JPS6343078B2 - - Google Patents

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Publication number
JPS6343078B2
JPS6343078B2 JP55181708A JP18170880A JPS6343078B2 JP S6343078 B2 JPS6343078 B2 JP S6343078B2 JP 55181708 A JP55181708 A JP 55181708A JP 18170880 A JP18170880 A JP 18170880A JP S6343078 B2 JPS6343078 B2 JP S6343078B2
Authority
JP
Japan
Prior art keywords
fruit juice
juice
grape
concentrated
sugar content
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
Application number
JP55181708A
Other languages
Japanese (ja)
Other versions
JPS57105180A (en
Inventor
Shinji Iwazawa
Kenkichi Ahiko
Toshihiko Kikuchi
Seiichiro Igarashi
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.)
Snow Brand Milk Products Co Ltd
Original Assignee
Snow Brand Milk Products Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Snow Brand Milk Products Co Ltd filed Critical Snow Brand Milk Products Co Ltd
Priority to JP55181708A priority Critical patent/JPS57105180A/en
Publication of JPS57105180A publication Critical patent/JPS57105180A/en
Publication of JPS6343078B2 publication Critical patent/JPS6343078B2/ja
Granted legal-status Critical Current

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Description

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

本発明は濃厚芳醇かつ色調の安定した高品質の
ブドウ酒の製造法に関する。 従来、ブドウ酒は、一般に、原料ブドウを除梗
後、破砕、圧搾して得られるブドウ果汁に酸化に
よる褐変防止又は有害微生物の繁殖抑制のための
メタ重亜硫酸カリウム又は異性重亜硫酸カリウム
や亜硫酸を添加したものに酒母を添加して発酵さ
せ、その後滓引き、過等を行い、ついで熟成さ
せることにより製造されている。 而してブドウ酒の製造上最も重要な事項な原料
としてのブドウの品質であつて、その糖度芳香及
び風味によりブドウ酒の品質が大きく影響され
る。 現在、吾国で栽培されているブドウから得られ
る果汁はブドウ酒原料としては糖度が低すぎるた
め、通常その発酵前又は発酵中に砂糖、グルコー
スのごとき糖分の添加による補糖が一般的に行な
われている。しかし、このように補糖したブドウ
果汁を原料として用いて製造したブドウ酒は濃厚
な芳醇性に欠け、風味も乏しいため、補糖したブ
ドウ果汁から高品質のブドウ酒を得るのは極めて
困難である。 因みに、吾国で栽培されているブドウ酒用原料
ブドウ、例えば甲州種、デラウエア種、マスカツ
ト・ベリーA種等は、欧州諸国の原料ブドウであ
るセミーヨン種(Semillon),シヤルドネー種,
リースリング種,カベルネ・ソービニヨン種等に
比較して芳香,風味ともに平坦かつ微弱であるこ
とも吾国における高品質なブドウ酒製造上の大き
な障害となつている。 近年、上述したごとき吾国における原料ブドウ
果汁の糖度の不足にかんがみ、ブドウ果汁を濃縮
処理することによりその糖度を高め、併せて芳
香,風味を増強する方法が考えられ、その濃縮手
段として凍結濃縮法ならびに逆浸透膜濃縮法等が
提案されている。 しかしながら、これらの濃縮手段のうち凍結濃
縮法は濃縮効率が悪く、加えて凍結のためのエネ
ルギーコストが高いなどの欠点がみられ、一方、
逆浸透膜濃縮法はエネルギーコストが低い利点が
あるも下記のような重要な欠点がみられる。 第一にブドウ酒にとつて最も重要な芳香、特に
アロマと呼ばれるブドウ由来の香りが変化した
り、時には低減するため、通常の逆浸透膜濃縮法
では香りの芳醇なブドウ洒を製造し得ない。第二
に濃縮時の果汁循環によるブドウ果汁の撹拌作用
が果汁の酸化,褐変現象を促進するため果汁のフ
レツシユネスが失われることになる。そのため、
このような果汁から製造されるブドウ酒には好ま
しくない酸化臭や着色がみられ、フレツシユネス
の乏しいブドウ果汁となる。 上述したように通常の逆浸透膜濃縮法による果
汁の濃縮はブドウ洒の製造上好ましくない影響を
与えるために原料ブドウ果汁を単に逆浸透膜を用
いて濃縮しただけでは高品質のブドウ洒を製造す
ることはできない。 本発明者らは、このような現状にかんがみ、原
料ブドウ果汁の変質を伴うことなく、その糖度を
増加させると共に芳香及び風味を増強し、よつて
濃厚芳醇な高品質のブドウ洒を製造し得る方法に
ついて検討した結果、食塩排除率の異なる2種類
の逆浸透膜を用いて原料ブドウ果汁をそれぞれ濃
縮して得られる2種の果汁を一定割合でブレンド
したものを原料果汁として用いることにより上記
高品質のブドウ酒が製造し得ることを見出し、本
発明をなすに至つた。 以下本発明を詳しく説明する。 本発明の特徴は、ブドウ果汁を酒母を添加し発
酵させてブドウ酒を製造するに際し、ブドウ果汁
を食塩排除率70〜95%を示す逆浸透膜と食塩排除
率96〜99%を示す逆浸透膜とを用いてそれぞれ濃
縮して糖度24〜35%(果汁A)及び20〜25%(果
汁B)を有する2種の果汁を調製し、この両者の
果汁を上記果汁Aに対して上記果汁Bを少くとも
10%容量ブレンドし、このようにして得られるブ
レンド果汁を原料として用いてブドウ酒を製造す
ることにある。 本発明で用いられる原料ブドウは通常ブドウ酒
の製造に用いられているものならいずれでもよ
く、完熟した糖度の高いブドウであれば果汁の濃
縮処理も短時間で済み好ましいが、糖度の低い未
熟ブドウ又は天候不順による不作年のブドウであ
つても一向に差支えがない。 原料ブドウからの果汁の調製は常法により原料
ブドウを除梗後、破砕,圧搾して得た果汁にメタ
重亜硫酸カリウム(又は異性重亜硫酸カリウムや
亜硫酸を添加した後、不溶物を除去し、清澄果汁
を得る。この果汁の清澄化は、沈降法とケイソウ
士,アスベストのごとき過助剤を用いる加圧
過法を併用する方法や遠心分離法を用いて実施さ
れるが、膜濃縮の際膜の目詰りを防止するととも
に濃縮効率をよくするために行うものである。 次に、このようにして調製した清澄果汁を二つ
の区分に分け、一方の果汁を食塩排除率70〜95%
を示す逆浸透膜を用いて糖度が24〜35%になるご
とく濃縮し、他方の果汁を食塩排除率96〜99%を
示す逆浸透膜を用いて糖度が20〜25%になるごと
く濃縮する。 ここでいう“食塩排除率”とは0.5%濃度の食
塩水を25℃において42Kg/cm2の加圧条件下で膜処
理した場合加圧してから30分経過後の膜透過液に
ついて測定される食塩量から算出される。すなわ
ち、膜透過液中の食塩量が低い程食塩排除率が高
いことになる。 本発明において上述のごとく食塩排除率の異な
る2種類の膜を用いて2種の濃縮果汁を調製し、
これらをブレンドしたものを原料果汁として用い
るのは下記理由に因る。 まず、原料果汁を食塩排除率70〜95%の逆浸透
膜を用いて濃縮して得られる糖度24〜35%の濃縮
果汁Aの調製はブドウ酒のアルコール濃度に見合
う十分な糖度を有する果汁にすること及び得られ
るブドウ酒の風味を濃厚にすることが目的であつ
て、この濃縮果汁の調製に際し食塩排除率70%未
満の膜を用いると酸,灰分,遊離アミノ酸のごと
き風味に大きな影響を及ぼす成分の含量が殆んど
増加しないことになり、一方食塩排除率を95%よ
り高くすると上記所望の糖度が短時間で得られな
くなる。 しかし、上記濃縮果汁Aのみでは芳香性に乏し
いので、別に食塩排除率96〜99%を示す膜を用い
