TW201215327A - Process for the production of extract of teas - Google Patents

Process for the production of extract of teas Download PDF

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TW201215327A
TW201215327A TW100100016A TW100100016A TW201215327A TW 201215327 A TW201215327 A TW 201215327A TW 100100016 A TW100100016 A TW 100100016A TW 100100016 A TW100100016 A TW 100100016A TW 201215327 A TW201215327 A TW 201215327A
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Taiwan
Prior art keywords
tea
enzyme
extract
protease
product
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TW100100016A
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Chinese (zh)
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TWI405541B (en
Inventor
Feng-Lei Chen
Rie Kawaguchi
Haruka Kino
Saemi Kato
Kazutane Nagano
Koji Murai
Rei Fujita
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Hasegawa T Co Ltd
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    • AHUMAN NECESSITIES
    • A23FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23FCOFFEE; TEA; THEIR SUBSTITUTES; MANUFACTURE, PREPARATION, OR INFUSION THEREOF
    • A23F3/00Tea; Tea substitutes; Preparations thereof
    • A23F3/06Treating tea before extraction; Preparations produced thereby
    • A23F3/08Oxidation; Fermentation
    • A23F3/10Fermentation with addition of microorganisms or enzymes
    • AHUMAN NECESSITIES
    • A23FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23FCOFFEE; TEA; THEIR SUBSTITUTES; MANUFACTURE, PREPARATION, OR INFUSION THEREOF
    • A23F3/00Tea; Tea substitutes; Preparations thereof
    • A23F3/16Tea extraction; Tea extracts; Treating tea extract; Making instant tea
    • A23F3/18Extraction of water soluble tea constituents

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  • Life Sciences & Earth Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Biotechnology (AREA)
  • Chemical & Material Sciences (AREA)
  • Food Science & Technology (AREA)
  • Polymers & Plastics (AREA)
  • Microbiology (AREA)
  • Tea And Coffee (AREA)

Abstract

The present invention provides a process for the production of extract of teas comprising the following steps: adding a protease, a tannic acid and an enzyme preparation having more than 20000 U/g of polygalacturonase activity to teas materials and performing an extraction treatment afterwards. According to the process of the present invention, the method can extract cell wall compounds from teas which can not be decomposed and extracted totally in a well-known enzyme treatment extraction. Further, the method is capable of bringing with decomposing cell wall compounds, and the extractable protein is further decomposed into amino acid. The result of the method of the present invention is that the extract of teas having amino acid-rich compounds, sweetness-rich, strong and good flavor can be obtained with high yield.

Description

201215327 六、發明說明: 【發明所屬之技術領域】 本發明係關於以高產率從茶葉製造甘味、濃味及鮮味 強、澀味少的茶類萃取物的方法。 【先前技術】 近年來’茶類飮料已以充塡於罐子或寶特瓶等的商品 方式提供,由於消費者離棄甜味而獲得高度支持,其生產 量不斷地增加。最近的傾向爲,鮮味或濃味強、澀味受抑 制的茶類飲料受到歡迎。 茶類萃取物製造時,利用酵素劑進行處理的方法已有 人提出例如:倂用原果膠酶與纖維素酶萃取茶葉的方法( 參照專利文獻1 )、將紅茶葉以單寧酶處理的方法(參照專 利文獻2)、以果膠酶、減粉酶及多酌氧化酶處理的方法( 參照專利文獻3)、使含浸於澱粉酶或蛋白酶或纖維素酶或 該等的混合酵素的水溶液並使乾燥再於1〇〇至170 〇c進行 加熱焙煎的穀茶的製造法(參照專利文獻4 )、利用黏著性 澱粉與選自(X-或β-澱粉酶、纖維素酶及蛋白酶當中至少1 種的酵素的混合物萃取的速溶茶的製法(參照專利文獻5) 、將紅糸的葉片以單寧酶及至少1種細胞壁消化酵素濕潤 的方法(參照專利文獻6)、將茶葉萃取殘渣以纖維素酶及 蛋白酶處理的方法(參照專利文獻7)、將茶類的熱水萃取 液預先以單寧酶處理後進行冷凍濃縮的方法(參照專利文 獻8)、使綠原酸酯酶作用於茶萃取液而製造少混濁的茶類 飮料的方法(參照專利文獻9)、將茶類原料於蛋白酶及單 201215327 寧酶存在下進行萃取的茶類萃取物的製造方法(參照專利 文獻10)、使用至少含有纖維素酿、半纖維素酶、果膠酶 及原果膠酶的酵素群將茶葉進行酵素分解萃取處理的茶葉 萃取液的製造方法(參照專利文獻n)、將茶葉於蛋白酶存 在下以水萃取並將獲得的萃取液進一步以蛋白酶處理的茶 類萃取物的萃取方法(參照專利文獻12)、於茶類原料萃取 時及/或萃取後使用葡萄糖濺粉酶、半纖維素酶、果膠酶 、聚甘露糖酶·、轉化酶或α-半乳糖苷酶等糖類分解酵素進 行酵素分解處理的茶類萃取物的製造方法(參照專利文獻 13)、使用鮮紅密孔菌(Pycn〇p〇rus C〇CCineUS)產生酵素及 纖維素酶、半纖維素酶、果膠酶或原果膠酶將茶類原料進 行酵素分解萃取處理的茶類萃取物的製造方法(參照專利 文獻14)等。 但是該等方法,目的爲達成改善甘味、濃味、鮮味等 呈味且提高產率,雖得出相應的成果,但是於茶的萃取殘 渣中仍然還殘存有細胞壁或蛋白質等有用成分,此等還算 不上已有效利用。 〔先前技術文獻〕 (發明專利文獻) 專利文獻1 :日本專利特公昭4 6 - 1 7 9 5 8號公報 專利文獻2 :日本專利特公昭5 2 - 4 2 8 7 7 專利文獻3 :日本專利特公昭62- 1 5 1 7 5號公報 專利文獻4 :日本專利特開昭57-47465號公報 專利文獻5 :日本專利特公平1 -479 79號公報 201215327 專利文獻6:日本專利特公平4-63662號公報 專利文獻7 :日本專利第3 1 5 7 5 3 9號公報 專利文獻8 :日本專利特開平5 - 3 2 8 9 0 1號公報 專利文獻9 :日本專利特開平1 1 - 3 0 8 9 6 5號公報 專利文獻1 〇 :日本專利特開2 0 0 3 - 1 4 4 0 4 9號公報 專利文獻1 1 :日本專利特開2 0 0 3 - 2 1 Ο 1 1 0號公報 專利文獻12:日本專利特開2008-67631號公報 專利文獻1 3 :日本專利特開2 0 0 8 - 8 6 2 8 0號公報 專利文獻14:日本專利特開2008-125477號公報 【發明內容】 〔所欲解決之技術問題〕 本發明的目的爲:提供一種茶類萃取物之製造方法, 可以萃取以往對於茶葉進行的酵素處理萃取中無法完全分 解、萃取的來自於茶葉的細胞壁成分,且可將伴隨細胞壁 成分分解而變得能萃取的蛋白質進一步分解成胺基酸,其 結果能以高產率獲得富含胺基酸成分且富有甘味、濃味及 鮮味且澀味少的茶類萃取物。 〔解決問題之技術方法〕 茶葉中約含有2 5 %的蛋白質(5訂食品成分表),預想 若將該蛋白質以蛋白酶分解則能得到鮮味強烈的茶類萃取 物。但是’僅以蛋白酶對茶葉作用,仍無法見到有此多量 程度的胺基酸游離。本案申請人,於以前的硏究中,推測 是不是氽葉中的蛋白質與單寧結合的原故而努力硏究,結 果發現藉由將余類原料於蛋白酶及單寧酶存在下進行萃取 201215327 ,可獲得鮮味及濃味強'澀味少的茶類萃取物,並已在先 前提申(參照前掲專利文獻1〇)。 但是,明瞭到:即使實施專利文獻1 〇記載的方法, 萃取後的茶葉中仍會殘存相當量未萃取出來的細胞壁成分 及蛋白質。然而’本案發明人等爲了將該未萃取出而殘存 的細胞壁成分及蛋白質有效利用進行硏究,結果發現:果 膠酶當中尤其是聚半乳糖醛酸酶會將茶葉的細胞組織以良 好效率分解。爲了將茶葉中的蛋白質分解而使可溶性固體 成分增加,通常認爲增加所添加的聚半乳糖醛酸酶的活性 單位即可。然而,市售大部分的果膠酶,聚半乳糖醛酸酶 的活性單位沒有如此高,以通常添加量(對於茶葉約0.1 至2質量%)時的效果小,又,若添加暈多,則來自於酵素 製劑的賦形劑或酵素的蛋白質,會使準得的茶類萃取物的 味道變淡,對於茶賦予異質的不自然的甘味,或生出雜味 等對於呈味造成壞影響。 所以,本案發明人等爲了解決該問題進一步努力硏究 ,結果這次意外發現:在茶葉當中除了蛋白酶及單寧酶以 外,更將具有20000U/g以上的聚半乳糖醛酸酶活性的酵 素製劑,以對於茶葉1克的聚半乳糖醛酸酶活性成爲 800U以上的量進行添加並萃取’則從茶葉而來的可溶性 固體成分產率飛躍地提高,且大量生成半乳糖醛酸,而且 胺基酸產率也提高,獲得的萃取物富有甘味、濃味及鮮味 其 法 方 造 製 之 物 取 萃 類 茶 C3B 種 1 供 提 明 。 發 明本 發, 本之 成言 完綜 乃 .201215327 特徵爲對於茶類原料添加(A)蛋白酶、(B)單寧酶、及(c) 具有20000U/g以上的聚半乳糖醛酸酶活性的酵素製劑並 萃取處理。 〔發明之功效〕 利用本發明的方法’係將作爲原料使用的茶類原料的 約40質量%至約80質量%變換爲可溶性固體成分,能大 幅提高從茶類原料而來的萃取物的產率,且獲得的茶類萃 取物含有多量半乳糖醛酸。又,能使從茶類原料而來的胺 基酸產率也提高。而且,依照本發明的方法獲得的茶類萃 取物富含甘味、濃味及鮮味,藉由添加在茶類飲料等,能 對於茶類飲料等賦予甘味、濃味及鮮味,或者增強茶類飮 料等的甘味、濃味及鮮味。又,本發明的方法中,由於伴 隨著茶類原料的酵素處理,酵素處理中的黏度降低且變得 順暢,因此從酵素處理漿體將茶葉殘渣分離的步驟變得可 輕易地進行。具體而言之,分離、過濾等作業所需花費的 時間可大幅縮短,製造時的作業性可提高,而且因爲作業 時間的縮短可獲得製造成本下降的效果。 【實施方式】 〔本發明之最佳實施方式〕 本發明的方法中作爲原料使用的茶類,例如從山茶科 的常綠樹茶樹(學名:Camellia sinensis(L)O.Kuntze)的 芽、葉、莖等獲得的生葉、經製茶的不發酵茶、半發酵茶 及發酵茶。就不發酵茶而言,例如:煎茶、粗茶(coarse tea)、焙茶、玉露、冠茶、碾茶等蒸製不發酵茶,或嬉野 201215327 茶、青柳茶、各種中國茶等釜炒茶等不發酵茶;就半發酵茶 而言’例如包種茶、鐵觀音茶、烏龍茶等;就發酵茶而言, 例如··紅茶、普洱茶、阿波番茶、碁石茶等。又,也可使用 將不發酵茶或半發酵茶以花加香而成的茶等.。該等之中,尤 其從具有新鮮且天然的香氣或可獲得具有甘味、鮮味等的茶 類萃取物的觀點,綠茶、烏龍茶、茉莉花茶等較佳。 本發明的方法,特徵爲:對於上述茶類原料添加(A) 蛋白酶、(B)單寧酶及(C)具有20000U/g以上的聚半乳 糖醛酸酶活性的酵素製劑,其對於茶類原料1克的添加量 爲使聚半乳糖醛酸酶活性成爲800U以上的量並進行萃取 處理。 依照本發明使用於酵素處理的(A)蛋白酶,係將蛋白 質或胜肽的胜肽鍵予以水解的酵素。該蛋白酶無特殊限制 ,可使用動植物來源或微生物來源的蛋白酶,例如: Protease A「Amano」、Protease Μ「Amano」、Protease P「Amano」3G、Protease N「Amano」、Pancreatin F、 Papain W-40 > P r o m e 1 ai n F (以上爲天野酵素公司製): Sumizyme(註冊商標)AP、LP、MP、FP、LPL(以上爲新曰 本化學工業公司製);Protin(註冊商標)FN(大和化成公司 製);Denapsin(註冊商標)2P、Denazyme(註冊商標)AP、 XP-415、食品用精製木瓜酶、Bioprase(註冊商標)又1^-416F' SP-4FG、SP-15FG(以上爲 NagaseChemtex 公司製) ;Orientase(註冊商標)22BF、0〇N、ONS、20A(以上爲 HBI公司製);Morsin(註冊商標)F、PD酵素、IP酵素、 201215327 AO-Protease(以上爲龜甲萬公司製);Sakanase (科硏製藥 公司製,麵菌來源的蛋白酶);Punchdase (註冊商標)NP-2 、P、可溶性木瓜酶、蛋白酶YP-SS(以上爲Yakult藥品工 業公司製);Flavorzyme (註冊商標)、Protamex (註冊商標 )、Neutrase (註冊商標)、鹼性蛋白酵素(Alkalase)(註冊 商標)(Novozyme日本公司製);Kokulase (註冊商標)SS、 P(以上爲三菱化學食品公司製):VERON PS、 COROLASE PN-L、COROLASE N、COROLASE 7089 、VERON W ' VERON P(以上、AB 酵素公司製); ProtinP、Deskin、Depirace、ProtinA、Thermoase(註冊商 標)(以上爲大和化成公司製);Orientase(註冊商標)90N、 10NL、22BF、Nucleicin(註冊商標)(以上爲HBI公司製); Alloase(註冊商標)AP-10(Yakult藥品工業公司製); Enzylon NBS(洛東化成工業公司製);Actinase(註冊商標 )AS、AF(以上爲科硏製藥公司製);鹼性蛋白酶GL440、 Purafect(註冊商標)4000L、蛋白酶 8 99、Protex 6L、 Tasinase (註冊商標)(Genencor協和公司製):此外,例如 動物來源的胃蛋白酶、胰蛋白酶等。該等蛋白酶可各別單 獨使用或將2種以上組合使用。該等(A)蛋白酶的使用量 視力價等而異,無法一槪而論,但對於茶類原料每1克, 例如通常約0.01U至約100U,較佳爲約1U至約80U的範 圍內。 又,依照本發明於酵素處理使用的(B)單寧酶,只要 是具有分解單寧的活性者即可,無特別限制可任意使用。 -10- 201215327 具體而言’例如將屬於麹黴屬、青黴屬、根黴屬、毛黴屬 等的單寧酶生產菌,使用該等絲狀菌培養通常使用的培養 基’依照常法進行固體培養或液體培養,並將獲得的培養 物或其處理物依照常法精製處理者。又,也可使用市售的 單寧酶例如:單寧酶「龜甲萬(5,000 U/g)」(龜甲萬公司製 )、單寧酶「龜甲萬(500U/g)」(龜甲萬公司製)、單寧酶( 三菱化學食品公司製)、SumizymeTAN(新日本化學公司製 )等。該等單寧酶可各別單獨使用或將2種以上組合使用 ° (B)單寧酶的使用量,視力價等而異,無法—槪而論, 但是對於茶類原料每1克,例如通常約0.1U至約50U, 較佳爲約0.5U至約45U的範圍內。 本發明的方法,除了前述蛋白酶及單寧酶以外,尙將 具有2000 0 U/g以上的聚半乳糖醛酸酶活性的酵素製劑, 以對於茶類原料1克添加量爲使聚半乳糖醛酸酶活性成爲 8 0 0U以上的量並進行萃取處理,此點爲固有的特徵,藉 此’能使來自於茶葉原料的可溶性固體成分產率飛躍地提 高’且有獲得的茶類萃取物富含半乳糖醛酸及胺基酸且甘 味、濃味及鮮味變得豐富的顯著效果。 將茶類原料以果膠酶處理並萃取的技術,如前述,在 本申請案提申以前爲已知。又,對於茶類原料除了添加蛋 白酶及單寧酶以外更添加果膠酶並萃取時,比起僅添加蛋 白酶及單寧酶並進行萃取的情形,可獲得相應的效果。然 而’若對於茶類原料除了添加蛋白酶及單寧酶以外,更對 於茶類原料每1克添加通常800U以上,較佳爲ιοοου以 -11- 201215327201215327 VI. Description of the Invention: [Technical Field of the Invention] The present invention relates to a method for producing a tea extract having a sweet taste, a strong taste, and a strong umami taste and a low astringency from tea leaves in a high yield. [Prior Art] In recent years, 'tea-based beverages have been supplied in the form of products such as cans or bottles, and the production has been increasing due to the high support of consumers for abandoning sweetness. The recent trend is that tea beverages with a strong taste or a strong taste and suppressed astringency are welcome. When a tea extract is produced, a method of treating with an enzyme agent has been proposed, for example, a method of extracting tea leaves by using pectinase and cellulase (refer to Patent Document 1), and a method of treating black tea leaves with tannase. (Refer to Patent Document 2), a method of treating with pectinase, a powder reducing enzyme, and a multi-oxidase (see Patent Document 3), and impregnating an aqueous solution of amylase or protease or cellulase or such a mixed enzyme. A method for producing a cereal tea which is dried and further calcined at 1 to 170 〇c (see Patent Document 4), and an adhesive starch selected from (X- or β-amylase, cellulase, and protease) A method for preparing instant tea extracted from a mixture of at least one enzyme (see Patent Document 5), a method of moistening a leaf of red peony with a tannin enzyme and at least one cell wall digestive enzyme (see Patent Document 6), and extracting a tea leaf residue A method of treating with a cellulase and a protease (see Patent Document 7), a method in which a hot water extract of tea is treated with tannase in advance, followed by freeze concentration (see Patent Document 8), and a green orthoester A method for producing a tea extract which is less turbid in a tea extract (see Patent Document 9), and a method for producing a tea extract obtained by extracting a tea raw material in the presence of a protease and a single 201215327-N-enzyme (see Patent Document 10) a method for producing a tea extract obtained by enzymatically decomposing and extracting tea leaves using an enzyme group containing at least cellulose brewing, hemicellulase, pectinase and protopectinase (see Patent Document n), and tea leaves in protease There is a method of extracting a tea extract which is further subjected to water extraction and further extracting the obtained extract by protease (refer to Patent Document 12), using glucose spattering enzyme, hemicellulose during extraction of the tea raw material and/or after extraction. A method for producing a tea extract obtained by enzymatic decomposition of a saccharide-degrading enzyme such as an enzyme, a pectinase, a polymannosidase, an invertase or an α-galactosidase (see Patent Document 13), and using a dense red crypt Pycn〇p〇rus C〇CCineUS) Teas that produce enzymes and cellulase, hemicellulase, pectinase or pro-pectinase to decompose and extract tea raw materials The method for producing the extract (see Patent Document 14), etc. However, the methods aim to improve the taste of sweet taste, rich taste, umami taste and the like, and improve the yield, and although the corresponding results are obtained, the extraction residue of the tea is obtained. There are still useful components such as cell walls or proteins, which are still not effectively utilized. [Prior Art Document] (Invention Patent Document) Patent Document 1: Japanese Patent Publication No. 4-6 - 1 7 9 5 8 Patent Document 2: Japanese Patent Publication No. 5-2 - 4 2 8 7 7 Patent Document 3: