JPS6242579B2 - - Google Patents
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- Publication number
- JPS6242579B2 JPS6242579B2 JP10441380A JP10441380A JPS6242579B2 JP S6242579 B2 JPS6242579 B2 JP S6242579B2 JP 10441380 A JP10441380 A JP 10441380A JP 10441380 A JP10441380 A JP 10441380A JP S6242579 B2 JPS6242579 B2 JP S6242579B2
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- Prior art keywords
- tea
- extract
- substances
- discoloration
- extraction
- Prior art date
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- Solid-Sorbent Or Filter-Aiding Compositions (AREA)
Description
【発明の詳細な説明】
(産業上の利用分野)
本発明は、好ましい色調をもつ茶抽出液の製法
に関するものである。DETAILED DESCRIPTION OF THE INVENTION (Industrial Field of Application) The present invention relates to a method for producing a tea extract having a desirable color tone.
更に詳細には、本発明は、茶抽出液から変色原
因物質を減少せしめた茶抽出液の製法に関するも
のである。 More specifically, the present invention relates to a method for producing a tea extract in which discoloration-causing substances are reduced from the tea extract.
本発明において処理された茶抽出液は変色原因
物質がかなり低減され、抽出されたときの色調の
よい茶抽出液の状態を長時間保持することができ
るので、缶入り紅茶、粉末紅茶等を製造する食品
関連業界に益するところきわめて大なるものがあ
る。 The tea extract processed in the present invention has significantly reduced substances that cause discoloration, and can maintain the state of the tea extract with good color tone for a long time, so it can be used to produce canned black tea, powdered black tea, etc. There are tremendous benefits to the food-related industry.
(発明が解決しようとする問題点)
一般に、緑茶、焙焼茶、半発酵茶又は発酵茶の
水性抽出液は経時的に極めて変質し易いものであ
る。この変質には色、香、味の変化が考えられる
が、最もはげしい変化は色調において起るもので
ある。そしてこの色調変化に付随しておこるフリ
ーラジカル反応に連鎖して、香り、味の低下もお
こるものと考えられる。日常生活においても保温
瓶に入れられた緑茶、紅茶の水抽出液が黒褐色な
いし褐色化し風味低下をもたらす現象は経験的に
広く知られていることである。更にこの抽出液か
ら即席茶を造るときは変質が著しくなる。即ち茶
葉の抽出工程、濃縮工程、粉末工程において、空
気酸化により褐変化がおこるわけである。特に工
業的製造においては大量処理による長時間処理、
また粉末化の際の空気接触などによる強い酸化は
避けられないことである。また粉末型即席茶の製
造においては、収率を上げるため茶葉から好まし
い成分、例えばアミノ酸、テアニン、糖類、芳香
成分などを高収率に抽出しなければならないが、
この操作は同時に変色原因物質を多量に抽出する
ことになる。常識的にはなるべく低い温度で短時
間に抽出を行えば有効成分がより多く抽出され、
変色原因物質が少なく抽出されることになるが、
この方法によると抽出収率が低くなる。また、工
業的原料としては、通常の製茶工程で副生する粉
砕された茶葉、即ち、一般に粉茶といわれている
安価な原料の使用が考えられるが、茶葉組織が破
壊されている粉茶では好ましくない成分の抽出も
容易に随伴してくるため工業的原料として使用さ
れにくいものであつた。(Problems to be Solved by the Invention) Generally, aqueous extracts of green tea, roasted tea, semi-fermented tea, or fermented tea are extremely susceptible to deterioration over time. This alteration can include changes in color, aroma, and taste, but the most severe change occurs in color tone. It is thought that the free radical reaction that accompanies this color tone change causes a reduction in aroma and taste. It is widely known from experience that even in daily life, the aqueous extract of green tea or black tea stored in a thermos bottle turns dark brown or brown, resulting in a loss of flavor. Furthermore, when instant tea is made from this extract, the quality of the tea is significantly altered. That is, browning occurs due to air oxidation during the tea leaf extraction process, concentration process, and powder process. Especially in industrial manufacturing, long-term processing due to large-scale processing,
In addition, strong oxidation due to air contact during powderization is unavoidable. In addition, in the production of powdered instant tea, desirable components such as amino acids, theanine, sugars, and aromatic components must be extracted from tea leaves at a high yield in order to increase the yield.
This operation simultaneously extracts a large amount of substances that cause discoloration. Common sense suggests that if extraction is performed at the lowest possible temperature and in a short time, more active ingredients will be extracted.
Although fewer substances that cause discoloration will be extracted,
This method results in a low extraction yield. In addition, as an industrial raw material, it is possible to use crushed tea leaves that are a by-product of the normal tea manufacturing process, that is, an inexpensive raw material that is generally referred to as powdered tea, but powdered tea whose tea leaf structure has been destroyed may Since undesirable components are easily extracted, it is difficult to use it as an industrial raw material.