て糖度20〜25%の濃縮果汁Bを調製する。すなわ
ち、食塩排除率96〜99%の膜を用いてブドウ果汁
を濃縮することにより果汁の芳香は保持され、か
つ濃縮にともない特に芳香のみならず風味も増強
された果汁Bが得られるようになる。しかし、こ
の果汁Bを得るには膜の食塩排除率が極めて高い
ためその糖度を25%以上に高めるには長時間を要
し、したがつて、該果汁のみを用いてブドウ酒を
製造することは得策でない。 したがつて、本発明では糖度の高い果汁Aに芳
香の高い果汁Bを10容量%以上ブレンドすること
によつて高品質のブドウ酒の製造に適した果汁を
調製するのである。 次に、ブドウ果汁の濃縮に用いる膜の食塩排除
率とそれにより濃縮した果汁を用いて製造したブ
ドウ酒の品質との関係を試験した結果を下記に示
す。 試験方法: 甲州種ブドウから果汁(糖度15.2%)500を
採取し、これにメタ重亜硫酸カリウム(又は異性
重亜硫酸カリウム50gを添加後、15時間放置して
不溶物を沈降させ、次いで上清果汁のみをアスベ
ストを過助剤として用いて過し、完全に透明
な清澄果汁450を得た。 次に、同一メーカーによる食塩排除率の異なる
逆浸透膜5種を用いて上記清澄果汁25づつを糖
度25.0%になるまでそれぞれ濃縮し、得られた5
種の濃縮果汁15づつを20用ビンに収容した。
なお、使用膜は何れも0.74m2の膜面積を有し、濃
縮条件は膜の出口圧力50〜60Kg/cm2、果汁温度12
℃、流量350〜400/時間で行い、果汁タンク内
はN2:CO2=1:1の混合ガスの雰囲気に保持
した。濃縮処理時間は使用膜の食塩排除率50,
70,90,95ならびに98%に応じてそれぞれ120分,
120分,150分,170分ならびに180分を要した。 上述のようにして得られた各濃縮果汁にブドウ
酒酵母(Saccharomyces cerevisiaeの菌株)の
ブドウ果汁培養液500mlづつを添加し、15℃で20
日間発酵させた。発酵終了後各発酵液に3gづつ
のメタ重亜硫酸カリウム(又は異性重亜硫酸カリ
ウム)を添加した後、常法に従つて滓引き,過
を行つて6ケ月間熟成させて新酒とした。得られ
た各新酒について分析及び官能評価した結果を下
記表1及び表2に示す。 なお、官能評価はパネラー15人により国際ブド
ウ酒品評会品質判定法に準拠して行い、色調0〜
2点,清澄度0〜2点,芳香0〜4点、風味及び
総合判定0〜12点の20点満点で評価し、その平均
値で表示した。
The present invention relates to a method for producing high-quality grape wine that is rich, mellow, and has a stable color tone. Traditionally, grape wine is generally made by adding potassium metabisulfite, isomeric potassium bisulfite, or sulfurous acid to the grape juice obtained by destemming raw material grapes, crushing them, and pressing them to prevent browning due to oxidation or suppress the growth of harmful microorganisms. It is produced by adding sake mash to the fermented product, fermenting it, then slaging and sieving it, and then aging it. The quality of grapes as a raw material is the most important factor in the production of wine, and the quality of the wine is greatly influenced by its sugar content, aroma and flavor. Currently, the fruit juice obtained from grapes grown in our country has too low a sugar content to be used as a raw material for wine, so supplementation by adding sugars such as sugar or glucose is generally performed before or during fermentation. It is. However, grape wine produced using sugar-enriched grape juice as a raw material lacks rich aroma and flavor, making it extremely difficult to obtain high-quality wine from sugar-enriched grape juice. be. Incidentally, the raw material grapes for wine grown in our country, such as Koshu, Delaware, and Muscat Berry A, are similar to the raw material grapes of European countries such as Semillon, Chardonnay,
Compared to Riesling, Cabernet Sauvignon, etc., grapes have a flat and weak aroma and flavor, which is also a major obstacle in producing high-quality wine in our country. In recent years, in view of the lack of sugar content in the raw material grape juice in our country as mentioned above, a method has been considered to increase the sugar content by concentrating grape juice and enhance its aroma and flavor. Freeze concentration is a method for concentrating grape juice. methods and reverse osmosis membrane concentration methods have been proposed. However, among these concentration methods, the freeze concentration method has disadvantages such as poor concentration efficiency and high energy cost for freezing.
Although the reverse osmosis membrane concentration method has the advantage of low energy costs, it has the following important drawbacks. Firstly, the most important aroma for grape wine, especially the aroma derived from grapes, changes or sometimes decreases, making it impossible to produce grapes with a rich aroma using the normal reverse osmosis membrane concentration method. . Second, the stirring action of the grape juice caused by the juice circulation during concentration promotes oxidation and browning of the fruit juice, resulting in a loss of freshness of the fruit juice. Therefore,
