JPS61152238A - Production of dried tea in pellet form - Google Patents

Production of dried tea in pellet form

Info

Publication number
JPS61152238A
JPS61152238A JP27976484A JP27976484A JPS61152238A JP S61152238 A JPS61152238 A JP S61152238A JP 27976484 A JP27976484 A JP 27976484A JP 27976484 A JP27976484 A JP 27976484A JP S61152238 A JPS61152238 A JP S61152238A
Authority
JP
Japan
Prior art keywords
mold
extract
tea
frozen
product
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.)
Pending
Application number
JP27976484A
Other languages
Japanese (ja)
Inventor
Kakuji Kobayakawa
小早川 格二
Yukiharu Fujita
藤田 行治
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Amano Jitsugyo Co Ltd
Original Assignee
Amano Jitsugyo Co Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Amano Jitsugyo Co Ltd filed Critical Amano Jitsugyo Co Ltd
Priority to JP27976484A priority Critical patent/JPS61152238A/en
Publication of JPS61152238A publication Critical patent/JPS61152238A/en
Pending legal-status Critical Current

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Abstract

PURPOSE:To obtain a product, by extracting tea with hot water, adding a saccharide to the extracted solution, injecting the solution to a mold, freezing the solution, lyophilizing the frozen extracted material in pellet form, and processing it into granular pellets in a fixed shape. CONSTITUTION:Tea is extracted with hot water, concentrated, blended with a saccharide (preferably dextrin, etc., having low sweetness, etc.), and injected into a mold having a large number of pellet-like dents. Preferably the dents look like cubes with sizes of about 2-5mm per side. The extracted solution is frozen in an injected state in the mold, taken out from the mold, and lyophilized while being in a frozen state.

Description

【発明の詳細な説明】 イ0発明の利用分野 本発明は食品製造業、とシわけて即席飲料製造業の分野
において利用されるべきものである。
DETAILED DESCRIPTION OF THE INVENTION Field of Application of the Invention The present invention is to be used in the food manufacturing industry, particularly in the instant beverage manufacturing industry.

口、従来の技術 従来の即席乾燥茶類の製造方法としては噴霧乾燥法、ド
ラム乾燥法、および凍結乾燥法によるものが知られてい
る。
BACKGROUND OF THE INVENTION Conventional methods for producing instant dried teas include spray drying, drum drying, and freeze drying.

最近の消費者の高級・志向により香味の良好な凍結乾燥
法によるものが需要を伸している。(例えば「乾燥食品
辞典」第336頁(朝食書店、1984年、第1版)を
参照されたい。9 凍結乾燥法により即席乾燥茶類を製造する方法としては
次の二つのものがある。
Due to recent consumers' preference for high-end products, demand for freeze-dried products with good flavor is increasing. (For example, see "Dictionary of Dry Foods," p. 336 (Shokusoku Shoten, 1984, 1st edition).

(A)茶類の抽出液を必要々らば濃縮し固型分濃度を調
整した後に凍結する。通常急速凍結した後にシャーベッ
ト状に一定の粒度の氷片を解砕機により製造しこのもの
を氷結状態のまま凍結乾燥する方法。(前出文献第16
2頁を参照されたい。本法はインスタントコーヒーにお
いて実用化てれているが、特開昭59−21346 号
に記載されているように茶類にも適用しうる。) (B)茶類の抽出液を(A)と同様に調整した後プレー
ト状に凍結し、そのまま凍結−乾燥する。かくして得ら
′れる板状の乾燥物をグラニーレータ−等により粉砕し
、ふるいわけた後に適当な粒度のものを製品とする方法
。(特開昭59−21346 号を参照のこと。)いづ
れの方法においても一定粒度の乾燥物として製品化する
必要がある。これは一般に粒状物の方が粉末状物よりも
粉立ちが々く、吸湿性も少なく取り扱い易いことと、使
用に際しての溶解性が良好なこと、および製品にした場
合にかさが大きくなって商品としての見栄えがすること
による。
(A) If necessary, the tea extract is concentrated to adjust the solid content concentration and then frozen. A method of producing ice chips of a certain size in the form of sherbet using a crusher after rapid freezing, and then freeze-drying this ice while still in its frozen state. (Ibid. Reference No. 16
Please refer to page 2. Although this method has been put to practical use in instant coffee, it can also be applied to tea as described in JP-A-59-21346. ) (B) A tea extract is prepared in the same manner as in (A), frozen in the form of a plate, and freeze-dried as it is. A method in which the plate-shaped dried product thus obtained is crushed using a graniller, etc., and after sieving, a product having an appropriate particle size is obtained. (See JP-A No. 59-21346.) In either method, it is necessary to commercialize the product as a dried product with a constant particle size. This is because granular materials are generally easier to handle than powdered materials, have less hygroscopicity, are easier to handle, have better solubility during use, and have a larger bulk when made into products. It depends on how good it looks.

