JPS596879A - Preparation of fruit wine - Google Patents

Preparation of fruit wine

Info

Publication number
JPS596879A
JPS596879A JP57115600A JP11560082A JPS596879A JP S596879 A JPS596879 A JP S596879A JP 57115600 A JP57115600 A JP 57115600A JP 11560082 A JP11560082 A JP 11560082A JP S596879 A JPS596879 A JP S596879A
Authority
JP
Japan
Prior art keywords
fruit
wine
concentration
fruit wine
fruit juice
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
JP57115600A
Other languages
Japanese (ja)
Other versions
JPH036787B2 (en
Inventor
Masaichi Sodeyama
袖山 政一
Hidekazu Soma
相馬 英一
Yoshizumi Iino
飯野 良純
Hideo Miyaji
宮地 秀夫
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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Abstract

PURPOSE:To prepare a fruit wine having a rich flavor, by concentrating a fruit wine at a suitable stage in the preparation process thereof by the reverse osmotic method with a membrane having a high exclusion ratio of common salt and tartaric acid. CONSTITUTION:In preparing a fruit wine by the conventional method, at least one concentrating step selected from the concentrating of fruit pressed juice, fermented unrefined wine and formed fruit wine is added to the process, and the above-mentioned concentrating step is carried out by using a reverse osmotic membrane having >=90% exclusion ratio of NaCl, >=90% exclusion ratio of tartaric acid, preferably close to 100%, at 0-50 deg.C within 5 times concentration ratio.

Description

【発明の詳細な説明】 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2発酵
醪および果実酒の中の少なくとも7種を濃縮する工程を
加えた果実酒の製造法に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for producing fruit wine, and more specifically, in the fruit wine production process, a specific reverse osmosis membrane is used to concentrate at least 7 types of fruit juice, fermented moromi, and fruit wine. This invention relates to a method for producing fruit wine that includes a step of

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2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々われでいた
。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
、香味の豊か々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。
Conventionally, when producing a high-quality fruit liquor with a rich flavor, raw materials were carefully selected, and appropriate methods were used in each step of preparation, fermentation, and storage. For example, when it comes to grapes, they must be of high quality, have a suitable location for cultivation, and have good weather during cultivation.
If the conditions such as proper cultivation method and harvest time are met,
It is necessary to use grapes that are fully ripe or overripe, have sufficient sugar 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.

ところで、天候の不順や栽培方法の失敗などによって収
穫時期になっても完熟しない場合がある。
By the way, due to unfavorable weather or failure of the cultivation method, the fruit may not fully ripen even at harvest time.

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
けておシ、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
とされていた。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
件等にょシ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
なものであった。
It was believed that it was impossible to produce high-quality wine from these grapes, as they had insufficient sugar content, lacked acid balance, and were bland with few flavor components. In addition, the Koshu variety, which is the most used variety of grapes for winemaking in Japan, tends to be bland and low in sugar content due to the characteristics of the variety and climatic conditions, so it has disadvantages as a raw material fruit, and it is a raw material for high-quality wine. It was unsatisfactory.

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々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。
Therefore, in order to produce wine with rich flavor using grapes with low sugar content and few flavor components,
Concentrating fruit or fruit juice has been considered for some time. 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.

しかしいずれの場合も香味の損傷が大きい、すなわち加
熱することによってフルーティーな香りが損なわれ、凍
結することによって味の重要部分である酸度が減少して
しまう。
However, in both cases, the flavor is severely damaged; heating destroys the fruity aroma, and freezing reduces the acidity, which is an important part of the taste.

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ってしまうからで
ある。
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, resulting in a concentrated liquid that lacks the characteristics of a fruit liquor.

最近、逆浸透膜や限外濾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30−729797号、同Sθ−ノタグ’l−9’
1号、同Sスー/!f;g9g号)。
Recently, a method has been proposed for concentrating fruit juice or fermented liquid after fermentation using a reverse osmosis membrane or an ultrafiltration membrane (Japanese Patent Application Laid-Open No. 30-729797, Sθ-Notag 'l-9'
No. 1, same S Sue/! f; g9g issue).

