズイミダゾロ
ン系ポリマーでNaCl阻止率98%、酒石酸阻止率
99%のものである。新酒はセミドライタイプのも
ので、エキス分および配はほぼ100%濃縮側に残
つた。アルコールは透過液側にも一部流出した
が、濃縮側と透過側の両者を合せると物質収支は
ほぼ100%になつた。すなわち透過液はアルコー
ル水でアルコール臭以外の香はなかつた。第6表
に濃縮果実酒の分析値を示す。果実酒のアルコー
ル分、エキス分および総酸の分析は国税庁所定分
析法注解に従つて行なつた。また第7表はその濃
縮果実酒の試飲結果である。〓酒は〓酒パネル10
名により香、味について5点満点法で行ない、優
れた品質のもの5点、良い品質のもの4点、平均
的品質のもの3点、多少欠点のある品質のもの2
点、劣つた品質のもの1点とし、その平均点で示
した。濃縮果実酒はいずれも香味が重厚で、特に
酸味が強く、高級ワインになり得るものと評価さ
れた。また、濃縮時の平均処理温度と膜のアルコ
ール阻止率との関係を第2図に示した。
[Table] Example 3 Fruit juice obtained from Koshu grapes was fermented in the same manner as in Example 1 without concentrating to obtain fruit wine. Four months after preparation, it was filtered through diatomaceous earth and subjected to reverse osmosis concentration treatment. The reverse osmosis membrane used is a polybenzimidazolone polymer with a NaCl rejection rate of 98% and a tartaric acid rejection rate.
It's 99% of the time. The new sake is a semi-dry type, and the extract content and distribution remained almost 100% on the concentrated side. Some alcohol also leaked out to the permeate side, but when both the concentrated and permeate sides were combined, the mass balance was almost 100%. In other words, the permeate was alcoholic water and had no scent other than the alcohol smell. Table 6 shows the analytical values of concentrated fruit liquor. The alcohol content, extract content, and total acid content of the fruit wine were analyzed in accordance with the commentary on analytical methods prescribed by the National Tax Agency. Table 7 shows the tasting results of the concentrated fruit wine. 〓As for alcohol〓Sake panel 10
Based on the name, aroma and taste are scored on a 5-point scale, with 5 points for excellent quality, 4 points for good quality, 3 points for average quality, and 2 points for somewhat defective quality.
One point was given to those with poor quality, and the average score was given. All of the concentrated fruit wines had a strong flavor and particularly strong acidity, and were evaluated as having the potential to be made into high-quality wines. Furthermore, the relationship between the average treatment temperature during concentration and the alcohol rejection rate of the membrane is shown in FIG.

【表】【table】

【表】 実施例 4 リンゴを常法により仕込んだ新酒をケイソウ土
過し、逆浸透濃縮処理した。逆浸透膜モジユー
ル(1.26m2/1モジユール)およびその装置は実
施例3と同一のものを使つた。ここでは処理温度
を一定に保つ為にその原液槽を冷却あるいは加温
し、目標処理温度を±1℃の範囲でコントロール
した。処理温度は10℃および25℃で行なつた。原
液50を処理し、透過液15を取り、濃縮液は濃
縮率で1.43倍とした。使用平均圧力は55Kg/cm2
で、15の透過膜を得るのに10℃で2時間25分、
25℃で1時間35分を要し、平均透過速度は10℃で
4.93/hr.m2、25℃で7.52/hr.m2であつた。 この濃縮におけるそれぞれの分析値は第8表
に、試飲評価は第9表に示した。アルコール阻止
率と温度の関係は実施例3で作成した相関関係に
ほぼ一致するものとみられた。 このよにして得られた濃縮リンゴ酒は、酸味が
やや強いがコク味があり、ブドウ酒の場合と同様
に高品位なものになり得ると評価された。
[Table] Example 4 New sake made from apples in a conventional manner was filtered through diatomaceous earth and subjected to reverse osmosis concentration treatment. The reverse osmosis membrane module (1.26 m 2 /1 module) and its equipment were the same as in Example 3. Here, in order to keep the processing temperature constant, the stock solution tank was cooled or heated, and the target processing temperature was controlled within a range of ±1°C. The treatment temperatures were 10°C and 25°C. 50 of the stock solution was treated, 15 of the permeate was taken, and the concentrated solution was made at a concentration rate of 1.43 times. Average working pressure is 55Kg/cm 2
So, to obtain 15 permeable membranes, it took 2 hours and 25 minutes at 10℃.
It takes 1 hour and 35 minutes at 25℃, and the average permeation rate is at 10℃.
4.93/hr.m 2 and 7.52/hr.m 2 at 25°C. The analytical values for each concentration are shown in Table 8, and the tasting evaluation is shown in Table 9. The relationship between alcohol inhibition rate and temperature was found to be approximately the same as the correlation created in Example 3. The concentrated cider liquor obtained in this way had a slightly strong acidity but a rich taste, and was evaluated as having the potential to be of high quality, similar to grape wine.