Grape wine produced from such fruit juice has undesirable oxidation odor and coloration, resulting in grape juice with poor freshness. As mentioned above, concentrating fruit juice using the normal reverse osmosis membrane concentration method has an unfavorable effect on the production of grape bottlings, so it is difficult to produce high-quality grape bottlings simply by concentrating raw grape juice using a reverse osmosis membrane. I can't. In view of the current situation, the present inventors have made it possible to increase the sugar content and enhance the aroma and flavor of raw grape juice without deteriorating its quality, thereby producing rich and mellow high-quality grape juice. As a result of considering the method, it was found that the above-mentioned high level can be achieved by using a blend of two types of fruit juice obtained by concentrating raw grape juice using two types of reverse osmosis membranes with different salt rejection rates at a constant ratio as raw fruit juice. The inventors discovered that it is possible to produce high-quality grape wine, leading to the present invention. The present invention will be explained in detail below. The features of the present invention include a reverse osmosis membrane that has a salt removal rate of 70 to 95% and a reverse osmosis membrane that has a salt removal rate of 96 to 99% when producing grape wine by fermenting grape juice with a yeast mother. Two kinds of fruit juices having a sugar content of 24 to 35% (fruit juice A) and 20 to 25% (fruit juice B) are prepared by concentrating them using a membrane, respectively, and these two fruit juices are added to the above fruit juice to the above fruit juice A. B at least
The purpose is to produce grape wine by blending 10% volume and using the blended juice obtained in this way as a raw material. The raw material grapes used in the present invention may be any grapes that are normally used in the production of wine; fully ripe grapes with a high sugar content are preferable because the juice can be concentrated in a short time, but unripe grapes with a low sugar content Or, there is no problem even if the grapes are from a bad year due to unseasonable weather. The preparation of fruit juice from the raw material grapes is done by destemming the raw material grapes using a conventional method, then crushing and pressing the resulting fruit juice, adding potassium metabisulfite (or isomeric potassium bisulfite or sulfurous acid), removing insoluble matter, and clarification. Obtain fruit juice. Clarification of this fruit juice is carried out using a combination of sedimentation method and pressurized filtration method using super-aids such as diatomizers and asbestos, or centrifugation method. This is done to prevent clogging and improve concentration efficiency.Next, the clarified juice prepared in this way is divided into two sections, and one of the juices is divided into two sections with a salt rejection rate of 70 to 95%.
Concentrate the fruit juice to a sugar content of 24-35% using a reverse osmosis membrane with a salt removal rate of 96-99%. . The "salt rejection rate" here refers to the membrane permeate that is measured 30 minutes after pressurization when 0.5% salt solution is subjected to membrane treatment at 25°C and under a pressure of 42 kg/ cm2 . Calculated from the amount of salt. In other words, the lower the amount of salt in the membrane permeate, the higher the salt rejection rate. In the present invention, two types of concentrated fruit juices are prepared using two types of membranes with different salt rejection rates as described above,