Japanese Patent Publication No. Sho 62- 1 5 1 7 5 Patent Document 4: Japanese Patent Laid-Open Publication No. SHO 57-47465 Japanese Patent Publication No. Hei. No. Hei. No. Hei. No. Hei. No. Hei. No. Hei. No. Hei. No. Hei. No. Hei. No. Hei. No. Hei. - 3 2 8 9 0 No. 1 Patent Document 9: Japanese Patent Laid-Open No. 1 1 - 3 0 8 9 6 5 Patent Document 1 〇: Japanese Patent Laid-Open No. 2 0 0 3 - 1 4 4 0 4 9 Patent Document 1 1 : Japanese Patent Special Opening 2 0 0 3 - 2 1 Ο 1 1 0 Patent Document 12: Japanese Patent Laid-Open Publication No. 2008-67631 (Patent Document 1): Japanese Patent Laid-Open Publication No. JP-A No. 2008-125477 [Technical Problem] The object of the present invention is to provide a method for producing a tea extract, which can extract cell wall components derived from tea leaves which cannot be completely decomposed and extracted in the enzyme treatment extraction of tea. Further, the protein which can be extracted by decomposition of the cell wall component can be further decomposed into an amino acid, and as a result, a tea rich in an amino acid-rich component and rich in sweetness, richness, flavor, and astringency can be obtained in a high yield. Extracts. [Technical method for solving the problem] Tea contains about 25 % protein (5 food ingredient list), and it is expected that if the protein is decomposed by protease, a strong tea extract can be obtained. However, it has not been possible to see that a large amount of amino acid is freed by the action of protease on tea leaves. The applicant in this case, in the previous study, speculated that it was not the combination of the protein in the eucalyptus leaves and the tannins, and found that by extracting the remaining raw materials in the presence of protease and tannase, 201215327, A tea extract having a savory flavor and a strong flavor and a low astringency can be obtained, and has been previously proposed (refer to Japanese Patent Laid-Open Publication No. Hei. However, it is understood that even if the method described in Patent Document 1 is carried out, a considerable amount of unextracted cell wall components and proteins remain in the extracted tea leaves. However, in order to effectively utilize the cell wall components and proteins remaining in the unextracted, the inventors of the present invention found that pectinase, especially polygalacturonase, decomposes the cell tissue of tea leaves with good efficiency. . In order to decompose the protein in the tea leaves to increase the soluble solid content, it is generally considered that the activity unit of the added polygalacturonase is increased. However, most of the pectinase commercially available, the activity unit of the polygalacturonase is not so high, and the effect is usually small when it is usually added (about 0.1 to 2% by mass for tea leaves), and if a halo is added, The protein derived from the excipient or enzyme of the enzyme preparation will lighten the taste of the obtained tea extract, impart a heterogeneous sweet taste to the tea, or produce a miscellaneous taste, which may adversely affect the taste. Therefore, the inventors of the present invention have made further efforts to solve this problem, and as a result, it has been found that, in addition to proteases and tannins, the enzyme preparation having a polygalacturonase activity of 20,000 U/g or more is contained in the tea. When the polygalacturonase activity of 1 gram of tea is 800 U or more, the amount of soluble solid content derived from tea leaves is drastically increased, and a large amount of galacturonic acid is produced, and amino acid is produced. The yield is also improved, and the obtained extract is rich in sweetness, richness and umami, and the extract obtained from the French method is extracted from the C3B species. Inventive of the present invention, the present invention is characterized by the addition of (A) protease, (B) tannin, and (c) polygalacturonase activity of more than 20,000 U/g to tea raw materials. Enzyme preparation and extraction treatment. [Effect of the Invention] The method of the present invention converts about 40% by mass to about 80% by mass of the tea raw material used as a raw material into a soluble solid component, and can greatly improve the yield of the extract from the tea raw material. The rate and the obtained tea extract contained a large amount of galacturonic acid. Further, the yield of the amino acid from the tea raw material can be improved. Moreover, the tea extract obtained by the method of the present invention is rich in sweetness, richness and umami, and can be added to a tea beverage or the like to impart a sweet taste, a strong taste and an umami taste to the tea beverage or the like, or to enhance the tea. Sweet, savory and umami flavors such as oysters. Further, in the method of the present invention, since the viscosity in the enzyme treatment is lowered and smoothed by the enzyme treatment of the tea raw material, the step of separating the tea residue from the enzyme-treated slurry can be easily performed. Specifically, the time required for the separation, filtration, and the like can be greatly shortened, the workability at the time of manufacture can be improved, and the effect of lowering the manufacturing cost can be obtained by shortening the work time. [Embodiment] [Best Mode for Carrying Out the Invention] The tea to be used as a raw material in the method of the present invention, for example, from the buds and leaves of the evergreen tree tea tree of the Camellia family (scientific name: Camellia sinensis (L) O. Kuntze) Leaves obtained from stems, stems, etc., non-fermented tea made from tea, semi-fermented tea and fermented tea. For non-fermented tea, for example, decocted tea, coarse tea, roasted tea, jade, crown tea, milled tea, etc., steamed non-fermented tea, or Ureshino 201215327 tea, Qingliu tea, various Chinese tea, etc. Tea; in the case of semi-fermented tea, for example, tea, Tieguanyin tea, oolong tea, etc.; for fermented tea, for example, black tea, Pu'er tea, Apofan tea, ochre tea, and the like. Further, a tea obtained by incubating unfermented tea or semi-fermented tea with flowers may be used. Among these, green tea, oolong tea, jasmine tea and the like are preferable from the viewpoint of having a fresh and natural aroma or obtaining a tea extract having a sweet taste, an umami taste and the like. The method of the present invention is characterized in that: (A) protease, (B) tannin, and (C) an enzyme preparation having a polygalacturonase activity of 20,000 U/g or more for the tea raw material, which is for tea One gram of the raw material was added in an amount such that the polygalacturonase activity was 800 U or more and subjected to extraction treatment. The (A) protease used in the enzyme treatment according to the present invention is an enzyme which hydrolyzes the peptide bond of a protein or a peptide. The protease is not particularly limited, and proteases of animal or plant origin or microbial origin can be used, for example, Protease A "Amano", Protease "Amano", Protease P "Amano" 3G, Protease N "Amano", Pancreatin F, Papain W-40. > P rome 1 ai n F (The above is manufactured by Amano Enzyme Co., Ltd.): Sumizyme (registered trademark) AP, LP, MP, FP, LPL (above is manufactured by Shinsei Chemical Industry Co., Ltd.); Protin (registered trademark) FN ( Daiwasei (registered trademark) 2P, Denazyme (registered trademark) AP, XP-415, refined papain for food, Bioprase (registered trademark) and 1^-416F' SP-4FG, SP-15FG (above) It is manufactured by Nagase Chemtex); Orientase (registered trademark) 22BF, 0〇N, ONS, 20A (above is HBI); Morsin (registered trademark) F, PD enzyme, IP enzyme, 201215327 AO-Protease (above is Kikkoman) Company system); Sakanase (manufactured by Keji Pharmaceutical Co., Ltd., protease derived from pasta); Punchdase (registered trademark) NP-2, P, soluble papain, protease YP-SS (above: Yakult Pharmaceutical Co., Ltd.); Flavorzyme ( Note Trademark), Protamex (registered trademark), Neutrase (registered trademark), alkaline protein (Alkalase) (registered trademark) (Novozyme Japan); Kokulase (registered trademark) SS, P (above is Mitsubishi Chemical Food Co., Ltd.) : VERON PS, COROLASE PN-L, COROLASE N, COROLASE 7089, VERON W ' VERON P (above, AB enzyme company); ProtinP, Deskin, Depirace, ProtinA, Thermoase (registered trademark) (above is Daiwa Kasei Co., Ltd.) ;Orientase (registered trademark) 90N, 10NL, 22BF, Nucleixin (registered trademark) (above is HBI company); Alloase (registered trademark) AP-10 (manufactured by Yakult Pharmaceutical Co., Ltd.); Enzylon NBS (made by Luodong Chemical Industry Co., Ltd.) ); Actinase (registered trademark) AS, AF (above is Kodak Pharmaceutical Co., Ltd.); alkaline protease GL440, Purafect (registered trademark) 4000L, Protease 8 99, Protex 6L, Tasinase (registered trademark) (manufactured by Genencor) Further, for example, animal-derived pepsin, trypsin, and the like. These proteases may be used singly or in combination of two or more kinds. The amount of the (A) protease used varies depending on the valence and the like, and cannot be ambiguous, but for every 1 gram of the tea raw material, for example, usually about 0.01 U to about 100 U, preferably about 1 U to about 80 U. . Further, the (B) tannase used for the enzyme treatment according to the present invention is not particularly limited as long as it has an activity of decomposing tannins. -10- 201215327 Specifically, for example, a tannase-producing bacterium belonging to the genus Pythium, Penicillium, Rhizopus, Mucor, etc., which is usually used in the culture of the filamentous fungi, is solid according to the usual method. The culture or liquid culture is carried out, and the obtained culture or the treated product thereof is refined according to a conventional method. In addition, a commercially available tannin enzyme such as a tannin enzyme "Kikkoman (5,000 U/g)" (manufactured by Kikkoman Co., Ltd.) and a tannin enzyme "Kei Kawan (500 U/g)" (Kikkoman Co., Ltd.) can be used. ), tannase (manufactured by Mitsubishi Chemical Corporation), Sumizyme TAN (manufactured by Shin-Nippon Chemical Co., Ltd.), and the like. These tannins may be used singly or in combination of two or more kinds. (B) The amount of tannin used, the visual acuity, etc. may not be the same, but for every 1 gram of the tea raw material, for example It is usually in the range of from about 0.1 U to about 50 U, preferably from about 0.5 U to about 45 U. In the method of the present invention, in addition to the protease and the tannase, the sputum will have an enzyme preparation having a polygalacturonase activity of 2000 0 U/g or more, and 1 gram of the tea raw material is added to make the polygalactosaldehyde The acidase activity is more than 800 U and is subjected to extraction treatment, which is an inherent feature, whereby 'the yield of soluble solid components derived from tea raw materials can be greatly improved' and the obtained tea extract is rich Contains galacturonic acid and amino acid and has a remarkable effect of becoming rich in sweetness, richness and umami taste. Techniques for treating and extracting tea raw materials with pectinase, as previously described, are known prior to the application of this application. Further, in the case where the pectinase is added and extracted in addition to the protease and tannase, the tea raw material can be obtained by extracting and extracting only the protease and the tannin. However, if the tea raw material is added with a protease and a tannase, it is usually added to the tea raw material in an amount of usually 800 U or more, preferably ιοοου to -11-201215327.

