JPH0342066B2 - - Google Patents
Info
- Publication number
- JPH0342066B2 JPH0342066B2 JP11661483A JP11661483A JPH0342066B2 JP H0342066 B2 JPH0342066 B2 JP H0342066B2 JP 11661483 A JP11661483 A JP 11661483A JP 11661483 A JP11661483 A JP 11661483A JP H0342066 B2 JPH0342066 B2 JP H0342066B2
- Authority
- JP
- Japan
- Prior art keywords
- powder
- tea
- green tea
- extract
- amylopectin
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired
Links
- 244000269722 Thea sinensis Species 0.000 claims description 65
- 239000000843 powder Substances 0.000 claims description 35
- 235000013616 tea Nutrition 0.000 claims description 35
- 235000009569 green tea Nutrition 0.000 claims description 32
- 239000000284 extract Substances 0.000 claims description 21
- 229920000945 Amylopectin Polymers 0.000 claims description 19
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 17
- 229920001353 Dextrin Polymers 0.000 claims description 11
- 239000004375 Dextrin Substances 0.000 claims description 11
- 238000000354 decomposition reaction Methods 0.000 claims description 11
- 235000019425 dextrin Nutrition 0.000 claims description 11
- 239000000203 mixture Substances 0.000 claims description 11
- 239000000892 thaumatin Substances 0.000 claims description 8
- 235000010436 thaumatin Nutrition 0.000 claims description 8
- 238000004519 manufacturing process Methods 0.000 claims description 7
- 239000003960 organic solvent Substances 0.000 claims description 7
- 239000002904 solvent Substances 0.000 claims 2
- 239000000047 product Substances 0.000 description 27
- 239000000796 flavoring agent Substances 0.000 description 21
- 235000019634 flavors Nutrition 0.000 description 21
- 239000007787 solid Substances 0.000 description 19
- CSCPPACGZOOCGX-UHFFFAOYSA-N Acetone Chemical compound CC(C)=O CSCPPACGZOOCGX-UHFFFAOYSA-N 0.000 description 15
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 14
- 238000000605 extraction Methods 0.000 description 10
- 239000007788 liquid Substances 0.000 description 9
- 102000004190 Enzymes Human genes 0.000 description 7
- 108090000790 Enzymes Proteins 0.000 description 7
- 239000012141 concentrate Substances 0.000 description 7
- 239000000049 pigment Substances 0.000 description 7
- 239000000243 solution Substances 0.000 description 6
- 230000006866 deterioration Effects 0.000 description 5
- 238000004945 emulsification Methods 0.000 description 5
- 235000019441 ethanol Nutrition 0.000 description 5
- 238000003860 storage Methods 0.000 description 5
- 125000003118 aryl group Chemical group 0.000 description 4
- RYYVLZVUVIJVGH-UHFFFAOYSA-N caffeine Chemical compound CN1C(=O)N(C)C(=O)C2=C1N=CN2C RYYVLZVUVIJVGH-UHFFFAOYSA-N 0.000 description 4
- 239000004615 ingredient Substances 0.000 description 4
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 3
- 239000011248 coating agent Substances 0.000 description 3
- 238000001035 drying Methods 0.000 description 3
- 239000000839 emulsion Substances 0.000 description 3
- 238000001704 evaporation Methods 0.000 description 3
- 230000008020 evaporation Effects 0.000 description 3
- 238000004508 fractional distillation Methods 0.000 description 3
- 238000002386 leaching Methods 0.000 description 3
- 238000004513 sizing Methods 0.000 description 3
- 239000000126 substance Substances 0.000 description 3
- 229920002472 Starch Polymers 0.000 description 2
- 229960001948 caffeine Drugs 0.000 description 2