【表】【table】

【表】【table】

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

第1図は果汁の濃縮倍率と水の透過速度との関
係を示すグラフ、第2図は濃縮時の平均処理温度
と膜のアルコール阻止率との関係を示すグラフで
ある。
FIG. 1 is a graph showing the relationship between the concentration ratio of fruit juice and the water permeation rate, and FIG. 2 is a graph showing the relationship between the average treatment temperature during concentration and the alcohol rejection rate of the membrane.

Claims (1)

【特許請求の範囲】 1 果実酒の製造において、果実搾汁液の濃縮工
程、発酵醪の濃縮工程および果実酒の濃縮工程の
中の少なくとも1つの濃縮工程を加え、かつ該濃
縮工程をNaCl排除率90%以上、酒石酸排除率90
%以上の逆浸透膜を使用して行なうことを特徴と
する果実酒の製造法。 2 濃縮工程を温度0〜50℃、濃縮倍率5倍以内
にて行なう特許請求の範囲第1項記載の方法。
[Scope of Claims] 1. In the production of fruit wine, at least one concentration step among a fruit juice concentration step, a fermentation moromi concentration step, and a fruit wine concentration step is added, and the concentration step is performed with a NaCl exclusion rate. More than 90%, tartaric acid rejection rate 90
A method for producing fruit wine, characterized in that it is carried out using a reverse osmosis membrane of % or more. 2. The method according to claim 1, wherein the concentration step is carried out at a temperature of 0 to 50°C and a concentration ratio of within 5 times.
JP57115600A 1982-07-05 1982-07-05 Preparation of fruit wine Granted JPS596879A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP57115600A JPS596879A (en) 1982-07-05 1982-07-05 Preparation of fruit wine

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP57115600A JPS596879A (en) 1982-07-05 1982-07-05 Preparation of fruit wine

Publications (2)

Publication Number Publication Date
JPS596879A JPS596879A (en) 1984-01-13
JPH036787B2 true JPH036787B2 (en) 1991-01-30

Family

ID=14666634

Family Applications (1)

Application Number Title Priority Date Filing Date
JP57115600A Granted JPS596879A (en) 1982-07-05 1982-07-05 Preparation of fruit wine

Country Status (1)

Country Link
JP (1) JPS596879A (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP6610036B2 (en) * 2014-07-03 2019-11-27 三菱ケミカル株式会社 Liquid food concentration method

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS50154494A (en) * 1974-05-28 1975-12-12
JPS57105180A (en) * 1980-12-22 1982-06-30 Snow Brand Milk Prod Co Ltd Preparation of wine from fruit juice concentrated with membrane

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS50154494A (en) * 1974-05-28 1975-12-12
JPS57105180A (en) * 1980-12-22 1982-06-30 Snow Brand Milk Prod Co Ltd Preparation of wine from fruit juice concentrated with membrane

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Publication number Publication date
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