JP2009125058A - Method for producing extract for tea-based beverage - Google Patents

Method for producing extract for tea-based beverage Download PDF

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JP2009125058A
JP2009125058A JP2007306993A JP2007306993A JP2009125058A JP 2009125058 A JP2009125058 A JP 2009125058A JP 2007306993 A JP2007306993 A JP 2007306993A JP 2007306993 A JP2007306993 A JP 2007306993A JP 2009125058 A JP2009125058 A JP 2009125058A
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extraction
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JP4778499B2 (en
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Haruhito Michida
晴仁 道田
Yoshiaki Takahashi
善昭 高橋
Takuzo Sonoda
拓三 園田
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Kao Corp
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Abstract

<P>PROBLEM TO BE SOLVED: To provide a method for producing an extract for tea-based beverage, containing non-polymer catechins at a high concentration and having proper flavor, without damaging the natural flavor of each tea. <P>SOLUTION: The method for producing the extract for the tea-based beverage includes a step A for collecting an extract A, by inserting one or more kinds of the tea having 15 mg/100 mL or higher caffeine-analyzed value of the extract obtained by a cup test, and water for the extraction at 30-60°C in an amount corresponding to 5-30 times as much as the total mass of the tea; a step B for collecting an extract B, by inserting one or more kinds of the tea having lower than 15 mg/100 mL caffeine-analyzed value of the extract obtained by the cup test, and water for the extraction at 40-100°C, in an amount corresponding to 40-100 times as much as the total mass of the tea; and a step C for mixing the extract A and the extract B. <P>COPYRIGHT: (C)2009,JPO&INPIT

Description

本発明は、非重合体カテキン類を高濃度で含む茶系飲料用抽出液の製造方法に関する。   The present invention relates to a method for producing an extract for tea-based beverages containing a high concentration of non-polymer catechins.

近年、缶入り又はボトル入りの茶系飲料が大量に販売されている。これら茶系飲料は、通常、単一の茶又は複数種の茶から得られた抽出液を用いて製造されるが、苦味、渋味、香味、うま味等をバランスさせるには、単一の茶では困難であるため、複数種の茶が使用されることが多い。   In recent years, large quantities of canned or bottled tea-based beverages have been sold. These tea-based beverages are usually produced using an extract obtained from a single tea or a plurality of types of tea. To balance bitterness, astringency, flavor, umami, etc., a single tea In many cases, multiple types of tea are used.

複数種の茶を用いた茶系飲料の製造方法として、例えば、ニーダー抽出機内で玉露の茶葉を40〜60℃の抽出用水を用いて2〜6分間抽出し、別のニーダー抽出機内で深蒸茶の茶葉を55〜80℃の抽出用水を用いて3〜7分間抽出し、そして得られた各茶抽出液を混合する方法(特許文献1)、甜茶の茶葉を、ニーダー抽出機内で茶葉の重量に対して40倍量以上の85〜95℃の熱水を用いて3〜12分間抽出して得られる抽出液と、緑茶の茶葉を、別のニーダー抽出機内で茶葉の重量に対して40倍量以上の60〜70℃の温水を用いて3〜10分間抽出して得られる抽出液を所定割合で混合する方法(特許文献2)、更にカラム型の抽出機に茶葉を入れて冷水又は熱水を連続的に供給しながら抽出液を排出することによって得られた茶抽出液Aと、ニーダー抽出機で浸漬攪拌抽出して得られた抽出液Bを、A液中の非重合体カテキン類重量/B液中の非重合体カテキン類重量比が所定割合になるように混合した茶抽出液を用いた茶飲料の製造方法(特許文献3)等が提案されている。   As a method for producing a tea-based beverage using a plurality of types of tea, for example, gyokuro tea leaves are extracted for 2 to 6 minutes using 40 to 60 ° C. extraction water in a kneader extractor, and deep steamed tea in another kneader extractor. A method of extracting 3 to 7 minutes using water for extraction at 55 to 80 ° C. and mixing the obtained tea extracts (Patent Document 1), the weight of tea leaves in a kneader extractor 40 times or more of the extract obtained by extracting with hot water at 85 to 95 ° C. for 3 to 12 minutes and the tea leaves of green tea in a separate kneader extractor 40 times the weight of tea leaves A method of mixing an extract obtained by extracting for 3 to 10 minutes using 60 to 70 ° C of hot water at a predetermined amount or more (Patent Document 2), further putting tea leaves in a column-type extractor, cold water or heat Obtained by draining the extract while continuously supplying water The ratio of non-polymer catechins in liquid A / weight ratio of non-polymer catechins in liquid B of tea extract A and extract B obtained by immersion and extraction with a kneader extractor is a predetermined ratio. A method for producing a tea beverage using a tea extract mixed in this manner (Patent Document 3) has been proposed.

特開平8−126472号公報JP-A-8-126472 特開2006−187253号公報JP 2006-187253 A 特開2005−168429号公報JP 2005-168429 A

しかしながら、これら従来技術においては、いずれもニーダー抽出機を用いたバッチ抽出を採用するため、アロマ成分が逸脱しやすく、しかも香味と非重合体カテキン類濃度とをバランスさせた茶系飲料が得難いという問題がある。また、バッチ抽出の場合、各バッチ間において成分濃度が略均一の抽出液を得ることができるが、抽出液中の成分量をバッチ間ごとに適宜調整することは難しい。
また、複数種の茶を使用する場合、茶の種類によってうま味や香味等を最大限に引き出すための抽出条件が異なり、しかも抽出条件によって非重合体カテキン類濃度が変動し苦味渋味やエグ味が増強されるため、非重合体カテキン類を高濃度に含有し、うま味、香味、苦味、渋味、エグ味等をバランスさせた風味の良好な飲みやすい茶系飲料を得ることは容易でない。
本発明は、各茶の持ち味を損なうことなく、非重合体カテキン類を高濃度で含み、かつ風味の良好な茶系飲料用抽出液の製造方法、及び当該茶系飲料用抽出液を用いた容器詰茶系飲料を提供することを目的とする。
However, in these conventional techniques, since batch extraction using a kneader extractor is adopted, it is difficult to obtain a tea-based beverage in which aroma components are easily deviated and the flavor and non-polymer catechin concentration are balanced. There's a problem. In addition, in the case of batch extraction, an extract with a substantially uniform component concentration can be obtained between batches, but it is difficult to appropriately adjust the amount of components in the extract between batches.
In addition, when using multiple types of tea, the extraction conditions for maximizing umami and flavor vary depending on the type of tea, and the concentration of non-polymer catechins varies depending on the extraction conditions, resulting in bitterness and astringency. Therefore, it is not easy to obtain an easy-to-drink tea-based beverage having a high flavor of non-polymer catechins and balanced in umami, flavor, bitterness, astringency, egg taste, and the like.
The present invention uses a method for producing a tea-based beverage extract containing a high concentration of non-polymer catechins and having a good flavor without impairing the taste of each tea, and the tea-based beverage extract. The object is to provide a packaged tea beverage.