- 238000007796 conventional method Methods 0.000 description 2
- 230000035622 drinking Effects 0.000 description 2
- 239000000469 ethanolic extract Substances 0.000 description 2
- 235000011389 fruit/vegetable juice Nutrition 0.000 description 2
- 239000008187 granular material Substances 0.000 description 2
- 238000001802 infusion Methods 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 235000019698 starch Nutrition 0.000 description 2
- 239000008107 starch Substances 0.000 description 2
- 240000005979 Hordeum vulgare Species 0.000 description 1
- 235000007340 Hordeum vulgare Nutrition 0.000 description 1
- LPHGQDQBBGAPDZ-UHFFFAOYSA-N Isocaffeine Natural products CN1C(=O)N(C)C(=O)C2=C1N(C)C=N2 LPHGQDQBBGAPDZ-UHFFFAOYSA-N 0.000 description 1
- 240000007594 Oryza sativa Species 0.000 description 1
- 235000007164 Oryza sativa Nutrition 0.000 description 1
- 240000008042 Zea mays Species 0.000 description 1
- 235000005824 Zea mays ssp. parviglumis Nutrition 0.000 description 1
- 235000002017 Zea mays subsp mays Nutrition 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 239000004480 active ingredient Substances 0.000 description 1
- 150000001413 amino acids Chemical class 0.000 description 1
- 239000007864 aqueous solution Substances 0.000 description 1
- 235000013361 beverage Nutrition 0.000 description 1
- 238000009835 boiling Methods 0.000 description 1
- VJEONQKOZGKCAK-UHFFFAOYSA-N caffeine Natural products CN1C(=O)N(C)C(=O)C2=C1C=CN2C VJEONQKOZGKCAK-UHFFFAOYSA-N 0.000 description 1
- 150000001720 carbohydrates Chemical class 0.000 description 1
- 235000014633 carbohydrates Nutrition 0.000 description 1
- 235000005822 corn Nutrition 0.000 description 1
- 230000002542 deteriorative effect Effects 0.000 description 1
- -1 dissipation of aroma Substances 0.000 description 1
- 239000012467 final product Substances 0.000 description 1
- 238000004108 freeze drying Methods 0.000 description 1
- 239000001056 green pigment Substances 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 150000002894 organic compounds Chemical class 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 230000002265 prevention Effects 0.000 description 1
- 239000011253 protective coating Substances 0.000 description 1
- 239000001397 quillaja saponaria molina bark Substances 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 235000009566 rice Nutrition 0.000 description 1
- 229930182490 saponin Natural products 0.000 description 1
- 150000007949 saponins Chemical class 0.000 description 1
- 238000000638 solvent extraction Methods 0.000 description 1
- 239000007921 spray Substances 0.000 description 1
- 238000010025 steaming Methods 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 238000001291 vacuum drying Methods 0.000 description 1
- 238000004383 yellowing Methods 0.000 description 1
Landscapes
- Tea And Coffee (AREA)
Description
【発明の詳細な説明】
本発明は通常の方法でいれた緑茶湯と風味のほ
とんど変らない茶湯を提供する優れた乾燥粉末状
または顆粒状インスタント緑茶の製造方法に関す
るものである。更に詳細には、茶葉組織中に存在
する茶の可溶性風味成分を安定かつ有効に抽出
し、必要に応じては、酵素によるアミロペクチン
低分解物(特殊デキストリン)を加えて担体と
し、又、更に、必要に応じては、少量のソーマチ
ンを添加し、香味を逸散又は劣化させることな
く、乾燥して乾燥品を得、別に茶アロマ抽出物を
前記の特殊デキストリンとを担体とし、水分散型
に乳化した后、凍結乾燥か真空乾燥を行つて香気
粉末を得、前記乾燥品と香気粉末とを混合し、必
要に応じては顆粒化することからなる、インスタ
ント緑茶の製造方法にかんするものである。
緑茶はその原料および製法によつて抹茶、玉
露、せん茶、番茶などさまざまな種類があるが、
普通は製品茶葉を湯で浸出した煎汁(茶湯)とし
て飲用される。煎汁へ抽出される有効成分として
はアミノ酸、炭水化物、テイン、サポニン、カフ
エイン及び香気成分等から成る。茶の種類によつ
ても異なるが、茶葉に30ないし100倍量の60℃以
上の温湯または熱湯を注いで30秒ないし5分間浸
出を行い、その煎汁を飲用している。同じ茶葉を
用いても湯の温度、浸出の時間、湯量等の条件に
よつて、抽出される成分組成および香りが異なつ
