JP2007044056A - Packaged green tea beverage and method for producing the same - Google Patents
Packaged green tea beverage and method for producing the same Download PDFInfo
- Publication number
- JP2007044056A JP2007044056A JP2006318552A JP2006318552A JP2007044056A JP 2007044056 A JP2007044056 A JP 2007044056A JP 2006318552 A JP2006318552 A JP 2006318552A JP 2006318552 A JP2006318552 A JP 2006318552A JP 2007044056 A JP2007044056 A JP 2007044056A
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- Prior art keywords
- green tea
- silica
- tea
- diatomaceous earth
- filtration
- 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
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Images
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- Tea And Coffee (AREA)
Abstract
Description
本発明は、長期保存してもオリを発生しない容器詰緑茶飲料及びその製造方法に関し、特に加温販売に適した容器詰緑茶飲料及びその製造方法に関する。 The present invention relates to a packaged green tea beverage that does not generate odor even after long-term storage and a method for producing the same, and more particularly to a packaged green tea beverage suitable for heated sales and a method for producing the same.
緑茶飲料は、容器充填後保存している間に浮遊物状、白濁状、フロック状(綿状)或いは沈殿物状のオリ(以下、これらをまとめて単に「オリ」という。)を生じることがあり、特に透明容器に充填された緑茶飲料では、この種のオリの発生は商品価値を失うほどに重要な問題である。 Green tea beverages may produce a floating, white cloudy, flocked (cotton-like) or sediment-like orientation (hereinafter collectively referred to as “ori”) during storage after filling into the container. In particular, in the case of green tea beverages filled in transparent containers, the occurrence of this kind of orientation is an important issue as it loses its commercial value.
一概に「オリ」と言っても、飲料製造直後から析出し始める「一次的なオリ」と、飲料製造後の保存中に経時的に発生する「二次的なオリ」とに分けられ、このうちの「一次的なオリ」は、一般的にティークリームといわれ、カフェイン、テアフラビンなどが結合して生成することが確認されており、遠心分離、酵素処理、膜濾過などを組合わせて行うことで防止できることが確かめられている。その一方、「二次的なオリ」は、「一次的なオリ」以上にやっかいな問題であり、従来様々な防止方法が提案されている。 Generally speaking, “Ori” is divided into “Primary Ori” that begins to precipitate immediately after beverage production and “Secondary Ori” that occurs over time during storage after beverage production. Of these, "primary ori" is generally called tea cream, and it has been confirmed that caffeine, theaflavin, etc. are bound and produced, and it is performed by combining centrifugation, enzyme treatment, membrane filtration, etc. It has been confirmed that this can be prevented. On the other hand, “secondary orientation” is a more troublesome problem than “primary orientation”, and various prevention methods have been proposed.
「二次的なオリ」の防止方法の一つとして、オリの原因物質を除去する方法が提案されている。例えば、茶を温水抽出し、得られた茶抽出液を冷却した後タンニン酸を添加静置し、次いで遠心分離等によって微細な茶粒子を除去し、その後珪藻土濾過により清澄化させる方法(特許文献1)が開示されている。
また、緑茶を抽出した茶抽出液にアスコルビン酸を加えて酸性にした後、急冷した上で遠心分離し、次いで珪藻土濾過を行って清澄化する方法(特許文献2)が開示されている。
さらにまた、緑茶を水又は熱温水で抽出し得られた水溶性茶成分の茶抽出液にキトサンを添加し、高分子成分ポリフェノール類を吸着せしめた後それを遠心分離機にて処理し、さらに珪藻土濾過して沈殿物の晶出をなくす方法(特許文献3)が開示されている。
As one of the methods for preventing “secondary orientation”, a method for removing the cause of the orientation has been proposed. For example, a method in which tea is extracted with warm water, the obtained tea extract is cooled, tannic acid is added and allowed to stand, then fine tea particles are removed by centrifugation or the like, and then clarified by diatomaceous earth filtration (Patent Document) 1) is disclosed.
Further, a method is disclosed in which ascorbic acid is added to a tea extract from which green tea has been extracted to make it acidic, followed by rapid cooling and centrifugation, followed by diatomaceous earth filtration to clarify (Patent Document 2).
Furthermore, chitosan was added to the tea extract of water-soluble tea component obtained by extracting green tea with water or hot water, adsorbed the polymer component polyphenols, and then treated with a centrifuge. A method (Patent Document 3) that eliminates crystallization of precipitates by diatomaceous earth filtration is disclosed.
そのほか、化学薬剤や酵素などを添加して不溶性複合体(オリ)を可溶化或いは安定化させる方法が提案されている。例えば、緑茶の温水茶抽出液を遠心分離または濾布濾過し、さらにヘミセルラーゼ活性を有する酵素を添加処理する工程を組み合わせて緑茶飲料の二次沈殿の発生を有効に抑制する方法(特許文献4)や、緑茶抽出液にα−アミラーゼを添加処理することで飲料におけるフロックの発生を抑制する方法(特許文献5)、緑茶抽出液にリゾレシチン等の酵素処理レシチンを添加配合することにより、混濁あるいは沈澱の生成が抑制する緑茶飲料の製造方法(特許文献6)などが開示されている。 In addition, a method for solubilizing or stabilizing an insoluble complex (ori) by adding a chemical agent or an enzyme has been proposed. For example, a method of effectively suppressing the occurrence of secondary precipitation of a green tea beverage by combining a step of centrifuging or filtering a hot water tea extract of green tea and further adding an enzyme having hemicellulase activity (Patent Document 4) ), A method for suppressing the occurrence of floc in a beverage by adding α-amylase to a green tea extract (Patent Document 5), or by adding an enzyme-treated lecithin such as lysolecithin to the green tea extract, A method for producing a green tea beverage that suppresses the formation of precipitation (Patent Document 6) is disclosed.
しかし、オリの原因物質を除去することにより二次的なオリの防止を図る方法は、緑茶飲料中に含まれる混濁・沈殿の原因物質を最終的に全て排除するものであったため、茶の香味に影響しオリの形成に関与しない成分も多量に除去することになり、茶が本来備えている香味が弱くなるという課題を抱えていた。
また、化学薬剤や酵素を添加して不溶性複合体を可溶化或いは安定化させる方法は、添加物と含有成分との反応によって茶本来の香味が変化するという問題があった。
Further, the method of solubilizing or stabilizing the insoluble complex by adding a chemical agent or an enzyme has a problem that the original flavor of tea changes due to the reaction between the additive and the contained component.
最近、冬場を中心に容器詰め緑茶飲料を55〜60℃程度に加温して販売することが行われているが、我々が研究したところ、加温状態で緑茶飲料を保管すると二次的なオリがより一層生じ易くなることが分かってきた。さらに、55〜60℃に加温販売することにより好熱性細菌による変敗や、熱変性からくる香味変化が生じる可能性があり、加温販売用の容器詰緑茶飲料にはこれらの対策を講じるのが好ましい。 Recently, green tea beverages packed in containers have been heated to about 55-60 ° C and sold mainly in winter, but when we researched, storing green tea beverages in a heated state is secondary. It has been found that the orientation is more likely to occur. Furthermore, there is a possibility that deterioration due to thermophilic bacteria and flavor change resulting from heat denaturation may occur by selling at 55 to 60 ° C., and these measures will be taken for containered green tea beverages for heating sales. Is preferred.
そこで本発明は、長期にわたり清澄で、しかも茶が本来備えている香味を維持した容器詰緑茶飲料であって、特に加温販売用に適した容器詰緑茶飲料及びその製造方法を提供せんとするものである。 Therefore, the present invention provides a packaged green tea beverage that is clear over a long period of time and that maintains the original flavor of tea, and is particularly suitable for heating sales and a method for producing the same. Is.
かかる課題に鑑みて、本発明は、緑茶葉を抽出して得られる茶抽出液を容器に充填してなる容器詰緑茶飲料であって、ガラクツロン酸を30〜50ppm含み、タンパク質量を6〜10ppm含むことを特徴とする容器詰緑茶飲料を提案する。
また、緑茶葉を70〜100℃の加温水にて抽出する抽出工程、得られた茶抽出液にシリカを添加して茶抽出液中のオリ成分を当該シリカに吸着させ、茶抽出液中のガラクツロン酸量を30ppm〜50ppmとし、且つ、タンパク質量を6ppm〜10ppmとする吸着工程、当該シリカを茶抽出液から除去するシリカ除去工程、殺菌工程及び容器充填工程を含む容器詰緑茶飲料の製造方法を提案する。
この際、シリカ除去工程は、濾過工程が兼ねてもよいし、濾過工程とは別にシリカ除去工程を設けてもよい。具体的に言えば、遠心分離、限外濾過、微細濾過、精密濾過、逆浸透膜濾過、電気透析、生物機能性膜などの膜濾過、その他の多孔質媒体(濾材)を用いて固体粒子を液体から分離し得る濾過方法或いはこれらのいずれか二種類を組合わせた濾過方法にて不要物と共に添加したシリカを茶抽出物から除去するようにしてもよいし、また、任意の濾過方法(例えば前記濾過方法)によってシリカを除去した後、別途、遠心分離、限外濾過、微細濾過、精密濾過、逆浸透膜濾過、電気透析、生物機能性膜などの膜濾過、或いはその他の多孔質媒体(濾材)を用いて固体粒子を液体から分離し得る濾過方法にて濾過を行うようにしてもよい。
なお、本発明では、例えば殺菌工程と容器充填工程の順序を入れ替えるなど工程の順番を入れ替えてもよいし、また、他の工程が挿入されてもよい。
In view of such a problem, the present invention is a container-packed green tea beverage obtained by filling a tea extract obtained by extracting green tea leaves into a container, containing 30 to 50 ppm of galacturonic acid, and containing 6 to 10 ppm of protein. A container-packed green tea beverage characterized by containing is proposed.
Moreover, the extraction process which extracts a green tea leaf with 70-100 degreeC warm water, a silica is added to the obtained tea extract, the oli component in a tea extract is made to adsorb | suck to the said silica, A method for producing a packaged green tea beverage comprising an adsorption step in which the amount of galacturonic acid is 30 ppm to 50 ppm and a protein amount is 6 ppm to 10 ppm, a silica removal step in which the silica is removed from the tea extract, a sterilization step, and a container filling step Propose.
At this time, the silica removing step may be combined with the filtering step, or a silica removing step may be provided separately from the filtering step. Specifically, solid particles can be obtained using centrifugal separation, ultrafiltration, microfiltration, microfiltration, reverse osmosis membrane filtration, electrodialysis, membrane filtration such as biofunctional membranes, and other porous media (filter media). Silica added together with unnecessary substances may be removed from the tea extract by a filtration method that can be separated from the liquid or a combination of these two types, or any filtration method (for example, The silica is removed by the filtration method), and then separately, centrifugal filtration, ultrafiltration, microfiltration, microfiltration, reverse osmosis membrane filtration, electrodialysis, membrane filtration such as biofunctional membrane, or other porous media ( Filtration may be performed by a filtration method capable of separating solid particles from a liquid using a filter medium.
In the present invention, for example, the order of the steps such as changing the order of the sterilization step and the container filling step may be changed, and other steps may be inserted.
本発明者は、茶飲料におけるオリ(一次的なオリ・二次的なオリを含む)の防止方法について鋭意研究した結果、茶抽出液にシリカを添加し接触させることで、茶抽出液中に含まれるオリ成分、具体的には、二次的なオリを形成する一部のタンパク質及び多糖類を当該シリカに選択的に吸着させることができることを見出し、かかる知見に基づき本発明を想到するに至った。従来、緑茶飲料の保存において二次的に発生するオリの原因は高分子成分の配合割合にあると考えられてきたため、オリの原因物質を除去する方法の多くは結果的に高分子含有成分を全て除去せんとするものであった。しかし、高分子含有成分中には茶の香味に影響を与える成分も多く含まれているため、従来の方法によればオリの発生を防止できても、茶が本来備えている香味が弱くなってしまっていた。これに対し本発明は、二次的なオリを形成する一部のタンパク質及び多糖類をシリカに選択的に吸着させて除去することができるため、これらの含有量を減少させることができ、同時にオリの発生に関与しない香味成分を茶抽出液中に多く残すことができる。その結果、長期にわたり清澄で、しかも茶が本来備えている香味を維持した容器詰緑茶飲料を製造することができる。
「二次的なオリ」の原因に関しては、最近、茶抽出液又は茶調合液中の「ストリクチニン 」が加熱殺菌によって「エラグ酸」に分解され、この「エラグ酸」がタンパク質や多糖類などと結合して二次オリを形成する旨が報告されている(特開2003−235452等参照)。この観点からすると、本発明は、緑茶抽出液にシリカを添加することで、「エラグ酸」に結合するタンパク質や多糖類を選択的にシリカに吸着し、真に二次的なオリの原因となる成分を茶抽出液から集中的に選択除去できるものと考えることができる。
As a result of earnest research on prevention methods for tea (including primary and secondary orientation) in tea beverages, the inventor added silica to the tea extract and brought it into contact with the tea extract. In order to conceive the present invention based on this finding, it has been found that a portion of the components contained therein, specifically, some proteins and polysaccharides that form secondary olis can be selectively adsorbed on the silica. It came. Conventionally, it has been thought that the cause of secondary occurrence in the storage of green tea beverages is due to the blending ratio of the polymer component. All were intended to be removed. However, since many ingredients that affect the flavor of tea are contained in the polymer-containing component, the flavor inherent to tea is weakened even if the conventional method can prevent the occurrence of orientation. It was. On the other hand, since the present invention can selectively adsorb and remove some proteins and polysaccharides that form secondary olis on silica, the content thereof can be reduced at the same time. Many flavor components that are not involved in the occurrence of orientation can be left in the tea extract. As a result, it is possible to produce a container-packed green tea beverage that is clear over a long period of time and that maintains the original flavor of tea.