ハ0発明が解決しようとする問題点 従来技術を実施する場合の問題点としては以下のものが
指摘される。
Problems to be Solved by the Invention The following problems can be pointed out when implementing the prior art.

(A)前述の←)法による場合には抽出液の組成によっ
て凍結点が異なり同様の条件で凍結させると組成のばら
つきにより抽出液の凍結物の硬度に著るしい差が生ずる
。このため解砕の条件設定を変え々くてはならず、同一
粒度の氷片を製造するのが困難となる。
(A) In the case of the above-mentioned ←) method, the freezing point differs depending on the composition of the extract, and when frozen under the same conditions, a significant difference in the hardness of the frozen product of the extract occurs due to variations in the composition. For this reason, it is necessary to change the crushing conditions, making it difficult to produce ice pieces of the same particle size.

特に単一種でなく多種の茶類を同一のプラントにて加工
する場合には凍結条件、解砕条件の切シ換えを行なうの
に熟練を要する。
In particular, when many types of tea are processed in the same plant, skill is required to switch between freezing and thawing conditions.

C)前述の(B)法による場合には簡便に実施しうる利
点のある半面、板状の乾燥物を一定の粒度の製品に粉砕
することは困難であり、必ず規゛格外の粉状物が発生す
る。本発明者等の経験によれば通常10〜2o%程度の
粉状物が発生する。粉状物は抽出液に添加して再使用す
るが、−たん凍結乾燥したものをリサイクルする形とな
りコスト的に無駄が多い。
C) Although method (B) above has the advantage of being easy to carry out, it is difficult to grind a plate-shaped dry product into a product with a constant particle size, and it always produces non-standard powder. occurs. According to the experience of the present inventors, approximately 10-20% of powdery matter is usually generated. The powder is added to the extract and reused, but the freeze-dried product is recycled, which is wasteful in terms of cost.

また、粉状物を造粒により製品化するとなると造粒工程
のだめのスペース、設備が必要となり工場管理上不利と
なる。
Furthermore, if powdered materials are to be made into products by granulation, extra space and equipment are required for the granulation process, which is disadvantageous in terms of factory management.

二9問題点を解決するだめの手段 本発明者等はこれらの問題点をふまえた上で、従来の即
席乾燥茶類とは異なったベレット状の乾燥茶類を製造す
る方法を検討し本発明を完成した。
29 Means for Solving the Problems In view of these problems, the present inventors have studied a method for producing pellet-shaped dried tea products that is different from conventional instant dry tea products, and have developed the present invention. completed.

前述の従来法のいづれにおいても、製造される乾燥茶類
は不定形粒状物であった。本発明においては定形のベレ
ット状の粒状物として製品が得られる。
In all of the conventional methods described above, the dried tea products produced are irregularly shaped granules. In the present invention, the product is obtained in the form of regular pellet-like granules.

定形粒状物の場合には不定形粒状物の場合と異なシ操業
条件に由来する粒度分布の変動がなく包装計量工程にお
ける誤差、かさ密度の変化による製品の外観の変動等の
トラブルを避けることができる。
In the case of regular-shaped granules, unlike the case of irregular-shaped granules, there is no fluctuation in particle size distribution due to operational conditions, and problems such as errors in the packaging and measuring process and changes in product appearance due to changes in bulk density can be avoided. can.

本発明により従来の不定形粒状物の即席茶類と同様の低
吸湿、易溶性、取扱い簡便性を有し、なおかつ従来品に
はなかった規格化された形状のペレツ)状即席茶類を簡
便に製造することができ、また本発明により提供される
製品は形状において新規であるという特徴が存在する。
The present invention enables the production of instant tea products in the form of pellets, which have the same low moisture absorption, easy solubility, and ease of handling as conventional instant tea products made of irregularly shaped particles, and have a standardized shape that was not available in conventional products. The product provided by the invention is characterized by being novel in shape.