(問題点を解決するための手段)
本発明者は、茶葉中の好ましい成分であるアミ
ノ酸類、糖類、芳香成分などが多く抽出され、好
ましくない変色原因物質がより少なく抽出される
方法についても研究したが、工業的製法において
は抽出法の改良のみでは目的を達し得ないこと、
および抽出歩留りの低下など経済的にも問題を残
すことを知つた。結局、両者を多量に含有する抽
出液から変色原因物質を選択的に減少せしめるこ
とにおいてのみ目的を達することができることを
知つた。そして、茶葉の水性抽出液中の風味成分
である含窒素化合物、糖類、芳香成分を可及的に
吸着もしくは凝集沈殿させないで、変色をもたら
す原因物質を選択的に吸着または凝集除去する除
去方法の探求を行なつた。(Means for Solving the Problems) The present inventor has also conducted research on a method that can extract a large amount of desirable components such as amino acids, sugars, aromatic components, etc. from tea leaves, and extract less undesirable discoloration-causing substances. However, in industrial production methods, the objective cannot be achieved only by improving the extraction method.
It was also learned that there remained economic problems such as a decrease in extraction yield. In the end, it was discovered that the objective could only be achieved by selectively reducing the discoloration-causing substance from an extract containing large amounts of both. We also developed a removal method that selectively adsorbs or coagulates and removes the substances that cause discoloration, without adsorbing or coagulating or precipitating the flavor components such as nitrogen-containing compounds, sugars, and aromatic components in the aqueous extract of tea leaves. carried out a search.
本発明でいう変色原因物質とは、茶葉水性抽出
液中に含まれていて、加工が保存中に非酵素的酸
化作用により、官能的に好ましくない変色をおこ
す原因となる物質群をいう。 The term "substances that cause discoloration" as used in the present invention refers to a group of substances that are contained in the aqueous tea leaf extract and cause sensually undesirable discoloration due to non-enzymatic oxidation during processing and storage.
変色原因物質を除去する物質として供試された
ものは、無機系吸着剤、無機系凝集剤、活性炭、
陰イオン交換樹脂、炭水化物系凝集剤、蛋白質系
凝集剤など数十種類であつた。 The substances tested to remove discoloration-causing substances were inorganic adsorbents, inorganic flocculants, activated carbon,
There were dozens of types, including anion exchange resins, carbohydrate-based flocculants, and protein-based flocculants.
これら多くの物質についての試験した結果、ポ
リアミド、ポリアミン高分子化合物、酸化アルミ
ニウム、メチルセルロースのみが本発明の目的を
効果的に達成することを知つた。そして他の吸着
剤、凝集剤は、茶葉抽出液中の好ましい成分、例
えばアミノ酸類まで除去するか、変色原因物質の
選択的除去作用が不十分か、生成した凝集物の分
離除去の作業が困難、などの好ましくない点がみ
られた。例えば活性炭、第4アンモニウム基をも
つイオン交換樹脂は、アミノ酸まで吸着してしま
うので好ましくなかつた。またゼオライト、シリ
カゲル、酸性白土、酸化マグネシウム、クロリジ
ル、硅藻土などの無機系吸着剤は変色原因物質を
吸着する力が弱く、実用性がなかつた。メチルセ
ルロース以外のセルロース誘導体、澱粉誘導体、
海藻抽出物、植物ガム類にも変色原因物質を選択
的に凝集沈殿させるものは見当らなかつた。ゼラ
チン、ミルクカゼイン、大豆蛋白質などの蛋白質
溶液を茶葉抽出物に加えると多少白濁はするが凝
集力が弱く凝集物を分離除去する作業が極めて困
難で、実用性のあるものは見当らなかつた。 After testing many of these materials, it has been found that only polyamides, polyamine polymers, aluminum oxide, and methylcellulose effectively achieve the objectives of the present invention. Other adsorbents and flocculants either remove desirable components in the tea leaf extract, such as amino acids, or their selective removal of discoloration-causing substances is insufficient, or it is difficult to separate and remove the aggregates formed. , and other unfavorable points were observed. For example, activated carbon and ion exchange resins having quaternary ammonium groups are not preferred because they also adsorb amino acids. Furthermore, inorganic adsorbents such as zeolite, silica gel, acid clay, magnesium oxide, chloridyl, and diatomaceous earth have a weak ability to adsorb substances that cause discoloration, and are therefore not practical. Cellulose derivatives other than methylcellulose, starch derivatives,
Neither seaweed extracts nor plant gums were found to selectively coagulate and precipitate discoloration-causing substances. When a protein solution such as gelatin, milk casein, or soybean protein is added to a tea leaf extract, it becomes somewhat cloudy, but the cohesive force is weak and it is extremely difficult to separate and remove the aggregates, so no practical solutions have been found.
