JP5800329B2 - Instant tea and method for producing the same - Google Patents
Instant tea and method for producing the same Download PDFInfo
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- JP5800329B2 JP5800329B2 JP2010231073A JP2010231073A JP5800329B2 JP 5800329 B2 JP5800329 B2 JP 5800329B2 JP 2010231073 A JP2010231073 A JP 2010231073A JP 2010231073 A JP2010231073 A JP 2010231073A JP 5800329 B2 JP5800329 B2 JP 5800329B2
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- 238000004519 manufacturing process Methods 0.000 title claims description 14
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- 238000000605 extraction Methods 0.000 claims description 57
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- 238000000034 method Methods 0.000 claims description 24
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- 238000010298 pulverizing process Methods 0.000 claims description 3
- 244000269722 Thea sinensis Species 0.000 description 93
- 235000013616 tea Nutrition 0.000 description 76
- 235000009569 green tea Nutrition 0.000 description 26
- 235000006468 Thea sinensis Nutrition 0.000 description 25
- 239000000796 flavoring agent Substances 0.000 description 23
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- 241000209219 Hordeum Species 0.000 description 22
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- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 18
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- 239000000047 product Substances 0.000 description 11
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- 239000008107 starch Substances 0.000 description 7
- 235000005206 Hibiscus Nutrition 0.000 description 6
- 235000007185 Hibiscus lunariifolius Nutrition 0.000 description 6
- 244000284380 Hibiscus rosa sinensis Species 0.000 description 6
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- CIWBSHSKHKDKBQ-JLAZNSOCSA-N Ascorbic acid Chemical compound OC[C@H](O)[C@H]1OC(=O)C(O)=C1O CIWBSHSKHKDKBQ-JLAZNSOCSA-N 0.000 description 2
- 240000006914 Aspalathus linearis Species 0.000 description 2
- 239000003125 aqueous solvent Substances 0.000 description 2
- 235000020279 black tea Nutrition 0.000 description 2
- 235000021329 brown rice Nutrition 0.000 description 2
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- 244000215068 Acacia senegal Species 0.000 description 1
- 108010076119 Caseins Proteins 0.000 description 1
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- 229920000084 Gum arabic Polymers 0.000 description 1
- 235000004347 Perilla Nutrition 0.000 description 1
- 244000124853 Perilla frutescens Species 0.000 description 1
- 108010064851 Plant Proteins Proteins 0.000 description 1
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- 239000003963 antioxidant agent Substances 0.000 description 1
- 235000006708 antioxidants Nutrition 0.000 description 1
- -1 ascorbic acid Chemical class 0.000 description 1
- 229960005070 ascorbic acid Drugs 0.000 description 1
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- 239000011668 ascorbic acid Substances 0.000 description 1
- 150000001720 carbohydrates Chemical class 0.000 description 1
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- BECPQYXYKAMYBN-UHFFFAOYSA-N casein, tech. Chemical compound NCCCCC(C(O)=O)N=C(O)C(CC(O)=O)N=C(O)C(CCC(O)=N)N=C(O)C(CC(C)C)N=C(O)C(CCC(O)=O)N=C(O)C(CC(O)=O)N=C(O)C(CCC(O)=O)N=C(O)C(C(C)O)N=C(O)C(CCC(O)=N)N=C(O)C(CCC(O)=N)N=C(O)C(CCC(O)=N)N=C(O)C(CCC(O)=O)N=C(O)C(CCC(O)=O)N=C(O)C(COP(O)(O)=O)N=C(O)C(CCC(O)=N)N=C(O)C(N)CC1=CC=CC=C1 BECPQYXYKAMYBN-UHFFFAOYSA-N 0.000 description 1
- 235000021240 caseins Nutrition 0.000 description 1
- 150000001765 catechin Chemical class 0.000 description 1
- ADRVNXBAWSRFAJ-UHFFFAOYSA-N catechin Natural products OC1Cc2cc(O)cc(O)c2OC1c3ccc(O)c(O)c3 ADRVNXBAWSRFAJ-UHFFFAOYSA-N 0.000 description 1
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- 229910021641 deionized water Inorganic materials 0.000 description 1
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- 229940094952 green tea extract Drugs 0.000 description 1
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- 238000000227 grinding Methods 0.000 description 1
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Description
本発明は、インスタント茶及びその製造方法に関し、特に、複数の乾燥方法から得られた茶類乾燥粉末を組み合わせたインスタント茶とその製造方法に関する。 The present invention relates to an instant tea and a method for producing the same, and more particularly to an instant tea obtained by combining tea dry powders obtained from a plurality of drying methods and a method for producing the instant tea.
