JPS62241A - Production of instant drink - Google Patents

Production of instant drink

Info

Publication number
JPS62241A
JPS62241A JP60137028A JP13702885A JPS62241A JP S62241 A JPS62241 A JP S62241A JP 60137028 A JP60137028 A JP 60137028A JP 13702885 A JP13702885 A JP 13702885A JP S62241 A JPS62241 A JP S62241A
Authority
JP
Japan
Prior art keywords
extract
concentration
starch hydrolyzate
roasted
tea leaves
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.)
Granted
Application number
JP60137028A
Other languages
Japanese (ja)
Other versions
JPH0336491B2 (en
Inventor
Jinichi Sato
仁一 佐藤
Toshiro Kurisu
栗栖 敏郎
Yasuji Takahama
保司 高浜
Hitoshi Hirai
整 平井
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.)
Sato Foods Industries Co Ltd
Original Assignee
Sato Foods Industries 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 Sato Foods Industries Co Ltd filed Critical Sato Foods Industries Co Ltd
Priority to JP60137028A priority Critical patent/JPS62241A/en
Publication of JPS62241A publication Critical patent/JPS62241A/en
Publication of JPH0336491B2 publication Critical patent/JPH0336491B2/ja
Granted legal-status Critical Current

Links

Abstract

PURPOSE:To efficiently produce an instant drink without causing deterioration in quality, e.g. hue or flavor, etc., by adding a starch hydrolyzate to an extract solution of green tea leaves, roasted grains, etc., and concentrating the resultant mixture solution with a semipermeable membrane. CONSTITUTION:A starch hydrolyzate, e.g. acyclic dextrin or cyclic dextrin having 4-10 average polymerization degree or a mixture thereof, in an amount of 10-150% based on the extract component (solid) of an extract is added and mixed with the extract of green tea leaves, roasted grains, roasted beans or medicinal tea leaves, etc. The resultant solution is then passed through a semipermeable membrane, preferably reverse osmosis membrane under temperature control of 15-60 deg.C under high pressure to give a concentrate which is spray-dried as desired.

Description

【発明の詳細な説明】 本発明は紅茶、ウーロン茶、緑茶などの茶菓類の抽出液
、焙煎麦、焙煎はと麦、焙煎コーヒー豆などの焙煎した
穀豆類の抽出液を品質の劣化がなく、且つ効率よく逆浸
透濃縮法により濃縮し、又は更にこの得られ・た濃縮液
を噴霧乾燥することからなるインスタント飲料の製造法
に関するものである。
[Detailed Description of the Invention] The present invention improves the quality of extracts from tea confections such as black tea, oolong tea, and green tea, and extracts from roasted grains such as roasted wheat, roasted pearl barley, and roasted coffee beans. The present invention relates to a method for producing an instant beverage that does not deteriorate and is efficiently concentrated by a reverse osmosis concentration method, or further comprises spray-drying the obtained concentrate.

従来、一般的な液状食品の濃縮には減圧加熱濃縮法、凍
結濃縮法などが利用されて来ている。しかし、これらの
方法は、種々の抽出液を品質の劣化なく、且つ効率よく
濃縮するにはそれぞれの欠点を有している。即ち減圧加
熱濃縮は効率はよいが、風味の変質(特に揮発性成分の
損失)が起こりやすく、凍結濃縮は排出氷晶へのエキス
成分の付着による風味成分の変化及び損失、特に茶類エ
キスの場合は極低温下処理によるタンニン成分などの不
溶化(白濁化)等が起こり、また濃縮の効率も非常に悪
いなどの種々の欠点があった。
Conventionally, methods such as vacuum heating concentration method, freeze concentration method, etc. have been used to concentrate general liquid foods. However, these methods each have their own drawbacks in efficiently concentrating various extracts without deterioration of quality. In other words, although vacuum heating concentration is efficient, flavor deterioration (particularly loss of volatile components) is likely to occur, while freeze concentration is prone to change and loss of flavor components due to adhesion of extract components to discharged ice crystals, especially of tea extracts. In this case, there were various drawbacks such as insolubilization (white turbidity) of tannin components etc. due to extremely low temperature treatment and very poor concentration efficiency.