本発明は、緑茶、焙焼茶、半発酵茶又は発酵茶
の水性抽出液をポリアミド、ポリアミン高分子化
合物、酸化アルミニウム、メチルセルロースから
選ばれた一つ以上のものもので処理し、抽出液中
の変色原因物質を減少せしめることを特徴とする
茶抽出液の製法である。 The present invention processes an aqueous extract of green tea, roasted tea, semi-fermented tea, or fermented tea with one or more selected from polyamide, polyamine polymer compound, aluminum oxide, and methyl cellulose, and This is a method for producing a tea extract characterized by reducing substances that cause discoloration.
本発明の処理によつて変色原因物質が減少した
茶抽出液は抽出されたときの好ましい色調をその
まま保つと同時に味や香りの変化もきわめて少な
いのである。 The tea extract with reduced discoloration-causing substances through the treatment of the present invention retains the desired color tone when extracted, and at the same time has very little change in taste or aroma.
本発明が有効に適用できる原料茶としては、緑
茶、番茶、焙焼茶(ほうじ茶)、半発酵茶、発酵
茶がある。変色がおこり易くまた色調が重視され
ている高級緑茶、発酵茶において有効である。特
に、現在あまり利用されていない製茶工程中に副
生する屑物、即ち粉茶を原料とする時に本発明の
方法は効果的である。 Raw material teas to which the present invention can be effectively applied include green tea, bancha, roasted tea (roasted tea), semi-fermented tea, and fermented tea. It is effective for high-grade green tea and fermented tea, which are prone to discoloration and where color tone is important. In particular, the method of the present invention is effective when the raw material is waste by-produced during the tea manufacturing process, that is, powdered tea, which is currently not widely used.
茶葉の水性抽出液としては軟水、硬水、無機塩
含有水、65%以下のエチルアルコール水溶液など
が用いられる。抽出方法は限定されるものではな
いが、一般に知られている多段向流抽出法が適し
ている。即席茶の製造を目的とするときは最終抽
出液の濃度が濃いほど良く、例えば10度ブリツク
ス以上であると、その後の工程が容易となり加熱
程度が少なくなり品質の良い製品が得られる。抽
出温度が低い程、抽出時間が短い程変色原因物質
の抽出量は少ないが、当然有効茶葉成分の抽出歩
留りが悪くなつてくる。また高能率抽出法である
多段向流抽出法で低温度抽出を行なうと、低温の
ため抽出液の粘度が高くなり作業性が困難とな
る。抽出温度は茶の種類で異なり高級緑茶、発酵
茶で比較的低く、番茶、焙焼茶などで高い温度で
行なわれるが、一般には40℃〜80℃位の温度が好
ましい。そして、比較的高温で長時間抽出され変
色原因物質を多く含む抽出液においても、本発明
の処理を行なえば品質の良い最終製品が得られ
る。 As the aqueous extract of tea leaves, soft water, hard water, water containing inorganic salts, 65% or less ethyl alcohol aqueous solution, etc. are used. Although the extraction method is not limited, a generally known multistage countercurrent extraction method is suitable. When the purpose is to produce instant tea, the higher the concentration of the final extract, the better; for example, if it is 10 degrees Brix or higher, subsequent steps will be easier and less heating will be required, resulting in a high-quality product. The lower the extraction temperature and the shorter the extraction time, the smaller the amount of discoloration-causing substances extracted, but naturally the extraction yield of effective tea leaf components becomes worse. Furthermore, when low-temperature extraction is performed using multistage countercurrent extraction, which is a highly efficient extraction method, the viscosity of the extract increases due to the low temperature, making workability difficult. The extraction temperature varies depending on the type of tea, and is relatively low for high-grade green tea and fermented tea, and higher for bancha, roasted tea, etc., but generally a temperature of about 40°C to 80°C is preferred. Even if the extract is extracted at a relatively high temperature for a long time and contains a large amount of discoloration-causing substances, a final product of good quality can be obtained by the treatment of the present invention.
このようにして得られた抽出液を、ポリアミ
ド、ポリアミン高分子化合物、酸化アルミニウ
ム、メチルセルロースから選ばれた一つ以上のも
ので処理し、抽出液中の変色原因物質を減少せし
められる。 The extract thus obtained can be treated with one or more selected from polyamide, polyamine polymer compound, aluminum oxide, and methylcellulose to reduce the substances that cause discoloration in the extract.
