JP6313889B1 - Granulated tea leaves and method for producing the same - Google Patents

Granulated tea leaves and method for producing the same Download PDF

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JP6313889B1
JP6313889B1 JP2017167579A JP2017167579A JP6313889B1 JP 6313889 B1 JP6313889 B1 JP 6313889B1 JP 2017167579 A JP2017167579 A JP 2017167579A JP 2017167579 A JP2017167579 A JP 2017167579A JP 6313889 B1 JP6313889 B1 JP 6313889B1
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倫典 森本
倫典 森本
秀二郎 廣澤
秀二郎 廣澤
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Matsutani Chemical Industries Co Ltd
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Abstract

【課題】本発明の課題は、水に対しても優れた分散性を示す造粒茶葉を提供することである。【解決手段】粉末茶葉を90質量%以上含有させ、且つ造粒茶葉の平均粒子径を80〜180μmに設定することにより、造粒茶葉の水への分散性が向上する。【選択図】なしAn object of the present invention is to provide a granulated tea leaf that exhibits excellent dispersibility in water. Dispersion of granulated tea leaves in water is improved by containing 90% by mass or more of powdered tea leaves and setting the average particle size of the granulated tea leaves to 80 to 180 μm. [Selection figure] None

Description

本発明は、水に対する分散性に優れた造粒茶葉、及び当該造粒茶葉の製造方法に関する。   The present invention relates to a granulated tea leaf excellent in water dispersibility and a method for producing the granulated tea leaf.

通常、飲用の「お茶」とは、茶葉を発酵若しくは発酵させないで乾燥し、これを粉砕若しくは粉砕せずに水、温水若しくは熱水で抽出した抽出液をいうが、抽出残渣を廃棄しなければならないという不便がある。   Usually, “tea” for drinking refers to an extract obtained by drying tea leaves without fermentation or fermentation and extracting them with water, warm water or hot water without crushing or crushing them. There is inconvenience that it must not.

一方、そのような抽出残渣の廃棄を必要としない飲用のお茶として、上記乾燥した茶葉をジェットミル等で平均粒径10μm未満の粉末茶としたものをそのまま熱水に分散させ、茶筅等で撹拌懸濁して飲用するものもある。しかし、このような粉末茶では、平均粒径10μmとするためのコストは非常に高く分散性は非常に低いため、利便性に劣る。   On the other hand, as a drinking tea that does not require the disposal of such extraction residue, the dried tea leaves, which are made into powdered tea with an average particle size of less than 10 μm with a jet mill or the like, are directly dispersed in hot water and stirred with a tea bowl or the like. Some are suspended for drinking. However, such powdered tea is inconvenient because the cost for making the average particle size 10 μm is very high and the dispersibility is very low.

そこで、最近では、粉末茶葉と、賦形剤として単糖、二糖、澱粉分解物等とを混合して顆粒化した粉末茶が主流となってきており、より良い顆粒化粉末茶を得ようと、種々の工夫がされている。   Therefore, recently, powdered tea that has been granulated by mixing powdered tea leaves with monosaccharides, disaccharides, starch degradation products, etc. as excipients has become the mainstream, so let's get better granulated powdered tea Various ideas have been made.

例えば、特許文献1には、賦形粉末と茶粉末よりなる顆粒を核とし、その表面に茶粉末を被覆してなる茶顆粒は、味・色・香りを維持したまま冷水への分散性が良好になることが開示されている。また、特許文献2には、緑茶葉粉末と、緑茶の抽出液とを混合し、これに賦形剤を加えた後、固形分40〜85質量%として真空乾燥することによって、抗酸化性に富み、かつ溶解色が良く、香り、呈味及び溶解性に優れた即席粉末茶が得られることが開示されている。更に、特許文献3には、抗酸化剤を含む水溶液中で、茶葉(a)を粉砕抽出並びに微粒化して水中粉砕茶葉(A)を含む微粒化液を調製する工程、得られた微粒化液に、茶葉(b)を粉砕乃至摩砕して得られた乾式粉砕茶葉(B)と、乾燥助剤とを加えて攪拌混合する工程、及び攪拌混合して得られた混合物を乾燥させる工程とを経ることにより、茶葉含有成分の変質を防ぎ、茶筅を使用せず水に手軽に溶解させることができる分散茶が得られることが開示されている。   For example, Patent Document 1 discloses that a granule comprising a shaped powder and a tea powder as a core and coated with a tea powder on its surface has a dispersibility in cold water while maintaining the taste, color and aroma. It is disclosed to be good. In Patent Document 2, green tea leaf powder and green tea extract are mixed, and after adding an excipient to this, it is vacuum-dried to a solid content of 40 to 85% by mass, thereby making it antioxidant. It is disclosed that an instant powdered tea that is rich and has a good dissolved color and is excellent in aroma, taste and solubility can be obtained. Furthermore, Patent Document 3 discloses a step of preparing a micronized liquid containing ground tea leaves (A) by pulverizing extraction and micronization of tea leaves (a) in an aqueous solution containing an antioxidant, and the resulting micronized liquid A step of adding a dry crushed tea leaf (B) obtained by pulverizing or grinding tea leaves (b) and a drying aid and stirring and mixing, and a step of drying the mixture obtained by stirring and mixing; It is disclosed that a dispersed tea that can be easily dissolved in water without using teacups can be obtained by passing through the above.

また、特許文献4には、気流式粉砕機を用いて5〜15ミクロンとした微粉末茶を流動層造粒コーティング装置により造粒することにより、分散・懸濁性に優れた10〜30ミクロンの粉末茶が得られることが開示されている。更に、特許文献5には、茶葉粉砕物40〜90質量%に賦形剤として難消化デキストリン10〜60質量%を混合して造粒された安息角が45度未満である茶葉顆粒は、水又は熱水へ加えた時にダマにならずに容易に分散し、茶葉の緑色や風味・旨味を安定して保持できることが開示されている。   In Patent Document 4, fine powdered tea having a particle size of 5 to 15 microns is granulated with a fluidized bed granulation coating apparatus using an air-flow type pulverizer, thereby achieving excellent dispersion and suspendability of 10 to 30 microns. It is disclosed that a powdered tea can be obtained. Furthermore, Patent Document 5 discloses that tea leaf granules having an angle of repose of less than 45 degrees, which is granulated by mixing 10 to 60% by mass of an indigestible dextrin as an excipient with 40 to 90% by mass of ground tea leaves, Alternatively, it is disclosed that when added to hot water, it is easily dispersed without becoming lumpy, and the green color, flavor and umami of tea leaves can be stably maintained.

