JP2006174760A - Concentrated fruit liquor and method for producing the same - Google Patents

Concentrated fruit liquor and method for producing the same Download PDF

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JP2006174760A
JP2006174760A JP2004371404A JP2004371404A JP2006174760A JP 2006174760 A JP2006174760 A JP 2006174760A JP 2004371404 A JP2004371404 A JP 2004371404A JP 2004371404 A JP2004371404 A JP 2004371404A JP 2006174760 A JP2006174760 A JP 2006174760A
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wine
concentrated
fruit
fruit liquor
concentration
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Masaaki Nagao
公明 長尾
Takashi Usami
孝 宇佐美
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Manns Wine Co Ltd
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Manns Wine Co Ltd
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Abstract

<P>PROBLEM TO BE SOLVED: To provide a concentrated fruit liquor suitable for drinking or cooking and a method for producing the liquor. <P>SOLUTION: The invention provides (1) a concentrated fruit liquor having an alcohol content of 1.5-3.0% and an extract content of ≥10% and produced by concentrating a raw fruit liquor 2-5 times by vacuum concentration, (2) a concentrated fruit liquor having an alcohol content of 1.5-3.0% and an extract content of ≥10% and produced by concentrating a raw fruit liquor at 40-55°C by vacuum concentration and (3) a concentrated fruit liquor having an alcohol content of 1.5-3.0% and an extract content of 2-5 times the extract content of the raw fruit liquor and produced by concentrating a raw fruit liquor at 40-55°C by vacuum concentration. <P>COPYRIGHT: (C)2006,JPO&NCIPI

Description

本発明は、濃縮果実酒およびその製造法に関する。   The present invention relates to a concentrated fruit liquor and a method for producing the same.

果実酒は、果実を原料として醸造したアルコール飲料であり、飲用、調理用として広く利用されている。代表的な果実酒は、ブドウ、ナシ、ビワ、リンゴ、マルメロ、アンズ等の果実を醸造して得られるワイン、シードル等である。
飲用としての果実酒は、市場の要求により、種々の濃度のアルコール度数あるいはエキス分の製品が必要とされている。近年では、気軽さ、飲みやすさの点で低アルコール飲料の人気が高い。
果実酒を調理に用いる場合は、アルコール度数の低減、エキス分の濃縮のために加熱して煮詰める方法が公知である。一方、加熱によるエキス分の変質等を低減し、温和な条件にて果実酒を濃縮して所望のアルコール度数、エキス分とし、調理用として用いることは公知であり、また濃縮方法として減圧濃縮法を用いることも公知である(特許文献1,2参照。)。
Fruit liquor is an alcoholic beverage brewed from fruits and widely used for drinking and cooking. Typical fruit wines are wine, cider, etc. obtained by brewing fruits such as grapes, pears, loquat, apples, quinces, and apricots.
Fruit drinks for drinking require products of various concentrations of alcohol content or extracts according to market demands. In recent years, low-alcohol drinks are popular due to their ease of use and ease of drinking.
In the case of using fruit wine for cooking, a method of boiling by heating for reducing the alcohol content and concentrating the extract is known. On the other hand, it is known to reduce deterioration of the extract due to heating, etc., concentrate the fruit liquor under mild conditions to obtain the desired alcohol content and extract, and use it for cooking. Is also known (see Patent Documents 1 and 2).

特許第2742827号公報Japanese Patent No. 2742827 特開平11−18718号公報Japanese Patent Laid-Open No. 11-18718

本発明の課題は、飲用または調理用として好適な濃縮果実酒およびその製造法を提供することにある。   An object of the present invention is to provide a concentrated fruit liquor suitable for drinking or cooking and a method for producing the same.

濃縮果実酒においては、アルコール度数、エキス分、還元糖類、有機酸あるいはタンニン成分がバランスよく含有されていることが重要であり、それが調理効果(素材の軟化効果等)、飲用時の香味に影響する。本発明者らは、特定条件の減圧濃縮法を採用することにより、飲料用あるいは調理用として好適なアルコール度数及びエキス分を有する濃縮果実酒が得られることを見出し本発明を完成した。すなわち本発明は、以下に記載する濃縮果実酒およびその製造法に関する。
1.原料果実酒を減圧濃縮により2〜5倍濃縮して得られる、アルコール度数が1.5%〜3.0%、エキス分が10%以上である濃縮果実酒。
2.原料果実酒を品温40〜55℃で減圧濃縮して得られる、アルコール度数が1.5%〜3.0%、エキス分が10%以上である濃縮果実酒。
3.原料果実酒を品温40〜55℃で減圧濃縮して得られる、アルコール度数が1.5%〜3.0%、エキス分が原料果実酒の2〜5倍である濃縮果実酒。
4.原料果実酒を品温40〜55℃の条件で減圧濃縮することを特徴とする、濃縮果実酒の製造法。
5.原料果実酒を品温40〜55℃で減圧濃縮し、濃縮物中のアルコール度数を1.5%〜3.0%、エキス分を原料果実酒の2倍以上とすることを特徴とする、濃縮果実酒の製造法。
6.原料果実酒を品温40〜45℃で減圧濃縮し、濃縮物中のアルコール度数を1.5%〜3.0%、エキス分を10%以上とすることを特徴とする、果実酒の減圧濃縮法。
In concentrated fruit liquor, it is important that the alcohol content, extract content, reducing sugar, organic acid or tannin component is contained in a balanced manner, which is effective for cooking effects (softening effect of ingredients, etc.) and flavor when drinking Affect. The present inventors have found that a concentrated fruit liquor having an alcohol content and an extract content suitable for beverages or cooking can be obtained by employing a vacuum concentration method under specific conditions. That is, this invention relates to the concentrated fruit wine described below and its manufacturing method.
1. Concentrated fruit liquor having an alcohol content of 1.5% to 3.0% and an extract content of 10% or more, obtained by concentrating the raw material fruit liquor by concentration 2-5 times under reduced pressure.
2. Concentrated fruit liquor with an alcohol content of 1.5% to 3.0% and an extract content of 10% or more, obtained by concentrating the raw fruit wine at a product temperature of 40 to 55 ° C. under reduced pressure.
3. A concentrated fruit liquor obtained by concentrating raw fruit wine at a temperature of 40 to 55 ° C. under reduced pressure, having an alcohol content of 1.5% to 3.0% and an extract content 2 to 5 times that of the raw fruit wine.
4). A method for producing concentrated fruit liquor, characterized in that the raw fruit wine is concentrated under reduced pressure at a temperature of 40 to 55 ° C.
5. The raw fruit wine is concentrated under reduced pressure at a product temperature of 40 to 55 ° C., the alcohol content in the concentrate is 1.5% to 3.0%, and the extract content is more than twice that of the raw fruit wine. A method for producing concentrated fruit wine.
6). The fruit juice is concentrated under reduced pressure at a product temperature of 40 to 45 ° C., the alcohol content in the concentrate is 1.5% to 3.0%, and the extract content is 10% or more. Concentration method.