The reason why a blend of these is used as raw fruit juice is as follows. First, concentrated fruit juice A with a sugar content of 24-35%, which is obtained by concentrating raw fruit juice using a reverse osmosis membrane with a salt rejection rate of 70-95%, is a fruit juice with a sugar content sufficient to match the alcohol concentration of grape wine. The purpose is to enrich the flavor of the resulting grape wine, and if a membrane with a salt rejection rate of less than 70% is used in the preparation of concentrated fruit juice, acids, ash, and free amino acids may have a large effect on the flavor. On the other hand, if the salt exclusion rate is higher than 95%, the desired sugar content cannot be obtained in a short time. However, since concentrated fruit juice A alone lacks aroma, concentrated fruit juice B with a sugar content of 20 to 25% is prepared separately using a membrane that exhibits a salt rejection rate of 96 to 99%. That is, by concentrating grape juice using a membrane with a salt rejection rate of 96 to 99%, the aroma of the fruit juice is retained, and as a result of the concentration, it becomes possible to obtain fruit juice B that has particularly enhanced not only the aroma but also the flavor. . However, in order to obtain this fruit juice B, it takes a long time to raise the sugar content to 25% or more because the salt rejection rate of the membrane is extremely high.Therefore, it is difficult to produce grape wine using only this fruit juice. is not a good idea. Therefore, in the present invention, fruit juice suitable for producing high-quality grape wine is prepared by blending fruit juice A with a high sugar content with fruit juice B with a high aroma at 10% by volume or more. Next, the results of testing the relationship between the salt rejection rate of the membrane used for concentrating grape juice and the quality of wine produced using the concentrated fruit juice are shown below. Test method: Take 500 g of fruit juice (sugar content 15.2%) from Koshu grapes, add potassium metabisulfite (or 50 g of isomeric potassium bisulfite), leave for 15 hours to precipitate insoluble matter, and then extract the supernatant juice. The clarified fruit juice was filtered using asbestos as a super-aiding agent to obtain 450 ml of completely transparent clarified fruit juice.Next, 25 of the clarified fruit juices were filtered to reduce the sugar content using 5 types of reverse osmosis membranes with different salt rejection rates made by the same manufacturer. Each was concentrated to 25.0%, and the obtained 5
15 portions of concentrated seed juice were placed in 20-sized bottles.
The membranes used each have a membrane area of 0.74 m 2 , and the concentration conditions are a membrane outlet pressure of 50 to 60 Kg/cm 2 and a fruit juice temperature of 12
The test was carried out at a flow rate of 350 to 400/hour at a temperature of 350 to 400 °C, and the inside of the fruit juice tank was maintained in a mixed gas atmosphere of N 2 :CO 2 =1:1. The concentration processing time is based on the salt rejection rate of the membrane used: 50,
120 minutes each according to 70, 90, 95 and 98%,
It took 120, 150, 170 and 180 minutes. 500 ml of grape juice culture of grape wine yeast (strain of Saccharomyces cerevisiae) was added to each concentrated fruit juice obtained as described above, and the mixture was incubated at 15°C for 20
Fermented for a day. After the completion of fermentation, 3 g of potassium metabisulfite (or isomeric potassium bisulfite) was added to each fermented liquor, followed by sloughing and straining according to conventional methods, and aging for 6 months to produce new sake. The results of analysis and sensory evaluation of each new sake obtained are shown in Tables 1 and 2 below. The sensory evaluation was conducted by 15 panelists in accordance with the Quality Judgment Method of the International Grape and Liquor Fair, and the color tone was 0 to 0.
2 points for clarity, 0 to 2 points for aroma, 0 to 4 points for aroma, and 0 to 12 points for flavor and overall evaluation, and the average value was expressed.

