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JPS637773A - Preparation of fruit liquor - Google Patents

Preparation of fruit liquor

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Publication number
JPS637773A
JPS637773A JP61148160A JP14816086A JPS637773A JP S637773 A JPS637773 A JP S637773A JP 61148160 A JP61148160 A JP 61148160A JP 14816086 A JP14816086 A JP 14816086A JP S637773 A JPS637773 A JP S637773A
Authority
JP
Japan
Prior art keywords
fruit
fruit juice
juice
concentration
ultrafiltration membrane
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
JP61148160A
Other languages
Japanese (ja)
Other versions
JPH051708B2 (en
Inventor
Yoshimi Shimazu
島津 善美
Takashi Shinohara
隆 篠原
Masaaki Nagao
公明 長尾
Masaru Shimazaki
大 島崎
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.)
Kikkoman Corp
Original Assignee
Kikkoman Corp
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 Kikkoman Corp filed Critical Kikkoman Corp
Priority to JP61148160A priority Critical patent/JPS637773A/en
Publication of JPS637773A publication Critical patent/JPS637773A/en
Publication of JPH051708B2 publication Critical patent/JPH051708B2/ja
Granted legal-status Critical Current

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

Abstract

PURPOSE:To prepare a fruit liquor emitting agreeable and refreshing rich fruity fragrance of fresh fruit juice and having high quality, by carrying out filtration of fruit juice with ultrafiltration membrane and concentration of the filtered juice and subjecting the product to alcoholic fermentation. CONSTITUTION:Fruit such as grape, apple, plum, etc., is crushed and squeezed by conventional method and the obtained fruit juice is filtered with an ultrafiltration membrane having a fractionation molecular weight of 10,000-100,000. The fruit juice is concentrated to 1.3-1.8 times by reverse- osmosis concentration, freeze-concentration, etc., before or after the filtration treatment. The filtered and concentrated juice is added with wine yeast or SAKE yeast, etc., and subjected to alcoholic fermentation by conventional methods.

Description

【発明の詳細な説明】 本発明は、果実酒の製造法、特に果実酒を常法により破
砕、圧搾して得られる果汁を限外濾過膜による濾過と、
濃縮の画処理を行ない、次いで常法によりアルコール発
酵させることによって、原果汁特有の良好で爽快な果実
様香気を濃厚に有し、品質も良好な果実酒が得られる、
画期的な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 in particular, to a process of filtering fruit juice obtained by crushing and pressing fruit wine using an ultrafiltration membrane using an ultrafiltration membrane.
By carrying out a concentration process and then carrying out alcoholic fermentation using a conventional method, a fruit liquor of good quality and rich in the pleasant and refreshing fruit-like aroma characteristic of original fruit juice can be obtained.
Concerning an innovative method for producing fruit wine.

近年、食生活の洋風化および高級化に伴い、風味が良好
で高品質の果実酒の需要が増大しつつあるが、−般に果
実酒は良好な果実様香気に乏しく充分に満足し得るもの
ではなかった。
In recent years, with the westernization and luxury of eating habits, the demand for high-quality fruit wines with good flavor has been increasing; It wasn't.

従来、香気、風味の優れた果実酒を得る方法として、果
汁を逆浸透膜などの膜分離法で濃縮(脱水)し、該濃縮
果汁を発酵させる方法(特開昭50−19797、同5
0−154494、同57−105180.同59−6
879)が知られているが、これらの方法は、果実の破
砕物またはその果汁に含まれる雑菌、混濁物質、高分子
量物質、好ましくない香味等を除去することなく濃縮し
た果汁を発酵させるために、原果汁特有の良好で爽快な
果実様香気を濃厚に有する果実酒は得られず、また製品
は色調、透明度が悪く、混濁が生じ易い等品質の面で充
分満足するものとは言い難い〇 また、果汁を限外濾過膜で濾過し、これを発酵させる方
法(特公昭55−8147)も知られているが、この方
法は糖度が低し・果汁を用いる場合、原果汁特有の一良
好な果実様香気を濃厚に有する果実酒は得られず、また
該果汁或いは発酵途中の醪に砂糖、グルコース等の糖類
を添加する、し・わゆる補糖の操作が必要となり、得ら
れる果実酒は風味が淡白となり、残糖組成においてグル
コースの割合が多くなり、切れの悪い甘味を呈する問題
点を有する。
Conventionally, as a method for obtaining fruit wine with excellent aroma and flavor, a method has been proposed in which fruit juice is concentrated (dehydrated) using a membrane separation method such as a reverse osmosis membrane, and the concentrated fruit juice is fermented (Japanese Patent Application Laid-Open No. 1979-1979, 1979-5).
0-154494, 57-105180. 59-6
879), but these methods are used to ferment concentrated fruit juice without removing bacteria, cloudy substances, high molecular weight substances, undesirable flavors, etc. contained in crushed fruit or its juice. However, it is not possible to obtain a fruit liquor that has a rich and refreshing fruit-like aroma characteristic of raw fruit juice, and the product is not completely satisfactory in terms of quality, such as poor color tone, poor transparency, and turbidity. In addition, a method of filtering fruit juice with an ultrafiltration membrane and fermenting it is also known (Japanese Patent Publication No. 55-8147), but this method has a low sugar content, and when using fruit juice, it has the characteristics of raw fruit juice. It is not possible to obtain a fruit liquor with a rich fruit-like aroma, and it is necessary to add sugars such as sugar, glucose, etc. to the fruit juice or moromi during fermentation, which is a so-called supplementary sugar operation. The problem is that the flavor is bland and the proportion of glucose in the residual sugar composition is high, resulting in a dull sweet taste.

