JPH1156241A - Production of tea drink - Google Patents
Production of tea drinkInfo
- Publication number
- JPH1156241A JPH1156241A JP22556697A JP22556697A JPH1156241A JP H1156241 A JPH1156241 A JP H1156241A JP 22556697 A JP22556697 A JP 22556697A JP 22556697 A JP22556697 A JP 22556697A JP H1156241 A JPH1156241 A JP H1156241A
- Authority
- JP
- Japan
- Prior art keywords
- liquid
- nitrogen gas
- sodium ascorbate
- production
- cross
- 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
Links
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- Tea And Coffee (AREA)
Abstract
Description
【0001】[0001]
【産業上の利用分野】本発明は、茶を原料とし、混濁や
沈澱等が発生することなく長期保存可能な清澄な風味の
優れた茶飲料の製造方法に関するものである。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for producing a tea beverage having a clear flavor which can be stored for a long time without causing turbidity or sediment, using tea as a raw material.
【0002】[0002]
【従来の技術】緑茶からの温水抽出液は、各種濾過剤を
用いて濾過あるいは遠心分離法により濁りを除去した後
に、金属製缶に充填して殺菌したもの、または殺菌後、
紙製、ガラス製、あるいは合成樹脂製の容器に充填した
ものを、緑茶飲料とする用途は、その簡便性から近時注
目されつつある。2. Description of the Related Art A hot water extract from green tea is subjected to filtration or centrifugation using various filter agents to remove turbidity, and then filled in a metal can and sterilized.
The use of green tea beverages filled in containers made of paper, glass, or synthetic resin has recently attracted attention due to its simplicity.
【0003】この緑茶飲料は、茶葉を40〜100 ℃の温水
に1〜10分間浸漬し、この間に随時緩慢な速度にて攪拌
して抽出液を得、次いで茶殼を分離した後、更に遠心分
離法、金属フィルターを用いた濾過、あるいは濾過パル
プを用いた加圧濾過法を行い、緑茶液を得、この緑茶液
に酸化防止剤としてアスコルビン酸またはアスコルビン
酸ナトリウムを添加した後、炭酸ナトリウムでpHを調整
して製造していた。[0003] In this green tea beverage, tea leaves are immersed in warm water at 40 to 100 ° C for 1 to 10 minutes, during which stirring is performed at a slow speed as needed to obtain an extract, and then the tea shell is separated and then centrifuged. Separation method, filtration using a metal filter, or pressure filtration method using filtration pulp to obtain a green tea liquor, after adding ascorbic acid or sodium ascorbate as an antioxidant to the green tea liquor, and then using sodium carbonate. It was manufactured by adjusting the pH.
【0004】[0004]
【発明が解決しようとする課題】しかし、このようにし
て得た緑茶飲料は、製造後、時間が経過するにつれてフ
ロックが析出する問題があった。このフロックは長期保
存によっても続くため、一時的に析出したフロックを分
離しても、その後再びフロックが析出してきて、緑茶飲
料に濁りが生じるのが特徴である。However, the green tea beverage obtained in this manner has a problem that floc precipitates as time passes after production. Since the floc continues even after long-term storage, even if the floc that has temporarily precipitated is separated, the floc is subsequently re-precipitated and the green tea beverage is turbid.
【0005】このことから従来の製造方法では清澄な緑
茶飲料を製造し、その品質を長期間維持することが不可
能である。フロックの析出は茶葉の成分であるタンニン
・タンパク・糖類等が長期保存中に抽出液中の微粒子を
核とし結合して発生すると考えられている。本発明の目
的は、従来のフロック析出の欠点を解決し、清澄な風味
の優れた緑茶飲料を簡易に大量生産するために、窒素雰
囲気下にアスコルビン酸ナトリウムを使用する茶飲料の
製造方法を提供することを目的とする。[0005] Therefore, it is impossible to produce a clear green tea beverage and maintain its quality for a long time by the conventional production method. It is thought that floc precipitation occurs when tannins, proteins, sugars, and the like, which are components of tea leaves, combine with the fine particles in the extract as nuclei during long-term storage. An object of the present invention is to provide a method for producing a tea beverage using sodium ascorbate under a nitrogen atmosphere in order to solve the drawbacks of the conventional floc precipitation and easily mass produce a green tea beverage having a clear and excellent flavor. The purpose is to do.