Regarding the cause of “secondary ori”, recently, “striketinin” in tea extract or tea preparation is decomposed into “ellagic acid” by heat sterilization, and this “ellagic acid” is converted into protein, polysaccharides, etc. It has been reported that a secondary orientation is formed by bonding (see JP2003-235451A). From this point of view, the present invention selectively adsorbs proteins and polysaccharides that bind to “ellagic acid” to silica by adding silica to the green tea extract, It can be considered that this component can be selectively removed from the tea extract.
本発明の製造方法は、特に加温販売用の容器詰緑茶飲料の製造に適している。加温販売は通常55〜60℃に加温された状態で保管及び販売される。緑茶飲料は加温状態で保管されると、二次的なオリがより一層生じ易くなるが、本発明の製造方法によれば、二次的なオリを形成するタンパク質及び多糖類を選択的に吸着除去でき、加温販売されても長期にわたり清澄を維持する緑茶飲料を製造することができる。
また、55〜60℃で加温販売する場合、常温では増殖しない好熱性細菌(耐熱性高温菌)の増殖が懸念されるが、本発明の製造方法によれば、茶抽出液中に含まれる抗菌性作用を備えたカテキン類を飲料中に残すことができるため、このカテキン類の抗菌作用により耐熱性細菌の発育を抑制することができる。この点、ポリフェノールを吸着する方法ではカテキン類が少なくなってしまうし、また、酵素等の分解による方法では余分な有機類が残ってしまう。
また、通常の緑茶飲料は55〜60℃で加温販売されると、熱変化や酸素劣化が加速され、加熱劣化が進むとイモ臭的な嫌な香りを感じるようになるが、本発明の製造方法では、劣化臭の原因である脂肪酸酸化分解物を選択的に減少させることができることが確認されている。その一方、ピラジン等の焙煎香成分は飲料中に多く残すことができることも確認されており、加温飲用時に嫌な香りが少なく、それでいてシャープな焙煎香を感じる香味の高い緑茶飲料を提供することができる。
香味の観点からみると、人間の味覚は温度によって感じ方が変ることが知られている。苦渋味は温度が高いと感じ方が鈍く、甘さは温度が高い方が感じ易いと言われているが、本発明の製造方法によれば、渋味成分であるカテキンと焙煎香成分とをしっかり飲料中に残すことができ、それでいて嫌なイモ臭を抑制することができるから、特に加温販売用として適した緑茶飲料を提供することができる。
The production method of the present invention is particularly suitable for the production of container-packed green tea beverages for warm sales. Warm sales are usually stored and sold in a state of being heated to 55-60 ° C. When the green tea beverage is stored in a warmed state, secondary orientation is more likely to occur. However, according to the production method of the present invention, proteins and polysaccharides that form secondary orientation are selectively selected. It is possible to produce a green tea beverage that can be adsorbed and removed and can maintain a clearness for a long time even if it is heated.
In addition, when heated at 55 to 60 ° C., there is a concern about the growth of thermophilic bacteria (heat-resistant thermophilic bacteria) that do not grow at room temperature, but according to the production method of the present invention, it is contained in the tea extract. Since catechins having an antibacterial action can be left in the beverage, the growth of heat-resistant bacteria can be suppressed by the antibacterial action of the catechins. In this regard, the method of adsorbing polyphenols reduces catechins, and the method of decomposing enzymes and the like leaves extra organics.
In addition, when a normal green tea beverage is heated and sold at 55 to 60 ° C., the heat change and oxygen deterioration are accelerated, and when the heating deterioration proceeds, a bad smell like potato smell is felt. In the production method, it has been confirmed that the fatty acid oxidative degradation product that causes the deterioration odor can be selectively reduced. On the other hand, it has also been confirmed that roasting incense ingredients such as pyrazine can be left in the beverage, providing a green tea beverage with a high flavor that has little unpleasant aroma when heated and yet has a sharp roasted incense. can do.
From the point of view of flavor, it is known that human taste changes with temperature. It is said that bitter and astringent taste feels dull when the temperature is high, and sweetness is easy to feel when the temperature is high, but according to the production method of the present invention, catechin and roasted aroma ingredients that are astringency ingredients Can be firmly left in the beverage, and the unpleasant potato odor can be suppressed, so that it is possible to provide a green tea beverage particularly suitable for warming sales.
なお、本発明において「緑茶飲料」とは、緑茶葉を抽出して得られた茶抽出液を主原料とする飲料の意である。烏龍茶飲料や紅茶飲料などの二次的なオリが生じづらい茶飲料は本発明が対象とする茶飲料として好ましくない。
また、本発明において「二次的なオリ」とは、微粉の沈殿を含まず、フロック状(綿状)の沈殿物を意図するものであり、「一次的なオリ」とは区別されるべきである。また、ワインなどのブドウを原料とする飲料ではフロック状ではない粒子の沈殿が見られるが、これとも区別されるべきである。
In the present invention, the term “green tea beverage” means a beverage whose main ingredient is a tea extract obtained by extracting green tea leaves. Tea beverages, such as oolong tea beverages and black tea beverages, that are difficult to produce secondary orientation are not preferred as the tea beverages targeted by the present invention.
Further, in the present invention, “secondary orientation” does not include precipitation of fine powder and intends flock-like (cotton-like) precipitation, and should be distinguished from “primary orientation”. It is. In addition, in beverages made from grapes such as wine, precipitation of particles that are not flock-like is observed, but this should also be distinguished.
以下、本発明を実施するための最良の実施形態について説明するが、本発明の実施形態が以下の例に限定されるものではない。 Hereinafter, although the best embodiment for carrying out the present invention is described, the embodiment of the present invention is not limited to the following examples.
本実施形態では、緑茶葉を加温水にて抽出する抽出工程、茶抽出液から抽出残渣を取り除く粗濾過工程、茶抽出液にシリカを添加して茶抽出液中のオリ成分を当該シリカに吸着させる吸着工程、濾過工程としての遠心分離(シリカ除去工程を兼ねる)及び珪藻土濾過、調合工程、殺菌工程、容器充填工程を経て容器詰緑茶飲料を製造する。
ただし、当該製造工程はあくまでも一例である。各工程の順序を入れ替えることも可能であるし、また各工程間に別の工程を挿入することも可能である。例えば、本製造工程では、遠心分離にて添加したシリカを茶抽出液から除去するようにしているが、遠心分離の前に、添加したシリカを茶抽出液から除去する濾過を挿入するようにしてもよい。
In this embodiment, an extraction process for extracting green tea leaves with warm water, a coarse filtration process for removing extraction residues from the tea extract, and silica is added to the tea extract to adsorb the oli component in the tea extract to the silica. The container-packed green tea beverage is manufactured through the adsorption process, the centrifugal separation (also serving as the silica removal process) and the diatomaceous earth filtration, the blending process, the sterilization process, and the container filling process.
However, the manufacturing process is merely an example. It is possible to change the order of each process, and it is also possible to insert another process between each process. For example, in this production process, silica added by centrifugation is removed from the tea extract, but before centrifugation, filtration for removing the added silica from the tea extract is inserted. Also good.
(原料茶)
緑茶葉、すなわち原料茶葉としては、茶樹(学名:Camellia sinensis)から摘採した葉であればその品種、産地、摘採時期、摘採方法、栽培方法などを限らず、どのような茶種も対象とすることができる。生茶葉等(葉や茎を含む)を原料茶葉とすることも可能である。更に、これらの生茶葉等を蒸すか或いは炒るかなどの手段で酵素活性を停止させる荒茶加工を施した荒茶であれば、煎茶、釜炒り茶、かぶせ茶、玉露、てん茶、抹茶、番茶、焙じ茶、蒸製玉緑茶、釜炒製玉緑茶、嬉野茶、青柳茶等のいずれの種類も原料茶葉として用いることができる。また、これらの荒茶を二種類以上組合わせてもよいし、香料を入れて作製してもよい。加えて、ジャスミン茶などの弱発酵茶も対象とすることができる。なお、ジャスミン茶にはいろいろな種類があるが、緑茶に人工香料を入れて作製するものは不発酵茶に分類されるものが好ましい。また、上記の荒茶に現在公知の仕上加工を施して得られる仕上茶も原料茶葉として用いることができる。
その一方、烏龍茶や鉄観音茶などの半発酵茶、紅茶などの発酵茶、プーアル茶などの後発酵茶は本発明の原料茶葉としては好ましくない。烏龍茶や紅茶で発生するクリームダウンは、不発酵茶で発生する不可逆性のフロック状のオリ(すなわち二次的なオリ)とは原因を異にするものだからである。
(Raw tea)
Green tea leaves, that is, raw tea leaves, are not limited to their cultivar, origin, picking time, picking method, cultivation method, etc., as long as they are picked from tea trees (scientific name: Camellia sinensis). be able to. Raw tea leaves (including leaves and stems) can be used as raw tea leaves. Furthermore, if it is rough tea that has been subjected to rough tea processing that stops the enzyme activity by means such as steaming or roasting these raw tea leaves etc., sencha, kettle roasted tea, kabuse tea, gyokuro, tencha, matcha, Any kind of bancha, roasted tea, steamed ball green tea, kettle roasted ball green tea, Ureshino tea, Aoyagi tea, etc. can be used as the raw tea leaves. Further, two or more kinds of these rough teas may be combined, or may be prepared by adding a fragrance. In addition, weakly fermented teas such as jasmine tea can also be targeted. There are various types of jasmine tea, but those prepared by adding artificial flavor to green tea are preferably classified as non-fermented tea. In addition, finished tea obtained by subjecting the above-mentioned crude tea to a currently known finishing process can also be used as a raw tea leaf.
On the other hand, semi-fermented tea such as oolong tea and iron kannon tea, fermented tea such as black tea, and post-fermented tea such as puer tea are not preferable as the raw tea leaves of the present invention. This is because the cream down that occurs in oolong tea or black tea has a different cause from the irreversible flock-like orientation (that is, secondary orientation) that occurs in non-fermented tea.
(抽出工程)
緑茶葉の抽出は、70〜100℃の加温水にて抽出すればよい。例えば、常法に従ってニーダーと呼ばれる抽出装置を用いて、原料茶に対して20〜100倍量、70〜100℃の抽出水で約1分〜20分間、必要に応じて1回〜数回攪拌して、常圧で抽出を行えばよい。但し、抽出方法及び抽出条件等を特に限定するものではなく、例えば加圧抽出を行うこともできる。
なお、抽出温度すなわち抽出する温水の温度は70〜100℃、特に好ましくは70〜90℃の温水で抽出するのがよい。70〜100℃、特に70〜90℃の温水で抽出すれば、所望の香りが得られ易く、かつ渋味が強くなることもない。
抽出に用いる抽出水は、純水(硬水、軟水、イオン交換水を含む)のほか、アスコルビン酸含有水溶液及びpH調製水等を例示することができる。
(Extraction process)
What is necessary is just to extract a green tea leaf with 70-100 degreeC warm water. For example, using an extraction device called a kneader according to a conventional method, it is stirred 20 to 100 times the amount of raw tea, 70 to 100 ° C. with extracted water for about 1 minute to 20 minutes, once to several times as necessary. Thus, extraction may be performed at normal pressure. However, the extraction method and extraction conditions are not particularly limited, and for example, pressure extraction can be performed.
The extraction temperature, that is, the temperature of hot water to be extracted is preferably 70 to 100 ° C, particularly preferably 70 to 90 ° C. Extracting with warm water of 70 to 100 ° C., particularly 70 to 90 ° C., makes it easy to obtain a desired scent and does not increase the astringency.
Examples of the extraction water used for extraction include pure water (including hard water, soft water, and ion exchange water), ascorbic acid-containing aqueous solution, pH adjustment water, and the like.
抽出によって得られた茶抽出液は、必要に応じて5〜40℃程度に冷却し、同時に又はその前後に、必要に応じて、茶抽出液にアスコルビン酸やアスコルビン酸ナトリウムなどを加えて酸性(pH4〜5)に調整するのがよい。茶抽出液の冷却或いは酸性調整によって抽出成分の酸化を防ぐことができると共に、一次オリ原因成分を沈殿させて後工程の遠心分離の効率を高めることができる。 The tea extract obtained by the extraction is cooled to about 5 to 40 ° C. as necessary, and at the same time or before and after that, ascorbic acid or sodium ascorbate is added to the tea extract as needed to make it acidic ( It is good to adjust to pH 4-5). By cooling or acid adjusting the tea extract, it is possible to prevent the extraction component from being oxidized, and to precipitate the primary causative component and increase the efficiency of the subsequent centrifugation.
(粗濾過工程)
粗濾過工程は、茶葉や大きな微粉などの抽出残渣を除去する工程である。例えばステンレスフィルターやネル布、ストレーナー、その他抽出残渣を除去するために現在採用されている濾過方法を任意に採用することができる。
なお、粗濾過工程は、大きな抽出残渣を除去する工程であって、茶飲料の分子量分布等に影響を与える処理ではないため、この役割を他の濾過手段(本例で言えば、遠心分離、珪藻土濾過)に委ねて当該粗濾過工程を省略することも可能である。
(Coarse filtration step)
The coarse filtration step is a step of removing extraction residues such as tea leaves and large fine powders. For example, the filtration method currently employ | adopted in order to remove a stainless steel filter, flannel cloth, a strainer, and other extraction residues can be arbitrarily employ | adopted.
The coarse filtration step is a step for removing a large extraction residue, and is not a treatment that affects the molecular weight distribution of the tea beverage, etc., so this role can be performed by other filtration means (in this example, centrifugation, It is also possible to omit the rough filtration step depending on diatomaceous earth filtration.