しかし、特許文献1〜3で開示されている顆粒化茶粉末では、多段造粒であったり、造粒工程前に茶抽出工程を採用したりと、製造工程が煩雑であるという欠点がある。また、特許文献4で開示されている粉末茶は分散性の点では満足できるものではなく、更に、特許文献5で開示されている茶葉顆粒は、多量の賦形剤を必要とするために茶本来の風味が損なわれるという欠点がある。   However, the granulated tea powders disclosed in Patent Documents 1 to 3 have a disadvantage that the production process is complicated, such as multistage granulation or the adoption of a tea extraction process before the granulation process. Further, the powdered tea disclosed in Patent Document 4 is not satisfactory in terms of dispersibility, and the tea leaf granule disclosed in Patent Document 5 requires a large amount of excipients, so There is a drawback that the original flavor is impaired.

特開2000−342180号公報JP 2000-342180 A 特開平06−178650号公報Japanese Patent Laid-Open No. 06-178650 特開2007−289115号公報JP 2007-289115 A 特開2006−296341号公報JP 2006-296341 A 特開2010−68741号公報JP 2010-68741 A

本発明の課題は、水に対しても優れた分散性を示す造粒茶葉を提供することにある。   The subject of this invention is providing the granulated tea leaf which shows the outstanding dispersibility also to water.

本発明者らは、かかる課題を解決すべく種々検討したところ、意外にも、粉末茶葉を90質量%以上含有させ、且つ造粒茶葉の平均粒子径を80〜180μmに設定することにより、造粒茶葉の水への分散性が顕著に向上することを見出した。本発明は、かかる知見に基づいて、更に検討を重ねることにより本発明を完成するに至った。   The present inventors have made various studies in order to solve this problem. Surprisingly, the powdered tea leaves are contained in an amount of 90% by mass or more, and the average particle diameter of the granulated tea leaves is set to 80 to 180 μm. It was found that the dispersibility of grain tea leaves in water was significantly improved. The present invention has been completed by further study based on such knowledge.

即ち、本発明は、下記に掲げる態様の発明を提供する。
(1)粉末茶葉を90質量%以上含有し、且つ平均粒子径が80〜180μmである造粒茶葉。
(2)粉末茶葉の平均粒子径が10〜30μmである、(1)に記載の造粒茶葉。
(3)粉末茶葉を90質量%以上含む原料粉末を湿式造粒し、平均粒子径が80〜180μmである造粒茶葉を得る、造粒茶葉の製造方法。
(4)前記湿式造粒が流動層造粒によって行われる、(3)に記載の製造方法。
(5)バインダー液の噴霧条件が、下記式に従って算出される水分上昇速度が1.03〜2.62%/分であり、且つバインダー液の噴霧終了時の造粒茶葉の水分量が24〜35%となるように設定して造粒される、(4)に記載の製造方法。
That is, this invention provides the invention of the aspect hung up below.
(1) Granulated tea leaves containing 90% by mass or more of powdered tea leaves and an average particle diameter of 80 to 180 μm.
(2) The granulated tea leaf according to (1), wherein the average particle size of the powdered tea leaf is 10 to 30 μm.
(3) A method for producing a granulated tea leaf, comprising wet granulating a raw material powder containing 90% by mass or more of powdered tea leaf to obtain a granulated tea leaf having an average particle size of 80 to 180 μm.
(4) The production method according to (3), wherein the wet granulation is performed by fluidized bed granulation.
(5) The condition for spraying the binder liquid is that the water increase rate calculated according to the following formula is 1.03 to 2.62% / min, and the water content of the granulated tea leaves at the end of spraying the binder liquid is 24 to The production method according to (4), wherein the granulation is performed with setting to be 35%.

本発明の造粒茶葉は、水に添加して混合すると、ダマを生じることなく容易に分散させることができる。また、本発明の造粒茶葉は、造粒に賦形剤を殆ど使用しないので、嵩が低く利便性に富んでいることに加え、賦形剤の呈味への悪影響を抑制して茶葉本来の良好な風味を呈することもできる。   When the granulated tea leaves of the present invention are added to water and mixed, they can be easily dispersed without causing lumps. In addition, the granulated tea leaf of the present invention uses almost no excipient for granulation, so that it has a low volume and is convenient, and also has an adverse effect on the taste of the excipient, thereby reducing the original tea leaves. It is also possible to exhibit a good flavor.

実施例1の造粒茶葉を20℃の水に分散させた際の外観(分散性の評価◎)を撮影した写真である。It is the photograph which image | photographed the external appearance (evaluation of dispersibility (double-circle)) at the time of disperse | distributing the granulated tea leaf of Example 1 in 20 degreeC water. 実施例1の造粒茶葉を60℃の水に分散させた際の外観(分散性の評価〇)を撮影した写真である。It is the photograph which image | photographed the external appearance (dispersion evaluation (circle)) at the time of disperse | distributing the granulated tea leaf of Example 1 to 60 degreeC water. 比較例3の造粒茶葉を20℃の水に分散させた際の外観(分散性の評価×)を撮影した写真である。It is the photograph which image | photographed the external appearance (dispersion evaluation x) at the time of disperse | distributing the granulated tea leaf of the comparative example 3 in 20 degreeC water.

本発明の造粒茶葉は、粉末茶葉を90質量%以上含有し、且つ平均粒子径が80〜180μmであることを特徴とする。以下、本発明の造粒茶葉について、詳述する。なお、単に「造粒茶葉」という場合は、最終の乾燥工程を含む一連の造粒を経て得られた製品を指し、「バインダー液(又は水)の噴霧終了時の造粒茶葉」という場合は、一連の造粒において最終乾燥工程を経ていない造粒茶葉を指す。   The granulated tea leaf of the present invention is characterized by containing 90% by mass or more of powdered tea leaf and having an average particle size of 80 to 180 μm. Hereinafter, the granulated tea leaves of the present invention will be described in detail. The term “granulated tea leaf” refers to a product obtained through a series of granulations including the final drying step, and the term “granulated tea leaf at the end of spraying the binder liquid (or water)” This refers to granulated tea leaves that have not undergone the final drying step in a series of granulations.

