JP6294676B2 - Method for producing tea extract - Google Patents

Method for producing tea extract Download PDF

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JP6294676B2
JP6294676B2 JP2014005054A JP2014005054A JP6294676B2 JP 6294676 B2 JP6294676 B2 JP 6294676B2 JP 2014005054 A JP2014005054 A JP 2014005054A JP 2014005054 A JP2014005054 A JP 2014005054A JP 6294676 B2 JP6294676 B2 JP 6294676B2
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extract
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adsorbent
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浩一郎 前川
浩一郎 前川
久典 釼持
久典 釼持
陽子 橋元
陽子 橋元
佐藤 剛
剛 佐藤
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Ogawa and Co Ltd
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Description

本発明は、容器詰茶飲料等の飲食品に優れた香味を付与する茶抽出液並びにその製造方法に関する。   The present invention relates to a tea extract that imparts an excellent flavor to foods and beverages such as containerized tea beverages and a method for producing the same.

緑茶に代表される茶飲料は、日々の生活に潤いを与え、日本人の生活にはなくてはならないものである。近年では茶の持つ抗酸化性が注目を集めており、ノンカロリーの健康的な飲み物として、茶飲料は無糖飲料の代表的なものとなってきている。さらに最近では嗜好性の多様化により、種々の茶飲料が市場に供されている。   Tea drinks, typified by green tea, provide moisture for daily life and are essential for the lives of Japanese people. In recent years, the antioxidant properties of tea have attracted attention, and as a non-calorie healthy drink, tea drinks have become representative of sugar-free drinks. More recently, various tea beverages have been put on the market due to diversification of palatability.

茶飲料は、一般に茶葉を水などの水性溶媒で抽出して茶抽出液を得、この茶抽出液を飲料に適した濃度になるように水などで希釈して濃度調整等を行った後、アルミニウムや鉄製などの缶、ポリエチレンテレフタラート(PET)などのプラスチックやガラス製のボトルなどの密封容器に封入して販売されている。
しかし、水性溶媒での抽出で得られた茶エキスは茶葉に含まれるカフェインやカテキン類などに由来する苦渋味が強く残るため消費者から敬遠されることが多い。このため、茶エキスの苦渋味を低減することを目的として、各種技術が提案されてきた。
Tea beverages generally extract tea leaves with an aqueous solvent such as water to obtain a tea extract, and after adjusting the concentration by diluting this tea extract with water or the like to a concentration suitable for beverages, It is sold in sealed containers such as aluminum and iron cans, plastics such as polyethylene terephthalate (PET), and glass bottles.
However, tea extracts obtained by extraction with an aqueous solvent are often avoided by consumers because the bitter and astringent taste derived from caffeine and catechins contained in tea leaves remains strong. For this reason, various techniques have been proposed for the purpose of reducing the bitter and astringent taste of the tea extract.

例えば、細胞壁消化酵素と共にタンナーゼを水に溶解させて調製した酵素水溶液を茶葉に作用させることで、カテキン類のうち強い苦渋味を有するエピカテキンガレート、エピガロカテキンガレートを加水分解し、苦渋味を軽減する方法(特許文献1)、緑茶・紅茶・ウーロン茶・マテ茶などのカフェインを含む茶類を素材とした茶の抽出時及び/又は抽出後、適量の活性炭を混合または添加してカフェインを低減した茶類抽出液を得る方法(特許文献2)、ガレート体率の高い原料から得られた緑茶抽出液を通常の方法でタンナーゼ処理し、pHを調節して、高濃度の非重合体カテキン類含有飲料においても風味や外観の優れた緑茶抽出物を得る方法(特許文献3)、茶葉から茶抽出液を濃縮抽出し、この濃縮抽出により得られた茶抽出液をタンナーゼまたはクロロゲン酸エステラーゼで処理することにより、旨味やコク味を損なわずに渋味を低減した茶飲料の製造方法(特許文献4)、アルカリ処理した紅茶抽出物又はアルカリ処理した後中和して得られた紅茶抽出物を活性炭処理することにより、摂取後に口中に残る不快な渋味及び尖った苦味が緩和された紅茶抽出物(特許文献5)、緑茶抽出物の有機溶媒水溶液を、該緑茶抽出物の固形分中のカテキン類に対して0.1〜1質量倍の活性炭と通常行われる処理時間よりも長く(12時間〜5日間)接触させることにより、緑茶風味の悪化の要因となる緑茶抽出物中のフラボノール類を低減させた精製緑茶抽出物の製造方法(特許文献6)など、がこれまでに提案されている。   For example, by causing an enzyme aqueous solution prepared by dissolving tannase in water together with cell wall digestive enzymes to act on tea leaves, hydrolyze epicatechin gallate and epigallocatechin gallate having strong bitter taste among catechins, Mitigation method (Patent Document 1), and / or after extraction of tea using caffeine-containing teas such as green tea, black tea, oolong tea, mate tea, etc. after mixing or adding an appropriate amount of activated carbon to caffeine A method for obtaining a tea extract with reduced content (Patent Document 2), a green tea extract obtained from a raw material having a high gallate body rate is treated with a tannase by a conventional method, pH is adjusted, and a high concentration non-polymer A method for obtaining a green tea extract having excellent flavor and appearance even in a catechin-containing beverage (Patent Document 3), concentrating and extracting a tea extract from tea leaves, and a tea extract obtained by this concentrated extraction By treating with tannase or chlorogenic acid esterase, a method for producing a tea beverage with reduced astringency without impairing umami or richness (Patent Document 4), alkali-treated black tea extract or alkali-treated and neutralized By subjecting the obtained black tea extract to activated carbon treatment, an unpleasant astringency remaining in the mouth after ingestion and a sharp bitter taste are alleviated (Patent Document 5), an organic solvent aqueous solution of the green tea extract, Contacting 0.1 to 1 times mass of activated carbon with the catechins in the solid content of the extract for longer than the usual treatment time (12 hours to 5 days) causes deterioration of the green tea flavor. A method for producing a purified green tea extract with reduced flavonols in the green tea extract (Patent Document 6) has been proposed so far.

