JPH0673446B2 - Watermelon wine manufacturing method - Google Patents

Watermelon wine manufacturing method

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Publication number
JPH0673446B2
JPH0673446B2 JP19121086A JP19121086A JPH0673446B2 JP H0673446 B2 JPH0673446 B2 JP H0673446B2 JP 19121086 A JP19121086 A JP 19121086A JP 19121086 A JP19121086 A JP 19121086A JP H0673446 B2 JPH0673446 B2 JP H0673446B2
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Japan
Prior art keywords
juice
watermelon
activated carbon
odor
heating
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Lifetime
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JP19121086A
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Japanese (ja)
Other versions
JPS6349060A (en
Inventor
富衛 中島
芳夫 榛葉
説爾 臼井
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NAGANO PREFECTURAL GOVERNMENT
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NAGANO PREFECTURAL GOVERNMENT
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Priority to JP19121086A priority Critical patent/JPH0673446B2/en
Publication of JPS6349060A publication Critical patent/JPS6349060A/en
Publication of JPH0673446B2 publication Critical patent/JPH0673446B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は、西瓜を原料とする西瓜ワインの製造法に関す
る。
TECHNICAL FIELD The present invention relates to a method for producing watermelon wine using watermelon as a raw material.

〔従来の技術〕[Conventional technology]

西瓜果実の消費形態のほとんどが生食用として扱われて
いるのが現状で、加工利用の面で他の果実類に遅れてい
る。その原因として、流通過程では果実として扱われな
がら、生産段階では野菜の域を出ていないことが挙げら
れるが、素材のもつ独特の青臭さ、いわゆる「うり臭」
の除去が極めて困難であることが食品加工分野での遅れ
を助長している。
Currently, most of the consumption patterns of watermelon fruits are treated as raw food, which lags other fruits in terms of processing and utilization. The reason for this is that it is treated as a fruit in the distribution process, but it does not leave the area of vegetables at the production stage.
The extremely difficult removal of lactic acid contributes to the delay in the food processing field.

西瓜を食品加工分野で利用する技術として、特開昭51−
86192号を以って開示の「西瓜を原料とする酒精飲料の
製造法」がある。これは、西瓜の搾汁液を減圧濃縮し、
酸糖比を調整し、発酵体を加えて発酵させ、西瓜ワイン
を得るものであり、また、かかる西瓜ワインを基にして
西瓜ブランデーを得るものである。
As a technique for using watermelon in the food processing field, JP-A-51-
There is a method for producing an alcoholic beverage made from watermelon as disclosed in Japanese Patent No. 86192. This is a vacuum-concentration of the watermelon juice,
The watermelon wine is obtained by adjusting the acid sugar ratio, adding a fermented product and fermenting, and also obtaining the watermelon brandy based on the watermelon wine.

〔解決すべき問題点〕 しかしながら、上記従来の西瓜を原料とする酒精飲料の
製造法によれば、次の問題点がある。
[Problems to be Solved] However, according to the conventional method for producing an alcoholic beverage using watermelon as a raw material, there are the following problems.

うり臭の除去方法は、西瓜の搾汁液を減圧濃縮する
ものであるが、高価な真空装置の設備を必要とし、西瓜
を原料とする酒精飲料のコストが必然的に高くなる。ま
た、減圧濃縮工程は多大な時間がかかり、西瓜出荷時期
に相応した多量供給には不向きである。
The method of removing the odor is to concentrate the squeezed juice of the watermelon under reduced pressure, but it requires expensive vacuum equipment and the cost of the alcoholic beverage made from the watermelon is inevitably high. Also, the vacuum concentration process takes a lot of time, and is not suitable for supplying a large amount according to the time of shipment of watermelon.

西瓜出荷時期に西瓜ジュースを多量製造して冷蔵し
ておき、適宜醸造工程にのせる必要があるが、減圧濃縮
液のままの冷蔵保存では、雑菌等の繁殖を防止する上で
問題点がある。
It is necessary to produce a large amount of watermelon juice at the time of shipment from the watermelon, refrigerate it, and put it in the brewing process as needed, but refrigeration storage as a vacuum concentrated solution poses a problem in preventing the growth of various bacteria. .

