JPH03143379A - Production of semitransparent fruit juice - Google Patents

Production of semitransparent fruit juice

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Publication number
JPH03143379A
JPH03143379A JP1279948A JP27994889A JPH03143379A JP H03143379 A JPH03143379 A JP H03143379A JP 1279948 A JP1279948 A JP 1279948A JP 27994889 A JP27994889 A JP 27994889A JP H03143379 A JPH03143379 A JP H03143379A
Authority
JP
Japan
Prior art keywords
juice
fruit
fruit juice
enzyme
turbidity
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
JP1279948A
Other languages
Japanese (ja)
Other versions
JP2649587B2 (en
Inventor
Tadaaki Wakayama
忠明 若山
Katsumi Horikawa
堀川 勝身
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.)
KITSUKOO SHOKUHIN KOGYO KK
Original Assignee
KITSUKOO SHOKUHIN KOGYO KK
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Application filed by KITSUKOO SHOKUHIN KOGYO KK filed Critical KITSUKOO SHOKUHIN KOGYO KK
Priority to JP1279948A priority Critical patent/JP2649587B2/en
Publication of JPH03143379A publication Critical patent/JPH03143379A/en
Application granted granted Critical
Publication of JP2649587B2 publication Critical patent/JP2649587B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Abstract

PURPOSE:To obtain the subject fruit juice, having suitable tastiness essential to a fruit and light throat passableness with hardly any precipitation of suspended particles by adding an enzyme to a pressed juice of the fruit and regulating the resultant juice so as to provide a specific turbidity after clarifying treatment. CONSTITUTION:An enzyme (e.g. pectin hydrolase) is added to a pressed juice of a fruit to carry out clarifying treatment. In the process, the juice is regulated so as to provide 0.03-0.05 turbidity expressed in terms of absorbance at 600-800nm light wavelength after the clarifying treatment and afford the objective fruit juice. Furthermore, the clarifying treatment is preferably performed at 5-15 deg.C for 5-90min, etc., in the case of a batch method and the amount of the enzyme is preferably 1-50mg based on 100g fruit juice.

Description

【発明の詳細な説明】 本発明は、果実本来のうま味やコク味を適度に有し、喉
ごしが軽く、しかも懸濁粒子の沈殿が殆どない半透明果
汁の製造法に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for producing translucent fruit juice that has an appropriate amount of umami and richness inherent to fruit, is easy to swallow, and has almost no precipitation of suspended particles.

従来製造されている果汁は、混濁果汁タイプと透明果汁
タイプの2種が知られている。
There are two types of fruit juices that are conventionally produced: cloudy fruit juice type and transparent fruit juice type.

混濁果汁タイプは、バルブ成分を多く含んでいる為に、
官能的には果実本来のうま味やコク味を有するが、喉ご
しか重く、しかも貯蔵中に懸濁粒子或いは果実組織の微
細片が沈殿し、果汁部との明らかな分離を生ずる問題が
ある。
The cloudy juice type contains a lot of valve components, so
Sensually, it has the umami and richness inherent to fruit, but it is heavy to swallow, and there is a problem in that suspended particles or fine pieces of fruit tissue settle during storage, resulting in obvious separation from the fruit juice.

一方、透明果汁タイプは、貯蔵中に懸濁粒子或いは果実
組織の微細片が沈殿することは無いが、果実が本来有す
るうま味やコク味を失う問題点を有する。
On the other hand, the transparent fruit juice type does not allow suspended particles or fine pieces of fruit tissue to precipitate during storage, but has the problem of losing the umami and richness inherent in the fruit.