【表】 ** 酒石酸の酸度として表示
*** アミノ酸自動分析計で測定
[Table] ** Displayed as acidity of tartaric acid
*** Measured with an automatic amino acid analyzer

【表】 上記表1及び表2にみられるごとく、食塩排除
率70%未満の膜で濃縮した果汁から製造したブド
ウ酒は芳香及び風味が劣る。一方食塩排除率が96
%以上の膜で濃縮した果汁からのものが著しく芳
香が優れている。 次に、甲州ブドウ果汁を用い、食塩排除率92%
の膜で濃縮した果汁Aに対して同じ果汁を食塩排
除率98%の膜を用いて濃縮した果汁Bを種々の容
量%でブレンドした果汁を用いて前述のごとくし
てブドウ酒を製造しその品質を評価した結果を表
3に示す。
[Table] As shown in Tables 1 and 2 above, wine produced from fruit juice concentrated with a membrane with a salt rejection rate of less than 70% has poor aroma and flavor. On the other hand, the salt exclusion rate is 96
% or more of fruit juice concentrated with a membrane has a significantly superior aroma. Next, using Koshu grape juice, the salt elimination rate is 92%.
Grape wine was produced as described above by blending fruit juice A concentrated using a membrane with various volume percentages of fruit juice B concentrated using a membrane with a salt rejection rate of 98%. Table 3 shows the results of quality evaluation.