上,更佳爲1000U至10000U,又更佳爲1500U至5000U 的聚半乳糖醛酸酶並進行萃取處理,則可獲得茶葉原料( 乾燥茶葉)當中的約40質量%至約80質量%可溶化的令人 意外的現象,而且隨著細胞壁成分分解,生成多量半乳糖 醛酸,且胺基酸的萃取量也增加,伴隨著該等的增加,鮮 味、甘味、濃味等增強,能以高產率獲得風味豐富的茶類 萃取物,而且能有效率地將茶葉組織分解,可提高水可溶 性成分的萃取效率。 聚半乳糖醛酸酶爲一種果膠酶。一般而言,分類爲果 膠酶的酵素包含聚半乳糖醛酸酶、果膠裂解酶及果膠甲基 酯酶。聚半乳糖醛酸酶,爲將果膠中的聚半乳糖醛酸主鏈 的α-1,4鍵結水解的酵素;果膠裂解酶,爲將果膠中的聚半 乳糖醛酸主鏈的α-1,4鍵結利用β-脫離反應進行分解的酵 素;果膠甲基酯酶係將果膠的甲基酯水解的酵素。果膠酶 係使植物的組織崩壞的酵素群當中處於中心的酵素,將茶 類原料以果膠酶處理並萃取的技術,如前所述,在本案提 申以前即爲已知。但是’以往例如前述專利文獻等記載的 果膠酶以通常的添加量使用並對於茶類原料進行酵素處理 ,仍算不上能將茶類的細胞組織充分分解。所以,探討是 否果膠酶中的聚半乳糖醛酸酶、果膠裂解酶、果膠甲基酯 酶當中任一酵素對於茶類的細胞組織特別有效,結果發現 :即使聚半乳糖醛酸酶單獨亦爲有效,而且藉由使用比起 以往所使用者具有更高活性單位者,能將細胞組織充分分 解。 -12- 201215327 又,本說明書中,聚半乳糖醛酸酶活性’係利用 Somogyi — Nelson 法(J. Biol. Chem. 153,3 7 5 -3 8 0,1 994 年 ),以聚半乳糖醛酸水溶液作爲基質使聚半乳糖醛酸酶作 用,並將爲酵素反應生成物的還原糖以比色法定量的方法 所測定之値,酵素1單位(1 U),意指於1分鐘生成半乳糖 醒酸Ιμηιοί的酵素量。 上述果膠酶,就市售品而言,例如Pectinase PL·「 Amano」、果膠酶G「Amano」(以上爲天野酵素公司製) 、Pectinase-GODO(合同酒精公司製)、Sucrase (註冊商標 )A、N .、S (以'上爲三菱化學食品公司製)、Sumizyme(註冊 商標)AP-2、SPC、SPG、MC、PX、液狀 SumizymeAP-2、 (以上爲新日本化學工業公司製)、Pectinase XP-5 3 4(NagaseChemtex 公司製)、Pectinex(註冊商標)、 Pectinex UltraSP-L、Ultrazyme (註冊商標)、Vinozym(註 冊商標)、Citorozym(註冊商標)、perezym (註冊商標)(以 上爲 Novo Nordisk Bioindustry 公司製);Cellulosin(註冊 商標)PC5、PE60、PEL、可溶性 Pectinase T(以上爲 ΗΒΙ 公司製)、Pectinase SS、Pectinase HL(以上爲 Yakult 藥品 工業公司製)等。該等當中’聚半乳糖醛酸酶活性尤其高 的果膠酶’例如‘· SumizymeAP-2、SPC、SPG(以上爲新日 本化學工業公司製)。 一般市售的果膠酶製劑的聚半乳糖醛酸酶活性,通常 約500U/g至約20000U/g。因此,爲了對於茶葉原料1克 添加800U,必需對於茶葉原料1克添加到〇 〇4g至i 6g -13- 201215327 的大量果膠酶製劑。此時,若例如對於茶葉原料1克添加 的酵素製劑量爲0.0 6g以上,尤其是0.08g以上,則賦形 劑或其他成分會對於茶類萃取液造成強大影響,會有以下 問題:獲得的茶類萃取物的味道變淡,對於茶賦予異質的 不自然的甘味,或生出雜味等對於呈味造成壞影響。因此 ,雖然可直接使用聚半乳糖醛酸酶活性原本爲20000U/g 以上的高活性的果膠酶,但是,當爲聚半乳糖醛酸酶活性 小於20000U/g的果膠酶製劑時,例如需要將該酵素製劑 利用水混合性有機溶劑(丙酮、乙醇等)沉澱、等電點沉澱 、超過濾、凝膠過濾等進行精製,並回收聚半乳糖醛酸酶 活性爲20000U/g以上的區段並使用。 又,萃取處理時,除了添加前述(A)蛋白酶、(B)單寧 酶及(C)聚半乳糖醛酸酶以外,藉由更添加來自於長枝木 黴(Trichoderma longibrachiatum)或里氏木黴(Trichoderma re esei)的纖維素酶並進行萃取,能更有效率地將茶葉組織 分解,並使得水可溶性成分的萃取效率增加。 將茶類以纖維素酶處理並萃取的技術,如前所述,在 本申請案提申以前爲已知。又,對於茶類原料添加蛋白酶 及單寧酶以外,更添加來自於黑麵黴(Aspergillus niger) 或綠木黴(Trichoderma viride)等的纖維素酶並萃取時,比 起僅添加蛋白酶及單寧酶並萃取時,可獲得相應的效果。 然而’解明:若對於茶類原料除了添加蛋白酶及單寧酶以 外’更添加來自於長枝木黴(Trichoderma longibrachiatum)或里氏木黴(Trichoderma reesei)的纖維 -14- 201215327 素酶並萃取,能將細胞組織充分分解。 上述來自於長枝木黴(Trichoderma longibrachiatum) 或里氏木黴(Trichoderma reesei)的纖維素酶,例如: Cellulosin(註冊商標)T3(HBI公司製)、Sumizyme(註冊商 標)CS、C(以上爲新日本化學工業公司製)、cellulase SS(NagaseChemtex公司製)、Sucrase (註冊商標)C(三菱化 學食品公司製)等。來自於長枝木黴(T r i c h 〇 d e r m a longibrachiatum)或里氏木黴(Trichoderma reesei)的纖維 素酶的使用量,視力價等而異,無法一槪而論,但是例如 茶類原料每1克,通常約0.1U至約200U,較佳爲約0.5U至 約100U、更佳爲約1U至約50U的範圍內。 本發明中,在不妨礙本.發明的效果的範圍,也可進一 步倂用半纖維素酶、原果膠酶、葡萄糖澱粉酶、聚葡萄糖 酶、聚甘露糖酶、α -半·乳糖苷酶等其他的糖質分解酵素。 用於製造本發明的茶類萃取物的—實施態樣的例子, 如下: 準備相對於茶類原料1重量份,爲4質量份至4〇質 量份的水及視需要溶解有茶類原料的〗質量%至1質量 %的抗壞血酸或抗壞血酸鈉的溶液,於其中添加茶類原料 ’並視需要於約6 0 °C至約1 2 1 °C進行約2秒至約2 0分鐘 殺菌後冷卻。接著,首先添加單寧酶並混合均勻後,再添 加蛋白酶及具有20000U/g以上的聚半乳糖醛酸酶活性的 酵素製劑,使添加量爲對於茶類原料丨克,聚半乳糖醛酸 酶活性成爲800U以上,於約2〇t至約6〇t:進行約3〇分 -15- 201215327 至約 24小時酵素處理。酵素處理後,於約 601:至約 121 °C進行約2秒至約20分鐘酵素失活並冷卻,利用離心 分離、濾紙過濾等適當分離方法進行分離,可獲得澄清的 茶類萃取物。獲得的茶類萃取物也可視所望,而使用適當 的濃縮方法製成濃縮液的形態。 利用以上的酵素處理萃取,比起完全未進行酵素處理 的茶類萃取物,可生成約4倍量至約5倍量的胺基酸,且 茶類原料的細胞組織分解而生成多量半乳糖醛酸,可將作 爲原料使用的茶類當中,約40質量%至約80質量%變換 爲可溶性固體成分。 利用上述方法,從茶類原料而來的固體成分的產率、 胺基酸產率及半乳糖醛酸產率均增加,結果可獲得以下茶 類萃取物:(a)以茶類萃取物的總固體成分(以Bx換算計 )爲基準,含有半乳糖醛酸1.1至5質量%、(b)半乳糖醛 酸/單寧的質量比爲0.04至0.8,且(c)半乳糖醛酸/胺基酸 的質量比爲〇·〇8至0.8 ;較佳爲(a)以茶類萃取物的總固體 成分(以Bx換算計)爲基準,含有半乳糖醛酸1.2至4質 量%,且(b)半乳糖醛酸/單寧的質量比爲0.06至0.4,且 (c)半乳糖醛酸/胺基酸的質量比爲0.14至0.6;更佳爲(a) 以茶類萃取物的總固體成分(以Bx換算計)爲基準,含有 半乳糖醛酸1.3至3質量%,(b)半乳糖醛酸/單寧的質量比 爲0.07至0.2,且(c)半乳糖醛酸/胺基酸的質量比爲0.19 至 0.4。 又,半乳糖醛酸給人像是抹茶等高級茶的印象的軟黏 201215327 ’又有使人耳目一新的酸味,因此推測具有苦澀味遮蔽' 異臭遮蔽、稠感賦予等的作用,推測半乳糖醛酸的增加爲 本發明的茶類萃取物的甘味、濃味、鮮味等的重要要因之 m * 〇 本發明的茶類萃取物,可視所望,充塡於容器後或於 充塡前進行加熱殺菌,藉此可處於可長期保存的狀態。 又’本發明的茶類萃取物,通常可直接以液狀形式利 用’但是也可視所望,於該萃取物中添加糊精、化工澱粉 '環糊精、阿拉伯膠等賦形劑而製成粉末狀。 以下利用實施例及比較例對於本發明更具體説明。 《實施例》 參考例1 聚半乳糖醛酸酶活性的測定(Somogyi —N?lS〇n法:參 照 J. Biol. Chem. 1 5 3, 3 75 -3 80, 1994 年) 於含有 1%聚半乳糖醛酸的 5 0mM乙酸緩衝液 (pH4.5)0.9ml中,添加酵素溶液的適當(適度)的稀釋液 0.1ml。使前述混合溶液於45°C反應適當(適度)時間後, 於沸騰水浴加熱1 〇分鐘使酵素失活,冰冷後作爲反應液 。於反應液〇.3ml加入Somogyi銅試藥0.3ml,於沸騰水 浴加熱10分鐘,冰冷並加入Nelson試藥0.3ml,以試管 混合器充分攪拌,再加入離子交換水3ml,以試管混合器 充分攪拌。將該溶液利用離心分離機9 0 00轉數處理3分 鐘,測定上清於500nm的吸光度(Abs.)。另一方面’使用 令前述酵素溶液的適當(適度)的稀釋液預先加熱失活者 -17- 201215327 ,進行與前述完全同樣的操作,作爲空白(blank)的吸光度 。從使用的酵素濃度、酵素反應時間、吸光度,計算酵素 lg於1分鐘生成的半乳糖醛酸μπιοί數,作爲酵素每lg 的單位(U)。 測定的酵素及聚半乳糖醛酸酶活性測定値: SumizymeAP2(新日本化學工業公司製):i2400U/g Cellulosin PE 60(HBI 公司製): 20600U/gMore preferably, from 1000 U to 10000 U, more preferably from 1500 U to 5000 U, of polygalacturonase and extraction treatment, about 40% to about 80% by mass of the tea raw material (dried tea) can be obtained. An unexpected phenomenon, and as the cell wall component decomposes, a large amount of galacturonic acid is formed, and the amount of extraction of the amino acid is also increased. With the increase of the odor, sweet taste, rich taste, etc., The high-yield tea extract is rich in flavor, and the tea tissue can be efficiently decomposed to improve the extraction efficiency of the water-soluble component. Polygalacturonase is a pectinase. In general, enzymes classified as pectinase include polygalacturonase, pectin lyase, and pectin methylesterase. Polygalacturonase, an enzyme that hydrolyzes the α-1,4 linkage of the polygalacturonic acid backbone in pectin; a pectin lyase, a polygalacturonic acid backbone in pectin The α-1,4 bond is an enzyme that is decomposed by the β-desorption reaction; the pectin methyl esterase is an enzyme that hydrolyzes the methyl ester of pectin. The pectinase is a central enzyme in the enzyme group that causes the tissue of the plant to collapse. The technique of treating and extracting the tea raw material with pectinase is as described above before the present invention. However, in the past, for example, the pectinase described in the above-mentioned patent documents and the like is used in an ordinary amount of addition and the enzyme treatment of the tea raw material is not enough to sufficiently decompose the cell tissue of the tea. Therefore, it is investigated whether any of the polygalacturonase, pectin lyase, and pectin methyl esterase in pectinase is particularly effective for the cell tissue of tea, and it is found that even polygalacturonase It is also effective alone, and the cell tissue can be sufficiently decomposed by using a higher activity unit than the conventional user. -12- 201215327 Also, in this specification, polygalacturonase activity is based on the Somogyi-Nelson method (J. Biol. Chem. 153, 3 7 5 - 38 0, 1994), with polygalactose The aqueous solution of aldehyde acid acts as a substrate for the polygalacturonase, and the reducing sugar which is the enzyme reaction product is determined by colorimetric method. The enzyme is 1 unit (1 U), which means that it is generated in 1 minute. The amount of enzyme that galactose awake sour Ιμηιοί. For the above-mentioned pectinase, for example, Pectinase PL·“Amano”, pectinase G “Amano” (above, manufactured by Amano Enzyme Co., Ltd.), Pectinase-GODO (manufactured by Contract Alcohol Co., Ltd.), Sucrase (registered trademark) ) A, N., S (made by 'Mitsubishi Chemical Food Co., Ltd.), Sumizyme (registered trademark) AP-2, SPC, SPG, MC, PX, liquid Sumizyme AP-2, (The above is New Japan Chemical Industry Co., Ltd.) , Pectinase XP-5 3 4 (manufactured by Nagase Chemtex), Pectinex (registered trademark), Pectinex UltraSP-L, Ultrazyme (registered trademark), Vinozym (registered trademark), Citorozym (registered trademark), perezym (registered trademark) ( The above are manufactured by Novo Nordisk Bioindustry Co., Ltd.; Cellulosin (registered trademark) PC5, PE60, PEL, soluble Pectinase T (manufactured by Sigma), Pectinase SS, Pectinase HL (manufactured by Yakult Pharmaceutical Co., Ltd.), and the like. Among these, pectinase having a particularly high polygalacturonase activity is, for example, 'Sumizyme AP-2, SPC, and SPG (the above is manufactured by Shin-Nippon Chemical Co., Ltd.). The polygalacturonase activity of a commercially available pectinase preparation is usually from about 500 U/g to about 20,000 U/g. Therefore, in order to add 800 U to 1 g of the tea raw material, it is necessary to add 1 g of the tea raw material to a large amount of pectinase preparation of 〇 4g to i 6g -13 - 201215327. At this time, if the amount of the enzyme preparation added to 1 g of the tea raw material is, for example, 0.06 g or more, particularly 0.08 g or more, the excipient or other ingredients may have a strong influence on the tea extract, and there are the following problems: The taste of the tea extract is light, and the unnatural taste of the tea is imparted to the tea, or the taste is generated, which has a bad influence on the taste. Therefore, although a highly active pectinase having a polygalacturonase activity of 20,000 U/g or more can be directly used, when it is a pectinase preparation having a polygalacturonase activity of less than 20,000 U/g, for example, The enzyme preparation needs to be purified by precipitation with a water-miscible organic solvent (acetone, ethanol, etc.), isoelectric precipitation, ultrafiltration, gel filtration, etc., and a polygalacturonase activity of 20,000 U/g or more is recovered. Segment and use. Further, in the extraction treatment, in addition to the addition of the above (A) protease, (B) tanninase, and (C) polygalacturonase, it is further added from Trichoderma longibrachiatum or Richter wood. The cellulase