本発明の目的は、上記問題点が解決するものであり、実
用に供しうる西瓜ワインの製造法を提供することにあ
り、特に、うり臭の除去方法の改良と、西瓜ワインの被
醸造液たる西瓜ジュースの保存性の向上を図るものであ
る。
An object of the present invention is to solve the above problems, and to provide a method for producing watermelon wine that can be put to practical use, and in particular, an improved method for removing smelt and a brewed liquid for watermelon wine. It is intended to improve the shelf life of watermelon juice.

〔問題点の解決手段〕[Means for solving problems]

上記の問題点を解決するため、本願発明に係る西瓜ワイ
ンの製造法は、次の6つの工程からなるものである。
In order to solve the above problems, the method for producing watermelon wine according to the present invention comprises the following six steps.

西瓜の可食部を破砕し予備加熱をして搾汁する搾汁
工程があること。
There must be a squeezing process in which the edible portion of watermelon is crushed, preheated and squeezed.

「予備加熱」を施すのは搾汁効果を上げるためで、うり
臭の除去にも若干寄与する。
The "preheating" is performed to improve the juice extraction effect and also contributes a little to the removal of odor.

該搾汁の固液分離処理により清澄果汁を得る工程が
あること。
There must be a step of obtaining clear fruit juice by solid-liquid separation treatment of the juice.

「固液分離処理」は該搾汁の残渣を除去するもので、通
常、遠心分離をした後濾過を行なう。
"Solid-liquid separation treatment" is to remove the residue of the squeezed juice. Usually, centrifugation is performed after centrifugation.

「清澄果汁」は、固液分離処理をしない混濁果汁(搾
汁)に比し、残渣が存在しない分うり臭が低い。
The “clarified fruit juice” has a lower odor than the cloudy fruit juice (squeezed juice) that is not subjected to the solid-liquid separation treatment because it does not have any residue.

該清澄果汁に対して一次活性炭素を添加した後、11
5〜130℃,15秒間〜127分間の範囲内でうり臭を除去し得
る加熱条件の下で加熱する高温加熱工程があること。
After adding primary activated carbon to the clear juice, 11
There shall be a high-temperature heating step in which heating is performed under the heating conditions capable of removing the odor in the range of 5 to 130 ° C for 15 seconds to 127 minutes.

「一次活性炭素」の添加は清澄果汁のうり臭を吸着させ
るためで、活性炭素の種類によりその添加量は異なる。
「高温加熱」はその吸着効果を高めるためである。その
加熱条件は加熱温度対加熱時間で特定されるが、例え
ば、約115℃−127分間、約125℃−2分間、約130℃−15
秒間である。この一次活性炭素を添加と高温加熱処理の
併用により、うり臭が除去された果汁を得ることができ
る。この高温加熱は同時に果汁に対する殺菌,減菌の作
用を果たし、長期保存性のある果汁を提供する。
The addition of "primary activated carbon" is for adsorbing the smell of clarified juice, and the amount added varies depending on the type of activated carbon.
"High temperature heating" is to enhance the adsorption effect. The heating conditions are specified by heating temperature versus heating time, and for example, about 115 ° C-127 minutes, about 125 ° C-2 minutes, about 130 ° C-15 minutes.
Seconds. By adding the primary activated carbon and using the high-temperature heat treatment in combination, it is possible to obtain fruit juice from which the odor has been removed. This high temperature heating also has the effect of sterilizing and sterilizing the fruit juice, and provides the fruit juice with long-term storage.

該加熱後の一次活性炭素入り果汁に対して二次活性
炭素を添加しこれを濾過する工程があること。
There is a step of adding secondary activated carbon to the juice containing the primary activated carbon after heating and filtering this.

高温加熱後のうり臭が除去された果汁は、その高温加熱
に伴ない、いわゆる「こげ臭又はカラメル臭」が付加さ
れる。このカラメル臭を除去するために、更に、「二次
活性炭素を添加し」、カラメル臭が吸着され、しかる後
一次活性炭素及び二次活性炭素が「濾過」により取除か
れ、うり臭もカラメル臭もない西瓜ジュースが得られ
る。
A so-called "burnt or caramel odor" is added to the fruit juice from which the odor has been removed after heating at high temperature, accompanying the high temperature heating. In order to remove this caramel odor, "secondary activated carbon is added" to adsorb the caramel odor, after which the primary activated carbon and secondary activated carbon are removed by "filtration", and the odor is also caramelized. You can get watermelon juice with no odor.