そこで本発明者等は、上記のような混濁果11及び透明
果汁の如き問題点を有しない、全く新しいタイプの果汁
を得ることを目的として種々検討を重ねた結果、果実の
圧搾液汁に酵素を添加して清澄処理するに当り、該清澄
処理後の濁度が光波長600〜800 nmにおける1
0mmセルの吸光度で003〜0.50となるように調
整するときは、得られる果汁が明るい色調を有し、果実
が本来性するうま味やコク味を適度に有して、喉ごしが
軽く、しかも懸濁粒子の沈殿が殆どない半透明の果汁が
得られることを知り、この知見に基づいて本発明を完成
した。
Therefore, the present inventors conducted various studies with the aim of obtaining a completely new type of fruit juice that does not have the problems of cloudy fruit 11 and transparent fruit juice as described above, and as a result, they added an enzyme to the pressed fruit juice. When adding and performing clarification treatment, the turbidity after the clarification treatment is 1 at a light wavelength of 600 to 800 nm.
When adjusting the absorbance of a 0mm cell to 0.03 to 0.50, the resulting fruit juice will have a bright color, have a moderate amount of umami and richness inherent in the fruit, and will be easy to swallow. Moreover, the present invention was completed based on this knowledge, and it was found that translucent fruit juice with almost no sedimentation of suspended particles could be obtained.

即ち本発明は、果実の圧搾液汁に酵素を添加して清澄処
理するに当り、該清澄処理後の濁度か光波長600〜8
00 nmにおける 10mmセルの吸光度で003〜
050となるように調整することを特徴とする半透明果
汁の製造法である。
That is, in the present invention, when an enzyme is added to the squeezed fruit juice for clarification, the turbidity after the clarification is adjusted to a light wavelength of 600 to 8.
Absorbance of 10mm cell at 00nm is 003~
This is a method for producing translucent fruit juice, which is characterized in that the juice is adjusted so that the juice becomes 0.050.

以下、本発明を具体的に説明する。The present invention will be specifically explained below.

先ず、本発明で用いられる原料の果実は特に制限はなく
、具体的にはリンゴ、パイナツプル、バナナ、ナシ、桃
、プラム、あんず、ブドウ、柑橘類等が挙げられる。
First, there are no particular restrictions on the fruits used as raw materials in the present invention, and specific examples include apples, pineapple, bananas, pears, peaches, plums, apricots, grapes, and citrus fruits.

これらは充分洗浄し、ハンマーミルやディスインチグレ
ーター等の破砕機により破砕した後、パルパー、フィニ
ッシャ−、スクリュープレス及び水圧圧搾機(プレス機
)等の圧搾機により搾汁して果汁を製造する。尚、果実
を破砕する際に、果実中の酸化酵素類によって果肉及び
果汁が褐変することを防止する為、L−アスコルビン酸
等の酸化防止剤を添加することが好ましい。
These are sufficiently washed and crushed using a crusher such as a hammer mill or a disinching grater, and then squeezed using a compressor such as a pulper, finisher, screw press, or hydraulic press to produce fruit juice. In addition, when crushing the fruit, it is preferable to add an antioxidant such as L-ascorbic acid in order to prevent the pulp and fruit juice from turning brown due to oxidative enzymes in the fruit.

次に、上記のようにして得られた果汁はそのままで、或
いはこの果汁を60〜100℃で5〜30分加熱して、
果汁に内在する酵素類を失活せしめたのち、酵素を添加
して部分清澄処理する。
Next, the fruit juice obtained as described above is used as it is, or this fruit juice is heated at 60 to 100°C for 5 to 30 minutes,
After deactivating the enzymes present in the fruit juice, enzymes are added to partially clarify the fruit juice.

ここに用いられる酵素としては、ペクチン分解酵素剤、
セルロース分解酵素剤、デンプン分解酵素剤、タンパク
分解酵素剤及びこれらの酵素剤を色々と組み合わせた混
合酵素剤等が挙げられる。
Enzymes used here include pectin-degrading enzymes,
Examples include cellulolytic enzymes, amylolytic enzymes, proteolytic enzymes, and mixed enzymes containing various combinations of these enzymes.

尚、上記処理において、凝集剤を併用すると酵素剤の使
用量が節約でき、また効率良く清澄処理ができるので好
ましい。ここに用いられる凝集剤としては、ゼラチン、
キトサン、カゼイン等及びこれらの凝集剤とクエン酸や
リンゴ酸等の有機酸を組合せた混合凝集剤が挙げられる
In the above treatment, it is preferable to use a flocculant in combination because the amount of enzyme agent used can be saved and the clarification treatment can be carried out efficiently. The flocculants used here include gelatin,
Examples include chitosan, casein, etc., and mixed flocculants made by combining these flocculants with organic acids such as citric acid and malic acid.