一方、近年半透膜による液状食品の濃縮方法が採用され
るようになってきているが、実際に紅茶などの抽出液を
逆浸透濃縮法により濃縮してみると、濃縮に際しての温
度は濃縮効率を考慮すると比較的高くしなければならず
、又濃縮に相当の時間を要するので濃縮中品質が劣化し
やすく、且つ従来常用されつつある乳清などの膜濃縮に
比較して濃縮効率が悪く、また濃縮中に濃縮効率が低下
して行くことなどの欠点があることが判った。
On the other hand, in recent years, methods for concentrating liquid foods using semi-permeable membranes have been adopted, but when actually concentrating extracts such as black tea using the reverse osmosis concentration method, it was found that the temperature during concentration had a significant effect on the concentration efficiency. Considering this, it has to be relatively high, and since it takes a considerable amount of time to concentrate, the quality tends to deteriorate during concentration, and the concentration efficiency is poor compared to membrane concentration of whey, etc., which has been commonly used in the past. It has also been found that there are drawbacks such as the concentration efficiency decreasing during concentration.

そこで1本発明者らは紅茶などの抽出液の膜濃縮法によ
る濃縮の欠点を改善すべく研究を進めていたところ、茶
類や焙煎殻豆類の抽出液に澱粉加水分解物を添加溶解せ
しめて後、これを濃縮すれば濃縮中の品質劣化がなく、
且つ、意外にも濃縮効率がむしろ向上するという知見を
得た。
Therefore, the present inventors were conducting research to improve the drawbacks of the membrane concentration method for extracts of black tea, etc., and discovered that starch hydrolyzate was added and dissolved in extracts of tea and roasted shell beans. After that, if this is concentrated, there will be no quality deterioration during concentration.
Moreover, it was surprisingly found that the concentration efficiency was actually improved.

本発明はこのような知見によって完成されたものであり
、逆浸透濃縮装置内に茶類や焙煎した殻豆類の抽出液を
高圧下に、且つ温度制御下に流過させて濃縮するに際し
て、濃縮前の抽出液に澱粉加水分解物を溶解して含有せ
しめることによって、濃縮効率が極めて向上し、且つ、
抽出液の品質劣化(色調の変化、風味の変化)を防止で
きる極めて新規で経済的な濃縮法を発明するに至ったも
のである。
The present invention was completed based on such knowledge, and when concentrating an extract of tea or roasted shell beans through a reverse osmosis concentrator under high pressure and temperature control, By dissolving and containing the starch hydrolyzate in the extract before concentration, the concentration efficiency is greatly improved, and
This led to the invention of an extremely novel and economical concentration method that can prevent quality deterioration (changes in color and flavor) of the extract.

本発明において処理される抽出液としては緑茶・はうじ
茶・ウーロン茶・紅茶等の茶菓類及びコーヒー豆・ココ
ア豆・大麦・はと麦等の焙煎狡豆類の水抽出液、またこ
れらに準するアマチャヅル・カキツバ・タコ・ゲンノシ
ョウコ・昆布・椎茸などの薬用茶類の水抽出液にも広く
採用されるものである。
Extracts to be treated in the present invention include water extracts of tea sweets such as green tea, spinach tea, oolong tea, and black tea, and aqueous extracts of roasted black beans such as coffee beans, cocoa beans, barley, and pearl barley; It is also widely used for water extracts of medicinal teas such as Jiaogulan, Kakitsuba, Octopus, Gennoshoko, Kelp, and Shiitake mushrooms.

用いる澱粉加水分解物としては平均重合度4〜10の非
環状デキストリン及び環状デキストリン、又はこれらの
混合物が好んで使用されるものである。非環状デキスト
リンにあっては平均重合度が10以上になると抽出液の
種類及び添加量にもよるが濃縮中に粘度が高くなり、濃
縮に悪影響を与え。
The starch hydrolyzate used is preferably an acyclic dextrin or a cyclic dextrin having an average degree of polymerization of 4 to 10, or a mixture thereof. When the average degree of polymerization of acyclic dextrin is 10 or more, the viscosity increases during concentration, depending on the type of extract and the amount added, which adversely affects concentration.

濃縮効率の向上が期待出来なくなり、一方、平均重合度
が4以下になるとその効果は殆どみられなくなる。
No improvement in concentration efficiency can be expected, and on the other hand, if the average degree of polymerization is 4 or less, the effect will hardly be seen.