西瓜ジュースとしての濾過に対する発酵調整を行な
う工程があること。
There must be a step of fermentation adjustment for filtration as watermelon juice.

「発酵調整」とは、有機酸(酒石酸,クエン酸,リンゴ
酸等)、重亜硫酸カリウムを添加し、抗菌性を付与する
ことや、各種糖質物の補糖又は酸度の調整等の香味調整
をいう。
"Fermentation adjustment" means adding organic acids (tartaric acid, citric acid, malic acid, etc.) and potassium bisulfite to impart antibacterial properties and adjusting flavors such as supplement sugar or adjustment of acidity of various sugars. Say.

該調整果汁に対して酵母菌を主体とする発酵担体を
添加し醸造する工程があること。
There is a step of brewing by adding a fermentation carrier mainly composed of yeast to the adjusted fruit juice.

〔実施例〕〔Example〕

次に、本発明の実施例を説明する。 Next, examples of the present invention will be described.

(西瓜ジュースの製造法について) まず、西瓜の可食部を破砕し、予備加熱(約95〜98℃)
をして、エキストターにて搾汁した。予備加熱は各種の
果汁の搾汁工程における常套の処理であり、搾汁効果を
高める作用をなす。特に西瓜の搾汁においては同時にう
り臭を軽減する作用もなす。ここに、西瓜の可食部の歩
留りは62.3%、搾汁率は79.1%、搾汁のブリックス度BX
゜は8.2であった。
(About the manufacturing method of watermelon juice) First, crush the edible portion of watermelon and preheat (about 95-98 ℃)
And squeezed with an extractor. Preheating is a conventional treatment in the juice extraction process of various fruit juices, and has the function of enhancing the juice extraction effect. Especially in the squeezing of watermelon, it also acts to reduce the odor. Here, the yield of the edible portion of watermelon is 62.3%, the squeezing rate is 79.1%, and the Brix degree of squeezing BX
The degree was 8.2.

次に、得られた搾汁を冷却し、遠心分離及び濾過による
固液分離処理を施し、清澄果汁(原料果汁)を得た。搾
汁のままでは混濁果汁であり、その残渣の存在がうり臭
の一原因となると考えられることから、清澄果汁を得る
ことが望ましい。ここに、清澄果汁の歩留りは87.6%で
あり、原料西瓜に対して42.6%の清澄果汁が得られた。
ここで、糖組成を液体クロマトグラフィーにより、直接
還元糖を常法により検討した。100ml当りの重量%の清
澄果汁の糖組成は、ブドウ糖1.38%,果糖3.39%,ショ
糖6.97%であり、合計11.74%で、直接還元糖で4.35%
と分析された。この結果によれば、清澄果汁は3つの主
要糖分からなり、無調整で発酵担体による単発酵が可能
であることが分かった。しかし、この清澄果汁のままで
はうり臭が残っており、西瓜ジュースとして供するに
は、積極的にうり臭除去方法を講じる必要がある。
Next, the obtained juice was cooled and subjected to a solid-liquid separation treatment by centrifugation and filtration to obtain a clear juice (raw fruit juice). Since squeezed juice is cloudy fruit juice and the presence of its residue is considered to be one of the causes of odor, it is desirable to obtain clear juice. Here, the yield of clear juice was 87.6%, and 42.6% of clear juice was obtained based on the raw watermelon.
Here, the sugar composition was examined by liquid chromatography, and the direct reducing sugar was examined by a conventional method. The sugar composition of 100% by weight of clear juice is 100% glucose, 3.39% fructose, 6.97% sucrose, 11.74% in total, 4.35% in direct reducing sugar.
Was analyzed. According to these results, it was found that the clarified fruit juice was composed of three main sugars, and simple fermentation with a fermentation carrier was possible without adjustment. However, this clarified fruit juice still has a smelt odor, and it is necessary to actively take a scent removal method in order to use it as watermelon juice.

ところで、うり臭の成分は、カルボニル化合物のアセト
アルデヒド、エナント酸エステル、ヘキシルアルコール
やアミン化合物に属するカプロン酸アルデヒド、メチル
メルカプタン等の混合物とみられているが、これらの物
質をすべて除去することが必要である。そこで、本願に
おける独特の除去方法は、活性炭素の添加と加熱処理を
併用するものであり、活性炭素の吸着を活発にし相乗的
な脱臭効果を発揮させるものである。
By the way, the odorous component is considered to be a mixture of acetaldehyde of carbonyl compound, enanthate ester, hexyl alcohol and caproic acid aldehyde belonging to amine compound, methyl mercaptan, etc., but it is necessary to remove all of these substances. is there. Therefore, the unique removal method in the present application is to use addition of activated carbon and heat treatment in combination to activate the adsorption of activated carbon and exert a synergistic deodorizing effect.