【表】 上記表3にみられるごとく、果汁Aに果汁Bを
10容量%以上ブレンドした果汁を用いて製造した
ブドウ酒は芳香及び風味の点で優れている。 本発明では上記膜による果汁の濃縮を不活性ガ
ス、例えば窒素ガス又は炭酸ガスもしくは両者の
混合ガスの雰囲気下で、かつ7〜15℃の温度下で
行うことが好ましい。これは空気との接触による
果汁の酸化を極力防止すること及び濃縮処理中高
圧下での繰返し循環による果汁温度の上昇に伴う
果汁劣化を防止することにある。特に、逆浸透膜
による濃縮法では果汁を高圧で循環させるため常
圧に防出される出口では剪断力が働いて空気の巻
き込みが大きくなつて酸化褐変の原因となる。ま
た、果汁の膜濃縮における温度は7〜15℃の範囲
が最適であつて、上記温度が7℃より低くなると
濃縮にともなつて果汁中の酒石酸カリウムの結晶
が多量析出してくるようになつて逆浸透膜の目詰
りを起して濃縮効率を低下させる原因となり、一
方15℃より高くなると果汁の褐変を起すおそれが
あり、延いてはブドウ酒の色調を劣化させること
にもなる。 本発明で使用する逆浸透膜は上述したごとき食
塩排除率を示すものであれば特に制限されること
がなく、一般の市販品を適用し得る。 上述のごとくして膜濃縮して得られる果汁Aと
果汁Bとのブレンド果汁からブドウ酒を製造する
には常法にしたがつて、ブドウ酒酵母を加えて発
酵させ、発酵終了後滓引き、過を行つて熟成さ
せて行う。 なお、上記果汁の発酵に際して果汁にブドウ果
皮や種子(すなわち原料ブドウの圧搾粕)を添加
後上記酵母を加えて発酵させることもできる。 以上のように、本発明によると糖度の比較的低
いブドウを原料として用いた場合でも香り及び風
味の極めて良好な高品質ブドウ酒を製造しうる顕
著な利点がみられる。 以下に実施例を例示する。 実施例 1 甲州種ブドウから常法により彩取した果汁(糖
度15.8%)170にメタ重亜硫酸(又は異性重亜
硫酸カリウム)を25gを添加後、該果汁をアスベ
ストを用いて加圧過し、150の清澄果汁を得
た。 このうち120の清澄果汁を食塩排除率92%を
示す逆浸透膜を用いて濃縮し、糖度26.0%の果汁
A65を得た。このときの濃縮条件は、膜面積
3.2m2、出口圧力50〜60Kg/cm2、流量600/時
間、果汁温度12℃であつて、濃縮に240分を要し
た。 なお、果汁タンク内はN2:CO2=1:1の混
合ガスで置換して不活性雰囲気にした。 一方、残部の清澄果汁30を食塩排除率98%を
示す逆浸透膜を用いて110分間濃縮して糖度22.0
%の果汁B21を得た。このときの濃縮条件は膜
面積1.6m2の膜を使用した以外は上記と同様であ
る。 上述のようにして得られた果汁A25に果汁
B5をブレンドした果汁を用い常法に従つて発
酵,熟成させ、6ケ月経過後得られたブドウ酒の
官能評価を15人のパネラーにより国際ブドウ酒品
評会品質判定法に準拠して行つた。その結果を表
4に示す。 なお、比較として果汁A30のみを用いて上記
と同様にして発酵,熟成させ、6ケ月経過後得ら
れたブドウ酒についても同様に官能評価を行つた
結果も併せて表4に示す。 評価は色調0〜2点,清澄度0〜2点,芳香0
〜4点及び風味0〜12点の総合点20満点で行い、
平均値で表示した。
[Table] As shown in Table 3 above, add fruit juice B to fruit juice A.
Grape wine produced using blended fruit juice of 10% or more by volume has excellent aroma and flavor. In the present invention, it is preferable to concentrate the fruit juice using the membrane in an atmosphere of an inert gas, such as nitrogen gas, carbon dioxide gas, or a mixture of both, and at a temperature of 7 to 15°C. The purpose of this is to prevent as much as possible the oxidation of the fruit juice due to contact with air, and to prevent the fruit juice from deteriorating due to the increase in the temperature of the fruit juice due to repeated circulation under high pressure during the concentration process. In particular, in the concentration method using a reverse osmosis membrane, the fruit juice is circulated at high pressure, so shearing force acts at the outlet, which is kept at normal pressure, and air entrainment increases, causing oxidative browning. Furthermore, the optimal temperature for membrane concentration of fruit juice is in the range of 7 to 15°C; if the above temperature is lower than 7°C, a large amount of potassium tartrate crystals in the fruit juice will precipitate during concentration. This can clog the reverse osmosis membrane and reduce concentration efficiency, while if the temperature is higher than 15°C, there is a risk of browning of the fruit juice, which in turn will deteriorate the color tone of the wine. The reverse osmosis membrane used in the present invention is not particularly limited as long as it exhibits the above-mentioned salt rejection rate, and any commercially available membrane may be used. To produce grape wine from the blended juice of fruit juice A and fruit juice B obtained by membrane concentration as described above, according to the conventional method, wine yeast is added and fermented, and after fermentation is completed, the slag is removed, It is done by going through a period of time to mature. In addition, upon fermentation of the fruit juice, grape skins and seeds (namely, pressed lees of raw material grapes) can be added to the fruit juice, and then the yeast can be added and fermented. As described above, the present invention has the remarkable advantage that even when grapes with relatively low sugar content are used as raw materials, high-quality wine with extremely good aroma and flavor can be produced. Examples are illustrated below. Example 1 After adding 25g of metabisulfite (or isomeric potassium bisulfite) to 170% fruit juice (sugar content 15.8%) colored by a conventional method from Koshu grapes, the juice was pressure-filtered using asbestos to obtain 150% A clear fruit juice was obtained. Of these, 120 clarified fruit juices are concentrated using a reverse osmosis membrane that has a salt removal rate of 92%, resulting in a fruit juice with a sugar content of 26.0%.
Got A65. The concentration conditions at this time are membrane area
3.2 m 2 , outlet pressure 50-60 Kg/cm 2 , flow rate 600/hour, juice temperature 12°C, and 240 minutes were required for concentration. Note that the inside of the fruit juice tank was replaced with a mixed gas of N 2 :CO 2 =1:1 to create an inert atmosphere. On the other hand, the remaining clarified fruit juice 30% was concentrated for 110 minutes using a reverse osmosis membrane with a salt rejection rate of 98%, resulting in a sugar content of 22.0.
% fruit juice B21 was obtained. The concentration conditions at this time were the same as above except that a membrane with a membrane area of 1.6 m 2 was used. Add fruit juice to fruit juice A25 obtained as described above.
The fruit juice blended with B5 was fermented and aged according to conventional methods, and after 6 months, the sensory evaluation of the resulting grape wine was conducted by a panel of 15 people in accordance with the Quality Judgment Method of the International Grape Liquor Competition. The results are shown in Table 4. For comparison, the results of a similar sensory evaluation of the grape wine obtained after 6 months of fermentation and aging using only fruit juice A30 in the same manner as above are also shown in Table 4. Evaluation: color tone 0-2 points, clarity 0-2 points, aroma 0 points
-4 points and flavor 0-12 points, total score out of 20,
Expressed as an average value.