本発明の造粒茶葉に含まれる粉末茶葉の茶葉の種類については、特に制限されず、例えば、緑茶、大麦若葉、ケール、モロヘイヤ、よもぎ、麦茶、はと麦茶等の茶葉;ウーロン茶等の半発酵茶葉;紅茶等の発酵茶葉等が挙げられる。これらの中でも、好ましくは緑茶茶葉が挙げられる。なお、「抹茶」は、その原料が「碾茶」であって、揉み作業は行われない等、狭義の「粉末茶葉」には含まれないが、本発明において、「粉末茶葉」という用語は、広義の意味で使用しており、「抹茶」を包含する。   The type of tea leaves of the powdered tea leaves contained in the granulated tea leaves of the present invention is not particularly limited, for example, green tea, barley young leaves, kale, morohaya, wormwood, barley tea, hato barley tea, etc .; semi-fermented oolong tea etc. Tea leaves: fermented tea leaves such as black tea. Among these, green tea leaves are preferable. In addition, the term “powdered tea leaves” in the present invention is not included in the narrowly defined “powdered tea leaves”, such as “Matcha”, since the raw material is “boiled tea” and no savory work is performed. Used in a broad sense and includes “matcha”.

粉末茶葉は、前記茶葉、半発酵茶葉、又は発酵茶葉を粉末化することにより得ることができる。当該粉末化の手法については、特に制限されないが、例えば、気流式やミキサー式による粉砕方式による粉末化処理が挙げられる。   Powdered tea leaves can be obtained by pulverizing the tea leaves, semi-fermented tea leaves, or fermented tea leaves. The powdering method is not particularly limited, and examples thereof include a powdering process by an airflow type or a mixer type pulverization method.

粉末茶葉の平均粒子径については、特に制限されないが、例えば、5〜40μmが挙げられる。より一層優れた分散性を備えさせるという観点から、粉末茶葉の平均粒子径として、好ましくは10〜40μm、更に好ましくは20〜30μmが挙げられる。本発明において、「粉末茶葉の平均粒子径」は、レーザー回折・散乱式粒子径分布測定装置を使用して測定されるメジアン径である。   Although it does not restrict | limit especially about the average particle diameter of a powdered tea leaf, For example, 5-40 micrometers is mentioned. From the viewpoint of providing further excellent dispersibility, the average particle diameter of the powdered tea leaves is preferably 10 to 40 μm, more preferably 20 to 30 μm. In the present invention, the “average particle diameter of powdered tea leaves” is a median diameter measured using a laser diffraction / scattering particle size distribution measuring apparatus.

本発明の造粒茶葉における粉末茶葉の含有量は90質量%以上に設定される。このように、粉末茶葉の含有量を高めつつ、造粒茶葉の平均粒子径を後述する所定の範囲に設定することにより、優れた分散性を備えさせることが可能になる。造粒茶葉の嵩を更に低下させつつ、優れた分散性を備えさせるという観点から、本発明の造粒茶葉における粉末茶葉の含有量として、好ましくは95質量%以上、更に好ましくは98質量%以上、より好ましくは99質量%以上、特に好ましくは100質量%が挙げられる。本発明において、粉末茶葉の含有量は、造粒茶葉に不可避的に吸湿又は残存している水の含有量を除いて算出される値である。   The content of the powdered tea leaf in the granulated tea leaf of the present invention is set to 90% by mass or more. Thus, it becomes possible to provide excellent dispersibility by setting the average particle diameter of the granulated tea leaves within a predetermined range described later while increasing the content of the powdered tea leaves. From the viewpoint of providing excellent dispersibility while further reducing the bulk of the granulated tea leaf, the content of the powdered tea leaf in the granulated tea leaf of the present invention is preferably 95% by mass or more, more preferably 98% by mass or more. More preferred is 99% by mass or more, and particularly preferred is 100% by mass. In the present invention, the content of the powdered tea leaf is a value calculated by excluding the content of water inevitably absorbed or remaining in the granulated tea leaf.

本発明の造粒茶葉において、粉末茶葉の含有量が100質量%未満である場合には、賦形剤を含んでいることが好ましい。本発明で使用される賦形剤の種類については、食品に使用可能であることを限度として特に制限されないが、例えば、澱粉分解物、澱粉、糖類及び増粘多糖類等の粘着性素材が挙げられる。これらの賦形剤は、1種単独で使用してもよく、また2種以上を組み合わせて使用してもよい。   The granulated tea leaf of the present invention preferably contains an excipient when the content of the powdered tea leaf is less than 100% by mass. The type of excipient used in the present invention is not particularly limited as long as it can be used in foods, and examples thereof include adhesive materials such as starch degradation products, starch, saccharides and thickening polysaccharides. It is done. These excipients may be used alone or in combination of two or more.

これらの賦形剤の中でも、好ましくは、澱粉分解物が挙げられる。本発明で使用される澱粉分解物のDE(デキストロース当量)については、特に制限されないが、例えばDE8〜25、好ましくはDE8〜18が挙げられる。   Among these excipients, starch decomposition products are preferable. Although it does not restrict | limit especially about DE (dextrose equivalent) of the starch degradation product used by this invention, For example, DE8-25, Preferably DE8-18 is mentioned.

本発明の造粒茶葉において賦形剤を含有させる場合、その含有量としては、10質量%以下、好ましくは0.1〜10質量%、更に好ましくは0.1〜5質量%、特に好ましくは0.1〜2質量%、特に好ましくは0.1〜1質量%が挙げられる。本発明において、賦形剤の含有量は、造粒茶葉に不可避的に吸湿又は残存している水の含有量を除いて算出される値である。   When the granulated tea leaves of the present invention contain an excipient, the content thereof is 10% by mass or less, preferably 0.1 to 10% by mass, more preferably 0.1 to 5% by mass, particularly preferably. 0.1-2 mass%, Most preferably, 0.1-1 mass% is mentioned. In the present invention, the content of the excipient is a value calculated by excluding the content of water inevitably absorbed or remaining in the granulated tea leaves.