of the mold (Trichoderma re esei) is extracted to more efficiently decompose the tea tissue and increase the extraction efficiency of the water-soluble component. Techniques for treating and extracting tea with cellulase are as previously described and are known prior to the application of this application. In addition, when proteases and tannins are added to tea raw materials, cellulase derived from Aspergillus niger or Trichoderma viride is added and extracted, compared with only protease and tannin. When the enzyme is extracted and extracted, the corresponding effect can be obtained. However, 'solution: if the tea raw material is added with protease and tannin, 'addition of fiber-14-201215327 from the Trichoderma longibrachiatum or Trichoderma reesei enzyme and extract, It can fully decompose cell tissue. The above cellulase derived from Trichoderma longibrachiatum or Trichoderma reesei, for example, Cellulosin (registered trademark) T3 (manufactured by HBI Corporation), Sumizyme (registered trademark) CS, C (above Nippon Chemical Industry Co., Ltd., Cellulase SS (manufactured by Nagase Chemtex Co., Ltd.), Sucrase (registered trademark) C (manufactured by Mitsubishi Chemical Food Co., Ltd.), and the like. The amount of cellulase used in T rich 〇derma longibrachiatum or Trichoderma reesei varies depending on the price of vision, and cannot be ambiguous, but for example, 1 gram of tea raw material Typically, it is in the range of from about 0.1 U to about 200 U, preferably from about 0.5 U to about 100 U, more preferably from about 1 U to about 50 U. In the present invention, a hemicellulase, a pro-pectinase, a glucoamylase, a polyglucose, a polymannerase, an α-gal-lactosidase may be further used without departing from the effects of the present invention. Other saccharolytic enzymes. An example of the embodiment for producing the tea extract of the present invention is as follows: Prepare 4 parts by mass to 4 parts by mass of water relative to 1 part by weight of the tea raw material, and if necessary, dissolve the tea raw material. 〗 〖% by mass to 1% by mass of ascorbic acid or sodium ascorbate solution, adding a tea raw material therein and optionally cooling at about 60 ° C to about 1 21 ° C for about 2 seconds to about 20 minutes after sterilization . Next, first add the tannin enzyme and mix it evenly, and then add the protease and the enzyme preparation having the polygalacturonase activity of 20,000 U/g or more, so that the added amount is for the tea raw material, the polygalacturonase The activity is 800 U or more, and is about 2 Torr to about 6 Torr: about 3 〇 -15 - 201215327 to about 24 hours of enzyme treatment. After the enzyme treatment, the enzyme is inactivated and cooled at about 601: to about 121 ° C for about 2 seconds to about 20 minutes, and separated by a separate separation method such as centrifugation or filter paper filtration to obtain a clarified tea extract. The obtained tea extract can also be expected to be in the form of a concentrate using an appropriate concentration method. By using the above enzyme treatment and extraction, an amino acid can be produced in an amount of about 4 times to about 5 times compared with the tea extract which is not completely subjected to the enzyme treatment, and the cell tissue of the tea raw material is decomposed to generate a large amount of galactose. The acid can be converted into a soluble solid component from about 40% by mass to about 80% by mass of the tea used as a raw material. By the above method, the yield of the solid component, the yield of the amino acid, and the yield of the galacturonic acid are increased from the tea raw material, and as a result, the following tea extract can be obtained: (a) the extract of the tea extract The total solid content (in terms of Bx) is 1.1 to 5% by mass of galacturonic acid, (b) the mass ratio of galacturonic acid/tannin is 0.04 to 0.8, and (c) galacturonic acid/ The mass ratio of the amino acid is 〇·〇 8 to 0.8; preferably (a) is 1.2 to 4% by mass based on the total solid content (in terms of Bx) of the tea extract, and galacturonic acid is used. (b) the mass ratio of galacturonic acid/tannin is from 0.06 to 0.4, and (c) the mass ratio of galacturonic acid/amino acid is from 0.14 to 0.6; more preferably (a) the extract of tea The total solid content (in terms of Bx) is 1.3 to 3% by mass of galacturonic acid, (b) the mass ratio of galacturonic acid/tannin is 0.07 to 0.2, and (c) galacturonic acid/ The mass ratio of the amino acid is from 0.19 to 0.4. In addition, galacturonic acid gives the impression that the impression of high-grade tea such as matcha is soft and sticky 201215327 'has a refreshing sour taste. Therefore, it is presumed to have a bitter taste masking effect, such as odor masking and thickening, and it is estimated that galacturonic acid The increase is the important factor of the sweet taste, rich taste and umami taste of the tea extract of the present invention. m * The tea extract of the present invention can be expected to be filled in the container or heat-sterilized before filling. Thereby, it can be in a state that can be stored for a long time. Further, the tea extract of the present invention can be directly used in a liquid form, but it is also possible to obtain a powder by adding an excipient such as dextrin, chemical starch 'cyclodextrin or gum arabic to the extract. shape. Hereinafter, the present invention will be more specifically described by way of examples and comparative examples. EXAMPLES Reference Example 1 Determination of polygalacturonase activity (Somogyi - N?lS〇n method: refer to J. Biol. Chem. 1 5 3, 3 75 -3 80, 1994) in containing 1% To 0.9 ml of a 50 mM acetate buffer (pH 4.5) of polygalacturonic acid, 0.1 ml of an appropriate (moderate) dilution of the enzyme solution was added. After the mixed solution was reacted at 45 ° C for an appropriate (moderate) time, the enzyme was inactivated by heating in a boiling water bath for 1 Torr, and then cooled to serve as a reaction liquid. Add 3 ml of Somogyi copper reagent to 3 ml of the reaction solution, heat in a boiling water bath for 10 minutes, ice-cool and add 0.3 ml of Nelson reagent, stir well with a test tube mixer, add 3 ml of ion-exchanged water, and stir well with a test tube mixer. . The solution was treated by a centrifugal separator at 900 rpm for 3 minutes, and the absorbance (Abs.) of the supernatant at 500 nm was measured. On the other hand, the inactivated person -17-201215327 was preheated by using an appropriate (moderate) dilution of the enzyme solution, and the same operation as described above was carried out as the blank absorbance. From the enzyme concentration used, the enzyme reaction time, and the absorbance, calculate the galacturonic acid μπιοί number produced by the enzyme lg in 1 minute as the unit (U) per lg of the enzyme. Measurement of enzyme and polygalacturonase activity 値: Sumizyme AP2 (manufactured by Nippon Chemical Industry Co., Ltd.): i2400 U/g Cellulosin PE 60 (manufactured by HBI Co., Ltd.): 20600 U/g

Sumizyme MC (新日本化學工業公司製):l690U/g SuCraseN(三菱化學食品公司製): 4550U/g 參考例2 將 SumizymeAP2(新日本化學工業公司製)l〇〇g(上述 測定的聚半乳糖醛酸酶活性:1 2400U/g)溶解於離子交換 水1 000g,以 Vivaflow(註冊商標)50VF05P2(區段分子量 30,000: Sartorius公司製)進行超過爐濃縮,回收未通過 部30ml,再進行冷凍乾燥,獲得參考品2(12.0g :上述測 定之聚半乳糖醛酸酶活性:8 6 5 00U/g)。 實施例1 在軟水900g中溶有抗壞血酸鈉〇.6g而成的溶液中添 加綠茶葉(中國產蒸青製法)l〇〇g,於80 °C進行5分鐘殺菌 ,冷卻至45°C。於其中添加單寧酶(三菱化學食品公司製 :500 U/g)lg,攪拌15分鐘。之後,添加Protease Μ(天 野酵素公司製:5 5 00U/g)lg及參考品2 (對於茶葉1克’ 由上述測定的聚半乳糖醛酸酶活性爲4152lJ/g) 4.8g並溶 解後,於40°C進行8小時酵素處理。 -18- 201215327 酵素處理後,於90°c進行10分鐘殺菌’冷卻至30°c ,再以布除去茶葉殘渣固體物後’使用在No.2濾紙(8 cm) 預塗覆有纖維素粉末l〇g的Nutsche過濾器,以固定壓力 進行吸引過濾(減壓度13. 3 3 KP a),獲得澄清的萃取液 825g (過濾所需時間3分42秒)。將該萃取液進行減壓濃 縮,獲得Bx48°的濃縮液165.3g。將該濃縮液進行95°C、 3 〇秒加熱殺菌,充塡於密閉容器後,急速地冷卻至常溫 ,獲得本發明品1的綠茶類萃取物。 實施例2 將實施例1中的參考品2的添加量從4.8g改爲2.4g( 對於茶葉1克,由上述測定的聚半乳糖醛酸酶活性爲 2076U/g),除此以外與實施例1進行完全相同的操作(過 濾所需時間4分2 5秒)’獲得本發明品2 (1 4 9.1 g)。 實施例3 將實施例1中的參考品2的添加量從4.8g改爲1.2g( 對於茶葉1克’由上述測定的聚半乳糖醛酸酶活性爲 1 03 8 U/g),除此以外與實施例i進行完全相同的操作(過 濾所需時間5分5 2秒)’獲得本發明品3 (1 3 8.5 g)。 實施例4 _ 將實施例1中的參考品2 (4.8 g)改爲添加C e 11 u 1 〇 s i η PE60(5.0g’對於茶葉1克’由上述測定的聚半乳糖醛酸 酶活性爲1 〇3 〇U/g) ’除此以外與實施例i進行完全相同的 操作(過濾所需時間5分2 1秒),獲得本發明品4 (〗4 6 3 g) -19- 201215327 實施例5 將實施例 1中添加參考品 2(4.8 g)以外更添加 Sumizyme C(新曰本化學工業公司製 Trichoderma longibrachiatum 來源的纖維素酶:1 5 00U/g)〇.25g,除此 以外與實施例1進行完全相同的操作(過濾所需時間3分 2 1秒),獲得本發明品5 (1 6 7 · 3 g)。 實施例6 將實施例 1中添加參考品 2 (4.8 g)以外更添加 Cellulosin T3(HBI公司製里氏木黴來源的纖維素酶: 2600U/g)0.25g,除此以外與實施例1進行完全相同的操 作(過濾所需時間3分32秒),獲得本發明品6(1 65.4g)。 參考例3 將 Sumizyme M C(新日本化學公司製)150g(由上述測 定的聚半乳糖醛酸酶活性·· 1 690U/g)溶於離子交換水 1 500g並清洗,利用離心分離(4,500 xg、5分)將沉澱部回 收,再進行冷凍乾燥,獲得參考品3(9.8g由上述測定之 聚半乳糖醛酸酶活性:20770U/g)。 實施例7 將實施例1中的參考品2(4.8 g)改爲添加參考品3 (相 對於茶葉1克,由上述測定之聚半乳糖醛酸酶活性爲 1018U/g) 4.9g,除此以外完全與實施例1進行相同操作( 過濾所需時間4分49秒),獲得本發明品7(153.2)。 參考例4 將SucraSeN(三菱化學食品公司製)i00g(由上述測定 -20- 201215327 之聚半乳糖醛酸酶活性:4550U/g)溶於離子交換水l〇〇〇g ,以Vivaflow (註冊商標)50VF05P2(區分分子量30,000: Sartorius公司製)·進行超過濾濃縮,回收未通過部25ml, 再進行冷凍乾燥,獲得參考品4(10.0g,由上述測定之聚 半乳糖醛酸酶活性:32,000U/g)。 實施例8 將實施例1中的參考品2(4.8g)改爲添加參考品4 (相 對於茶葉1克,由上述測定之聚半乳糖醛酸酶活性爲 1 600U/g)5.0g,除此以外完全與實施例1進行相同操作( 過濾所需時間4分1 6秒),獲得本發明品8 (1 5 5.4 g) ° 比較例1 在實施例1中完全不使用酵素,除此以外與實施例1 進行完全相同的操作(過濾所需時間1 〇分25秒)’獲得比 較品 1(66.8 g)。 比較例2 在實施例1不使用參考品2(4.8g) ’除此以外與實施 例1進行完全相同的操作(過濾所需時間9分5 7秒)’獲 得比較品2(72.9g)。 