また、用いる澱粉加水分解物の量は上記抽出液に含有さ
れる溶出エキス分(固形分)量に対しておおよそ10〜
150%重量添加するものであり、抽出液の種類及び澱
粉加水分解物の質にもよるが、おおよそ10%以下では
濃縮効率の向上が殆ど認められず、一方150%以上で
は粘度が上がるなどして濃縮効率の向上が期待出来なく
なる。
In addition, the amount of starch hydrolyzate used is approximately 10 to 10% of the amount of eluted extract (solid content) contained in the above extract.
It is added by 150% by weight, and it depends on the type of extract and the quality of starch hydrolyzate, but if it is less than 10%, there will be almost no improvement in concentration efficiency, while if it is more than 150%, the viscosity will increase. Therefore, no improvement in concentration efficiency can be expected.

また、抽出液への澱粉加水分解物の添加方法は抽出に際
して用いる水にあらかじめ添加溶解しておいてもよく、
また抽出液を得てから後に添加溶解してもよい。
In addition, the starch hydrolyzate may be added to the extract by adding and dissolving it in the water used for extraction in advance.
Alternatively, it may be added and dissolved after obtaining the extract.

本発明の濃縮処理には、抽出液に澱粉加水分解物を含有
せしめた混溶液を半透膜内に高圧下に流過せしめる方法
がとられる。具体例としては、混溶液を15℃〜60℃
の温度制御下に逆浸透濃縮装置内に加圧下に流通せしめ
る方法があげられる。半透膜としては逆浸透膜が好まし
く、処理温度は15℃〜60℃が好ましい。60℃を越
えると品質の劣化が起りやすくなり、また、 15℃を
下廻ると濃縮効率が落ちてくるので好ましくない。
The concentration treatment of the present invention employs a method in which a mixed solution containing a starch hydrolyzate in the extract is passed through a semipermeable membrane under high pressure. As a specific example, the mixed solution is heated to 15°C to 60°C.
One example is a method in which the water is allowed to flow under pressure in a reverse osmosis concentrator under temperature control. The semipermeable membrane is preferably a reverse osmosis membrane, and the treatment temperature is preferably 15°C to 60°C. If the temperature exceeds 60°C, quality deterioration tends to occur, and if the temperature falls below 15°C, the concentration efficiency decreases, which is not preferable.

本発明の方法によって得られる濃縮物はこれを冷水又は
温水に溶解すれば即席のインスタント飲料となるもので
あり、更にこの得られた固形分濃度(澱粉加水分解物を
含む)がおおよそ20%tOW%以上の濃縮物を噴霧乾
燥すれば、濃縮前の希薄な抽出液を乾燥するのに比較し
て、揮発性成分の揮散が非常に少なく、また効率よく乾
燥できるので風味の優れたインスタント紅茶、インスタ
ント煎茶、インスタント麦茶などのインスタント飲料類
を製出可能なものである。
The concentrate obtained by the method of the present invention becomes an instant beverage when dissolved in cold or hot water, and furthermore, the solid content concentration (including starch hydrolyzate) obtained is approximately 20% tOW. % or more concentrate, compared to drying a dilute extract before concentration, there is very little volatilization of volatile components and it can be dried efficiently, resulting in instant black tea with excellent flavor. It is possible to produce instant beverages such as instant sencha and instant barley tea.

本発明を試験例で説明すると次の通りである。The present invention will be explained using test examples as follows.

なお、ここで単に固形分濃度という場合は、澱粉加水分
解物を含む全固形分濃度を意味している。
In addition, when it is simply referred to as solid content concentration here, it means the total solid content concentration including starch hydrolyzate.

試験例 (イ)紅茶葉55kgに対して60℃の温水400Qを
加え、攪拌しながら60℃、30分間の条件で抽出し、
圧搾濾過し、品質が劣化しないように10℃に冷却して
、エキス分(固形分)濃度の4.2w/%1%の紅茶抽
出液390kgを得た。
Test Example (a) Add 400Q of 60°C warm water to 55kg of black tea leaves and extract at 60°C for 30 minutes while stirring,
The mixture was compressed and filtered, and cooled to 10° C. to prevent quality deterioration, to obtain 390 kg of black tea extract having an extract (solid content) concentration of 4.2 w/% and 1%.