本発明により、飲料用あるいは調理用として好適な濃縮果実酒が得られる。   According to the present invention, a concentrated fruit liquor suitable for beverages or cooking is obtained.

以下、本発明を具体的に説明する。
1.濃縮果実酒
本発明は、原料果実酒を減圧濃縮により2〜5倍濃縮して得られる、アルコール度数が1.5%〜3.0%、エキス分が10%である濃縮果実酒に関する。なお、本発明では、アルコール度数の単位は(%.v/v)、エキス分の単位は(%.w/v)を意味する。
アルコール度数が1.5%〜3.0%であることは、低アルコール飲料として好適である。またアルコール臭が弱い、アルコール度調整のために長時間煮詰める必要がないという点で、調理用としても好適である。
上記濃縮果実酒のエキス分は10%以上、好ましくは10〜15%である。このことは、飲用としてはしっかりとしたコク味があるがくどくはないという点で好適である。
当該濃縮果実酒は、原料果実酒を減圧濃縮することによって得られるが、その際、原料果実酒を容量換算で2〜5倍となるように濃縮する。また、アルコール度数は1.5%〜3.0%、エキス分は10%以上、好ましくは10〜15%となるように濃縮する。
原料として利用する果実酒は、果実を原料として醸造したアルコール飲料であれば特に限定されないが、ブドウ、ナシ、ビワ、リンゴ、マルメロ、アンズ等の果実を醸造することにより得られるワイン、シードル等が挙げられる。特に好適な原料果実酒とは、ブドウ酒等のワインである。ワインとしては、葡萄の果汁のみを発酵して醸造される所謂赤ワイン、白ワイン、ロゼワインの他に、発泡性を有するスパークリングワイン、ワインに濃縮果汁、ブランデーを添加したシェリー、ポート、マデラ、マラガ、マルサラ等の所謂補強ワイン、あるいはワインに薬草、香料、色素等を添加して得られる、ベルモットを代表とする混成ワイン等が使用できる。
減圧濃縮は、通常の減圧濃縮装置あるいは減圧蒸留装置を利用すればよい。装置としては、濃縮缶、ロータリーエバポレーター等が利用できる。減圧濃縮法は、常圧濃縮法に比べ低温で濃縮ができるので、加熱による香味の劣化を抑制する点で優れている。装置の流路を減圧する為には、水封ポンプ、水流ポンプあるいは真空ポンプ等が使用できる。高い真空度を得るためには真空ポンプの使用が望ましい。真空度は、使用する装置や原料果実酒の種類に応じて設定すればよいが、例えば50〜700Torr(トール)、好ましくは、100〜200Torrである。真空度が高い条件(50〜100Torr)では、得られる濃縮果実酒の品質は、フルーティな香りが少なくなり、真空度が低い条件(250〜700Torr)では、得られる濃縮果実酒の品質は、香りのやや少ないものとなる傾向がある。濃縮操作の効率化のために原料果実酒を加熱する場合、真空度によっても異なるが、原料果実酒の品温を30〜70℃、好ましくは40〜55℃とすればよい。
また本発明は、原料果実酒を品温40〜55℃で減圧濃縮して得られる、アルコール度数が1.5%〜3.0%、エキス分が10%以上である濃縮果実酒に関する。なお、好ましいエキス分は10%〜15%である。
減圧濃縮が品温40〜55℃の条件で行われると、短時間で濃縮でき香りの劣化、減少が少ないので、得られる濃縮果実酒の品質が良好(フルーティで強い香りを有する)となる。
原料果実酒がブドウ酒である場合、原料のアルコール度数は通常、10〜13%、エキス分は通常、赤ワイン2.5〜3.5%、白ワイン2.0〜3.0%である。これをアルコール度数が1.5%〜3.0%、エキス分が原料果実酒の2倍以上、あるいは10%以上となるまで減圧濃縮すると、アルコール刺激が少なく、フルーティな香りが強く、しかもしっかりとしたコク味を有するという特性の濃縮ワインが得られる。
The present invention will be specifically described below.
1. TECHNICAL FIELD The present invention relates to a concentrated fruit liquor obtained by concentrating raw fruit liquor 2 to 5 times by vacuum concentration and having an alcohol content of 1.5% to 3.0% and an extract content of 10%. In the present invention, the unit of alcohol content means (% .v / v) and the unit of extract means (% .w / v).
An alcohol content of 1.5% to 3.0% is suitable as a low alcoholic beverage. It is also suitable for cooking because it has a weak alcohol odor and does not need to be boiled for a long time to adjust the alcohol content.
The concentrated fruit wine has an extract content of 10% or more, preferably 10 to 15%. This is preferable in that it has a firm and rich taste for drinking.
The concentrated fruit liquor is obtained by concentrating the raw fruit wine under reduced pressure. At that time, the raw fruit wine is concentrated so as to be 2 to 5 times in terms of volume. The alcohol content is 1.5% to 3.0%, and the extract content is 10% or more, preferably 10 to 15%.
The fruit liquor used as a raw material is not particularly limited as long as it is an alcoholic beverage brewed from fruits, but wines, ciders, etc. obtained by brewing fruits such as grapes, pears, loquats, apples, quinces, apricots, etc. Can be mentioned. Particularly suitable raw fruit wine is wine such as wine. In addition to the so-called red wine, white wine, and rose wine, which are fermented only by the fruit juice of strawberry, the wine is sparkling wine that has effervescence, concentrated fruit juice to wine, brandy added sherry, port, madera, Malaga, So-called reinforced wine such as Marsala, or hybrid wine represented by vermouth obtained by adding medicinal herbs, fragrances, pigments and the like to wine can be used.
The vacuum concentration may be performed using a normal vacuum concentration device or a vacuum distillation device. As the apparatus, a concentrated can, a rotary evaporator, or the like can be used. The vacuum concentration method is superior in that it can be concentrated at a lower temperature than the atmospheric pressure concentration method, so that it suppresses flavor deterioration due to heating. In order to depressurize the flow path of the apparatus, a water seal pump, a water pump, a vacuum pump, or the like can be used. In order to obtain a high degree of vacuum, it is desirable to use a vacuum pump. The degree of vacuum may be set according to the type of apparatus used and the raw fruit wine, and is, for example, 50 to 700 Torr, preferably 100 to 200 Torr. Under high vacuum conditions (50 to 100 Torr), the quality of the concentrated fruit liquor obtained is less fruity and under low vacuum conditions (250 to 700 Torr), the quality of the concentrated fruit wine obtained is fragrant. There is a tendency to be somewhat less. When the raw fruit wine is heated to increase the efficiency of the concentration operation, the product temperature of the raw fruit wine may be 30 to 70 ° C., preferably 40 to 55 ° C., depending on the degree of vacuum.
The present invention also relates to a concentrated fruit wine obtained by concentrating a raw fruit wine at a product temperature of 40 to 55 ° C. under reduced pressure and having an alcohol content of 1.5% to 3.0% and an extract content of 10% or more. A preferable extract content is 10% to 15%.
When the vacuum concentration is carried out under the condition of the product temperature of 40 to 55 ° C., it can be concentrated in a short time, and the quality and quality of the concentrated fruit liquor obtained is good (having a fruity and strong scent) because the fragrance is less deteriorated and reduced.
When the raw fruit wine is grape wine, the alcohol content of the raw material is usually 10 to 13%, and the extract content is usually 2.5 to 3.5% red wine and 2.0 to 3.0% white wine. If this is concentrated under reduced pressure until the alcohol content is 1.5% to 3.0% and the extract content is more than twice that of the raw fruit wine, or more than 10%, there is less alcohol irritation, a strong fruity fragrance, and firmness. Concentrated wine with the characteristic of having a full-bodied taste is obtained.