【0006】[0006]
【課題を解決するための手段】本発明は、茶葉を抽出し
た原液にアスコルビン酸ナトリウムを添加する工程と、
該液を精密濾過膜を用いクロスフロー方式にて窒素ガス
条件下で処理して濃縮液と透過液に分離する工程と、窒
素ガス条件下で濃縮液を循環させる工程と、透過液を取
り出す工程とを含むことを特徴とする、茶飲料の製造方
法である。The present invention comprises a step of adding sodium ascorbate to a stock solution from which tea leaves have been extracted;
A step of treating the liquid under a nitrogen gas condition in a cross-flow method using a microfiltration membrane to separate the concentrate into a permeate, a step of circulating the concentrate under a nitrogen gas condition, and a step of removing the permeate And a method for producing a tea beverage.
【0007】好ましくは、窒素ガス条件を0.5 〜1.4 kg
/cm2とする。また、好ましくは、アスコルビン酸ナトリ
ウムを茶葉1gあたり0.015g以上、0.03g未満添加す
る。窒素ガスが0.5 kg/cm2未満では、製造工程中での品
質劣化を十分に抑えることができず、またアスコルビン
酸ナトリウムの添加量が茶葉1gあたり0.015g未満で
は、品質劣化を十分に抑えることができず、また添加量
が0.04g以上では、緑茶の風味が損なわれる。Preferably, the nitrogen gas condition is 0.5 to 1.4 kg.
/ cm 2 . Preferably, sodium ascorbate is added in an amount of 0.015 g or more and less than 0.03 g per 1 g of tea leaves. If the nitrogen gas content is less than 0.5 kg / cm 2 , quality deterioration during the manufacturing process cannot be sufficiently suppressed. If the amount is 0.04 g or more, the flavor of green tea is impaired.
【0008】原液の濾過には、クロスフロー方式に精密
濾過膜を用いる。限外濾過膜の使用も考えられるが、耐
圧性の低い精密濾過膜の方がフロック析出を防止し茶葉
の風味を保持する点から優れている。濾過方式として、
クロスフロー方式とデッドエンド方式があるが、本発明
ではクロスフロー方式を用いる。クロスフロー方式は、
濾過面に対し平行方向に液を流し、原液内の一部を濾過
する方式であり、原液が濾過用膜モジュールに送られる
と、濾過液と濃縮液に分けられ、濃縮液は原液タンクに
戻り、再び濾過用膜モジュールに送られる。この方式の
利点は、液が濾過面に対して平行方向にあるので、濾過
面を閉塞することなく濾過ができることである。これに
対して、デッドエンド方式は、濾過面に対して垂直方向
に流れを与え全量を濾過するため、全量濾過が可能であ
るが、濾過面の閉塞が起こる欠点がある。[0008] For filtration of the stock solution, a microfiltration membrane is used in a cross flow system. The use of an ultrafiltration membrane is also conceivable, but a microfiltration membrane having a low pressure resistance is superior in preventing floc deposition and maintaining the flavor of tea leaves. As a filtration method,
There are a cross-flow method and a dead-end method, but the present invention uses the cross-flow method. The cross flow method is
In this method, liquid flows in a direction parallel to the filtration surface and a part of the stock solution is filtered.When the stock solution is sent to the membrane module for filtration, it is separated into a filtrate and a concentrate, and the concentrate returns to the stock tank. , Again sent to the filtration membrane module. The advantage of this method is that the liquid is in a direction parallel to the filtration surface, so that filtration can be performed without blocking the filtration surface. On the other hand, in the dead end method, since the flow is applied in a direction perpendicular to the filtration surface and the entire amount is filtered, the entire amount can be filtered, but there is a disadvantage that the filtration surface is blocked.