本発明の造粒茶葉の平均粒子径は、80〜180μmに設定される。このような平均粒子径を具備しつつ、粉末茶葉の含有量が前述する範囲を充足することによって、水、温水、及び熱水に対して、優れた分散性を備えさせることが可能になる。分散性をより一層向上させるという観点から、本発明の造粒茶葉の平均粒子径として、好ましくは90〜180μm、更に好ましくは95〜180μmが挙げられる。   The average particle diameter of the granulated tea leaves of the present invention is set to 80 to 180 μm. It becomes possible to provide excellent dispersibility with respect to water, hot water, and hot water by satisfying the above-described range of the content of the powdered tea leaves while having such an average particle diameter. From the viewpoint of further improving dispersibility, the average particle size of the granulated tea leaves of the present invention is preferably 90 to 180 μm, more preferably 95 to 180 μm.

本発明において、造粒茶葉の平均粒子径は、篩い分け法によって測定される値である。造粒茶葉の平均粒子径の測定方法は、具体的には、以下に示す通りである。先ず、目開きが53μm、63μm、75μm、106μm、150μm、及び250μmの篩を準備し、目開きが小さいものが下、目開きが大きいものを上になるように積み重ね、最上段の篩に造粒茶葉を載せて蓋をし、振動機にて振動を与える。次いで、各篩残った造粒茶葉の重量を測定する。以下の算出式に従って、平均粒子径(重量ベースの累積50%値)を算出する。
In the present invention, the average particle size of the granulated tea leaves is a value measured by a sieving method. The method for measuring the average particle size of the granulated tea leaves is specifically as follows. First, prepare sieves with 53, 63, 75, 106, 150, and 250 μm openings, and stack them so that the one with the small opening is the bottom and the one with the large opening is the top. Place the brown tea leaves on the lid and apply vibration with a vibrator. Next, the weight of each sieved granulated tea leaf is measured. The average particle diameter (weight-based cumulative 50% value) is calculated according to the following calculation formula.

本発明の造粒茶葉の粒度分布については、前述する平均粒子径を満たす限り、特に制限されないが、造粒茶葉の総重量に対する106μm以上150μm未満の造粒茶葉の重量の比率として、例えば、20%以上、具体的には20%以上35%未満が挙げられる。ここで、「造粒茶葉の総重量に対する75μm以上150μm未満の造粒茶葉の重量の比率」は、前記平均粒子径の測定と同様の条件の篩い分け法によって求められる値である。   The particle size distribution of the granulated tea leaf of the present invention is not particularly limited as long as the average particle size described above is satisfied. As a ratio of the weight of the granulated tea leaf of 106 μm or more and less than 150 μm to the total weight of the granulated tea leaf, for example, 20 % Or more, specifically 20% or more and less than 35%. Here, “the ratio of the weight of the granulated tea leaf of 75 μm or more and less than 150 μm to the total weight of the granulated tea leaf” is a value obtained by a sieving method under the same conditions as the measurement of the average particle diameter.

本発明の造粒茶葉は、粉末茶葉及び必要に応じて添加される賦形剤を含む原料粉末を用いて、前述する平均粒子径に造粒することによって製造される。本発明の造粒茶葉を製造する際の造粒法については、前述する平均粒子径の造粒物が得られることを限度として特に制限されず、湿式造粒法又は乾式造粒法のいずれであってもよいが、好ましくは湿式造粒法が挙げられる。   The granulated tea leaves of the present invention are produced by granulating to the above-mentioned average particle diameter using raw material powder containing powdered tea leaves and excipients added as necessary. The granulation method for producing the granulated tea leaves of the present invention is not particularly limited as long as the above-mentioned granulated product having an average particle diameter can be obtained, and either a wet granulation method or a dry granulation method. Although there may be, wet granulation method is mentioned preferably.

本発明の造粒茶葉を湿式造粒法で製造する場合、流動層造粒、転動式造粒、攪拌造粒、押出造粒等のいずれの造粒法で行ってもよいが、前述する平均粒子径の造粒茶葉を効率的に製造するという観点から、好ましくは流動層造粒法が挙げられる。   When the granulated tea leaf of the present invention is produced by a wet granulation method, it may be performed by any granulation method such as fluidized bed granulation, rolling granulation, stirring granulation, extrusion granulation, etc. From the viewpoint of efficiently producing granulated tea leaves having an average particle size, a fluidized bed granulation method is preferably used.

本発明の造粒茶葉を湿式造粒法で製造する場合、バインダー液として水を使用し、原料粉末(粉末茶葉及び必要に応じて添加される賦形剤を含む原料)に対して噴霧等によって添加すればよい。また、本発明の造粒茶葉に賦形剤を含有させる場合、バインダー液として使用される水には、造粒茶葉に含有させる賦形剤の一部又は全部を溶解又は分散させておいてもよい。バインダー液として使用される水に賦形剤を溶解又は分散させる場合、バインダー液として使用される水における賦形剤の濃度は、例えば、0.1〜20w/v%程度に設定すればよい。   When the granulated tea leaf of the present invention is produced by a wet granulation method, water is used as a binder liquid, and spraying or the like is performed on the raw material powder (a raw material containing powdered tea leaves and excipients added as necessary). What is necessary is just to add. In addition, when the granulated tea leaf of the present invention contains an excipient, a part or all of the excipient contained in the granulated tea leaf may be dissolved or dispersed in the water used as the binder liquid. Good. When the excipient is dissolved or dispersed in the water used as the binder liquid, the concentration of the excipient in the water used as the binder liquid may be set to about 0.1 to 20 w / v%, for example.

本発明の造粒茶葉を湿式造粒法で製造する場合、湿式造粒の条件については、前述する平均粒子径の造粒物が得られることを限度として特に制限されないが、例えば、流動層造粒法の場合であれば、下記式に従って算出される水分上昇速度が、1.03〜2.62%/分、好ましくは1.36〜2.62%/分、更に好ましくは1.66〜2.62%/分となり、且つバインダー液の噴霧終了時の造粒茶葉の水分量が24〜35%、好ましくは26〜35%、更に好ましくは30〜34%となるように、バインダー液の噴霧条件を制御することによって、前述する平均粒子径の造粒物を効率的に製造することができる。
When the granulated tea leaves of the present invention are produced by a wet granulation method, the wet granulation conditions are not particularly limited as long as the above-mentioned granulated product having an average particle diameter is obtained. In the case of the grain method, the rate of water increase calculated according to the following formula is 1.03 to 2.62% / min, preferably 1.36 to 2.62% / min, and more preferably 1.66 to The content of the binder liquid is 2.62% / min, and the water content of the granulated tea leaves at the end of spraying of the binder liquid is 24 to 35%, preferably 26 to 35%, and more preferably 30 to 34%. By controlling the spraying conditions, the above-mentioned granulated product having an average particle diameter can be efficiently produced.