てくる。また、浸出された煎汁を放置しておく
と、その風味および色調は刻々と変化するデリケ
ートな飲料である。また、このような煎汁を得た
後には茶の出しガラを捨てなければならず、面倒
な事である。
従来、このような茶湯を簡単に得るため種々の
方法で、製造された粉末固形状インスタント緑茶
が提案されている。しかしながら、従来のインス
タント緑茶の製造方法では茶の色および風味の劣
化、香気の逸散、製品の保存安定性、製品の歩止
り等の諸問題についてかならずしも満足のいく製
品が得られなかつた。これらの諸問題点を更に具
体的に示せば次の通りである。
(1) 工業規模での製造段階における香気および風
味成分の逸散または劣化。
(2) 製造段階における色の黄色化現象。
(3) 乾燥粉末または顆粒状製品の貯蔵保管中にお
ける香りおよび風味の劣化、または吸湿による
ケーキングの発生。
(4) 飲用時における、1杯の茶湯をいれるための
秤量が困難であること。
発明者らは上記の4つの問題を適切に解決し、
高品質なインスタント緑茶を製造することに成功
した。
本発明のインスタント緑茶製品は次のように製
造される。
(イ) 緑茶を必要に応じて、粉砕し、カラム抽出等
により、100倍重量以上の60℃以上の温湯また
は、熱水を用いて浸出し、この抽出液に、必要
に応じて茶固型分100gにたいして、0.1〜100
mgのソーマチンおよび/または0〜99倍の特殊
デキストリンを加え、完全に溶解し、更に必要
に応じては、APV濃縮装置などにより、濃縮
を行つた後、乾燥して乾燥茶粉末をうる。
(ロ) 一方、別の茶葉、好ましくは高級緑茶葉を有
機溶媒、例えばエチルアルコール、メチルアル
コール、アセトン、その他の適当な有機化合物
またはそれらと水との混合液で低温抽出を行つ
て主として香気および色素成分から成る抽出液
を得る。得られた抽出液を濃縮して有機溶媒を
除去した後、特殊デキストリンおよび温水を添
加して約3〜80%、好しくは約40%の固型分濃
度を持つ混合物を得る。この液を例えば高圧乳
化法によつて乳化し、その後噴霧乾燥または凍
結乾燥によつて緑茶の香気成分および色素を主
成分とする粉末を得る。
(ハ) 上記(イ)で製造した乾燥茶粉末に上記(ロ)で得た
粉末を(イ)の粉末に対して0.5ないし20%配合し
て混合し、必要に応じて顆粒化を行つて目的の
インスタント緑茶製品を得る。
本発明の(ロ)の工程で使用される特殊デキストリ
ンとはアミロペクチンの低分解物質である。すな
わち、アミロペクチンを主体とする澱粉、例えば
モチ米、モチ大麦、モチトウモロコシ等の95%以
上のアミロペクチンを含有する澱粉をDEが2な
いし5になるように加水分解し、その後十分にア
ルフア化するまで蒸煮し、次いで乾燥して製造す
ることができる。このアミロペクチン低分解物
を、有機溶媒で低温抽出した抽出液に添加するこ
とにより、抽出された茶の香気成分および色素が
保護コーテイングされ、その後の乾燥工程および
貯蔵管理中にも香気成分の劣化、逸散が起らな
い。同時に、緑茶特有の薄緑色の色素も安定に維
持できる。
また、工程(イ)において、茶葉の浸出液にソーマ
チンを添加することによつて緑茶の主固型分の風
味が増進されることが判明した。
このような工程(ロ)による香気および色素成分の
低温有機溶媒抽出、および特殊デキストリン等の
コーテイング剤の使用、並びに工程(イ)におけるソ
ーマチンの添加により、茶の香気、色素および風
味成分の逸散、劣化を防止でき、前述の問題点
1、2および3を解決した。
香気および色素成分は低温有機溶媒で抽出さ
れ、その後上記コーテイング剤で被覆されるため
後の乾燥工程および製品の保存中においても逸散
および劣化が起らない。また、茶の主固型分(工
程(イ)で製造されるもの)もソーマチンの使用によ
り風味が向上している。
また、上記コーテイング剤の使用により、最終
製品のカサが増すため、一杯分の茶湯を作るため
の製品量をスプーンでより容易かつ正確に秤量す
ることができる。したがつて、前述の問題点4も
解決された。
製品の保存中におけるケーキングの防止(問題
点3)は、特殊デキストリンを使用して香気およ
び色素成分を被覆することによつて達成される。
特にアミロペクチン低分解物質による場合は通常
のデキストリンでは得られない、香気および色素
成分の安定保持特性および低級湿性を示す。
一方、アミロペクチン低分解物質に変えて、ア
ミロペクチン自体を添加する場合には、アミロペ
クチンが30℃、10%(w/w)水溶液で24000cps
と高粘度であり(本発明のアミロペクチン低分解
物質は同条件で6.5cps)、製造工程における操作
に問題を生じ、更に飲用時の茶湯に粘度を与えて
好しくない味覚を与えるという欠点がある。
以下の実施例によつて本発明を更に詳細に説明
する。
実施例 1
(1) 通常煎茶をグラインダーで10〜20メツシユに
粉砕した。粉砕煎茶45Kgを5本の耐圧カラムに
充填し、連続向流カラム抽出(液温70℃)を行
い、茶固形分濃度10%(w/w)の抽出液50Kg
を得た。(茶固形分:5Kg)
(2) 酵素により分解したアミロペクチン低分解物
5Kgを上記(1)の茶抽出液に添加し、溶解した。
(3) 別に、高級緑茶(100g)を0.5の80%
(w/w)エタノールで温度40℃にて浸出抽出
し、緑色の香気エツセンスを得た。このエタノ
ール抽出液を低温で分溜蒸発してほぼエタノー
ルが無くなるまで濃縮した。この濃縮物に水
200mlおよび酵素により予じめ分解したアミロ
ペクチン低分解物50gを添加し、良く撹拌して
均質乳化を行つた。この均質化液を凍結乾燥
し、軽く粉砕して10〜20メツシユの香味成分粉
末を得た。
(4) 上記(2)で得た溶液にソーマチン50mgを添加
し、溶解した。この溶液を噴霧乾燥して乾燥粉
末品を得た。
(5) 上記(4)で得た乾燥粉末品10Kgに上記(3)で得た
香味成分粉末5gを添加し、十分に混合した。
得られた混合物を流動層造粒装置で造粒し、12
〜20メツシユに整粒して本発明のインスタント
緑茶製品を得た。
実施例 2
(1) 通常緑茶をグラインダーで約20メツシユに粗
く粉砕した。粉砕緑茶25Kgを耐圧カラムに充填
し、連続向流カラム抽出(液温60〜65℃)を行
い、茶固形分濃度8%(w/w)の抽出液40Kg
を得た。(茶固形分:3.2Kg)
(2) 別に、高級緑茶(500g)を2のアセトン
で温度35〜40℃で浸出し、過して緑茶の香気
エツセンスを得た。このアセトン抽出液を低温
で分溜蒸発してアセトンを留去した。この残留
物に温湯500mlと酵素により予じめ分解したア
ミロペクチン低分解物50gとを添加し、完全に
溶解した。この溶液をよく撹拌して均質乳化を
行つた。この均質乳化液を凍結乾燥し、軽く粉
砕して10〜20メツシユの香味成分粉末を得た。
(3) 上記(1)で得た溶液にソーマチン35mgを添加
し、溶解した。この溶液をAPV装置を使用し
て固形分35%(w/w)まで濃縮した。この液
を凍結乾燥して水分2.8%の乾燥粉末を得た。
(4) 上記(3)で得た乾燥粉末3.2Kgに上記(2)で得た
香味成分紛末9gを添加し、十分に混合した。
得られた混合物をブルーノツクス式造粒装置で
造粒し、その後20〜32メツシユに整粒して本発
明のインスタント緑茶製品を得た。
実施例 3
(1) 市販粉茶10Kgを5本の耐圧カラムに充填し、
連続向流カラム抽出(液温65〜70℃)を行い、
茶固形分濃度10%(w/w)の抽出液20を得
た。(茶固形分:2Kg)
(2) 酵素により分解したアミロペクチン低分解物
2Kgを上記(1)の茶抽出液に添加し、溶解した。
(3) 別に、高級緑茶(1Kg)を5の95%(w/
w)アセトンで温度45℃で浸出抽出し、過し
て緑色の香気エツセンスを得た。このアセトン
抽出液を低温で分溜蒸発し、アセトンを溜去し
て濃縮した。この残留物に水100mlを添加して