比較例3至5 將實施例 1中的參考品 2(4.8 g) ’各改爲添加 Sumizyme AP2(新日本化學工業公司製)2.0g(對於朱葉1 克,由上述測定之聚半乳糖醛酸酶活性爲24 8 U/g)、 Sumizyme MC(新日本化學工業公司製)2.0g(對於茶葉1克 ,由上述測定之聚半乳糖醛酸酶活性爲33.8U/g)、 SuCraSeN(三菱化學食品公司製)2.0g(對於茶葉1克,由上 -21 - 201215327 述測定之聚半乳糖醛酸酶活性爲9 1 U/g),除此以外完全與 實施例1進行相同操作,獲得比較品3至5(過濾所花時間 及產量、其他測定値合倂記載如下表1所示)° 比較例6至8 (藉由多量使用市售果膠酶,使對於茶葉1克之聚半乳糖 醛酸酶活性爲8 0 0 U以上的例子) 將實施例 1中的參考品 2(4.8g) ’各改爲使用 SumizymeAP2(新日本化學工業公司製)8.〇g(對於茶葉1克 ,由上述測定之聚半乳糖醛酸酶活性爲 992 U/g)、 Sumizyme MC(新日本化學工業公司製)5〇.〇g(對於茶葉1 克,由上述測定之聚半乳糖醛酸酶活性爲 845U/g)、 Sucrase N(三菱化學食品公司製)20g(對於茶葉1克,由上 述測定之聚半乳糖醛酸酶活性爲910U/g),除此以外完全 與實施例1進行相同操作’獲得比較品6至8 (過濾所花時 間及產量、其他測定値’合倂記載於下表1)。 成分分析 對於本發明品1至8及比較品1至8,進行單寧、胺 基酸及半乳糖醛酸的濃度(%爲質量基準)的測定。 測定方法 胺基酸:胺基酸自動分析計 單寧:酒石酸鐵法 半乳糖醛酸:高速液體層析(HPLC)法 本發明品1至8及比較品1至8從綠茶原料而來的產 量及各成分的測定値(濃度)及過濾所用時間,如下表丨所 不 ° -22- 201215327 過濾所需時間 3分42秒 4分25秒 5分52秒 5分21秒 3分21秒 1- 3分32秒 L—―― 1 1 4分49秒 4分16秒 10分25秒 9分57秒 7分12秒 8分16秒 7分57秒 4分25秒 4分56秒 4分47秒 半乳糖醛酸濃度 (%) 0.870 0.776 0.661 i i 0.674 0.921 0.943 0.641 0.665 0.018 0.061 0.348 0.163 0.225 0.521 0.374 0.456 單寧濃度 (%) 8.51 8.96 9.32 8.85 , 7.91 8.09 9.02 9*13 17.82 15.32 12.34 14.68 13.21 8.89 5.62 6.54 胺基酸濃度 (%) CN rn 3.38 3.45 3.32 | 3.14 00 cn 3.21 1 3.32 CN 5.57 4.53 5.02 4.47 3.18 2.01 2.68 萃取物產量 (g) 165.3 149.1 138.5 146.3 167.3 165.4 142,3 66.8 72_9 103.5 83.1 96.5 158.5 225.2 175.6 果膠酶 职扫 «-Η nml ΠΠΙΓ |1 4152 2076 1038 1030 i 4152 1 4152 1 1018 1600 未使用 未使用 248 33,8 992 910 o g 2薇3 M鎵_ 涤S另 迄嫛滕 莉s 〇〇 寸 <s <N 〇 w-i 00 寸 1 〇〇 — 1 〇\ 寸 〇 〇 (Ν 〇 (N 〇 fN 〇 〇〇 50.0 20.0 跋題习 蝕聽 86500 86500 86500 20600 86500 1 86500 1 1 20770 32000 12400 1690 4550 12400 1690 4550 酵素名 2 ng < ^ I* ε熙 2ng Is s囤 Sag em !爍 ε囤 3豳 Cellulosin PE60 βΜ ε锻 〇 Ό 艮 Ν S Sng gM !鹪 s围 5豳 Cellulosin T3 Sumizyme MC 精製品 Sucrase N 爐濃縮品 Sumizyme AP2 Sumizyme MC Sucrase Ν Sumizyme AP2 Sumizyme MC Sucrase N 本發明品1 本發明品2 本發明品3 本發明品4 本發明品5 本發明品6 本發明品7 本發明品8 比較品1 比較品2 比較品3 比較品4 比較品5 比較品6 比較品7 比較品8 。題¢1¾¾:健aat-^isir-e-ng鎰 q-l-x,ΠΗα^餾—出s^zilng^ajq 。邮 lHH}fl-H 題-mKel,經碘輒1¾¾ 伥 ΐιπ°α 鎰 qq -ιτ- 201215327 如表1所示,對於茶類原料添加蛋白酶、單寧酶、及 添加對於茶葉1克使聚半乳糖醛酸酶活性成爲800U以上 的量並進行萃取獲得的本發明品1至8及比較品6至8, 比起完全不使用酵素的比較品1、添加蛋白酶及單寧酶並 萃取的比較品2、添加蛋白酶、單寧酶及對於茶葉1克小 於800U的聚半乳糖醛酸酶並萃取獲得的比較品3至5當 中任一者,明顯地,過濾時間大幅縮短,作業性提高許多 〇 又’上述過濾時間的縮短,雖然在上述少量的製備時 爲分鐘單位的差異’沒有很大差別,但是一般的萃取物類 的工業生產中,過濾步驟乃限制總行程的作業時間的速度Sumizyme MC (manufactured by Shin-Nippon Chemical Industry Co., Ltd.): l690U/g SuCraseN (manufactured by Mitsubishi Chemical Corporation): 4550 U/g Reference Example 2 Sumizyme AP2 (manufactured by Nippon Chemical Industry Co., Ltd.) l〇〇g (polygalactose measured above) The aldase activity: 1 2400 U/g) was dissolved in 1 000 g of ion-exchanged water, and it was concentrated in a furnace by Vivaflow (registered trademark) 50 VF05P2 (segment molecular weight: 30,000: manufactured by Sartorius Co., Ltd.), and 30 ml of the unpassed portion was recovered, followed by freeze-drying. Reference material 2 (12.0 g: polygalacturonase activity measured above: 8 6 5 00 U/g) was obtained. Example 1 Green tea leaves (manufactured by Chinese steaming method) were added to a solution containing 6 g of sodium ascorbate in 900 g of soft water, and sterilized at 80 ° C for 5 minutes, and cooled to 45 ° C. A tannase (manufactured by Mitsubishi Chemical Food Co., Ltd.: 500 U/g) lg was added thereto, and the mixture was stirred for 15 minutes. Then, Protease Μ (manufactured by Amano Enzyme Co., Ltd.: 5 5 00 U/g) lg and reference product 2 (for 1 g of tea, the polygalacturonase activity measured by the above was 4152 lJ/g) 4.8 g and dissolved, The enzyme treatment was carried out for 8 hours at 40 °C. -18- 201215327 After the enzyme treatment, it is sterilized at 90 ° C for 10 minutes 'cooling to 30 ° C, and then removing the solid residue of the tea leaves with cloth. 'Used on No. 2 filter paper (8 cm) pre-coated with cellulose powder L〇g's Nutsche filter was suction filtered at a fixed pressure (pressure reduction of 13.3 3 KP a) to obtain a clear extract of 825 g (3 minutes and 42 seconds for filtration). The extract was concentrated under reduced pressure to obtain 165.3 g of a concentrated solution of B? This concentrated solution was heat-sterilized at 95 ° C for 3 〇 seconds, and after being filled in a sealed container, it was rapidly cooled to room temperature to obtain a green tea extract of the product 1 of the present invention. Example 2 The amount of the reference product 2 in Example 1 was changed from 4.8 g to 2.4 g (for 1 g of tea leaves, the polygalacturonase activity measured by the above was 2076 U/g), and the same was carried out. Example 1 was carried out in exactly the same operation (the time required for filtration was 4 minutes and 25 seconds) to obtain the product 2 (1 4 9.1 g) of the present invention. Example 3 The amount of reference product 2 in Example 1 was changed from 4.8 g to 1.2 g (for a tea leaf 1 g 'the polygalacturonase activity determined by the above was 1 8 8 U/g), The same operation as in Example i (5 minutes and 5 seconds for filtration) was carried out to obtain the present invention 3 (1 3 8.5 g). Example 4 _ The reference product 2 (4.8 g) in Example 1 was changed to add C e 11 u 1 〇si η PE60 (5.0 g '1 g for tea leaves') as determined by the polygalacturonase activity described above. 1 〇3 〇U/g) 'Besides this, the same operation as in Example i (5 minutes and 21 seconds required for filtration) was obtained, and the present invention 4 (〗 4 6 3 g) was obtained -19-201215327 Example 5 In addition to the addition of the reference product 2 (4.8 g) in Example 1, Sumizyme C (cellulase derived from Trichoderma longibrachiatum manufactured by Shinjuku Chemical Industry Co., Ltd.: 1 500 00/g) was added. 25 g, in addition to The same operation was carried out in Example 1 (the time required for filtration was 3 minutes and 21 seconds), and the present invention 5 (1 6 7 · 3 g) was obtained. Example 6 In addition to the addition of Reference Product 2 (4.8 g) in Example 1, Cellulosin T3 (cellulase derived from Trichoderma reesei: 2600 U/g manufactured by HBI Co., Ltd.) was added in an amount of 0.25 g, except that it was carried out in the same manner as in Example 1. The same operation (3 minutes and 32 seconds for filtration) was carried out to obtain the inventive product 6 (1 65.4 g). Reference Example 3 150 g of Sumizyme MC (manufactured by Nippon Chemical Co., Ltd.) (polygalacturonase activity·1 690 U/g measured as described above) was dissolved in ion-exchanged water (1,500 g) and washed, and centrifuged (4,500 x g, 5 points) The precipitate was recovered and lyophilized to obtain Reference Product 3 (9.8 g of the polygalacturonase activity measured by the above: 20770 U/g). Example 7 The reference product 2 (4.8 g) in Example 1 was changed to the reference material 3 (1 g to the tea leaf, and the polygalacturonase activity measured by the above was 1018 U/g) 4.9 g, except The same operation as in Example 1 was carried out except that the time required for filtration was 4 minutes and 49 seconds, and the present invention 7 (153.2) was obtained. Reference Example 4 SucraSeN (manufactured by Mitsubishi Chemical Foods Co., Ltd.) i00g (polygalacturonase activity of the above-mentioned measurement -20-201215327: 4550 U/g) was dissolved in ion-exchanged water l〇〇〇g to Vivaflow (registered trademark) 50VF05P2 (different molecular weight: 30,000: manufactured by Sartorius Co., Ltd.) was subjected to ultrafiltration and concentration, and 25 ml of a non-passing portion was collected, followed by lyophilization to obtain a reference product 4 (10.0 g, polygalacturonase activity measured by the above: 32,000 U) /g). Example 8 The reference product 2 (4.8 g) in Example 1 was changed to the reference material 4 (relative to 1 g of tea leaves, the polygalacturonase activity measured by the above was 1 600 U/g) 5.0 g, except Other than the same operation as in Example 1 (the time required for filtration was 4 minutes and 16 seconds), the product of the present invention 8 (1 5 5.4 g) was obtained. Comparative Example 1 In Example 1, no enzyme was used at all, and otherwise The same operation as in Example 1 (the time required for filtration was 1 〇 25 minutes) was obtained to obtain Comparative Product 1 (66.8 g). Comparative Example 2 In the same manner as in Example 1, except that the reference product 2 (4.8 g) was used, the same operation as in Example 1 (the time required for filtration was 9 minutes and 57 seconds) was obtained, and Comparative Product 2 (72.9 g) was obtained. Comparative Examples 3 to 5 The reference product 2 (4.8 g) in Example 1 was changed to 2.0 g of Sumizyme AP2 (manufactured by Nippon Chemical Industry Co., Ltd.) (for 1 g of Zhu Ye, the polygalactosaldehyde measured by the above) Acid enzyme activity was 24 8 U/g), Sumizyme MC (manufactured by Shin-Nippon Chemical Industry Co., Ltd.) 2.0 g (for a tea leaf 1 g, the polygalacturonase activity measured by the above was 33.8 U/g), SuCraSeN (Mitsubishi 2.0 g (manufactured by Chemical Foods Co., Ltd.) (1 g of tea, the polygalacturonase activity measured by the above -21 - 201215327 is 9 1 U/g), except that the same operation as in Example 1 was carried out completely. Comparative products 3 to 5 (the time and yield of filtration, and other measurement combinations are shown in Table 1 below). Comparative Examples 6 to 8 (1 gram of polygalactose for tea leaves by using a large amount of commercially available pectinase) Example of the aldehyde acidase activity of 8000 U or more) The reference product 2 (4.8 g) in Example 1 was changed to use Sumizyme AP2 (manufactured by Nippon Chemical Industry Co., Ltd.) 8. 