2.濃縮果実酒の製造法
濃縮果実酒の製造法は、原料果実酒を品温40〜55℃で減圧濃縮することを特徴とする。
減圧濃縮操作において、品温40〜55℃で行うと、短時間で濃縮でき、香りの劣化、減少が少ないという効果がある。一方、品温40℃未満では、濃縮作業が長く掛かりフルーティな香りが減少するという場合があり、55℃を超えるとフルーティな香りの変質とフルーティな香りが減少するという場合がある。以上の減圧濃縮の条件は、しっかりとしたフルーティな香りが残存するという点で優れており、得られる濃縮果実酒の品質が豊かなフルーティな香りを有し優れたものとなる。
なお、原料果実酒の種類によっては、減圧濃縮中に酒石が晶析する場合がある。その際は、メンブランフィルターによるろ過等を用いて酒石を除去すればよい。
また、本発明の濃縮果実酒の製造法は、原料果実酒を品温40〜55℃で減圧濃縮し、濃縮物中のアルコール度数を1.5%〜3.0%、エキス分を原料果実酒の2倍以上とすることを特徴とする。なお、エキス分は原料果実酒の2.5〜3.5倍とすることが好ましい。
以上の減圧濃縮の条件は、ワインのフルーティな特徴とアルコール以外の成分が濃縮されてそのまま残るという点で優れており、得られる濃縮果実酒の品質がフルーティでコク味がありアルコール刺激の少ないものとなる。
また本発明の濃縮果実酒の製造法は、原料果実酒を品温40〜45℃で減圧濃縮し、濃縮物中のアルコール度数を1.5%〜3.0%、エキス分を10%以上とすることを特徴とする。なお、好ましいエキス分は10〜15%である。
以上の減圧濃縮の条件は、アルコール以外のフルーティな香りを含む成分が品質劣化することなく濃縮残存するという点で優れており、得られる濃縮果実酒の品質がフルーティな香りを有し、アルコール刺激の少ないコク味のしっかりした優れたものとなる。
以下、実施例及び参考例を挙げて本発明を具体的に説明するが、本発明はこれ等により、何ら制限されるものではない。
2. Method for Producing Concentrated Fruit Liquor The method for producing concentrated fruit liquor is characterized in that the raw fruit wine is concentrated under reduced pressure at a product temperature of 40 to 55 ° C.
In the vacuum concentration operation, if it is carried out at a product temperature of 40 to 55 ° C., it can be concentrated in a short time, and there is an effect that there is little deterioration and decrease in fragrance. On the other hand, if the product temperature is less than 40 ° C., the concentration work may take a long time and the fruity fragrance may decrease, and if it exceeds 55 ° C., the alteration of the fruity fragrance and the fruity fragrance may decrease. The above-mentioned conditions for concentration under reduced pressure are excellent in that a firm and fruity fragrance remains, and the resulting concentrated fruit liquor has an excellent fruity fragrance.
Depending on the type of raw fruit wine, tartar may crystallize during vacuum concentration. In that case, the tartar may be removed by filtration with a membrane filter or the like.
Moreover, the manufacturing method of the concentrated fruit liquor of this invention concentrates raw material fruit liquor under reduced pressure at the product temperature of 40-55 degreeC, the alcohol content in a concentrate is 1.5% -3.0%, and an extract part is raw material fruit. It is characterized by being at least twice as much as sake. The extract content is preferably 2.5 to 3.5 times that of the raw fruit wine.
The above-mentioned conditions for concentration under reduced pressure are excellent in that the fruity characteristics of wine and the components other than alcohol are concentrated and remain as they are, and the quality of the resulting concentrated fruit wine is fruity and rich in taste and has little alcohol irritation It becomes.
Moreover, the manufacturing method of the concentrated fruit wine of this invention concentrates raw material fruit wine under reduced pressure at the product temperature of 40-45 degreeC, the alcohol content in a concentrate is 1.5% -3.0%, and an extract part is 10% or more. It is characterized by. In addition, a preferable extract content is 10 to 15%.
The above-mentioned conditions for concentration under reduced pressure are excellent in that components containing a fruity fragrance other than alcohol remain concentrated without deterioration, and the quality of the resulting concentrated fruit liquor has a fruity fragrance and is alcohol-stimulated. It will be a solid and excellent one with little richness.
EXAMPLES Hereinafter, although an Example and a reference example are given and this invention is demonstrated concretely, this invention is not restrict | limited at all by these.