(吸着工程)
吸着工程では、茶抽出液にシリカを添加して茶抽出液とシリカとを接触させ、茶抽出液中のオリ成分を選択的にシリカに吸着させ、本工程で添加したシリカは後工程にて除去する。
(Adsorption process)
In the adsorption process, silica is added to the tea extract and brought into contact with the tea extract and the silica is selectively adsorbed on the silica in the tea extract. Remove.
添加するシリカとしては、シリカ(二酸化珪素;SiO2)のほか、シリカを主成分として含有する(全質量の50%以上を占有)シリカ含有物を用いることができる。
シリカ(二酸化珪素;SiO2)は、結晶質及び非晶質のいずれでもよい。また、天然物及び合成物のいずれでもよい。合成物の場合、乾式法(気相法)、湿式法(水ガラス法;ゲルタイプ及び沈降性タイプを含む)、ゾル・ゲル法などの任意の合成法により製造されたシリカを用いることができる。
シリカ含有物としては、例えば天然物である珪酸塩や珪藻土等の粘土鉱物、水晶、石英などを挙げることができる。
As silica to be added, in addition to silica (silicon dioxide; SiO2), a silica-containing material containing silica as a main component (occupying 50% or more of the total mass) can be used.
Silica (silicon dioxide; SiO2) may be either crystalline or amorphous. Moreover, any of a natural product and a synthetic product may be sufficient. In the case of a synthetic product, silica produced by any synthetic method such as a dry method (gas phase method), a wet method (water glass method; including a gel type and a sedimentation type), a sol-gel method, or the like can be used. .
Examples of the silica-containing material include clay minerals such as silicate and diatomaceous earth, quartz, quartz, etc., which are natural products.
茶抽出液にシリカを添加して茶抽出液とシリカとを接触させることで、茶抽出液中に含まれているオリ成分、特に二次的なオリを形成する一部のタンパク質及び多糖類をシリカに選択的に吸着させることができ、茶抽出液中のこれらの濃度を低下させることができる。
シリカの添加量は、抽出する緑茶原料(茶葉質量)に対し0.5〜20倍量、特に1〜10倍量とするのが好ましい。
添加量のほか、シリカの粒子径、細孔径、電荷、シリカ表面に存在する水酸基(シラノール基)を制御することにより、シリカの吸着性能を調整し、これによって吸着除去するタンパク質や多糖類の種類と量を調整して緑茶飲料の香味を調整することができる。
By adding silica to the tea extract and bringing the tea extract and silica into contact with each other, some of the proteins and polysaccharides that form the secondary ingredients are contained in the tea extract. It can be selectively adsorbed on silica and the concentration of these in the tea extract can be reduced.
The amount of silica added is preferably 0.5 to 20 times, particularly 1 to 10 times the amount of green tea raw material (tea leaf mass) to be extracted.
In addition to the addition amount, the silica particle size, pore size, electric charge, and the hydroxyl group (silanol group) present on the silica surface are controlled to adjust the silica adsorption performance, and the types of proteins and polysaccharides that are adsorbed and removed by this. The amount of the green tea beverage can be adjusted by adjusting the amount.
具体的な吸着方法としては、例えば、茶抽出液中にシリカを添加し攪拌するようにしてもよいし、また、粗濾過後の茶抽出液中にシリカを添加し、当該茶抽出液をシリカとともに次工程に送ることで、その送液過程で茶抽出液とシリカとを接触させるようにしてもよい。また、数回に分けてシリカを添加して分散吸着させるようにしてもよい。
この際、茶抽出液中にシリカを添加した後、茶抽出液を20〜40℃になるまで冷却させながらシリカと接触させるのが好ましい。茶抽出液を20℃以下まで冷却させると、クリームダウンが生じてシリカの吸着能力を低下させるおそれがある。その一方、40℃よりも高くすると茶抽出液が熱によって変化し香味が損なわれる可能性がある。
また、シリカを添加する茶抽出液は、弱酸性領域(pH4.5〜5.5)に調整するのが好ましい。弱酸性領域に調整することでカテキン類の変化が抑えられる。なお、pH4.5より低くするとクリームダウンが生じてシリカの吸着能力を低下させるおそれがある点に注意する必要がある。
茶抽出液からシリカを除去するには、シリカを除去するためのシリカ濾過工程を別途挿入するようにしてもよいし、吸着工程に続く遠心分離、珪藻土濾過或いはその他の濾過工程でシリカを除くようにしてもよい。
As a specific adsorption method, for example, silica may be added to the tea extract and stirred, or silica may be added to the tea extract after coarse filtration, and the tea extract may be mixed with silica. Moreover, you may make it contact a tea extract and a silica in the liquid feeding process by sending to the next process. Also, silica may be added and dispersed and adsorbed in several times.
At this time, after adding silica to the tea extract, it is preferable to contact the silica extract while cooling the tea extract to 20 to 40 ° C. When the tea extract is cooled to 20 ° C. or lower, cream-down may occur and the silica adsorption ability may be reduced. On the other hand, if the temperature is higher than 40 ° C., the tea extract may change due to heat and the flavor may be impaired.
Moreover, it is preferable to adjust the tea extract to which silica is added to a weakly acidic region (pH 4.5 to 5.5). Changes in catechins can be suppressed by adjusting to a weakly acidic region. It should be noted that if the pH is lower than 4.5, cream-down may occur and the silica adsorption capacity may be reduced.
In order to remove silica from the tea extract, a silica filtration step for removing the silica may be inserted separately, or the silica may be removed by centrifugation, diatomaceous earth filtration or other filtration steps following the adsorption step. It may be.
(遠心分離)
遠心分離は、例えば流速:200〜500L/h、回転数:5000〜20000rpmの条件で行えばよく、この際、流速、回転数、遠心沈降面積(Σ)などを変えることで最終的に得られる容器詰緑茶飲料の清澄度(T%)を調整することができる。
遠心分離するに当たって予め5〜40℃程度に茶抽出液を冷却しておくのが好ましいが、必ずしも冷却しなくてもよい。
(Centrifugation)
Centrifugation may be performed, for example, under conditions of a flow rate of 200 to 500 L / h and a rotational speed of 5000 to 20000 rpm, and finally obtained by changing the flow rate, the rotational speed, the centrifugal sedimentation area (Σ), and the like. The clarity (T%) of the containered green tea beverage can be adjusted.
In centrifuging, it is preferable to cool the tea extract to about 5 to 40 ° C. in advance, but it is not always necessary to cool it.
遠心分離は、微粉を取り除く処理であるが、上記の如く添加したシリカを取り除くことができる。
また、他に微粉を除去し得る工程があれば遠心分離は必ずしも必要ではないが、珪藻土濾過の前に遠心分離を行うことによって珪藻土濾過の負担を軽減することができる。例えば透過流量の増加及び透過圧の低下により濾過時間を短縮することができる。ただし、珪藻土濾過でも微粉を取り除くことができるため、負担は多少大きくなるが、珪藻土濾過を行う場合には遠心分離を省略することも可能である。
Centrifugation is a process for removing fine powder, but the silica added as described above can be removed.
Further, if there is another process that can remove fine powder, centrifugation is not always necessary, but the diatomaceous earth filtration burden can be reduced by performing centrifugation before diatomaceous earth filtration. For example, the filtration time can be shortened by increasing the permeation flow rate and decreasing the permeation pressure. However, since fine powder can be removed by diatomaceous earth filtration, the burden is somewhat increased. However, when diatomaceous earth filtration is performed, centrifugation can be omitted.
(珪藻土濾過)
珪藻土濾過は、濾過助剤として珪藻土を使用する濾滓濾過である。
珪藻土は、珪藻類と呼ばれる植物プランクトンが長年にわたり海底や湖底に堆積して化石化し、微細な珪藻殻が集積した土である。直径は数〜数十μmで、表面に0.1〜1.0μmの無数の微細な穴が存在するため、金網、濾布に緻密な濾過助剤のケーク層を形成することにより、濾過時に清澄な液が得られる。
珪藻土の主成分はシリカ(SiO2)、特に非結晶シリカであり、濾過助剤の用途には、焼成によって精製されたものを用いるのが一般的である。
(Diatomaceous earth filtration)
Diatomaceous earth filtration is filter cake filtration using diatomaceous earth as a filter aid.
Diatomaceous earth is a soil in which phytoplankton, called diatoms, accumulates on the seabed and lake bottom for fossilization and fossilizes, and fine diatom shells accumulate. The diameter is several to several tens of μm, and there are innumerable fine holes of 0.1 to 1.0 μm on the surface. Therefore, by forming a dense filter aid cake layer on the wire mesh and filter cloth, A clear liquid is obtained.
The main component of diatomaceous earth is silica (SiO 2), particularly amorphous silica, and it is common to use a filter aid that has been purified by firing.
珪藻土濾過の方法としては、濾過担体表面に珪藻土からなる助剤層(プリコート)を形成させ、必要に応じて珪藻土濾過剤を原液(未濾過液としての茶抽出液)に注入(ボディフィード)しながら、原液(未濾過液としての茶抽出液)を前記助剤層に送るようにすればよい。
ここで、「プリコート」とは、濾過操作の前に、助剤を清澄な液体に分散させ、これを循環させて、濾過担体(例えば金属製の網(leaf)、厚手濾紙(filter pad)、積層金属環(candle)、セラミック筒(candle)など)の表面に厚さ数mmの助剤の層を形成することであり、これによって懸濁固形分が濾材に直接付着して汚染することを防ぐことができ、また、濾液の清澄度を向上させることができる。
As a method of diatomite filtration, an auxiliary layer (precoat) made of diatomaceous earth is formed on the surface of the filter carrier, and diatomaceous earth filter agent is injected into the stock solution (tea extract as unfiltered liquid) as needed (body feed). However, the stock solution (tea extract as an unfiltered solution) may be sent to the auxiliary layer.
Here, the “precoat” means that an auxiliary agent is dispersed in a clear liquid before the filtration operation, and this is circulated to obtain a filter carrier (for example, a metal net, a thick filter paper, This is to form a layer of an auxiliary agent with a thickness of several millimeters on the surface of a laminated metal ring (ceramic), a ceramic cylinder (candle), etc. Can be prevented, and the clarity of the filtrate can be improved.
本発明で用いる珪藻土は、珪藻土の原鉱を粉砕・乾燥処理したもの、粉砕・乾燥処理したものに更に焼成又は融剤焼成処理を施したものなど、濾過助剤として使用される珪藻土であれば用いることが可能であるが、Darcy0.05〜0.1の珪藻土濾過助剤を用いるのが好ましい。Darcy 0.05〜0.1の珪藻土濾過助剤を用いることにより、より一層清澄な容器詰茶飲料を製造することができる。なお、「Darcy0.05〜0.1の珪藻土濾過助剤」とは、Darcyの透過率Kが0.05〜0.1の範囲内にある珪藻土濾過助剤の意である。「Darcyの透過率K」は濾過助剤の透過性を示す指標の一つであり、水透過法或いは空気透過法により求めることができる。現在、「Darcy」はこの値を指定して珪藻土濾過助剤を購入できる程一般的に用いられている。
また、本発明で用いる珪藻土には、酸処理によって鉄が溶出除去された珪藻土を用いるのが好ましい。鉄は、緑茶飲料において味に影響するばかりか、褐変の原因にもなるからである。珪藻土の酸処理の方法については、特に限定するものではないが、例えば、混合槽に珪藻土と酸性水とを投入した後攪拌する方法や、混合槽中の珪藻土と水との混合物に酸を添加した後攪拌する方法など、任意の方法で珪藻土と酸性水とを接触させた後、固液分離に続いて水洗浄し、水懸濁状態又は湿潤状態のまま珪藻土を用いる方法などを採用することができる。水懸濁状態又は湿潤状態のまま珪藻土を用いることにより、珪藻土から溶出する鉄分をより低減させることができる。なお、ここでの酸性水とは、pH7.0未満、好ましくはpH1〜5の酸性水(酸性を呈する水溶液)であり、例えばクエン酸、乳酸、酢酸等の有機酸や、燐酸、硝酸、塩酸等の無機酸の水溶液などを挙げることができる。
珪藻土にシリカゲル、パーライト、セルロース等の他の濾過助剤を混合して用いてもよい。
The diatomaceous earth used in the present invention is diatomaceous earth used as a filter aid, such as pulverized / dried diatomaceous earth or crushed / dried baked or melt-baked. Although it is possible to use it, it is preferable to use a diatomaceous earth filter aid having a Darcy of 0.05 to 0.1. By using Darcy 0.05-0.1 diatomaceous earth filter aid, a clearer packaged tea beverage can be produced. The term “Darcy 0.05 to 0.1 diatomaceous earth filter aid” means a diatomaceous earth filter aid having a Darcy permeability K in the range of 0.05 to 0.1. “Darcy's permeability K” is one of the indexes indicating the permeability of the filter aid, and can be determined by a water permeation method or an air permeation method. Currently, “Darcy” is commonly used so that diatomite filter aids can be purchased by specifying this value.
The diatomaceous earth used in the present invention is preferably diatomaceous earth from which iron is eluted and removed by acid treatment. This is because iron not only affects the taste in green tea beverages but also causes browning. The method for acid treatment of diatomaceous earth is not particularly limited, but for example, a method of adding diatomaceous earth and acidic water to a mixing tank and then stirring, or adding an acid to a mixture of diatomaceous earth and water in the mixing tank After diatomaceous earth and acidic water are brought into contact with each other by any method, such as a method of stirring, the solid-liquid separation is followed by water washing, and a method using diatomaceous earth in a water suspended state or wet state is adopted. Can do. By using diatomaceous earth in a water suspended state or a wet state, the iron content eluted from the diatomaceous earth can be further reduced. Here, the acidic water is acidic water having a pH of less than 7.0, preferably pH 1 to 5 (aqueous solution exhibiting acidity). For example, organic acids such as citric acid, lactic acid and acetic acid, phosphoric acid, nitric acid, hydrochloric acid An aqueous solution of an inorganic acid such as
You may mix and use other filter aids, such as a silica gel, a pearlite, and a cellulose, in diatomaceous earth.