(ロ)次にこの得られた抽出液を2分割して、一方は澱
粉加水分解物を添加することなく(これを紅茶抽出液A
とする。液量195kg)、もう一方に澱粉加水分解物
(日本食品化工(株)製、平均重合度5の非環状デキス
トリン60%、環状デキストリン15%、水分25%の
、もの)5kgを添加溶解したもの(これを紅茶抽出液
Bとする。液量200kg)の各々の抽出液を調製した
(b) Next, this obtained extract was divided into two, and one was divided into two without adding starch hydrolyzate (this was divided into black tea extract A).
shall be. 195 kg of liquid) and 5 kg of starch hydrolyzate (manufactured by Nihon Shokuhin Kako Co., Ltd., containing 60% acyclic dextrin, 15% cyclic dextrin, and 25% water with an average degree of polymerization of 5) was added and dissolved in the other. (This is referred to as black tea extract B. Liquid amount: 200 kg) were prepared.

(ハ)この調製された各々の抽出液を40℃に加温し、
逆浸透濃縮装置を用いて、逆浸透膜(日東電工(株)製
、スパイラル型、NTR−7250、膜面積2m2)に
30kg/cI112の加圧下に流量10Q/winで
流過させ、抽出液Aを約35kgになるまで、抽出液B
は約40kgになるまで濃縮したが、濃縮過程における
透過水量と固形分濃度との関係を第1図に、濃縮に要し
た時間及び脱水量などを表1に、また各々の得られた濃
縮物の品質(色・香・味)をa祭した結果を表1に示し
た。なお1色・香・味の品質については濃縮前の抽出液
(10℃に冷却し保存したもの)、抽出液Aの濃縮物及
び抽出液Bの濃縮物を紅茶エキス分が0.4%になるよ
うに水で溶解したものについて比較した。
(c) Warming each of the prepared extracts to 40°C,
Using a reverse osmosis concentrator, the extract A was passed through a reverse osmosis membrane (manufactured by Nitto Denko Corporation, spiral type, NTR-7250, membrane area 2 m2) under a pressure of 30 kg/cI112 at a flow rate of 10 Q/win. until it weighs about 35 kg, and add extract B.
Figure 1 shows the relationship between the amount of permeated water and the solid content concentration during the concentration process, and Table 1 shows the time required for concentration and the amount of water removed. Table 1 shows the results of evaluating the quality (color, aroma, taste) of Regarding the quality of color, aroma, and taste, the extract before concentration (cooled and stored at 10°C), extract A concentrate, and extract B concentrate were used with a black tea extract content of 0.4%. A comparison was made of those dissolved in water.

表1 この試験結果より判るように、常識的には浸透圧が高く
なっている筈の抽出液Bの方が濃縮効率が低下すべきで
あるのに対して、逆に濃縮効率は高まっており、しかも
その差は非常に大きい。また、品質面では抽出液Aの方
が色調及び香味共に変質したのに対して、抽出液Bの方
は品質の劣化が殆ど認められなかった。このような効果
は茶菓や焙煎奴豆類から溶出される種々の複雑な構成成
分であるエキス分を混合溶解した澱粉加水分解物分子が
包み込むか、またはこれらが会合するために起こるので
はないかと推論される。
Table 1 As can be seen from this test result, the concentration efficiency should be lower for extract B, which should have a higher osmotic pressure according to common sense, but on the contrary, the concentration efficiency was higher. , and the difference is huge. In addition, in terms of quality, extract A had a change in both color tone and flavor, whereas extract B showed almost no deterioration in quality. This effect may be caused by the encapsulation or association of starch hydrolyzate molecules mixed with extracts, which are various complex components eluted from tea confections and roasted beans. It is inferred.

実施例1 60℃の温水9,400Qに澱粉加水分解物(商品名、
セルデックスCH−20、日本食品化工(株)製、平均
重合度5の非環状デキストリン60%、環状デキストリ
ン15%、水分25%からなるもの) 500kgとβ
型−環状デキストリン(商品名、セルデックスN、日本
食品加工(株)製、水分10%のもの) 50kgとを
添加溶解し、これに煎茶2,000kgを加え、60℃
、30分間の条件で抽出し固形分濃度8.7w/v%の
抽出液9,000kgを得た。この抽出液中の茶菓から
の溶出エキス分はおおよそ4.5w/w%であり、添加
された澱粉加水分解物はおおよそ4.2w/w%含有さ
れるものである。
Example 1 Starch hydrolyzate (trade name,
Celldex CH-20, manufactured by Nihon Shokuhin Kako Co., Ltd., consisting of 60% acyclic dextrin with an average degree of polymerization of 5, 15% cyclic dextrin, and 25% water) 500 kg and β
Type: Add and dissolve 50 kg of cyclic dextrin (trade name, Seldex N, manufactured by Nihon Shokuhin Kogyo Co., Ltd., water content 10%), add 2,000 kg of Sencha to this, and heat at 60°C.
, for 30 minutes to obtain 9,000 kg of an extract having a solid content concentration of 8.7 w/v%. The content of the eluted extract from the tea confectionery in this extract was approximately 4.5 w/w%, and the added starch hydrolyzate was approximately 4.2 w/w%.