そこで、本発明者らは、原果汁特有の良好で爽快な果実
様香気を濃厚に有し、品質も良好な果実酒の製造法を開
発することができれば、果実酒業界にとって多大の貢献
となることに着目し、種々検討を重ねた結果、果汁を特
定の限外濾過膜による濾過と、逆浸透膜等による濃縮の
画処理を行ない、次いで常法によりアルコール発酵させ
るときは原果汁特有の良好で爽快な果実様香気を濃厚に
有し、品質も良好な果実酒が得られること、そして前記
果汁の濃縮が1.3〜1.8倍濃縮の場合、その効果が
著しいことを知った。
Therefore, the present inventors believe that if they can develop a method for producing fruit wine that has a rich, refreshing fruit-like aroma unique to raw fruit juice and is of good quality, it will be a great contribution to the fruit wine industry. Focusing on this, and as a result of various studies, we found that when fruit juice is filtered using a specific ultrafiltration membrane and concentrated using a reverse osmosis membrane, etc., and then subjected to alcoholic fermentation using a conventional method, it is possible to achieve the unique properties of original fruit juice. It has been found that a fruit wine with a rich refreshing fruity aroma and good quality can be obtained, and that the effect is remarkable when the fruit juice is concentrated 1.3 to 1.8 times.

以下、これらの点に関し、実験例を挙げて説明する。These points will be explained below using experimental examples.

実験例1 昭和58年度産「甲州ブドウ」を常法により破砕、圧搾
して得られた果汁に、亜硫酸およびペクチン分解酵素を
添加し、5°Cで15時間静置後、滓引、遠心分離し、
その上澄部分をセライトにより清澄濾過し、清澄果汁(
糖度16.3%)を得た。
Experimental Example 1 Sulfurous acid and pectin-degrading enzyme were added to the juice obtained by crushing and pressing Koshu grapes produced in 1982 using a conventional method, and after standing at 5°C for 15 hours, the juice was sludged and centrifuged. death,
The supernatant part is clarified and filtered through Celite, and the clarified fruit juice (
The sugar content was 16.3%).

この果汁を201づつA、B、Cの3つの区分に分け、
Aの区分(比較例1)は分画分子量50.000の限外
濾過膜を用いて濾過し、Bの区分(比較例2)は逆浸透
膜を用いて約1.6倍濃縮し、Cの区分(本発明)は分
画分子量50.000の限外濾過膜を用いて濾過した後
、該濾液を逆浸透膜を用いて約1.6倍濃縮し、それぞ
れ3種類の調製果汁を得た。
Divide this fruit juice into 3 categories of 201 each: A, B, and C.
Category A (Comparative Example 1) was filtered using an ultrafiltration membrane with a molecular weight cutoff of 50.000, and Category B (Comparative Example 2) was concentrated approximately 1.6 times using a reverse osmosis membrane. In the category (the present invention), after filtration using an ultrafiltration membrane with a molecular weight cutoff of 50.000, the filtrate is concentrated approximately 1.6 times using a reverse osmosis membrane to obtain three types of prepared fruit juice. Ta.

次いで、この調製果汁にブドウ酒酵母を加え、常法によ
り30日間アルコール発酵させ、次いで滓引き、メンプ
ランフィルターンこよる清澄濾過を行ない、それぞれA
、B、Cの3種類の果実酒(白ワイン)を得た。
Next, grape wine yeast was added to this prepared fruit juice, and alcoholic fermentation was carried out for 30 days by a conventional method, followed by slag removal and clarification filtration using a membrane filter.
Three types of fruit wine (white wine), B and C, were obtained.

次いて、上記Cの果実酒(本発明)について、2点比較
法ンこよりA(比較例1)またはB(比較例2)を対照
として、20名の識別能力を有する訓諌されたパネルに
より官能検査を行なったところ第1表ンこ記載の如き結
果が得られた。
Next, the above fruit wine C (the present invention) was compared with A (Comparative Example 1) or B (Comparative Example 2) using a two-point comparison method by a trained panel of 20 people with discernment ability. When a sensory test was conducted, the results shown in Table 1 were obtained.

この結果から明らかな如く、果汁を限外濾過と濃縮の両
処理を施した果汁を用いて得られた果実酒は、限外濾過
果汁を用いて得られた果実酒Aまたは逆浸透膜濃縮果汁
を用いて得られた果実酒Bに比べて、著しく果実様香気
に優れ、またその香気も強いことが判る。
As is clear from this result, fruit liquor obtained using fruit juice that has been subjected to both ultrafiltration and concentration treatment is different from fruit liquor A obtained using ultrafiltered fruit juice or fruit juice concentrated by reverse osmosis membrane. It can be seen that the fruit-like aroma is significantly superior to that of fruit liquor B obtained using the above-mentioned fruit liquor B, and the aroma is also strong.