【0009】[0009]
【実施例】以下、本発明を実施例により説明する。 実施例 アミノ酸含量の多い緑茶の茶葉100gを70℃の温水4リッ
トル中4分間抽出した後、茶殼を除去した。この抽出液
を30℃まで冷却後、遠心分離処理を行い、アスコルビン
酸ナトリウムを茶葉1gあたり0.02g 添加し、原液タン
クに収容した。原液タンクからポンプで原液を膜モジュ
ールに送液し、フッ素樹脂製の精密濾過膜を使用して、
クロスフロー方式の濾過を行った。この濾過の工程で装
置内の雰囲気を窒素で置換し、膜透過液と濃縮液に分離
した。濃縮液は原液タンクに戻した。原液タンクを含む
装置内の窒素圧は1.0kg/cm2 に保持した。得られた膜透
過液は、緑茶飲料として加工した後も清澄な風味に優
れ、さらに1年程度の長期の保存にもその品質は保持さ
れた。The present invention will be described below with reference to examples. Example 100 g of green tea leaves having a high amino acid content was extracted in 4 liters of hot water at 70 ° C. for 4 minutes, and then the tea husk was removed. After the extract was cooled to 30 ° C., it was subjected to centrifugal separation, and sodium ascorbate was added in an amount of 0.02 g per 1 g of tea leaves and stored in a stock solution tank. Pump the undiluted solution from the undiluted solution tank to the membrane module using a microfiltration membrane made of fluororesin,
Cross-flow filtration was performed. In this filtration step, the atmosphere in the apparatus was replaced with nitrogen to separate into a membrane permeate and a concentrate. The concentrate was returned to the stock tank. The nitrogen pressure in the apparatus including the stock solution tank was maintained at 1.0 kg / cm 2 . The obtained membrane-permeated liquid had an excellent clear flavor even after being processed as a green tea beverage, and its quality was maintained even after long-term storage of about one year.
【0010】次に、前記アスコルビン酸ナトリウムと窒
素圧を変えて実験を行い、製造後の褐変の度合(表1)
および本来の風味の保持(表2)について、その結果を
次表に示す。Next, an experiment was conducted by changing the above-mentioned sodium ascorbate and the nitrogen pressure, and the degree of browning after the production (Table 1)
The results are shown in the following table for the retention of the original flavor (Table 2).
【0011】[0011]
【表1】 [Table 1]
【0012】[0012]
【表2】 表から、茶飲料の褐変防止には、窒素圧が0.5kg/cm2 未
満ではアスコルビン酸が添加されないと好ましくなく、
窒素雰囲気下でもアスコルビン酸添加量が0.04g 以上で
は風味が損なわれ、0.014g以下では風味が十分に保持で
きないので好ましくない。よって、窒素圧が0.5 kg/cm2
以上であり、茶葉1gあたりのアスコルビン酸添加量が
0.015g以上、0.04g未満において、本来の清澄な風味の
優れた緑茶飲料を得ることができる。[Table 2] From the table, the browning prevention of tea beverage, not preferred when not added ascorbic acid in less than 0.5 kg / cm 2 nitrogen pressure,
Even in a nitrogen atmosphere, if the amount of ascorbic acid added is 0.04 g or more, the flavor is impaired, and if it is 0.014 g or less, the flavor cannot be sufficiently maintained, which is not preferable. Therefore, the nitrogen pressure is 0.5 kg / cm 2
As mentioned above, the amount of ascorbic acid added per 1 g of tea leaves
When the content is 0.015 g or more and less than 0.04 g, an original green tea beverage having an excellent clear flavor can be obtained.