本発明者らは、性状の異なる複数種の茶を、それぞれカラム型抽出機を用いて特定条件で抽出し各抽出液を混合することで、各茶の持ち味を損なうことなく、風味と非重合体カテキン類濃度とをバランスさせた抽出液が得られることを見出した。   The present inventors extract a plurality of types of teas having different properties by using a column type extractor under specific conditions and mix each extract, thereby reducing the flavor and non-heavyness without impairing the taste of each tea. It has been found that an extract with a balanced catechin concentration can be obtained.

すなわち、本発明は、カップテストで得られる抽出液のカフェイン分析値が15mg/100mL以上となる茶の1種又は2種以上をカラム型抽出機内に仕込み、該茶の合計質量に対して5〜30倍量に相当する30〜60℃の抽出用水を供給して抽出液Aを採取するA工程と、カップテストで得られる抽出液のカフェイン分析値が15mg/100mL未満となる茶の1種又は2種以上をカラム型抽出機内に仕込み、該茶の合計質量に対して40〜100倍量に相当する40〜100℃の抽出用水を供給して抽出液Bを採取するB工程と、抽出液Aと抽出液Bとを混合するC工程とを含む茶系飲料用抽出液の製造方法を提供するものである。
本発明はまた、かかる製造方法により得られた茶系飲料用抽出液を、そのまま又は希釈して容器内に充填してなる容器詰茶系飲料を提供するものである。
That is, in the present invention, one or more teas whose caffeine analysis value of the extract obtained by the cup test is 15 mg / 100 mL or more are charged into a column-type extractor, and 5% of the total mass of the tea is obtained. A process of collecting extraction liquid A by supplying 30 to 60 ° C. extraction water corresponding to ˜30 times the amount, and 1 of tea whose caffeine analysis value of the extraction liquid obtained by the cup test is less than 15 mg / 100 mL B step of charging seeds or two or more species into a column type extractor, collecting extraction liquid B by supplying 40 to 100 ° C. extraction water corresponding to 40 to 100 times the total mass of the tea, The manufacturing method of the extract for tea type | system | group drinks including the C process which mixes the extract A and the extract B is provided.
The present invention also provides a packaged tea-based beverage obtained by filling a tea-based beverage extract obtained by such a production method as it is or after diluting it into a container.

本発明によれば、アロマ成分の逸脱を防止して、非重合体カテキン類を高濃度で含み、かつ風味の良好な茶系飲料用抽出液を簡便に製造することができる。かかる抽出液は、高い香りを有しながらも、苦渋味、エグ味が少ないことから、当該抽出液を用いることで、非重合体カテキン類を大量に摂取できる飲みやすい容器詰茶系飲料の提供が可能となる。   ADVANTAGE OF THE INVENTION According to this invention, the deviation of an aroma component can be prevented and the extract for tea-type drinks which contain non-polymer catechins by high concentration and has favorable flavor can be manufactured simply. Since such an extract has a high fragrance and has little bitterness and taste, the use of the extract provides an easy-to-drink packaged tea-based beverage that can ingest large amounts of non-polymer catechins. Is possible.

本発明の茶系飲料用抽出液の製造方法は、A工程、B工程及びC工程を含むことを特徴とする。以下、各工程について説明する。   The method for producing an extract for tea-based beverage of the present invention is characterized by comprising an A step, a B step and a C step. Hereinafter, each step will be described.

(A工程)
A工程は、カップテストで得られる抽出液のカフェイン分析値が15mg/100mL以上となる茶の1種又は2種以上をカラム型抽出機内に仕込み、該茶の合計質量に対して5〜30倍量に相当する30〜60℃の抽出用水を供給して抽出液Aを採取する工程である。
本発明においては、抽出方法としてカラム型抽出機を用いるカラム抽出を採用するが、カラム抽出とは、カラム型抽出機内に茶を充填し、これに抽出用水を通過させ抽出液を得る方法をいう。
(Process A)
In step A, one or more teas whose caffeine analysis value of the extract obtained by the cup test is 15 mg / 100 mL or more are charged into a column-type extractor, and 5 to 30 based on the total mass of the tea. In this step, extraction water at 30 to 60 ° C. corresponding to the double amount is supplied to extract extract A.
In the present invention, column extraction using a column type extractor is adopted as an extraction method. Column extraction refers to a method of filling a column type extractor with tea and passing extraction water therethrough to obtain an extract. .

カラム型抽出機としては、抽出用水の供給口と、抽出液の抜き出し口とを備えるものであれば特に限定されるものではないが、例えば、カラム型抽出機の上方から抽出用水を供給するタイプ、下方から抽出用水を供給するタイプ、あるいは双方から抽出用水を供給可能なタイプ等が利用できる。また、カラムの設置は縦型でも横型であってもよい。具体的には、図1に示すような閉鎖型抽出カラム1を用いることができる。抽出カラム1は、抽出用水を供給するための抽出用水供給用シャワーノズル2及び抽出用水供給用バルブ3と、抽出水を抜き出すための抽出液抜き出し用バルブ4を備えており、抽出カラム1内には茶6を保持するため茶保持板5が装着されている。
茶保持板としては、茶と抽出液とを分離できるものであれば特に限定されないが、金網(メッシュ)が好ましく、フラット、円錐状、角錐状等の形状のものを用いることができる。また、金網のメッシュサイズは、実質的に仕込んだ茶と茶抽出液との分離の点から、18〜100メッシュであるのが好ましい。
The column type extractor is not particularly limited as long as it has an extraction water supply port and an extraction liquid extraction port. For example, a type that supplies extraction water from above the column type extractor A type that supplies extraction water from below or a type that can supply extraction water from both sides can be used. The column may be installed vertically or horizontally. Specifically, a closed extraction column 1 as shown in FIG. 1 can be used. The extraction column 1 includes an extraction water supply shower nozzle 2 and an extraction water supply valve 3 for supplying extraction water, and an extraction liquid extraction valve 4 for extracting extraction water. A tea holding plate 5 is attached to hold tea 6.
The tea holding plate is not particularly limited as long as it can separate the tea and the extract, but a wire mesh (mesh) is preferable, and a plate having a flat shape, a conical shape, a pyramid shape, or the like can be used. Moreover, it is preferable that the mesh size of a wire mesh is 18-100 mesh from the point of isolation | separation of the tea and the tea extract which were substantially prepared.