水またはお湯を注ぐだけで飲むことが出来るインスタント茶は、通常の喫茶法で飲むお茶に比べ簡便に飲用できるものとして、様々なものが開発されている。 Various types of instant tea that can be drunk simply by pouring water or hot water have been developed as those that can be drunk more easily than tea that is drunk by the ordinary tea method.
なお、本発明において、「インスタント茶」とは、紅茶、ウーロン茶、緑茶、ほうじ茶などの茶葉類、麦、はと麦、玄米などの穀物茶類、プアール、ルイボスなどの健康茶類などを抽出、濃縮、乾燥、造粒などによって製造し、水またはお湯を注ぐだけで飲むことが出来るインスタント茶などに限らず、シソ、ウメ、ハーブなど、種々の材料を抽出、濃縮、乾燥、造粒などによって製造し、水またはお湯を注ぐだけで飲むことが出来るインスタント茶に類似している食品を含むものである。 In the present invention, `` instant tea '' is extracted tea leaves such as black tea, oolong tea, green tea, roasted tea, grain teas such as wheat, hato wheat, brown rice, health teas such as puer, rooibos, It is manufactured by concentration, drying, granulation, etc. Not only instant tea that can be drunk just by pouring water or hot water, but also various materials such as perilla, plum, herb etc. extracted, concentrated, dried, granulation etc. Includes foods that are similar to instant teas that can be made and drunk just by pouring water or hot water.
インスタント茶を製造する過程(抽出、濃縮、乾燥、造粒)では、その香気成分が揮散したり或いは損失するといった問題があり、特に茶類エキスの乾燥粉末化工程における香気成分の揮散は著しい。 In the process of producing instant tea (extraction, concentration, drying, granulation), there is a problem that the aroma component is volatilized or lost, and in particular, the aroma component is volatilized in the dry powdering process of tea extracts.
インスタント茶類の乾燥工程には通常、噴霧乾燥、ドラムドライヤ、真空ベルト乾燥、フリーズドライ等の乾燥方法が存在するが、どの乾燥方法においても香気成分の損失を免れることは難しく、そのため最終工程として茶葉の粉砕品や香料を添加、混合することで、失われた香気成分や風味を付与することが多い。 There are usually drying methods such as spray drying, drum dryer, vacuum belt drying, freeze drying, etc. in the drying process of instant teas, but it is difficult to avoid loss of aroma components in any drying method, so as a final process By adding and mixing tea leaf pulverized products and flavors, lost flavor components and flavors are often added.
しかし、最終工程での粉砕品や香料の添加ではあくまで風味、香りの補強としての効果は望めるものの、表面的な印象が強く本来のお茶が有する風味、香りの厚み、深みといった部分を再現するのは難しい。 However, the addition of pulverized products and fragrances in the final process can be expected to have an effect on flavor and fragrance, but the surface impression is strong and the original tea flavor, fragrance thickness and depth are reproduced. Is difficult.
また粉砕品については製造面において粉体類との分散性や加熱による風味の低減、変色といった課題、問題点もある。 In addition, the pulverized product has problems and problems such as dispersibility with powders, reduction of flavor by heating, and discoloration.