【表】 実施例 2 甲州種ブドウから採取した果汁(糖度16.0%)
2100を採取し、これにメタ重亜硫酸カリウム
(又は異性重亜硫酸カリウム)200gを添加し、15
時間放置した。得られる上澄果汁を遠心分離機に
通して不溶物を連続的に除去し清澄果汁2000を
得た。このうち1500を食塩排除率92%を示す逆
浸透膜を用いて糖度26.0%まで濃縮して900の
果汁Aを得た。このときの濃縮条件は膜面積10.0
m2,出口圧力60Kg/cm2,流量700/時間、果汁
温度12℃であり、果汁は500づつ分けて3回濃
縮した。この濃縮に要した時間は合計で約6時間
であつた。 一方、残部の清澄果汁500を食塩排除率98%
を示す逆浸透膜を用いて糖度22%まで濃縮して
380の果汁Bを得た。この濃縮に150分要した。
また、このときの濃縮条件は上記と同様である。 なお、上記両方の濃縮に際して果汁タンク内は
N2:CO2=1:1の混合ガスで置換して不活性
雰囲気に保持した。 このようにして得られた果汁B380を上記果
汁B900にブレンドし、これにブドウ酒酵母で
あるSaccharomyces cerevisiaeの菌株の果汁培
養液20を添加し、150℃で20日間発酵させた。 発酵終了後は常法に従つて処理し、6ケ月間熟
成後得られる新酒の分析と官能評価(実施例1に
準じて)を行つた。その結果を表5及び表6に示
す。 なお、比較として上記と同一ブドウから採取し
た清澄果汁に砂糖を添加してその糖度が26.0%に
なるごとく補糖した果汁1280を同様にして発酵
させ、ついで6ケ月間熟成させて得られる新酒に
ついても同様に分析と官能評価を行つた結果を併
せて表5及び表6に示す。
[Table] Example 2 Juice collected from Koshu grapes (sugar content 16.0%)
2100 was collected, 200g of potassium metabisulfite (or isomeric potassium bisulfite) was added to it, and 15
I left it for a while. The obtained supernatant juice was passed through a centrifuge to continuously remove insoluble matter to obtain clarified fruit juice 2000. Of these, 1500 was concentrated to a sugar content of 26.0% using a reverse osmosis membrane with a salt removal rate of 92% to obtain 900 fruit juice A. The concentration conditions at this time are membrane area 10.0
m 2 , outlet pressure 60 Kg/cm 2 , flow rate 700/hour, and juice temperature 12° C. The juice was divided into 500 portions and concentrated three times. The total time required for this concentration was about 6 hours. On the other hand, the salt removal rate for the remaining clarified fruit juice 500% is 98%.
The sugar content is concentrated to 22% using a reverse osmosis membrane that shows
380 fruit juice B was obtained. This concentration required 150 minutes.
Further, the concentration conditions at this time are the same as above. In addition, when concentrating both of the above, the inside of the fruit juice tank is
The atmosphere was replaced with a mixed gas of N 2 :CO 2 =1:1 to maintain an inert atmosphere. The fruit juice B380 thus obtained was blended with the above-mentioned fruit juice B900, 20 pieces of fruit juice culture of a strain of Saccharomyces cerevisiae, which is a wine yeast, was added thereto and fermented at 150°C for 20 days. After completion of fermentation, processing was carried out according to conventional methods, and the new sake obtained after aging for 6 months was analyzed and sensory evaluated (according to Example 1). The results are shown in Tables 5 and 6. For comparison, the new sake obtained by fermenting fruit juice 1280, which was obtained by adding sugar to the clarified fruit juice taken from the same grapes as above to bring the sugar content to 26.0%, was fermented in the same way, and then aged for 6 months. Similarly, the results of analysis and sensory evaluation are also shown in Tables 5 and 6.