特開平5−308901号公報JP-A-5-308901 特開平8−70772号公報JP-A-8-70772 特開2004−321105号公報JP 2004-321105 A 特開2005−130809号公報JP 2005-130809 A 特開2009−159833号公報JP 2009-159833 A 特開2012−55205号公報JP2012-55205A

しかし、茶葉をタンナーゼ等の酵素で処理する方法では苦渋味が十分に低減されず、また、活性炭等の吸着剤を使用すると苦渋味はある程度低減できるものの、茶が本来有する豊かな風味も減少する。
従って、本発明の課題はカテキン類等に起因する苦渋味が低減され、かつ風味の優れた茶抽出液を製造する方法を提供することである。
However, the method of treating tea leaves with an enzyme such as tannase does not sufficiently reduce bitterness and astringent taste. However, if an adsorbent such as activated carbon is used, bitterness and taste can be reduced to some extent, but the rich flavor inherent in tea also decreases. .
Accordingly, an object of the present invention is to provide a method for producing a tea extract having a reduced bitter and astringent taste due to catechins and the like and having an excellent flavor.

本発明者らは茶葉をタンナーゼ水溶液で抽出して得られた抽出液を活性炭で処理したところ、苦渋味は十分に低減できたが、茶の風味も減少した。そこで、茶葉をタンナーゼ水溶液で抽出する時に活性炭を共存させたところ、意外にも風味の減少が抑えられ、苦渋味が少なく、茶本来の風味豊かな茶抽出液が得られることを見出し、本発明を完成した。   When the present inventors treated the extract obtained by extracting tea leaves with a tannase aqueous solution with activated carbon, the bitter and astringent taste was sufficiently reduced, but the flavor of tea was also reduced. Therefore, when coexisting activated carbon when extracting tea leaves with a tannase aqueous solution, it was surprisingly found that a decrease in flavor is suppressed, a bitter and astringent taste, and a tea-rich tea flavor is obtained. Was completed.

すなわち、本発明は、
(1)茶葉を吸着剤存在下、タンニン分解活性を有する酵素の水溶液で抽出処理することを特徴とする茶抽出液の製造方法、
(2)吸着剤が活性炭又は合成吸着剤である(1)記載の製造方法、
(3)タンニン分解活性を有する酵素がタンナーゼである(1)又は(2)記載の製造方法、
(4)茶葉が不発酵茶、半発酵茶、発酵茶から選択される少なくとも1種の茶葉である(1)乃至(3)のいずれかに記載の製造方法、
(5)(1)乃至(4)のいずれかの方法で製造された茶抽出液、
(6)(1)乃至(4)のいずれかに記載の方法で製造された茶抽出液を含んでなる飲食品、
である。
That is, the present invention
(1) A method for producing a tea extract, comprising subjecting tea leaves to extraction with an aqueous solution of an enzyme having tannin decomposing activity in the presence of an adsorbent,
(2) The production method according to (1), wherein the adsorbent is activated carbon or a synthetic adsorbent,
(3) The production method according to (1) or (2), wherein the enzyme having tannin degrading activity is tannase.
(4) The production method according to any one of (1) to (3), wherein the tea leaf is at least one tea leaf selected from unfermented tea, semi-fermented tea, and fermented tea,
(5) A tea extract produced by any one of the methods (1) to (4),
(6) A food or drink comprising the tea extract produced by the method according to any one of (1) to (4),
It is.

本発明により、カテキン類等に起因する苦渋味が少なく、茶本来の風味豊かな茶抽出液を得ることができる。従って、飲食品において嗜好の多様化が進む中で、新たな食品素材として各種飲食品に幅広く適用することが可能となる。   According to the present invention, it is possible to obtain a tea extract with little bitterness and astringency caused by catechins and the like, and rich in the original flavor of tea. Therefore, it is possible to widely apply to various foods and drinks as a new food material while the diversification of preferences in foods and drinks.