このような課題に関して、特許文献1には、穀物茶類、健康茶類、ハーブ類の抽出液を逆浸透圧濃縮するにあたり、第一段階として食塩除去率が10%〜60%のルーズRO膜にて濃縮し、得られる透過水を、第二段階として食塩除去率が93%〜100%のRO膜にて濃縮し、次に濃縮液を乾燥するにあたっては、第一段階の濃縮液は揮発性成分の保持が良い乾燥方法で、また第二段階の濃縮液は乾燥効率の良い乾燥方法を用いて別々に乾燥し、さらに、第一段階の濃縮液の乾燥品と第二段階の濃縮液の乾燥品を混合する茶類エキス粉末の製造方法が提案されている。これによって、茶類エキスに含まれる揮発性成分を保持した茶類エキス粉末を、効率よく、且つ乾燥時のエネルギーコストを抑え、経済的に得ることができるとされている。 Regarding such problems, Patent Document 1 discloses a loose RO membrane having a salt removal rate of 10% to 60% as a first step in concentrating the extract of cereal tea, healthy tea and herbs by reverse osmotic pressure. In the second step, the permeate obtained is concentrated on a RO membrane having a salt removal rate of 93% to 100%, and then the concentrated solution is volatilized. The second stage concentrate is dried separately using a drying method with good drying efficiency, and the second stage concentrate is further dried. A method for producing a tea extract powder in which a dried product is mixed has been proposed. Thereby, it is said that the tea extract powder retaining the volatile components contained in the tea extract can be obtained efficiently and economically with reduced energy costs during drying.
そこで、本発明では通常の喫茶法で得られる茶湯と殆ど同様の風味を有するインスタント茶を得ることを目的にしている。 Therefore, the present invention aims to obtain an instant tea having a flavor almost the same as that of a tea bath obtained by a normal tea method.
本願の発明者等は、茶類抽出液を乾燥粉末化するに際し、その乾燥方法の違いにより損失する風味が変わることに着目し、異なる乾燥方法により得られた複数の茶類乾燥粉末を組み合わせることにより、それぞれが損失した風味を補うことで通常の喫茶法で得られる茶湯と殆ど同様の風味を有するインスタント茶を製造できることを見い出し、本発明に到達した。 The inventors of the present application pay attention to the fact that the flavor that is lost due to the difference in the drying method changes when the tea extract is made into a dry powder, and combine a plurality of tea dry powders obtained by different drying methods. Thus, it has been found that instant tea having almost the same flavor as tea water obtained by a normal tea method can be produced by supplementing the flavor lost by each, and the present invention has been achieved.
すなわち、本願の発明者等は、スプレードライヤー、ドラムドライヤーなど様々な乾燥方法により得られる茶類乾燥粉末を混合することで独特な風味を有したインスタント茶類を製造する方法を見い出し、本発明に到達したのである。 That is, the inventors of the present application have found a method for producing instant teas having a unique flavor by mixing dry tea powders obtained by various drying methods such as spray dryers and drum dryers. It has been reached.
請求項1記載の発明は、
原料から抽出液を得る抽出工程と、前記抽出液を乾燥粉末化する乾燥工程と、その後の混合及び/又は造粒工程を経てインスタント茶を製造する方法であって、
前記原料について、15℃より高く40℃以下の温度範囲である低温領域における抽出温度で前記抽出工程を行い、
前記低温領域における抽出温度で前記抽出工程を行う前記原料と同一の原料について、40℃より高く80℃以下の温度範囲である中間温度領域における抽出温度で前記抽出工程を行い、
前記低温領域における抽出温度で前記抽出工程を行う前記原料と同一の原料について、80℃より高く100℃を越えない温度範囲である高温領域における抽出温度で前記抽出工程を行う
ことにより、前記同一の原料について複数の異なる温度範囲でそれぞれ前記抽出工程を行い、
前記低温領域で行った抽出工程で得た低温抽出液について真空ベルト乾燥法により乾燥を行い、
前記中間温度領域で行った抽出工程で得た中温抽出液について噴霧乾燥法により乾燥を行い、
前記高温領域で行った抽出工程で得た高温抽出液についてドラムドライヤ法により乾燥を行い、
前記異なる3種の乾燥方法による乾燥工程を終えた前記同一の原料からなる乾燥粉末を各乾燥工程で得た乾燥粉末ごとにそれぞれ混合及び/又は造粒した後、前記異なる3種の乾燥方法による3種のものの配合比率を調整して前記異なる3種の乾燥方法による3種のものを混合して
インスタント茶を製造する方法
である。
The invention described in claim 1
An extraction process for obtaining an extract from a raw material, a drying process for dry-pulverizing the extract, and a method for producing instant tea through a subsequent mixing and / or granulation process,
About the raw material, the extraction step is performed at an extraction temperature in a low temperature range that is higher than 15 ° C. and lower than or equal to 40 ° C.,
Wherein for the same raw material and the raw material to perform the extraction process in the extraction temperature in the low temperature range, performs the extraction process in the extraction temperature in the intermediate temperature region is a temperature range of 80 ° C. or less higher than 40 ° C.,
For the same raw material as the raw material that performs the extraction step at the extraction temperature in the low temperature region, the extraction step is performed at an extraction temperature in a high temperature region that is higher than 80 ° C. and does not exceed 100 ° C.