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、コク味やボディー感が不充分であり
香味の豊かなものが得られなかった。
However, with these methods, some of the organic acids and amino acids permeate, resulting in insufficient richness and body, and it is not possible to obtain products with rich flavor.

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って目的を達成出来
ることを見出し、かかる知見に基いて本発明を完成する
に至った。
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.

本発明は、果実酒の製造において、果実搾汁液の濃縮工
程2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7つの濃縮工程を加え、かつ該濃縮工程をNa
Ct排除率70%以上、酒石酸排除率′70%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。
In the production of fruit wine, the present invention adds at least seven concentration steps among the fruit juice concentration step 2, the fermented mash concentration step, and the fruit wine concentration step, and the concentration step is
This is a method for producing fruit wine characterized by using a reverse osmosis membrane with a Ct exclusion rate of 70% or more and a tartaric acid exclusion rate of 70% or more.

本発明に使用する逆浸透膜はNaC1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700%に
近いものを選択する。
The reverse osmosis membrane used in the present invention has a NaCl exclusion rate of 90% or more, and is selected to have the highest possible exclusion rate for acids, alcohols, and the like. In particular, tartaric acid, which is the main acidic component of fruit wine, is selected to have an exclusion rate of 90% or more, preferably close to 700%.

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
族ポリイミダシロン)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。
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 polyimidacylon) are not recommended. There is something that meets the purpose of the invention. In addition, the structure of the reverse osmosis membrane concentrator is a pressure plate type or a tubular type.

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
Any shape such as a hollow fiber type can be used.

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2発酵、貯蔵等を行なうもので
ある。
As for the production method of fruit wine, it is sufficient to adopt the commonly used method, and there are no restrictions on the raw materials.
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 the fruit, but in the present invention, the preparation, fermentation, storage, etc. of raw materials are carried out with consideration to maintaining the balance of sour taste. .

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2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5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\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痙過しだ後の液体から
貯蔵された該液体までを意味する。
As mentioned above, in the process of producing fruit wine in the present invention,
Fruit juice concentration step 2 At least one of the fermentation moromi concentration step and fruit wine concentration step is added. 5 In order to obtain a product with good quality, fruit juice or fruit wine or It is preferable to concentrate both of these. Note that the fruit wine to be concentrated here refers to the liquid from the fermented liquid after fermentation to the stored liquid.

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。
Concentration of fruit juice, that is, fruit juice, will be explained using grapes as an example. The raw material grapes are destemmed and crushed.

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\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
は遠心分離によって滓部と清澄部に分画し、該清澄部を
さらに濾過するものである。
It is pressed into free-run fruit juice and pressed fruit juice, which are used alone or in a mixture as raw fruit juice. This fruit juice may be used as is, or it may be used after being clarified. Clarification treatment is carried out as necessary for the purpose of improving the concentration effect and the shelf life of fruit juice, etc. This treatment involves, for example, separating raw fruit juice into a dregs portion and a clarified portion by cooling and standing or centrifuging. , the clarified portion is further filtered.

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−SO℃に調整して香シの飛散や酸化の促進等が
起らないようにして行なう。
Next, when applying the fruit juice to a reverse osmosis concentrator, the temperature should be adjusted within a range where the fruit juice does not freeze or boil, preferably at 0-SO°C, to avoid scattering of incense and promotion of oxidation. Try to avoid it.

また、逆浸透を起させるだ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75度で使用圧力b O
kg/ cTL2の場合、濃縮倍率は約2倍が最大であ
り、また果汁糖度3度で使用圧力gOkg/cm2の場
合は約5倍が最大である。
In addition, regarding the pressure in the reservoir that causes reverse osmosis, consideration must be given to the pressure resistance of the membrane used, but the higher the pressure is, the faster water permeates and the higher the concentration efficiency. The concentration ratio of fruit juice varies depending on the osmotic pressure and working pressure of the original fruit juice. For example, if the sugar content of fruit juice is 75 degrees and the working pressure is
kg/cTL2, the maximum concentration ratio is about 2 times, and when the fruit juice sugar content is 3 degrees and the working pressure is gOkg/cm2, the maximum concentration ratio is about 5 times.