(調合)
調合では、水(硬水、軟水、イオン交換水、天然水その他)、アスコルビン酸、アスコルビン酸ナトリウム、重曹、糖類、デキストリン、香料、乳化剤、安定剤、或いはその他の呈味原料などのいずれか或いはこれらのうち二種以上の組合わせを添加し、主にpH調整、濃度調整、味の調整を行うようにすればよい。例えば、pHを6前後に調整すると共にBrixを0.3前後に調整する例を挙げることができる。
(Formulation)
In preparation, water (hard water, soft water, ion exchange water, natural water, etc.), ascorbic acid, sodium ascorbate, baking soda, saccharides, dextrin, fragrance, emulsifier, stabilizer, or other flavoring ingredients, or any of these Of these, a combination of two or more kinds may be added to adjust pH, concentration, and taste. For example, an example in which pH is adjusted to around 6 and Brix is adjusted to around 0.3 can be given.
(殺菌及び容器充填)
加熱殺菌は、缶飲料であれば、必要に応じて再加熱(ホットパック)した後充填し、レトルト殺菌(例えば、適宜加圧下(1.2mmHgなど)、121℃で7分間加熱殺菌する。)を行い、プラスチックボトル飲料の場合にはUHT殺菌(調合液を120〜150℃で1秒〜数十秒保持する。)を行うようにすればよい。
(Sterilization and container filling)
If heat sterilization is a can drink, it will be reheated (hot pack) as needed, it will be filled, and retort sterilization (For example, heat sterilize at 121 degreeC for 7 minutes suitably under pressure (1.2 mmHg etc.)). In the case of a plastic bottle beverage, UHT sterilization (the prepared solution is held at 120 to 150 ° C. for 1 second to several tens of seconds) may be performed.
本発明で得られる緑茶飲料は、茶抽出液中のガラクツロン酸量を30〜50ppm、特に加温販売では35〜45ppmとし、或いは/及び、茶抽出液中のタンパク質量を6〜10ppm、特に加温販売では7〜9ppmとするようにするのが好ましい。よって、これらを指標に吸着工程におけるシリカの種類・添加量を選択及び調整するのが好ましい。なお、ガラクツロン酸量及びタンパク質量は実施例と同様に測定した値を基準とする。
ガラクツロン酸は、緑茶飲料のオリ発生原因の一つである多糖(ペクチン)を構成する成分であるため、緑茶飲料中のガラクツロン酸の含有量を測定することにより、オリ発生原因であるペクチンの総量が明らかになる。
The green tea beverage obtained by the present invention has a galacturonic acid content in the tea extract of 30 to 50 ppm, particularly 35 to 45 ppm in the warm sales, and / or a protein content in the tea extract of 6 to 10 ppm, especially added. In warm sales, the content is preferably 7 to 9 ppm. Therefore, it is preferable to select and adjust the type and amount of silica in the adsorption process using these as indices. The amount of galacturonic acid and the amount of protein are based on values measured in the same manner as in the examples.
Since galacturonic acid is a component of polysaccharide (pectin), which is one of the causes of occurrence of oli in green tea beverages, measuring the content of galacturonic acid in green tea beverages, the total amount of pectin that is the cause of oliogenesis Becomes clear.
また、加温販売用途を考えると、緑茶飲料の清澄度を、透過率(660nm)で93〜98T%、特に95〜98T%とするのが好ましい。この際、緑茶飲料の清澄度は、遠心分離及び珪藻土濾過などの濾過条件によって調整することができる。この意味では、緑茶飲料の清澄度を透過率(660nm)93〜98T%に調整することができれば、遠心分離及び珪藻土濾過をする代わりに、他の濾過方法、例えば限外濾過、微細濾過、精密濾過、逆浸透膜濾過、電気透析、生物機能性膜などの膜濾過、或いはこれらのいずれかを二つ以上を組合わせた濾過を採用することも可能である。ただし、茶飲料は酸素劣化の影響を受けやすいため、一般的にいわれる膜濾過・限外濾過で行われるクロスフロー方式よりも全濾過方式を採用するのが望ましく、濾過助剤を使用した濾滓濾過のような清澄濾過を遠心分離と組合わせて行うのが香味バランスの点から適している。中でも、本発明においては珪藻土濾過が濾液へのシリカの残留防止や特別な技術経験がなくても安定的に高品質の茶飲料を製造できる点で優れている。 Moreover, when considering the heating sales application, it is preferable that the clarity of the green tea beverage is 93 to 98 T%, particularly 95 to 98 T% in terms of transmittance (660 nm). At this time, the clarity of the green tea beverage can be adjusted by filtration conditions such as centrifugation and diatomaceous earth filtration. In this sense, if the clarity of the green tea beverage can be adjusted to a transmittance (660 nm) of 93 to 98 T%, instead of centrifugation and diatomaceous earth filtration, other filtration methods such as ultrafiltration, microfiltration, precision It is also possible to employ filtration, reverse osmosis membrane filtration, electrodialysis, membrane filtration such as a biofunctional membrane, or filtration combining any two of these. However, since tea beverages are susceptible to oxygen degradation, it is desirable to use the total filtration method rather than the cross-flow method that is commonly used for membrane filtration and ultrafiltration. It is suitable from the point of flavor balance to perform clarification filtration such as soot filtration in combination with centrifugation. Especially, in this invention, diatomaceous earth filtration is excellent at the point which can manufacture a high quality tea drink stably, without the residue prevention of the silica to a filtrate, and a special technical experience.
なお、上記の製造工程、すなわち抽出工程、粗濾過工程、吸着工程、遠心分離・珪藻土濾過を含む濾過工程、調合工程、殺菌工程、容器充填工程を経て緑茶飲料を製造する製造工程は本発明のあくまで一例であり、これに限定するものではない。例えば、工程の順序を入れ替えたり、別工程を付加したりすることもできる。 In addition, the manufacturing process which manufactures a green tea drink through said manufacturing process, ie, an extraction process, a rough filtration process, an adsorption process, a filtration process including centrifugation and diatomaceous earth filtration, a blending process, a sterilization process, and a container filling process is the present invention. This is merely an example, and the present invention is not limited to this. For example, the order of the steps can be changed, or another step can be added.
(試験1:常温保存での品質評価)
緑茶原料(静岡産やぶきた品種の一番茶と二番茶を50:50でブレンドしたものの浅蒸し緑茶)10gに対して80℃の熱水1000mlで3.5分間抽出した。得られた茶抽出液を80メッシュのステンレスフィルターで粗濾過し、粗濾過済みの茶抽出液を貯めたタンク内に、緑茶原料(茶葉質量)に対して各種添加量(表1参照)のシリカ(非晶質含水シリカ;水澤化学工業(株)社製「ミズカソープ」)を加え、30℃になるように強制冷却しながらシリカと十分接触するように茶抽出液(pH5.0)を15分間攪拌し、静置した後、ウエストファリアー社製SA1連続遠心分離機を使用して遠心分離(流速:300L/h、回転数:10000rpm、遠心沈降面積(Σ):1000m2)を行った。
次に、遠心分離後の濾過液にアスコルビン酸を300ppm添加し重曹にてpH6に調整し、イオン交換水を加えて1000mLに調整(メスアップ)した後、UHT殺菌(135℃、30秒)を行い、プレート内で冷却し、85℃にて透明プラスチック容器(PETボトル)に充填して容器詰緑茶飲料とした。その後キャップ部を30秒間転倒殺菌し、ただちに冷却した。
(Test 1: Quality evaluation at room temperature storage)
Extraction was performed for 3.5 minutes with 1000 ml of hot water at 80 ° C. with respect to 10 g of green tea material (shallow steamed green tea blended with 50:50 of the first and second teas from Shizuoka and Bukita varieties). The obtained tea extract is roughly filtered with an 80 mesh stainless steel filter, and various addition amounts (see Table 1) of silica are added to the green tea raw material (tea leaf mass) in the tank in which the roughly filtered tea extract is stored. (Amorphous hydrous silica; “Mizuka Soap” manufactured by Mizusawa Chemical Co., Ltd.) was added, and the tea extract (pH 5.0) was allowed to come into sufficient contact with silica while forcibly cooling to 30 ° C. for 15 minutes. After stirring and allowing to stand, centrifugation (flow rate: 300 L / h, rotation speed: 10,000 rpm, centrifugal sedimentation area (Σ): 1000 m 2) was performed using a SA1 continuous centrifuge manufactured by Westphalia.
Next, 300 ppm of ascorbic acid is added to the filtrate after centrifugation, pH is adjusted to 6 with sodium bicarbonate, ion-exchanged water is added to adjust to 1000 mL (measup), and then UHT sterilization (135 ° C., 30 seconds) is performed. And cooled in a plate and filled into a transparent plastic container (PET bottle) at 85 ° C. to give a container-packed green tea beverage. Thereafter, the cap part was sterilized by tumbling for 30 seconds, and immediately cooled.
上記の如く製造した容器詰緑茶飲料を室温にて2週間保存し、その後のオリの発生状況を観察するとともに、香味を評価した。香味の評価は10名のパネラーにより評価し判定した。
オリの評価は、次の基準を指標とした。
+++ :多量のオリ発生
++ :オリ発生
+ :若干のオリ発生
± :微粉発生
− :オリ発生無し
The container-packed green tea beverage produced as described above was stored at room temperature for 2 weeks, and the subsequent occurrence of orientation was observed and the flavor was evaluated. The evaluation of flavor was evaluated and judged by 10 panelists.
The following criteria were used as indicators for the evaluation of orientation.
++++: A large amount of occurrence ++: An occurrence of occurrence +: A slight occurrence of occurrence ±: Generation of fine powder −: No occurrence of occurrence
茶抽出液にシリカを添加し接触させることにより、オリの発生を抑制することができることが分かった。特に、緑茶原料(茶葉質量)に対し0.5倍量以上のシリカを添加し接触させた時にこの効果は顕著であった。他方、緑茶原料(茶葉質量)に対し20倍量を超える量を添加すると香味が薄くなることも分かった。 It was found that the occurrence of orientation can be suppressed by adding silica to the tea extract and bringing it into contact. In particular, this effect was remarkable when 0.5 times or more of silica was added and brought into contact with the green tea raw material (tea leaf mass). On the other hand, it was also found that when the amount exceeding 20 times the amount of green tea raw material (tea leaf mass) was added, the flavor became thin.
(試験2:加温保存した場合の品質評価)
緑茶原料(静岡産やぶきた品種の一番茶と二番茶を50:50でブレンドしたものの浅蒸し緑茶)10gに対して80℃の熱水1000mlで3.5分間抽出した。得られた茶抽出液を80メッシュのステンレスフィルターで粗濾過し、粗濾過済みの茶抽出液を貯めたタンク内に、緑茶原料(茶葉質量)に対して各種添加量(表2参照)のシリカ(非晶質含水シリカ;水澤化学工業(株)社製「ミズカソープ」)を加え、30℃になるように強制冷却しながらシリカと十分接触するように茶抽出液(pH5.0)を15分間攪拌し、静置した後、ウエストファリアー社製SA1連続遠心分離機を使用し、流速を200〜400L/hの間で変化させて遠心分離(回転数10000rpm、遠心沈降面積(Σ):1000m2)を行った。
次に、遠心分離後の濾過液にアスコルビン酸を300ppm添加し重曹にてpH6に調整し、イオン交換水を加えて1000mLに調整(メスアップ)した後、UHT殺菌(135℃、30秒)を行い、プレート内で冷却し、85℃にて透明プラスチック容器(PETボトル)に充填して容器詰緑茶飲料とした。その後キャップ部を30秒間転倒殺菌し、ただちに冷却した。
なお、容器詰緑茶飲料の清澄度(T%)は、遠心分離における流速を変化させることで調整した。
(Test 2: Quality evaluation when stored warm)
Extraction was performed for 3.5 minutes with 1000 ml of hot water at 80 ° C. with respect to 10 g of green tea material (shallow steamed green tea blended with 50:50 of the first and second teas from Shizuoka and Bukita varieties). The obtained tea extract is roughly filtered with an 80 mesh stainless steel filter, and various addition amounts (see Table 2) of silica are added to the green tea raw material (tea leaf mass) in the tank in which the roughly filtered tea extract is stored. (Amorphous hydrous silica; “Mizuka Soap” manufactured by Mizusawa Chemical Industry Co., Ltd.) was added, and the tea extract (pH 5.0) was added for 15 minutes so as to be in sufficient contact with silica while forcibly cooling to 30 ° C. After stirring and allowing to stand, SA1 continuous centrifuge manufactured by Westphalia Co. is used, and the flow rate is changed between 200 to 400 L / h, and the centrifugal separation (the number of revolutions is 10,000 rpm, the centrifugal sedimentation area (Σ) is 1000 m 2. )
Next, 300 ppm of ascorbic acid is added to the filtrate after centrifugation, pH is adjusted to 6 with sodium bicarbonate, ion-exchanged water is added to adjust to 1000 mL (measup), and then UHT sterilization (135 ° C., 30 seconds) is performed. And cooled in a plate and filled into a transparent plastic container (PET bottle) at 85 ° C. to give a container-packed green tea beverage. Thereafter, the cap part was sterilized by tumbling for 30 seconds, and immediately cooled.
The clarity (T%) of the packaged green tea beverage was adjusted by changing the flow rate in the centrifugation.