(1)原料茶葉
本発明の茶抽出液の原料である茶葉は、ツバキ科の常緑樹であるチャ(Camellia sinensis)の芽、葉、茎に飲料用として前処理を施したものである。茶の前処理方法としては不発酵、半発酵、発酵があるが、いずれの処理方法によるものでもよい。不発酵茶としては緑茶(煎茶、玉露、かぶせ茶、番茶、玉緑茶、抹茶、ほうじ茶、釜炒り茶、てん茶等)、半発酵茶としてはウーロン茶、包種茶等、発酵茶としては紅茶、プーアール茶が挙げられる。
茶葉は種類、等級、産地、製法などは何ら限定されることはなく、いずれの茶葉でも可能である。あるいは、種類の異なる茶葉を1種または2種以上を混合して用いてもよい。
(1) Raw Tea Leaves Tea leaves, which are the raw material of the tea extract of the present invention, are prepared by subjecting tea (Camellia sinensis) buds, leaves, and stems to be used for beverages. Tea pretreatment methods include non-fermentation, semi-fermentation, and fermentation, and any treatment method may be used. Non-fermented tea is green tea (sencha, gyokuro, kabusecha, bancha, tamago green tea, matcha tea, hojicha, kettle roasted tea, tencha, etc.), semi-fermented tea is oolong tea, bald tea, etc., fermented tea is black tea, Pu-erh tea can be mentioned.
There are no restrictions on the type, grade, production area, and production method of tea leaves, and any tea leaves are possible. Alternatively, different types of tea leaves may be used alone or in combination of two or more.

(2)酵素
本発明ではタンニンを加水分解する活性を有する酵素であれば特に制限なく使用できるが、好ましくはタンナーゼ(EC番号3.1.1.20)が用いられる。タンナーゼはタンニンの没食子酸エステル結合を選択的に加水分解する酵素であり、Aspergillus属やPenicillium属等に属する微生物から得ることができる。
本発明においては、酵素製剤として市販されているものを用いてもよく、具体的には「タンナーゼ」(三菱化学フーズ社製)、「スミチームTAN」(新日本化学工業社製)、「タンナーゼ」(キッコーマンバイオケミファ社製)等を挙げることができる。
この他、植物の細胞壁分解酵素(セルラーゼ、ヘミセルラーゼ、ペクチナーゼ等)やタンパク分解酵素(プロテアーゼ等)のうち、夾雑酵素によるタンナーゼ活性を有している酵素も使用することができる。
(2) Enzyme In the present invention, an enzyme having an activity of hydrolyzing tannin can be used without particular limitation, but tannase (EC number 3.1.1.20) is preferably used. Tannase is an enzyme that selectively hydrolyzes the gallic acid ester bond of tannin and can be obtained from microorganisms belonging to the genus Aspergillus, Penicillium, and the like.
In the present invention, commercially available enzyme preparations may be used. Specifically, “Tannase” (manufactured by Mitsubishi Chemical Foods), “Sumiteam TAN” (manufactured by Shin Nippon Chemical Industry), “Tannase” (Kikkoman Biochemifa Co., Ltd.).
In addition, among the plant cell wall degrading enzymes (cellulase, hemicellulase, pectinase, etc.) and proteolytic enzymes (proteases, etc.), enzymes having tannase activity by contaminating enzymes can also be used.

(3)吸着剤
本発明で用いる吸着剤は、活性炭又は合成吸着剤であり、いずれも特に限定することなく用いることができる。
活性炭は、木材、木炭、ヤシ殻、石炭類を原材料として炭化し、水蒸気等で賦活化して得られるもので、大きな比表面積と吸着能をもつ多孔質の炭素質物質であり、粉末状や粒状体のものがある。原料の木炭、ヤシがら、石炭チャー等を十分に炭化した後、水蒸気による高温処理あるいは塩化亜鉛等の水溶液の含浸と高温焼成などの方法で賦活し製造されている。
(3) Adsorbent The adsorbent used in the present invention is activated carbon or a synthetic adsorbent, and any of them can be used without any particular limitation.
Activated carbon is obtained by carbonizing wood, charcoal, coconut shells, and coals as raw materials and activating with water vapor, etc., and is a porous carbonaceous material with a large specific surface area and adsorption capacity. There is a thing of the body. After sufficiently charcoalizing raw charcoal, palm, coal char, etc., it is activated and produced by high temperature treatment with steam or impregnation with an aqueous solution such as zinc chloride and high temperature firing.