By performing the extraction step in a plurality of different temperature ranges for the same raw material ,
For the low temperature extract obtained in the extraction step performed in the low temperature region, drying by a vacuum belt drying method,
The intermediate temperature extract obtained in the extraction step performed in the intermediate temperature range is dried by spray drying,
For the high-temperature extract obtained in the extraction step performed in the high-temperature region is dried by a drum dryer method,
After mixing and / or granulating the dry powder made of the same raw material after the drying step by the three different drying methods for each dry powder obtained in each drying step, the three different drying methods are used. the mixing ratio of the three things adjusted to a mixture of those three by the three different drying methods is a method for producing instant tea.
請求項2記載の発明は、
請求項1記載のインスタント茶を製造する方法によって製造したインスタント茶である。
The invention according to claim 2
An instant tea produced by the process for producing the instant tea according to claim 1 Symbol placement.
本発明を用いれば、通常の喫茶法にて得られる茶類とほぼ同等な風味を有するインスタント茶が得られる。 If this invention is used, the instant tea which has the flavor substantially equivalent to the teas obtained by a normal tea method will be obtained.
次に、本発明の好ましい実施の形態を説明する。 Next, a preferred embodiment of the present invention will be described.
本発明は、従来公知の、原料から抽出液を得る抽出工程と、前記抽出液を乾燥粉末化する乾燥工程と、その後の混合及び/又は造粒工程を経てインスタント茶を製造する方法において、前記乾燥工程を異なる複数の乾燥方法によって行い、前記異なる複数の乾燥方法による乾燥工程を終えた乾燥粉末をそれぞれ混合及び/又は造粒した後、前記異なる複数の乾燥方法によるものを混合してインスタント茶を製造する方法と、これによって製造したインスタント茶を提案するものである。 The present invention relates to a known method for producing instant tea through an extraction step of obtaining an extract from a raw material, a drying step of dry-pulverizing the extract, and a subsequent mixing and / or granulation step. The drying process is performed by a plurality of different drying methods, and the dried powders after the drying processes by the plurality of different drying methods are mixed and / or granulated, respectively, and then mixed by the different drying methods to be instant tea. And a method for producing instant tea.
前記の抽出工程は、原料から抽出液を得るものであり、ここで、茶類に水性溶媒を加えて抽出液を得る。この際使用する原料、すなわち、茶類には、紅茶、ウーロン茶、緑茶、ほうじ茶などの茶葉類、麦、はと麦、玄米などの穀物茶類、プアール、ルイボスなどの健康茶類、その他としてシソ、ウメやハーブなどをあげることができ、インスタント茶の原料として使用され得る物はいずれも使用可能である。これらの茶類は単独もしくは2種以上の混合物として用いることができる。 The extraction step is to obtain an extract from a raw material, and here, an aqueous solvent is added to teas to obtain an extract. Ingredients used at this time, that is, teas include tea leaves such as black tea, oolong tea, green tea, and roasted tea, grain teas such as wheat, hato barley, brown rice, health teas such as pear and rooibos, and other types of tea Ume and herbs can be used, and any of those that can be used as a raw material for instant tea can be used. These teas can be used alone or as a mixture of two or more.
抽出に使用する水性溶媒としては、単なる水道水、脱イオン水、蒸留水のいずれでも使用することができる。また、これらに糖類、ゼラチン、カゼイン、植物蛋白、アラビアガム、乳化剤類、アルコール類、アスコルビン酸などの抗酸化剤類などを、適宜添加したものを使用することもできる。 As an aqueous solvent used for extraction, any of simple tap water, deionized water, and distilled water can be used. In addition, saccharides, gelatin, casein, plant protein, gum arabic, emulsifiers, alcohols, antioxidants such as ascorbic acid, and the like can be used as appropriate.