なお、前記「造粒茶葉の水分量」及び「原料粉末の水分量」は、赤外線水分計を用いて設定温度105℃で測定される値である。また、前記「バインダー液の噴霧時間」は、バインダー液の噴霧開始から所定量のバインダー液の噴霧が終了までに要する時間であり、バインダー液の噴霧時間内で、持続的にバインダー液の噴霧を行ってもよく、また断続的にバインダー液の噴霧を行ってもよい。断続的にバインダー液の噴霧を行う態様としては、例えば、バインダー液の噴霧、停止、払い落し、停止を1サイクルとして、当該サイクルを繰り返し行う態様が挙げられる。断続的にバインダー液の噴霧を行う場合には、前記「バインダー液の噴霧時間」には、前記停止及び払い落しに要する時間も包含される。   The “moisture content of the granulated tea leaf” and the “moisture content of the raw material powder” are values measured at a set temperature of 105 ° C. using an infrared moisture meter. The “binder liquid spraying time” is the time required from the start of spraying the binder liquid to the end of spraying a predetermined amount of the binder liquid, and the spraying of the binder liquid is continuously performed within the spraying time of the binder liquid. Alternatively, the binder liquid may be sprayed intermittently. As an aspect which sprays a binder liquid intermittently, the aspect which repeats the said cycle by making spraying of a binder liquid, stop, wiping off, and stopping into 1 cycle is mentioned, for example. In the case where the binder liquid is sprayed intermittently, the “binder liquid spraying time” includes the time required for the stop and removal.

流動層造粒法において、水分上昇速度及び噴霧終了時の造粒茶葉の水分量が前記範囲となるように、バインダー液の噴霧条件を調整するには、原料粉末に対するバインダー液の噴霧量、バインダー液の噴霧速度、及び造粒機内への給気温度等を適宜制御すればよい。具体的には、造粒機内への給気温度を20〜40℃の範囲に設定する場合であれば、原料粉末100質量部当たり、使用(噴霧)するバインダー液量を30〜80質量部、好ましくは40〜80質量部、更に好ましくは50〜70質量部の範囲内で適宜設定し、且つ原料粉末1kg当たりのバインダー液の噴霧速度を4.8〜63ml/分の範囲内で適宜設定すればよい。ここで、原料粉末1kg当たりのバインダー液の噴霧速度とは、湿式造粒装置内に供給される水の噴霧速度を、湿式造粒に供される原料粉末の重量(Kg)で除した値を指す。   In the fluidized bed granulation method, in order to adjust the spray condition of the binder liquid so that the moisture increase rate and the moisture content of the granulated tea leaf at the end of spraying are within the above ranges, the spray amount of the binder liquid on the raw material powder, the binder What is necessary is just to control the spraying speed of a liquid, the supply temperature to the inside of a granulator, etc. suitably. Specifically, if the supply temperature into the granulator is set in the range of 20 to 40 ° C., the amount of binder liquid to be used (sprayed) per 100 parts by mass of the raw material powder is 30 to 80 parts by mass, Preferably, it is appropriately set within the range of 40 to 80 parts by mass, more preferably within the range of 50 to 70 parts by mass, and the spray rate of the binder liquid per 1 kg of the raw material powder is appropriately set within the range of 4.8 to 63 ml / min. That's fine. Here, the spray rate of the binder liquid per 1 kg of the raw material powder is a value obtained by dividing the spray rate of the water supplied into the wet granulator by the weight (Kg) of the raw material powder used for the wet granulation. Point to.

なお、造粒茶葉の風味を維持させる上で、造粒機内への給気温度は20〜40℃の範囲に設定することが望ましい。但し、造粒機内への給気温度を20℃未満に設定する場合であれば、バインダー液の噴霧速度を前記範囲よりも低くする、及び/又は原料粉末100質量部当たりのバインダー液量を前記範囲よりも減らす、等によって、水分上昇速度及び噴霧終了時の造粒茶葉の水分量が前記範囲を満たすように調整することができる。また、造粒機内への給気温度を40℃超に設定する場合であれば、バインダー液の噴霧速度を前記範囲よりも高くする、及び/又は原料粉末100質量部当たりのバインダー液量を前記範囲よりも増やす、等によって、水分上昇速度及び噴霧終了時の造粒茶葉の水分量が前記範囲を満たすように調整することができる。また、水分上昇速度及び噴霧終了時の造粒茶葉の水分量は、使用する流動層造粒機の大きさ、原料粉末の量等によって影響を受けるので、使用する流動層造粒機の大きさ、原料粉末の量等を踏まえた上で、原料粉末に対するバインダー液の噴霧量、バインダー液の噴霧速度、及び造粒機内への給気温度等を、前記範囲を参考にして適宜設定すればよい。   In addition, when maintaining the flavor of granulated tea leaves, it is desirable to set the temperature of the air supplied to the granulator within a range of 20 to 40 ° C. However, if the air supply temperature into the granulator is set to less than 20 ° C., the spray rate of the binder liquid is made lower than the above range, and / or the binder liquid amount per 100 parts by mass of the raw material powder is By reducing the amount from the range, etc., it is possible to adjust the water rising rate and the water content of the granulated tea leaf at the end of spraying to satisfy the above range. Further, if the supply temperature into the granulator is set to more than 40 ° C., the spray rate of the binder liquid is made higher than the above range, and / or the binder liquid amount per 100 parts by mass of the raw material powder is It can be adjusted so that the moisture increase rate and the moisture content of the granulated tea leaf at the end of spraying satisfy the above range by increasing the range or the like. Also, the rate of moisture rise and the amount of water in the granulated tea leaves at the end of spraying are affected by the size of the fluidized bed granulator used, the amount of raw material powder, etc., so the size of the fluidized bed granulator used Based on the amount of the raw material powder, the amount of the binder liquid sprayed on the raw material powder, the spray rate of the binder liquid, the supply temperature into the granulator, etc. may be set appropriately with reference to the above range. .