ここでいうポリアミドとは活性基にアミド基を
持つ合成非水溶性高分子化合物をいい、通常ナイ
ロンと言われているもので代表される。ポリアミ
ドを茶葉水性抽出液中に加えると変色原因物質を
選択的に吸着し、有効成分を全く吸着しない。処
理は中性または微酸性で行なわれる。 The polyamide herein refers to a synthetic water-insoluble polymer compound having an amide group as an active group, and is typified by what is commonly called nylon. When polyamide is added to an aqueous tea leaf extract, it selectively adsorbs substances that cause discoloration and does not adsorb any active ingredients. The treatment is carried out in neutral or slightly acidic conditions.
また、ポリアミン高分子化合物とは、第1また
は第2アミン基を炭素結合2〜6個毎に繰返し有
する非水溶性高分子化合物をいう。水溶性ものは
製品に処理剤が残留するので使えない。一般にポ
リアミン型キレート樹脂と言われているものなど
がこれに当る。例えば市販品のダイヤイオンCR
―20などである。ポリアミン高分子化合物は中性
または微酸性において茶葉水性抽出液中のアミノ
酸などの有効成分を吸着しないが、変色原因物質
をよく選択的に吸着する。 Moreover, the polyamine polymer compound refers to a water-insoluble polymer compound having a first or second amine group repeated every 2 to 6 carbon bonds. Water-soluble products cannot be used because the processing agent will remain on the product. This includes what is generally called a polyamine type chelate resin. For example, the commercially available Diamond Ion CR
-20 etc. Polyamine polymer compounds do not adsorb active ingredients such as amino acids in the aqueous tea leaf extract under neutral or slightly acidic conditions, but they selectively adsorb substances that cause discoloration.
また、酸化アルミニウムとは一般に活性アルミ
ナといわれているもので、アルミナ水和物を熱処
理により活性化させたもので、Al2O3・nH2O
(n=1〜3)の組成をもつ。活性アルミナにも
種々な結晶型のものがあるが、一般の市販品が使
用できる。活性アルミナはモノフエノール系化合
物は吸着しないが、ポリフエノール化合物の一部
を選択的に吸着する興味ある性質があることを知
つた。ポリフエノール化合物の中でもオルトジハ
イドロキシ化合物を選択的によく吸着すること
が、変色原因物質を除くことに効果的なものと考
える。また、活性アルミナは再生使用が容易な利
点を有する。処理は中性または微酸性で行なわれ
る。 Additionally, aluminum oxide is generally referred to as activated alumina, and is made by activating alumina hydrate through heat treatment .
(n=1 to 3). There are various crystal forms of activated alumina, and commercially available products can be used. We learned that activated alumina does not adsorb monophenolic compounds, but has the interesting property of selectively adsorbing some polyphenol compounds. It is believed that selectively adsorbing ortho-dihydroxy compounds among polyphenol compounds is effective in removing substances that cause discoloration. Activated alumina also has the advantage of being easy to recycle. The treatment is carried out in neutral or slightly acidic conditions.
また、メチルセルロースは食品添加用のものが
使われる。本物質は水でコロイド状となるので、
上記の他の物質とは使用方法を多少異にする。茶
葉水性抽出液にメチルセルロースの濃厚溶液例え
ば2〜10%水溶液を加えて撹拌すると白濁凝集物
が生じてくる。この凝集物を濾過または遠心分離
して除去すると変色原因物質を除去することがで
きる。処理は中性または微酸性で行なわれる。 Methylcellulose is also used as a food additive. This substance becomes colloidal with water, so
The method of use is slightly different from the other substances listed above. When a concentrated solution of methylcellulose, for example, a 2-10% aqueous solution, is added to an aqueous tea leaf extract and stirred, a cloudy agglomerate is formed. If this aggregate is removed by filtration or centrifugation, the discoloration-causing substance can be removed. The treatment is carried out in neutral or slightly acidic conditions.
以上の物質に共通していることは、第1アミ
ン、第2アミンあるいはアミド基からなる弱塩基
性活性基またはOH型水素結合活性基を0.14〜
0.7nm(ナノメーター)間隔で繰返し有する高分
子化合物であることで、これに属さない化合物は
茶葉水性抽出液中の変色原因物質を選択的に除去
する作用がないものと考えられる。 What the above substances have in common is that they have weakly basic active groups consisting of primary amines, secondary amines, or amide groups, or OH-type hydrogen bond active groups of 0.14~
Since it is a polymeric compound that repeats at intervals of 0.7 nm (nanometers), it is thought that compounds that do not belong to this category do not have the effect of selectively removing substances that cause discoloration in the aqueous tea leaf extract.