A工程で使用される茶の製茶手段、すなわち発酵度合いとしては不発酵、半発酵、発酵が挙げられる。不発酵茶としては、Camellia属、例えばC.sinensis及びC.assamica、やぶきた種、又はそれらの雑種から得られる茶から製茶された、煎茶、番茶、玉露、てん茶、釜入り茶等の緑茶が挙げられる。半発酵茶又は発酵茶としては、Camellia属、例えばC.sinensis及びC.assamica、やぶきた種、又はそれらの雑種から得られる茶から半発酵又は発酵工程を経て製茶された、紅茶、烏龍茶、黒茶等が挙げられる。中でも、非重合体カテキン類の含有割合の高い不発酵茶が好ましい。   Examples of the tea making means used in step A, that is, the degree of fermentation, include non-fermentation, semi-fermentation, and fermentation. As non-fermented tea, green tea such as sencha, bancha, gyokuro, tencha, tea with tea made from teas obtained from the genus Camellia, such as C. sinensis and C. assamica, Yabutaki, or hybrids thereof Is mentioned. Semi-fermented tea or fermented tea includes teas, oolong teas, black teas made from teas obtained from the genus Camellia, for example, C. sinensis and C. assamica, Yabukita seeds, or hybrids thereof, through a semi-fermentation or fermentation process Tea etc. are mentioned. Among these, non-fermented tea having a high content of non-polymer catechins is preferable.

本発明においては、茶葉だけなく、茎茶、棒茶、芽茶を使用することができる。茎茶としては茶の茎の部分であって通常茎茶として用いられているものが挙げられ、また棒茶としては茶葉の軸や茎の部分であって通常棒茶として用いられているものが挙げられ、更に芽茶としては未だ葉にならない柔らかい芽の部分であって通常芽茶として用いられているものが挙げられる。
また、茶葉、茎茶及び棒茶は、火入れ加工が施されていてもよい。火入れ加工の原料としては不発酵茶が好ましく、苦味抑制効果の点から、茶葉より茎茶、棒茶の方が好適に使用される。火入れは、例えば、120〜300℃、更に170〜230℃の温度で、1〜15分、更に1〜10分加熱するのが苦味抑制効果及び風味の点から好ましい。
本発明においては、単一の茶だけなく、2種以上の茶を組み合わせて使用することができる。
In the present invention, not only tea leaves but also stem tea, stick tea, and bud tea can be used. Examples of stem tea include tea stem parts that are usually used as stem tea, and stick tea parts that are the stems and stem parts of tea leaves that are usually used as stick tea. Furthermore, examples of bud tea include soft bud portions that have not yet become leaves and are usually used as bud tea.
In addition, the tea leaves, stem tea, and stick tea may be subjected to a burning process. Non-fermented tea is preferred as a raw material for the firing process, and stem tea and stick tea are more preferably used than tea leaves from the viewpoint of the bitterness suppressing effect. For example, heating is preferably performed at a temperature of 120 to 300 ° C. and further 170 to 230 ° C. for 1 to 15 minutes, and further for 1 to 10 minutes from the viewpoint of bitterness suppressing effect and flavor.
In the present invention, not only a single tea but also two or more kinds of tea can be used in combination.

A工程においては、カップテストで得られる抽出液のカフェイン分析値が15mg/100mL以上となる茶を使用するが、カフェイン分析値が20mg/100mL以上、特に30mg/100mL以上のものが好ましい。カフェイン分析値が15mg/100mL未満であると、風味及びカテキン類の抽出効率上好ましくない。なお、カフェイン分析値の上限は、飲料本来の外観の観点から、45mg/100mLとするのが望ましい。
ここで、本明細書において、カップテストとは茶3gを審査茶碗(容量200cc)に秤取し、茶に熱湯180mLを注ぎ、5分間静置した後、茶殻を除いた抽出液について官能検査することをいい(新茶葉業全書 改訂発行6版 昭和55年8月10日 編集 静岡県茶業会議所)、カフェイン分析値とはこのカップテストで得られた抽出液中に含まれるカフェイン量を分析したものである。そして、この分析結果に基づき、使用する茶を選択する。なお、カフェイン含有量は、非重合体カテキン類含有量と同様に後掲の実施例に記載の測定方法によって高速液体クロマトグラフにより分析することができる。
In step A, tea whose caffeine analysis value of the extract obtained by the cup test is 15 mg / 100 mL or more is used, but a caffeine analysis value of 20 mg / 100 mL or more, particularly 30 mg / 100 mL or more is preferable. A caffeine analysis value of less than 15 mg / 100 mL is not preferable in terms of flavor and catechin extraction efficiency. The upper limit of the caffeine analysis value is preferably 45 mg / 100 mL from the viewpoint of the original appearance of the beverage.
Here, in this specification, the cup test means that 3 g of tea is weighed into an examination teacup (capacity 200 cc), 180 mL of hot water is poured into the tea, and the mixture is allowed to stand for 5 minutes, and then the sensory test is performed on the extract from which the tea shell is removed. That's good (new tea leaf business revised edition 6th edition August 10, 1980 edited by the Shizuoka Prefectural Tea Chamber), and the caffeine analysis value is the amount of caffeine contained in the extract obtained by this cup test Is an analysis. And based on this analysis result, the tea to be used is selected. The caffeine content can be analyzed by a high performance liquid chromatograph by the measurement method described in the examples described later in the same manner as the non-polymer catechin content.

抽出用水は水道水、蒸留水、イオン交換水等を適宜選択することができるが、味の面からイオン交換水が好ましい。また、抽出用水に、アスコルビン酸又はその塩、重曹等を添加してもよい。アスコルビン酸又はその塩の濃度は、抗酸化効果及び味の点から、0.01〜0.2質量%、更には0.02〜0.15質量%、特に0.03〜0.1質量%が好ましい。   The extraction water can be appropriately selected from tap water, distilled water, ion-exchanged water, etc., but ion-exchanged water is preferred in terms of taste. Moreover, you may add ascorbic acid or its salt, baking soda, etc. to the water for extraction. The concentration of ascorbic acid or a salt thereof is 0.01 to 0.2% by mass, further 0.02 to 0.15% by mass, particularly 0.03 to 0.1% by mass, from the viewpoint of antioxidant effect and taste. Is preferred.

抽出方法としては、いわゆる循環法や1パス法等を採用することができる。ここで、本明細書において、「循環法」とは、茶から得られた抽出液をカラム型抽出機内に再度戻し、この操作を繰り返し行う抽出法をいい、一方「1パス法」とは抜き出した抽出液をカラム型抽出機内に再度戻すことなく、一度の通水により抽出する抽出法をいう。
また、通水方向としては、抽出用水をカラム型抽出機の下方から上方に通水(上昇流)しても、カラム型抽出機の上方から下方に通水(下降流)してもよいが、茶が圧密化によりカラム型抽出機内で閉塞することを防止可能な上昇流が好ましい。
As the extraction method, a so-called circulation method, one-pass method, or the like can be employed. Here, in this specification, the “circulation method” refers to an extraction method in which the extract obtained from tea is returned again into the column type extractor and this operation is repeated, while the “one-pass method” is extracted. This is an extraction method in which the extracted liquid is extracted by passing water once without returning it to the column type extractor.
In addition, as the water flow direction, the extraction water may flow from the bottom to the top of the column type extractor (upflow) or may flow from the top to the bottom of the column type extractor (downflow). An upward flow capable of preventing the tea from being clogged in the column type extractor due to compaction is preferable.