抽出温度は、特に限定するものではないが、15℃以上100℃以下が好ましい。抽出温度が15℃未満では抽出効率が著しく低下し、また、100℃を越えた温度では、不要な成分が過剰に抽出され、且つ好ましい香気成分の変性が起こりやすくなる。 Although extraction temperature is not specifically limited, 15 degreeC or more and 100 degrees C or less are preferable. When the extraction temperature is less than 15 ° C., the extraction efficiency is remarkably lowered. When the extraction temperature is higher than 100 ° C., unnecessary components are excessively extracted, and the preferred aroma component tends to be denatured.
しかし、抽出温度の適正範囲内においては、浸出するお茶の香味成分が異なり、たとえば緑茶においては50度程度の低温で抽出した場合旨味成分であるテアニンが浸出しやすく、逆に80度以上の高温では渋み、苦みの成分であるカテキンやタンニンが浸出しやすい。 However, within the proper range of extraction temperature, the flavor components of tea to be brewed differ, for example, green tea is extracted at a low temperature of about 50 degrees, the theanine component theanine tends to leach, and conversely, the high temperature of 80 degrees or more Then catechins and tannins, which are astringent and bitter, tend to leach out.
そのため最終的に得られるインスタント茶類に求められる品質に応じて、15℃以上100℃以下の範囲内で、抽出温度の調整を行う。また、後述するように、乾燥工程で使用される乾燥方法に応じて、15℃以上100℃以下の範囲内で、抽出温度を調整することができる。 Therefore, the extraction temperature is adjusted within the range of 15 ° C. or higher and 100 ° C. or lower according to the quality required for the instant teas finally obtained. Further, as will be described later, the extraction temperature can be adjusted within a range of 15 ° C. or more and 100 ° C. or less according to the drying method used in the drying step.
抽出工程では、前述した茶類1重量部を、前述した水溶性溶媒4から30重量部程度で浸漬あるいは、攪拌しながら、前述した所定の温度範囲で抽出する。 In the extraction step, 1 part by weight of the above-described tea is extracted in the above-mentioned predetermined temperature range while being immersed or stirred with about 4 to 30 parts by weight of the above-mentioned water-soluble solvent.
こうして抽出したものから粗分離により、抽出液を得ることができる。この抽出液は、必要に応じて遠心分離機等を用い清澄化を行う。 An extract can be obtained from the thus extracted product by rough separation. This extract is clarified using a centrifuge or the like as necessary.
抽出工程後、乾燥工程の前に、必要に応じて、濃縮工程を行うことができる。濃縮工程は、抽出液を乾燥工程の前に予め濃縮することで、乾燥の経費を少なくするために行うものであり、必要に応じて行えばよい。減圧濃縮、凍結濃縮、逆浸透圧膜濃縮などの周知の方法により濃縮を行うことができる。 After the extraction step and before the drying step, a concentration step can be performed as necessary. The concentration step is performed in order to reduce the cost of drying by concentrating the extract in advance before the drying step, and may be performed as necessary. Concentration can be performed by a known method such as vacuum concentration, freeze concentration, reverse osmosis membrane concentration, or the like.
乾燥工程では、抽出液(或いは濃縮液)の乾燥粉末化を行うが、本発明ではこの乾燥工程に異なる複数の乾燥方法を採用している。 In the drying process, the extract (or concentrated liquid) is dried and powdered. In the present invention, a plurality of different drying methods are employed in the drying process.
乾燥工程で採用する複数の異なる乾燥方法としては、例えば、真空ベルト乾燥、噴霧乾燥、ドラムドライヤを上げることができるが、これに限られるものではなく、フリーズドライなど、この技術分野で公知の乾燥方法を採用することができる。 As a plurality of different drying methods employed in the drying process, for example, vacuum belt drying, spray drying, drum dryer can be raised, but not limited thereto, drying known in this technical field such as freeze drying, etc. The method can be adopted.
なお、乾燥工程にあたって、この技術分野で公知のように、品質を維持 する目的で、前記抽出液(或いは濃縮液)に対してデキストリンなど を添加してもよい。 In the drying process, as known in this technical field, dextrin or the like may be added to the extract (or concentrated solution) for the purpose of maintaining quality.