部分清澄処理の時間は、前述した所定の濁度が得られる
ように調整され、通常回分式の場合5〜15℃で5〜9
0分、連続式の場合35〜450Cで3〜90秒の間で
選択される。なお、使用する酵素の量は果汁100gに
対して1〜50mgとすることが好ましい。
The time for the partial clarification treatment is adjusted so as to obtain the predetermined turbidity described above, and in the case of a batch method, the time for the partial clarification treatment is usually 5 to 9 degrees Celsius at 5 to 15 degrees Celsius.
0 minutes, and in the case of continuous type, it is selected between 35 to 450C and 3 to 90 seconds. Note that the amount of enzyme used is preferably 1 to 50 mg per 100 g of fruit juice.

本発明において、清澄処理後の果汁の濁度を003〜0
50とすることは極めて重要である。
In the present invention, the turbidity of fruit juice after clarification is set to 003 to 0.
Setting the value to 50 is extremely important.

即ち、濁度が0403未満であるときは果実が本来有す
るうま味やコク味を失う問題点を有し、また反対に0.
50を超えると懸濁粒子の沈殿が生ずるので好ましくな
い。これに対し、濁度が」二記範囲内にあるときは、果
実本来のうま味やコク味を適度に有して、喉ごしが軽く
、しかも懸濁粒子の沈殿が殆どない半透明の果汁が得ら
れる。
That is, when the turbidity is less than 0.403, there is a problem in that the umami and richness inherent in the fruit are lost;
If it exceeds 50, precipitation of suspended particles will occur, which is not preferable. On the other hand, when the turbidity is within the range specified in ``2'', the fruit juice has a moderate amount of umami and richness inherent to the fruit, is easy to swallow, and is translucent with almost no sedimentation of suspended particles. is obtained.

尚、上記濁度は光波長600〜800 nmにおける1
0mmセルの吸光度で測定した値である。
In addition, the above turbidity is 1 at a light wavelength of 600 to 800 nm.
This is a value measured by absorbance of a 0 mm cell.

以下、半透明果汁の濁度と貯蔵安定性について実験例を
挙げて説明する。
The turbidity and storage stability of translucent fruit juice will be explained below using experimental examples.

実験例1 後記実施例1及び2の半透明果汁の製造法において、酵
素反応時間を調節する以外は、はぼ同様に処理して、種
々の濁度を有する半透明果汁を調製し、35℃下に貯蔵
して、経口的に沈殿の生成の有無を肉眼で観察し、沈殿
に対する安定性を調べた。その結果を第1表及び第2表
に示す。
Experimental Example 1 Translucent fruit juices with various turbidities were prepared in the same manner as in the method for producing translucent fruit juice in Examples 1 and 2 described below, except that the enzyme reaction time was adjusted, and the translucent fruit juices were heated at 35°C. The stability against precipitation was examined by orally observing the presence or absence of precipitate with the naked eye. The results are shown in Tables 1 and 2.

第 表 (リンゴ半透明果汁の濁度と貯蔵安定性)(注)(1) 濁度; 60 0m における 0 mmセルの吸 光度 (2) 沈殿物含有の有無は、 調整した半透明す ンゴ果汁を95℃まで加熱してビンに充填し徐冷した後
、35°Cの恒温室で10日間、経時的に肉眼観察し、
結果はマイナス(=)、プラス(+)で表示した。表中
の記号−は沈殿物の生成なし、+は沈殿物が生成するこ
とを示す。
Table (Turbidity and storage stability of semi-transparent apple juice) (Note) (1) Turbidity; Absorbance of 0 mm cell at 600 m (2) The presence or absence of precipitates is determined by measuring the prepared semi-transparent apple juice. After heating to 95°C, filling into bottles and slowly cooling, visually observing over time in a constant temperature room at 35°C for 10 days,
The results were displayed as minus (=) and plus (+). The symbol - in the table indicates that no precipitate is formed, and the symbol + indicates that a precipitate is formed.