すなわち、清澄果汁300ml容量をオートクレーブ(高温
高圧加熱器)を用いて一次活性炭素の量と加熱条件を変
えて得たデータを明細書末尾の第1表に示す。ここに、
使用した活性炭素は特選白鷺及び白鷺MCL(武田薬品工
業製)で、各場合のうり臭の官能評価を加えた。官能評
価方法は、パネラー8名による極限法で、下降系列の不
可知刺激価をr′、上昇系列の可知刺激価をr″とし、
刺激閾RL=(r′+r″)/2を以って判定する。第1表
中、きき味Iは一次活性炭素の添加及び高温加熱後の果
汁に対するうり臭の官能評価であり、一次活性炭素の使
用量が多く、かつ加熱温度を上げるか又は加熱時間を長
くする程、脱臭の効果が増大することが分かった。ここ
で、下降系列の不可知刺激価r′=8.3,上昇系列の価値
刺激価をr″=10.5で、刺激閾RL=9.4となった。した
がって、少なくともきき味IのNO.10以上、つまり約121
℃−10分間以上の加熱条件の下では一次活性炭素使用量
が500gの場合でもうり臭の除去が遜色なく行われること
が判明した。約121℃−10分間以上の加熱条件は、この
加熱温度及び加熱時間にのみ限定されないことは言う迄
もない。約121℃−10分間の加熱は、熱的に例えば約115
℃−127分間、約125℃−2分間,約130℃−15秒間の加
熱と等価であることに留意すべきである。うり臭の除去
は、一次活性炭素の添加が必須の条件であるが、その吸
着効果は高温加熱によってすこぶる顕著になるのであっ
て、一次活性炭素の多量添加は必ずしも吸着効果を増大
させるとは断定できない。すなわち、実施例によれば、
既に一次活性炭素500gの添加は上記の加熱条件の下では
十分足りていると推測できるからである。
That is, the data obtained by changing the amount of primary activated carbon and the heating conditions by using an autoclave (high-temperature high-pressure heater) in 300 ml of clarified juice are shown in Table 1 at the end of the specification. here,
The activated carbon used was selected Shirasagi and Shirasagi MCL (manufactured by Takeda Pharmaceutical Co., Ltd.), and sensory evaluation of the smell of smelt in each case was added. The sensory evaluation method is a limit method by 8 panelists, where the descending series of ignorant stimulus values is r ′ and the rising series of ignorant stimulus values is r ″,
The stimulus threshold RL = (r ′ + r ″) / 2 is used for determination. In Table 1, Kikimi I is a sensory evaluation of the smell of fruit juice after the addition of primary activated carbon and high temperature heating, and the primary activity It was found that the effect of deodorization increases as the amount of carbon used is increased and the heating temperature is increased or the heating time is increased. The value stimulus value was r ″ = 10.5 and the stimulation threshold RL = 9.4. Therefore, at least Kikimi No. 10 or more, that is, about 121
It was found that under the heating condition of -10 ° C for 10 minutes or more, the odor can be removed without any problem when the amount of primary activated carbon used is 500 g. It goes without saying that the heating conditions of about 121 ° C. for 10 minutes or more are not limited to this heating temperature and heating time. Heating at about 121 ° C. for 10 minutes is thermally performed, for example, at about 115 ° C.
It should be noted that it is equivalent to heating at -127 minutes, about 125-2 minutes, and about 130-15 seconds. The removal of odor is an essential condition for the addition of primary activated carbon, but its adsorption effect becomes extremely remarkable by high temperature heating, so it is concluded that the addition of a large amount of primary activated carbon does not necessarily increase the adsorption effect. Can not. That is, according to the embodiment,
This is because it can be presumed that the addition of 500 g of primary activated carbon is already sufficient under the above heating conditions.