良く溶解し、酵素により予じめ分解したアミロ
ペクチン低分解物50gを添加し、よく撹拌して
均質乳化を行つた。この均質乳化液を真空乾燥
し、軽く粉砕して約20メツシユの香味成分粉末
を得た。
(4) 上記(2)で得た溶液をAPV装置によつて濃縮
し、固形分30%(w/w)の濃縮液を得た。こ
の濃縮液を凍結乾燥し、12〜20メツシユに粉砕
して乾燥粉末(水分2.4%)を得た。
(5) 上記(4)で得た乾燥粉末2Kgに上記(3)で得た香
味成分粉末1.5gを添加し、十分に混合した。
得られた混合物を流動層造粒装置で造粒し、12
〜20メツシユに整粒して本発明のインスタント
緑茶製品を得た。
実施例 4
(1) 市販番茶50Kgを10本の耐圧カラムに充填し、
連続向流カラム抽出(液温70℃)を行い、茶固
形分濃度11%(w/w)の抽出液100を得た。
(茶固形分:11Kg)
(2) 別に、高級緑茶(1Kg)を10のエタノール
(99%(w/w)で温度40℃で浸出による抽出
を行い、過して緑色の香気エツセンスを得
た。このエタノール抽出液を低温で分溜蒸発し
てほぼエタノールが無くなるまで濃縮した。こ
の残留物を水100mlに良く溶解し、酵素により
予じめ分解したアミロペクチン低分解物50gを
添加溶解後、よく撹拌して均質乳化を行つた。
この均質乳化液を凍結乾燥し、軽く粉砕して15
〜20メツシユに整粒し、香味成分粉末60gを得
た。
(3) 上記(1)で得た抽出液をAPV装置で38%
(w/w)固形分濃度に濃縮した。この濃縮液
を噴霧乾燥して乾燥粉末(水分2.5%(w/
w))を得た。
(4) 上記(3)で得た茶乾燥粉末1Kgに上記(2)で得た
香味成分紛末20gを添加し、十分に混合した。
得られた混合物を流動層造粒装置で造粒し、12
〜20メツシユに整粒して本発明のインスタント
緑茶製品を得た。
対照例
(1) 通常緑茶をグラインダーで約20メツシユに粗
く粉砕し、この25Kgを耐圧カラムに詰め、連続
向流カラム抽出(液温60〜65℃)を行い、茶固
形分濃度8%(w/w)の抽出液40Kgを得た。
(茶固形分:3.2Kg)
(2) 上記(1)で得た抽出液をAPV装置を使用して
固形分濃度35%(w/w)に濃縮した。
(3) 上記(2)の濃縮液を実施例2と同様の条件で凍
結乾燥し、水分含量2.8%のインスタント緑茶
乾燥粉末製品を得た。
以下に、本願発明の製品である実施例1〜4の
生成物と対照例によつて製造された生成物との諸
性質を比較して次表に要約する。
香味、色、安定性、秤量性のいずれについても
本発明の製品が優れていることが理解されよう。
【表】DETAILED DESCRIPTION OF THE INVENTION The present invention relates to an excellent method for producing instant green tea in the form of dry powder or granules, which provides a tea tea whose flavor is almost the same as that made by conventional methods. More specifically, the soluble flavor components of tea present in the tea leaf tissue are stably and effectively extracted, and if necessary, amylopectin low decomposition product by enzymes (special dextrin) is added as a carrier, and further, If necessary, add a small amount of thaumatin and dry to obtain a dry product without loosing or deteriorating the flavor. Separately, tea aroma extract is used as a carrier with the above special dextrin and made into a water-dispersed type. After emulsification, freeze drying or vacuum drying is performed to obtain an aroma powder, and the dried product and the aroma powder are mixed, and if necessary, granulated. . There are various types of green tea, including matcha, gyokuro, sencha, and bancha, depending on the raw materials and manufacturing methods.
It is usually drunk as a decoction (chayu) made by steeping the tea leaves in hot water. The active ingredients extracted into the decoction include amino acids, carbohydrates, thein, saponin, caffeine, and aromatic ingredients. Depending on the type of tea, 30 to 100 times the volume of hot or boiling water at 60°C or higher is poured over the tea leaves, steeped for 30 seconds to 5 minutes, and the resulting juice is drunk. Even if the same tea leaves are used, the extracted component composition and aroma will vary depending on conditions such as the temperature of the hot water, the time of infusion, and the amount of hot water. Furthermore, if the infused juice is left to stand, it is a delicate beverage whose flavor and color change constantly. Furthermore, after obtaining such a decoction, the tea leaves must be thrown away, which is troublesome. BACKGROUND ART In the past, powdered solid instant green tea produced by various methods has been proposed in order to easily obtain such tea tea. However, conventional methods for producing instant green tea have not always produced a product that is satisfactory in terms of problems such as deterioration of tea color and flavor, dissipation of aroma, product storage stability, and product yield. These various problems are shown in more detail as follows. (1) Dissipation or deterioration of aroma and flavor components during manufacturing on an industrial scale. (2) Yellowing phenomenon during the manufacturing stage. (3) Deterioration of aroma and flavor or caking due to moisture absorption during storage of dry powder or granular products. (4) Difficult to weigh tea to make one cup of tea for drinking. The inventors appropriately solved the above four problems,