本発明は以下のような工程の結合によって実施される。The present invention is carried out by combining the following steps.

(A)茶類を熱水によシ抽出する工程 本工程は従来法に従って実施される。本発明にいう茶類
とは例えば紅茶、せん茶、はうじ茶、ばん茶、ウーロン
茶、麦茶、プアール茶、マチ基、あまちゃづる茶、〈こ
茶、はぶ茶、かき茶、はと麦茶、甘茶等を指称する。
(A) Step of extracting tea with hot water This step is carried out according to a conventional method. The teas referred to in the present invention include, for example, black tea, sencha, haujicha, bancha, oolong tea, barley tea, puerh tea, machiki, amachazuru tea, 〈kocha, habucha, kakicha, pigeon-barley tea, Refers to sweet tea etc.

通常これらの茶類は回分式、あるいは多段抽出法によシ
抽出される。一般的には90℃以上(但し日本茶の場合
には60〜70℃程度が良い。)の熱水を用いて抽出す
る。回分式の場合には茶類の5〜10 倍量程度の熱水
を用いて5〜10分間程度、多段抽出法の場合には同様
の熱水にて1段当り数10 分間〜数時間程度抽出する
These teas are usually extracted using a batch or multi-stage extraction method. Generally, extraction is carried out using hot water of 90°C or higher (however, in the case of Japanese tea, about 60 to 70°C is better). In the case of a batch extraction method, hot water of 5 to 10 times the amount of tea is used for 5 to 10 minutes, and in the case of a multi-stage extraction method, the same amount of hot water is used for several 10 minutes to several hours per stage. Extract.

CB)抽出物を構給する工程 かくして得られる抽出液は必要ならば沈でん法、フカ法
、遠心分離法等の清澄化を施された後、固型分濃度を調
整するために濃縮される。但し本工程は必ずしも必須で
はなく省略しうる場合もあるが、均一の風味の製品を製
造するためにけ必要な場合が多い。また抽出効率の悪い
麦茶、はとむぎ茶については必要な工程である。
CB) Step of preparing the extract The extract thus obtained is clarified, if necessary, by a sedimentation method, a float method, a centrifugation method, etc., and then concentrated to adjust the solid content concentration. However, this step is not necessarily essential and may be omitted in some cases, but is often necessary in order to produce a product with a uniform flavor. This is also a necessary process for barley tea and hatomugi tea, which have poor extraction efficiency.

本工程により抽出液のブリックス度が5〜15 程度に
なるように調整する。
In this step, the Brix degree of the extract is adjusted to about 5 to 15.

(C)抽出液に糖類を添加する工程 固型分調整を受けた抽出液に糖類を添加する。糖類とし
てはデキストリン、麦芽糖、乳糖等の甘味の弱いものが
適当である。糖類は抽出液のブリックス度が20〜30
の範囲になるように添加する。
(C) Step of adding sugars to the extract Saccharides are added to the extract that has undergone solid content adjustment. Suitable sugars include those with weak sweetness such as dextrin, maltose, and lactose. For sugars, the Brix degree of the extract is 20 to 30.
Add so that it falls within the range of .

これらの糖類は凍結乾燥時の風味の散逸を防止するとと
もに、乾燥後のベレy l・状乾燥物に強じん性を付与
するという効果を奏する。添加する糖は抽出液中の固型
分の]−〜3倍程度になるようにする。
These saccharides have the effect of preventing the flavor from dissipating during freeze-drying and imparting toughness to the beret-like dried product after drying. The amount of sugar added should be about 3 times the solid content in the extract.

抽出液のブリックス度が20 を下まわると一般的に乾
燥体の保型性は悪くこわれ易い。しかしブリ。
When the Brix degree of the extract is less than 20, the dry product generally has poor shape retention and is easily broken. But yellowtail.

クス度が30 を十捷わると抽出液の凍結点が著るしく
降下し、通常の凍結条件である−20〜−40℃では凍
結し雛くなる。
When the temperature exceeds 30°C, the freezing point of the extract drops significantly, and the extract freezes and becomes chicks under normal freezing conditions of -20 to -40°C.