〇g (for tea 1 g, The polygalacturonase activity measured by the above was 992 U/g), and Sumizyme MC (manufactured by Shin-Nippon Chemical Industry Co., Ltd.) 5〇. g (for 1 g of tea, the galacturonase activity measured by the above is 845 U/g), Sucrase N (manufactured by Mitsubishi Chemical Foods Co., Ltd.) 20 g (for 1 g of tea, the polygalacturonase measured by the above) The activity was 910 U/g), and the same operation as in Example 1 was carried out completely. 'Comparative products 6 to 8 were obtained (the time and yield of filtration, and other measurement 値' are collectively shown in Table 1 below). Component Analysis For the inventive products 1 to 8 and comparative products 1 to 8, the concentration (% by mass) of tannin, amino acid and galacturonic acid was measured. Determination method Amino acid: Amino acid automatic analyzer Tannin: iron tartrate galacturonic acid: high-speed liquid chromatography (HPLC) method The yields of the inventive products 1 to 8 and comparative products 1 to 8 from green tea raw materials And the determination of each component 浓度 (concentration) and the time used for filtration, as shown below. -22- 201215327 Filtration time required 3 minutes 42 seconds 4 minutes 25 seconds 5 minutes 52 seconds 5 minutes 21 seconds 3 minutes 21 seconds 1 3 minutes 32 seconds L --- 1 1 4 minutes 49 seconds 4 minutes 16 seconds 10 minutes 25 seconds 9 minutes 57 seconds 7 minutes 12 seconds 8 minutes 16 seconds 7 minutes 57 seconds 4 minutes 25 seconds 4 minutes 56 seconds 4 minutes 47 seconds Galacturonic acid concentration (%) 0.870 0.776 0.661 ii 0.674 0.921 0.943 0.641 0.665 0.018 0.061 0.348 0.163 0.225 0.521 0.374 0.456 Tannin concentration (%) 8.51 8.96 9.32 8.85 , 7.91 8.09 9.02 9*13 17.82 15.32 12.34 14.68 13.21 8.89 5.62 6.54 Amino acid concentration (%) CN rn 3.38 3.45 3.32 | 3.14 00 cn 3.21 1 3.32 CN 5.57 4.53 5.02 4.47 3.18 2.01 2.68 Extract yield (g) 165.3 149.1 138.5 146.3 167.3 165.4 142,3 66.8 72_9 103.5 83.1 96.5 158.5 225.2 175.6 Pectin enzyme sweep «-Η nml ΠΠΙΓ |1 4152 2076 1038 1030 i 4152 1 41 52 1 1018 1600 Unused Unused 248 33,8 992 910 og 2Wei 3 M Gallium _ Diluted S Another 嫛 莉 莉 s &&<s<N 〇wi 00 inch 1 〇〇 — 1 〇 〇〇(Ν 〇(N 〇fN 〇〇〇50.0 20.0 习 习 86 86500 86500 86500 20600 86500 1 86500 1 1 20770 32000 12400 1690 4550 12400 1690 4550 Enzyme name 2 ng < ^ I* ε熙 2ng Is s囤Sag em ! 囤ε囤3豳Cellulosin PE60 βΜ εForging 艮Ν S Sng gM !鹪s circumference 5豳Cellulosin T3 Sumizyme MC Fine product Sucrase N Furnace concentrate Sumizyme AP2 Sumizyme MC Sucrase Ν Sumizyme AP2 Sumizyme MC Sucrase N The present invention 1 product 2 invention product 3 product product 4 invention product 5 invention product 6 invention product 7 invention product 8 comparison product 1 comparison product 2 comparison product 3 comparison product 4 comparison product 5 Comparison product 7 comparison product 8 . Title ⁄13⁄43⁄4: Jian aat-^isir-e-ng镒 q-l-x, ΠΗα^ distillate-out s^zilng^ajq. lHH}fl-H title-mKel, iodine 辄 13⁄43⁄4 伥ΐιπ°α 镒qq -ιτ- 201215327 As shown in Table 1, add protease, tannin, and add 1g for tea to the tea raw material The present inventions 1 to 8 and the comparative products 6 to 8 obtained by extracting the lacturonanase amount in an amount of 800 U or more, compared with the comparative product in which the enzyme is not used at all, the protease and the tannin, and the comparative product are extracted. 2. Adding protease, tannase and any of the comparative products 3 to 5 obtained by extracting 1 g of polygalacturonase of less than 800 U of tea, obviously, the filtration time is greatly shortened, and the workability is improved a lot. 'The above-mentioned shortening of the filtration time, although the difference in minute units in the above-mentioned small preparations is not greatly different, but in the industrial production of general extracts, the filtration step limits the operation time of the total stroke.

V 的步驟,於工業化大量製造(數噸至數十噸)時,可預想會 大幅改善。 又’成分方面如表1所示,比起完全不使用酵素的比 較品1,使用蛋白酶及單寧酶的比較品2至8及本發明品 1至8,胺基酸的含量均有大幅增加。 對於綠茶原料添加蛋白酶、單寧酶、及相對於茶葉i 克爲800U以上的聚半乳糖醛酸酶而進行萃取獲得的本發 明品1至8及比較品6至8,比起對於綠茶原料僅添加蛋 白酶與單寧酶而萃取獲得的比較品2,萃取物(Bx4 8。)的產 率增加達約2倍’能以極高產率獲得萃取物。又,除了本 發明品1使用的酵素以外更使用來自於長枝木黴的的纖維 素酶而獲得的本發明品5及使用來自於里氏木黴的纖維素 -24- 201215327 酶而獲得的本發明品6,萃取物產率更爲增加。 本發明品2及3減少本發明品1的聚半乳糖醛酸酶的 使用量者’卒取物(Bx48。)的產率比起本發明品1雖少了 右干’但是若比起比較品2至5,增加約1 .3至約2倍, 可知利用本發明的方法’來自於茶類原料的可溶性固體成 分的產率大幅增加。 完全不使用酵素的比較品1幾乎不含半乳糖醛酸,又 ’對於綠茶原料僅使蛋白酶及單寧酶作用而獲得的比較品 2 ’半乳糖醛酸僅有約〇.〇6質量%,但是添加果膠酶並萃 取獲得的比較品3至8及本發明品丨至8,含有半乳糖醛 酸〇 . 1 6質量%至〇 . 9 2質量%。其中,解明:半乳糖醛酸濃 度會伴隨著所添加的聚半乳糖醛酸酶活性單位增加而增加 。對於茶葉1克添加800U以上的聚半乳糖醛酸酶而萃取 獲得的本發明品1至8,萃取物中的半乳糖醛酸濃度爲 0 · 6 6質量%至〇 _ 9 4質量%,含量特別多^ 另一方面’本發明品1至8與比較品3至5相比,胺 基酸濃度、單寧濃度稍低。但是,此可認爲是由於細胞壁 的分解成分的增加,使得胺基酸濃度及單寧濃度相對降低 〇 又,對於茶類原料添加蛋白酶、單寧酶、及對於茶葉 1克添加聚半乳糖醛酸酶活性小於20000U/g的酵素製劑 其添加量爲使聚半乳糖醛酸酶活性成爲8 00U以上之量, 並萃取獲得的比較品6至8,雖然固體成分產率多,但是 -25- 201215327 胺基酸、單寧、半乳糖醛酸的各濃度,比起本發明品1至 8相對較低,據認爲是茶類萃取物中含有來自於酵素製劑 中的賦形劑等的成分。 下表2記載本發明品丨.至8及比較品1至8之從綠茶 原料而來的可溶性固體成分產率及各成分的產率(由表1 計算而得)。 -26- 201215327 (%)§經襲Ίέ 并馨震賊達 91.1 S.0 660 寸-一 9-1 16Ό 96Ό 5.0 寸00 92 -.0 so ε·0 i 08ΌThe steps of V are expected to improve significantly when industrially mass-produced (several tons to tens of tons). Further, as shown in Table 1, the contents of the amino acid were greatly increased compared with the comparative product 1 in which the enzyme was not used at all, the comparative products 2 to 8 using the protease and the tannin, and the products 1 to 8 in the present invention. . The present inventions 1 to 8 and the comparative products 6 to 8 obtained by extracting green tea raw materials with protease, tannase, and polygalacturonase of 800 U or more, compared with green tea raw materials only Comparative product 2 obtained by extracting protease and tannase, and the yield of the extract (Bx4 8) was increased by about 2 times', and the extract was obtained in a very high yield. Further, in addition to the enzyme used in the product 1 of the present invention, the present invention 5 obtained by using a cellulase derived from Trichoderma longissima and a cellulose-24-201215327 enzyme obtained from Trichoderma reesei are used. In the present invention 6, the yield of the extract is further increased. In the products 2 and 3 of the present invention, the use amount of the polygalacturonase of the present invention 1 is reduced, and the yield of the 'batch (Bx48.) is less than that of the present invention 1 but the right is dry, but if compared The product 2 to 5 was increased by about 1.3 to about 2 times, and it was found that the yield of the soluble solid component derived from the tea raw material was greatly increased by the method of the present invention. The comparative product 1 which does not use the enzyme at all is almost free of galacturonic acid, and the comparative product 2 'galacturonic acid obtained by the action of only the protease and the tannin enzyme for the green tea raw material is only about 〇.〇6 mass%. However, the pectinase was added and the obtained comparative products 3 to 8 and the present invention were added to 8 and contained galacturonate. 16% by mass to 〇.92% by mass. Among them, it is explained that the concentration of galacturonic acid increases as the unit of polygalacturonase activity added increases. For the present inventions 1 to 8 obtained by extracting 1 g of polygalacturonase of 800 U or more, the concentration of galacturonic acid in the extract is 0 · 66% by mass to 〇 _ 9.4% by mass. In particular, the present invention has a slightly lower concentration of amino acid and tannin than the comparative products 3 to 5. However, this is considered to be due to an increase in the decomposition component of the cell wall, resulting in a relative decrease in the concentration of the amino acid and the concentration of tannin. In addition, proteases, tannins are added to the tea raw material, and polygalactosaldehyde is added to 1 g of the tea leaves. The enzyme preparation having an acid enzyme activity of less than 20,000 U/g is added in an amount such that the polygalacturonase activity is more than 800 U and the comparative products 6 to 8 are obtained, although the solid content yield is high, but -25- 201215327 The respective concentrations of amino acid, tannin, and galacturonic acid are relatively lower than those of the present inventions 1 to 8, and it is considered that the tea extract contains ingredients derived from excipients and the like in the enzyme preparation. . Table 2 below shows the yields of soluble solid components and the yields of the respective components (calculated from Table 1) of the green tea raw materials of the products of the present invention, to 8 and Comparative Products 1 to 8. -26- 201215327 (%) §After attack and Xin Zhen thief 91.1 S.0 660 inch-a 9-1 16Ό 96Ό 5.0 inch 00 92 -.0 so ε·0 i 08Ό