We succeeded in producing high-quality instant green tea. The instant green tea product of the present invention is manufactured as follows. (b) Grind the green tea as necessary, infuse it with hot water of 60℃ or higher or hot water of 100 times its weight or more by column extraction, etc., and add tea solids to this extract as necessary. 0.1 to 100 per 100g
Add mg of thaumatin and/or 0 to 99 times special dextrin to dissolve completely, and if necessary, concentrate using an APV concentrator or the like, and then dry to obtain dry tea powder. (b) On the other hand, another tea leaf, preferably a high-grade green tea leaf, is subjected to low-temperature extraction with an organic solvent such as ethyl alcohol, methyl alcohol, acetone, or other suitable organic compound or a mixture of these and water to mainly produce aroma and flavor. An extract consisting of pigment components is obtained. After concentrating the obtained extract to remove the organic solvent, special dextrin and warm water are added to obtain a mixture having a solid content concentration of about 3 to 80%, preferably about 40%. This liquid is emulsified by, for example, a high-pressure emulsification method, and then spray-dried or freeze-dried to obtain a powder containing green tea aroma components and pigments as main components. (c) Mix the powder obtained in (b) above with the dry tea powder produced in (a) above at a ratio of 0.5 to 20% based on the powder in (a), and granulate as necessary. Obtain the desired instant green tea product. The special dextrin used in step (b) of the present invention is a low-decomposition substance of amylopectin. That is, starch mainly containing amylopectin, such as starch containing 95% or more of amylopectin, such as waxy rice, waxy barley, waxy corn, etc., is hydrolyzed to a DE of 2 to 5, and then until it is sufficiently converted into alpha. It can be produced by steaming and then drying. By adding this low decomposition product of amylopectin to the extract obtained by low-temperature extraction with an organic solvent, the aroma components and pigments of the extracted tea are protected with a protective coating, preventing the deterioration of the aroma components during the subsequent drying process and storage management. No dissipation occurs. At the same time, the light green pigment unique to green tea can be maintained stably. Furthermore, it has been found that the flavor of the main solid content of green tea is enhanced by adding thaumatin to the tea leaf infusion in step (a). The aroma, pigment and flavor components of tea are dissipated by the low-temperature organic solvent extraction of the aroma and pigment components in step (b), the use of a coating agent such as special dextrin, and the addition of thaumatin in step (a). , deterioration can be prevented and problems 1, 2 and 3 mentioned above have been solved. The aroma and pigment components