実験例2 上記実験例1のCの区分(本発明)の果実酒の製法にお
いて、濃縮倍率を第2表記載の如き値とする以外は全く
同様にして果実酒を製造し、得られた果実酒について1
0名の識別能力を有する訓練されたパネルにより官能検
査を行なったところ、第2表に示す如ぎ結果が得られた
Experimental Example 2 Fruit wine was produced in exactly the same manner as above in the method for producing fruit wine in Category C (invention) of Experimental Example 1, except that the concentration ratio was set to the values listed in Table 2. About alcohol 1
When a sensory test was conducted by a trained panel of 0 people with discrimination ability, the results shown in Table 2 were obtained.

尚、官能検査は、対照(濃縮倍率1.0、即ち濃縮なし
)の果実酒を標準(士O)とし、下記基準で採点し、そ
の平均値をもって示した。
In addition, for the sensory test, the fruit wine of the control (concentration ratio 1.0, ie, no concentration) was used as the standard (ShiO), and was scored according to the following criteria, and the average value was shown.

−4−3−2−1±O+1  +2  +3  +4常
  な  る  や  準  や  い  な  常に
   リ       劣      良      
 リ   に劣  劣      る      い 
     良  良る   る           
                い   いこの結果
から明らかな如く、果汁を特定の限外濾過膜による濾過
と、逆浸透膜等による濃縮の両処理を行なうに際し、濃
縮倍率が1.3〜1.8倍のとき、特に爽快な果実様香
気を濃厚に有する果実酒が得られることが判る。
-4-3-2-1±O+1 +2 +3 +4 always poor
inferior to li
good good
As is clear from these results, when fruit juice is both filtered using a specific ultrafiltration membrane and concentrated using a reverse osmosis membrane, it is especially refreshing when the concentration ratio is 1.3 to 1.8 times. It can be seen that a fruit wine with a rich fruit-like aroma can be obtained.

本発明は、これらの知見に基づいて完成したものであっ
て、果汁を分画分子量10.000〜100.000の
限外濾過膜を用いて濾過し、その前または後ンこ該果汁
を濃縮し、次いで前記濾過によって得られた濾過果汁を
常法によりアルコール発酵させることを特徴とする果実
酒の製造法である。
The present invention was completed based on these findings, and involves filtering fruit juice using an ultrafiltration membrane with a molecular weight cutoff of 10.000 to 100.000, and concentrating the fruit juice before or after that. This is a method for producing fruit wine, which is characterized in that the filtered fruit juice obtained by the filtration is then subjected to alcoholic fermentation by a conventional method.

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

先ず、本発明において用いられる果汁としては例えば、
ブドウ、リンゴ、ナ7、ビワ、モモ、ミカン、ウメ、ス
モモ等の果実酒を常法により破砕、圧搾して得た生果汁
が特に好適であるが、市販の果汁、更には例えば乾ブド
ウ等を水抽出して得た果汁を用いることもできる。また
果実としては上記したような果実類を単独または組合せ
て用いることがてきる。
First, examples of fruit juices used in the present invention include:
Fresh fruit juices obtained by crushing and pressing fruit wines such as grapes, apples, loquats, peaches, mandarin oranges, plums, and plums in a conventional manner are particularly suitable, but commercially available fruit juices, as well as dried grapes, etc. It is also possible to use fruit juice obtained by extracting with water. Further, as the fruit, the above-mentioned fruits can be used alone or in combination.

次に、この果汁を限外濾過膜を用いて濾過するか、また
は逆浸透膜等による濃縮するに際しては、予め、この果
汁に防腐、酸化防止のために、常法により例えば亜硫酸
、メタ重亜硫酸カリウム等を加えるのが好ましく、その
添加量は20〜300 p、p、m、となるようVこす
るのが好適である。
Next, when this fruit juice is filtered using an ultrafiltration membrane or concentrated using a reverse osmosis membrane, etc., the fruit juice is pretreated with sulfurous acid, metabisulfite, etc., in order to preservative and prevent oxidation. It is preferable to add potassium or the like, and the amount of addition is preferably 20 to 300 p, p, m.