第 表 (パインアップル半透明果汁の濁度と貯蔵安定性)(注
)(1) 濁度; 60 nm における 0 mmセルの吸 光度 (2) 沈殿物含有の有無は、 調整した半透明パ インアップル果汁を 5 0Cまで加熱して ビンに充填し徐冷した後、35℃の恒温室で10日間、
経時的に肉眼観察し、結果はマイナス(−)、プラス(
+)で表示した。表中の記号−は沈殿物の生成なし、+
は沈殿物が生成することを示す。
Table (Turbidity and storage stability of translucent pineapple juice) (Note) (1) Turbidity; Absorbance of 0 mm cell at 60 nm (2) The presence or absence of precipitate is determined by the prepared translucent pineapple juice. After heating it to 50C, filling it in a bottle and slowly cooling it, it was kept in a constant temperature room at 35C for 10 days.
Observe with the naked eye over time, and the results are negative (-) and positive (
Indicated by +). The symbol - in the table indicates no precipitation, +
indicates that a precipitate is formed.

以上の結果から、果汁の濁度を050以下とすると、3
5°CでlO日日間貯蔵(室温に於ける1ケ月貯蔵に相
当)で目立った沈殿物の生成が見られず安定であること
が判る。
From the above results, if the turbidity of fruit juice is set to 050 or less, 3
It can be seen that the product is stable with no noticeable precipitate formed even after storage for 10 days at 5°C (corresponding to storage for 1 month at room temperature).

次に、このように部分清澄処理した果汁は、果実本来の
諸酵素類又は添加した酵素剤の活性を失活する為、60
〜100℃に加熱し、冷却した後そのまま、又はこれに
ゼラチン、その他の凝集剤を添加した後、高速の遠心処
理(例えば3,000〜to、000 G、  5〜2
0秒)又は振動篩等で、粗い不溶性の懸濁粒子を除去す
る。
Next, the fruit juice partially clarified in this way is heated to a 60%
After heating to ~100°C and cooling, the gelatin or other flocculant is added thereto, followed by high-speed centrifugation (e.g., 3,000 to 1,000 G, 5 to 2
0 seconds) or with a vibrating sieve to remove coarse insoluble suspended particles.

次に、得られた果汁を、そのままか、又は濾布、濾過綿
等によって粗く濾過し、濾液中に不溶性で微細な懸濁粒
子を一部残存させた、濁度が0.03〜0.50である
果汁を得、これをそのまま、又は加熱殺菌して、本発明
製品を得る。
Next, the obtained fruit juice is directly filtered or coarsely filtered using a filter cloth, filter cotton, etc., and the turbidity is 0.03 to 0.0. 50 is obtained, and the product of the present invention is obtained as it is or by heat sterilizing it.

以上、説明したことから明らかなように、本発明は果実
の圧搾液汁に酵素を添加して清澄処理するに当り、該清
澄処理後の濁度が光波長600〜800 nmにおける
10mmセルの吸光度で0,03〜050どなるように
調整するものであるから、果汁が明るい色調を有し、果
実が本来有するうま味やコク味を適度に有して、喉ごし
が軽く、しかも長期間の貯蔵に於いても著しいパルプ部
と」二澄液の分離を生ぜず、安定した半透明果汁を得る
ことができる。
As is clear from the above explanation, in the present invention, when an enzyme is added to the squeezed fruit juice for clarification, the turbidity after the clarification is determined by the absorbance of a 10 mm cell at a light wavelength of 600 to 800 nm. 0.03 to 050, the fruit juice has a bright color tone, has the right amount of umami and richness inherent in the fruit, is easy to swallow, and can be stored for a long time. Even in this case, a stable translucent fruit juice can be obtained without significant separation between the pulp part and the clear liquid.

以下、実施例を示して本発明をより具体的に説明する。Hereinafter, the present invention will be described in more detail with reference to Examples.