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Ds糴靡鹦围® 3JV ^^Z!S3S uixziums ng糴靡鹦顆豳 NJV i^zlsns nnDi us3UIXZJUIns 昭躍_鹪顆靼 zions usi^2!sns zs2°ns 2vus^z!is υ2ωε^2!εη§ zl3ns CN嗽 寸唣誃餾件 卜昭睬鎞怜 一昭鎰- ^nnns ^ nnni 寸昍鎰- ^ Dnni 9Ds□鎰- ^ ΠΠΠΙ 00¾□鎰- 。卿|出仵純韙0酬,韙腾11¾¾伥I昭鎰- \ 201215327 如表2所示,比起完全不使用酵素的比較品1,添加 蛋白酶及單寧酶並萃取獲得的比較品2至8及本發明品1 至8,從茶葉而來的胺基酸產率增加到4至5倍。又,添 加蛋白酶與單寧酶以外更對於茶葉1克添加8 OOU以上的 聚半乳糖醛酸酶並萃取獲得的本發明品1至8及比較品6 至8,比起添加蛋白酶、單寧酶、及對於茶葉1克小於 8 0 0U的聚半乳糖醛酸酶並萃取獲得的比較品3至5,從茶 葉而來的胺基酸產率提高約2成。 又,關於從茶葉而來的單寧產率,於除了蛋白酶、單 寧酶更添加聚半乳糖醛酸酶並萃取獲得的本發明品1至8 及比較品3至8,從茶葉而來的單寧產率隨著固體成分產 率增加而增加。尤其是,於添加蛋白酶、單寧酶以外更添 加對於茶葉1克爲800U以上的聚半乳糖醛酸酶而萃取獲 得的本發明品1至8及比較品6至8中,從茶葉而來的單 寧產率相對於茶葉質量爲約丨2至14%,比起完全不使用 酵素的比較品1及使用蛋白酶及單寧酶的比較品2,產率 提筒約2成。 本發明品1至8及比較品6至8,從茶葉而來的半乳 糖醛酸產率爲約0.80%至1.54%,可知生成多量半乳糖醛 酸。 另一方面,比較品6至8使用與本發明品3、4、7爲 同程度的聚半乳糖醛酸酶活性單位,雖然半乳糖醛酸產率 爲同程度’但是固體成分產率比起本發明品3、4、7爲多 -28- 201215327 ’特別多的是添加的酵素製劑的絕對量多的比較品7,其 次是比較品8 °如此’可料想比較品6至8含有多量來自 於酵素製劑中的賦形劑等的成分。 官能評價 將本發明品1至8及比較品1至8以離子交換水稀釋 成1 6 0倍(B X 0 · 3。)後’請經過良好訓練的} 〇名品評員進行 官能評價。評價方法,係就苦澀味、甘味、鮮味、均衡性 ,各以:非常良好:1〇分、良好分、稍好:6分、稍 差:4分、差:2分、非常差:〇分,進行官能評價、又 ,將評語記錄下來。其平均分數及評語的平均內容記載於 下表3。 -29-Ds籴靡鹦鹉围® 3JV ^^Z!S3S uixziums ng籴靡雀豳豳NJV i^zlsns nnDi us3UIXZJUIns 昭跃_鹪片靼zions usi^2!sns zs2°ns 2vus^z!is υ2ωε^2!εη § zl3ns CN嗽 inch 唣誃 件 卜 睬鎞 镒 镒 镒 ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^卿|Exporting pure 韪0 reward, 韪腾113⁄43⁄4伥I 镒 镒 - \ 201215327 As shown in Table 2, compared with the comparison product 1 which does not use enzyme at all, add protease and tannin and extract the comparative product 2 to 8 and the inventive products 1 to 8, the yield of amino acids derived from tea leaves was increased to 4 to 5 times. Further, in addition to the protease and the tannase, the polygalacturonase of 8 OOU or more is added to 1 g of the tea leaves, and the inventive products 1 to 8 and the comparative products 6 to 8 obtained by extraction are compared with the addition of protease and tannase. And for the comparison products 3 to 5 obtained by extracting 1 g of the polygalacturonase of less than 800 U of tea, the yield of amino acid from the tea leaves is increased by about 20%. Further, regarding the tannin yield from the tea leaves, the present inventions 1 to 8 and the comparative products 3 to 8 obtained by extracting polygalacturonase in addition to protease and tannin are derived from tea leaves. The tannin yield increases as the solid component yield increases. In particular, in addition to the addition of a protease or a tannase, the present inventions 1 to 8 and comparative products 6 to 8 obtained by extracting 1 g of polygalacturonase having 1 g of tea leaves are derived from tea leaves. The yield of tannin is about 2 to 14% with respect to the quality of the tea. Compared with the comparative product 1 which does not use the enzyme at all and the comparative product 2 which uses the protease and the tannin, the yield is about 20%. In the products 1 to 8 and the comparative products 6 to 8, the yield of galacturonic acid derived from tea leaves was about 0.80% to 1.54%, and it was found that a large amount of galacturonic acid was formed. On the other hand, Comparative Products 6 to 8 used the same degree of polygalacturonase activity units as in the present inventions 3, 4, and 7, although the yield of galacturonic acid was the same degree, but the solid content yield was compared. The present invention products 3, 4, and 7 are more than -28-201215327 'particularly the comparative product 7 having a larger absolute amount of the added enzyme preparation, and the second is the comparative product 8 °. 'It is expected that the comparative products 6 to 8 contain a large amount of A component of an excipient or the like in an enzyme preparation. Functional evaluation The inventive products 1 to 8 and the comparative products 1 to 8 were diluted with ion-exchanged water to 160 × (B X 0 · 3), and then [well-trained] annotated product evaluation. The evaluation method is based on bitterness, sweetness, umami, and balance. Each is very good: 1 point, good score, slightly better: 6 points, slightly worse: 4 points, difference: 2 points, very poor: 〇 We perform faculty evaluation and record the comment. The average score and the average content of the reviews are shown in Table 3 below. -29-

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2 [5 m Κ- #i 5? 黎 32' 磨。 賴 ,誃 # K-扭岷 -51 # -戡坻 S _ 袼湘 邀蚺 蚺溫 7 <n-f 联 腺 扭 i 验。 s嵌 枨輯 蕖湘 槪腺。 151 Igw 繼五。 —五娌 ng嵌_ 鎰駿要 gj。0 救珀 S脒 掩湿 邀神! S嵌 埘駿 Μ 磨m丨。 «THW 龌ί〇痤 r? ^ 5? 鍇嵌- m Ή s脒 蕖蚺 S泜 乸駿 P 5〇1 〇 械-糊 m^m ΐπ礙 [Ε1,迎 titi. MZ. 翻篮" 躲33 S戗 格歲 蕖蚺 S # 鹋駿 m m 睡ml。 枨TDW m^rn 蹈扭凝 t? ·扨 ?m4 4^. 锻篮" s球痤 掩面:S1 si * - S跑迤 圈51迤 « - ίπ Μ嵌S。 齒运1¾她1 向·瞰譃 韹迤脈擗 漉袼胡 S踏痤 枨面圯 邊* -S跑迤 頃埋世 械-耘 面迤S 齒运1¾ [?,瞰。 媸迤脈籼 戡掩劫 s截痤 掩面驭 s蹈坻 圈51迤 枨-耘 面#S 跑長挪; 1?,酿。 媸迤脈糊 ο 1 出 -Β- Η jm (N <N CN — 〇〇 1〇 v〇 OS — Ό\ (N — VO ν〇 00 »ri ON 寸 寸 卜 'd ν〇 卜 ν〇 (N v〇 cn 寸 »ri 00 七 ^r cn — l〇 VO m (si rf vS 〇〇 »ri CN in m … 1—Η rn 〇 S 昍 4Κ 旺 赵 张 oo 艺 00 cn cn 5: 〇 »n s 〇 OS 〇 iri ο (Ν ο CN 〇 (N 〇 00 o 〇 Ο 1 ro Ο 窆 v〇 >n 〇 v〇 ng 耀 §喪> <yi S3 2 C <υ ε ε 泛 〇 5 ❹ 6 泛 S z 0 s u 1 < <υ ! 1 u 2 0> B B <υ ϋ t& •CO m m 倒1 螂 00 ng 餾 ^-» ng 鎰 JJ CN ng 鎰 m ng 鎰 jJ a· ng 鎰 Λ3 »n u JlJ ο ng 麄 卜 ng ii a 00 Ππ β 〇J J屮、 伥 ng 鎰 -Ie- 201215327 如表3所示’完全不使用酵素的比較品1,獲得評價 爲:綠茶的鮮味、甘味弱’具有強烈苦澀味,關於苦澀味 、甘味、鮮味、均衡性的評價均低。又’對於綠茶原料僅 添加蛋白酶與單寧酶並萃取獲得的比較品2,比起比較品 1,獲得以下評價:綠茶的鮮味強烈,苦澀味比起比較品 1爲弱,但是仍相當強烈’欠缺甘味,關於苦澀味、甘味 、鮮味、均衡性的評價均比比較品1高出一些。 相對於此,除了蛋白酶與單寧酶以外,更將具有聚半 乳糖醛酸酶活性爲20000U/g以上之酵素製劑以對於茶葉 1克使聚半乳糖醛酸酶活性成爲800U以上之量添加並萃 取獲得的本發明品1至8 ’獲得評價爲:綠茶的鮮味、 甘味、濃味強烈,苦澀味清淡且輕微,整體的風味均衡性 良好,爲如高級抹茶的呈味’爲極高評價。 另一方面,添加蛋白酶與單寧酶以外更對於茶葉1克 添加小於800U之聚半乳糖醛酸酶並萃取獲得的比較品3 至5,獲得的評價爲:雖可感到某個程度的綠茶的鮮味 、甘味,但苦澀味有點突出,均衡性差,比起本發明品1 至8的評價差。 又,除了添加蛋白酶與單寧酶以外,更將聚半乳糖醛 酸酶活性小於20000U/g的酵素製劑以對於茶葉1克使聚 半乳糖醛酸酶活性成爲800U以上的量添加並萃取獲得的 比較品6至8,獲得之評價爲:雖可感到某個程度的綠茶 的鮮味、甘味,但是會感到與茶異質的甘味及雜味,均衡 -32- 201215327 性有點差,尤其添加的酵素製劑的絕對量多的比較品7及 比較品8 ’會強烈感到與茶爲異質的甘味及雜味,均衡性 差,風味差。 成分間的比率 半乳糖醛酸給人像是抹茶等高級茶的印象的軟黏,又 有使人耳目一新的酸味’因此推測具有苦澀味遮蔽、異臭 遮蔽、稠感賦予等的作用’推測半乳糖醛酸的增加爲本發 明的茶類萃取物的甘味、濃味、鮮味等的重要要因之—。 亦即’除了茶類中原本含有的胺基酸或由於蛋白酶處理而 分解生成的胺基酸的鮮味或甘味以外,半乳糖醛酸還發揮 遮蔽效果’預想會將兒茶素的苦澀味遮蔽,並進一步將由 於單寧酶處理生成的没食子酸的酸味或苦味遮蔽,使呈味 改善。 由表1至表3所示之結果,可認爲:本發明品中,半 乳糖醛酸比起其他成分,含量相對較多,因此,就本發明 品1至8及比較品1至8 ’計算:(a)以茶類萃取物的總固 體成分(以Bjc換算計)爲基準的半乳糖醛酸量(質量)、(b) 半乳糖醛酸/單寧的質量比、(c)半乳糖醛酸/胺基酸的質量 比。結果如下表4。 -33- 2 1X20 3 -_-_-_-ΓΠΠ-.- 5 寸嗽 S27 m 氍 m 鹅 0.279 0.230 0.192 0.203 0.293 0.297 0.200 0.200 0.012 0.011 0.077 0.032 0.050 0.164 0.186 0.170 半乳糖醛酸/單寧 0.102 0.087 _ 0.076 0.116 0.117 0.071 「0.073 0.001 0.004 0.028 0.011 0.017 0.059 0.067 0.070 半乳糖醛酸/固體成分(%) 1.813 1.617 1.377 1.404 1.919 1.942 1.335 1.385 0.037 0.127 0.725 0.340 0.469 1.085 0.779 0.950 果膠酶 -螂 mm P 4152 2076 1038 1030 4152 1 4152 1 1018 1600 未使用 未使用 00 33.8 〇\ <N Ο σ\ 00 910 對於茶葉l〇〇g的酵素製 劑的添加量(g) 00 — 寸 <N* (N 〇 »n 〇〇 寸· < 00 1 Os 〇 〇 (N 〇 (N 〇 fN ο 00 50.0 20.0 12400 1690 4550 12400 1690 4550 鹅ώ 3V B 并#! him 账氍 豳 86500 86500 86500 20600 86500 1 86500 1 20770 [ 32000 _里 酵素名 § ng I驅 S'鹌 1强 CO齒 § ng < m |l 6镅 <N η |ϋ g围 Cellulosin PE60 g ng S戴 泛鹪 E镯 〇 〇 1 ε § ag (U耀 βμ S'鹪 •画辑 Cellulosin T3 1 Sumizyme MC 精製品 Sumizyme AP2 Sumizyme MC Sucrase N Sumizyme ΑΡ2 Sumizyme MC Sucrase N 1 本發明品1 本發明品2 本發明品3 本發明品4 本發明品5 本發明品6 本發明品7 本發明品8 比較品1 比較品2 比較品3 比較品4 比較品5 比較品ό 比較品7 比較品8 _κ. 。韙酬^:題»»|-昍^^-6-0§^^'昭誃餾li>s^rilng鎰五 。聛—出子Η題{Π酬,鍵娜酹還伥—q 201215327 如表4所示’風味獲得極高評價的本發明品1至8, (a)以茶類萃取物的總固體成分(以Bx換算計)爲基準的半 乳糖醛酸的含量(質量)爲1.3至2.0%、(b)半乳糖醛酸/單 寧的質量比爲0.07至0.12、(c)半乳糖醛酸/胺基酸的質量 比爲0.19至0.30的範圍內。 另一方面’比較品1至5,(a)以茶類萃取物的總固體 成分(以Bx換算計)爲基準的半乳糖醛酸的含量(質量)小於 0.8%、(b)半乳糖醛酸/單寧的質量比小於〇.〇3、(c)半乳糖 醛酸/胺基酸的質量比小於0.0 8。 又’比較品6至8,(a)以茶類萃取物的總固體成分( 以BX換算計)爲基準的半乳糖醛酸的含量(質量)爲0.78至 1.1%、(b)半乳糖醛酸/單寧的質量比爲0.059至0.07、(〇 半乳糖醛酸/胺基酸的質量比爲0. 164至0.186,均比起本 發明品1至8稍低。 因此,可推測由於該等差異帶來本發明獲得的茶類萃 取物的甘味、濃味、鮮味等。 又,就其數値範圍,從上述實施例,可認爲若爲(a) 以茶類萃取物的總固體成分(以Bx換算計)爲基準的半乳 糖醛酸的含乳量(質量)爲1.1至5%、(b)半乳糖醛酸/單寧 的質量比爲0.04至0.8,且(c)半乳糖醛酸/胺基酸的質量 比爲〇.〇8至0.8 ;較佳爲(a)以茶類萃取物的總固體成分( 以Bx換算計)爲基準的半乳糖醛酸的含量(質量)爲1.2至 4%、(b)半乳糖醛酸/單寧的質量比爲0.06至0.4,且(c)半 -35- 201215327 乳糖醛酸/胺基酸的質量比爲0.14至〇.6;更佳】 類萃取物的總固體成分(以Bx換算計)爲基準的 酸的含量(質量)爲1 .3至3%、(b)半乳糖醛酸/單 比爲0.07至0.2’且(c)半乳糖醛酸/胺基酸的: 〇·19至0.4,則能帶來本發明的效果而來的呈味。 【圖式簡單說明】 4nt, 撕0 【主要元件符號說明】 無。 (a)以茶 乳糖醛 的質量 量比爲 -36-2 [5 m Κ- #i 5? 黎 32' grinding. Lai, 誃 # K-扭岷 -51 # -戡坻 S _ 袼 蚺 蚺 蚺 7 7 7 7 7 7 7 7 7 7 7 7 7 7 7 7 7 7 7 7 7 7 7 7 7 7 7 7 7 7 7 7 7 7 7 7 7 7 7 7 7 7 7 7 7 7 7 7 7 7 7 7 7 7 7 7 7 s embedded 枨 蕖 蕖 槪 槪 槪 槪. 151 Igw follows five. —五娌 ng embedded _ 镒 要 want gj. 0 救珀 S脒 Covering the wet invites God! S embedded 埘 Μ 磨 grinding m丨. «THW 龌ί〇痤r? ^ 5? 锴 - - m Ή s脒蕖蚺S泜乸骏 P 5〇1 -机械-糊m^m ΐπ障碍[Ε1,迎titi. MZ. 翻篮" 躲33 S 戗 蕖蚺 蕖蚺 S # 鹋 mm mm sleep ml.枨TDW m^rn 扭 扭 t? ·扨?m4 4^. Forged basket" s ball 掩 Cover: S1 si * - S 迤 迤 迤 51迤 « - ίπ S S. Tooth transport 13⁄4 her 1 direction · 譃 譃 韹迤 擗 漉袼 S S S S S S S - - - - - - - - - - - - - - - - - - - - - - - - - - - - - - - - - - - - - - -媸迤 籼 戡 戡 戡 s s 痤 痤 掩 掩 s s 迤 迤 迤 迤 迤 迤 迤 迤 迤 迤 迤 迤 迤 迤 迤 迤 迤 迤 迤 迤 迤 迤 迤 迤 迤 S S S S媸迤脉糊ο 1 出-Β- Η jm (N <N CN — 〇〇1〇v〇OS — Ό\ (N — VO ν〇00 »ri ON 寸 inchb'd ν〇卜ν〇(N V〇cn inch»ri 00 七^r cn — l〇VO m (si rf vS 〇〇»ri CN in m ... 1—Η rn 〇S 昍4Κ 旺赵张oo 00 cn cn 5: 〇»ns 〇 OS 〇iri ο (Ν ο CN 〇(N 〇00 o 〇Ο 1 ro Ο 窆v〇>n 〇v〇ng 耀 丧 &><yi S3 2 C <υ ε ε 〇 〇 5 ❹ 6 Pan S z 0 su 1 <<υ ! 1 u 2 0> BB <υ ϋ t& •CO mm 1 螂 00 ng Distillation ^-» ng 镒JJ CN ng 镒m ng 镒jJ a· ng 镒Λ3 »nu JlJ ο ng 麄 ng ii a 00 Ππ β 〇JJ屮, 伥ng 镒-Ie- 201215327 As shown in Table 3, 'Comparative product 1 without enzymes was evaluated as: fresh and sweet taste of green tea Weak 'has a strong bitter taste, and has low evaluations on bitterness, sweetness, umami, and balance. Also, 'Comparative product 2 obtained by adding only protease and tannase to green tea raw materials, compared with Comparative Product 1, obtained The following evaluation: green tea The umami taste is strong, the bitterness is weaker than the comparison product 1, but it is still quite strong. 