また、果汁に混濁物が含まれていても、これをそのまま
限外濾過膜で濾過処理することは可能であるが、この場
合は、限外濾過膜の処理能力が低下するので、この果汁
に常法により例えばペクチン分解酵素を混合、分散させ
た後、静置による混濁物質の沈下、セライト等を用いて
清澄濾過、遠心分離等の適宜の清澄化法を施して果汁を
清澄化させ、次いでこの果汁を限外濾過膜で処理するの
が好ましい。尚、ペクチン分解酵素の添加量は、果実、
使用酵素剤の種類等によって異なるので、適宜選択決定
すれば良い。
Furthermore, even if the fruit juice contains turbid substances, it is possible to directly filter it through an ultrafiltration membrane, but in this case, the processing capacity of the ultrafiltration membrane will decrease, so the fruit juice cannot be filtered. After mixing and dispersing, for example, a pectin-degrading enzyme by a conventional method, the fruit juice is clarified by settling the turbid substances by standing, performing an appropriate clarification method such as clarification filtration using Celite, centrifugation, etc., and then clarifying the fruit juice. Preferably, this fruit juice is treated with an ultrafiltration membrane. The amount of pectin-degrading enzyme added is based on fruit,
Since it differs depending on the type of enzyme used, etc., it may be selected and determined as appropriate.

次ニ、本発明において用いる限外濾過膜の例としては、
ダイセル化学工業社製限外濾過膜、アミコン社製のダイ
アフロー限外濾過膜、日本真空技術社製のダイアフィル
ター、バイオエンジニアリング社製のダイアフィルター
膜等が挙げられる0そして、本発明において用いる限外
濾過膜は分子量10.000以上の物質を除去する能力
を有する限外濾過膜(分画分子量10.000の限外濾
過膜)乃至分子量100.000以上の物質を除去する
能力を有する限外濾過膜(分画分子量100.000の
限外濾過膜)が、果汁中に含まれ、品質の良い果実酒を
得るのに不都合な微生物群、混濁物質、高分子量物質口
例えば高分子ポリフェノール、高分子ペクチン、グルカ
ン、蛋白質(酸化褐変酵素群等)]す除去するのに好適
であり、特に分画分子量20.000〜50.000の
限外濾過膜が好適である。そしてこのような限外濾過膜
の具体例としては、例えばDUY−H(分画分子量to
、000) 、DUY−M (同20.000) 、D
UY−L (同40,000)  (以上いずれもダイ
セル化学工業社製限外濾過膜の商品名)、UMIO(同
10.000) 、UM20E (同20,000) 
、PMlo(同10,000) 、PM30 (同30
,000) 、XM50(同50,000) 、XMl
ooA (同100,000)  (以上アミコン社製
ダイアフロー限外濾過膜の商品名)、G−107(同1
0,000) 、HFA−180(同15,000)、
HFA −200(同20,000) 、HFA−30
0(同30.000 )(以上バイオエンジニアリング
社製ダイアフィルター膜の商品名)等が挙げられる。
Second, examples of ultrafiltration membranes used in the present invention include:
Ultrafiltration membranes manufactured by Daicel Chemical Industries, Ltd., Diaflow ultrafiltration membranes manufactured by Amicon, Diafilters manufactured by Japan Vacuum Technology Co., Ltd., Diafilter membranes manufactured by Bioengineering, etc. The extrafiltration membrane is an ultrafiltration membrane that has the ability to remove substances with a molecular weight of 10.000 or more (ultrafiltration membrane with a molecular weight cutoff of 10.000) or an ultrafiltration membrane that has the ability to remove substances with a molecular weight of 100.000 or more. A filtration membrane (ultrafiltration membrane with a molecular weight cutoff of 100.000) is used to filter out microorganisms, turbid substances, and high molecular weight substances contained in fruit juice that are inconvenient for obtaining high quality fruit wine, such as high molecular weight polyphenols and high molecular weight substances. It is suitable for removing molecular pectin, glucan, protein (oxidative browning enzyme group, etc.), and an ultrafiltration membrane with a molecular weight cutoff of 20.000 to 50.000 is particularly suitable. As a specific example of such an ultrafiltration membrane, for example, DUY-H (molecular weight cutoff to
, 000), DUY-M (20.000), D
UY-L (40,000 yen) (all of the above are product names of ultrafiltration membranes manufactured by Daicel Chemical Industries, Ltd.), UMIO (10,000 yen), UM20E (20,000 yen)
, PMlo (10,000), PM30 (30
,000), XM50 (50,000), XMl
ooA (100,000) (trade name of Diaflow ultrafiltration membrane made by Amicon), G-107 (100,000)
0,000), HFA-180 (15,000),
HFA-200 (20,000), HFA-30
0 (30.000) (the above is a trade name of Diafilter membrane manufactured by Bio Engineering Co., Ltd.), and the like.

次に、果汁を限外濾過膜により濾過処理するには、適当
な限外濾過装置を選んで行なえばよい。
Next, in order to filter the fruit juice using an ultrafiltration membrane, an appropriate ultrafiltration device may be selected.