一般に、比表面積は800〜3000m2/g、好ましくは1000〜2000m2/g、細孔容積は0.2〜2cm3/g、好ましくは1〜2cm3/g、細孔径は1〜5nm、好ましくは2.5〜4.5nmである。さらに、吸着後の分離性の観点から粉末状の活性炭よりも平均粒径が0.1〜1.0mm程度の顆粒状の活性炭が好ましい。
活性炭の組成は炭素を主成分とするが、他に少量の水素、酸素、無機成分を含み、化学構造はグラファイトを基本とするが無定形で表面にヒドロキシル基、キノン基などの官能基を持っている。
活性炭としては例えば、「クラレコール」(クラレケミカル社製)、「白鷺」(日本エンバイロンケミカルズ社製)、「太閤」(フタムラ化学社製)などを挙げることができる。
Generally, the specific surface area 800~3000m 2 / g, preferably from 1000 to 2000 2 / g, pore volume 0.2~2cm 3 / g, preferably from 1 to 2 cm 3 / g, pore size 1 to 5 nm, Preferably it is 2.5-4.5 nm. Furthermore, granular activated carbon having an average particle diameter of about 0.1 to 1.0 mm is preferable to powdered activated carbon from the viewpoint of separability after adsorption.
The composition of activated carbon is mainly composed of carbon, but also contains a small amount of hydrogen, oxygen, and inorganic components. The chemical structure is based on graphite, but it is amorphous and has functional groups such as hydroxyl and quinone groups on the surface. ing.
Examples of the activated carbon include “Kuraray Coal” (manufactured by Kuraray Chemical Co., Ltd.), “Shirakaba” (manufactured by Nippon Environ Chemicals Co., Ltd.), “Dazai” (manufactured by Phutamura Chemical Co., Ltd.), and the like.

合成吸着剤としては、その母体がスチレン系ポリマー、例えば「アンバーライト(登録商標)XAD-16」(オルガノ株式会社製)、スチレン−ジビニルベンゼン系ポリマー、例えば「ダイヤイオン(登録商標)HP-20」(三菱化学株式会社製)、アクリル系ポリマー、例えば「ダイヤイオン(登録商標)WK-10」(三菱化学株式会社製)、メタクリル系ポリマー、例えば「ダイヤイオン(登録商標)HP-2MG」(三菱化学株式会社製)、アクリル酸エステル系ポリマー、例えば「アンバーライト(登録商標)XAD-7」(オルガノ株式会社製)、アミド系ポリマー、例えば「アンバーライト(登録商標)XAD-11」(オルガノ株式会社製)、二酸化ケイ素系、例えば「サイロピュート(登録商標)202」(富士シリシア化学株式会社製)、デキストラン系、例えば「セファデックス(登録商標)G-25」(アマシャム ファルマシア バイオテク社製)、ポリビニル系、例えば「ダイヤイオン(登録商標)FP-II」(三菱化学株式会社製)、ポリビニルアミド系のポリビニルポリピロリドン(PVPP)、例えば「ポリクラール(登録商標)」(アイエスピー・ジャパン社製)、「ダイバガン(登録商標)」(BASF社製)などを挙げることができる。   As the synthetic adsorbent, the matrix is a styrene polymer such as “Amberlite (registered trademark) XAD-16” (manufactured by Organo Corporation), or a styrene-divinylbenzene polymer such as “Diaion (registered trademark) HP-20”. (Mitsubishi Chemical Corporation), acrylic polymers such as “Diaion (registered trademark) WK-10” (Mitsubishi Chemical Corporation), methacrylic polymers such as “Diaion (registered trademark) HP-2MG” ( Mitsubishi Chemical Co., Ltd.), acrylic ester polymers such as “Amberlite (registered trademark) XAD-7” (manufactured by Organo Corporation), amide polymers such as “Amberlite (registered trademark) XAD-11” (organo) Co., Ltd.), silicon dioxide type, such as “Silo Pute® 202” (manufactured by Fuji Silysia Chemical Ltd.), Adex (registered trademark) G-25 "(manufactured by Amersham Pharmacia Biotech), polyvinyl-based, for example," Diaion (registered trademark) FP-II "(manufactured by Mitsubishi Chemical Corporation), polyvinylamide-based polyvinyl polypyrrolidone (PVPP) Examples thereof include “Polyclar (registered trademark)” (manufactured by IPS Japan), “Daibagan (registered trademark)” (manufactured by BASF), and the like.

本発明では活性炭又はポリビニルポリピロリドンの使用が好ましく、活性炭の使用が特に好ましい。さらに、ポリビニルポリピロリドン製吸着剤の中でも平均粒径が10〜60μm、比表面積が0.5〜3.5m2/g、かさ密度が0.1〜0.5g/cm3のものが好ましい。 In the present invention, the use of activated carbon or polyvinylpolypyrrolidone is preferred, and the use of activated carbon is particularly preferred. Further, among the adsorbents made of polyvinyl polypyrrolidone, those having an average particle diameter of 10 to 60 μm, a specific surface area of 0.5 to 3.5 m 2 / g, and a bulk density of 0.1 to 0.5 g / cm 3 are preferable.