are extracted with a low-temperature organic solvent and then coated with the above-mentioned coating agent, so that they do not escape or deteriorate during the subsequent drying process and during product storage. Furthermore, the flavor of the main solid content of tea (produced in step (a)) is improved by the use of thaumatin. Additionally, the use of the coating agent increases the bulk of the final product, making it easier and more accurate to weigh out the amount of product with a spoon to make one cup of tea tea. Therefore, the aforementioned problem 4 has also been solved. Prevention of caking during storage of the product (Problem 3) is achieved by using special dextrins to coat the flavor and color components.
In particular, when amylopectin is used as a low-decomposition substance, it exhibits characteristics of stably retaining aroma and pigment components and low humidity that cannot be obtained with ordinary dextrin. On the other hand, when amylopectin itself is added instead of a low-degradable amylopectin substance, amylopectin has a 10% (w/w) aqueous solution of 24,000 cps at 30°C.
It has a high viscosity (the low amylopectin decomposition material of the present invention is 6.5 cps under the same conditions), which causes problems in operation during the manufacturing process, and has the disadvantage that it adds viscosity to the tea ceremony when drinking, giving it an unpleasant taste. . The present invention will be explained in further detail by the following examples. Example 1 (1) Regular sencha was ground into 10 to 20 mesh pieces using a grinder. 45kg of ground green tea was packed into 5 pressure-resistant columns and subjected to continuous countercurrent column extraction (liquid temperature 70℃) to produce 50kg of extract with a tea solid content concentration of 10% (w/w).
I got it. (Tea solid content: 5 kg) (2) 5 kg of amylopectin low decomposition product degraded by enzymes was added to the tea extract obtained in (1) above and dissolved. (3) Separately, add 0.5% of high quality green tea (100g) to 80%
A green aroma essence was obtained by leaching and extraction with (w/w) ethanol at a temperature of 40°C. This ethanol extract was concentrated by fractional distillation and evaporation at low temperature until almost all ethanol was removed. water to this concentrate
200 ml and 50 g of low-degraded amylopectin that had been previously decomposed with enzymes were added, and the mixture was thoroughly stirred to achieve homogeneous emulsification. This homogenized liquid was freeze-dried and lightly ground to obtain 10 to 20 meshes of flavor component powder. (4) 50 mg of thaumatin was added to the solution obtained in (2) above and dissolved. This solution was spray dried to obtain a dry powder product. (5) 5 g of the flavor ingredient powder obtained in (3) above was added to 10 kg of the dry powder product obtained in (4) above, and mixed thoroughly.
The resulting mixture was granulated using a fluidized bed granulator, and 12
The instant green tea product of the present invention was obtained by sizing to ~20 mesh. Example 2 (1) Regular green tea was coarsely ground into approximately 20 mesh pieces using a grinder. 25kg of ground green tea was packed into a pressure column and subjected to continuous countercurrent column extraction (liquid temperature 60-65℃) to produce 40kg of extract with a tea solid content concentration of 8% (w/w).