その例としては、例えば耐圧且つ密閉状につくられた容
器の底部付近に設けらハた耐圧性の合成樹脂などで作ら
れた多孔板の上に限外濾過膜をセットし、上部に原液投
入口および圧力調整器を、そして底部に透過液排出口を
有し、原液投入口より原液(果汁)を入れ、圧力調整器
を通じて圧縮空気または窒素ガスを1〜5 kg / 
ctl (ゲージ圧)の圧力で圧入し、該容器内の原液
を撹拌しながら限外濾過膜による濾過を行ない、透過液
排出口より濾液を得るようになっている装置等が挙げら
れる。このような装置としては、例えばアミフン社製の
撹拌セル方式スタンダードセル: モデル402、限外
濾過器モデルTC−1.ダイセル化学工業社製限外濾過
モジュール組込装置等が挙げられる。
For example, an ultrafiltration membrane is placed near the bottom of a pressure-resistant and airtight container, and an ultrafiltration membrane is set on a perforated plate made of pressure-resistant synthetic resin, and the undiluted solution is poured into the top. It has an opening and a pressure regulator, and a permeated liquid outlet at the bottom.The stock solution (fruit juice) is input from the stock solution input port, and compressed air or nitrogen gas is supplied through the pressure regulator at a rate of 1 to 5 kg/
Examples include an apparatus in which the liquid is injected under pressure of CTL (gauge pressure), the stock solution in the container is filtered through an ultrafiltration membrane while stirring, and the filtrate is obtained from a permeate outlet. Examples of such devices include, for example, the stirred cell type standard cell model 402 manufactured by Amifun Co., Ltd., and the ultrafilter model TC-1. Examples include an ultrafiltration module built-in device manufactured by Daicel Chemical Industries, Ltd.

果汁の濾過速度(透過速度)は圧力、限外濾過膜の種類
、その表面積等によっても異なるが、例えば上記のスタ
ンダードセル:モデル402に限外濾過膜PM30をセ
ットして、清澄化させた果汁を処理する場合は2 kg
 / crl (ゲージ圧)で流速2〜20が/d/時
間である。
The filtration rate (permeation rate) of fruit juice varies depending on the pressure, the type of ultrafiltration membrane, its surface area, etc.; 2 kg when processing
/crl (gauge pressure) and the flow rate is 2-20 /d/hour.

次に、果汁を濃縮する方法としては、該果汁が褐変せず
、しかも果汁の有用な風味、芳香および成分の変化、損
失等、品質の劣化が少ない方法であれば、いかなる方法
でも良い。例えば、セルロースアセテート膜を通し、浸
透圧よりさらに高い圧力で加圧することにより、水分を
希薄溶液の方に移行させる逆浸透圧による濃縮法、果汁
を減圧下において低温で比較的長時間(35°C以下、
30〜60分)濃縮する、強制循環式または薄膜降下式
などの真空低温濃縮法、果汁を減圧下において比較的高
温でごく短時間(30〜60°C1数分以下)濃縮する
、デ・ラバル・セントリサーム(De Laval C
entritherm ) 、チースト(Taste)
 、APvなどのエバポレーターによる真空高温濃縮法
および果汁に含まれる水分を固形の氷の形で分離除去す
る凍結濃縮法が挙げられるが、これらのうち特に逆浸透
濃縮法及び凍結濃縮法が品質劣化が少ないので好ましい
Next, as a method for concentrating the fruit juice, any method may be used as long as the method does not cause browning of the fruit juice and causes less deterioration of quality such as change or loss of useful flavor, aroma, and components of the fruit juice. For example, there is a concentration method using reverse osmosis in which water is transferred to a dilute solution by applying pressure higher than osmotic pressure through a cellulose acetate membrane. Below C,
30 to 60 minutes), vacuum low-temperature concentration methods such as forced circulation type or thin film descent type, concentrating fruit juice under reduced pressure at a relatively high temperature for a very short time (30 to 60°C, a few minutes or less), De Laval・Scentrisam (De Laval C
Entritherm), Cheest (Taste)
, high-temperature vacuum concentration using an evaporator such as APv, and freeze concentration that separates and removes water contained in fruit juice in the form of solid ice. Among these methods, reverse osmosis concentration and freeze concentration are particularly susceptible to quality deterioration. It is preferable because it is small.

次ンこ濃縮の程度は任意であるが、上記実験例2の結果
からも明らかな如く、原果汁を1.3〜1.8倍濃縮す
るとき、特に爽快な果実様香気を濃厚に有する果実酒が
得られるので好ましい。
The degree of condensation is arbitrary, but as is clear from the results of Experimental Example 2 above, when the original fruit juice is concentrated 1.3 to 1.8 times, fruit with a particularly refreshing fruit-like aroma is concentrated. This is preferable because alcohol can be obtained.

次に、本発明において、果汁を限外濾過膜による濾過と
、濃縮の両処理を行なうことは極めて重要であって、い
ずれか−方の処理だけでは、前記実験例の結果からも明
らかな如く、良好な果実様香気を濃厚に有する果実酒は
得られない。
Next, in the present invention, it is extremely important to perform both filtration of fruit juice using an ultrafiltration membrane and concentration. , it is not possible to obtain a fruit wine that has a rich fruit-like aroma.

そして、どちらの処理を先に行なっても良いが、先に濃
縮を行ない、次いで限外濾過膜による濾過を行なうとき
は、その逆の場合に比べて更に果実様香気の高い果実酒
が得られるので好ましし)。
Although either treatment may be performed first, if the concentration is first performed and then the filtration is performed using an ultrafiltration membrane, a fruit liquor with a higher fruit-like aroma will be obtained than the reverse case. Therefore, it is preferable).