抽出倍率、すなわち(抽出用水の供給量)/(茶の合計質量)は、5〜30であるが、更には10〜30、特に15〜30が好ましい。これにより、抽出液中の非重合体カテキン濃度を高めることができる。
抽出用水の供給速度をカラム断面積で割った値、すなわちカラム型抽出機内における抽出用水の線速度は、0.9〜1.9cm/min、更には1.1〜1.7cm/min、特に1.3〜1.5cm/minが好ましい。これにより、茶が圧密となって閉塞するのを防止して効率的に抽出することができる。
抽出用水の温度は30〜60℃であるが、40〜60℃、特に50〜60℃が好ましい。30℃未満であると、抽出液の風味及びカテキン類の抽出効率上好ましくない。他方60℃を超えると、抽出液の風味上好ましくない。
滞留時間は、3.5〜6.5分、更には4.5〜6.5分、特に5.5〜6.5分が好ましい。これにより、非重合体カテキン類を高濃度で含み、風味豊かな抽出液を得ることができる。
The extraction magnification, that is, (extraction water supply amount) / (total tea mass) is 5 to 30, more preferably 10 to 30, and particularly preferably 15 to 30. Thereby, the non-polymer catechin density | concentration in an extract can be raised.
The value obtained by dividing the supply rate of the extraction water by the column cross-sectional area, that is, the linear velocity of the extraction water in the column type extractor is 0.9 to 1.9 cm / min, more particularly 1.1 to 1.7 cm / min. 1.3 to 1.5 cm / min is preferable. Thereby, it is possible to efficiently extract tea while preventing the tea from being consolidated and blocked.
Although the temperature of the water for extraction is 30-60 degreeC, 40-60 degreeC, especially 50-60 degreeC are preferable. If it is lower than 30 ° C., it is not preferable in terms of the flavor of the extract and the extraction efficiency of catechins. On the other hand, when it exceeds 60 degreeC, it is unpreferable on the flavor of an extract.
The residence time is preferably 3.5 to 6.5 minutes, more preferably 4.5 to 6.5 minutes, and particularly preferably 5.5 to 6.5 minutes. Thereby, a non-polymer catechin can be obtained at a high concentration, and an extract rich in flavor can be obtained.

本発明においては、得られた抽出液の一部又は全部を抽出液Aとすることができる。例えば、抽出初期、抽出中期、抽出後期のうちのいずれかの抽出段階において採取された抽出液のみを用いてもよく、またそれらの一部又は全てを混合した抽出液を用いてもよい。また、一部の抽出段階の抽出液を廃棄し、それ以外の抽出段階において採取した抽出液を用いてもよく、例えば、風味向上の観点から、抽出初期のものを廃棄し、それ以降の抽出段階から採取した抽出液を用いてもよい。この場合、茶の合計質量に対して0.15〜3倍量、特に0.75〜2.3倍量に相当する抽出初期の抽出液を廃棄し、それ以降(抽出中期及び抽出後期)の抽出液を採取するのが好ましい。0.15倍未満では風味向上効果が不十分となる傾向にあり、他方3倍を超えるとカテキン類の抽出収率が低下する傾向にある。また、採取倍率、すなわち(抽出液の採取量)/(茶の合計質量)は、抽出倍率の80%以上、特に85%以上とするのが好ましい。
得られた抽出液Aは、活性炭や膜処理等の処理を施してもよい。
In the present invention, a part or all of the obtained extract can be used as the extract A. For example, it is possible to use only the extract collected at the extraction stage in any one of the initial stage, the middle stage of extraction, and the late stage of extraction, or use an extract obtained by mixing a part or all of them. Alternatively, the extract from some extraction stages may be discarded, and the extract collected at other extraction stages may be used. For example, from the viewpoint of flavor improvement, the initial extraction is discarded and the subsequent extraction is performed. An extract collected from the stage may be used. In this case, the initial extraction liquid corresponding to 0.15 to 3 times, especially 0.75 to 2.3 times the total mass of tea is discarded, and thereafter (mid-extraction and late extraction) It is preferable to collect the extract. If it is less than 0.15 times, the flavor improving effect tends to be insufficient, and if it exceeds 3 times, the extraction yield of catechins tends to decrease. Further, it is preferable that the sampling rate, that is, (amount of extract extracted) / (total tea mass) is 80% or more, particularly 85% or more of the extraction rate.
The obtained extract A may be subjected to treatment such as activated carbon or membrane treatment.

(B工程)
B工程は、カップテストで得られる抽出液のカフェイン分析値が15mg/100mL未満となる茶の1種又は2種以上をカラム型抽出機内に仕込み、該茶の合計質量に対して40〜100倍量に相当する40〜100℃の抽出用水を供給して抽出液Bを採取する工程である。
(Process B)
In Step B, one or more teas whose caffeine analysis value of the extract obtained by the cup test is less than 15 mg / 100 mL are charged in a column-type extractor, and 40 to 100 based on the total mass of the tea. This is a step of collecting extraction liquid B by supplying extraction water at 40 to 100 ° C. corresponding to the double amount.

B工程においてはA工程と同種の茶を使用することができるが、カップテストで得られる抽出液のカフェイン分析値が15mg/100mL未満となる茶を使用する。カフェイン分析値は、12mg/100mL未満、特に8mg/100mL未満のものが好ましい。カフェイン分析値が15mg/100mL以上であると、風味のバランス上好ましくない。なお、カフェイン分析値の下限は、風味の観点から、2mg/100mLとするのが望ましい。   In step B, the same type of tea as in step A can be used, but tea whose caffeine analysis value of the extract obtained by the cup test is less than 15 mg / 100 mL is used. The caffeine analysis value is preferably less than 12 mg / 100 mL, particularly less than 8 mg / 100 mL. A caffeine analysis value of 15 mg / 100 mL or more is not preferable in terms of flavor balance. The lower limit of the caffeine analysis value is preferably 2 mg / 100 mL from the viewpoint of flavor.