次にこの得られた抽出液を72fl+2の膜面積をもつ
スパイラル型逆浸透膜(日東電工(株)製、NTR−7
250)を備えた濃縮装置を用いて液温を35℃に保持
しながら、加圧30kg/cm2の条件で固形分が30
%になるまで濃縮し、濃縮物2,600kgを得た。濃
縮に要した時間は6時間であり、澱粉加水分解物を添加
しないで同一条件で抽出した抽出液を同一条件で濃縮し
たものに対して、その濃縮効率は1.4倍であった。ま
た濃縮前の抽出液に比較して、その色調、香、味は殆ど
変化していなかった。
Next, this obtained extract was applied to a spiral reverse osmosis membrane (manufactured by Nitto Denko Corporation, NTR-7) having a membrane area of 72fl+2.
Using a concentrator equipped with 250), the solid content was reduced to 30 kg/cm2 while maintaining the liquid temperature at 35°C.
% to obtain 2,600 kg of concentrate. The time required for concentration was 6 hours, and the concentration efficiency was 1.4 times that of an extract extracted under the same conditions without adding starch hydrolyzate and concentrated under the same conditions. Furthermore, compared to the extract before concentration, its color tone, aroma, and taste were almost unchanged.

更に、この得られた濃縮物2,600kgを噴霧乾燥機
を用いてチャンバ一温度87℃の条件で噴霧乾燥したと
ころ、約780kgの紅茶エキス乾燥物を得たが、この
ものは乾燥による風味の劣化がなく、温水又は冷水に溶
解すれば優れた風味の紅茶となるものである。
Furthermore, when 2,600 kg of this obtained concentrate was spray-dried using a spray dryer at a chamber temperature of 87°C, approximately 780 kg of dried black tea extract was obtained, but this product had no flavor due to drying. It does not deteriorate, and when dissolved in hot or cold water, it becomes black tea with excellent flavor.

実施例2 焙煎し割砕した大麦’350kgを75℃の温水2,4
50fiで40分間抽出し、固形分濃度約4.8%の麦
茶抽出液2.300kgを得た。次に得られた抽出液の
半分(1,150kg)を膜面積72II12の逆浸透
膜(日東電工(株)製、NTR−7250)を用いて、
液温40℃、圧力30kg/clの条件で、固形分濃度
25%(脱水量約930kg)まで逆浸透濃縮したとこ
ろ、60分かかった。一方残りの半分(1,150kg
)は澱粉加水分解物(商品名、グリスターP、松谷化学
(株)製、平均重合度6.3、水分5%) 20kgを
添加溶解した後、同条件で固形分濃度31%(脱水量約
930kg)まで逆浸透濃縮したところ約40分かかっ
た。
Example 2 350 kg of roasted and crushed barley was heated to 75° C.
Extraction was carried out at 50fi for 40 minutes to obtain 2.300 kg of barley tea extract having a solid content concentration of approximately 4.8%. Next, half of the obtained extract (1,150 kg) was transferred using a reverse osmosis membrane (manufactured by Nitto Denko Corporation, NTR-7250) with a membrane area of 72II12.
Concentration by reverse osmosis to a solid content concentration of 25% (dehydrated amount: about 930 kg) took 60 minutes under conditions of a liquid temperature of 40° C. and a pressure of 30 kg/cl. Meanwhile, the remaining half (1,150 kg)
) is a starch hydrolyzate (trade name, Glister P, manufactured by Matsutani Kagaku Co., Ltd., average degree of polymerization 6.3, water 5%). It took about 40 minutes to concentrate by reverse osmosis to 930 kg).

両濃縮液の風味を比較したところ、澱粉加水分解物を添
加したものの方が香りが強かった。
When the flavors of both concentrates were compared, the one containing starch hydrolyzate had a stronger aroma.