原料果実酒として市販白ワイン(商品名「マティエール白」マンズワイン(株)製)2,500mlを、ロータリー・エバポレーターにて、湯浴の温度をそれぞれ40℃、50℃、60℃、70℃、80℃に設定し、各500mlを2倍濃縮となるよう250mlまで減圧濃縮した。減圧は真空機工(株)製ダイアフラム式真空ポンプMDA−015を用い、トラップの冷却は低温恒温循環機(ADVANTEC LV−600、(株)東洋製作所製)にて5℃に制御した。減圧濃縮時の真空度は100Torrであった。得られた濃縮ワインの品質を表1に示す。   2500 ml of commercially available white wine (trade name “Matière White” Mans Wine Co., Ltd.) as the raw fruit liquor, the temperature of the hot water bath is 40 ° C., 50 ° C., 60 ° C. and 70 ° C., respectively, using a rotary evaporator. The temperature was set at 80 ° C., and each 500 ml was concentrated under reduced pressure to 250 ml so as to be double concentrated. The vacuum was controlled by using a vacuum vacuum pump MDA-015 manufactured by Vacuum Kiko Co., Ltd., and the cooling of the trap was controlled at 5 ° C. by a low-temperature constant temperature circulator (ADVANTEC LV-600, manufactured by Toyo Manufacturing Co., Ltd.). The degree of vacuum during vacuum concentration was 100 Torr. Table 1 shows the quality of the obtained concentrated wine.

Figure 2006174760
Figure 2006174760

原料果実酒として市販白ワイン(商品名「マティエール白」、マンズワイン(株)製)1,000mlを、ロータリー・エバポレーターを用い、400mlまで濃縮した(2.5倍濃縮)。減圧は真空機工(株)製ダイアフラム式真空ポンプMDA−01を用い、トラップの冷却は低温恒温循環機(ADVANTEC LV−600、(株)東洋製作所製)にて5℃に制御した。減圧濃縮時の真空度は100Torrであった。湯浴温度は75℃とした。この時、原料果実酒の品温は53℃であった。
得られた濃縮ワインを0℃の低温室に5日間放置したところ、著量の酒石が晶析したので、メンブランフィルターによる加圧濾過(使用メンブランフィルター:孔径0.45μ、酢酸セルロース膜、東洋濾紙(株)製)を行った。
1,000 ml of commercially available white wine (trade name “Matière White”, manufactured by Mann's Wine Co., Ltd.) was concentrated as a raw material fruit liquor to 400 ml using a rotary evaporator (2.5 times concentrated). The vacuum was controlled by using a vacuum vacuum pump MDA-01 manufactured by Vacuum Kiko Co., Ltd., and the cooling of the trap was controlled at 5 ° C. by a low temperature constant temperature circulator (ADVANTEC LV-600, manufactured by Toyo Manufacturing Co., Ltd.). The degree of vacuum during vacuum concentration was 100 Torr. The bath temperature was 75 ° C. At this time, the product temperature of the raw fruit wine was 53 ° C.
When the obtained concentrated wine was left in a low-temperature room at 0 ° C. for 5 days, a significant amount of tartar crystallized, so pressure filtration with a membrane filter (membrane filter used: pore size 0.45 μ, cellulose acetate membrane, Toyo (Made by filter paper).