B工程においては、A工程と同様の抽出方法を採用することができる。
抽出条件において、抽出用水の供給量は、茶の合計質量に対して40〜100倍量であるが、50〜90倍量、特に60〜80倍量が好ましい。40倍量未満であると、風味とカテキン類の抽出効率から好ましくなく、他方100倍量を超えると、風味上好ましくない。すなわち、抽出倍率は40〜100であるが、好ましくは50〜90、特に60〜80が好ましい。これにより、風味と物性のバランスの取れた抽出液を抽出することが出来る。
抽出用水の温度は40〜100℃であるが、50〜90℃、特に55〜80℃が好ましい。40℃未満であると、風味上好ましくなく、他方80℃を超えると、使用する茶の種類によっては苦渋味が増強されるため、好ましくない。
In the B process, the same extraction method as in the A process can be employed.
In the extraction conditions, the supply amount of the extraction water is 40 to 100 times the total amount of tea, but is preferably 50 to 90 times, particularly 60 to 80 times. If it is less than 40 times the amount, it is not preferable from the taste and the extraction efficiency of catechins, and if it exceeds 100 times the amount, it is not preferable on the flavor. That is, the extraction magnification is 40 to 100, preferably 50 to 90, and particularly preferably 60 to 80. Thereby, it is possible to extract an extract having a good balance between flavor and physical properties.
Although the temperature of the water for extraction is 40-100 degreeC, 50-90 degreeC, especially 55-80 degreeC are preferable. If it is less than 40 ° C., it is not preferable in terms of flavor, and if it exceeds 80 ° C., the bitter astringency is enhanced depending on the type of tea used, which is not preferable.

B工程においてもA工程と同様に、抽出液の一部又は全部を抽出液Bとすることができるが、抽出用水を供給して得られた抽出液の全部を抽出液Bとするのが好ましい。   In Step B as well as Step A, a part or the whole of the extract can be used as Extract B, but it is preferable that all of the extract obtained by supplying the extraction water is used as Extract B. .

(C工程)
C工程は、A工程で得られた抽出液Aと、B工程で得られた抽出液Bとを混合する工程である。抽出液Aと抽出液Bとの混合割合は、目的とする茶系飲料の呈味に応じて適宜決定することができるが、抽出液Aと抽出液Bとの混合質量比(A/B)を1〜5、更には1.5〜4.5、特に2〜4とするのが、茶系飲料用抽出液中の非重合体カテキン類濃度の確保、及び風味の維持の点から好ましい。
(Process C)
The C process is a process of mixing the extract A obtained in the A process and the extract B obtained in the B process. The mixing ratio of the extract A and the extract B can be appropriately determined according to the taste of the target tea beverage, but the mixing mass ratio of the extract A and the extract B (A / B) Is preferably from 1 to 5, more preferably from 1.5 to 4.5, and particularly preferably from 2 to 4, from the viewpoints of securing the concentration of non-polymer catechins in the tea-based beverage extract and maintaining the flavor.

このようにして茶系飲料用抽出液が得られるが、茶系飲料用抽出液中の非重合体カテキン類の含有量は、0.1〜0.5質量%が好ましく、更には0.3〜0.5質量%、特に0.4〜0.5質量%であるのが好ましい。なお、このような濃度で非重合体カテキン類を含む茶系飲料用抽出液とするには、例えば、上記した割合で抽出液A及び抽出液Bを混合すればよい。ここで、非重合体カテキン類とは、カテキン、ガロカテキン、カテキンガレート、ガロカテキンガレート等の非エピ体カテキン類及びエピカテキン、エピガロカテキン、エピカテキンガレート、エピガロカテキンガレート等のエピ体カテキン類をあわせての総称であり、非重合体カテキン類の濃度は、上記8種の合計量に基づいて定義される。   Thus, an extract for tea-based beverages is obtained. The content of non-polymer catechins in the extract for tea-based beverages is preferably 0.1 to 0.5% by mass, and more preferably 0.3. It is preferably -0.5% by mass, particularly 0.4-0.5% by mass. In order to obtain a tea-based beverage extract containing non-polymer catechins at such a concentration, for example, the extract A and the extract B may be mixed at the aforementioned ratio. Here, non-polymer catechins are non-epimeric catechins such as catechin, gallocatechin, catechin gallate, gallocatechin gallate, and epicatechins such as epicatechin, epigallocatechin, epicatechin gallate, epigallocatechin gallate, etc. And the concentration of non-polymer catechins is defined based on the total amount of the above eight types.

上記工程により得られた茶系飲料用抽出液は、高濃度の非重合体カテキン類を含有しながらも、苦味渋味やエグ味が少なく香味が豊かで風味がよいので、そのまま、又は希釈することにより容器詰茶系飲料とすることができる。このとき、非重合体カテキン類濃度を、好ましくは0.05〜0.6質量%、より好ましくは0.07〜0.5質量%、更に好ましくは0.092〜0.4質量%、特に好ましくは0.12〜0.3質量%になるように調整するのが望ましい。この範囲にあると多量の非重合体カテキン類を摂取しやすくなる。   The tea-based beverage extract obtained by the above process contains a high concentration of non-polymer catechins, but has little bitter astringency and abundant taste, rich flavor, and good flavor. By this, it can be set as a packaged tea beverage. At this time, the concentration of non-polymer catechins is preferably 0.05 to 0.6% by mass, more preferably 0.07 to 0.5% by mass, still more preferably 0.092 to 0.4% by mass, particularly It is desirable to adjust so that it may become 0.12-0.3 mass% preferably. When it is within this range, a large amount of non-polymer catechins can be easily ingested.

また、本発明の容器詰茶飲料には、茶由来の成分にあわせて、酸化防止剤、香料、各種エステル類、有機酸類、有機酸塩類、無機酸類、無機酸塩類、無機塩類、色素類、乳化剤、保存料、調味料、甘味料、酸味料、ガム、油、ビタミン、アミノ酸、果汁エキス類、野菜エキス類、花蜜エキス類、pH調整剤、苦味調製剤、品質安定剤等の添加剤を単独で又は2種以上組み合わせて配合してもよい。   In addition, in the packaged tea beverage of the present invention, an antioxidant, a fragrance, various esters, an organic acid, an organic acid salt, an inorganic acid, an inorganic acid salt, an inorganic salt, a pigment, Additives such as emulsifiers, preservatives, seasonings, sweeteners, acidulants, gums, oils, vitamins, amino acids, fruit juice extracts, vegetable extracts, nectar extracts, pH adjusters, bitterness adjusters, quality stabilizers, etc. You may mix | blend individually or in combination of 2 or more types.

甘味料としては、例えば、砂糖、ぶどう糖、果糖、異性化液糖、グリチルリチン、ステビア、アスパルテーム、スクラロース、フラクトオリゴ糖、ガラクトオリゴ糖が挙げられる。苦味調整剤としては、シクロデキストリンに代表される環状デキストリンが挙げられる。環状デキストリンとしては、α−、β−、γ−シクロデキストリン及び、分岐のシクロデキストリンが使用できる。酸味料としては、例えば、天然成分から抽出した果汁類のほか、クエン酸、酒石酸、リンゴ酸、乳酸、フマル酸、リン酸が挙げられる。無機酸類、無機酸塩類としては、例えば、リン酸、リン酸二ナトリウム、メタリン酸ナトリウム、ポリリン酸ナトリウム等が挙げられ、有機酸類、有機酸塩類としては、例えば、クエン酸、コハク酸、イタコン酸、リンゴ酸、クエン酸ナトリウム等が挙げられる。   Examples of the sweetener include sugar, glucose, fructose, isomerized liquid sugar, glycyrrhizin, stevia, aspartame, sucralose, fructooligosaccharide, and galactooligosaccharide. Examples of the bitterness adjusting agent include cyclic dextrin typified by cyclodextrin. As the cyclic dextrin, α-, β-, γ-cyclodextrin and branched cyclodextrin can be used. Examples of the sour agent include citric acid, tartaric acid, malic acid, lactic acid, fumaric acid, and phosphoric acid, in addition to fruit juices extracted from natural ingredients. Examples of inorganic acids and inorganic acid salts include phosphoric acid, disodium phosphate, sodium metaphosphate, and sodium polyphosphate. Examples of organic acids and organic acid salts include citric acid, succinic acid, and itaconic acid. , Malic acid, sodium citrate and the like.