次いで、このようにして得られた果汁を常法により優良
純粋酵母を添加後、例えば5〜35°C1pH2〜5で
7〜60日間、アルコールJi[させる。ここに用いら
れる優良酵母としては、通常の果実酒製造に用いられる
酵母が有効に適用される。
Next, after adding good quality pure yeast to the fruit juice obtained in this way by a conventional method, it is subjected to alcohol treatment at, for example, 5 to 35[deg.] C. and pH 2 to 5 for 7 to 60 days. As the excellent yeast used here, yeast used in ordinary fruit wine production can be effectively applied.

そして、例えばワイン酵母、清酒酵母等が好適な例とし
て挙げられ、その最も代表的なものとしては、例えばサ
ツカロミセス・セレビシェ等が挙げられる。
Suitable examples include wine yeast and sake yeast, and the most representative example is Satscharomyces cerevisiae.

アルコール発酵を終了した醪は、常法により滓引したの
ち、例えばセライト等を用いての濾過、遠心分離等によ
る清澄化を行なって、酵母菌体等を除き、貯蔵タンク等
に貯蔵して嫌気的に保ち、例えば3〜12ケ月間熟成さ
せて製品とする。
After alcoholic fermentation, the moromi is sludged using a conventional method, and then clarified by filtration using Celite, centrifugation, etc. to remove yeast cells, etc., and stored in a storage tank etc. for anaerobic storage. The product is then aged for, for example, 3 to 12 months.

このようにして、本発明によれば、原料果汁を限外濾過
膜による濾過と、濃縮の両処理を行なうもので、処理果
汁中には野生酵母、バクテリア等の雑菌、混濁物質、高
分子ポリフェノール、高分子ペクチン、グルカン、酸化
褐変酵素群等が少ないか、または殆ど無く、反対に酵母
の増殖に有用な窒素成分およびカリウム、マグネシウム
等の灰分の濃度が高いので、優良純粋酵母による健全で
しかも旺盛な発酵を持続して行なうことが可能となる。
In this way, according to the present invention, raw fruit juice is subjected to both filtration using an ultrafiltration membrane and concentration, and the processed fruit juice contains wild yeast, bacteria such as bacteria, turbid substances, and polymeric polyphenols. , high-molecular pectin, glucans, oxidative browning enzymes, etc. are low or almost absent, and conversely, the concentration of nitrogen components useful for yeast growth and ash content such as potassium and magnesium is high, so it is healthy and made with high-quality pure yeast. It becomes possible to sustain vigorous fermentation.

そして、■原果汁特有の良好で爽快な果実様香気を濃厚
に有し、■窒素成分およびカリウム等呈味成分濃度が非
常に高いので、頗る味が濃厚で、即ちボディー感を有し
、■濃縮により相対的に酒石酸濃度が高いので、しっか
りとした酸味を有し、■濃縮により糖度が必要量まで上
昇可能なことから、果汁または発酵途中の醪に対し砂糖
等の補糖の必要性がなくなる。また残菌の多いせロタイ
ブの果実酒としたとき、製品果実酒の残菌組成において
は切れの悪い甘味を呈するグルコースではなくプラクド
ースが主体となり、すっきりとした甘味を呈し、モして
■貯蔵した場合に酸化劣化が極めて少なく、良好な熟成
経過をたどり、酒質が向上するなどの特徴を有し、その
結果高品質の果実酒が得られる。また、本発明は、白色
果実酒のみならず、桃色あるいは濃色(例えば赤色)果
実酒にも適用できる。
■ It has a rich and refreshing fruit-like aroma unique to original fruit juice, ■ It has a very high concentration of taste components such as nitrogen and potassium, so it has a rich flavor, that is, it has a body, ■ Due to the concentration, the tartaric acid concentration is relatively high, so it has a strong sour taste. ■Concentration allows the sugar content to rise to the required amount, so there is no need to add supplementary sugar such as sugar to the fruit juice or moromi during fermentation. It disappears. In addition, when making fruit wine from Serotib, which has a lot of residual bacteria, the residual bacteria composition of the product fruit wine mainly consists of plaquedose rather than glucose, which has a dull sweet taste, and has a refreshing sweet taste. It has characteristics such as very little oxidative deterioration, good aging process, and improved alcohol quality, resulting in high-quality fruit alcohol. Further, the present invention is applicable not only to white fruit wines but also to pink or dark colored (for example, red) fruit wines.

以下、実施例を示して、本発明を具体的に説明する。EXAMPLES Hereinafter, the present invention will be specifically explained with reference to Examples.

実施例1 昭和58年度産「甲州ブドウ」を常法により破砕、圧搾
して得られた果汁に亜硫酸およびペクチン分解酵素とし
てスクラーゼ(三共製幕社製商品名)を添加し、十分撹
拌、分散させ、5°Cで15時間静置後、滓引し、その
上澄部分をメンブランフィルタ−により・清澄濾過し、
第3表記載の如き成分分析値を有する清澄果汁を得た。
Example 1 Sulfite and sucrase (trade name, manufactured by Sankyo Seisakusha Co., Ltd.) as a pectin-degrading enzyme were added to the juice obtained by crushing and pressing Koshu grapes produced in 1982 using a conventional method, and the mixture was thoroughly stirred and dispersed. After standing at 5°C for 15 hours, the slurry was removed, and the supernatant was filtered for clarification using a membrane filter.
A clarified fruit juice having the component analysis values shown in Table 3 was obtained.