実施例1 フジ種のリンゴ果実3 kgを洗浄、選別した後、破砕
、搾汁して搾汁液2 kgを得た。破砕機はフードブロ
ッセサーを、搾汁機としてフィルタープレスを用いた。
Example 1 After washing and sorting 3 kg of Fuji apple fruits, they were crushed and squeezed to obtain 2 kg of squeezed liquid. A food brother was used as the crusher, and a filter press was used as the juice extractor.

この搾汁液を40℃まで加温した後、ペクチン分解酵素
剤の濃度が搾汁液に対して50■%となる様に酵素液を
添加し良く攪拌した。
After the juice was heated to 40° C., an enzyme solution was added so that the concentration of the pectin-degrading enzyme agent was 50% based on the juice, and the mixture was thoroughly stirred.

この反応液を40°Cで保持し、1分、2分及び3分後
にサンプリングした。サンプル液を直ちに98°Cまで
加熱し、急速冷却した。次に遠心分離機で不溶性物質を
除去した後、上澄液の660 nmにおける吸光度を測
定した。その結果を図1に示した。この予備試験結果か
ら、搾汁液を40°Cまで加温し、ペクチン分解酵素剤
を50■%となる様に酵素液を添加し、60秒間反応す
ると予想される半透明果汁のA660 nmは0054
であった。
The reaction solution was kept at 40°C and sampled after 1, 2 and 3 minutes. The sample solution was immediately heated to 98°C and rapidly cooled. Next, after removing insoluble substances using a centrifuge, the absorbance of the supernatant at 660 nm was measured. The results are shown in Figure 1. From this preliminary test result, the A660 nm of the translucent fruit juice, which is expected to react for 60 seconds by heating the juice to 40°C and adding an enzyme solution to make the pectin-degrading enzyme agent 50%, is 0054.
Met.

この様にして得られた酵素反応条件を用いて、半透明果
汁を得た。その実施例を以下に示す。フジ種のリンゴ果
実1.00 kgを洗浄、選別した後、破砕、搾汁して
搾d−液72kgを得た。破砕機はハンマーミル、搾汁
機としてフィルタープレスを用いた。この搾汁液を温水
循環式チューブヒーターに投入する事で液温を40°C
まで上昇した。ここにペクチン分解酵素剤の溶液をマイ
クロチューブポンプで連続的に添加した。酵素濃度は搾
汁l夜に対して5.0mg%となる様に調整した。酵素
液を1 添加した後、スタテックミキサ一部を経てホールデング
部に輸送し、ここで60秒間保持した後、それを98℃
に加熱し、冷却した。続いてその液を連続遠心分離機に
輸送し、大部分の不溶性物質を除去した。次に濾過綿を
充填した濾過機で更に微細な不溶性物質を除去し、常法
にて殺菌し最終製品を得た。
Translucent fruit juice was obtained using the enzyme reaction conditions thus obtained. Examples thereof are shown below. After washing and sorting 1.00 kg of Fuji apple fruits, they were crushed and squeezed to obtain 72 kg of squeezed d-liquid. A hammer mill was used as the crusher, and a filter press was used as the juice extractor. By putting this squeezed liquid into a hot water circulation type tube heater, the liquid temperature is raised to 40°C.
It rose to A solution of a pectin-degrading enzyme agent was continuously added thereto using a microtube pump. The enzyme concentration was adjusted to 5.0 mg% per squeezed juice. After adding 1 part of the enzyme solution, it is transported through a part of the static mixer to the holding section, where it is held for 60 seconds, and then heated to 98°C.
and cooled. The liquid was then transferred to a continuous centrifuge to remove most of the insoluble material. Next, fine insoluble substances were removed using a filter filled with filter cotton, and the product was sterilized in a conventional manner to obtain a final product.

一方、−船釣に行なわれている方法に従って、同一果実
50kgにI7−アスコルビン酸を添加しながら、破砕
、搾汁して混濁果/(−33kgを得た。これを〔対照
区1〕とする。
On the other hand, according to the method used for boat fishing, 50 kg of the same fruit was crushed and squeezed while adding I7-ascorbic acid to obtain 33 kg of cloudy fruit. do.