また、本発明の容器詰茶系飲料には、抗酸化剤としてのアスコルビン酸又はその塩を茶の抽出後に添加することができる。容器詰茶系飲料中におけるアスコルビン酸又はその塩の濃度は、抗酸化効果及び味の点から、0.01〜0.2質量%、更には0.02〜0.15質量%、特に0.03〜0.1質量%が好ましい。   In addition, ascorbic acid or a salt thereof as an antioxidant can be added to the container-packed tea beverage of the present invention after tea extraction. The concentration of ascorbic acid or a salt thereof in the packaged tea-based beverage is 0.01 to 0.2% by mass, further 0.02 to 0.15% by mass, and particularly preferably from the viewpoint of the antioxidant effect and taste. 03-0.1 mass% is preferable.

本発明の容器詰茶飲料のpHは25℃で3〜7、更には4〜7、特に5〜7とするのが、味及び非重合体カテキン類の安定性の点で好ましい。   The pH of the packaged tea beverage of the present invention is preferably 3 to 7, more preferably 4 to 7, and particularly preferably 5 to 7 at 25 ° C. in terms of taste and stability of non-polymer catechins.

本発明の容器詰茶飲料に使用される容器は、一般の飲料と同様にポリエチレンテレフタレートを主成分とする成形容器(いわゆるPETボトル)、金属缶、金属箔やプラスチックフィルムと複合化した紙容器、瓶などの通常の形態で提供することができる。ここでいう容器詰茶飲料とは希釈せずに飲用できるものをいう。   The container used for the container-packed tea beverage of the present invention is a molded container mainly composed of polyethylene terephthalate (so-called PET bottle), a metal can, a paper container combined with a metal foil or a plastic film, as with a general beverage, It can be provided in a conventional form such as a bottle. The container-packed tea beverage here means a beverage that can be drunk without dilution.

本発明の容器詰茶飲料は、例えば、金属缶のように容器に充填後、加熱殺菌できる場合にあっては食品衛生法(例えば、UHT殺菌、レトルト殺菌)に定められた殺菌条件で製造されるが、ポリエチレンテレフタレートを主成分とする成形容器(いわゆるPETボトル)や、金属箔又はプラスチックフィルムにより複合化された紙容器のようにレトルト殺菌できないものについては、あらかじめ上記と同等の殺菌条件、例えばプレート式熱交換器等で高温短時間殺菌後、一定温度まで冷却して容器に充填する等の方法が採用される。更に、酸性下で加熱殺菌後、無菌下でpHを中性に戻すことや、中性下で加熱殺菌後、無菌下でpHを酸性に戻すなどの操作も可能である。   The container-packed tea beverage of the present invention is manufactured under the sterilization conditions stipulated in the Food Sanitation Law (for example, UHT sterilization, retort sterilization) if it can be sterilized by heating after filling the container like a metal can. However, for those that cannot be retort sterilized, such as molded containers mainly composed of polyethylene terephthalate (so-called PET bottles) and paper containers that are composited with metal foil or plastic film, A method of sterilizing at a high temperature and short time with a plate heat exchanger or the like and then cooling to a certain temperature and filling the container is adopted. Furthermore, after sterilizing under heat, the pH can be returned to neutral under aseptic conditions, or after sterilizing under heat under neutral conditions, the pH can be returned to acidic conditions under aseptic conditions.

(非重合体カテキン類及びカフェインの測定)
抽出液又は飲料をイオン交換水で100gに希釈した後、メンブランフィルター(0.8μm)でろ過し、次いで蒸留水で希釈した試料を、オクタデシル基導入液体クロマトグラフ用パックドカラム L−カラムTM ODS(4.6mmφ×250mm:財団法人 化学物質評価研究機構製)を装着した、島津製作所製、高速液体クロマトグラフ(型式SCL−10AVP)を用いて、カラム温度35℃でグラジエント法により測定した。移動相A液は酢酸を0.1mol/L含有の蒸留水溶液、B液は酢酸を0.1mol/L含有のアセトニトリル溶液とし、試料注入量は20μL、UV検出器波長は280nmの条件で行った。
(Measurement of non-polymer catechins and caffeine)
The extract or beverage was diluted to 100 g with ion-exchanged water, filtered through a membrane filter (0.8 μm), and then diluted with distilled water, and a sample packed in an octadecyl group-introduced liquid chromatograph L-column TM ODS ( 4.6 mmφ × 250 mm: Measured by a gradient method at a column temperature of 35 ° C. using a high performance liquid chromatograph (model SCL-10AVP) manufactured by Shimadzu Corporation equipped with a chemical substance evaluation research organization. The mobile phase A solution was a distilled aqueous solution containing 0.1 mol / L of acetic acid, the B solution was an acetonitrile solution containing 0.1 mol / L of acetic acid, the sample injection amount was 20 μL, and the UV detector wavelength was 280 nm. .

濃度勾配条件(体積%)
時間 移動相A 移動相B
0分 97% 3%
5分 97% 3%
37分 80% 20%
43分 80% 20%
43.5分 0% 100%
48.5分 0% 100%
49分 97% 3%
62分 97% 3%
Concentration gradient condition (volume%)
Time Mobile phase A Mobile phase B
0 minutes 97% 3%
5 minutes 97% 3%
37 minutes 80% 20%
43 minutes 80% 20%
43.5 minutes 0% 100%
48.5 minutes 0% 100%
49 minutes 97% 3%
62 minutes 97% 3%