(4)抽出処理
本発明では原料となる茶葉を吸着剤の存在下、酵素の水溶液で抽出することにより、カテキン類等に起因する苦渋味が少なく、茶本来の風味豊かな茶抽出液を得ることができる。すなわち、吸着剤と酵素が共存する態様で抽出操作を行う点に本発明の特徴がある。
酵素水溶液での抽出方法は特に制限はないが、通常は予め調製した酵素の水溶液に茶葉と吸着剤を投入し、一定時間静置又は撹拌条件下で酵素処理と同時に抽出を行う。
酵素の使用量は力価などにより異なるが、通常は乾燥茶葉1質量部に対し、酵素0.0001〜0.1質量部、水5〜100質量部、好ましくは酵素0.0002〜0.02質量部、水10〜50質量部である。
(4) Extraction treatment In the present invention, the tea leaves as raw materials are extracted with an aqueous solution of an enzyme in the presence of an adsorbent, thereby obtaining a tea extract that has little bitter and astringent taste due to catechins and the like and is rich in the original flavor of tea. be able to. That is, the present invention is characterized in that the extraction operation is performed in a mode in which the adsorbent and the enzyme coexist.
The extraction method using an aqueous enzyme solution is not particularly limited. Usually, tea leaves and an adsorbent are put into an aqueous solution of an enzyme prepared in advance, and extraction is performed simultaneously with the enzyme treatment under a fixed time or stirring condition.
The amount of the enzyme used varies depending on the titer and the like, but is usually 0.0001 to 0.1 part by weight of enzyme and 5 to 100 parts by weight of water, preferably 0.0002 to 0.02 part of enzyme for 1 part by weight of dried tea leaves. It is a mass part and 10-50 mass parts of water.

吸着剤の使用量は種類により異なるが、後述するように抽出液のBrix比は60〜90%の範囲が好ましく、この観点から吸着剤の使用量は、通常は茶葉1質量部に対して吸着剤0.01〜1質量部、好ましくは0.05〜0.2質量部、より好ましくは0.05〜0.15質量部、さらに好ましくは0.07〜0.15質量部である。
抽出は通常は30〜55℃、好ましくは35〜50℃の温度範囲で、通常は10分〜3時間、好ましくは30分〜2時間の条件下で行う。
抽出時のpHは特に制限なく、使用する酵素や吸着剤の種類に応じて適宜適切なpHに調整することができる。
なお、抽出時に、茶葉の細胞壁を分解し細胞内容物が浸出され易くすることを目的としてセルラーゼ、ヘミセルラーゼ、ペクチナーゼ等の細胞壁分解酵素や、プロテアーゼ等のタンパク質分解酵素などを添加してもよく、酸化防止剤としてアスコルビン酸又はその塩などを添加してもよい。
Although the amount of adsorbent used varies depending on the type, as described later, the Brix ratio of the extract is preferably in the range of 60 to 90%. From this viewpoint, the amount of adsorbent used is usually adsorbed on 1 part by weight of tea leaves. The agent is 0.01 to 1 part by mass, preferably 0.05 to 0.2 part by mass, more preferably 0.05 to 0.15 part by mass, and still more preferably 0.07 to 0.15 part by mass.
The extraction is usually carried out in the temperature range of 30 to 55 ° C, preferably 35 to 50 ° C, and usually 10 minutes to 3 hours, preferably 30 minutes to 2 hours.
The pH at the time of extraction is not particularly limited, and can be appropriately adjusted to an appropriate pH according to the type of enzyme and adsorbent used.
In addition, cell wall degrading enzymes such as cellulase, hemicellulase and pectinase, and proteolytic enzymes such as protease may be added for the purpose of degrading the cell wall of tea leaves and facilitating the leaching of cell contents during extraction. Ascorbic acid or a salt thereof may be added as an antioxidant.

抽出後、固液分離により茶葉、吸着剤その他の不溶物を除去し、酵素を失活させる。酵素の失活は、例えば抽出液を80〜95℃で1〜20分間加熱することにより行う。酵素失活後、遠心分離、濾過等の処理により清澄な茶抽出液を得る。   After extraction, tea leaves, adsorbents and other insoluble matters are removed by solid-liquid separation to deactivate the enzyme. Inactivation of the enzyme is performed, for example, by heating the extract at 80 to 95 ° C. for 1 to 20 minutes. After deactivation of the enzyme, a clear tea extract is obtained by treatment such as centrifugation and filtration.

本発明の茶抽出液は、優れた香味の観点から、製造される茶抽出液のBrixが、吸着剤処理を行わずに作製した抽出液のBrixとの比(以下「Brix比」と記す)が60〜90%となるように抽出時に使用する吸着剤の量を調整することが好ましく、香りの強さの観点からは70〜90%がより好ましい。Brix比が90%を超えると苦渋味が強く、また、Brix比が60%以下の場合には香りが弱くなってしまう。
ここで、Brix(ブリックス)とは、溶液100gあたりの可溶性固形物重量(g)のことである。
From the viewpoint of excellent flavor, the tea extract of the present invention has a ratio of Brix of the produced tea extract to Brix of the extract prepared without performing the adsorbent treatment (hereinafter referred to as “Brix ratio”). It is preferable to adjust the amount of the adsorbent used at the time of extraction so that it becomes 60 to 90%, and 70 to 90% is more preferable from the viewpoint of fragrance strength. When the Brix ratio exceeds 90%, the bitter and astringent taste is strong, and when the Brix ratio is 60% or less, the fragrance becomes weak.
Here, Brix means the weight (g) of soluble solids per 100 g of solution.