【図面の簡単な説明】[Brief explanation of the drawing]

第1図は試験例で、抽出液と澱粉加水分解物添加抽出液
の逆浸透圧濃縮におけるそれぞれの透過水量を示す図で
ある。 代理人 弁理士 戸 1)親 男 第  1   図 固形分溝度/、(W/W)
FIG. 1 is a test example showing the amount of permeated water in reverse osmotic concentration of an extract and a starch hydrolyzate-added extract. Agent: Patent Attorney 1) Parent: Male No. 1 Diagram: Solid content /, (W/W)

Claims (4)

【特許請求の範囲】[Claims] (1)茶葉類、焙煎穀類、焙煎豆類、薬用茶類などの抽
出液に澱粉加水分解物を含有せしめ、得られた混溶液を
半透膜内に高圧下に流過せしめて濃縮することを特徴と
するインスタント飲料の製造法。
(1) Add starch hydrolyzate to the extract of tea leaves, roasted grains, roasted beans, medicinal teas, etc., and concentrate the resulting mixed solution by flowing it under high pressure through a semipermeable membrane. A method for producing an instant beverage characterized by:
(2)澱粉加水分解物が平均重合度4〜10の非環状デ
キストリン又は環状テキストリン、もしくはこれらの混
合物である特許請求の範囲第1項記載のインスタント飲
料の製造法。
(2) The method for producing an instant beverage according to claim 1, wherein the starch hydrolyzate is an acyclic dextrin or a cyclic textrin having an average degree of polymerization of 4 to 10, or a mixture thereof.
(3)澱粉加水分解物を抽出液のエキス成分(固形分)
に対して10〜150%含有せしめる特許請求の範囲第
1項及び第2項記載のインスタント飲料の製造法。
(3) Extract component (solid content) of starch hydrolyzate
The method for producing an instant beverage according to claims 1 and 2, wherein the instant beverage is contained in an amount of 10 to 150%.
(4)得られる該抽出液の濃縮物を噴霧乾燥することか
らなる特許請求の範囲第1、第2及び第3項記載のイン
スタント飲料の製造方法。
(4) A method for producing an instant beverage according to claims 1, 2, and 3, which comprises spray-drying the obtained concentrate of the extract.
JP60137028A 1985-06-25 1985-06-25 Production of instant drink Granted JPS62241A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP60137028A JPS62241A (en) 1985-06-25 1985-06-25 Production of instant drink

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP60137028A JPS62241A (en) 1985-06-25 1985-06-25 Production of instant drink

Publications (2)

Publication Number Publication Date
JPS62241A true JPS62241A (en) 1987-01-06
JPH0336491B2 JPH0336491B2 (en) 1991-05-31

Family

ID=15189155

Family Applications (1)

Application Number Title Priority Date Filing Date
JP60137028A Granted JPS62241A (en) 1985-06-25 1985-06-25 Production of instant drink

Country Status (1)

Country Link
JP (1) JPS62241A (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS63237739A (en) * 1987-03-25 1988-10-04 Kimura Koohiiten:Kk Concentration and production of coffee extract solution
JP2004121135A (en) * 2002-10-04 2004-04-22 Takara Shuzo Co Ltd Liquefied product of rice and method for producing the same
JP2008136367A (en) * 2006-11-30 2008-06-19 Asahi Soft Drinks Co Ltd Tea beverage
JP2012120447A (en) * 2010-12-06 2012-06-28 Kao Corp Flavor improver
JP2017063787A (en) * 2015-09-28 2017-04-06 花王株式会社 Packed beverage

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
AU2020260801A1 (en) 2019-04-26 2021-12-23 Suntory Holdings Limited Powder composition

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS63237739A (en) * 1987-03-25 1988-10-04 Kimura Koohiiten:Kk Concentration and production of coffee extract solution
JP2004121135A (en) * 2002-10-04 2004-04-22 Takara Shuzo Co Ltd Liquefied product of rice and method for producing the same
JP2008136367A (en) * 2006-11-30 2008-06-19 Asahi Soft Drinks Co Ltd Tea beverage
JP2012120447A (en) * 2010-12-06 2012-06-28 Kao Corp Flavor improver
JP2017063787A (en) * 2015-09-28 2017-04-06 花王株式会社 Packed beverage

Also Published As

Publication number Publication date
JPH0336491B2 (en) 1991-05-31

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