(実施例1)
緑茶(煎茶:カップテストで得られた抽出液のカフェイン分析値33.6mg/100mL)100gをカラム型抽出機内(内径97mm、高さ400mm)に入れ、55℃に加熱したイオン交換水を0.103L/minの速度でカラム下方から供給した。このとき、抽出時の高さは83mm、線速度は1.4cm/min、平均滞留時間は5.9minであった。その後、カラム下方から抽出液を抜き出しながら55℃に加熱したイオン交換水を0.107L/minの速度でカラム上方から供給した。このとき、平均滞留時間は5.9minであった。抽出液の質量が仕込み茶葉質量の1.5倍になったところから採液を開始し、15倍になったところで通液を終了し、採液タンク内の液を均一に混合して抽出液Aを得た(A工程)。
緑茶(棒茶:カフェイン分析値7.2mg/100mL)100gをカラム型抽出機内(内径97mm、高さ400mm)に入れ、75℃に加熱したイオン交換水を0.103L/minの速度でカラム下方から供給した。このとき、抽出時の高さは83mm、線速度は1.4cm/min、平均滞留時間は5.9minであった。その後、カラム下方から抽出液を抜き出しながら75℃に加熱したイオン交換水を0.103L/minの速度でカラム上方から供給した。このとき、平均滞留時間は5.9minであった。最初から採液を開始し、抽出液の質量が仕込み茶葉質量の60倍になったところで通液を終了し、採液タンク内の液を均一に混合して抽出液Bを得た(B工程)。
得られた各抽出液を質量比(抽出液A/抽出液B)4で混合し(C工程)、茶系飲料用抽出液を得た。茶系飲料用抽出液の非重合体カテキン濃度は0.41質量%であった。次いで、茶系飲料用抽出液に、0.03質量%のアスコルビン酸を加え加水した後、殺菌処理し、常法によりPETボトルに詰め容器詰茶系飲料を得た。
Example 1
100 g of green tea (sencha: caffeine analysis value of the extract obtained in the cup test 33.6 mg / 100 mL) is placed in a column-type extractor (inner diameter 97 mm, height 400 mm) and ion-exchanged water heated to 55 ° C is 0.103 L / Min was fed from the bottom of the column. At this time, the height during extraction was 83 mm, the linear velocity was 1.4 cm / min, and the average residence time was 5.9 min. Thereafter, ion-exchanged water heated to 55 ° C. was extracted from the bottom of the column at a rate of 0.107 L / min while extracting the extract from the bottom. At this time, the average residence time was 5.9 min. When the amount of the extract is 1.5 times the amount of the tea leaves charged, the liquid collection is started, and when the amount is 15 times, the liquid flow is terminated, and the liquid in the liquid collection tank is uniformly mixed to obtain the extract A. Obtained (step A).
100 g of green tea (stick tea: caffeine analysis value 7.2 mg / 100 mL) is placed in a column type extractor (inner diameter 97 mm, height 400 mm), and ion-exchanged water heated to 75 ° C. is added from the bottom of the column at a rate of 0.103 L / min. Supplied. At this time, the height during extraction was 83 mm, the linear velocity was 1.4 cm / min, and the average residence time was 5.9 min. Thereafter, ion-exchanged water heated to 75 ° C. was extracted from the top of the column at a rate of 0.103 L / min while extracting the extract from the bottom of the column. At this time, the average residence time was 5.9 min. Liquid collection was started from the beginning. When the mass of the extract became 60 times the charged tea leaf mass, the liquid flow was terminated, and the liquid in the liquid collection tank was uniformly mixed to obtain extract B (Step B) ).
Each obtained extract was mixed at a mass ratio (extract A / extract B) 4 (step C) to obtain an extract for tea-based beverages. The concentration of non-polymer catechin in the tea-based beverage extract was 0.41% by mass. Next, 0.03% by mass of ascorbic acid was added to the tea-based beverage extract, and the mixture was sterilized and then packed into PET bottles by a conventional method to obtain a container-packed tea-based beverage.

(実施例2)
A工程において抽出液を全量採液し、B工程における抽出条件を表1に記載のものに変更したこと以外は、実施例1と同様な方法にて容器詰茶系飲料を得た。なお、茶系飲料用抽出液の非重合体カテキン濃度は0.49質量%であった。
(Example 2)
A packaged tea beverage was obtained in the same manner as in Example 1 except that the entire amount of the extract was collected in step A and the extraction conditions in step B were changed to those shown in Table 1. The non-polymer catechin concentration in the tea-based beverage extract was 0.49% by mass.

(実施例3)
A工程において抽出液を全量採液し、B工程における抽出条件を表1に記載のものに変更したこと以外は、実施例1と同様な方法にて容器詰茶系飲料を得た。なお、茶系飲料用抽出液の非重合体カテキン濃度は0.49質量%であった。
(Example 3)
A packaged tea beverage was obtained in the same manner as in Example 1 except that the entire amount of the extract was collected in step A and the extraction conditions in step B were changed to those shown in Table 1. The non-polymer catechin concentration in the tea-based beverage extract was 0.49% by mass.

(実施例4)
A工程における抽出条件を表1に記載のものに変更して抽出液を全量採取し、C工程における混合質量比を表1に記載のものに変更したこと以外は、実施例1と同様な方法にて容器詰茶系飲料を得た。なお、茶系飲料用抽出液の非重合体カテキン濃度は0.38質量%であった。
Example 4
The same method as in Example 1 except that the extraction conditions in step A were changed to those shown in Table 1 and the whole extract was collected and the mixing mass ratio in step C was changed to that shown in Table 1. A canned tea-based beverage was obtained. The non-polymer catechin concentration in the tea-based beverage extract was 0.38% by mass.

(比較例1)
55℃のイオン交換水1500g(抽出倍率15倍に相当)を入れたニーダー抽出機内に、緑茶(煎茶)100gを投入し5分間攪拌抽出して抽出液Aを得た。75℃の熱水6000g(抽出倍率60倍に相当)を入れた別のニーダー抽出機内に、緑茶(棒茶)100gを投入し5分間攪拌抽出して抽出液Bを得た。次いで、各抽出液を質量比(抽出液A/抽出液B)4で混合して茶系飲料用抽出液を得た。茶系飲料用抽出液の非重合体カテキン濃度は0.38質量%であった。次いで、茶系飲料用抽出液を実施例1と同様の方法により処理して容器詰茶系飲料を得た。
(Comparative Example 1)
100 g of green tea (sencha) was placed in a kneader extractor containing 1500 g of ion-exchanged water at 55 ° C. (corresponding to an extraction ratio of 15 times), and extracted with stirring for 5 minutes to obtain Extract A. In another kneader extractor containing 6000 g of hot water at 75 ° C. (corresponding to an extraction ratio of 60 times), 100 g of green tea (bar tea) was added and stirred and extracted for 5 minutes to obtain an extract B. Subsequently, each extract was mixed at a mass ratio (extract A / extract B) 4 to obtain an extract for tea-based beverages. The non-polymer catechin concentration in the tea-based beverage extract was 0.38% by mass. Next, the tea-based beverage extract was processed in the same manner as in Example 1 to obtain a packaged tea-based beverage.