吸着剤あるいは凝集剤の使用量は、原料茶の種
類と質、抽出方法、水性抽出液中の成分濃度、吸
着剤、凝集剤の種類と吸着能活性度などによつて
決まるものである。例えば、通常変色原因物質は
高級茶に多く番茶、焙焼茶などの低級茶に少ない
ので、吸着剤の使用量もそれぞれによつて決めら
れるべきである。また同じ系統の茶葉でも、変色
原因物質の抽出は葉の組織が比較的壊れていない
もので少なく、組織が強く破壊されている粉茶が
原料に用いられているときは多くなる。 The amount of adsorbent or flocculant used is determined by the type and quality of the raw tea, the extraction method, the concentration of components in the aqueous extract, the type and adsorption activity of the adsorbent or flocculant, and so on. For example, substances that cause discoloration are usually found in higher quality teas and less in lower quality teas such as bancha and roasted tea, so the amount of adsorbent used should be determined depending on each type of tea. Furthermore, even among tea leaves of the same strain, the extraction of discoloration-causing substances is low if the leaf tissue is relatively intact, and increases when the raw material is powdered tea whose tissue has been strongly destroyed.
また、抽出温度が高いとき、或は濃厚な抽出液
においては吸着剤、凝集剤を多く必要とする。 Furthermore, when the extraction temperature is high or the extract is concentrated, a large amount of adsorbent or flocculant is required.
また、同系統の吸着剤においても、回収再生の
状態によつても、吸着特性、吸着容量を異にして
いる。 In addition, adsorbents of the same type have different adsorption characteristics and adsorption capacities depending on the state of recovery and regeneration.
従つて、吸着剤、凝集剤の使用量、処理時間、
処理温度などは、予備試験によつて決められるも
のである。予備試験は、茶葉抽出液に吸着剤また
は凝集剤を一定量加え一定の条件下で反応せしめ
反応物を除去した液を、一定条件下に空気酸化さ
せて酸化後の変色の程度を見ることによつてなさ
れる。簡易法の一例をあげると次のような方法が
ある。処理された液の一定容量を濾紙に滲ませ
て、一定条件下で保置酸化させたのち濾紙片の色
調を予め用意された標準比色表と較べることによ
り、処理条件を決めることができる。 Therefore, the amount of adsorbent and flocculant used, processing time,
Processing temperature, etc. are determined through preliminary tests. In the preliminary test, a certain amount of adsorbent or flocculant was added to the tea leaf extract, the reaction was allowed to occur under certain conditions, and the reactants were removed.The liquid was then air oxidized under certain conditions to see the degree of discoloration after oxidation. It is done by hand. An example of a simple method is as follows. The treatment conditions can be determined by soaking a certain volume of the treated liquid onto a filter paper, storing it under certain conditions for oxidation, and then comparing the color tone of the filter paper piece with a standard color comparison table prepared in advance.
吸着剤、凝集剤による処理時のPHは4.0〜7.5の
間が好ましい。PH4.0以下の酸性では吸着能が低
下し、PH7.5以上では変色原因物質が変化してよ
くない。好ましくはPH5.0〜6.5の間で行なわれ
る。吸着剤の使用方法には大きくわけてバツチ法
とカラム法があるが、カラム法では液の通過に時
間を要するので、通常のバツチ法で行なわれる。
メチルセルロースを使うときは茶葉を抽出する水
性液に、前もつてメチルセルロースを添加してお
いてもよく、抽出液にあとから加えてもよい。前
者の方法は工程が簡略化される利点をもつ。吸着
剤、凝集剤の分離除去は濾過、遠心分離などの公
知の方法でなされる。 The pH during treatment with an adsorbent or flocculant is preferably between 4.0 and 7.5. If the pH is acidic, below 4.0, the adsorption capacity will decrease, and if the pH is above 7.5, the substances that cause discoloration will change, which is not good. Preferably, the pH is between 5.0 and 6.5. There are two main methods for using adsorbents: the batch method and the column method. Since the column method requires time for the liquid to pass through, the conventional batch method is used.
When using methylcellulose, methylcellulose may be added in advance to the aqueous liquid from which tea leaves are extracted, or it may be added to the extract afterwards. The former method has the advantage of simplifying the process. The adsorbent and flocculant are separated and removed by known methods such as filtration and centrifugation.
処理された茶抽出液は、缶容器に入れ殺菌され
たのち6ケ月間室温保存されたが色調、風味とも
優れていた。これは緑茶、発酵茶など何れの茶に
おいても同様であつた。 The treated tea extract was placed in a can and sterilized and then stored at room temperature for 6 months, and it had excellent color and flavor. This was true for any tea, including green tea and fermented tea.