一方、高温加熱に伴うカラメル臭の付加が問題となる。
高温加熱はうり臭の短時間脱臭を達成するが、反面、カ
ラメル臭の付加による品質の劣化を招く。かかるカラメ
ル臭の除去方法は、加熱後の一次活性炭素入り果汁に対
して二次活性炭素を添加するもので、二次活性炭素の使
用量を変えて得たデータを第1表に示す。カラメル臭に
対する官能評価(きき味II)を加えた。評価方法はうり
臭の方法と同じで、加熱条件が最大で二次活性炭素使用
量が500gの場合をきき味IIのNO.1とした。この結果、き
き味IIの下降系列の不可知刺激価r′=7、上昇系列の
価値刺激価r″=9.8で、刺激閾RL=8.4となった。した
がって、少なくともきき味IIのNO.9以上、つまり、加熱
条件約121℃−10分間で、二次活性炭素使用量が2000gの
場合にはカラメル臭を払拭できると言える。カラメル臭
を除去しうる二次活性炭素の最小使用量は、第1表が示
唆するように、一次活性炭素使用量と相関関係にあると
推察される。一次活性炭素使用量がうり臭除去に十分な
量であれば、高温加熱中にもそれによるカラメル臭を吸
着するであろうから、二次活性炭素使用量は必然的に少
なくて済む。加熱条件約121℃−10分間で、一次活性炭
素使用量2000g,二次活性炭素使用量2000gの場合からそ
れを推察できる。逆に、一次活性炭素使用量がうり臭除
去にほとんど費やされた場合には、二次活性炭素使用量
を多量添加する必要がある。これは加熱条件約121℃−1
0分間で、一次活性炭素使用量500g,二次活性炭素使用量
2000gの場合から推察できる。しかし、加熱条件役121℃
−10分間で、一次活性炭素使用量500g,二次活性炭素使
用量500gの場合にも、うり臭及びカラメル臭が共に除去
されている事実から、カラメル臭の除去には二次活性炭
素使用量500gで足りると言えよう。
On the other hand, the addition of caramel odor associated with high temperature heating poses a problem.
High-temperature heating achieves short-time deodorization of odor, but on the other hand, it causes deterioration of quality due to addition of caramel odor. In this method of removing caramel odor, secondary activated carbon is added to fruit juice containing primary activated carbon after heating, and Table 1 shows data obtained by changing the amount of secondary activated carbon used. A sensory evaluation for caramel odor (Kikimi II) was added. The evaluation method is the same as that of the smelt odor, and the case where the heating condition is maximum and the amount of secondary activated carbon used is 500 g is defined as No. 1 of the KIKI II. As a result, the ignorance stimulus value r '= 7 in the descending series of Kikimi II and the value stimulus value r "= 9.8 in the ascending series, and the stimulation threshold RL = 8.4. In other words, it can be said that the caramel odor can be wiped off when the amount of secondary activated carbon used is 2000 g under heating conditions of about 121 ° C. for 10 minutes The minimum amount of secondary activated carbon that can remove the caramel odor is It is inferred that there is a correlation with the amount of primary activated carbon used, as suggested by Table 1. If the amount of primary activated carbon used is sufficient to remove the odor, the caramel odor caused by it may be increased during high temperature heating. The amount of secondary activated carbon used is inevitably small, since the amount of primary activated carbon used is 2000 g and the amount of secondary activated carbon used is 2000 g at heating conditions of about 121 ° C for 10 minutes. On the contrary, the amount of primary activated carbon used is mostly spent to remove the odor. In this case, it is necessary to addition of a large amount of secondary activated carbon usage. This heating conditions about 121 ° C. -1
In 0 minutes, primary activated carbon usage 500g, secondary activated carbon usage
It can be inferred from the case of 2000 g. However, heating condition role 121 ℃
Even if the primary activated carbon usage amount is 500 g and the secondary activated carbon usage amount is 500 g in 10 minutes, both the odor and caramel odor are removed. You can say that 500g is enough.