(比較例2)
実施例1と同様にして抽出液Aを得た。75℃の熱水6000g(抽出倍率60倍に相当)を入れたニーダー抽出機内に、緑茶(棒茶)100gを投入し5分間攪拌抽出して抽出液Bを得た。次いで、各抽出液を質量比(抽出液A/抽出液B)4で混合して茶系飲料用抽出液を得た。茶系飲料用抽出液の非重合体カテキン濃度は0.41質量%であった。次いで、茶系飲料用抽出液を実施例1と同様の方法により処理して容器詰茶系飲料を得た。
(Comparative Example 2)
Extract A was obtained in the same manner as Example 1. In a kneader extractor containing 6000 g of hot water at 75 ° C. (corresponding to an extraction ratio of 60 times), 100 g of green tea (bar tea) was added and stirred for 5 minutes to obtain an extract B. Subsequently, each extract was mixed at a mass ratio (extract A / extract B) 4 to obtain an extract for tea-based beverages. The concentration of non-polymer catechin in the tea-based beverage extract was 0.41% by mass. Next, the tea-based beverage extract was processed in the same manner as in Example 1 to obtain a packaged tea-based beverage.

(比較例3)
A工程及びB工程における抽出条件を表1に記載のものに変更し、C工程における混合質量比を表1に記載のものに変更したこと以外は、実施例1と同様な方法にて容器詰茶系飲料を得た。なお、茶系飲料用抽出液の非重合体カテキン濃度は0.18質量%であった。
(Comparative Example 3)
Containers were packed in the same manner as in Example 1 except that the extraction conditions in Step A and Step B were changed to those shown in Table 1, and the mixing mass ratio in Step C was changed to that shown in Table 1. A tea-based beverage was obtained. The non-polymer catechin concentration in the tea-based beverage extract was 0.18% by mass.

(比較例4)
A工程及びB工程における抽出条件を表1に記載のものに変更し、C工程における混合質量比を表1に記載のものに変更したこと以外は、実施例1と同様な方法にて容器詰茶系飲料を得た。なお、茶系飲料用抽出液の非重合体カテキン濃度は0.39質量%であった。
(Comparative Example 4)
Containers were packed in the same manner as in Example 1 except that the extraction conditions in Step A and Step B were changed to those shown in Table 1, and the mixing mass ratio in Step C was changed to that shown in Table 1. A tea-based beverage was obtained. The non-polymer catechin concentration in the tea-based beverage extract was 0.39% by mass.

(比較例5)
A工程及びB工程で使用した茶葉、並びにA工程における抽出条件を表1に記載のものに変更したこと以外は、実施例1と同様な方法にて容器詰茶系飲料を得た。なお、茶系飲料用抽出液の非重合体カテキン濃度は0.22質量%であった。
(Comparative Example 5)
A packaged tea-based beverage was obtained in the same manner as in Example 1 except that the tea leaves used in Step A and Step B and the extraction conditions in Step A were changed to those shown in Table 1. The non-polymer catechin concentration in the tea-based beverage extract was 0.22% by mass.

(風味の評価)
各茶系飲料用抽出液を最終カテキン濃度が0.10質量%になるように希釈し、パネラー4名で風味を評価した。評価項目は、香り、飲用中の苦渋味、飲用後のエグ味である。
(Evaluation of flavor)
Each tea beverage extract was diluted so that the final catechin concentration was 0.10% by mass, and the flavor was evaluated by 4 panelists. Evaluation items are aroma, bitter and astringent taste during drinking, and taste after drinking.

(評価基準)
◎:非常に良好。〇:良好。△:やや不良。×:不良。
(Evaluation criteria)
A: Very good. ○: Good. Δ: Slightly poor X: Defect.

Figure 2009125058
Figure 2009125058

実施例1で得られた茶系飲料用抽出液は、苦味及び渋味がなく、香りが高いものであった。また、実施例2〜4で得られた茶系飲料用抽出液は、苦味及び渋味が殆どなく、香りが高いものであった。これに対し、比較例1〜5で得られた茶系飲料用抽出液は、香りが少なく、また、比較例1〜5は苦味及び渋味があり、エグ味が残るものであった。   The extract for tea-based beverages obtained in Example 1 had no bitterness and astringency and a high aroma. Moreover, the extract for tea-based beverages obtained in Examples 2 to 4 had little bitterness and astringency and high aroma. On the other hand, the extract for tea-based beverages obtained in Comparative Examples 1 to 5 had little fragrance, and Comparative Examples 1 to 5 had bitterness and astringency, and the taste remained.

本発明の製造方法に使用可能なカラム型抽出機の一例を示す模式図である。It is a schematic diagram which shows an example of the column type extractor which can be used for the manufacturing method of this invention.

符号の説明Explanation of symbols

1 カラム型抽出機
2 抽出用水供給用シャワーノズル
3 抽出用水供給用バルブ
4 抽出液抜き出し用バルブ
5 茶保持板
6 茶葉
DESCRIPTION OF SYMBOLS 1 Column type extractor 2 Shower nozzle for water supply for extraction 3 Valve for water supply for extraction 4 Valve for extraction liquid extraction 5 Tea holding plate 6 Tea leaf

Claims (4)

カップテストで得られる抽出液のカフェイン分析値が15mg/100mL以上となる茶の1種又は2種以上をカラム型抽出機内に仕込み、該茶の合計質量に対して5〜30倍量に相当する30〜60℃の抽出用水を供給して抽出液Aを採取するA工程と、
カップテストで得られる抽出液のカフェイン分析値が15mg/100mL未満となる茶の1種又は2種以上をカラム型抽出機内に仕込み、該茶の合計質量に対して40〜100倍量に相当する40〜100℃の抽出用水を供給して抽出液Bを採取するB工程と、
抽出液Aと抽出液Bとを混合するC工程とを含む茶系飲料用抽出液の製造方法。
One or two or more teas with a caffeine analysis value of 15 mg / 100 mL or more of the extract obtained in the cup test are charged into a column-type extractor, which corresponds to 5 to 30 times the total mass of the tea A process of collecting extraction liquid A by supplying water for extraction at 30 to 60 ° C.,
One or two or more teas whose caffeine analysis value of the extract obtained by the cup test is less than 15 mg / 100 mL is charged into a column-type extractor, which corresponds to 40 to 100 times the total mass of the tea B step of collecting extraction liquid B by supplying extraction water at 40-100 ° C.
The manufacturing method of the extract for tea type | system | group drinks including the C process which mixes the extract A and the extract B.
抽出液Aと抽出液Bとの混合質量比(A/B)が1〜5である、請求項1記載の製造方法。   The manufacturing method of Claim 1 whose mixing mass ratio (A / B) of the extract A and the extract B is 1-5. 茶系飲料用抽出液中の非重合体カテキン類の含有量が0.1〜0.5質量%である、請求項1又は2記載の製造方法。   The manufacturing method of Claim 1 or 2 whose content of non-polymer catechins in the extract for tea-based beverages is 0.1 to 0.5% by mass. 請求項1〜3のいずれか1項に記載の製造方法により得られた茶系飲料用抽出液を、そのまま又は希釈して容器内に充填してなる、容器詰茶系飲料。   A container-packed tea-based beverage obtained by filling a tea-based beverage extract obtained by the production method according to any one of claims 1 to 3 directly or diluted into a container.
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