本発明において処理された茶抽出液を用いて即
席茶を製造すれば、色、香、味にすぐれた即席茶
を得ることができる。即席茶を製造するときは、
以上の処理がなされた茶葉水性抽出液を公知の方
法により濃縮するか、またはそのまま粉末化され
る。抽出工程において10度ブリツクス以上になる
よう濃く抽出し、その後の濃縮工程を省いて粉末
化工程に入るのが、風味物質の逸散を防ぐので好
ましい。粉末化は公知の方法が用いられるが、凍
結乾燥法、噴霧乾燥法、減圧乾燥法などが好まし
い。必要により多糖類などの保形剤、または酸度
調整剤、アミノ酸などの呈味物質、レモンエツセ
ンス、ジヤスミンなどの着香料などを何れかの工
程で加えることができる。上記の方法で造られた
粉末即席茶を熱水、温水、または冷水で溶解して
飲用すると、色調がよく風味もすぐれており、ま
た粉末のままで保存される場合も色調、風味の変
化が少ない。 If instant tea is produced using the tea extract treated in the present invention, instant tea with excellent color, aroma, and taste can be obtained. When producing instant tea,
The aqueous tea leaf extract subjected to the above treatment is concentrated by a known method, or is directly powdered. In the extraction step, it is preferable to extract at a concentration of 10 degrees Brix or higher, and then proceed to the powdering step without the subsequent concentration step, in order to prevent flavor substances from escaping. A known method can be used for powdering, but freeze-drying, spray-drying, reduced-pressure drying, etc. are preferable. If necessary, shape preservatives such as polysaccharides, acidity regulators, taste substances such as amino acids, and flavoring agents such as lemon essence and diasmine can be added at any step. When powdered instant tea made by the above method is dissolved in hot, hot, or cold water and drunk, it has a good color and excellent flavor, and when stored as a powder, there is no change in color or flavor. few.
実施例 1
セイロン紅茶1Kgを60の85℃温水で4分間抽
出し残渣を除去し、1Mのクエン酸・クエン酸ナ
トリウム緩衝液を加えてPH5.5とし、約40℃で活
性アルミナ(住友金属工業)4gを加えてゆるく
10分間撹拌し濾過すると約57の美しい鮮紅色の
紅茶抽出液が得られた。この液に砂糖を9w/w
%加え飲料用缶に詰め115℃、15分の加圧殺菌を
行なつて缶入り紅茶飲料(処理品)とした。Example 1 Extract 1 kg of Ceylon black tea with 85℃ hot water at 60°C for 4 minutes to remove the residue, add 1M citric acid/sodium citrate buffer to adjust the pH to 5.5, and extract activated alumina (Sumitomo Metal Industries, Ltd.) at about 40℃. ) Add 4g and mix loosely.
After stirring for 10 minutes and filtering, a beautiful bright red black tea extract was obtained. Add 9w/w sugar to this liquid
% and then packed into beverage cans and sterilized under pressure at 115°C for 15 minutes to produce canned tea beverages (processed products).
活性アルミナ処理のみを省略し、他は前記のも
のと同様の方法で造られた飲料を無処理品とし
た。両者を室温に保存したところ、無処理品は製
造直後(殺菌直後)で既に黒変がみられ3週間後
には明らかな変色がみられ風味も劣化していた。
これに対し処理品は6ケ月後も鮮紅色を呈し、風
味も飲用に適するものであつた。 A beverage made in the same manner as above except for the activated alumina treatment was used as an untreated beverage. When both were stored at room temperature, the untreated product had already turned black immediately after production (immediately after sterilization), and after 3 weeks, obvious discoloration was observed and the flavor had deteriorated.
In contrast, the treated product remained bright red even after 6 months and had a drinkable flavor.
実施例 2
緑茶の破砕されたもの、所謂粉茶(市販品)7
Kgを7本のジヤケツト方式により60℃に保持され
た筒内に各々1Kgずつ詰め、各筒の下方より60℃
の温水を加圧注入し、多段式向流抽出法により約
16度ブリツクスの緑茶水抽出液を得た。この抽出
液をPH5.6に調整したのち1当り65gの活性ア
ルミナ(メルク社製)を抽出液に投入し、約15分
室温下でゆるく撹拌したのち遠心分離して沈殿物
を除去し、色調のすぐれた緑茶飲料を得た。Example 2 Crushed green tea, so-called powdered tea (commercial product) 7
1 kg each is packed into seven cylinders maintained at 60°C using a jacket method, and each cylinder is heated to 60°C from the bottom of each cylinder.
of hot water is injected under pressure, and a multi-stage countercurrent extraction method is used to extract approximately
A green tea water extract of 16 degrees Brix was obtained. After adjusting the pH of this extract to 5.6, 65 g of activated alumina (manufactured by Merck) was added to the extract, stirred gently at room temperature for about 15 minutes, and then centrifuged to remove the precipitate. An excellent green tea beverage was obtained.
実施例 3
番茶7Kgを7本の耐圧筒に各々1Kgずつ詰め、
約90℃の熱水を加圧注入し、多段式向流抽出法に
より約11度ブリツクスの番茶水抽出液を得た。こ
の抽出液をPH5.8に調整したのち、1当り55g
のナイロン66粉末(旭化成)を抽出液に加え、約
40℃で15分ゆるく撹拌したのち、吸着剤を濾過し
て除き、風味のすぐれた番茶液を得た。Example 3 Pack 7 kg of bancha into seven pressure-resistant cylinders, each weighing 1 kg.