原果汁もしくは」二記の如く濃縮された果汁はそのま\
あるいは補糖、稀釈等の果汁調整を行なってから発酵さ
せる。発酵はサツカロミセス・セレビシェIAM−4’
 2711.などのブドウ酒酵母を使用し、通常の方法
によって培養することによシ行なう。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/−
70%(v/v )の割合で接種し、3−3左00の温
度、pH,2−3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。
Raw fruit juice or concentrated fruit juice as described in 2.
Alternatively, the fruit juice may be fermented after adjusting the fruit juice, such as adding sugar or diluting it. Fermented by Satucharomyces cerevisiae IAM-4'
2711. This is done by using grape wine yeast such as and culturing it by the usual method. For example, a culture solution obtained by culturing grape wine yeast in a conventional manner is added to the above fruit juice.
It is inoculated at a ratio of 70% (v/v), and alcoholic fermentation is carried out under the conditions of temperature, pH, and 2-3. The fermentation ends when the target alcohol content and residual sugar content are reached.

発酵が終了した後、常法により滓引き、貯蔵。After fermentation is complete, the slag is removed and stored using conventional methods.

熟成、濾過等を行なって果実酒を得る。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10−3!;Omy/
を添加する。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−/年で香味の豊か
な酸味の強い、しかもボディーの重厚なワインが得られ
る。貯蔵。
Fruit wine is obtained by aging, filtration, etc. During this time, sulfites (sulfur dioxide gas, potassium metabisulfite) may be used as an antioxidant as needed with SO2 as 10-3! ;Omy/
Add. 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 several months to a year after grapes are harvested. storage.

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。
Even if the wine is aged further, this characteristic does not disappear, and the flavor matures even further.

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、濾
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。
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.

発酵終了後は前記の如く常法によシ滓引き、貯蔵、熟成
、濾過等を行なって果実酒を得る。この場合も、香味が
豊かで酸味の強いボディーの重厚なワインが得られる。
After the fermentation is completed, the fruit liquor is obtained by sloughing, storage, ripening, filtration, etc. in the conventional manner as described above. In this case as well, the result is a heavy-bodied wine with rich flavor and strong acidity.

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7回の処理量を適宜に決定できる等の利点があ
る。
It should be noted that the fermentation mash can be concentrated at any time during the fermentation period, and the amount of the seven times to be processed can be appropriately determined.

内の新酒が主に対象とされ、必要に応じてp過処理、低
温化処理を行なってから濃縮する。濃縮の条件は前述と
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°Cに保つことによってほとんど抑制
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S倍程度までの濃縮が可能であるが、
糖、酸、香味のバランスを保つためにはコ倍以内とする
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、コク味やボディー感が重厚である。
The main target is new sake, which is concentrated after being subjected to p-overtreatment and low-temperature treatment as necessary. The conditions for concentration are the same as described above. When fruit wine is concentrated, some of the water and alcohol flow out as a permeate, similar to the case with fermented moromi, and alcohol, acids, sugars, extracts, aroma components, etc. are concentrated. For alcohol permeation, the temperature during concentration of fruit liquor is low,
For example, it can be almost suppressed by maintaining the temperature at 0-10°C. Concentrating at high temperatures is not preferred because the amount of alcohol permeated increases. In addition, regarding the concentration ratio, it is possible to concentrate up to about S times in terms of liquid volume ratio,
In order to maintain the balance of sugar, acid, and flavor, it is preferable to keep the amount within 10 times. The concentrated fruit liquor obtained in this way has a rich flavor and a strong body and flavor.

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シが高く、酸味の強い
果実酒が得られ、酸味は熟成することによって丸味を帯
び重厚なボディ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
粒を潰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。
According to the present invention, a fruit liquor with high aroma and strong acidity can be obtained even when using light grapes with low sugar content such as Koshu grapes as raw materials, and the acidity becomes rounder with ripening and has a heavy body. It becomes a high-quality sake. Furthermore, in the production of red wine, in order to extract pigments from the pericarp, the fruit is generally crushed and subjected to fermentation, 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.

次に、本発明の実施例を示す。Next, examples of the present invention will be shown.

実施例/ 甲州種ブドウを常法により除梗、破砕、圧搾し。Example/ Koshu grapes are destemmed, crushed, and pressed using conventional methods.