上記の如く製造した容器詰緑茶飲料を55℃の恒温槽にて2週間保存し、7日後・14日後のオリの発生状況を観察した。
清澄度(T%)は、サンプルをよく振り、透過率(660nm)を測定した。標準ガラスセルに4.0mLサンプリングし、測定装置:日立分光光度計U−3310で測定した。なお、後述する試験においても同様にT%を測定した。
なお、オリの評価は試験1と同様に行った。
The container-packed green tea beverage produced as described above was stored in a thermostatic bath at 55 ° C. for 2 weeks, and the occurrence of orientation was observed after 7 and 14 days.
For clarity (T%), the sample was shaken well and the transmittance (660 nm) was measured. 4.0 mL was sampled in a standard glass cell and measured with a measuring apparatus: Hitachi spectrophotometer U-3310. In the test described later, T% was similarly measured.
The orientation was evaluated in the same manner as in Test 1.
加温保管した場合には、緑茶原料(茶葉質量)に対し0.5倍量以上のシリカを添加してもオリの発生がみられたが、遠心分離の条件を調整して清澄度(T%)を高めることにより、加温保管の場合であってもオリの発生も抑制できることが判明した。 In the case of warm storage, the occurrence of orientation was observed even when silica more than 0.5 times the amount of green tea material (tea leaf mass) was added, but the clarification (T %) Can be suppressed even in the case of warm storage.
(試験3:濾過方法別での品質評価)
[製造方法3−1:遠心分離]
緑茶原料(静岡産やぶきた品種の一番茶と二番茶を50:50でブレンドしたものの浅蒸し緑茶)10gに対して80℃の熱水1000mlで3.5分間抽出した。得られた茶抽出液を80メッシュのステンレスフィルターで粗濾過し、粗濾過済みの茶抽出液を30℃になるように強制冷却し、静置した後、ウエストファリアー社製SA1連続遠心分離機を使用して遠心分離(流速:300L/h、回転数:10000rpm、遠心沈降面積(Σ):1000m2)を行った。
次に、遠心分離後の濾過液にアスコルビン酸を300ppm添加し重曹にてpH6に調整し、イオン交換水を加えて1000mLに調整(メスアップ)した後、UHT殺菌(135℃、30秒)を行い、プレート内で冷却し、85℃にて透明プラスチック容器(PETボトル)に充填し容器詰緑茶飲料とした。その後キャップ部を30秒間転倒殺菌し、ただちに冷却した。
(Test 3: Quality evaluation by filtration method)
[Production Method 3-1: Centrifugation]
Extraction was performed for 3.5 minutes with 1000 ml of hot water at 80 ° C. with respect to 10 g of green tea material (shallow steamed green tea blended with 50:50 of the first and second teas from Shizuoka and Bukita varieties). The obtained tea extract was roughly filtered with an 80-mesh stainless steel filter, and the roughly filtered tea extract was forcibly cooled to 30 ° C. and allowed to stand, and then SA1 continuous centrifuge manufactured by Westphalia. Was centrifuged (flow rate: 300 L / h, rotation speed: 10,000 rpm, centrifugal sedimentation area (Σ): 1000 m 2).
Next, 300 ppm of ascorbic acid is added to the filtrate after centrifugation, pH is adjusted to 6 with sodium bicarbonate, ion-exchanged water is added to adjust to 1000 mL (measup), and then UHT sterilization (135 ° C., 30 seconds) is performed. And cooled in a plate and filled into a transparent plastic container (PET bottle) at 85 ° C. to obtain a container-packed green tea beverage. Thereafter, the cap part was sterilized by tumbling for 30 seconds, and immediately cooled.
[製造方法3−2:遠心分離⇒珪藻土濾過]
緑茶原料(静岡産やぶきた品種の一番茶と二番茶を50:50でブレンドしたものの浅蒸し緑茶)10gに対して80℃の熱水1000mlで3.5分間抽出した。得られた茶抽出液を80メッシュのステンレスフィルターで粗濾過し、粗濾過済みの茶抽出液を30℃になるように強制冷却し、静置した後、ウエストファリアー社製SA1連続遠心分離機を使用して遠心分離(流速:300L/h、回転数:10000rpm、遠心沈降面積(Σ):1000m2)を行った。
次いで、遠心分離後の濾過液を、Darcy0.1の珪藻土を用いて珪藻土濾過を行い、珪藻土濾過処理液を得た。
次に、珪藻土濾過処理液にアスコルビン酸を300ppm添加し重曹にてpH6に調整し、イオン交換水を加えて1000mLに調整(メスアップ)した後、UHT殺菌(135℃、30秒)を行い、プレート内で冷却し、85℃にて透明プラスチック容器(PETボトル)に充填し容器詰緑茶飲料とした。その後キャップ部を30秒間転倒殺菌し、ただちに冷却した。
[Production method 3-2: Centrifugation ⇒ Diatomaceous earth filtration]
Extraction was performed for 3.5 minutes with 1000 ml of hot water at 80 ° C. with respect to 10 g of green tea material (shallow steamed green tea blended with 50:50 of the first and second teas from Shizuoka and Bukita varieties). The obtained tea extract was roughly filtered with an 80-mesh stainless steel filter, and the roughly filtered tea extract was forcibly cooled to 30 ° C. and allowed to stand, and then SA1 continuous centrifuge manufactured by Westphalia. Was centrifuged (flow rate: 300 L / h, rotation speed: 10,000 rpm, centrifugal sedimentation area (Σ): 1000 m 2).
Next, the filtrate after centrifugation was subjected to diatomaceous earth filtration using Darcy 0.1 diatomaceous earth to obtain a diatomaceous earth filtration treatment liquid.
Next, 300 ppm of ascorbic acid was added to the diatomaceous earth filtration treatment solution, adjusted to pH 6 with sodium bicarbonate, adjusted to 1000 mL with ion-exchanged water (meas up), and then subjected to UHT sterilization (135 ° C., 30 seconds), It was cooled in the plate and filled into a transparent plastic container (PET bottle) at 85 ° C. to obtain a container-packed green tea beverage. Thereafter, the cap part was sterilized by tumbling for 30 seconds, and immediately cooled.
[製造方法3−3:吸着工程⇒遠心分離]
緑茶原料(静岡産やぶきた品種の一番茶と二番茶を50:50でブレンドしたものの浅蒸し緑茶)10gに対して80℃の熱水1000mlで3.5分間抽出した。得られた茶抽出液を80メッシュのステンレスフィルターで粗濾過し、粗濾過済みの茶抽出液を貯めたタンク内に、緑茶原料(茶葉質量)に対し2倍量のシリカ(非晶質含水シリカ;水澤化学工業(株)社製「ミズカソープ」)を加え、30℃になるように強制冷却しながらシリカと十分接触するように茶抽出液(pH5.0)を15分間攪拌し、静置した後、ウエストファリアー社製SA1連続遠心分離機を使用して遠心分離(流速:300L/h、回転数:10000rpm、遠心沈降面積(Σ):1000m2)を行った。
次に、遠心分離後の濾過液にアスコルビン酸を300ppm添加し重曹にてpH6に調整し、イオン交換水を加えて1000mLに調整(メスアップ)した後、UHT殺菌(135℃、30秒)を行い、プレート内で冷却し、85℃にて透明プラスチック容器(PETボトル)に充填し容器詰緑茶飲料とした。その後キャップ部を30秒間転倒殺菌し、ただちに冷却した。
[Manufacturing method 3-3: adsorption process ⇒ centrifugation]
Extraction was performed for 3.5 minutes with 1000 ml of hot water at 80 ° C. with respect to 10 g of green tea material (shallow steamed green tea blended with 50:50 of the first and second teas from Shizuoka and Bukita varieties). The obtained tea extract is roughly filtered with an 80 mesh stainless steel filter, and the amount of silica (amorphous hydrous silica) is twice as large as the green tea raw material (tea leaf mass) in the tank where the roughly filtered tea extract is stored. Mizusawa Chemical Co., Ltd. “Mizuka Soap”) was added, and the tea extract (pH 5.0) was stirred for 15 minutes so that it was in sufficient contact with silica while forcibly cooling to 30 ° C. and allowed to stand. Thereafter, centrifugation (flow rate: 300 L / h, rotation speed: 10,000 rpm, centrifugal sedimentation area (Σ): 1000 m 2) was performed using a SA1 continuous centrifuge manufactured by Westphalia.
Next, 300 ppm of ascorbic acid is added to the filtrate after centrifugation, pH is adjusted to 6 with sodium bicarbonate, ion-exchanged water is added to adjust to 1000 mL (measup), and then UHT sterilization (135 ° C., 30 seconds) is performed. And cooled in a plate and filled into a transparent plastic container (PET bottle) at 85 ° C. to obtain a container-packed green tea beverage. Thereafter, the cap part was sterilized by tumbling for 30 seconds, and immediately cooled.
[製造方法3−4:吸着工程⇒遠心分離⇒珪藻土濾過(酸未処理品使用)]
緑茶原料(静岡産やぶきた品種の一番茶と二番茶を50:50でブレンドしたものの浅蒸し緑茶)10gに対して80℃の熱水1000mlで3.5分間抽出した。得られた茶抽出液を80メッシュのステンレスフィルターで粗濾過し、粗濾過済みの茶抽出液を貯めたタンク内に、緑茶原料(茶葉質量)に対して2倍量のシリカ(非晶質含水シリカ;水澤化学工業(株)社製「ミズカソープ」)を加え、30℃になるように強制冷却しながらシリカと十分接触するように茶抽出液(pH5.0)を15分間攪拌し、静置した後、ウエストファリアー社製SA1連続遠心分離機を使用して遠心分離(流速:300L/h、回転数:10000rpm、遠心沈降面積(Σ):1000m2)を行った。
次いで、遠心分離後の濾過液を、Darcy0.1の珪藻土を用いて珪藻土濾過を行い、珪藻土濾過処理液を得た。
次に、珪藻土濾過処理液にアスコルビン酸を300ppm添加し重曹にてpH6に調整し、イオン交換水を加えて1000mLに調整(メスアップ)した後、UHT殺菌(135℃、30秒)を行い、プレート内で冷却し、85℃にて透明プラスチック容器(PETボトル)に充填し容器詰緑茶飲料とした。その後キャップ部を30秒間転倒殺菌し、ただちに冷却した。
[Production method 3-4: Adsorption process ⇒ Centrifugation ⇒ Diatomaceous earth filtration (use of acid untreated product)]
Extraction was performed for 3.5 minutes with 1000 ml of hot water at 80 ° C. with respect to 10 g of green tea material (shallow steamed green tea blended with 50:50 of the first and second teas from Shizuoka and Bukita varieties). The obtained tea extract is roughly filtered with an 80 mesh stainless steel filter, and the amount of silica (amorphous water content) is twice as much as the green tea raw material (tea leaf mass) in the tank in which the roughly filtered tea extract is stored. Silica; “Mizuka Soap” manufactured by Mizusawa Chemical Co., Ltd.) was added, and the tea extract (pH 5.0) was stirred for 15 minutes so that it was in sufficient contact with silica while forcibly cooling to 30 ° C. and allowed to stand. After that, centrifugal separation (flow rate: 300 L / h, rotation speed: 10,000 rpm, centrifugal sedimentation area (Σ): 1000 m 2) was performed using a SA1 continuous centrifuge manufactured by Westphalia.
Next, the filtrate after centrifugation was subjected to diatomaceous earth filtration using Darcy 0.1 diatomaceous earth to obtain a diatomaceous earth filtration treatment liquid.
Next, 300 ppm of ascorbic acid was added to the diatomaceous earth filtration treatment solution, adjusted to pH 6 with sodium bicarbonate, adjusted to 1000 mL with ion-exchanged water (meas up), and then subjected to UHT sterilization (135 ° C., 30 seconds), It was cooled in the plate and filled into a transparent plastic container (PET bottle) at 85 ° C. to obtain a container-packed green tea beverage. Thereafter, the cap part was sterilized by tumbling for 30 seconds, and immediately cooled.
[製造方法3−5:吸着工程⇒遠心分離⇒珪藻土濾過(酸処理品使用)]
珪藻土濾過に用いる珪藻土として、酸処理した珪藻土を使用し、その他は上記製造方法3−4と同様に、容器詰緑茶飲料を製造した。
なお、珪藻土の酸処理は、製造方法3−3で使用した珪藻土を40倍量の塩酸液(2.5%濃度)に浸し、24時間攪拌しながら室温にて放置した後、水洗いして濾液がpH5になるまで洗浄した後、回転式ドラムにて乾燥するように行った。
[Production method 3-5: Adsorption process ⇒ Centrifugation ⇒ Diatomaceous earth filtration (Use of acid-treated product)]
As the diatomaceous earth used for diatomaceous earth filtration, acid-treated diatomaceous earth was used, and the others were produced in the same manner as in the above production method 3-4.
In addition, the acid treatment of diatomaceous earth involves immersing the diatomaceous earth used in Production Method 3-3 in 40 times the amount of hydrochloric acid solution (2.5% concentration), leaving it to stand at room temperature with stirring for 24 hours, washing with water, and filtrate. Was washed until the pH reached 5 and then dried on a rotary drum.
上記の如く製造した容器詰緑茶飲料([3−1]〜[3−5])を37℃又は55℃の恒温槽内にて30日間保存し、7日後・14日後・30日後のオリの発生状況、水色、香味を観察及び評価した。
水色、香味の評価は10名のパネラーにより評価し判定した。
また、オリの評価は、試験1と同様に行った。
Container-packed green tea beverages ([3-1] to [3-5]) produced as described above are stored in a constant temperature bath at 37 ° C. or 55 ° C. for 30 days, after 7 days, 14 days, and 30 days. Occurrence, light blue, and flavor were observed and evaluated.