Hot water at about 90°C was injected under pressure and a multi-stage countercurrent extraction method was used to obtain a bancha water extract with a temperature of about 11°C. After adjusting this extract to pH5.8, 55g per 1
Add nylon 66 powder (Asahi Kasei) to the extract and
After gently stirring at 40°C for 15 minutes, the adsorbent was removed by filtration to obtain a bancha liquid with excellent flavor.
実施例 4
焙焼茶(ほうじ茶)を実施例3と同じ90℃の条
件で抽出し、約10度ブリツクスの抽出液を得た。
この抽出液1当り50gのダイヤイオンCR―20
(スチレンとジビニールベンゼン共重合体にポリ
アミンを導入した合成樹脂)を投入し、同時にPH
5.5に調整したのち室温で15分ゆるく撹拌し、濾
過して樹脂粒子を除き、風味のよいほうじ茶を得
た。Example 4 Roasted tea (roasted tea) was extracted under the same conditions as in Example 3 at 90°C to obtain an extract having a concentration of approximately 10°C.
50g of Diaion CR-20 per 1 extract
(synthetic resin in which polyamine is introduced into styrene and divinylbenzene copolymer), and at the same time the pH
After adjusting the temperature to 5.5, the mixture was gently stirred at room temperature for 15 minutes and filtered to remove resin particles, yielding hojicha with a good flavor.
実施例 5
半発酵茶(ウーロン茶)7Kgを実施例2の方法
に準じて70℃で抽出し、約11度ブリツクスの抽出
液を得た。この抽出液をPH6.0に調整したのち、
1当り13gのメチルセルロースを3%水溶液と
して抽出液に加え、室温で10分ゆるく撹拌し、凝
集物を遠心分離して除き、色調のよいウーロン茶
を得た。Example 5 7 kg of semi-fermented tea (oolong tea) was extracted at 70° C. according to the method of Example 2 to obtain an extract of approximately 11 degrees Brix. After adjusting this extract to pH6.0,
13 g of methylcellulose was added to the extract as a 3% aqueous solution, stirred gently at room temperature for 10 minutes, and aggregates were removed by centrifugation to obtain oolong tea with good color.
実施例 6
紅茶7Kgを実施例2の方法に準じて7本の60℃
に保持された筒に詰め、メチルセルロースを
0.005%含む50℃の温水でもつて多段式向流抽出
を行ない、約10度ブリツクスの抽出液を得た。次
に抽出液をPH5.3に1Mのクエン酸・クエン酸ナト
リウム緩衝液で調整したのち、遠心分離して懸濁
物を除き、色調のすぐれた紅茶液を得た。Example 6 Seven bottles of 7 kg of black tea were heated at 60°C according to the method of Example 2.
Filled with methyl cellulose in a cylinder held by
Multi-stage countercurrent extraction was performed using hot water at 50°C containing 0.005% to obtain an extract with a thickness of approximately 10°C. Next, the extract was adjusted to pH 5.3 with 1M citric acid/sodium citrate buffer, and then centrifuged to remove suspended matter to obtain black tea liquid with excellent color.
参考例 1
実施例2で得た緑茶飲料1当りデキストリン
150gを加えて、あとは常法により凍結乾燥を行
つた。得られた製品は冷水にも容易に溶解するも
ので、好ましい色調をもち、かつ優れた風味をも
つ即席緑茶用粉末であつた。なお、PH調整は1M
のクエン酸・クエン酸ナトリウム緩衝液で行なわ
れた。Reference example 1 Dextrin per green tea drink obtained in Example 2
150 g was added, and the rest was freeze-dried in a conventional manner. The resulting product was an instant green tea powder that was easily soluble in cold water, had a desirable color tone, and had an excellent flavor. In addition, PH adjustment is 1M
was carried out in citric acid/sodium citrate buffer.
参考例 2
実施例3で得た番茶液を減圧濃縮して約40度ブ
リツクスとし、この液1に対しデキストリン
200g、グリシン30g、グルタミン酸ナトリウム
10g、食塩5gを加えて真空式トレイ乾燥方式で
乾燥し粉末化した。得られた製品を熱水に溶解し
たものは、美しい黄金色を有する風味の良い番茶
液であつた。Reference Example 2 The bancha liquid obtained in Example 3 was concentrated under reduced pressure to about 40 degrees Brix, and dextrin was added to this liquid 1.
200g, glycine 30g, monosodium glutamate
10 g and 5 g of common salt were added, and the mixture was dried and powdered using a vacuum tray drying method. The resulting product dissolved in hot water was a bancha liquid with a beautiful golden color and good flavor.