抽出液中の固型分の量より添加する糖類の量が少ない場
合には乾燥物の保型性は悪く、3倍を越すと往々にして
溶解性(特に冷水への速溶性)が悪くなる。
If the amount of sugar added is less than the amount of solids in the extract, the shape retention of the dried product will be poor, and if it exceeds three times the amount, the solubility (especially quick solubility in cold water) will often deteriorate. .

(D)抽出液をペレνl・状のくぼみを多数有する型に
注入する工程 糖の添加された抽出液はペレット状のくぼみを多数有す
る型に注入される。
(D) Process of pouring the extract into a mold having a large number of pellet-shaped depressions The extract to which sugar has been added is poured into a mold having a large number of pellet-shaped depressions.

型は通常金属(例えばアルミニウム、ステンレス等、好
ましくはテフロンコーチングを施せばなお良い。)プラ
スチ、クス(例えばポリエチレン、ポリプロピレン、ポ
リスチレン、ポリ酢酸ビニール、アクリル樹脂、ナイロ
ン等により製作されるが、これらの薄板をプレスしてl
・レイを製作しこれを型として使用することもできる。
The mold is usually made of metal (for example, aluminum, stainless steel, etc., preferably coated with Teflon), plastic, or plastic (for example, polyethylene, polypropylene, polystyrene, polyvinyl acetate, acrylic resin, nylon, etc.). Press the thin plate
- You can also make a lei and use it as a mold.

くぼみの形状としては乾燥物を抜き出し易い形状、例え
ば球、ダ円体、円すい体、角すい体の切断体、あるいは
ハツト状、金型等の形状が例示される。
Examples of the shape of the recess include shapes that allow easy removal of the dried material, such as a sphere, a cylindrical shape, a cone, a cut piece of a pyramid, a hat shape, a mold shape, and the like.

大きさとしては一片が2〜5wn程度の立方体、好まし
くは2〜3謳程度の立方体程度の量感を有するものが良
い。
As for the size, one piece should have a cube size of about 2 to 5 wn, preferably a cube of about 2 to 3 pieces.

この程度の形状であればスプーン1〜2杯程度で1カ、
プ分の茶類を復元しうる8またスプーンで計量したり、
計量包装機で包装する場合でも扱い易いさらに乾燥物の
取シ出しを容易化するために離型促進剤、例えば油脂、
可食性ロウ、可食性界面活性剤を型に塗布することも許
容される。
If the shape is like this, 1 to 2 spoons will be enough for 1 cup.
8. You can also measure it with a spoon,
It is easy to handle even when packaging with a weighing and packaging machine.In addition, release accelerators, such as oils and fats, are used to facilitate the removal of dried products.
It is also acceptable to coat the mold with an edible wax or an edible surfactant.

本工程を大規模に実施する場合には多数の型をエンドレ
スに循環させ(例えば金型をチェーンベルトに取りつけ
てスプロケットによシ回転させる。)、金型が循環路上
面に来た時に抽出液を注ぎ、これに密接するスクレーパ
ーの作用(あるいはローラーでも良い。)によって金型
上に残った余剰の液を除去し、次いで循環路上面上に設
置したトンネルフリ−ザーを通過させて凍結せしめる。
When carrying out this process on a large scale, a large number of molds are circulated endlessly (for example, the molds are attached to a chain belt and rotated by a sprocket), and when the molds come to the surface of the circulation path, the extracted liquid The excess liquid remaining on the mold is removed by the action of a scraper (or a roller may be used) in close contact with the mold, and then passed through a tunnel freezer installed on the circulation path surface to be frozen.

トンネルフリーザーを通過し金型が循環路下面に来た時
に金型底面を軽く加熱(例えば赤外線加熱器、熱風等に
より)し金型に接触する凍結部を薄く融解させることに
よって金型より凍結抽出液のペレットを落下せしめる。
When the mold passes through the tunnel freezer and comes to the bottom of the circulation path, the bottom of the mold is lightly heated (e.g. with an infrared heater, hot air, etc.) to thinly thaw the frozen part that comes into contact with the mold, allowing extraction from the mold. Allow the liquid pellets to fall.

落下を促進させるだめに金型にバイブレータ−を接触さ
せて振動を与えると々お良い。
It is a good idea to bring a vibrator into contact with the mold to vibrate it in order to accelerate the fall.