(5)茶抽出液の製剤化
本発明の茶抽出液は、さらに濃縮してペースト状の抽出エキスとしても、また噴霧乾燥、凍結乾燥又は加熱乾燥などの処理を行い粉末として使用してもよい。
一般的には各種成分(糖、酸味料、酸化防止剤、香料など)を組み合わせて、例えば水、アルコール、グリセリン、プロピレングリコール等、又はこれらを混合した溶剤に適当な濃度で溶解させて液剤とする。具体的には、水/エタノール、水/エタノール/グリセリン、水/グリセリン等の混合溶剤が好ましい。
また、各溶液に賦形剤(例えばデキストリン等)を添加し噴霧乾燥により粉末状にすることも可能であり、用途に応じて種々の剤形を採用することができる。
(5) Formulation of tea extract The tea extract of the present invention may be further concentrated to give a paste-like extract, or may be used as a powder after being subjected to treatment such as spray drying, freeze drying or heat drying. .
In general, various components (sugar, acidulant, antioxidant, fragrance, etc.) are combined and dissolved in water, alcohol, glycerin, propylene glycol, etc., or a mixed solvent thereof at a suitable concentration, To do. Specifically, a mixed solvent such as water / ethanol, water / ethanol / glycerin, water / glycerin and the like is preferable.
Moreover, it is also possible to add an excipient | filler (for example, dextrin etc.) to each solution, and it can also be made into a powder form by spray drying, and various dosage forms can be employ | adopted according to a use.

(6)茶抽出液の適用
得られた茶抽出液は、茶飲料としてそのまま飲用することができる。あるいは他の飲食品に添加して使用することができる。
例えば、緑茶、ウーロン茶、紅茶などの茶類飲料に添加すると、飲料に苦渋味を増加させることなく茶の本来の風味を付与することができる。茶類飲料に添加する場合は飲料に対して通常0.05〜2質量%、好ましくは0.1〜1質量%の添加量(抽出液として)が適当である。
(6) Application of tea extract The obtained tea extract can be drunk as it is as a tea beverage. Or it can add and use for other food-drinks.
For example, when added to tea beverages such as green tea, oolong tea and black tea, the original flavor of tea can be imparted to the beverage without increasing the bitter taste. When added to tea beverages, an addition amount (as an extract) of generally 0.05 to 2% by mass, preferably 0.1 to 1% by mass with respect to the beverage is appropriate.

さらに、本発明の茶抽出液は苦味や渋みが少なく優れた香味を有することから、茶類飲料以外の茶風味を有する飲食品、例えば、茶の風味を付与したスナック類、栄養食品、アイスクリーム、シャーベット等の冷菓類、饅頭、羊かん、ういろう、クッキー、ケーキ、チョコレート、チューイングガム、ゼリー、プリン、ムース等の菓子類、菓子パン、食パン等のパン類、ラムネ菓子、タブレット、錠菓類などに添加することができる。
具体的には、茶エキス入りキャンディー、抹茶アイスクリーム、抹茶ムース、抹茶入り乳飲料、緑茶ゼリーや抹茶チョコレート等が例示される。
Furthermore, since the tea extract of the present invention has an excellent flavor with little bitterness and astringency, foods and drinks having a tea flavor other than tea beverages, for example, snacks imparted with a tea flavor, nutritional food, ice cream Add to frozen confectionery such as sherbet, buns, sheep kan, wairo, cookies, cakes, chocolate, chewing gum, jelly, pudding, mousse, confectionery bread, bread such as bread, ramune confectionery, tablets, tablet confectionery, etc. be able to.
Specific examples include candies with tea extract, matcha ice cream, matcha mousse, milk drinks with matcha, green tea jelly, matcha chocolate, and the like.

以下、実施例を挙げて本発明を具体的に説明するが、本発明は実施例の記載に限定されるものではない。   EXAMPLES Hereinafter, although an Example is given and this invention is demonstrated concretely, this invention is not limited to description of an Example.

〔実施例1〜6〕
抽出器に所定量の水及び0.02質量部のタンナーゼ酵素「スミチームTAN」(新日本化学工業社製)を仕込み、溶解させた後、茶葉100質量部と所定量の吸着剤を加え、40℃で1.5時間抽出した。
その後固液分離を行い、得られた抽出液を85℃で5分間加熱して酵素を失活させ、10℃まで冷却した。
10℃で遠心分離を行い、上澄み液を回収して茶抽出液を得た。抽出液のBrixは(株)アタゴ製のデジタル屈折計「RX−7000α」で測定した。
なお、本実施例及び比較例において、茶葉は市販の緑茶、紅茶又はウーロン茶を使用した。また、吸着剤は活性炭又はポリビニルポリピロリドン(PVPP)を使用した。
[Examples 1 to 6]
A predetermined amount of water and 0.02 parts by mass of tannase enzyme “Sumiteam TAN” (manufactured by Shin Nippon Chemical Industry Co., Ltd.) were charged into an extractor and dissolved, and then 100 parts by mass of tea leaves and a predetermined amount of adsorbent were added. Extract at 1.5 ° C. for 1.5 hours.
Thereafter, solid-liquid separation was performed, and the obtained extract was heated at 85 ° C. for 5 minutes to deactivate the enzyme and cooled to 10 ° C.
Centrifugation was performed at 10 ° C., and the supernatant was collected to obtain a tea extract. The Brix of the extract was measured with a digital refractometer “RX-7000α” manufactured by Atago Co., Ltd.
In the present examples and comparative examples, commercially available green tea, black tea or oolong tea was used as the tea leaves. Moreover, activated carbon or polyvinyl polypyrrolidone (PVPP) was used as the adsorbent.