Light blue and flavor were evaluated and judged by 10 panelists.
The evaluation of orientation was performed in the same manner as in Test 1.
長期(30日)で加温保管した場合、シリカ吸着に続いて遠心分離を行って清澄度を高めることにより、沈殿の発生を抑えることができたが、濁りの発生が若干みられた(3−3)。さらに珪藻土で清澄性を高めたものは、そのような濁りの発生もみられなかった(3−5)。なお、酸処理してない珪藻土で濾過したものは著しく変色した(3−4)。 When heated and stored for a long time (30 days), it was possible to suppress precipitation by centrifuging following silica adsorption to increase clarification, but some turbidity was observed (3 -3). Furthermore, diatomaceous earth with higher clarity did not show such turbidity (3-5). In addition, what was filtered with the diatomaceous earth which has not been acid-treated changed the color remarkably (3-4).
(試験4:珪藻土濾材の鉄溶出量の評価)
珪藻土濾材5gを、精製水(イオン交換水)100mLに浸し24時間室温にて静置(途中5回攪拌)した後、濾材と精製水を濾過分離し、濾液(精製水)について鉄分量を簡易鉄分分析器(発色吸光度)にて測定した。その結果、もとの珪藻土1g当りに換算して鉄溶出量としたところ、鉄溶出量/珪藻土は0.10μg/gであった。
(Test 4: Evaluation of iron elution from diatomaceous earth filter media)
5 g of diatomaceous earth filter medium is immersed in 100 mL of purified water (ion exchange water) and allowed to stand at room temperature for 24 hours (stirring 5 times in the middle), then the filter medium and purified water are separated by filtration, and the iron content of the filtrate (purified water) is simplified. It was measured with an iron analyzer (color absorbance). As a result, when the iron elution amount was converted to 1 g of the original diatomaceous earth, the iron elution amount / diatomaceous earth was 0.10 μg / g.
(試験5:濾過方法別でのガラクツロン酸及びタンパク質の含有量測定)
[製造方法5−1:吸着工程⇒遠心分離]
緑茶原料(静岡産やぶきた品種の一番茶と二番茶を50:50でブレンドしたものの浅蒸し緑茶)10gに対して80℃の熱水1000mlで3.5分間抽出した。得られた茶抽出液を80メッシュのステンレスフィルターで粗濾過し、粗濾過済みの茶抽出液を貯めたタンク内に、緑茶原料(茶葉質量)に対し0倍量、0.5倍量、5倍量又は20倍量のシリカ(非晶質含水シリカ;水澤化学工業(株)社製「ミズカソープ」)を加え、30℃になるように強制冷却しながらシリカと十分接触するように茶抽出液(pH5.0)を15分間攪拌し、静置した後、ウエストファリアー社製SA1連続遠心分離機を使用して遠心分離(流速:300L/h、回転数:10000rpm、遠心沈降面積(Σ):1000m2)を行った。
次に、遠心分離後の濾過液にアスコルビン酸を300ppm添加し重曹にてpH6に調整し、イオン交換水を加えて1000mLに調整(メスアップ)した後、UHT殺菌(135℃、30秒)を行い、プレート内で冷却し、85℃にて透明プラスチック容器(PETボトル)に充填し容器詰緑茶飲料とした。その後キャップ部を30秒間転倒殺菌し、ただちに冷却し、これを容器詰緑茶飲料試料とした。
(Test 5: Content measurement of galacturonic acid and protein by filtration method)
[Production Method 5-1: Adsorption Step ⇒ Centrifugation]
Extraction was performed for 3.5 minutes with 1000 ml of hot water at 80 ° C. with respect to 10 g of green tea material (shallow steamed green tea blended with 50:50 of the first and second teas from Shizuoka and Bukita varieties). The obtained tea extract is roughly filtered with an 80 mesh stainless steel filter, and the amount of the green tea raw material (tea leaf mass) is 0 times, 0.5 times, 5 times in the tank storing the roughly filtered tea extract. Double or 20 times the amount of silica (amorphous hydrous silica; “Mizuka Soap” manufactured by Mizusawa Chemical Industry Co., Ltd.) is added, and the tea extract is brought into sufficient contact with the silica while forcibly cooling to 30 ° C. (PH 5.0) was stirred for 15 minutes and allowed to stand, and then centrifuged using a SA1 continuous centrifuge manufactured by Westphalia (flow rate: 300 L / h, rotation speed: 10,000 rpm, centrifugal sedimentation area (Σ) : 1000 m2).
Next, 300 ppm of ascorbic acid is added to the filtrate after centrifugation, pH is adjusted to 6 with sodium bicarbonate, ion-exchanged water is added to adjust to 1000 mL (measup), and then UHT sterilization (135 ° C., 30 seconds) is performed. And cooled in a plate and filled into a transparent plastic container (PET bottle) at 85 ° C. to obtain a container-packed green tea beverage. Thereafter, the cap part was sterilized by overturning for 30 seconds, and immediately cooled, and this was used as a packaged green tea beverage sample.
[製造方法5−2:吸着工程⇒遠心分離⇒珪藻土濾過(酸処理品使用)]
緑茶原料(静岡産やぶきた品種の一番茶と二番茶を50:50でブレンドしたものの浅蒸し緑茶)10gに対して80℃の熱水1000mlで3.5分間抽出した。得られた茶抽出液を80メッシュのステンレスフィルターで粗濾過し、粗濾過済みの茶抽出液を貯めたタンク内に、緑茶原料(茶葉質量)に対し0倍量、0.5倍量、5倍量又は20倍量のシリカ(非晶質含水シリカ;水澤化学工業(株)社製「ミズカソープ」)を加え、30℃になるように強制冷却しながらシリカと十分接触するように茶抽出液(pH5.0)を15分間攪拌し、静置した後、ウエストファリアー社製SA1連続遠心分離機を使用して遠心分離(流速:300L/h、回転数:10000rpm、遠心沈降面積(Σ):1000m2)を行った。
次いで、遠心分離後の濾過液を、Darcy0.1の酸処理済み珪藻土を用いて珪藻土濾過を行い、珪藻土濾過処理液を得た。
次に、珪藻土濾過処理液にアスコルビン酸を300ppm添加し重曹にてpH6に調整し、イオン交換水を加えて1000mLに調整(メスアップ)した後、UHT殺菌(135℃、30秒)を行い、プレート内で冷却し、85℃にて透明プラスチック容器(PETボトル)に充填し容器詰緑茶飲料とした。その後キャップ部を30秒間転倒殺菌し、ただちに冷却し、これを容器詰緑茶飲料試料とした。
珪藻土の酸処理は、Darcy0.1の珪藻土を40倍量の塩酸液(2.5%濃度)に浸し、24時間攪拌しながら室温にて放置した後、水洗いして濾液がpH5になるまで洗浄した後、回転式ドラムにて乾燥するように行った。
[Production Method 5-2: Adsorption Process ⇒ Centrifugation ⇒ Diatomaceous Earth Filtration (Using Acid-treated Products)]
Extraction was performed for 3.5 minutes with 1000 ml of hot water at 80 ° C. with respect to 10 g of green tea material (shallow steamed green tea blended with 50:50 of the first and second teas from Shizuoka and Bukita varieties). The obtained tea extract is roughly filtered with an 80 mesh stainless steel filter, and the amount of the green tea raw material (tea leaf mass) is 0 times, 0.5 times, 5 times in the tank storing the roughly filtered tea extract. Double or 20 times the amount of silica (amorphous hydrous silica; “Mizuka Soap” manufactured by Mizusawa Chemical Industry Co., Ltd.) is added, and the tea extract is brought into sufficient contact with the silica while forcibly cooling to 30 ° C. (PH 5.0) was stirred for 15 minutes and allowed to stand, and then centrifuged using a SA1 continuous centrifuge manufactured by Westphalia (flow rate: 300 L / h, rotation speed: 10,000 rpm, centrifugal sedimentation area (Σ) : 1000 m2).
Subsequently, the filtrate after centrifugation was subjected to diatomaceous earth filtration using Darcy 0.1 acid-treated diatomaceous earth to obtain a diatomaceous earth filtered liquid.
Next, 300 ppm of ascorbic acid was added to the diatomaceous earth filtration treatment solution, adjusted to pH 6 with sodium bicarbonate, adjusted to 1000 mL with ion-exchanged water (meas up), and then subjected to UHT sterilization (135 ° C., 30 seconds), It was cooled in the plate and filled into a transparent plastic container (PET bottle) at 85 ° C. to obtain a container-packed green tea beverage. Thereafter, the cap part was sterilized by overturning for 30 seconds, and immediately cooled, and this was used as a packaged green tea beverage sample.
The acid treatment of diatomaceous earth involves immersing Darcy 0.1 diatomaceous earth in 40 volumes of hydrochloric acid solution (2.5% concentration), leaving it to stand at room temperature with stirring for 24 hours, and then washing with water until the filtrate reaches
[ガラクツロン酸の分析]
製造方法5−1及び5−2で得られた各容器詰緑茶飲料試料100mLを、カラムクロマトグラフィー(セファデックスLH−20)により除タンニンし、その後5倍濃縮した。濃縮液1mLに対してエタノール4mL添加し、−30℃で一晩冷却した。冷却後遠心分離にかけて上清を捨て、エタノールで2回洗浄後、減圧乾固し分析用試料とした。
減圧乾固した分析用試料全量を1mLの蒸留水で溶かし、氷冷した0.025M四ホウ酸ナトリウム5mLを添加し、熱水中で10分間反応させた。
反応後、室温で冷却させた後、7.5mMカルバゾール液200μLを添加し、更に熱水中で10分間反応させた。室温で冷却させた後、530nmの吸光度で測定し(分析装置:日立分光光度計 U−3310)、ガラクツロン酸含有量を測定した。結果を図1及び図2に示す。
[Analysis of galacturonic acid]
100 mL of each container-packed green tea beverage sample obtained by Production Methods 5-1 and 5-2 was removed by tannin by column chromatography (Sephadex LH-20), and then concentrated 5 times. 4 mL of ethanol was added to 1 mL of the concentrated solution, and the mixture was cooled at −30 ° C. overnight. After cooling, the supernatant was discarded by centrifugation, washed twice with ethanol, and then dried under reduced pressure to obtain a sample for analysis.
The whole sample for analysis dried under reduced pressure was dissolved in 1 mL of distilled water, and 5 mL of ice-cooled 0.025 M sodium tetraborate was added and reacted in hot water for 10 minutes.
After the reaction, the mixture was cooled at room temperature, 200 μL of 7.5 mM carbazole solution was added, and further reacted in hot water for 10 minutes. After cooling at room temperature, the absorbance was measured at 530 nm (analyzer: Hitachi spectrophotometer U-3310), and the galacturonic acid content was measured. The results are shown in FIGS.
[タンパク質の分析]
上記製造方法5−1及び5−2で得られた各容器詰緑茶飲料試料100mLを、カラムクロマトグラフィー(セファデックスLH−20)により除タンニンし、その後5倍濃縮した。濃縮液1mLに対してエタノール4mL添加し、−30℃で一晩冷却した。冷却後遠心分離にかけて上清を捨て、エタノールで2回洗浄後、減圧乾固し、更に15%トリクロロ酢酸でタンパク質を沈澱させ、定量用試料とした。
前記定量用試料全量を100μLの蒸留水に溶解後、1NのNaOHで30分以上かけて溶解させた。溶解後、炭酸ナトリウムアルカリ性銅試薬1mLを加え、10分間以上放置した。その後、Folin試薬100μLを添加し、素早く混合した後、30分間以上放置して吸光度750nmで測定し(分析装置:日立分光光度計 U−3310)、タンパク質の含有量を測定した。結果を図1及び図2に示す。
[Protein analysis]
100 mL of each container-packed green tea beverage sample obtained by the above production methods 5-1 and 5-2 was removed by tannin by column chromatography (Sephadex LH-20), and then concentrated 5 times. 4 mL of ethanol was added to 1 mL of the concentrated solution, and the mixture was cooled at −30 ° C. overnight. After cooling, the supernatant was discarded by centrifugation, washed twice with ethanol, dried under reduced pressure, and further precipitated with 15% trichloroacetic acid to obtain a sample for quantification.
The whole sample for quantification was dissolved in 100 μL of distilled water, and then dissolved in 1N NaOH over 30 minutes. After dissolution, 1 mL of sodium carbonate alkaline copper reagent was added and left for 10 minutes or longer. Thereafter, 100 μL of Folin reagent was added and mixed rapidly, and then allowed to stand for 30 minutes or more, and the absorbance was measured at 750 nm (analyzer: Hitachi spectrophotometer U-3310), and the protein content was measured. The results are shown in FIGS.
[T%の測定]
上記製造方法5−2で得られた各容器詰緑茶飲料試料(サンプル)をよく振り、透過率(660nm)を測定した。標準ガラスセルに4.0mLサンプリングし、測定装置:日立分光光度計U−3310で測定した。
[Measurement of T%]
Each container-packed green tea beverage sample (sample) obtained by the production method 5-2 was shaken well, and the transmittance (660 nm) was measured. 4.0 mL was sampled in a standard glass cell and measured with a measuring apparatus: Hitachi spectrophotometer U-3310.
茶抽出液にシリカを添加して接触させ、その後遠心分離することにより(試験5−1)、遠心後のガラクツロン酸とタンパク質の量は減少し、清澄度も高くなった。また、遠心後にさらに珪藻土濾過した場合(試験5−2)も、試験5−1と同様の傾向がみられた。
なお、酸処理しない珪藻土を使用して製造方法5−2と同様に容器詰緑茶飲料試料を作製したが、著しく変色、沈殿し、ガラクツロン酸及びタンパク質の分析は不可能であった。
Silica was added to and brought into contact with the tea extract, and then centrifuged (Test 5-1). As a result, the amounts of galacturonic acid and protein after centrifugation were reduced and the clarity was increased. Further, when diatomaceous earth was filtered after centrifugation (Test 5-2), the same tendency as in Test 5-1 was observed.