各乾燥方法により得られた茶類乾燥粉末の風味や香気成分の損失の傾向は異なる。 The tendency of loss of flavor and aroma components of tea dry powder obtained by each drying method is different.
例えば、真空ベルト乾燥では乾燥中品温が極めて低く、熱がかかりにくいため比較的新鮮な生っぽい風味を有する乾燥粉末が得られる。 For example, in vacuum belt drying, the product temperature during drying is extremely low and it is difficult to apply heat, so that a dry powder having a relatively fresh raw flavor can be obtained.
一方、ドラムドライヤは、乾燥品温はかなり高温になり、非常に熱がかかるため香気成分の損失は激しいが、代わりに火入れ香といわれる製茶における火入れ工程にて茶葉に付与される香りに似た風味を有する乾燥粉末が得られる。 On the other hand, the drum dryer has a very high temperature of the dried product and is very heated, so the loss of aroma components is severe, but instead it resembles the fragrance imparted to the tea leaves in the tea making process in tea making, which is called burning incense. A dry powder having a flavor is obtained.
噴霧乾燥においては、乾燥中の香気成分の損失が比較的少なく乾燥効率が高いため経費を少なくすることができ、インスタント茶類のベースとなる乾燥粉末を得られる。 In spray drying, the loss of aroma components during drying is relatively small and the drying efficiency is high, so that the cost can be reduced and a dry powder serving as a base for instant teas can be obtained.
また、以上の特性を考慮して、抽出工程を複数の異なる温度範囲で行い、この異なる温度範囲で行った抽出工程により得た各温度範囲での抽出液を、それぞれ、前記異なる乾燥方法で乾燥粉末化することが望ましい。すなわち、抽出工程の段階において各乾燥法に適した抽出条件にて得られた茶類抽出液を用いるのが好ましい。 In consideration of the above characteristics, the extraction process is performed in a plurality of different temperature ranges, and the extraction liquid in each temperature range obtained by the extraction process performed in the different temperature ranges is dried by the different drying methods. It is desirable to powder. That is, it is preferable to use a tea extract obtained under extraction conditions suitable for each drying method at the stage of the extraction process.
例えば、真空ベルト乾燥には、低温領域(15℃より高く、40℃以下の温度範囲)で抽出した抽出液を用いることが望ましい。低温領域で抽出した抽出液は比較的渋みが少なく旨味の多いので、真空ベルト乾燥法と組み合わせることにより、より新鮮味、青味のある生葉に近い風味を有する乾燥粉末を得ることができる。 For example, for vacuum belt drying, it is desirable to use an extract extracted in a low temperature region (temperature range higher than 15 ° C. and lower than 40 ° C.). Since the extract extracted in the low temperature region has relatively little astringency and a lot of umami, it can be combined with a vacuum belt drying method to obtain a dry powder having a fresh, greenish flavor similar to fresh leaves.
ドラムドライヤには、高温領域(80℃より高く、100℃を越えない温度範囲)で抽出した抽出液を用いることが望ましい。高温領域で抽出した抽出液は渋みが強く出るので、ドラムドライヤと組み合わせることにより、渋み、火入れ香を有した力価の強い乾燥粉末が得られる。 For the drum dryer, it is desirable to use an extract extracted in a high temperature region (temperature range higher than 80 ° C. and not exceeding 100 ° C.). The extract extracted in the high temperature region has a strong astringency, and when combined with a drum dryer, a strong powder having astringency and a burning incense can be obtained.
噴霧乾燥には、前記低温領域と高温領域との間の中間温度領域(40℃より高く、80℃以下の温度範囲)で抽出した抽出液を用いることが望ましい。中間温度領域で抽出した抽出液はベースとなりうる旨味、渋みのバランスがとれているからである。 For spray drying, it is desirable to use an extract extracted in an intermediate temperature range between the low temperature range and the high temperature range (temperature range higher than 40 ° C. and lower than 80 ° C.). This is because the extract extracted in the intermediate temperature range has a balance of umami and astringency that can be a base.
乾燥工程で、乾燥粉末化した後、混合工程、又は、造粒工程を行う。なお、必要に応じて、混合工程と造粒工程との双方を行っても良い。 In the drying process, after the powder is dried, a mixing process or a granulating process is performed. In addition, you may perform both a mixing process and a granulation process as needed.