得られた濃縮ワインの分析を第3回改正、国税庁所定分析法注解のワイン分析方法に準じて分析した。結果を表2に示す。pHは元のワイン濃度まで水で希釈し、測定した。   The analysis of the obtained concentrated wine was analyzed in accordance with the wine analysis method in the third revision, commented on by the National Tax Agency. The results are shown in Table 2. The pH was measured by diluting with water to the original wine concentration.

Figure 2006174760
Figure 2006174760

得られた濃縮白ワインは、褐変の指標である、420nmにおける吸光度(OD)値が低く、褐変が進んでいないことが分かる。また、風味的にも良好で、濃縮ワインとして調理用に適していた。   It can be seen that the obtained concentrated white wine has a low absorbance (OD) value at 420 nm, which is an index of browning, and browning has not progressed. It was also good in flavor and suitable as a concentrated wine for cooking.

原料果実酒として市販赤ワイン(商品名「マティエール赤」、マンズワイン(株)製)1,000mlをロータリー・エバポレーターを用い、400mlまで濃縮した(2.5倍濃縮)。減圧は真空機工(株)製ダイアフラム式真空ポンプMDA−01を用い、トラップの冷却は低温恒温循環機(ADVANTEC LV−600、(株)東洋製作所製)にて5℃に制御した。湯浴温度は75℃とした。真空度は100Torrであった。この時の品温は53℃であった。
得られた濃縮ワインを0℃の低温室に5日間放置したところ、著量の酒石が晶析したので、メンブランフィルターによる加圧濾過(使用メンブランフィルター:孔径0.45μ、酢酸セルロース膜、東洋濾紙(株)製)を行った。
1,000 ml of commercially available red wine (trade name “Matière Red”, manufactured by Mann's Wine Co., Ltd.) was concentrated as a raw material fruit liquor to 400 ml using a rotary evaporator (2.5 times concentration). The vacuum was controlled by using a vacuum vacuum pump MDA-01 manufactured by Vacuum Kiko Co., Ltd., and the cooling of the trap was controlled at 5 ° C. by a low temperature constant temperature circulator (ADVANTEC LV-600, manufactured by Toyo Manufacturing Co., Ltd.). The bath temperature was 75 ° C. The degree of vacuum was 100 Torr. The product temperature at this time was 53 ° C.
When the obtained concentrated wine was left in a low-temperature room at 0 ° C. for 5 days, a significant amount of tartar crystallized, so pressure filtration with a membrane filter (membrane filter used: pore size 0.45 μ, cellulose acetate membrane, Toyo (Made by filter paper).

濃縮ワインの分析を第3回改正、国税庁所定分析法注解のワイン分析方法に準じて分析した。結果を表3に示す。pHは元のワイン濃度まで水で希釈し、測定した。   The analysis of concentrated wine was analyzed in accordance with the 3rd revision of the analysis method of wines specified in the National Tax Agency. The results are shown in Table 3. The pH was measured by diluting with water to the original wine concentration.

Figure 2006174760
Figure 2006174760

得られた濃縮赤ワインは、赤ワインの赤紫色の吸収である、520nmにおける吸光度(OD)値が高く、鮮やかな色調であった。また、風味的にも良好で、濃縮ワインとして調理用に適していた。   The obtained concentrated red wine had a high absorbance (OD) value at 520 nm, which is reddish purple absorption of red wine, and had a vivid color tone. It was also good in flavor and suitable as a concentrated wine for cooking.

〔参考例1〕
原料果実酒として市販白ワイン(商品名「マティエール白」、マンズワイン(株)製)2,000mlを、容量約4Lの鍋にとり、ガスレンジを用い、強火で加熱し、液量が約800mlになるまで濃縮した。得られた濃縮ワインを10℃の定温室に16時間放置したところ、著量の酒石が晶析したので、メンブランフィルターによる加圧濾過(使用メンブランフィルター:孔径0.45μ、酢酸セルロース膜、東洋濾紙(株)製)を行った。最終的に得られた濃縮白ワインの容量は750mlであった。従って、濃縮倍率は2.7倍であった。得られた濃縮ワインの分析を第3回改正、国税庁所定分析法注解のワイン分析法に準じて分析した。結果を表4に示す。pHは元のワインの濃度まで水で希釈し、測定した。
[Reference Example 1]
2,000 ml of commercially available white wine (trade name “Matière White”, Mann's Wine Co., Ltd.) as a raw fruit liquor is placed in a pan with a capacity of about 4 L, heated with high heat using a gas range, and the liquid volume is about 800 ml. Concentrated to. When the obtained concentrated wine was left in a constant temperature room at 10 ° C. for 16 hours, a significant amount of tartar crystallized, so pressure filtration with a membrane filter (membrane filter used: pore size 0.45 μ, cellulose acetate membrane, Toyo (Made by filter paper). The volume of the concentrated white wine finally obtained was 750 ml. Therefore, the concentration ratio was 2.7 times. The analysis of the obtained concentrated wine was analyzed in accordance with the third revised amendment of the analysis method specified by the NTA. The results are shown in Table 4. The pH was measured by diluting with water to the original wine concentration.