In addition, the container-packed green tea beverage sample was produced using the diatomaceous earth which is not acid-treated like the manufacturing method 5-2, However, discoloration and precipitation remarkably, and the analysis of galacturonic acid and protein was impossible.
(試験6:濾過方法別でのカテキンの含有量測定)
[製造方法6−1:吸着工程⇒遠心分離⇒珪藻土濾過(酸処理品使用)]
緑茶原料(静岡産やぶきた品種の一番茶と二番茶を50:50でブレンドしたものの浅蒸し緑茶)10gに対して85℃の熱水1000mlで3.5分間抽出した。得られた茶抽出液を80メッシュのステンレスフィルターで粗濾過し、粗濾過済みの茶抽出液を貯めたタンク内に、緑茶原料(茶葉質量)に対し5倍量のシリカ(非晶質含水シリカ;水澤化学工業(株)社製「ミズカソープ」)を加え、30℃になるように強制冷却しながらシリカと十分接触するように茶抽出液(pH5.0)を15分間攪拌し、静置した後、ウエストファリアー社製SA1連続遠心分離機を使用して遠心分離(流速:300L/h、回転数:10000rpm、遠心沈降面積(Σ):1000m2)を行った。
次いで、遠心分離後の濾過液を、Darcy0.1の酸処理済み珪藻土を用いて珪藻土濾過を行い、珪藻土濾過処理液を得た。
次に、珪藻土濾過処理液にアスコルビン酸を300ppm添加し重曹にてpH6に調整し、これにイオン交換水を加えて1000mLに調整(メスアップ)した後、UHT殺菌(135℃、30秒)を行い、プレート内で冷却し、85℃にて透明プラスチック容器(PETボトル)に充填し容器詰緑茶飲料とした。その後キャップ部を30秒間転倒殺菌し、ただちに冷却し、これを容器詰緑茶飲料試料とした。
なお、珪藻土の酸処理は、Darcy0.1の珪藻土を40倍量の塩酸液(2.5%濃度)に浸し、24時間攪拌しながら室温にて放置した後、水洗いして濾液がpH5になるまで洗浄した後、回転式ドラムにて乾燥するように行った。
(Test 6: Measurement of catechin content by filtration method)
[Production method 6-1: Adsorption process ⇒ Centrifugation ⇒ Diatomaceous earth filtration (using acid-treated product)]
Extraction was performed for 3.5 minutes with 1000 ml of hot water at 85 ° C. with respect to 10 g of green tea raw material (shallow steamed green tea obtained by blending the first and second teas of Shizuoka and Bukita varieties at 50:50). The obtained tea extract is roughly filtered with an 80 mesh stainless steel filter, and the amount of silica (amorphous hydrous silica) is 5 times the amount of green tea raw material (tea leaf mass) in the tank in which the roughly filtered tea extract is stored. Mizusawa Chemical Co., Ltd. “Mizuka Soap”) was added, and the tea extract (pH 5.0) was stirred for 15 minutes so that it was in sufficient contact with silica while forcibly cooling to 30 ° C. and allowed to stand. Thereafter, centrifugation (flow rate: 300 L / h, rotation speed: 10,000 rpm, centrifugal sedimentation area (Σ): 1000 m 2) was performed using a SA1 continuous centrifuge manufactured by Westphalia.
Subsequently, the filtrate after centrifugation was subjected to diatomaceous earth filtration using Darcy 0.1 acid-treated diatomaceous earth to obtain a diatomaceous earth filtered liquid.
Next, 300 ppm of ascorbic acid was added to the diatomaceous earth filtration treatment solution, adjusted to pH 6 with sodium bicarbonate, ion-exchanged water was added to adjust to 1000 mL (meas up), and then UHT sterilization (135 ° C., 30 seconds) was performed. And cooled in a plate and filled into a transparent plastic container (PET bottle) at 85 ° C. to obtain a container-packed green tea beverage. Thereafter, the cap part was sterilized by overturning for 30 seconds, and immediately cooled, and this was used as a packaged green tea beverage sample.
The acid treatment of diatomaceous earth involves immersing Darcy 0.1 diatomaceous earth in 40 volumes of hydrochloric acid solution (2.5% concentration), leaving it to stand at room temperature with stirring for 24 hours, and then washing with water to bring the filtrate to
[製造方法6−2:遠心分離⇒珪藻土濾過]
緑茶原料(静岡産やぶきた品種の一番茶と二番茶を50:50でブレンドしたものの浅蒸し緑茶)10gに対して85℃の熱水1000mlで3.5分間抽出した。得られた茶抽出液を80メッシュのステンレスフィルターで粗濾過し、粗濾過済みの茶抽出液を30℃になるように強制冷却し、静置した後、ウエストファリアー社製SA1連続遠心分離機を使用して遠心分離(流速:300L/h、回転数:10000rpm、遠心沈降面積(Σ):1000m2)を行った。
次に、遠心分離後の濾過液にアスコルビン酸を300ppm添加し重曹にてpH6に調整し、イオン交換水を加えて1000mLに調整(メスアップ)した後、UHT殺菌(135℃、30秒)を行い、プレート内で冷却し、85℃にて透明プラスチック容器(PETボトル)に充填し容器詰緑茶飲料とした。その後キャップ部を30秒間転倒殺菌し、ただちに冷却し、これを容器詰緑茶飲料試料とした。
[Production method 6-2: Centrifugation ⇒ Diatomaceous earth filtration]
Extraction was performed for 3.5 minutes with 1000 ml of hot water at 85 ° C. with respect to 10 g of green tea raw material (shallow steamed green tea obtained by blending the first and second teas of Shizuoka and Bukita varieties at 50:50). The obtained tea extract was roughly filtered with an 80-mesh stainless steel filter, and the roughly filtered tea extract was forcibly cooled to 30 ° C. and allowed to stand, and then SA1 continuous centrifuge manufactured by Westphalia. Was centrifuged (flow rate: 300 L / h, rotation speed: 10,000 rpm, centrifugal sedimentation area (Σ): 1000 m 2).
Next, 300 ppm of ascorbic acid is added to the filtrate after centrifugation, pH is adjusted to 6 with sodium bicarbonate, ion-exchanged water is added to adjust to 1000 mL (measup), and then UHT sterilization (135 ° C., 30 seconds) is performed. And cooled in a plate and filled into a transparent plastic container (PET bottle) at 85 ° C. to obtain a container-packed green tea beverage. Thereafter, the cap part was sterilized by overturning for 30 seconds, and immediately cooled, and this was used as a packaged green tea beverage sample.
[製造方法6−3:キトサン添加⇒遠心分離]
緑茶原料(静岡産やぶきた品種の一番茶と二番茶を50:50でブレンドしたものの浅蒸し緑茶)10gに対して85℃の熱水1000mlで3.5分間抽出した。得られた茶抽出液を80メッシュのステンレスフィルターで粗濾過し、粗濾過済みの茶抽出液を貯めたタンク内に、緑茶原料(茶葉質量)に対して0.3質量%のキトサンを添加した。添加後、30℃になるように強制冷却しながらキトサンと十分接触するように茶抽出液(pH5.0)を15分間攪拌し、静置した後、ウエストファリアー社製SA1連続遠心分離機を使用して遠心分離(流速:300L/h、回転数:10000rpm、遠心沈降面積(Σ):1000m2)を行った。
次に、遠心分離後の濾過液にアスコルビン酸を300ppm添加し重曹にてpH6に調整し、イオン交換水を加えて1000mLに調整(メスアップ)した後、UHT殺菌(135℃、30秒)を行い、プレート内で冷却し、85℃にて透明プラスチック容器(PETボトル)に充填し容器詰緑茶飲料とした。その後キャップ部を30秒間転倒殺菌し、ただちに冷却し、これを容器詰緑茶飲料試料とした。
[Production method 6-3: addition of chitosan ⇒ centrifugation]
Extraction was performed for 3.5 minutes with 1000 ml of hot water at 85 ° C. with respect to 10 g of green tea raw material (shallow steamed green tea obtained by blending the first and second teas of Shizuoka and Bukita varieties at 50:50). The obtained tea extract was roughly filtered with an 80 mesh stainless steel filter, and 0.3% by mass of chitosan was added to the green tea raw material (tea leaf mass) into the tank in which the roughly filtered tea extract was stored. . After the addition, the tea extract (pH 5.0) was stirred for 15 minutes so as to be in sufficient contact with chitosan while forcedly cooling to 30 ° C. and allowed to stand, and then a West Farier SA1 continuous centrifuge was used. Centrifugation (flow rate: 300 L / h, rotation speed: 10,000 rpm, centrifugal sedimentation area (Σ): 1000 m 2) was performed.
Next, 300 ppm of ascorbic acid is added to the filtrate after centrifugation, pH is adjusted to 6 with sodium bicarbonate, ion-exchanged water is added to adjust to 1000 mL (measup), and then UHT sterilization (135 ° C., 30 seconds) is performed. And cooled in a plate and filled into a transparent plastic container (PET bottle) at 85 ° C. to obtain a container-packed green tea beverage. Thereafter, the cap part was sterilized by overturning for 30 seconds, and immediately cooled, and this was used as a packaged green tea beverage sample.
[製造方法6−4:遠心分離⇒膜処理]
緑茶原料(静岡産やぶきた品種の一番茶と二番茶を50:50でブレンドしたものの浅蒸し緑茶)10gに対して85℃の熱水1000mlで3.5分間抽出した。得られた茶抽出液を80メッシュのステンレスフィルターで粗濾過し、粗濾過済みの茶抽出液を30℃になるように強制冷却した後、ウエストファリアー社製SA1連続遠心分離機を使用して遠心分離(流速:300L/h、回転数:10000rpm、遠心沈降面積(Σ):1000m2)を行った。
次に、遠心分離後の濾過液を膜処理した。膜処理は、膜処理装置(日東電工社製メンブランマスター)、ミリポワ社製UF膜(100,000分画)を使用し、処理圧力6kg/cm2で膜濾過した。
そして、膜濾過処理液にアスコルビン酸を300ppm添加し重曹にてpH6に調整し、イオン交換水を加えて1000mLに調整(メスアップ)した後、UHT殺菌(135℃、30秒)を行い、プレート内で冷却し、85℃にて透明プラスチック容器(PETボトル)に充填し容器詰緑茶飲料とした。その後キャップ部を30秒間転倒殺菌し、ただちに冷却し、これを容器詰緑茶飲料試料とした。
[Production method 6-4: Centrifugal separation → Membrane treatment]
Extraction was performed for 3.5 minutes with 1000 ml of hot water at 85 ° C. with respect to 10 g of green tea raw material (shallow steamed green tea obtained by blending the first and second teas of Shizuoka and Bukita varieties at 50:50). The obtained tea extract was roughly filtered with an 80-mesh stainless steel filter, and the roughly filtered tea extract was forcibly cooled to 30 ° C., and then used with a Westphalia SA1 continuous centrifuge. Centrifugation (flow rate: 300 L / h, rotation speed: 10,000 rpm, centrifugal sedimentation area (Σ): 1000 m 2) was performed.
Next, the filtrate after centrifugation was subjected to membrane treatment. For membrane treatment, membrane filtration was performed using a membrane treatment apparatus (membrane master manufactured by Nitto Denko Corporation) and a UF membrane (100,000 fraction) manufactured by Millipore Corporation at a treatment pressure of 6 kg / cm 2.
Then, 300 ppm of ascorbic acid was added to the membrane filtration treatment solution, adjusted to pH 6 with sodium bicarbonate, adjusted to 1000 mL with ion-exchanged water (meas up), UHT sterilization (135 ° C., 30 seconds), and plate It was cooled inside and filled into a transparent plastic container (PET bottle) at 85 ° C. to obtain a container-packed green tea drink. Thereafter, the cap part was sterilized by overturning for 30 seconds, and immediately cooled, and this was used as a packaged green tea beverage sample.
[カテキン類の分析方法]
粗濾過済みの茶抽出液をコントロールとし、各容器詰緑茶飲料試料中のカテキン量を次のように測定し、カテキン残存率を測定した。結果を表4に示す。
[Method for analyzing catechins]
Using the roughly filtered tea extract as a control, the amount of catechin in each containered green tea beverage sample was measured as follows, and the catechin residual rate was measured. The results are shown in Table 4.