なお、前述したように、複数の乾燥工程を採用しているので、各乾燥工程で得た乾燥粉末ごとに混合及び/又は造粒工程を行う。 In addition, since several drying processes are employ | adopted as mentioned above, a mixing and / or granulation process is performed for every dry powder obtained at each drying process.
この混合工程では、各種乾燥方法にて得られた茶類の乾燥粉末を粉体ブレンダーにて混合する。また、造粒工程では、各種乾燥方法にて得られた茶類の乾燥粉末を主に流動層造粒にて造粒する。前述したように、これらの混合工程と造粒工程との両方を用いてもよい。造粒工程は、製造するインスタント茶の充填時の流動性、もしくは喫茶時の溶解性を向上させる目的で行うものであり、必要に応じて行えばよい。 In this mixing step, dry powders of tea obtained by various drying methods are mixed in a powder blender. In the granulation step, dry powder of tea obtained by various drying methods is granulated mainly by fluidized bed granulation. As described above, both the mixing step and the granulating step may be used. The granulation step is performed for the purpose of improving the fluidity at the time of filling of the instant tea to be produced or the solubility at the time of coffee, and may be performed as necessary.
以上のような工程により得た、前記異なる複数の乾燥方法に茶類の乾燥粉末を混合して本発明のインスタント茶にすることができる。すなわち、各種乾燥方法にて得られた風味の異なる乾燥粉末(真空ベルト乾燥粉末、噴霧乾燥粉末、ドラムドライヤ粉末)を用いて、それぞれの特徴を有した、通常の喫茶法で得られる茶湯と殆ど同様の風味を有するインスタント茶を得ることができる。なお、ここで、各種乾燥方法にて得られた風味の異なる乾燥粉末の配合比率を調整することで、より好ましい風味を有するインスタント茶にすることができる。 The instant tea of the present invention can be obtained by mixing dry powders of teas into the plurality of different drying methods obtained by the above steps. In other words, using dry powders (vacuum belt dry powder, spray dried powder, drum dryer powder) with different flavors obtained by various drying methods, the tea teas obtained by ordinary tea methods having the respective characteristics are almost the same. An instant tea having a similar flavor can be obtained. In addition, it can be set as the instant tea which has a more preferable flavor by adjusting the mixture ratio of the dry powder from which the flavor obtained by various drying methods differs here.
次に実施例によって本発明を具体的に説明する。 Next, the present invention will be described specifically by way of examples.
40度30分(低温抽出)、80度30分(中温抽出)、90度55分(高温抽出)の3つの条件にて、それぞれ緑茶1kg、温水20kg投入し抽出した。 Extraction was performed by adding 1 kg of green tea and 20 kg of warm water under three conditions of 40 degrees 30 minutes (low temperature extraction), 80 degrees 30 minutes (medium temperature extraction), and 90 degrees 55 minutes (high temperature extraction).
粗分離して得られた各抽出液(ブリックス0.5〜3程度、約16kg)は、遠心分離にかけて液を清澄化後、濃縮機にて約20倍濃縮液(ブリックス約30、約0.8kg)を得た。 Each extract (brix about 0.5-3, about 16 kg) obtained by rough separation was clarified by centrifugation and then concentrated about 20 times (brix about 30, about 0.00). 8 kg) was obtained.
低温抽出により得られた濃縮液とデキストリン(三和澱粉工業(株)製、商品名サンデック#30)を撹拌、混合し80度20分にて加熱殺菌した後、真空度1330〜1729Pa、加熱温度130度、120度、110度の条件で真空ベルト乾燥し、インスタント緑茶Aを得た(約300g)。 The concentrate obtained by low temperature extraction and dextrin (manufactured by Sanwa Starch Kogyo Co., Ltd., trade name: Sundeck # 30) are stirred and mixed and sterilized by heating at 80 degrees 20 minutes, and then the degree of vacuum 1330-1729 Pa, heating temperature Vacuum belt drying was performed at 130, 120, and 110 degrees to obtain instant green tea A (about 300 g).