Figure 2006174760
Figure 2006174760

得られた濃縮白ワインは、褐変の指標である、420nmにおける吸光度(OD)値が実施例2での値(0.126)より顕著に高く0.578であり、褐変が進んでいることが判る。実際、目視的にも本濃縮白ワインは赤褐色を呈し、調理用白ワインとしても好ましくなかった、また、風味的にも所謂焦げ臭が付き、調理用に適していなかった。また、ガスレンジの加熱では、アルコールおよび揮発成分が部屋中にたち込め、臭いの点およびアルコールが飛ぶので引火性の点に問題があった。更に、この方法では、ワインの焦げ付きに注意を払う必要があり、煮込んでいる間中監視する必要があった。
以上より、本発明の減圧濃縮による濃縮ワイン製造方法の優位性が証明された。
The obtained concentrated white wine has an absorbance (OD) value at 420 nm, which is an index of browning, which is significantly higher than the value (0.126) in Example 2 and is 0.578, and browning is progressing. I understand. Actually, the present concentrated white wine was reddish brown and was not preferable as a white wine for cooking. Also, the so-called burnt odor was not good for cooking. In addition, the heating of the gas range has a problem in terms of flammability because alcohol and volatile components get into the room and the smell and alcohol fly away. Furthermore, this method requires attention to the scorching of the wine and must be monitored throughout the cooking.
From the above, the superiority of the method for producing concentrated wine by vacuum concentration according to the present invention was proved.

〔参考例2〕
原料果実酒として市販赤ワイン(商品名「マティエール赤」、マンズワイン(株)製)2,000mlを容量約4Lの鍋にとり、ガスレンジを用い、参考例と同様に、液量が約800mlになるまで濃縮した。得られた約2.5倍まで濃縮した赤ワイン液を、0℃の低温室に5日間放置したところ、著量の酒石が晶析したので、メンブランフィルターによる加圧濾過を実施例1と同様に行った。最終的濃縮赤ワイン750mlが得られたので、濃縮倍率は2.7倍であった。得られた濃縮ワインの分析を第3回改正、国税庁所定分析法注解のワイン分析法に準じて分析した。結果を表5に示す。pHは元のワインの濃度まで水で希釈し、測定した。
[Reference Example 2]
2,000 ml of commercially available red wine (trade name “Matière Red”, manufactured by Mann's Wine Co., Ltd.) as a raw fruit wine is placed in a pan with a capacity of about 4 L, and the liquid volume is about 800 ml as in the reference example using a gas range. Concentrated to When the obtained red wine liquid concentrated to about 2.5 times was left in a low-temperature room at 0 ° C. for 5 days, a significant amount of tartar crystallized, and pressure filtration using a membrane filter was performed in the same manner as in Example 1. Went to. Since 750 ml of final concentrated red wine was obtained, the concentration factor was 2.7 times. The analysis of the obtained concentrated wine was analyzed in accordance with the third revised amendment of the analysis method specified by the NTA. The results are shown in Table 5. The pH was measured by diluting with water to the original wine concentration.

Figure 2006174760
Figure 2006174760

ワインの色は、「赤紫色を示す520nmにおけるOD値/褐変の指標である420nmにおけるOD値」の値が大きい程、鮮やかである。この値が低いワインは褐変赤色褪色が進んでいると判断できる。
参考例2で得られた濃縮赤ワインは「520nmにおけるOD値(7.930)/420nmにおけるOD値(7.420)=1.07」であり、一方、実施例3で得られた濃縮赤ワインは「520nmにおけるOD値(5.620)/420nmにおけるOD値(4.100)=1.37」であった。参考例2の濃縮赤ワインは、実施例3の濃縮赤ワインより、褐変赤色褪色が進んでいることが判る。
実際、目視でも本濃縮赤ワインは褐変赤色褪色の程度が高く、調理用赤ワインとしても好ましくなかった。また、風味的にも所謂焦げ臭が付き、調理用に適していなかった。また、ガスレンジの加熱では、アルコールおよび揮発成分が部屋中に立ち込め、臭いの点およびアルコールが飛ぶので引火性の点で実用は不可能と感じられた。更に、この方法では、ワインの焦げ付きに注意を払う必要があり、煮込んでいる間中監視する必要があった。
以上より、本発明の減圧濃縮による濃縮ワイン製造方法の優位性が証明された。
The color of wine is more vivid as the value of “OD value at 520 nm indicating reddish purple / OD value at 420 nm, which is an index of browning” is larger. It can be judged that the wine with this low value has progressed browning red amber color.
The concentrated red wine obtained in Reference Example 2 is “OD value at 520 nm (7.930) / OD value at 420 nm (7.420) = 1.07”, while the concentrated red wine obtained in Example 3 is “OD value at 520 nm (5.620) / OD value at 420 nm (4.100) = 1.37”. It can be seen that the concentrated red wine of Reference Example 2 has a more browned red amber color than the concentrated red wine of Example 3.
Actually, the present concentrated red wine also has a high brownish red amber color and is not preferable as a cooking red wine. In addition, the so-called burnt odor was added to the flavor, which was not suitable for cooking. In addition, in the heating of the gas range, it was felt that practical use was impossible in terms of flammability because alcohol and volatile components trapped in the room and the smell and alcohol flew. Furthermore, this method requires attention to the scorching of the wine and must be monitored throughout the cooking.
From the above, the superiority of the method for producing concentrated wine by vacuum concentration according to the present invention was proved.

〔参考例3〕
原料果実酒として市販白ワイン(商品名「エコノミー白」、マンズワイン(株)製)2Lをビニール袋に水を抜いて密封し、最初‐30℃の冷凍庫で冷却し、わずかに氷が出来たところで、−10℃の冷蔵室に移し、一晩放置し、氷を徐々に増加させ冷凍濃縮を行った。約24時間後、濾紙を用いた減圧濾過により、非凍結部分を分取したところ、960mlの濃縮白ワインが得られた。従って、濃縮度は約2倍であった。得られた凍結濃縮ワインの一般分析を実施例1と同様に行った。結果を表6に示す。
[Reference Example 3]
2L of commercially available white wine (product name "Economy White", Mann's Wine Co., Ltd.) as a raw fruit liquor was sealed by draining water into a plastic bag, and cooled in a freezer at -30 ° C for the first time. By the way, it moved to the -10 degreeC refrigerator compartment, left to stand overnight, ice was gradually increased, and it concentrated by freezing. After about 24 hours, the non-frozen portion was separated by vacuum filtration using filter paper, and 960 ml of concentrated white wine was obtained. Therefore, the concentration was about twice. General analysis of the obtained frozen concentrated wine was performed in the same manner as in Example 1. The results are shown in Table 6.