また、同一果実50kgを破砕、搾汁して、搾汁液にペ
クチン分解酵素剤を添加して、酵素的清澄化を行ない清
澄果汁36kgを得た。これを(対照区2)とする。
Further, 50 kg of the same fruit was crushed and juiced, and a pectin-degrading enzyme agent was added to the squeezed juice for enzymatic clarification to obtain 36 kg of clarified fruit juice. This will be referred to as (control area 2).

得られたこれらの果汁の分析結果を第3表に示す。Table 3 shows the analysis results of these fruit juices obtained.

2 3 実施例2 パインアップル果実3 kgを洗浄した後、果皮をパイ
ンピラーで取り除き破砕、搾汁して搾汁液1、.5kg
を得た。破砕機はフードプロッセサーを、搾汁機として
フィニッシャ−を用いた。この搾汁液を400Cまで加
温した後、ペクチン分解酵素剤の濃度が搾汁液に対して
10.0■%となる様に酵素液を添加し、更にゼラチン
の濃度が搾汁液に対して0.5 mg%となる様に添加
し良く攪拌した。
2 3 Example 2 After washing 3 kg of pineapple fruit, the skin was removed with a pine pillar, crushed, and squeezed to obtain squeezed liquid 1, . 5kg
I got it. A food processor was used as the crusher, and a finisher was used as the juice extractor. After heating this juice to 400C, an enzyme solution was added so that the concentration of pectin-degrading enzyme agent was 10.0% based on the juice, and the concentration of gelatin was 0.0% relative to the juice. It was added to a concentration of 5 mg% and stirred well.

この反応液を40℃で保持し、1分、2分3分及び4分
後にサンプリングした。サンプル液を直ちに75°Cま
で加熱し、急速冷却した。次に遠心分離機で不溶性物質
を除去した後、上澄液の660 nmにおける吸光度を
測定した。その結果を図2に示した。この予備試験結果
から、搾汁液を40℃に加温し、ペクチン分解酵素剤を
10.0 mg%、更にゼラチンを0.5mg%となる
様に添加し、120秒間反応すると予想される半透明果
汁のA660 nmは0.071であった。
This reaction solution was maintained at 40° C. and sampled after 1, 2, 3, and 4 minutes. The sample solution was immediately heated to 75°C and rapidly cooled. Next, after removing insoluble substances using a centrifuge, the absorbance of the supernatant at 660 nm was measured. The results are shown in FIG. Based on the preliminary test results, the juice was heated to 40°C, pectin-degrading enzyme agent was added to 10.0 mg%, and gelatin was added to 0.5 mg%, and it was predicted that the juice would react for 120 seconds to form a translucent liquid. The A660 nm of the fruit juice was 0.071.

この様にして得られた酵素−ゼラチン混合の反応条件を
用いて、半透明果汁を得た。その実施例を以下に示す。
Translucent fruit juice was obtained using the enzyme-gelatin mixing reaction conditions thus obtained. Examples thereof are shown below.

パインアップル果実60kgを洗浄した後、破砕、搾汁
して搾汁液27kgを得た。破砕機はハンマーミル、搾
汗機としてフィルタープレスを用いた。この搾汗l夜に
セラチンが0.5mg%となる様に添加し良く攪押した
後、温水循環式チューブヒーターに投入する事で液温を
40℃まで上昇した。ここにペクチン分解酵素剤の溶液
をマイクロチューブポンプで連続的に添加した。酵素濃
度は搾汁液に対して10.0mg%となる様に調整した
。酵素液を添加した後、スタテックミキザ一部を経てホ
ールデング部に輸送し、ここで120秒間保持した後、
それを80℃に加熱し、冷却した。続いてその液を連続
遠心分離機に輸送し、大部分の不溶性物質を除去した。
After washing 60 kg of pineapple fruits, they were crushed and squeezed to obtain 27 kg of juice. A hammer mill was used as the crusher, and a filter press was used as the sweat extractor. During the sweating process, 0.5 mg% of seratin was added, stirred well, and then placed in a hot water circulating tube heater to raise the liquid temperature to 40°C. A solution of a pectin-degrading enzyme agent was continuously added thereto using a microtube pump. The enzyme concentration was adjusted to 10.0 mg% based on the squeezed juice. After adding the enzyme solution, it is transported through a part of the static mixer to the holding section, where it is held for 120 seconds, and then
It was heated to 80°C and cooled. The liquid was then transferred to a continuous centrifuge to remove most of the insoluble material.