〔比較例1、3、9〕
抽出器に所定量の水及び0.02質量部の「スミチームTAN」(新日本化学工業社製)を仕込み、溶解させた後、茶葉100質量部を加え、40℃で1.5時間抽出した。
その後固液分離を行い、得られた抽出液を85℃で5分間加熱して酵素を失活させ、10℃まで冷却した。
10℃で遠心分離を行い、上澄み液を回収した。抽出液のBrixは実施例1〜6と同じ方法で測定した。
[Comparative Examples 1, 3, 9]
A predetermined amount of water and 0.02 parts by weight of “Sumiteam TAN” (manufactured by Shin Nippon Chemical Industry Co., Ltd.) were charged into an extractor and dissolved, and then 100 parts by weight of tea leaves were added and extracted at 40 ° C. for 1.5 hours. .
Thereafter, solid-liquid separation was performed, and the obtained extract was heated at 85 ° C. for 5 minutes to deactivate the enzyme and cooled to 10 ° C.
Centrifugation was performed at 10 ° C., and the supernatant was recovered. The Brix of the extract was measured by the same method as in Examples 1-6.

〔比較例2、5〜8、10〕
抽出器に所定量の水及び0.02質量部の「スミチームTAN」(新日本化学工業社製)を仕込み、溶解させた後、茶葉100質量部を加え、40℃で1.5時間抽出した。
その後固液分離を行い、得られた抽出液を85℃で5分間加熱して酵素を失活させ、40℃まで冷却した。これに吸着剤を所定量加え40℃で1.5時間吸着剤処理を行った。
その後10℃まで冷却して遠心分離を行い、上澄み液を回収して抽出液を得た。抽出液のBrixは実施例1〜6と同じ方法で測定した。
[Comparative Examples 2, 5-8, 10]
A predetermined amount of water and 0.02 parts by weight of “Sumiteam TAN” (manufactured by Shin Nippon Chemical Industry Co., Ltd.) were charged into an extractor and dissolved, and then 100 parts by weight of tea leaves were added and extracted at 40 ° C. for 1.5 hours. .
Thereafter, solid-liquid separation was performed, and the obtained extract was heated at 85 ° C. for 5 minutes to deactivate the enzyme and cooled to 40 ° C. A predetermined amount of adsorbent was added thereto, and adsorbent treatment was performed at 40 ° C. for 1.5 hours.
Thereafter, the mixture was cooled to 10 ° C. and centrifuged, and the supernatant was collected to obtain an extract. The Brix of the extract was measured by the same method as in Examples 1-6.

〔比較例4〕
抽出器に所定量の水及び所定量の吸着剤を仕込んだ後、茶葉100質量部を加え、40℃で1.5時間抽出した。
その後固液分離を行い、得られた抽出液を10℃まで冷却した。
10℃で遠心分離を行い、上澄み液を回収した。抽出液のBrixは実施例1〜6と同じ方法で測定した。
[Comparative Example 4]
After adding a predetermined amount of water and a predetermined amount of adsorbent to the extractor, 100 parts by mass of tea leaves were added and extracted at 40 ° C. for 1.5 hours.
Thereafter, solid-liquid separation was performed, and the obtained extract was cooled to 10 ° C.
Centrifugation was performed at 10 ° C., and the supernatant was recovered. The Brix of the extract was measured by the same method as in Examples 1-6.

〔試験例〕
実施例1〜6及び比較例1〜10で得られた茶抽出液の香り及び苦渋味の強さを3名の専門パネルにより評価した。
評価の基準は吸着剤不使用の比較例1及び3を4点(強い)とし、3点(やや強い)、2点(やや弱い)、1点(弱い)の4段階とした。各パネルの評価点の平均を表1に示す。なお、吸着剤量は茶葉100質量部に対して使用した吸着剤の質量部で表示した。
[Test example]
The strength of the aroma and bitterness of the tea extracts obtained in Examples 1 to 6 and Comparative Examples 1 to 10 were evaluated by three specialist panels.
The standard of evaluation was as follows: Comparative Examples 1 and 3 without adsorbent were 4 points (strong), and 4 levels were 3 points (slightly strong), 2 points (slightly weak), and 1 point (weak). Table 1 shows the average evaluation score of each panel. In addition, the amount of adsorbent was displayed by the mass part of the adsorbent used with respect to 100 mass parts of tea leaves.