Figure 2006174760
Figure 2006174760

得られた冷凍濃縮白ワインは、濃縮倍率が約2倍と低く、調理用の濃縮ワインとしては実用性がなかった。本方法では、冷凍をプログラムし、効率を上げても、10倍濃縮までは濃縮が不可能であり、本発明で必要としている品質を得ることはできない。
従って、冷凍濃縮により調理用の濃縮ワインを得ることは出来ないことが判明した。
The obtained frozen concentrated white wine had a concentration rate as low as about 2 times, and was not practical as a concentrated wine for cooking. In this method, even if refrigeration is programmed and efficiency is increased, concentration cannot be performed up to 10-fold concentration, and the quality required in the present invention cannot be obtained.
Accordingly, it has been found that concentrated wine for cooking cannot be obtained by freeze concentration.

〔参考例4〕
原料果実酒として市販赤ワイン(商品名「エコノミー赤」、マンズワイン(株)製)2Lをビニール袋に水を抜いて密封し、最初‐30℃の冷凍庫で冷却し、わずかに氷が出来たところで、‐10℃の冷蔵室に移し、一晩放置し、氷を徐々に増加させ冷凍濃縮を行った。約24時間後、濾紙を用いた減圧濾過により、非凍結部分を分取したところ、1,070mlの濃縮赤ワインが得られた。従って、濃縮度は約2倍であった。得られた凍結濃縮ワインの一般分析を実施例1と同様に行った。結果を表7に示す。
[Reference Example 4]
2L of commercially available red wine (product name "Economy Red", manufactured by Mann's Wine Co., Ltd.) as a raw fruit wine is drained into a plastic bag, sealed, cooled in a freezer at -30 ° C, and slightly iced. , Moved to a -10 ° C. refrigerated room, left overnight, gradually increased ice and concentrated by freezing. After about 24 hours, the non-frozen portion was separated by filtration under reduced pressure using a filter paper to obtain 1,070 ml of concentrated red wine. Therefore, the concentration was about twice. General analysis of the obtained frozen concentrated wine was performed in the same manner as in Example 1. The results are shown in Table 7.

Figure 2006174760
Figure 2006174760

得られた冷凍濃縮赤ワインは、濃縮倍率が約2倍と低く、また、含まれるアルコール度数が高く、調理用の濃縮ワインとしては実用性がなかった。冷凍濃縮法では、冷凍をプログラムし、効率を上げても、10倍濃縮までは濃縮が不可能であり、本発明で必要としている品質を得ることはできない。従って、冷凍濃縮により調理用の濃縮ワインを得ることはできない事が判明した。
以上、参考例1〜4より、本発明の減圧濃縮法による濃縮ワインは、鍋で煮る等の常圧濃縮法や冷凍濃縮法による濃縮ワインよりも、明らかに優れており、本発明の優位性が証明された。
The obtained frozen concentrated red wine has a low concentration factor of about 2 times and a high alcohol content, and was not practical as a concentrated wine for cooking. In the refrigeration concentration method, even if the refrigeration is programmed and the efficiency is increased, concentration up to 10-fold concentration is impossible, and the quality required in the present invention cannot be obtained. Accordingly, it has been found that concentrated wine for cooking cannot be obtained by freeze concentration.
As described above, from Reference Examples 1 to 4, the concentrated wine by the vacuum concentration method of the present invention is clearly superior to the concentrated wine by the atmospheric concentration method such as boiling in a pan or the frozen concentration method, and the superiority of the present invention Proved.

原料果実酒として市販白ワイン(商品名「マティエール白」、マンズワイン(株)製)1,000mlを、ロータリー・エバポレーターを用い、400mlまで濃縮した。減圧は真空機工(株)製ダイアフラム式真空ポンプMDA−01を用い、トラップの冷却は低温恒温循環機(ADVANTEC LV−600、(株)東洋製作所製)にて5℃に制御した。湯浴温度は75℃とした。原料果実酒の品温は53℃であった。
以上のようにして、ワインを2.5倍まで濃縮後、0℃の低温室に5日間放置したところ、著量の酒石が晶析したので、メンブランフィルターによる加圧濾過(使用メンブランフィルター:孔径0.45μ、酢酸セルロース膜、東洋濾紙(株)製)を行った。同様にマティエール白2,000mlを、ロータリー・エバポレーターを用い、200mlまで濃縮した。減圧は真空機工(株)製ダイアフラム式真空ポンプMDA−015を用い、トラップの冷却は低温恒温循環機(ADVANTEC LV−600、(株)東洋製作所製)にて5℃に制御した。湯浴温度は45℃とした。この時の品温は42℃であった。
以上のようにして、原料果実酒を10倍まで濃縮後、0℃の低温室に5日間放置したところ、著量の酒石が晶析したので、メンブランフィルターによる加圧濾過(使用メンブランフィルター:孔径0.45μ、酢酸セルロース膜、東洋濾紙(株)製)を行った。これを10倍濃縮率の白ワイン濃縮物とした。各サンプルの分析値は表8に示した通りであった。
1,000 ml of commercially available white wine (trade name “Matière white”, manufactured by Mann's Wine Co., Ltd.) was concentrated as a raw material fruit liquor to 400 ml using a rotary evaporator. The vacuum was controlled by using a vacuum vacuum pump MDA-01 manufactured by Vacuum Kiko Co., Ltd., and the cooling of the trap was controlled at 5 ° C. by a low temperature constant temperature circulator (ADVANTEC LV-600, manufactured by Toyo Manufacturing Co., Ltd.). The bath temperature was 75 ° C. The product temperature of the raw fruit wine was 53 ° C.
As described above, after concentrating the wine to 2.5 times and leaving it in a low-temperature room at 0 ° C. for 5 days, a significant amount of tartar crystallized, so pressure filtration with a membrane filter (used membrane filter: A pore diameter of 0.45 μ, a cellulose acetate membrane, manufactured by Toyo Filter Paper Co., Ltd.) was performed. Similarly, 2,000 ml of matière white was concentrated to 200 ml using a rotary evaporator. Vacuum reduction was performed using a vacuum vacuum pump MDA-015 manufactured by Vacuum Kiko Co., Ltd., and cooling of the trap was controlled at 5 ° C. by a low-temperature constant temperature circulator (ADVANTEC LV-600, manufactured by Toyo Manufacturing Co., Ltd.). The bath temperature was 45 ° C. The product temperature at this time was 42 ° C.
As described above, after concentrating the raw fruit liquor up to 10 times and leaving it in a low temperature room at 0 ° C. for 5 days, a significant amount of tartar crystallized, so pressure filtration with a membrane filter (used membrane filter: A pore diameter of 0.45 μ, a cellulose acetate membrane, manufactured by Toyo Filter Paper Co., Ltd.) was performed. This was a white wine concentrate having a 10-fold concentration ratio. The analysis value of each sample was as shown in Table 8.