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700ppmになる
様に添加し、7日5−70°Cの温度で静置後、清澄部
と滓部(液量で70%)に分画した。
Free-run fruit juice (juice extraction rate of 60%) was obtained. Potassium metabisulfite was added to this fruit juice at a concentration of 700 ppm as SO2, and after standing at a temperature of 5-70°C for 7 days, it was fractionated into a clear part and a dregs part (70% in liquid volume).

この清澄部をケイソウ上濾過し、清澄果汁100tを調
製した。この果汁を逆浸透装置で濃縮した。
The clarified portion was filtered over a diatomaceous filter to prepare 100 tons of clarified fruit juice. This fruit juice was concentrated using a reverse osmosis device.

逆浸透膜はポリベンズイミダシロン系膜で、 NaC1
阻止率qg%、酒石酸阻止率99%のものを使用した。
The reverse osmosis membrane is a polybenzimidacylon-based membrane, with NaC1
The one with a blocking rate of qg% and a tartaric acid blocking rate of 99% was used.

また、その装置は膜面積7.2乙m2の管状膜構造のも
のを用いた。温度は室温(75°C)で行なったが、操
作中7−23.3℃までの温度上昇がみられた。使用圧
は35kg/cn12とした。透過液はほとんど無味無
臭の水であった。濃縮倍率7.99倍のもの(濃縮液■
)をttot、濃縮倍率/6g3倍のもの(濃縮液■)
を2,2を得だ。
The device used had a tubular membrane structure with a membrane area of 7.2 m2. Although the temperature was room temperature (75°C), the temperature rose to 7-23.3°C during the operation. The working pressure was 35 kg/cn12. The permeate was almost tasteless and odorless water. Concentration magnification 7.99 times (concentrated solution■
) tot, concentration ratio/6g3 times (concentrate ■)
I got 2.2.

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表に示しだ。
Table 1 shows the fruit juice analysis values for the three types of concentrated liquid and original fruit juice before concentration.

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77度であったので、
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。酒母ハサツ力ロミセス・セレビ
シェIAM1.2’711の発酵醪をそれぞれに5%ず
つ添加した。発酵温度はlS±/℃とした。
Wine was made from three types of fruit juice: raw fruit juice, concentrated liquid ■, and ■, and a comparative study was conducted. The sugar content of the original fruit juice was 77 degrees, so
Sugar was supplemented with caster sugar to aim for a sugar content of 22 degrees. Concentrates ■ and ■ were used as fermented moromi as they were. 5% of the fermented mash of the yeast mother Hasatsuriki Romyces cerevisiae IAM1.2'711 was added to each. The fermentation temperature was 1S±/°C.

発酵状況はいずれも順調であシ、原果汁および濃縮液■
は/(L−12日でアルコール発酵が終了した。濃縮液
■は/l1日目でアルコールが/4度近くになったので
、冷却、S02の添加で発酵を停止させた。発酵終了時
にはSO2を/ 00 ppm添加し、5’Cまで冷却
してケイソウ上濾過によシ酵母を分離した。得られた果
実酒はピン詰めし、70−72°Cで貯蔵した。
Fermentation status is good, raw fruit juice and concentrate ■
/(L- Alcoholic fermentation was completed in 12 days. As for the concentrated liquid ■, the alcohol was almost /4 degrees on the 1st day, so the fermentation was stopped by cooling and adding SO2. At the end of fermentation, SO2 /00 ppm was added, cooled to 5'C and filtered over diatomaceous to separate the yeast.The resulting fruit wine was packed in pins and stored at 70-72°C.

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勇退速度との関係を第1図
に示す。
Table 2 shows the analytical values for the fruit wine. Table 3 also shows the results of product tasting by experts. As is clear from the table,
Fermented concentrate produces a rich and heavy wine. Figure 1 shows the relationship between the concentration ratio of fruit juice and the rate of water withdrawal.