したがって、本実施例からきき味I及びきき味IIを総合
すると、うり臭及びカラメル臭を駆逐できる条件は、加
熱条件が約121℃−10分間で、一次活性炭素の最小使用
量は一応500gとみることができ、二次活性炭素の最小使
用量も一応500gとみることができる。しかし、本実施例
においては活性炭素は特選白鷺及び白鷺MCL(武田薬品
工業製)を使用したが、他の各種の活性炭素に対して、
脱臭に必要十分な使用量は上記のデータと若干異なるこ
ととなるので、活性炭素の最小使用量は上記実施例に限
定されるものでないことに留意されたい。
Therefore, when the Kiki Taste I and Kiki Taste II are combined from this Example, the conditions for being able to drive out the odor and caramel odor are heating conditions of about 121 ° C. for 10 minutes, and the minimum amount of primary activated carbon used is 500 g. It can be seen that the minimum amount of secondary activated carbon used is tentatively 500 g. However, in the present example, the activated carbon used was selected Shirasagi and Shirasagi MCL (manufactured by Takeda Pharmaceutical Co., Ltd.).
It should be noted that the minimum amount of activated carbon used is not limited to the above examples, since the amount required and sufficient for deodorization will be slightly different from the above data.

約121℃−10分間の加熱条件で得た果汁を濾過して活性
炭素を分離し、うり臭及びカラメル臭もない西瓜ジュー
スを得たが、活性炭素使用及び高温加熱の如何に伴う成
分面での影響を検討した。第1表において、T.Aは酸度,
A.Aはアミノ酸度,D.R.Sは直接還元糖を示すが、ほとん
ど変動は認められなかった。
The fruit juice obtained under heating conditions of about 121 ° C. for 10 minutes was filtered to separate the active carbon, and a watermelon juice with no odor or caramel odor was obtained, but in terms of the components associated with the use of activated carbon and high temperature heating. I examined the effect of. In Table 1, TA is acidity,
AA showed amino acid content, and DRS showed direct reducing sugar, but almost no change was observed.

(西瓜ワイン製造法について) 約121℃−10分間の加熱条件で、一次活性炭素使用量500
g及び二次活性炭素使用量500gで得た西瓜ジュースを用
い西瓜ワイン製造法について検討した。かかる原料西瓜
ジュースのブリックス度BX゜は9.4で、無調整で発酵担
体による単発酵が可能である。高いアルコール度の西瓜
ワインを得る場合には、補糖を行なう必要がある。本実
施例では、アルコール発酵における雑菌に対する抗菌性
を促すためにメタカリ(重亜硫酸カリウム)を100ppm添
加し原料果汁とした。なお、抗菌性の付与として有機酸
(酒石酸,クエン酸,リンゴ酸等)の添加も可能であ
る。
(About watermelon wine manufacturing method) Primary activated carbon consumption 500 at heating temperature of about 121 ℃ -10 minutes
The production method of watermelon wine was investigated by using watermelon juice obtained with g and secondary activated carbon amount of 500g. The raw watermelon juice has a Brix degree BX ° of 9.4, which allows unfermented fermentation using a fermentation carrier. In order to obtain high-alcohol watermelon wine, it is necessary to supplement sugar. In this example, 100 ppm of meta potassium (potassium bisulfite) was added to the raw material juice in order to promote antibacterial activity against various bacteria in alcohol fermentation. It is also possible to add an organic acid (tartaric acid, citric acid, malic acid, etc.) to impart antibacterial properties.

発酵担体である酵母菌としては、財団法人日本醸造協会
販売の酒用協会酵母3号(W−3号),酒用協会酵母7
号(K−7号),酒用協会酵母9号(K−9号)を用い
た。
As yeasts which are fermentation carriers, sake association yeast 3 (W-3) sold by the Japan Brewing Association, sake yeast 7
No. (K-7) and Sake Association Yeast No. 9 (K-9) were used.

まず、上記発酵調整をした原料果汁100mlにそれぞれ上
記3種類の酵母菌を接種して28℃にて2日間発酵を行な
い、酒母の調整をした。次に、原料果汁400mlにそれぞ
れ各酒母40mlを添加し、25℃にて5日間発酵を行ない、
西瓜ワインを得た。原料果汁及び各西瓜ワインの成分を
明細書末尾の第2表に示す。
First, 100 ml of the above-prepared raw material juice was inoculated with each of the above-mentioned three types of yeast and fermented at 28 ° C. for 2 days to prepare a mother of liquor. Next, add 40 ml of each liquor to 400 ml of raw juice and ferment for 5 days at 25 ° C.
I got gourd wine. The ingredients of the raw juice and each watermelon wine are shown in Table 2 at the end of the specification.