Figure 2006174760
(注)*総酸:酒石酸換算値を示した。
Figure 2006174760
(Note) * Total acid: Tartaric acid equivalent.

2.5倍濃縮物果実酒の香味は、明るい黄色、強いフルーティな香りを有し殆どアルコール刺激を感じさせないコク味のしっかりとしたバランスであり好ましい品質を有していた。
また、白ワイン10倍果実酒の香味は、明るい淡黄色、非常にフルーティな香りとコク味がありアルコール刺激の無いソフトなバランスであり好ましい品質を有していた。
The flavor of the 2.5-fold concentrated fruit liquor had a bright yellow color, a strong fruity fragrance, and a good balance that had almost no alcohol stimulation, and had a favorable quality.
Further, the flavor of white wine 10-fold fruit liquor had a light pale yellow color, a very fruity fragrance and a rich taste, a soft balance without alcohol stimulation, and a favorable quality.

Claims (6)

原料果実酒を減圧濃縮により2〜5倍濃縮して得られる、アルコール度数が1.5%〜3.0%、エキス分が10%以上である濃縮果実酒。 Concentrated fruit liquor having an alcohol content of 1.5% to 3.0% and an extract content of 10% or more, obtained by concentrating the raw material fruit liquor by concentration 2-5 times under reduced pressure. 原料果実酒を品温40〜55℃で減圧濃縮して得られる、アルコール度数が1.5%〜3.0%、エキス分が10%以上である濃縮果実酒。 Concentrated fruit liquor with an alcohol content of 1.5% to 3.0% and an extract content of 10% or more, obtained by concentrating the raw fruit wine at a product temperature of 40 to 55 ° C. under reduced pressure. 原料果実酒を品温40〜55℃で減圧濃縮して得られる、アルコール度数が1.5%〜3.0%、エキス分が原料果実酒の2〜5倍である濃縮果実酒。 A concentrated fruit liquor obtained by concentrating raw fruit wine at a temperature of 40 to 55 ° C. under reduced pressure, having an alcohol content of 1.5% to 3.0% and an extract content 2 to 5 times that of the raw fruit wine. 原料果実酒を品温40〜55℃の条件で減圧濃縮することを特徴とする、濃縮果実酒の製造法。 A method for producing concentrated fruit liquor, characterized in that the raw fruit wine is concentrated under reduced pressure at a temperature of 40 to 55 ° C. 原料果実酒を品温40〜55℃で減圧濃縮し、濃縮物中のアルコール度数を1.5%〜3.0%、エキス分を原料果実酒の2倍以上とすることを特徴とする、濃縮果実酒の製造法。 The raw fruit wine is concentrated under reduced pressure at a product temperature of 40 to 55 ° C., the alcohol content in the concentrate is 1.5% to 3.0%, and the extract content is more than twice that of the raw fruit wine. A method for producing concentrated fruit wine. 原料果実酒を品温40〜45℃で減圧濃縮し、濃縮物中のアルコール度数を1.5%〜3.0%、エキス分を10%以上とすることを特徴とする、果実酒の減圧濃縮法。

The fruit juice is concentrated under reduced pressure at a product temperature of 40 to 45 ° C., the alcohol content in the concentrate is 1.5% to 3.0%, and the extract content is 10% or more. Concentration method.

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Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2012244965A (en) * 2011-05-30 2012-12-13 Suntory Holdings Ltd Alcoholic beverage base
JP2016123415A (en) * 2014-12-26 2016-07-11 サントリーホールディングス株式会社 Low alcoholic beverage
JP2017104032A (en) * 2015-12-08 2017-06-15 サッポロビール株式会社 Fruit wine and method for producing the same, and method for improving flavor of fruit wine

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2012244965A (en) * 2011-05-30 2012-12-13 Suntory Holdings Ltd Alcoholic beverage base
JP2016123415A (en) * 2014-12-26 2016-07-11 サントリーホールディングス株式会社 Low alcoholic beverage
JP2017104032A (en) * 2015-12-08 2017-06-15 サッポロビール株式会社 Fruit wine and method for producing the same, and method for improving flavor of fruit wine

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