I got it. (Tea solid content: 3.2Kg) (2) Separately, high quality green tea (500g) was leached with acetone in step 2 at a temperature of 35-40°C and passed through to obtain the aromatic essence of green tea. This acetone extract was fractionally distilled and evaporated at low temperature to remove acetone. To this residue were added 500 ml of warm water and 50 g of amylopectin low decomposition product that had been previously decomposed with an enzyme, and the mixture was completely dissolved. This solution was thoroughly stirred to achieve homogeneous emulsification. This homogeneous emulsion was freeze-dried and lightly pulverized to obtain 10 to 20 meshes of flavor component powder. (3) 35 mg of thaumatin was added to the solution obtained in (1) above and dissolved. The solution was concentrated to 35% (w/w) solids using an APV apparatus. This liquid was freeze-dried to obtain a dry powder with a water content of 2.8%. (4) To 3.2 kg of the dry powder obtained in (3) above, 9 g of the flavor ingredient powder obtained in (2) above was added and mixed thoroughly.
The resulting mixture was granulated using a Bluenox granulator, and then sized to 20 to 32 meshes to obtain an instant green tea product of the present invention. Example 3 (1) 10 kg of commercially available powdered tea was packed into five pressure-resistant columns,
Perform continuous countercurrent column extraction (liquid temperature 65-70℃),
Extract 20 with a tea solid content concentration of 10% (w/w) was obtained. (Tea solid content: 2 kg) (2) 2 kg of amylopectin low decomposition product degraded by enzymes was added to the tea extract obtained in (1) above and dissolved. (3) Separately, add high quality green tea (1Kg) to 95% (w/
w) Leaching and extraction with acetone at a temperature of 45°C was carried out to obtain a green aromatic essence. This acetone extract was subjected to fractional distillation and evaporation at low temperature to remove acetone and concentrate. 100 ml of water was added to this residue to dissolve it well, and 50 g of low-degraded amylopectin, which had been previously decomposed with enzymes, was added and stirred well to homogeneously emulsify. This homogeneous emulsion was vacuum dried and lightly pulverized to obtain about 20 meshes of flavor component powder. (4) The solution obtained in (2) above was concentrated using an APV device to obtain a concentrated liquid with a solid content of 30% (w/w). This concentrate was freeze-dried and ground into 12 to 20 meshes to obtain a dry powder (water content 2.4%). (5) 1.5 g of the flavor component powder obtained in (3) above was added to 2 kg of the dry powder obtained in (4) above, and mixed thoroughly.
The resulting mixture was granulated using a fluidized bed granulator, and 12
The instant green tea product of the present invention was obtained by sizing to ~20 mesh. Example 4 (1) 50 kg of commercially available bancha was packed into 10 pressure-resistant columns,
Continuous countercurrent column extraction (liquid temperature 70°C) was performed to obtain an extract 100 having a tea solid content concentration of 11% (w/w).
(Tea solid content: 11Kg) (2) Separately, high-quality green tea (1Kg) was extracted by leaching with 10% ethanol (99% (w/w) at a temperature of 40℃, and then passed through to obtain a green aromatic essence. This ethanol extract was concentrated by fractional distillation and evaporation at low temperature until almost all ethanol was removed.This residue was well dissolved in 100 ml of water, and 50 g of amylopectin, which had been previously degraded with enzymes, was added and dissolved. Homogeneous emulsification was achieved by stirring.
This homogeneous emulsion was freeze-dried, lightly crushed, and
The particles were sized to ~20 mesh pieces to obtain 60 g of flavor ingredient powder. (3) 38% of the extract obtained in (1) above using an APV device
Concentrate to (w/w) solids concentration. This concentrate was spray-dried into a dry powder (moisture 2.5% (w/
w)) was obtained. (4) To 1 kg of the dried tea powder obtained in (3) above, 20 g of the flavor component powder obtained in (2) above was added and mixed thoroughly.
The resulting mixture was granulated using a fluidized bed granulator, and 12
The instant green tea product of the present invention was obtained by sizing to ~20 mesh. Control example (1) Regular green tea is coarsely ground into approximately 20 meshes using a grinder, 25 kg of this is packed into a pressure column, and continuous countercurrent column extraction (liquid temperature 60-65°C) is performed to obtain a tea solids concentration of 8% (w). 40 kg of extract of /w) was obtained.