参考例 3
実施例4で得たほうじ茶を40度ブリツクスまで
減圧濃縮し、濃縮液1に対してデキストリン
200g、グリシン40g、食塩10gを加えて、あと
は常法により噴霧乾燥して粉末ほうじ茶を得た。Reference example 3 The hojicha obtained in Example 4 was concentrated under reduced pressure to 40 degrees Brix, and dextrin was added to 1 part of the concentrate.
200 g, 40 g of glycine, and 10 g of salt were added, and the rest was spray-dried in a conventional manner to obtain powdered hojicha.
参考例 4
実施例5で得たウーロン茶を約37度ブリツクス
まで減圧濃縮し、濃縮液1に対してデキストリ
ン200g、アラニン40g、グルタミン酸ナトリウ
ム10gを加えて、あとは常法により噴霧乾燥して
粉末を得た。この製品を熱水に溶かしたものは、
通常の方法により半発酵茶を熱湯抽出した液より
も美しい黄金色の色調を持つものであつた。Reference Example 4 The oolong tea obtained in Example 5 was concentrated under reduced pressure to about 37 degrees Brix, and 200 g of dextrin, 40 g of alanine, and 10 g of sodium glutamate were added to 1 part of the concentrate, and the rest was spray-dried using a conventional method to form a powder. Obtained. When this product is dissolved in hot water,
The liquid had a more beautiful golden color than the liquid obtained by extracting half-fermented tea with boiling water using the usual method.
参考例 5
実施例6で得た紅茶液を約30度ブリツクスまで
減圧濃縮を行なつた。この濃縮液1に砂糖を加
えて58度ブリツクスとし更に香料を加えて、紅茶
シラツプ液とした。Reference Example 5 The black tea liquid obtained in Example 6 was concentrated under reduced pressure to about 30 degrees Brix. Sugar was added to this concentrate 1 to make it 58 degrees, and flavoring was added to prepare a black tea syrup liquid.
Claims (1)
出液をポリアミド、ポリアミン高分子化合物、酸
化アルミニウム、メチルセルロースから選ばれた
一つ以上のもので処理し、抽出液中の変色原因物
質を減少せしめることを特徴とする茶抽出液の製
法。 2 緑茶、焙焼茶、半発酵茶又は発酵茶が粉茶で
あることを特徴とする特許請求の範囲第1項記載
の茶抽出液の製法。[Scope of Claims] 1. An aqueous extract of green tea, roasted tea, semi-fermented tea, or fermented tea is treated with one or more selected from polyamide, polyamine polymer compound, aluminum oxide, and methylcellulose to obtain an extract. A method for producing a tea extract characterized by reducing the substances that cause discoloration in the tea extract. 2. The method for producing a tea extract according to claim 1, wherein the green tea, roasted tea, semi-fermented tea, or fermented tea is powdered tea.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP10441380A JPS5729250A (en) | 1980-07-31 | 1980-07-31 | Production of tea extract and instant tea of good color |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP10441380A JPS5729250A (en) | 1980-07-31 | 1980-07-31 | Production of tea extract and instant tea of good color |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5729250A JPS5729250A (en) | 1982-02-17 |
| JPS6242579B2 true JPS6242579B2 (en) | 1987-09-09 |
Family
ID=14380002
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP10441380A Granted JPS5729250A (en) | 1980-07-31 | 1980-07-31 | Production of tea extract and instant tea of good color |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5729250A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106900923A (en) * | 2015-12-22 | 2017-06-30 | 云南天士力帝泊洱生物茶集团有限公司 | A kind of method of content of beary metal in reduction instant tea |
Families Citing this family (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS62278948A (en) * | 1986-05-27 | 1987-12-03 | Fuji Debuison Kagaku Kk | Preparation of clear extraction liquid of tea |
| JP4986375B2 (en) * | 2003-11-12 | 2012-07-25 | 三井農林株式会社 | Method for suppressing change in transmittance of containerized tea beverage |
| JP3597859B2 (en) * | 2003-12-22 | 2004-12-08 | 花王株式会社 | Containerized green tea beverage and method for producing the same |
| KR20070026005A (en) * | 2005-09-01 | 2007-03-08 | 카오카부시키가이샤 | Method of Preparation of Purified Green Tea Extract |
| JP5612395B2 (en) * | 2010-08-12 | 2014-10-22 | 三井農林株式会社 | Method for suppressing occurrence of floc in packed tea beverage |
-
1980
- 1980-07-31 JP JP10441380A patent/JPS5729250A/en active Granted
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106900923A (en) * | 2015-12-22 | 2017-06-30 | 云南天士力帝泊洱生物茶集团有限公司 | A kind of method of content of beary metal in reduction instant tea |
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5729250A (en) | 1982-02-17 |
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