この清澄果汁を逆浸透膜による濃縮を行なって、第3表
記載の如き成分分析値を有する約1.3倍濃縮果汁を得
、次いでこの濃縮果汁を分画分子量20.000の限外
濾過膜を用いて濾過し、第3表記載の如き成分分析値を
有する濾過果汁を得た。
This clarified fruit juice was concentrated using a reverse osmosis membrane to obtain approximately 1.3 times concentrated fruit juice having the component analysis values listed in Table 3, and then this concentrated fruit juice was filtered through an ultrafiltration membrane with a molecular weight cutoff of 20.000. A filtered fruit juice having component analysis values as shown in Table 3 was obtained.

こうして得られた果汁107!にブドウ酒酵母「きよう
かい、酵母1号」(サツカロミセス・セレビシェ)口日
本醸造協会販売]の純粋培養液100、肩lを加え、1
11容密閉発酵タンクで常法によりpH3,3,20°
Cで20日間発酵させた。発酵は、極めて旺盛に、しか
も持続して行なわれることが確認された。
The fruit juice obtained in this way is 107! Add 100 liters of pure culture solution of grape wine yeast ``Kiyoukai Yeast No. 1'' (Satsucharomyces cerevisiae sold by Japan Brewing Association) and 1 liter of pure culture to
pH 3, 3, 20° by conventional method in 11 volume closed fermentation tank
Fermented at C for 20 days. It was confirmed that fermentation was carried out extremely vigorously and continuously.

発酵終了後、常法により滓引したのち、メンブランフィ
ルタ−を用いて清澄濾過し、「甲州ブドウ」の果汁特有
の良好で爽快な果実様香気を濃厚に有し、第4表ンこ記
載の如き成分分析値を有する白ワインを得た。
After completion of fermentation, the sludge is drained using a conventional method, and then clarified and filtered using a membrane filter to produce a product that has a rich, refreshing fruit-like aroma characteristic of the juice of "Koshu grapes" and is described in Table 4. A white wine having the following component analysis values was obtained.

また、こうして得られた白ワインに亜硫酸50myll
宛を添加し、720 ae壜に充填してコルク打栓した
のち、60″C達温火入を行ない、放冷後15〜20°
Cの地下セラーにて1年間貯蔵したところ、良好な熟成
経過を示した。その結果、「甲州ブドウ」品種特有の果
実様香気を濃厚に有し、しかも風味がバランス良く、調
和し、良質の白ワインが得られた。
In addition, 50 myll of sulfite was added to the white wine thus obtained.
After filling a 720 ae bottle and corking it, it was heated to 60"C and heated to 15~20° after cooling.
When stored for one year in the underground cellar of C, it showed good aging progress. As a result, a high-quality white wine was obtained that had a rich fruit-like aroma characteristic of the "Koshu grape" variety, and had well-balanced and harmonious flavors.

次に、このようにして得られた白ワインについて、11
f11酒による官能検査を実施したところ、第5表に示
す如き結果が得られた。
Next, regarding the white wine obtained in this way, 11
When a sensory test was conducted using f11 sake, the results shown in Table 5 were obtained.

尚、第4〜5表における区分の欄で、「対照」、「比較
例1」および「比較例2」は、それぞれ以下のように処
理して得られたものである。
In addition, in the classification column of Tables 4 and 5, "Control", "Comparative Example 1", and "Comparative Example 2" were obtained by the following processing, respectively.

対照:仕込清澄果汁について、逆浸透膜による濃縮と限
外濾過膜による濾過を行なわないで、砂糖による補糖(
糖度21.5%)を行なう以外は、上記と全く同様に処
理して得られた白ワイン。
Control: For the prepared clarified fruit juice, supplementation with sugar (
White wine obtained by processing exactly the same as above, except that the sugar content was 21.5%.

比較例1:仕込清澄果汁について限外濾過膜による濾過
を行なわない以外は上記と全く同様に処理して得られた
白ワイン。
Comparative Example 1: White wine obtained by processing in exactly the same manner as above except that the clarified fruit juice was not filtered using an ultrafiltration membrane.

比較例2:仕込清澄果汁について、逆浸透膜による濃縮
を行なわないで、砂糖による補糖(糖度21.5%)を
行なう以外は上記と全く同様に処理して得られた白ワイ
ン。
Comparative Example 2: White wine obtained by processing the clarified fruit juice in exactly the same manner as above except that it was not concentrated using a reverse osmosis membrane and supplemented with sugar (sugar content 21.5%).