【0013】[0013]
【発明の効果】本発明によると、少量のアスコルビン酸
ナトリウムの存在で低圧の窒素雰囲気下にて精密濾過を
行うため、各種の精密濾過膜を使用でき、長期保存にお
いて清澄な風味の優れた緑茶飲料を得ることができる。According to the present invention, various types of microfiltration membranes can be used for performing microfiltration in a low-pressure nitrogen atmosphere in the presence of a small amount of sodium ascorbate. You can get a drink.
───────────────────────────────────────────────────── フロントページの続き (72)発明者 野坂 亙 東京都中野区江古田1−25−10 湘南香料 株式会社内 ──────────────────────────────────────────────────続 き Continued on the front page (72) Inventor Wataru Nosaka 1-25-10 Ekoda, Nakano-ku, Tokyo Shonan fragrance Co., Ltd.
Claims (3)
トリウムを添加する工程と、該液を精密濾過膜を用いク
ロスフロー方式にて窒素ガス条件下で処理して濃縮液と
透過液に分離する工程と、窒素ガス条件下で濃縮液を循
環させる工程と、透過液を取り出す工程とを含むことを
特徴とする、茶飲料の製造方法。1. A step of adding sodium ascorbate to a stock solution from which tea leaves have been extracted, and a step of treating the solution under a nitrogen gas condition by a cross-flow method using a microfiltration membrane to separate it into a concentrate and a permeate. And a step of circulating the concentrated liquid under nitrogen gas conditions, and a step of extracting the permeated liquid.
とを特徴とする請求項1記載の方法。2. The method according to claim 1, wherein the nitrogen gas condition is 0.5 kg / cm 2 or more.
たり0.015g以上、0.04g 未満添加することを特徴とする
請求項1または2記載の方法。3. The method according to claim 1, wherein sodium ascorbate is added in an amount of 0.015 g or more and less than 0.04 g per 1 g of tea leaves.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP22556697A JP3676914B2 (en) | 1997-08-08 | 1997-08-08 | Method for producing tea beverage |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP22556697A JP3676914B2 (en) | 1997-08-08 | 1997-08-08 | Method for producing tea beverage |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH1156241A true JPH1156241A (en) | 1999-03-02 |
JP3676914B2 JP3676914B2 (en) | 2005-07-27 |
Family
ID=16831320
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP22556697A Expired - Fee Related JP3676914B2 (en) | 1997-08-08 | 1997-08-08 | Method for producing tea beverage |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP3676914B2 (en) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP1338207A1 (en) * | 2002-02-20 | 2003-08-27 | Ito En, Ltd. | Manufacturing process of tea beverages |
KR100739919B1 (en) * | 1999-11-16 | 2007-07-16 | 디에스엠 아이피 어셋츠 비.브이. | Process for concentrating catechin solutions |
JPWO2006064756A1 (en) * | 2004-12-13 | 2008-06-12 | サントリー株式会社 | Method for producing coffee beverage using extracted liquid after filtration |
CN106974035A (en) * | 2017-02-03 | 2017-07-25 | 康师傅饮品控股有限公司 | Jasmine tea beverage and preparation technology |
-
1997
- 1997-08-08 JP JP22556697A patent/JP3676914B2/en not_active Expired - Fee Related
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR100739919B1 (en) * | 1999-11-16 | 2007-07-16 | 디에스엠 아이피 어셋츠 비.브이. | Process for concentrating catechin solutions |
EP1338207A1 (en) * | 2002-02-20 | 2003-08-27 | Ito En, Ltd. | Manufacturing process of tea beverages |
US6797305B2 (en) | 2002-02-20 | 2004-09-28 | Ito En, Ltd. | Manufacturing process of tea beverages |
JPWO2006064756A1 (en) * | 2004-12-13 | 2008-06-12 | サントリー株式会社 | Method for producing coffee beverage using extracted liquid after filtration |
CN106974035A (en) * | 2017-02-03 | 2017-07-25 | 康师傅饮品控股有限公司 | Jasmine tea beverage and preparation technology |
Also Published As
Publication number | Publication date |
---|---|
JP3676914B2 (en) | 2005-07-27 |
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