流動層造粒法において、前記条件でバインダー液の噴霧が完了した後に、流動層造粒機内で所望の水分含量になるまで引き続き乾燥を行うことにより、本発明の造粒茶葉が得られる。   In the fluidized bed granulation method, after spraying of the binder liquid is completed under the above conditions, the granulated tea leaf of the present invention is obtained by continuously drying in the fluidized bed granulator until a desired water content is obtained.

造粒によって得られた造粒茶葉は、必要に応じて、整粒等を行い、粒子径を調節してもよい。   The granulated tea leaves obtained by granulation may be adjusted in size and the particle diameter may be adjusted as necessary.

以下、本発明の実施例について詳述するが、本発明はこれらに限定されるものではない。   Examples of the present invention will be described in detail below, but the present invention is not limited thereto.

試験例1
1.造粒茶葉の製造
まず、国産碾茶微粉末(以下、「原料抹茶」という)2kgを5型流動層造粒機(フローコーター、フロイント産業社)に投入し、排気ファンから吸引した20℃エアーを底部より吹き込み流動させた。次に、原料抹茶に対して80℃の水(バインダー液)1000mlを噴霧して造粒し、噴霧終了後に給気温度100℃及び30分の条件で引き続き乾燥を行うことにより、造粒茶葉を得た。なお、使用した原料抹茶の平均粒子径、水の噴霧速度、水の噴霧時間は、以下の表1の通りである。水の噴霧は、「40秒噴霧+1秒停止+10秒払い落し+1秒停止」を1サイクルとして、当該サイクルを繰り返すことにより断続的に行った。また、原料抹茶の平均粒子径は、レーザー回折・散乱式粒子径分布測定装置(MT3000、日機装製)を使用して測定したメジアン径である。
Test example 1
1. Manufacture of granulated tea leaves First, 2 kg of domestically produced tea tea powder (hereinafter referred to as “raw green tea”) is put into a type 5 fluidized bed granulator (flow coater, Freund Sangyo Co., Ltd.), and 20 ° C. air sucked from an exhaust fan It was made to flow by blowing from the bottom. Next, 1000 ml of 80 ° C. water (binder liquid) is sprayed on the raw material matcha tea and granulated, and after the spraying is completed, drying is continued under the conditions of a supply air temperature of 100 ° C. and 30 minutes, whereby the granulated tea leaves are obtained. Obtained. In addition, the average particle diameter of the raw material matcha used, the spray speed of water, and the spray time of water are as shown in Table 1 below. Water spraying was performed intermittently by repeating the cycle with “40 seconds spray + 1 second stop + 10 seconds wiped off + 1 second stop” as one cycle. The average particle diameter of the raw material matcha is a median diameter measured using a laser diffraction / scattering particle size distribution measuring device (MT3000, manufactured by Nikkiso).

また、水の噴霧前の原料抹茶及び噴霧終了時の造粒茶葉をサンプリングし、赤外線水分計(「FD−610」、ケツト科学研究所株式会社製)を用いて設定温度105℃で水分量の測定を行った。得られた各水分量の値を用いて、前記算出式に従って、水分上昇率を算出した。結果を表1に示す。   In addition, the raw material matcha before spraying water and the granulated tea leaves at the end of spraying are sampled, and the moisture content is measured at a set temperature of 105 ° C. using an infrared moisture meter (“FD-610”, manufactured by Kett Science Laboratory Co., Ltd.). Measurements were made. The water increase rate was calculated according to the calculation formula using the obtained water content values. The results are shown in Table 1.

2.造粒茶葉の平均粒子径及び粒度分布の測定
目開きが53μm、63μm、75μm、106μm、150μm、250μmの篩を細かいものから順に上に載せて6段に積み、最上段の篩に、造粒茶葉を20g投入して蓋をし、振動機(IIDA SIEVE SHAKER 飯田製作所製)にて10分間、蓋上部より衝撃を加えて振動させ、各篩上に存在する造粒茶葉の重量を測定し、測定に供した造粒茶葉に対する各篩上の造粒茶葉の重量割合(分布割合(%))を算出した。また、前述の算出式に従って、平均粒子径を求めた。得られた結果を表2に示す。
2. Measurement of average particle size and particle size distribution of granulated tea leaves Screens with 53, 63, 75, 106, 150, and 250 μm openings are placed in order from the finest and stacked in six stages, and granulated on the uppermost sieve. 20g of tea leaves were put in, covered, and shaken with a vibrator (IIDA SIEVE SHAKER Iida Seisakusho) for 10 minutes from the top of the lid to vibrate, and the weight of the granulated tea leaves present on each sieve was measured. The weight ratio (distribution ratio (%)) of the granulated tea leaves on each sieve to the granulated tea leaves subjected to the measurement was calculated. Moreover, the average particle diameter was calculated | required according to the above-mentioned calculation formula. The obtained results are shown in Table 2.

3.造粒茶葉の分散性評価
20℃及び60℃の水100mlに造粒茶葉0.5gを撹拌しながら加え、10秒間攪拌後、懸濁液の分散性を目視で観察し、下記判定基準に従って分散性を評価した。
(分散性の判定基準)
◎:ダマが発生しない
〇:発生するダマの数が10個未満
×:発生するダマの数が10個以上
なお、5mm以上の塊を「ダマ」とした。
3. Evaluation of dispersibility of granulated tea leaves Add 0.5 g of granulated tea leaves to 100 ml of water at 20 ° C. and 60 ° C. with stirring, and after stirring for 10 seconds, visually observe the dispersibility of the suspension and disperse according to the following criteria. Sex was evaluated.
(Distribution criteria)
A: Dama does not occur. O: Number of generated lumps is less than 10. X: Number of generated lumps is 10 or more. A lump of 5 mm or more is defined as “dama”.

得られた結果を表3に示す。また、参考のため、実施例1の造粒茶葉を20℃の水に分散させた際の外観(分散性の評価◎)を撮影した写真を図1、実施例1の造粒茶葉を60℃の水に分散させた際の外観(分散性の評価〇)を撮影した写真を図2、比較例3の造粒茶葉を20℃の水に分散させた際の外観(分散性の評価×)を撮影した写真を図3に示す。   The obtained results are shown in Table 3. For reference, the photograph of the appearance (evaluation of dispersibility) when the granulated tea leaves of Example 1 are dispersed in 20 ° C. water is shown in FIG. 1, and the granulated tea leaves of Example 1 are 60 ° C. A photograph of the appearance (dispersibility evaluation 0) taken when dispersed in water of FIG. 2 and the appearance when the granulated tea leaves of Comparative Example 3 are dispersed in water at 20 ° C. (dispersibility evaluation ×). The photograph which image | photographed is shown in FIG.