第2表から明らかなように、原料果汁の糖質物の約98%
以上が発酵し、相応のアルコール分が製成された。残糖
分は直接還元糖として僅かに残った。各西瓜ワインは勿
論うり臭及びカラメル臭もない芳醇な果実酒で、使用酵
母菌の種類の相違から、醸された各西瓜ワインはそれそ
れ香味に特徴のある良好なものであった。
As is clear from Table 2, about 98% of the sugar content of the raw fruit juice
The above was fermented to produce a corresponding amount of alcohol. A small amount of residual sugar remained as direct reducing sugar. Of course, each watermelon wine is a rich fruit wine without smelling or caramel odor, and each watermelon wine brewed was a good one with its own flavor due to the difference in the type of yeast used.

(西瓜ブランデーの製造法) 上記約121℃−10分間の加熱条件で、一次活性炭素使用
量500g及び二次活性炭素使用量500gで得た西瓜ジュース
を発酵調整として、酒石酸を添加してpH4.25とし、原料
西瓜ワイン10.8Lを得た。財団法人日本醸造協会販売の
酒用協会酵母3号(W−3号)を使用し、予め香味調整
した西瓜ワインの10%を用いて、28℃にて3日間発酵さ
せ酒母を造った。この酒母を用いて全原料果汁について
25℃にて6日間発酵させて、原料西瓜ワインを得た。
(Production method of watermelon brandy) Under the heating conditions of about 121 ° C. for 10 minutes, the watermelon juice obtained at a primary activated carbon usage amount of 500 g and a secondary activated carbon usage amount of 500 g was used as a fermentation adjustment, and tartaric acid was added to pH 4. The raw material watermelon wine 10.8L was obtained. Using Sake Association Yeast No. 3 (W-3) sold by the Japan Brewing Association, 10% of the watermelon wine whose flavor was adjusted beforehand was fermented at 28 ° C. for 3 days to prepare a sake mother. About all the raw juices using this sake mother
Fermentation was carried out at 25 ° C. for 6 days to obtain a raw watermelon wine.

この原料西瓜ワインについて、ポットスチル型蒸留装置
(20L容,銅合金製)で蒸留を行ない、粗留液3.7Lを得
た。更に、この粗留液についてポットスチル型蒸留装置
(3L容,ガラス製)で再蒸留を行ない西瓜ブランデー
(アルコール分73%,0.5L)を醸出した。原料西瓜ワイ
ン及び西瓜ブランデーの成分を明細書末尾の第3表に示
す。
The raw watermelon wine was distilled using a pot still type distillation apparatus (20 L capacity, made of copper alloy) to obtain 3.7 L of a crude distillate. Further, this crude distillate was redistilled with a pot still type distillation apparatus (3 L, glass) to produce watermelon brandy (alcohol content 73%, 0.5 L). The ingredients of the raw watermelon wine and watermelon brandy are shown in Table 3 at the end of the specification.

この西瓜ブランデーにおいては、勿論官能的には原料特
性のうり臭は認められず、香味的に蒸留酒に移行したフ
ルーティーの香りやマイルドな味を呈する。
In this watermelon brandy, of course, the odor of the raw material characteristic is not sensually recognized, and it has a fruity aroma and mild taste, which is flavorfully converted to distilled liquor.

〔発明の効果〕〔The invention's effect〕

以上説明したように、本発明に係る西瓜ワインの製造法
は、原料特性のうり臭の除去方法に特徴を有するもので
あり、清澄果汁に対して一次活性炭素を添加した後所定
の加熱条件の下で加熱する高温加熱工程を以ってうり臭
を除去し、高温加熱工程により付与されるカラメル臭を
二次活性炭素の添加により除去するものであるから、次
の効果を奏する。
As described above, the method for producing watermelon wine according to the present invention is characterized by the method of removing the odor of the raw material characteristics, and after adding the primary activated carbon to the clarified juice, the temperature of the predetermined heating conditions is increased. Since the odor is removed by the high temperature heating step of heating below, and the caramel odor imparted by the high temperature heating step is removed by the addition of secondary activated carbon, the following effects are exhibited.