抽出液の注入部、金型上面の余剰液かきとシ部、凍結物
の金型よりのはく離部において発生する余剰液、々いし
はトリ、プは留めに回収し再び使用すれば良い。
Excess liquid, water, or liquid generated at the extraction liquid injection part, the excess liquid scraping part on the upper surface of the mold, and the peeling part of the frozen product from the mold can be collected and used again.

金型への注入部においては常時一定量を金型上に落下供
給せしめる方式でもよいし、金型の動きに同期させて一
定時間のみ供給させる方式を採用してもよい。
In the injection section into the mold, a method may be adopted in which a fixed amount is always dropped onto the mold, or a method in which it is synchronized with the movement of the mold and is supplied only for a fixed period of time may be adopted.

((ホ)抽出液を凍結する工程 連続的に抽出液を金型に注入する場合は(D)において
述べたが、回分式にて各金型に注入する場合には各金型
を架台に多数個固定して凍結室に保存するが・あるいは
トンネルフリーザ中に順次送りこんで凍結する。凍結条
件としては−20〜−40℃のエアープラスト、あるい
はコンタクトフリーザーを用いる(F)凍結された抽出
液を型より取り出す工程型に注入された状態で凍結され
た抽出液は凍結状態のまま型よシ取シ出される。連続式
の装置を用いる場合については(’))において述べだ
が剛直な型の場合にはこれと同様に型面を下にして底面
を軽く加熱すればよい。振動を与えれば良いことは同じ
である薄いトレイを型として用いる場合にはトレイを適
当にたわませることにより容易に離型しうる。
((e) Freezing the extract The process of injecting the extract into the mold continuously was described in (D), but when injecting into each mold batchwise, each mold is placed on a stand. Fix a large number of samples and store them in a freezing chamber, or send them one by one into a tunnel freezer and freeze them.The freezing conditions are -20 to -40°C Air Plast or contact freezer (F) Frozen extract solution The process of removing the liquid from the mold The frozen extract injected into the mold is removed from the mold in a frozen state.As mentioned in (')), when using a continuous type device, it is necessary to use a rigid mold. In that case, you can simply turn the mold side down and lightly heat the bottom. If a thin tray is used as a mold, it is only necessary to apply vibration, and the mold can be easily released by appropriately bending the tray.

(G)凍結物を凍結乾燥する工程 離型されたペレット状の凍結された抽出液は凍結状態の
まま凍結乾燥工程に付される。このため離型工程から凍
結乾燥の仕こみまでは輸送をも含めて凍結ふん囲気下、
好ましくは一り℃〜−15℃にて実施するのが良い。
(G) Step of freeze-drying the frozen product The frozen extract in the form of pellets that has been released from the mold is subjected to a freeze-drying step in a frozen state. For this reason, everything from the mold release process to the freeze-drying process, including transportation, is carried out under a freezing atmosphere.
Preferably, it is carried out at a temperature of 1°C to -15°C.

通常の凍結乾燥の操作に従い凍結物を厚さ1〜2mにト
レー盛りし、これを凍結乾燥機中に仕こんだ後0.5 
Torr 以下(好ましくは0.3 Torr以下)の
減圧下にて乾燥する。この場合に常法に従い被乾燥物が
融解しない範囲内で棚温を上昇せしめ乾燥時間を短縮す
ることは許容されうる。
Following normal freeze-drying operations, the frozen material is placed on a tray to a thickness of 1 to 2 m, and then placed in the freeze dryer.
Dry under reduced pressure of less than Torr (preferably less than 0.3 Torr). In this case, it is permissible to raise the shelf temperature and shorten the drying time within a range that does not melt the material to be dried according to a conventional method.

以上のような工程を経て得られるペレット状の定形粒状
物は各貴公づつ個別包装されるか、ビン、カン、パウチ
等のバルク包装に付されて製品とされる以下に実施例、
実験例を示して本発明を具体的に説明するが本発明の範
囲はこれらのみに限定されない0 ホ、実施例 実施例1 スリランカ産紅茶1 kgを90℃の熱水71にて10
分間抽出し熱時吸引口ヵする。このもののブリックス度
を測定すれば7.4であった。このものを減圧下60℃
 にて濃縮しブリックス度9.6としだ。
The pellet-shaped regular granules obtained through the above steps are packaged individually for each customer or packaged in bulk packaging such as bottles, cans, and pouches to form products.
The present invention will be specifically explained with reference to experimental examples, but the scope of the present invention is not limited to these examples.
Extract for a minute and use the suction port when hot. The Brix degree of this material was measured to be 7.4. This material was heated at 60℃ under reduced pressure.
It was concentrated to a Brix degree of 9.6.