【表】【table】

【表】 実施例 3 セミーヨン種ブドウから採取した果汁(糖度
15.8%)100を遠心分離機を用い清澄果汁とし、
このうち70を食塩排除率90%の逆浸透膜で、ま
た20を食塩排除率98%のもので、それぞれ糖度
26.0%(取得果汁量42),21.0%(取得果汁量
15)に濃縮した。得られた2種類の果汁を混合
し、ブドウ酒酵母(Saccharomyces cerevisiae
の菌株)を添加後20℃で14日間発酵させた。 発酵終了後、常法どおり処理し熟成6ケ月後の
ブドウ酒を評価した結果、香りが非常に高く、ボ
デイーもしつかりした濃厚芳醇なブドウ酒が製造
できた。 実施例 4 マスカツト・ベリーA種ブドウ(糖度16.0%)
100Kgを除梗後、破砕,圧搾し果汁65を採取し、
これを遠心分離機を用い清澄果汁とした。このう
ち45を食塩排除率90%、20を食塩排除率98%
の逆浸透膜でそれぞれ糖度25.0%及び22.0%に濃
縮した。このときの果汁量は、それぞれ27及び
13であつた。 次に、これら2種類を混合した果汁に圧搾時に
廃出された圧搾粕を添加、さらにブドウ酒酵母
(Saccharomyces cerevisiaeの菌株)の果汁培養
液1を加え、25℃にて発酵させた。2日後圧搾
し果汁のみとし、さらに25℃にて14日間発酵させ
た。 発酵終了後、常法どおり処理し、熟成6ケ月後
のブドウ酒を評価した結果、芳香が非常に豊か
で、酸味、渋味もバランスよくかつ濃厚で、非常
にすぐれたブドウ酒を製造することができた。
[Table] Example 3 Juice collected from Semillon grapes (sugar content
15.8%) 100 is made into clarified fruit juice using a centrifuge,
Of these, 70 are reverse osmosis membranes with a salt rejection rate of 90%, and 20 are with a salt rejection rate of 98%, each with a sugar content.
26.0% (obtained fruit juice amount 42), 21.0% (obtained fruit juice amount
15). The two types of fruit juices obtained were mixed and mixed with grape wine yeast (Saccharomyces cerevisiae).
strain) was added and fermented at 20°C for 14 days. After fermentation, the grapes were treated in the usual way and after 6 months of aging, the grapes were evaluated. As a result, a rich and mellow wine with a very strong aroma and firm body was produced. Example 4 Muscat berry type A grape (sugar content 16.0%)
After destemming 100kg, crush and press to collect 65% of juice.
This was made into clarified fruit juice using a centrifuge. Of these, 45 have a salt rejection rate of 90%, and 20 have a salt rejection rate of 98%.
The sugar content was concentrated using a reverse osmosis membrane to 25.0% and 22.0%, respectively. The amount of juice at this time is 27 and 27, respectively.
It was 13. Next, pressed lees discarded during pressing was added to the mixed fruit juice of these two types, and fruit juice culture solution 1 of grape wine yeast (a strain of Saccharomyces cerevisiae) was added, followed by fermentation at 25°C. Two days later, the juice was pressed and fermented at 25°C for another 14 days. After fermentation, the grapes were processed in the usual manner and evaluated after 6 months of aging. The results showed that the grapes were very aromatic and had a rich and well-balanced acidity and astringency, producing an excellent wine. was completed.

Claims (1)

【特許請求の範囲】 1 ブドウ果汁を食塩排除率70〜95%を示す逆浸
透膜を用いて濃縮して糖度24〜35%を有する濃縮
果汁Aを調製し、一方ブドウ果汁を食塩排除率96
〜99%を示す逆浸透膜を用いて濃縮して糖度20〜
25%を有する濃縮果汁Bを調製し、上記濃縮果汁
Aに上記濃縮果汁Bを少くとも10%容量ブレンド
し、ついで得られるブレンド濃縮果汁を常法によ
り発酵処理することを特徴とするブドウ酒の製造
法。 2 濃縮果汁の調製を不活性ガスの雰囲気下で行
うことを特徴とする特許請求の範囲第1項に記載
のブドウ酒の製造法。 3 ブドウ果汁の逆浸透膜による濃縮を、果汁の
温度を7〜15℃の範囲に維持して行なうことを特
徴とする特許請求の範囲第1項又は第2項に記載
のブドウ酒の製造法。
[Scope of Claims] 1 Grape juice is concentrated using a reverse osmosis membrane that exhibits a salt rejection rate of 70 to 95% to prepare concentrated fruit juice A having a sugar content of 24 to 35%, while grape juice has a salt rejection rate of 96%.
Concentrated using reverse osmosis membrane showing ~99% sugar content ~20~
25% concentrated fruit juice B is prepared, the concentrated fruit juice B is blended with the concentrated fruit juice A at least 10% by volume, and the resulting blended concentrated fruit juice is then fermented by a conventional method. Manufacturing method. 2. The method for producing grape wine according to claim 1, wherein the concentrated fruit juice is prepared in an inert gas atmosphere. 3. The method for producing grape wine according to claim 1 or 2, characterized in that the concentration of grape juice using a reverse osmosis membrane is carried out while maintaining the temperature of the fruit juice in the range of 7 to 15°C. .
JP55181708A 1980-12-22 1980-12-22 Preparation of wine from fruit juice concentrated with membrane Granted JPS57105180A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP55181708A JPS57105180A (en) 1980-12-22 1980-12-22 Preparation of wine from fruit juice concentrated with membrane

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP55181708A JPS57105180A (en) 1980-12-22 1980-12-22 Preparation of wine from fruit juice concentrated with membrane

Publications (2)

Publication Number Publication Date
JPS57105180A JPS57105180A (en) 1982-06-30
JPS6343078B2 true JPS6343078B2 (en) 1988-08-26

Family

ID=16105463

Family Applications (1)

Application Number Title Priority Date Filing Date
JP55181708A Granted JPS57105180A (en) 1980-12-22 1980-12-22 Preparation of wine from fruit juice concentrated with membrane

Country Status (1)

Country Link
JP (1) JPS57105180A (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS596879A (en) * 1982-07-05 1984-01-13 Sapporo Breweries Ltd Preparation of fruit wine
JPS637773A (en) * 1986-06-26 1988-01-13 Kikkoman Corp Preparation of fruit liquor

Also Published As

Publication number Publication date
JPS57105180A (en) 1982-06-30

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