この結果から、平均粒子径が80〜180μmを満たす造粒茶葉(実施例1〜5)は、20℃及び60℃の双方の水に対して、優れた分散性を示すことが確認された。   From this result, it was confirmed that the granulated tea leaves (Examples 1 to 5) having an average particle diameter of 80 to 180 μm exhibit excellent dispersibility in both 20 ° C. and 60 ° C. water.

試験例2
1.造粒茶葉の製造
まず、国産碾茶微粉末(以下、「原料抹茶」という)2kgを5型流動層造粒機(フローコーター、フロイント産業社)に投入し、排気ファンから吸引した20℃エアーを底部より吹き込み流動させた。次に、原料抹茶に対して80℃の水(バインダー液)を噴霧して造粒し、噴霧終了後に給気温度100℃及び30分の条件で引き続き乾燥を行うことにより、造粒茶葉を得た。なお、使用した原料抹茶の平均粒子径、噴霧した水の量、水の噴霧速度、水の噴霧時間は、以下の表4の通りである。水の噴霧は、「40秒噴霧+1秒停止+10秒払い落し+1秒停止」を1サイクルとして、当該サイクルを繰り返すことにより断続的に行った。また、原料抹茶の平均粒子径は、レーザー回折・散乱式粒子径分布測定装置(MT3000、日機装製)を使用して測定したメジアン径である。また、水の噴霧前の原料抹茶及び噴霧終了時の造粒茶葉をサンプリングし、赤外線水分計(「FD−610」、ケツト科学研究所株式会社製)を用いて設定温度105℃で水分量の測定を行った。得られた各水分量の値を用いて、前記算出式に従って、水分上昇率を算出した。
Test example 2
1. Manufacture of granulated tea leaves First, 2 kg of domestically produced tea tea powder (hereinafter referred to as “raw green tea”) is put into a type 5 fluidized bed granulator (flow coater, Freund Sangyo Co., Ltd.), and 20 ° C. air sucked from an exhaust fan It was made to flow by blowing from the bottom. Next, granulated tea leaves are obtained by spraying water (binder liquid) at 80 ° C. to the raw material matcha tea, followed by drying at the supply temperature of 100 ° C. and 30 minutes after the spraying is completed. It was. In addition, the average particle diameter of the raw material matcha used, the amount of sprayed water, the spray speed of water, and the spray time of water are as shown in Table 4 below. Water spraying was performed intermittently by repeating the cycle with “40 seconds spray + 1 second stop + 10 seconds wiped off + 1 second stop” as one cycle. The average particle diameter of the raw material matcha is a median diameter measured using a laser diffraction / scattering particle size distribution measuring device (MT3000, manufactured by Nikkiso). In addition, the raw material matcha before spraying water and the granulated tea leaves at the end of spraying are sampled, and the moisture content is measured at a set temperature of 105 ° C. using an infrared moisture meter (“FD-610”, manufactured by Kett Science Laboratory Co., Ltd.). Measurements were made. The water increase rate was calculated according to the calculation formula using the obtained water content values.

2.造粒茶葉の平均粒子径及び分散性の評価
得られた造粒茶葉について前記試験例1と同条件で平均粒子径及び分散性の評価を行った。結果を表5に示す。その結果、実施例1、6、7、8、及び9は、平均粒子径が80〜180μmを満し、20℃及び60℃の双方の水に対して、優れた分散性を示すことが確認された。一方、比較例5は、平均粒子径が80μm未満であり、分散性が悪かった。なお、比較例6は、水噴霧終了時の水分量が36.1%と高く、製造時に流動不良が発生して造粒茶葉を製造することができなかった。
2. Evaluation of average particle diameter and dispersibility of granulated tea leaves The obtained granulated tea leaves were evaluated for average particle diameter and dispersibility under the same conditions as in Test Example 1. The results are shown in Table 5. As a result, it was confirmed that Examples 1, 6, 7, 8, and 9 had an average particle diameter of 80 to 180 μm and exhibited excellent dispersibility in both 20 ° C. and 60 ° C. water. It was done. On the other hand, Comparative Example 5 had an average particle size of less than 80 μm and poor dispersibility. In Comparative Example 6, the amount of water at the end of water spraying was as high as 36.1%, and flow failure occurred during production, making it impossible to produce granulated tea leaves.

試験例3
1.造粒茶葉の製造
表6に示す割合で国産碾茶微粉末(以下、「原料抹茶」という)と賦形剤(粉飴(澱粉分解物)、DE25、松谷化学工業株式会社製「MPD」)を混合した原料粉末2Kgを5型流動層造粒機(フローコーター、フロイント産業社)に投入し、排気ファンから吸引した20℃のエアーを底部より吹き込み流動させた。次に、原料粉末に対して80℃の水1000mlを噴霧して造粒し、噴霧終了後に給気温度100℃及び30分の条件で引き続き乾燥を行うことにより、造粒茶葉を得た。なお、使用した原料抹茶の平均粒子径、水の噴霧速度、水の噴霧時間は、以下の表6の通りである。水の噴霧は、「40秒噴霧+1秒停止+10秒払い落し+1秒停止」を1サイクルとして、当該サイクルを繰り返すことにより断続的に行った。また、原料抹茶の平均粒子径は、レーザー回折・散乱式粒子径分布測定装置(MT3000、日機装製)を使用して測定したメジアン径である。また、原料抹茶の平均粒子径は、レーザー回折・散乱式粒子径分布測定装置(MT3000、日機装製)を使用して測定したメジアン径である。また、水の噴霧前の原料粉末及び噴霧終了時の造粒茶葉(比較例7の場合は原料粉末)をサンプリングし、赤外線水分計(「FD−610」、ケツト科学研究所株式会社製)を用いて設定温度105℃で水分量の測定を行った。得られた各水分量の値を用いて、前記算出式に従って、水分上昇率を算出した。
Test example 3
1. Manufacture of granulated tea leaves Domestic tea tea powder (hereinafter referred to as “raw green tea”) and excipients (powder cake (starch degradation product), DE25, “MPD” manufactured by Matsutani Chemical Co., Ltd.) at the ratios shown in Table 6 2 kg of the mixed raw material powder was put into a type 5 fluidized bed granulator (flow coater, Freund Sangyo Co., Ltd.), and 20 ° C. air sucked from an exhaust fan was blown from the bottom to flow. Next, 1000 ml of 80 ° C. water was sprayed on the raw material powder for granulation, and after the spraying was completed, drying was continued under conditions of an air supply temperature of 100 ° C. and 30 minutes to obtain granulated tea leaves. In addition, the average particle diameter of the raw material matcha used, the spraying speed of water, and the spraying time of water are as shown in Table 6 below. Water spraying was performed intermittently by repeating the cycle with “40 seconds spray + 1 second stop + 10 seconds wiped off + 1 second stop” as one cycle. The average particle diameter of the raw material matcha is a median diameter measured using a laser diffraction / scattering particle size distribution measuring device (MT3000, manufactured by Nikkiso). The average particle diameter of the raw material matcha is a median diameter measured using a laser diffraction / scattering particle size distribution measuring device (MT3000, manufactured by Nikkiso). In addition, the raw material powder before spraying water and the granulated tea leaves at the end of spraying (in the case of Comparative Example 7) are sampled, and an infrared moisture meter (“FD-610”, manufactured by Kett Science Laboratory Co., Ltd.) is used. The moisture content was measured at a set temperature of 105 ° C. The water increase rate was calculated according to the calculation formula using the obtained water content values.