松谷化学工業(株)パインデックス扁2(デキストリン
)、乳糖1水和物の9=1混合物を調製し、熱時に抽出
液差添加してブリックス度を22.3  とした。この
液を冷時に上面の一辺3.5簡の正方形、下面の一辺2
.5ffl+++の正方形、高さ2.5 =の金型のく
ぼみを多数有する厚さ0.3恒程度のポリプロピレンの
トレイに注加し、余剰液をトレイ上面をスクレーパーに
よりそうはすることによって除去した。
A 9=1 mixture of Pine Index 2 (dextrin) manufactured by Matsutani Chemical Industry Co., Ltd. and lactose monohydrate was prepared, and the extract liquid was added to the mixture while it was heated to adjust the Brix degree to 22.3. When this liquid is cooled, a square of 3.5 squares on each side on the top side and 2 squares on each side on the bottom side.
.. The solution was poured into a polypropylene tray with a thickness of approximately 0.3 mm and having a number of mold depressions of 5 ffl +++ square and 2.5 mm high, and the excess liquid was removed by scraping the upper surface of the tray with a scraper.

−30℃のエアプラストの凍結庫に1時間保存し、−5
℃の冷戻室内に−てトレイを軽くたわませることにより
凍結物を離型せしめた。
Store in Airplast freezer at -30℃ for 1 hour, -5
The frozen product was released from the mold by slightly bending the tray in a cooling chamber at .

これをアルミニウム製のトレイに厚さ1.5備程度に盛
り0.3 TOrr  の減圧下にて20 時間凍結乾
燥した。凍結乾燥物は水分含量2.9チであり、手で触
れても特にべたつかず、冷水への易溶性も良好であった
This was placed on an aluminum tray to a thickness of about 1.5 mm and freeze-dried for 20 hours under reduced pressure of 0.3 Torr. The freeze-dried product had a moisture content of 2.9%, was not particularly sticky to the touch, and had good solubility in cold water.

本品2.42を計量し、各貴公を防湿ラミネートフィル
ムにてノ、シックしサンプルとした。
Weighed 2.42 ounces of this product and covered each of them with a moisture-proof laminated film to use as samples.

本品は加速度3G、振動中2諭、振動数500サイクル
/分の振動を10 分間与えても崩壊しなかった。また
水、熱水に落すと数秒程度で崩壊溶解した。
This product did not disintegrate even after 10 minutes of vibration at an acceleration of 3G, 2 vibrations, and a frequency of 500 cycles/min. Also, when dropped into water or hot water, it disintegrated and dissolved within a few seconds.

このもの1食分を160にlの熱水(約90℃)に溶解
し、同様の熱水にて抽出した市販のティーバッグ紅茶を
対照品として20  名のパネラ−を用いて試飲し二点
比較法にて評価した結果本旨を良しとしたものは11名
であった。
One serving of this product was dissolved in 160 liters of hot water (approximately 90°C), and a commercially available tea bag black tea extracted with the same hot water was tasted by a panel of 20 people and compared. As a result of the legal evaluation, 11 people found the main idea to be good.

実施例2 二重になったガラスカラム中にウーロン茶1502を充
てんしたものを5本直列に連結する。端のカラムに90
℃の熱水を供給し、順次カラムを通過させて他端より抽
出液を取り出す。外側には90℃の熱水を通水してカラ
ムを保温し、毎分150g7の流量にて30分間抽出す
ることによシプリックス度10.9 程席のものを得た
。このものを口紙口ヵし、パインデックスA2.75%
麦芽糖水あめ8:2の割合の混合物を75チ固型分濃度
になるように調整した溶液を添加してブリックス度を2
5.0  とした。
Example 2 Five double glass columns filled with oolong tea 1502 were connected in series. 90 in the end column
℃ hot water is supplied, passed through the column in sequence, and the extract is taken out from the other end. Hot water at 90°C was passed through the outside of the column to keep it warm, and extraction was carried out for 30 minutes at a flow rate of 150 g/min to obtain a column with a Siprix degree of about 10.9. Use this as a mouthpiece, and use Paindex A2.75%.
Add a mixture of maltose starch syrup at a ratio of 8:2 to a solution adjusted to have a solid content of 75%, and bring the Brix degree to 2.
It was set at 5.0.