(Tea solid content: 3.2 Kg) (2) The extract obtained in (1) above was concentrated to a solid content concentration of 35% (w/w) using an APV device. (3) The concentrate obtained in (2) above was freeze-dried under the same conditions as in Example 2 to obtain an instant green tea dry powder product with a water content of 2.8%. Below, various properties of the products of Examples 1 to 4, which are products of the present invention, and the products produced by the control example are compared and summarized in the following table. It will be appreciated that the products of the present invention are superior in terms of flavor, color, stability, and weighability. 【table】
Claims (1)
チンの低分解物(特殊デキストリン)、ソーマ
チンまたはこれらの両成分を添加し混合液を乾
燥して乾燥茶粉末を得、 (ロ) 別に、緑茶の茶葉を有機溶媒で低温抽出し、
溶媒を除去した後、温水およびアミロペクチン
の低分解物(特殊デキストリン)を添加し、混
合して乳化し、乾燥して香気成分粉末を得、 (ハ) 上記(イ)の粉末を主体として、これに少量の(ロ)
の粉末を混合し、必要に応じて顆粒化すること
から成る、香気の良い保存性の良好なインスタ
ント緑茶の製造方法。 2 (イ) 緑茶の茶葉を抽出し、この抽出液を乾燥
して乾燥抽出分粉末を得、 (ロ) 別に、緑茶の茶葉を有機溶媒で低温抽出し、
溶媒を除去した後、温水およびアミロペクチン
の低分解物(特殊デキストリン)を添加し、混
合して乳化し、乾燥して香気成分粉末を得、 (ハ) 上記(イ)の粉末を主体とし、これに少量の(ロ)の
粉末を混合し、必要に応じて顆粒化することか
ら成る、香気の良い保存性の良好なインスタン
ト緑茶の製造方法。[Claims] 1 (a) Extract green tea leaves, add a low decomposition product of amylopectin (special dextrin), thaumatin, or both of these components, and dry the mixture to obtain dry tea powder, (b) Separately, green tea leaves are extracted at low temperature with an organic solvent,
After removing the solvent, warm water and a low decomposition product of amylopectin (special dextrin) are added, mixed and emulsified, and dried to obtain an aroma component powder, (c) mainly containing the powder of (a) above, and this a small amount (b)
A method for producing instant green tea with good aroma and good shelf life, which comprises mixing powders of and granulating if necessary. 2 (a) Extract green tea leaves and dry this extract to obtain a dry extract powder; (b) Separately, extract green tea leaves at a low temperature with an organic solvent;
After removing the solvent, warm water and a low decomposition product of amylopectin (special dextrin) are added, mixed and emulsified, and dried to obtain an aroma component powder, (c) mainly consisting of the powder of (a) above, A method for producing instant green tea with a good aroma and good shelf life, which comprises mixing a small amount of the powder of (B) with the powder and granulating it as necessary.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP11661483A JPS609449A (en) | 1983-06-28 | 1983-06-28 | Preparation of instant green tea |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP11661483A JPS609449A (en) | 1983-06-28 | 1983-06-28 | Preparation of instant green tea |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS609449A JPS609449A (en) | 1985-01-18 |
JPH0342066B2 true JPH0342066B2 (en) | 1991-06-26 |
Family
ID=14691536
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP11661483A Granted JPS609449A (en) | 1983-06-28 | 1983-06-28 | Preparation of instant green tea |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS609449A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP1780022A1 (en) | 2005-10-31 | 2007-05-02 | SII Printek Inc | Inkjet recording apparatus |
Families Citing this family (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS61187747A (en) * | 1985-02-14 | 1986-08-21 | T Hasegawa Co Ltd | Method for preventing clouding of extracted tea |
JPH0746969B2 (en) * | 1985-07-18 | 1995-05-24 | 塩水港精糖株式会社 | Matcha with improved shelf life and its manufacturing method |
JPS633755A (en) * | 1986-06-23 | 1988-01-08 | House Food Ind Co Ltd | Instant powdery tea |
KR100437724B1 (en) * | 2002-05-06 | 2004-06-30 | 전라남도 | Producing method of granular tea using powder green tea |
JP4381665B2 (en) * | 2002-09-04 | 2009-12-09 | アサヒ飲料株式会社 | Tea drink containing oil-soluble components of tea |
JP3629489B1 (en) * | 2003-12-12 | 2005-03-16 | 花王株式会社 | Production method of tea extract |
JP5800329B2 (en) * | 2010-10-14 | 2015-10-28 | 日研フード株式会社 | Instant tea and method for producing the same |
-
1983
- 1983-06-28 JP JP11661483A patent/JPS609449A/en active Granted
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP1780022A1 (en) | 2005-10-31 | 2007-05-02 | SII Printek Inc | Inkjet recording apparatus |
Also Published As
Publication number | Publication date |
---|---|
JPS609449A (en) | 1985-01-18 |
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