実施例ス リンゴ700に’jを常法により破砕、圧搾し、リンゴ
果汁70t(糖度/l’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700ppmにな
るように添加し、3日間冷温静置後、清澄濾過処理し、
清澄果汁ろ0tを得た。この果汁を原果汁とし、その4
tOtを逆浸透装置を使って濃縮した。逆浸透膜および
その装置は実施例/と同一のものを使用した。濃縮によ
り透過液/2tを得、濃縮率を/、17.3倍とした。
Example 700 tons of apple juice (sugar content/l' degree) was obtained by crushing and pressing Slingo 700 'j' in a conventional manner. Potassium metabisulfite was added to this apple juice to a concentration of 700 ppm as SO2, and after being left at a cold temperature for 3 days, it was subjected to a clarifying filtration treatment,
0 tons of clarified fruit juice was obtained. This fruit juice is used as the original fruit juice, part 4
The tOt was concentrated using a reverse osmosis device. The reverse osmosis membrane and its equipment were the same as in Example. The permeate/2t was obtained by concentration, and the concentration ratio was 17.3 times.

この透過液は無味無臭であったが、その揮発性香気成分
をガスクロマトグラフィーを用いて検討した。原果汁に
はエチル−ニーメチルブチレイト、ヘキサノール。
Although this permeate was tasteless and odorless, its volatile aroma components were investigated using gas chromatography. The raw fruit juice contains ethyl-nimethylbutyrate and hexanol.

ノーへキザ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った。
Substances characteristic of apples such as Nohekizanal were observed, but they were hardly detected in the permeate.

この濃縮液および原果汁を常法によシ発酵させ、果実酒
を得だ。原果汁は糖度が/弘度であったので、砂糖で糖
度2θ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、7.2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/ 00 ppm添加し、濾過処理してぎン詰め
貯蔵した。仕込後ダケ月目での分析値および試飲結果を
第を表および第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っ
て行なった。また、刑酒は刑酒パネル70名により香、
味についてS点滴点法で行ない、優れた品質のもの3点
、良い品質のもの9点、平均的品質のもの3点、多少欠
点のある品質のものλ点、劣った品質のもの7点とし、
その平均点で示した。
This concentrate and raw fruit juice are fermented in a conventional manner to obtain fruit wine. Since the original fruit juice had a sugar content of 20 degrees, it was supplemented with sugar to a sugar content of 2θ degrees to make it the same as the sugar content of the concentrate. All fermentation conditions were normal, and main fermentation was completed in 7.2 days. At the same time as the main fermentation is completed, add potassium metabisulfite to SO2.
/ 00 ppm was added, filtered and stored in a bottle. The analysis values and tasting results in the month after preparation are shown in Table 1 and Table 5. The alcohol content, extract content, and total acid content of the fruit wine were analyzed in accordance with the National Tax Agency's prescribed analytical method commentary. In addition, 70 members of the Goshu panel have selected the incense for Goshu.
The taste was evaluated using the S drip method, and 3 points were given for excellent quality, 9 points were given for good quality, 3 points were given for average quality, λ points were given for somewhat defective quality, and 7 points were given for poor quality. ,
The average score is shown.

濃縮リンゴ酒は特に芳香が強く、特徴のある酒となった
Concentrated cider has a particularly strong aroma and has become a distinctive drink.

実施例3 甲州種ブドウから得た果汁を濃縮することな〈実施例/
と同様にして発酵させ果実酒を得た。仕込後qケ月でケ
イソウ士濾過し、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シロン系ポリマーでNaC1阻止
率9g%、酒石酸阻止率99%のものである。新酒はセ
ミドライタイブのもので、エキス分および酸はほぼ10
0%濃縮側に残った。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700%になった。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った。
Example 3 Without concentrating the juice obtained from Koshu grapes (Example/
It was fermented in the same manner as above to obtain fruit wine. After q months of preparation, it was filtered through a diaphragm filter and subjected to reverse osmosis concentration treatment. The reverse osmosis membrane used was a polybenzimidacylon polymer having a NaCl rejection of 9 g% and a tartaric acid rejection of 99%. The new sake is a semi-dry type, with an extract content and acid content of approximately 10%.
It remained on the 0% concentration side. Although some alcohol also leaked out to the permeate side, when both the concentrated side and permeate side were combined, the mass balance was approximately 700%. In other words, the permeate was alcoholic water and had no scent other than the alcohol smell.