実施例1及び10では、製造時にトラブルを生じさせることなく造粒茶葉が得られたが、比較例7では、賦形剤の割合が多く、原料抹茶の割合が少なかったために、製造時に流動不良が発生した。そこで、以下に示す平均粒子径の測定、並びに分散性評価は、実施例1及び10の造粒茶葉を用いて行った。   In Examples 1 and 10, granulated tea leaves were obtained without causing trouble during production, but in Comparative Example 7, the proportion of excipients was large and the proportion of raw material matcha was small, so poor flow during production. There has occurred. Therefore, measurement of the average particle diameter and evaluation of dispersibility shown below were performed using the granulated tea leaves of Examples 1 and 10.

2.造粒茶葉の平均粒子径及び分散性の評価
得られた造粒茶葉について前記試験例1と同条件で平均粒子径及び分散性の評価を行った。結果を表7に示す。その結果、賦形剤を10質量%含んでいても、平均粒子径が80〜180μmを満たす造粒茶葉は、良好な分散性を有していることが確認された。
2. Evaluation of average particle diameter and dispersibility of granulated tea leaves The obtained granulated tea leaves were evaluated for average particle diameter and dispersibility under the same conditions as in Test Example 1. The results are shown in Table 7. As a result, it was confirmed that the granulated tea leaves having an average particle diameter of 80 to 180 μm have good dispersibility even when containing 10% by mass of the excipient.

Claims (3)

緑茶の粉末茶葉を90質量%以上含有し、且つ平均粒子径が80〜180μmである造粒茶葉。   Granulated tea leaves containing 90% by mass or more of green tea powder tea leaves and an average particle size of 80 to 180 μm. 緑茶の粉末茶葉の平均粒子径が10〜30μmである、請求項1に記載の造粒茶葉。   The granulated tea leaf according to claim 1, wherein the average particle size of the green tea powder tea leaf is 10 to 30 µm. 造粒茶葉の製造方法であって、
緑茶の粉末茶葉を90質量%以上含む原料粉末を湿式造粒し、平均粒子径が80〜180μmである造粒茶葉を得る工程を有し、
前記湿式造粒が流動層造粒によって行われ、
バインダー液の噴霧条件が、下記式に従って算出される水分上昇速度が1.03〜2.62%/分であり、且つバインダー液の噴霧終了時の造粒茶葉の水分量が24〜35%となるように設定して造粒される、製造方法。


A method for producing granulated tea leaves, comprising:
Wet granulating a raw material powder containing 90% by mass or more of green tea powder tea leaves, and obtaining a granulated tea leaf having an average particle size of 80 to 180 μm ,
The wet granulation is performed by fluidized bed granulation,
The spray condition of the binder liquid is such that the rate of water rise calculated according to the following formula is 1.03 to 2.62% / min, and the water content of the granulated tea leaves at the end of spraying the binder liquid is 24 to 35%. The manufacturing method which is set and granulated.


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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2020065550A (en) * 2018-10-25 2020-04-30 アモーレパシフィック コーポレーションAmorepacific Corporation Processed products of tea with quick dispersibility in water and method for manufacturing processed products of tea
CN112401012A (en) * 2019-08-21 2021-02-26 株式会社爱茉莉太平洋 Tea processed product and method for producing the same

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2019201629A (en) * 2018-05-17 2019-11-28 大正製薬株式会社 Solid material
JP6621125B1 (en) * 2019-06-24 2019-12-18 佐藤食品工業株式会社 Granulated powder tea leaves and method for producing the same
JP2021145676A (en) * 2020-03-18 2021-09-27 アモーレパシフィック コーポレーションAmorepacific Corporation Processed product of tea in particle form

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2006121930A (en) * 2004-10-27 2006-05-18 Q'sai Co Ltd Plant powder and method for producing the same
JP2010068741A (en) * 2008-09-17 2010-04-02 Ito En Ltd Tea leaf granule and method for producing tea leaf granule

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2006121930A (en) * 2004-10-27 2006-05-18 Q'sai Co Ltd Plant powder and method for producing the same
JP2010068741A (en) * 2008-09-17 2010-04-02 Ito En Ltd Tea leaf granule and method for producing tea leaf granule

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2020065550A (en) * 2018-10-25 2020-04-30 アモーレパシフィック コーポレーションAmorepacific Corporation Processed products of tea with quick dispersibility in water and method for manufacturing processed products of tea
CN111096373A (en) * 2018-10-25 2020-05-05 株式会社爱茉莉太平洋 Processed product of tea having rapid dispersibility in water and method for preparing processed product of tea
JP7304266B2 (en) 2018-10-25 2023-07-06 アモーレパシフィック コーポレーション Processed tea product that quickly disperses in water and method for producing processed tea product
CN112401012A (en) * 2019-08-21 2021-02-26 株式会社爱茉莉太平洋 Tea processed product and method for producing the same

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