すなわち、かかる製造法によれば、高価な真空装置の設
備を不要として、うり臭のない西瓜ワインのための西瓜
ジュースを迅速かつ安価に量産でき、西瓜ワインの商品
化が実現できる。また、食用に供し得ない西瓜の利用を
図ることができる。高温加熱工程にかかった清澄果汁
(西瓜ジュース)は減菌,殺菌処理が同時に施される結
果、後続工程までの保存性が保障されるので、食品衛生
面で利点がある。特に、醸造工程においてうり臭の除去
に考慮する必要がなく、常套の醸造工程を採用している
から、従来の果実酒の製造設備を利用できる。
That is, according to such a manufacturing method, it is possible to mass-produce the watermelon juice for the watermelon wine without the smell of odor quickly and inexpensively without the need for an expensive vacuum device, and to commercialize the watermelon wine. In addition, it is possible to use watermelon that cannot be used for food. The clarified juice (watermelon juice) that has been subjected to the high temperature heating process is subjected to sterilization and sterilization at the same time, and as a result, its preservability up to the subsequent process is guaranteed, which is advantageous in food hygiene. In particular, since it is not necessary to consider the removal of the smell of odor in the brewing process and the conventional brewing process is adopted, conventional equipment for producing fruit wine can be used.

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】西瓜の可食部を破砕し予備加熱をして搾汁
する搾汁工程と、該搾汁の固液分離処理により清澄果汁
を得る工程と、該清澄果汁に対して一次活性炭素を添加
した後、115〜130゜C,15秒間〜127分間の範囲内でうり
臭を除去し得る加熱条件の下で加熱する高温加熱工程
と、該加熱後の一次活性炭素入り果汁に対して二次活性
炭素を添加しこれを濾過する工程と、該濾液に対する発
酵調整を行なう工程と、該調整果汁に対して酵母菌を主
体とする発酵担体を添加し醸造する工程と、を有するこ
とを特徴とする西瓜ワインの製造法。
1. A squeezing step of crushing the edible portion of watermelon and squeezing it by preheating, a step of obtaining a clear juice by solid-liquid separation treatment of the juice, and a primary activity against the clear juice. After adding carbon, a high temperature heating step of heating under a heating condition capable of removing the odor in the range of 115 to 130 ° C for 15 seconds to 127 minutes, and to the juice containing primary activated carbon after the heating Secondary activated carbon is added and filtered, the step of performing fermentation adjustment on the filtrate, and the step of brewing by adding a fermentation carrier mainly composed of yeast to the adjusted fruit juice. A method for producing watermelon wine characterized by.
JP19121086A 1986-08-15 1986-08-15 Watermelon wine manufacturing method Expired - Lifetime JPH0673446B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP19121086A JPH0673446B2 (en) 1986-08-15 1986-08-15 Watermelon wine manufacturing method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP19121086A JPH0673446B2 (en) 1986-08-15 1986-08-15 Watermelon wine manufacturing method

Publications (2)

Publication Number Publication Date
JPS6349060A JPS6349060A (en) 1988-03-01
JPH0673446B2 true JPH0673446B2 (en) 1994-09-21

Family

ID=16270737

Family Applications (1)

Application Number Title Priority Date Filing Date
JP19121086A Expired - Lifetime JPH0673446B2 (en) 1986-08-15 1986-08-15 Watermelon wine manufacturing method

Country Status (1)

Country Link
JP (1) JPH0673446B2 (en)

Families Citing this family (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH04152869A (en) * 1990-10-17 1992-05-26 Kazuyuki Masuzawa Watermelon juice
KR100424043B1 (en) * 2001-06-22 2004-03-22 전라북도(농업기술원) Waterm elon wine using saccharomyces sp. kws06 and method for the preparation of it
JP2005021032A (en) * 2003-06-30 2005-01-27 Tadao Hiroi Method for producing fruit honey liquor
WO2005042691A1 (en) * 2003-10-31 2005-05-12 Suntory Limited Process for producing cloudy fruit wine
CN101868156B (en) * 2007-11-16 2014-03-12 协和发酵生化株式会社 Citrulline-containing drink
JP4927114B2 (en) * 2009-02-26 2012-05-09 佐藤 誠 Beverage production method and beverage
KR101073830B1 (en) 2011-06-21 2011-10-14 성숙자 Manufacturing method of watermelon makgeolri
CN103005555A (en) * 2012-12-11 2013-04-03 石河子大学 Method for processing seed melon condensed juice
JP6244564B2 (en) * 2013-12-25 2017-12-13 山形県 Method for reducing odor of fruit juice of cucurbitaceae fruit or processed product of pulverized pulp and method of manufacturing processed cucurbitaceae fruit
CN104357280B (en) * 2014-11-20 2017-10-10 新疆冰雪果业有限责任公司 A kind of preparation method of melon wine

Also Published As

Publication number Publication date
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