第乙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
解に従って行なった。また第7表はその濃縮果実酒の試
飲結果である。刑酒は荊酒パネル70名によシ香、味に
ついて5点滴点法で行ない、優れた品質のもの3点、良
い品質のもの9点、平均的品質のもの3点、多少欠点の
ある品質のものλ点、劣った品質のもの7点とし、その
平物点て示した。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用型
率との関係を第2図に示した。
Table B 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 National Tax Agency's prescribed analytical method commentary. Table 7 shows the tasting results of the concentrated fruit wine. The sake was tested by 70 members of the Jingzhu panel to determine the aroma and taste using the 5-point infusion method.3 points were of excellent quality, 9 points were of good quality, 3 points were of average quality, and 3 points were of slightly defective quality. The λ points for those with poor quality and 7 points for those with inferior quality are shown. All concentrated fruit liquors have a strong flavor,
It was praised for its particularly strong acidity and potential for becoming a high-quality wine. Furthermore, the relationship between the average treatment temperature during concentration and the alcohol molding rate of the membrane is shown in FIG.

実施例グ リンゴを常法によシ仕込んだ新酒をケイソウ十濾過し、
逆浸透濃縮処理した。逆浸透膜モジコーーール(/、、
24m2//モジユール)およびその装置は実施例3と
同一のものを使った。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±
7℃の範囲でコントロールした。処理温度は10℃およ
び2S℃で行なった。
Example New sake made with gringo in a conventional manner is filtered through a diatomaceous filter.
Concentrated by reverse osmosis. Reverse osmosis membrane module (/,,
24 m2//module) and its equipment were the same as in Example 3. Here, in order to keep the processing temperature constant, the stock solution tank is cooled or heated to keep the target processing temperature within ±
The temperature was controlled within the range of 7°C. The treatment temperature was 10°C and 2S°C.

原液S0tを処理し、透過液/Stを取り、濃縮液は濃
縮率で/、’13倍とした。使用平均圧力は33 kg
/cm’で、/Stの透過液を得るのに10°Cでλ時
間25分、、230Cで7時間35分を要し、平均透過
速度は10°Cで’1.93 t/ hr、m2.23
00で7.321/ hr 、 m2であった。
The stock solution S0t was processed, the permeate solution /St was taken, and the concentrated solution was made at a concentration ratio of /, '13. Average operating pressure is 33 kg
/cm', it takes λ time 25 min at 10°C to obtain a permeate of /St, 7 hours 35 min at 230C, and the average permeation rate is '1.93 t/hr at 10°C. m2.23
00, it was 7.321/hr, m2.

この濃縮におけるそれぞれの分析値は第5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。
The analytical values for each concentration are shown in Table 5, 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.

このよう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。
The concentrated apple wine obtained in this way had a slightly strong sour taste but a rich taste, and was evaluated as having the potential to be of high quality, similar to grape wine.

【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。 特許出願人 サッポロビール株式会社 代 理 人 弁理士人傑1)藤 部  23−
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. Patent applicant: Sapporo Breweries Ltd. Representative: Patent attorney Hitoshi 1) Fujibe 23-

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1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7つの濃縮工程を加え、かつ該濃縮工程をNaC1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−SO℃、濃縮倍率3倍以内にて
行なう特許請求の範囲第1項記載の方法。
[Claims] 1. In the production of fruit wine, at least seven concentration steps among the fruit juice concentration step 1 fermentation moromi concentration step and fruit wine concentration step are added, and the concentration step is performed by eliminating NaCl. A method for producing fruit wine, characterized in that it is carried out using a reverse osmosis membrane with a tartaric acid removal rate of 90% or more and a tartaric acid rejection rate of 90% or more. 2. The method according to claim 1, wherein the concentration step is carried out at a temperature of 0-SO° C. and at a concentration ratio of 3 times or less.
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 true JPS596879A (en) 1984-01-13
JPH036787B2 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)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2016026492A (en) * 2014-07-03 2016-02-18 三菱化学株式会社 Method for concentrating liquid food

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

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2016026492A (en) * 2014-07-03 2016-02-18 三菱化学株式会社 Method for concentrating liquid food

Also Published As

Publication number Publication date
JPH036787B2 (en) 1991-01-30

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