'Lack of sweet taste. The evaluation of bitterness, sweetness, umami and balance is higher than that of the comparative product 1. In contrast, In addition to the protease and the tannase, the enzyme preparation having a polygalacturonase activity of 20,000 U/g or more is added and extracted in an amount of 1 gram or more of the polygalacturonase activity of the tea leaves. The products 1 to 8' were evaluated as follows: the umami, sweet and strong taste of green tea is strong, the bitter taste is light and slight, and the overall flavor balance is good, which is highly praised for the taste of high-grade matcha. On the other hand, Adding proteases and tannins to the tea 1 g of less than 800 U of polygalacturonase and extracting the comparative products 3 to 5, the evaluation is: although a certain degree of green tea umami, sweet taste However, the bitter taste is somewhat prominent, and the balance is poor, which is inferior to the evaluation of the present invention 1 to 8. Further, in addition to the addition of the protease and the tannase, the enzyme having a polygalacturonase activity of less than 20,000 U/g is further used. The comparative product 6 to 8 obtained by adding and extracting the polygalacturonase activity to an amount of 800 U or more for 1 g of the tea was evaluated as follows: although the taste and sweetness of the green tea were felt to some extent, I will feel the sweetness and miscellaneous taste of the tea, and the balance -32- 201215327 is a little bit worse. In particular, the comparative product 7 and the comparative product 8' which have a large absolute amount of the enzyme preparation will strongly feel the sweet taste and the miscellaneous taste of the tea. The balance is poor and the flavor is poor. The ratio of galacturonic acid to the portrait is soft and sticky to the impression of high-grade tea such as Matcha, and it has a refreshing sour taste. Therefore, it is presumed to have a bitter taste mask, an odor mask, a thick feeling, etc. The increase of acid is an important factor for the sweet taste, rich taste and umami taste of the tea extract of the present invention. That is, in addition to the umami or sweet taste of the amino acid originally contained in the tea or the amino acid which is decomposed by the protease treatment, the galacturonic acid also exerts a masking effect, which is expected to obscure the bitterness of the catechin. Further, the sour taste or bitterness of gallic acid produced by the tannase treatment is further shielded, and the taste is improved. From the results shown in Tables 1 to 3, it can be considered that, in the present invention, galacturonic acid is relatively more abundant than other components, and therefore, the present inventions 1 to 8 and comparative products 1 to 8 ' Calculation: (a) galacturonic acid amount (mass) based on the total solid content of the tea extract (in terms of Bjc), (b) mass ratio of galacturonic acid/tannin, (c) half The mass ratio of lacturonic acid/amino acid. The results are shown in Table 4 below. -33- 2 1X20 3 -_-_-_-ΓΠΠ-.- 5 inch 嗽S27 m 氍m goose 0.279 0.230 0.192 0.203 0.293 0.297 0.200 0.200 0.012 0.011 0.077 0.032 0.050 0.164 0.186 0.170 galacturonic acid / tannin 0.102 0.087 _ 0.076 0.116 0.117 0.071 "0.073 0.001 0.004 0.028 0.011 0.017 0.059 0.067 0.070 galacturonic acid / solid content (%) 1.813 1.617 1.377 1.404 1.919 1.942 1.335 1.385 0.037 0.127 0.725 0.340 0.469 1.085 0.779 0.950 Pectinase-螂mm P 4152 2076 1038 1030 4152 1 4152 1 1018 1600 Unused unused 00 33.8 〇\ <N Ο σ\ 00 910 Addition amount of enzyme preparation for tea l〇〇g (g) 00 — inch <N* (N 〇» n 〇〇··< 00 1 Os 〇〇(N 〇(N 〇fN ο 00 50.0 20.0 12400 1690 4550 12400 1690 4550 Goose 3V B and #! him Account 86500 86500 86500 20600 86500 1 86500 1 20770 [ 32000 _ _ _ _ _ _ _ _ _ _ _ _ _ _ U Yaoβμ S'鹪•画画Cellulosin T3 1 Sumizyme MC 精品Sum Izyme AP2 Sumizyme MC Sucrase N Sumizyme ΑΡ2 Sumizyme MC Sucrase N 1 Inventive product 1 Inventive product 2 Inventive product 3 Inventive product 4 Inventive product 5 Inventive product 6 Inventive product 7 Inventive product 8 Comparative product 1 Comparative product 2 Comparison product 3 Comparison product 4 Comparison product 5 Comparison product ό Comparison product 7 Comparison product 8 _κ. 韪 Reward ^: Question »»|昍昍^^-6-0§^^' Zhao 誃 誃 & s s ril ril镒 five.聛 出 出 出 出 { { { { { { { { 2012 2012 2012 2012 2012 2012 2012 2012 2012 2012 2012 2012 2012 2012 2012 2012 2012 2012 2012 2012 2012 2012 2012 2012 2012 2012 2012 2012 2012 2012 2012 2012 2012 2012 2012 2012 2012 2012 2012 2012 2012 2012 2012 2012 2012 2012 2012 2012 2012 2012 2012 2012 2012 2012 2012 2012 2012 2012 2012 2012 2012 2012 2012 2012 2012 2012 2012 2012 2012 2012 2012 2012 2012 2012 2012 2012 2012 2012 2012 2012 2012 2012 2012 2012 2012 The content (mass) of galacturonic acid based on Bx is 1.3 to 2.0%, (b) the mass ratio of galacturonic acid/tannin is 0.07 to 0.12, and (c) galacturonic acid/amine The mass ratio of the base acid is in the range of 0.19 to 0.30. On the other hand, 'Comparative Products 1 to 5, (a) The content (mass) of galacturonic acid based on the total solid content (in terms of Bx) of the tea extract is less than 0.8%, (b) galacturaldehyde The mass ratio of acid/tannin is less than 〇.〇3, and the mass ratio of (c) galacturonic acid/amino acid is less than 0.08. Further, 'Comparative Products 6 to 8, (a) the content (mass) of galacturonic acid based on the total solid content (in terms of BX) of the tea extract is 0.78 to 1.1%, (b) galacturaldehyde The mass ratio of the acid/tannin is 0.059 to 0.07, and the mass ratio of the galacturonic acid/amino acid is 0.164 to 0.186, which is slightly lower than the products 1 to 8 of the present invention. Therefore, it is presumed that The difference is the sweet taste, the rich taste, the umami taste, etc. of the tea extract obtained by the present invention. Further, from the above examples, it can be considered that (a) the total amount of the tea extract is The milk content (mass) of the galacturonic acid based on the solid content (in terms of Bx) is 1.1 to 5%, and the mass ratio of (b) galacturonic acid/tannin is 0.04 to 0.8, and (c) The mass ratio of galacturonic acid/amino acid is 〇.〇8 to 0.8; preferably (a) the content of galacturonic acid based on the total solid content (in terms of Bx) of the tea extract ( The mass ratio is 1.2 to 4%, (b) the mass ratio of galacturonic acid/tannin is 0.06 to 0.4, and the mass ratio of (c) half-35 to 201215327 lacturonic acid/amino acid is 0.14 to 〇. 6; more佳] The total solid content (in terms of Bx) of the extract is based on the acid content (mass) of 1.3 to 3%, and (b) the galacturonic acid/single ratio is 0.07 to 0.2' and (c) ) galacturonic acid/amino acid: 〇·19 to 0.4, which can bring about the effect of the present invention. [Simple description of the figure] 4nt, tearing 0 [Description of main component symbols] None. a) The mass ratio of tea lactose aldehyde is -36-

Claims (1)

201215327 七、申請專利範圍: 1. —種茶類萃取物之製造方法,其特徵爲對茶類原料添加 (A)蛋白酶、(B)單寧酶、及(C)具有20000 u/g 以上的聚半乳糖醛酸酶活性之酵素製劑而進行萃取處理 〇 2. 如申請專利範圍第第1項之茶類萃取物之製造方法,其 中茶類原料爲綠茶、烏龍茶或茉莉花茶。 3. 如申請專利範圍第1或2項之茶類萃取物之製造方法, 其中以對每1公克之茶類原料爲0.01 U至100 U的範圍 內添加(A )蛋白酶。 4. 如申請專利範圍第1至3項中任一項之茶類萃取物之製 造方法,其中以對每1克之茶類原料爲0.1 U至50 U的 範圍內添加(B)單寧酶。 5. 如申請專利範圍第1至4項中任一項之茶類萃取物之製 造方法,其中以對茶類原料1克之聚半乳糖醛酸酶活性 成爲800 U以上的量添加(C)具有20000 U/g以上的 聚半乳糖醛酸酶活性之酵素製劑。 6. 如申請專利範圍第1至5項中任一項之茶類萃取物之製 造方法’其進一步包括下列步驟:添加來自於長枝木黴 (Trichoderma longibrachiatum ) 或里氏木黴( Trichoderma reesei)的纖維素酶而進行萃取處理。 -37- 201215327 四、指定代表圖: (一) 本案指定代表圖為:無。 (二) 本代表圖之元件代表符號簡單說明: 並。 y» \\ 五、本案若有化學式時,請揭示最能顯示發明特徵的化學式: 〇 J ί201215327 VII. Patent application scope: 1. A method for producing a tea extract, characterized in that (A) protease, (B) tannin, and (C) have a 20,000 u/g or more added to the tea raw material. The method for producing a tea extract according to the first aspect of the invention, wherein the tea material is green tea, oolong tea or jasmine tea. 3. The method for producing a tea extract according to claim 1 or 2, wherein the protease (A) is added in a range of 0.01 U to 100 U per 1 gram of the tea raw material. 4. The method for producing a tea extract according to any one of claims 1 to 3, wherein (B) the tannase is added in a range of from 0.1 U to 50 U per 1 gram of the tea raw material. 5. The method for producing a tea extract according to any one of claims 1 to 4, wherein the polygalacturonase activity of 1 gram of the tea raw material is added in an amount of 800 U or more (C) An enzyme preparation of polygalacturonase activity of 20000 U/g or more. 6. The method for producing a tea extract according to any one of claims 1 to 5, which further comprises the step of adding Trichoderma longibrachiatum or Trichoderma reesei from Trichoderma longibrachiatum or Trichoderma reesei The cellulase is subjected to extraction treatment. -37- 201215327 IV. Designated representative map: (1) The representative representative of the case is: None. (2) The symbolic representation of the symbol of the representative figure is simple: y» \\ V. If there is a chemical formula in this case, please reveal the chemical formula that best shows the characteristics of the invention: 〇 J ί
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