このものを実施例1と同様にトレイに注入し、凍結、離
型、乾燥しペレット状の乾燥ウーロン茶を得た。易溶性
、保型性は実施例1と同様であった。
This product was poured into a tray in the same manner as in Example 1, frozen, released from the mold, and dried to obtain dried oolong tea in the form of pellets. Easy solubility and shape retention were the same as in Example 1.

市販のウーロン茶抽出液と本品の熱水復元物とを実施例
1と同様にテストした。(160@lの、熱水にペレッ
ト2.6fを溶解した。) 。
A commercially available oolong tea extract and a hot water reconstituted product of this product were tested in the same manner as in Example 1. (2.6f of pellets were dissolved in 160@l hot water).

本品を良、しとしたものは9名であった。Nine people rated this product as good or bad.

実施例3 麦茶1 kgを90℃の熱水81にてlO分間煮出し熱
時吸引ロカする。ブリックス度は5.6であった。この
ものを減圧下に濃縮しブリックス度は5.6であった。
Example 3 1 kg of barley tea was boiled in hot water of 90° C. for 10 minutes and then heated under suction. The Brix degree was 5.6. This product was concentrated under reduced pressure and the Brix degree was 5.6.

このものを減圧下に濃縮しブリックス度を7.2とした
。パインデックスA2、麦芽糖水あめ9:1の混合液(
75%濃度)を添加してブリックス度を21.0  に
調整し、実施例1と同様に乾燥した。
This material was concentrated under reduced pressure to have a Brix degree of 7.2. A mixture of Pine Index A2 and maltose starch syrup 9:1 (
75% concentration) to adjust the Brix degree to 21.0, and drying was carried out in the same manner as in Example 1.

本品は水、熱水に落すと数秒程度で崩壊溶解する。実施
例1の崩壊テストによっては崩壊しない。
When dropped into water or hot water, this product disintegrates and dissolves within a few seconds. It does not disintegrate according to the disintegration test of Example 1.

本品2.31を160.7の熱水にて復元し、市販の麦
茶を煮出しだ液との比較試験を実施例1と同様に実施す
れば、本品を良しとしたものは10  名であった実験
例1 実施例2のウーロン茶抽出物を減圧下濃縮しブリックス
度]、8.2  とした。これにデキストリン・麦芽糖
水あめ混合物を添加しブリックス度29.6  とし実
施例2と同様に乾燥した。得られたペレット状物を実施
例1の崩壊試験に付すと32.6  %の粉が発生し実
験例2 実施例1の紅茶抽出液を濃縮せずデキス) IJンを添
加してブリ、クス度を19.0  とした。実施例1と
同様に乾燥しペレット状物を得た。本品を実施例1の崩
壊テストに付すと19.6  %の粉が発生した。
If this product 2.31 was reconstituted with 160.7 hot water and a comparison test was conducted with commercially available barley tea broth in the same manner as in Example 1, 10 people would rate this product as good. The oolong tea extract of Experimental Example 1 and Example 2 was concentrated under reduced pressure to have a Brix degree of 8.2. A dextrin/maltose starch syrup mixture was added to this to give a Brix degree of 29.6, and the mixture was dried in the same manner as in Example 2. When the obtained pellets were subjected to the disintegration test of Example 1, 32.6% of powder was generated. The degree was set to 19.0. It was dried in the same manner as in Example 1 to obtain pellets. When this product was subjected to the disintegration test of Example 1, 19.6% of powder was generated.

実験例3 実施例1の紅茶抽出液を水で希釈し、ブリ、クス度を4
.6としだ。デキストリンを添加してブリ、クス度を2
7.0  とし、同様に乾燥してペレット状物を得た。
Experimental Example 3 The black tea extract of Example 1 was diluted with water, and the yellowtail and cuspidity were adjusted to 4.
.. 6. Add dextrin to increase yellowtail and chestnut content by 2
7.0 and dried in the same manner to obtain pellets.