1)装置および器具
高速液体クロマトグラフユニット:日立製作所D-7000 HPLCシステム
HPLC用カラム:YMC Jsphere ODS-H80 φ4.6×250mm
2)試薬
移動相:アセトニトリル(高速液体クロマトグラフ用または特級)、リン酸(特級)、超純水(0.45μmで処理したイオン交換水)
カテキン標準液:(-)-エピガロカテキンガレート(EGCg)、(-)-エピカテキンガレート(ECg)、(-)-エピカテキン(EC)、(-)-エピガロカテキン(EGC)、(-)-ガロカテキンガレート(GCg)、(-)-カテキンガレート(Cg)、(-)-ガロカテキン(GC)、(+)-カテキン(C)
3)試料の定量法
容器詰緑茶飲料試料5mlを正確に量り、50ml容メスフラスコに入れ、蒸留水で定容した。0.45μmメンブランフィルターで濾過し、高速液体クロマトグラフにより定量した。予め、各カテキンの標品を10〜100ppm程度に調製し、3点検量線を求めた。
4)高速液体クロマトグラフの操作条件
カラム:YMC Jsphere ODS-H80 φ4.6×250mm, カラム温度:40℃
移動相:A相 5%アセトニトリル(リン酸0.1%含有),
B相 50%アセトニトリル(リン酸0.1%含有)によるグラジエント
流速:10ml/min, 注入量:10μl, 検出:UV230nm
1) Equipment and instruments High-performance liquid chromatograph unit: Hitachi, Ltd. D-7000 HPLC system
HPLC column: YMC Jsphere ODS-H80 φ4.6 × 250mm
2) Reagent
Mobile phase: acetonitrile (for high performance liquid chromatograph or special grade), phosphoric acid (special grade), ultrapure water (ion-exchanged water treated with 0.45 μm)
Catechin standard solutions: (-)-epigallocatechin gallate (EGCg), (-)-epicatechin gallate (ECg), (-)-epicatechin (EC), (-)-epigallocatechin (EGC), (- ) -Gallocatechin gallate (GCg), (-)-catechin gallate (Cg), (-)-gallocatechin (GC), (+)-catechin (C)
3) Quantitative method of
4) Operating conditions of high performance liquid chromatograph
Column: YMC Jsphere ODS-H80 φ4.6 × 250mm, Column temperature: 40 ℃
Mobile phase:
Phase B Gradient with 50% acetonitrile (containing 0.1% phosphoric acid)
Flow rate: 10ml / min, Injection volume: 10μl, Detection: UV230nm
シリカを添加し吸着させた場合(6−1)、並びに、珪藻土濾過をした場合(6−2)は、カテキン量の減少はみられなかったが、キトサンを添加した場合(6−3)並びに膜濾過の場合(6−4)は、カテキン量が減少することが分かった。 When silica was added and adsorbed (6-1), and when diatomaceous earth was filtered (6-2), the amount of catechin was not reduced, but when chitosan was added (6-3) and In the case of membrane filtration (6-4), it was found that the amount of catechin decreased.
(試験7:濾過方法別での香気成分の変化)
[製造方法7−1:遠心分離]
緑茶原料(静岡産やぶきた品種の一番茶と二番茶を50:50でブレンドしたものの浅蒸し緑茶を火入れ乾燥した仕上げ茶)10gに対して85℃の熱水1000mlで3.5分間抽出した。得られた茶抽出液を80メッシュのステンレスフィルターで粗濾過し、粗濾過済みの茶抽出液を30℃になるように強制冷却した後、ウエストファリアー社製SA1連続遠心分離機を使用して遠心分離(流速:300L/h、回転数:10000rpm、遠心沈降面積(Σ):1000m2)を行った。
次に、遠心分離後の濾過液にアスコルビン酸を300ppm添加し重曹にてpH6に調整した。次いで、イオン交換水を加えて1000mLに調整(メスアップ)した後、UHT殺菌(135℃、30秒)を行い、プレート内で冷却し、85℃にて透明プラスチック容器(PETボトル)に充填し容器詰緑茶飲料とした。その後キャップ部を30秒間転倒殺菌し、ただちに冷却し、これを容器詰緑茶飲料試料とした。
(Test 7: Change in aroma component by filtration method)
[Production method 7-1: Centrifugation]
Extraction was performed for 3.5 minutes with 1000 ml of hot water at 85 ° C. per 10 g of green tea raw material (finished tea obtained by burning lightly steamed green tea blended with Shizuoka and Bukita varieties Ichibancha and Nibancha at 50:50). The obtained tea extract was roughly filtered with an 80-mesh stainless steel filter, and the roughly filtered tea extract was forcibly cooled to 30 ° C., and then used with a Westphalia SA1 continuous centrifuge. Centrifugation (flow rate: 300 L / h, rotation speed: 10,000 rpm, centrifugal sedimentation area (Σ): 1000 m 2) was performed.
Next, 300 ppm of ascorbic acid was added to the filtrate after centrifugation, and the pH was adjusted to 6 with sodium bicarbonate. Next, after adding ion-exchanged water to adjust to 1000 mL (meas up), UHT sterilization (135 ° C, 30 seconds) is performed, cooled in a plate, and filled into a transparent plastic container (PET bottle) at 85 ° C. A container-packed green tea beverage was obtained. Thereafter, the cap part was sterilized by overturning for 30 seconds, and immediately cooled, and this was used as a packaged green tea beverage sample.
[製造方法7−2:吸着工程⇒遠心分離]
緑茶原料(静岡産やぶきた品種の一番茶と二番茶を50:50でブレンドしたものの浅蒸し緑茶を火入れ乾燥した仕上げ茶)10gに対して85℃の熱水1000mlで3.5分間抽出した。得られた茶抽出液を80メッシュのステンレスフィルターで粗濾過し、粗濾過済みの茶抽出液を貯めたタンク内に、緑茶原料(茶葉質量)に対し5倍量のシリカ非晶質含水シリカ;水澤化学工業(株)社製「ミズカソープ」)を加え、30℃になるように強制冷却しながらシリカと十分接触するように茶抽出液(pH5.0)を15分間攪拌し、静置した後、ウエストファリアー社製SA1連続遠心分離機を使用して遠心分離(流速:300L/h、回転数:10000rpm、遠心沈降面積(Σ):1000m2)を行った。
次いで、遠心分離後の濾過液にアスコルビン酸を300ppm添加し重曹にてpH6に調整し、イオン交換水を加えて1000mLに調整(メスアップ)した後、UHT殺菌(135℃、30秒)を行い、プレート内で冷却し、85℃にて透明プラスチック容器(PETボトル)に充填し容器詰緑茶飲料とした。その後キャップ部を30秒間転倒殺菌し、ただちに冷却し、これを容器詰緑茶飲料試料とした。
[Production method 7-2: Adsorption process ⇒ Centrifugation]
Extraction was performed for 3.5 minutes with 1000 ml of hot water at 85 ° C. per 10 g of green tea raw material (finished tea obtained by burning lightly steamed green tea blended with Shizuoka and Bukita varieties Ichibancha and Nibancha at 50:50). The obtained tea extract is roughly filtered with an 80-mesh stainless steel filter, and in the tank in which the roughly filtered tea extract is stored, 5 times the amount of silica amorphous hydrous silica with respect to the green tea raw material (tea leaf mass); Mizusawa Chemical Co., Ltd. “Mizuka Soap”) was added, and the tea extract (pH 5.0) was stirred for 15 minutes so that it was in sufficient contact with silica while forcibly cooling to 30 ° C. and allowed to stand. Then, centrifugal separation (flow rate: 300 L / h, rotation speed: 10,000 rpm, centrifugal sedimentation area (Σ): 1000 m 2) was performed using a SA1 continuous centrifuge manufactured by Westphalia.
Next, 300 ppm of ascorbic acid is added to the filtrate after centrifugation, the pH is adjusted to 6 with sodium bicarbonate, and ion-exchanged water is added to adjust to 1000 mL (meas up), followed by UHT sterilization (135 ° C., 30 seconds). The plate was cooled in a plate and filled in a transparent plastic container (PET bottle) at 85 ° C. to obtain a container-packed green tea beverage. Thereafter, the cap part was sterilized by overturning for 30 seconds, and immediately cooled, and this was used as a packaged green tea beverage sample.
[製造方法7−3:吸着工程⇒遠心分離⇒珪藻土濾過(酸処理品使用)]
緑茶原料(静岡産やぶきた品種の一番茶と二番茶を50:50でブレンドしたものの浅蒸し緑茶を火入れ乾燥した仕上げ茶)10gに対して85℃の熱水1000mlで3.5分間抽出した。得られた茶抽出液を80メッシュのステンレスフィルターで粗濾過し、粗濾過済みの茶抽出液を貯めたタンク内に、緑茶原料(茶葉質量)に対し5倍量のシリカ非晶質含水シリカ;水澤化学工業(株)社製「ミズカソープ」)を加え、30℃になるように強制冷却しながらシリカと十分接触するように茶抽出液(pH5.0)を15分間攪拌し、静置した後、ウエストファリアー社製SA1連続遠心分離機を使用して遠心分離(流速:300L/h、回転数:10000rpm、遠心沈降面積(Σ):1000m2)を行った。
次いで、遠心分離後の濾過液を、Darcy0.1の酸処理済み珪藻土を用いて珪藻土濾過を行い、珪藻土濾過処理液を得た。
次に、珪藻土濾過処理液にアスコルビン酸を300ppm添加し重曹にてpH6に調整し、イオン交換水を加えて1000mLに調整(メスアップ)した後、UHT殺菌(135℃、30秒)を行い、プレート内で冷却し、85℃にて透明プラスチック容器(PETボトル)に充填し容器詰緑茶飲料とした。その後キャップ部を30秒間転倒殺菌し、ただちに冷却し、これを容器詰緑茶飲料試料とした。
なお、珪藻土の酸処理は、Darcy0.1の珪藻土を40倍量の塩酸液(2.5%濃度)に浸し、24時間攪拌しながら室温にて放置した後、水洗いして濾液がpH5になるまで洗浄した後、回転式ドラムにて乾燥するように行った。
[Production method 7-3: Adsorption process ⇒ Centrifugation ⇒ Diatomaceous earth filtration (use of acid-treated product)]
Extraction was performed for 3.5 minutes with 1000 ml of hot water at 85 ° C. per 10 g of green tea raw material (finished tea obtained by burning lightly steamed green tea blended with Shizuoka and Bukita varieties Ichibancha and Nibancha at 50:50). The obtained tea extract is roughly filtered with an 80-mesh stainless steel filter, and in the tank in which the roughly filtered tea extract is stored, 5 times the amount of silica amorphous hydrous silica with respect to the green tea raw material (tea leaf mass); Mizusawa Chemical Co., Ltd. “Mizuka Soap”) was added, and the tea extract (pH 5.0) was stirred for 15 minutes so that it was in sufficient contact with silica while forcibly cooling to 30 ° C. and allowed to stand. Then, centrifugal separation (flow rate: 300 L / h, rotation speed: 10,000 rpm, centrifugal sedimentation area (Σ): 1000 m 2) was performed using a SA1 continuous centrifuge manufactured by Westphalia.
Subsequently, the filtrate after centrifugation was subjected to diatomaceous earth filtration using Darcy 0.1 acid-treated diatomaceous earth to obtain a diatomaceous earth filtered liquid.
Next, 300 ppm of ascorbic acid was added to the diatomaceous earth filtration treatment solution, adjusted to pH 6 with sodium bicarbonate, adjusted to 1000 mL with ion-exchanged water (meas up), and then subjected to UHT sterilization (135 ° C., 30 seconds), It was cooled in the plate and filled into a transparent plastic container (PET bottle) at 85 ° C. to obtain a container-packed green tea beverage. Thereafter, the cap part was sterilized by overturning for 30 seconds, and immediately cooled, and this was used as a packaged green tea beverage sample.
The acid treatment of diatomaceous earth involves immersing Darcy 0.1 diatomaceous earth in 40 volumes of hydrochloric acid solution (2.5% concentration), leaving it to stand at room temperature with stirring for 24 hours, and then washing with water to bring the filtrate to
[香気成分の分析方法]
容器詰緑茶飲料試料を10mlバイアルビンに取り、NaClを3g加えた。また、内部標準として0.1%シクロヘキサノールを5μl添加した。香気成分の抽出は固層マイクロ抽出(SPME)法を用い、GC/MSにて分析を行い、結果を図4に示す。
なお、香気成分量は内部標準物質(0.1%シクロヘキサノール5μL)の面積を1とした時の相対比で求めた。
[Aroma component analysis method]
A packaged green tea beverage sample was taken in a 10 ml vial and 3 g of NaCl was added. Further, 5 μl of 0.1% cyclohexanol was added as an internal standard. Extraction of aroma components was analyzed by GC / MS using a solid layer micro extraction (SPME) method, and the results are shown in FIG.
In addition, the amount of fragrance components was calculated | required by the relative ratio when the area of an internal standard substance (0.1
(分析条件)
GC/MS : Agilent5973N,
カラム: DB-WAX(0.25mmI.D.×60m×0.25μm),
流速: 0.9ml/min,
オーブン温度: 35℃(3min)〜5℃/min〜240℃(5min),
注入口温度:-50℃〜12℃/s〜240℃, スプリットレス
(Analysis conditions)
GC / MS: Agilent5973N,
Column: DB-WAX (0.25mmI.D. × 60m × 0.25μm),
Flow rate: 0.9ml / min,
Oven temperature: 35 ℃ (3min) ~ 5 ℃ / min ~ 240 ℃ (5min),
Inlet temperature: -50 ° C to 12 ° C / s to 240 ° C, splitless
シリカを添加し吸着させた場合(7−2)、並びにさらに珪藻土濾過をした場合(7−3)は、遠心分離のみの場合(7−1)に比べ、ピラジン類は多く、脂肪酸酸化分解物が少なくなる傾向が認められた。 When silica is added and adsorbed (7-2), and when diatomaceous earth filtration is further performed (7-3), there are more pyrazines and fatty acid oxidative degradation products compared with the case of only centrifugation (7-1). A tendency to decrease was observed.
Claims (5)
The method for producing a packaged green tea beverage according to any one of claims 2 to 4, wherein diatomaceous earth filtration is performed using acid-treated diatomaceous earth in a subsequent step of the silica removing step.
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JP2014008052A (en) * | 2012-07-03 | 2014-01-20 | Suntory Holdings Ltd | Tea extract liquid for bottled green tea drink, and bottled green tea drink |
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WO2009025326A1 (en) * | 2007-08-21 | 2009-02-26 | Dsm Ip Assets B.V. | Method for production of hydroxytyrosol-containing aqueous olive extract |
JP2014008052A (en) * | 2012-07-03 | 2014-01-20 | Suntory Holdings Ltd | Tea extract liquid for bottled green tea drink, and bottled green tea drink |
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