V施 イク11   ≦こ− 上記実施例1と同様にして、甲州ブドウの清澄果汁(糖
度16.32%)を得、これを分画分子量20.000
の限外濾過膜を用いて濾過し、該濾液を凍結濃縮機を用
いて約1.3倍濃縮した。
In the same manner as in Example 1 above, clarified fruit juice of Koshu grapes (sugar content 16.32%) was obtained, and this was mixed with a molecular weight cut-off of 20.000.
The filtrate was concentrated approximately 1.3 times using a freeze concentrator.

次いで、このようにして得られた果汁10Jにブドウ酒
酵母「きようかい酵母1号」の純粋培養液LOOmlを
加え、以下、実施例1と全く同様にして、甲州ブドウ果
汁特有の良好で爽快な果実様香気を有する白ワインを得
た。
Next, to 10 J of the fruit juice obtained in this way, LOOml of a pure culture solution of grape wine yeast "Kiyoukai Yeast No. 1" was added, and the following procedure was carried out in exactly the same manner as in Example 1 to obtain the good and refreshing taste characteristic of Koshu grape juice. A white wine with fruity aroma was obtained.

Claims (3)

【特許請求の範囲】[Claims] (1)果汁を分画分子量10,000〜100,000
の限外濾過膜を用いて濾過し、その前または後に該果汁
を濃縮し、次いで前記濾過によって得られた濾過果汁を
常法によりアルコール発酵させることを特徴とする果実
酒の製造法。
(1) Fruit juice with a molecular weight cutoff of 10,000 to 100,000
A method for producing fruit wine, which comprises filtering the fruit juice using an ultrafiltration membrane, concentrating the fruit juice before or after the filtration, and then subjecting the filtered fruit juice obtained by the filtration to alcoholic fermentation by a conventional method.
(2)濃縮が1.3〜1.8倍濃縮である特許請求の範
囲第1項記載の果実酒の製造法。
(2) The method for producing fruit wine according to claim 1, wherein the concentration is 1.3 to 1.8 times.
(3)果実酒がワインである特許請求の範囲第1項また
は2項記載の果実酒の製造法。
(3) The method for producing fruit liquor according to claim 1 or 2, wherein the fruit liquor is wine.
JP61148160A 1986-06-26 1986-06-26 Preparation of fruit liquor Granted JPS637773A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP61148160A JPS637773A (en) 1986-06-26 1986-06-26 Preparation of fruit liquor

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP61148160A JPS637773A (en) 1986-06-26 1986-06-26 Preparation of fruit liquor

Publications (2)

Publication Number Publication Date
JPS637773A true JPS637773A (en) 1988-01-13
JPH051708B2 JPH051708B2 (en) 1993-01-08

Family

ID=15446598

Family Applications (1)

Application Number Title Priority Date Filing Date
JP61148160A Granted JPS637773A (en) 1986-06-26 1986-06-26 Preparation of fruit liquor

Country Status (1)

Country Link
JP (1) JPS637773A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2001245639A (en) * 2000-03-09 2001-09-11 Iwate Prefecture Method for producing apple juice
US20160205959A1 (en) * 2013-08-29 2016-07-21 Meiji Co., Ltd. Production method for concentrated product using membrane-concentration method and freeze-concentration method

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103659975B (en) * 2013-12-13 2016-01-20 广东省九江酒厂有限公司 Ageing Eaux-De-Vie lichee wood chip and Synthesis and applications technique thereof

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS50154494A (en) * 1974-05-28 1975-12-12
GB1454792A (en) * 1973-02-20 1976-11-03 Danske Sukkerfab Method of concentrating grape juice for use in the production of wines
JPS558147A (en) * 1978-07-05 1980-01-21 Toshiba Corp Automatic frequency adjuster
JPS57105180A (en) * 1980-12-22 1982-06-30 Snow Brand Milk Prod Co Ltd Preparation of wine from fruit juice concentrated with membrane
JPS6019488A (en) * 1983-07-15 1985-01-31 Ehimeken Seika Nogyo Kyodo Kumiai Rengokai Preparation of fruit liquor

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB1454792A (en) * 1973-02-20 1976-11-03 Danske Sukkerfab Method of concentrating grape juice for use in the production of wines
JPS50154494A (en) * 1974-05-28 1975-12-12
JPS558147A (en) * 1978-07-05 1980-01-21 Toshiba Corp Automatic frequency adjuster
JPS57105180A (en) * 1980-12-22 1982-06-30 Snow Brand Milk Prod Co Ltd Preparation of wine from fruit juice concentrated with membrane
JPS6019488A (en) * 1983-07-15 1985-01-31 Ehimeken Seika Nogyo Kyodo Kumiai Rengokai Preparation of fruit liquor

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2001245639A (en) * 2000-03-09 2001-09-11 Iwate Prefecture Method for producing apple juice
US20160205959A1 (en) * 2013-08-29 2016-07-21 Meiji Co., Ltd. Production method for concentrated product using membrane-concentration method and freeze-concentration method
US9913484B2 (en) * 2013-08-29 2018-03-13 Meiji Co., Ltd. Production method for concentrated product using membrane-concentration method and freeze-concentration method

Also Published As

Publication number Publication date
JPH051708B2 (en) 1993-01-08

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