本品を実施例1と同様の崩壊テストに付すと粉の発生は
なかった。このものを冷水に落すと崩壊溶解するのに1
 、2分間を要する。
When this product was subjected to the same disintegration test as in Example 1, no powder was generated. When you drop this thing into cold water, it disintegrates and dissolves, but 1
, takes 2 minutes.

本品を実施例1のパネル試験に付すと本品を良しとした
ものはいなかった。
When this product was subjected to the panel test of Example 1, no one found this product to be good.

手  続  ネ111   正  書(自発)3、補正
をする者 6、補正により増加する発明の数 0 7、補正の対象  明細書
Procedure 111 Original author (voluntary) 3, Person making the amendment 6, Number of inventions increased by the amendment 0 7, Subject of the amendment Description

Claims (1)

【特許請求の範囲】 次の工程の結合、すなわち、 (A)茶類を熱水にて抽出する工程 (B)糖類を抽出液に添加する工程 (C)ペレット状のくぼみを多数有する型に抽出液を注
入する工程 (D)型に注入された状態で抽出液を凍結する工程(E
)凍結された抽出液を型より取り出す工程(F)型から
取り出されたペレット状の凍結抽出物を凍結状態のまま
凍結乾燥に付す工程 よりなることを特徴とするペレット状乾燥茶類の製造法
[Claims] Combining the following steps: (A) Extracting tea with hot water (B) Adding sugars to the extract (C) Making pellets into a mold with many depressions Step (D) of injecting the extract solution; Step (E) of freezing the extract solution while it is injected into the mold.
) a step of taking out the frozen extract from the mold; and (F) a step of subjecting the frozen extract taken out of the mold to freeze-drying in a frozen state. .
JP27976484A 1984-12-27 1984-12-27 Production of dried tea in pellet form Pending JPS61152238A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP27976484A JPS61152238A (en) 1984-12-27 1984-12-27 Production of dried tea in pellet form

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP27976484A JPS61152238A (en) 1984-12-27 1984-12-27 Production of dried tea in pellet form

Publications (1)

Publication Number Publication Date
JPS61152238A true JPS61152238A (en) 1986-07-10

Family

ID=17615574

Family Applications (1)

Application Number Title Priority Date Filing Date
JP27976484A Pending JPS61152238A (en) 1984-12-27 1984-12-27 Production of dried tea in pellet form

Country Status (1)

Country Link
JP (1) JPS61152238A (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP1437128A1 (en) * 2003-01-07 2004-07-14 Michael Kaufmann Pellet made from a matrix comprising tee as starting material and its method of preparation
WO2007009600A1 (en) * 2005-07-22 2007-01-25 Unilever Plc Beverage precursor and process for manufacture thereof
KR100811680B1 (en) * 2007-02-26 2008-03-11 주식회사 멀베리식품 A freeze drying method for mulberry leaves
US10813368B1 (en) * 2019-10-31 2020-10-27 Gregory Glancy Systems and methods for the preparation of tablets of botanical extracts including tea
WO2022215744A1 (en) 2021-04-08 2022-10-13 ザ コカ・コーラ カンパニー Freeze-dried beverage solidified product

Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP1437128A1 (en) * 2003-01-07 2004-07-14 Michael Kaufmann Pellet made from a matrix comprising tee as starting material and its method of preparation
WO2007009600A1 (en) * 2005-07-22 2007-01-25 Unilever Plc Beverage precursor and process for manufacture thereof
KR100811680B1 (en) * 2007-02-26 2008-03-11 주식회사 멀베리식품 A freeze drying method for mulberry leaves
US10813368B1 (en) * 2019-10-31 2020-10-27 Gregory Glancy Systems and methods for the preparation of tablets of botanical extracts including tea
JP2021069376A (en) * 2019-10-31 2021-05-06 グレゴリー グランシーGregory Glancy Systems and methods for preparation of tablets of botanical extracts including tea
US11700863B2 (en) 2019-10-31 2023-07-18 Gregory Glancy Systems and methods for the preparation of tablets of botanical extracts including tea
EP4030922A4 (en) * 2019-10-31 2023-10-25 Gregory Glancy Systems and methods for the preparation of tablets of botanical extracts including tea
WO2022215744A1 (en) 2021-04-08 2022-10-13 ザ コカ・コーラ カンパニー Freeze-dried beverage solidified product
KR20230165837A (en) 2021-04-08 2023-12-05 더 코카콜라 컴파니 Freeze-dried beverage solids

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