Figure 0006294676
Figure 0006294676

酵素のみを使用し吸着剤を使用しなかった比較例1、3、9に比べ、酵素処理の後吸着剤を使用した比較例2、5〜8、10では苦渋味は低減されたが香りも減少した。酵素を使用せず吸着剤のみを使用した比較例4も同様の結果となった。これに対し、吸着剤存在下で酵素反応を行った実施例1〜6では香りの減少が抑えられ、苦渋味が少なく風味の豊かな茶抽出液が得られた。また、実施例1〜6では吸着剤として活性炭を使用した場合に効果が高く、Brix比が70〜90%の場合に香りの強い抽出液が得られた。   Compared to Comparative Examples 1, 3, and 9 in which only the enzyme was used and no adsorbent was used, in Comparative Examples 2, 5 to 8, and 10 in which the adsorbent was used after the enzyme treatment, the bitter and astringent taste was reduced but the aroma was also present. Diminished. The same result was obtained in Comparative Example 4 in which only the adsorbent was used without using the enzyme. On the other hand, in Examples 1 to 6 in which the enzyme reaction was performed in the presence of the adsorbent, a decrease in fragrance was suppressed, and a tea extract with little bitter and astringent taste and rich flavor was obtained. Moreover, in Examples 1-6, when activated carbon was used as an adsorbent, the effect was high, and when the Brix ratio was 70-90%, a strong fragrant extract was obtained.

本願発明の効果は、苦渋味が少なく風味豊かな茶抽出液が得られる点にある。
すなわち、表1において「香りの強さ」の平均評価点が高いことと、「苦渋味の強さ」の平均評価点が低いことが重要である。
例えば、苦渋味の強さを1.0まで抑えた比較例7と実施例4を対比すれば、比較例7の香りの強さは1.0なのに対し、実施例4は1.7であり、苦渋味を強く抑えても香りの強さは一定程度維持されるという点で効果が優れる。
The effect of the present invention is that a tea extract with little bitter and astringent taste and rich flavor can be obtained.
That is, in Table 1, it is important that the average evaluation point of “scent intensity” is high and the average evaluation point of “bitter taste strength” is low.
For example, if Comparative Example 7 and Example 4 in which the intensity of bitterness and astringency is suppressed to 1.0 are compared, the fragrance intensity of Comparative Example 7 is 1.0, whereas Example 4 is 1.7. Even if the bitter and astringent taste is strongly suppressed, the effect is excellent in that the strength of the fragrance is maintained to a certain degree.

本発明により、カフェインやカテキン類等に起因する苦渋味が少ない茶本来の風味豊かな茶抽出液を得ることができる。茶抽出液は茶風味を付与する素材として茶飲料に使用することができる。また、茶飲料以外の飲食品にも幅広く使用することが可能である。   According to the present invention, it is possible to obtain a tea extract rich in the original flavor of tea with less bitterness and astringency caused by caffeine, catechins and the like. The tea extract can be used in tea beverages as a material imparting tea flavor. Moreover, it can be used widely for food and drink other than tea drinks.

Claims (6)

茶葉を吸着剤存在下、タンニン分解活性を有する酵素の水溶液で抽出処理することを特徴とする茶抽出液の製造方法であって、
吸着剤が活性炭又はポリビニルポリピロリドンであり、且つ吸着剤の使用量が茶葉1質量部に対し0.05〜0.15質量部である、上記の製造方法。
A method for producing a tea extract, characterized in that tea leaves are extracted with an aqueous solution of an enzyme having tannin degrading activity in the presence of an adsorbent ,
Said manufacturing method whose adsorbent is activated carbon or polyvinyl polypyrrolidone, and the usage-amount of adsorbent is 0.05-0.15 mass part with respect to 1 mass part of tea leaves.
タンニン分解活性を有する酵素がタンナーゼである請求項に記載の製造方法。 The method according to claim 1 , wherein the enzyme having tannin degrading activity is tannase. 茶葉が不発酵茶、半発酵茶、発酵茶から選択される少なくとも1種の茶葉である請求項1又は2に記載の製造方法。 The method according to claim 1 or 2 , wherein the tea leaf is at least one tea leaf selected from unfermented tea, semi-fermented tea, and fermented tea. 茶葉が紅茶である、請求項1〜3のいずれかの項に記載の製造方法。The production method according to any one of claims 1 to 3, wherein the tea leaves are black tea. 茶葉を、茶葉1質量部に対し0.05〜0.15質量部の活性炭又はポリビニルポリピロリドン存在下、タンニン分解活性を有する酵素の水溶液で抽出処理して製造された茶抽出液。A tea extract produced by subjecting tea leaves to extraction with an aqueous solution of an enzyme having tannin decomposing activity in the presence of 0.05 to 0.15 parts by mass of activated carbon or polyvinylpolypyrrolidone with respect to 1 part by mass of tea leaves. 請求項5記載の抽出液を含んでなる飲食品。 A food or drink comprising the extract according to claim 5 .
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