次に濾過綿を充填した濾過機で更に微細な不溶性物質を
除去し、常法にて殺菌し最終製品を得た。
Next, fine insoluble substances were removed using a filter filled with filter cotton, and the product was sterilized in a conventional manner to obtain a final product.

一方、−船釣に行なわれている方法に従って、同一果実
60kgを除皮後、破砕、搾t1− して混濁果汁30
kgを得た。これを(対照区工)とする。
On the other hand, - according to the method used for boat fishing, 60 kg of the same fruit was peeled, crushed, and squeezed t1 - to obtain 30 kg of cloudy fruit juice.
I got kg. This will be referred to as the (control area construction).

得られたこれらの采目の分析結果を第4表に示す。Table 4 shows the results of the analysis of these squares obtained.

【図面の簡単な説明】[Brief explanation of the drawing]

第1図はリンゴの圧搾液汁に酵素(ペクチナーゼ)を添
加して清澄処理するに当り、反応時間と濁度の関係を示
す図、第2図はパインアップルの圧搾液汁にペクチナー
ゼと凝集剤(ゼラチン)を添加して清澄処理するに当り
、反応時間と濁度の関係を示す図である。
Figure 1 shows the relationship between reaction time and turbidity when clarification is performed by adding an enzyme (pectinase) to pressed apple juice. Figure 2 shows the relationship between pectinase and flocculant (gelatin) added to pressed pineapple juice. ) is a diagram showing the relationship between reaction time and turbidity during clarification treatment by adding.

Claims (1)

【特許請求の範囲】[Claims] (1)果実の圧搾液汁に酵素を添加して清澄処理するに
当り、該清澄処理後の濁度が光波長600〜800nm
における10mmセルの吸光度で0.03〜0.50と
なるように調整することを特徴とする半透明果汁の製造
法。
(1) When adding enzymes to clarification of pressed fruit juice, the turbidity after the clarification is at a light wavelength of 600 to 800 nm.
A method for producing translucent fruit juice, which comprises adjusting the absorbance of a 10 mm cell to 0.03 to 0.50.
JP1279948A 1989-10-30 1989-10-30 Translucent juice production method Expired - Fee Related JP2649587B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1279948A JP2649587B2 (en) 1989-10-30 1989-10-30 Translucent juice production method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1279948A JP2649587B2 (en) 1989-10-30 1989-10-30 Translucent juice production method

Publications (2)

Publication Number Publication Date
JPH03143379A true JPH03143379A (en) 1991-06-18
JP2649587B2 JP2649587B2 (en) 1997-09-03

Family

ID=17618154

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1279948A Expired - Fee Related JP2649587B2 (en) 1989-10-30 1989-10-30 Translucent juice production method

Country Status (1)

Country Link
JP (1) JP2649587B2 (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2006067951A (en) * 2004-09-03 2006-03-16 Asama Chemical Co Ltd Method for producing grape juice and grape fruit grain enriched with resveratrol content
JP2012055294A (en) * 2010-09-13 2012-03-22 Suntory Holdings Ltd Method for processing mango fruit juice

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2006067951A (en) * 2004-09-03 2006-03-16 Asama Chemical Co Ltd Method for producing grape juice and grape fruit grain enriched with resveratrol content
JP2012055294A (en) * 2010-09-13 2012-03-22 Suntory Holdings Ltd Method for processing mango fruit juice
WO2012036108A1 (en) * 2010-09-13 2012-03-22 サントリーホールディングス株式会社 Method for processing mango juice
US20130196029A1 (en) * 2010-09-13 2013-08-01 Suntory Holdings Limited Method of processing mango juice

Also Published As

Publication number Publication date
JP2649587B2 (en) 1997-09-03

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