中温抽出により得られた濃縮液とデキストリン(三和澱粉工業(株)製、商品名サンデック#70)を撹拌、混合し80度20分にて加熱殺菌した後、チャンバー内温度90度の条件で噴霧乾燥し、インスタント緑茶Bを得た(約300g)。 The concentrated solution obtained by the medium temperature extraction and dextrin (trade name: Sundeck # 70, manufactured by Sanwa Starch Co., Ltd.) are stirred and mixed and sterilized by heating at 80 ° C for 20 minutes. Spray drying was performed to obtain instant green tea B (about 300 g).
高温抽出により得られた濃縮液とデキストリン(三和澱粉工業(株)製、商品名サンデック#70)を撹拌、混合した後、ドラムドライヤにて乾燥粉末化し、インスタント緑茶Cを得た(約600g)。 The concentrated solution obtained by high temperature extraction and dextrin (manufactured by Sanwa Starch Co., Ltd., trade name: Sundeck # 70) were stirred and mixed, and then dried and powdered with a drum dryer to obtain instant green tea C (about 600 g). ).
各乾燥法の各緑茶濃縮液における緑茶エキス固形分とデキストリンの配合比率は1:1とした。 The blending ratio of green tea extract solids and dextrin in each green tea concentrate of each drying method was 1: 1.
各乾燥法にて得られたインスタント緑茶A、インスタント緑茶B、インスタント緑茶Cを2:3:4の重量割合で混合し、本発明のインスタント緑茶Dを得た。 Instant green tea A, instant green tea B, and instant green tea C obtained by each drying method were mixed at a weight ratio of 2: 3: 4 to obtain instant green tea D of the present invention.
この実施例で原料に用いた緑茶を用いて通常の喫茶法にて得られた緑茶と、この実施例で得られたインスタント緑茶Dとを試飲したところ、ほとんど同様の風味であった。 When tasting the green tea obtained by the ordinary tea method using the green tea used as a raw material in this example and the instant green tea D obtained in this example, the taste was almost the same.
なお、前記ではインスタント緑茶A、インスタント緑茶B、インスタント緑茶Cを2:3:4の重量割合で混合して本発明のインスタント緑茶Dとしていたが、本願発明者等が更に追加試験を行ったところ、インスタント緑茶A、インスタント緑茶B、インスタント緑茶Cを重量割合で1〜8:1〜8:1〜8の範囲で混合したインスタント緑茶であれば、この実施例で原料に用いた緑茶を用いて通常の喫茶法にて得られた緑茶と、ほとんど同様の風味で喫飲できることを確認できた。 In the above, instant green tea A, instant green tea B, and instant green tea C were mixed at a weight ratio of 2: 3: 4 to obtain instant green tea D of the present invention, but the inventors of the present application further conducted additional tests. , Instant green tea A, instant green tea B, and instant green tea C are mixed in a weight ratio of 1 to 8: 1 to 8: 1 to 8 using the green tea used as a raw material in this example. It was confirmed that the tea can be drunk with almost the same flavor as the green tea obtained by the ordinary coffee method.
産地の異なる烏龍茶を組み合わせて本発明のインスタント烏龍茶を調製した。 The instant oolong tea of the present invention was prepared by combining oolong tea from different production areas.
それぞれ産地が異なっていて、香りの良い烏龍茶と、味の良い烏龍茶とを選抜した。 Each has a different production area, and selected fragrant oolong tea and delicious oolong tea.
香りの良い烏龍茶100kgに温水1900kgを投入し、35度55分の条件で低温抽出した。粗分離して得られた抽出液(ブリックス1.0程度、約 1600kg)は、遠心分離にかけて液を清澄化後、濃縮機にて約20倍濃縮液(ブリックス約20、約80kg)を得た。この濃縮液とデキストリン(三和澱粉工業(株)製、商品名サンデック#30)を撹拌、混合し、80度20分にて加熱殺菌した後、真空度1330〜1729Pa、加熱温度130度、120度、110度の条件で真空ベルト乾燥し、インスタント烏龍茶Eを得た(約 100kg)。 1900 kg of hot water was put into 100 kg of fragrant oolong tea and extracted at a low temperature under the condition of 35 degrees 55 minutes. The extract obtained by rough separation (about Brix 1.0, about 1600 kg) was clarified by centrifugation, and then a concentrated solution (Brix about 20, about 80 kg) was obtained with a concentrator. . This concentrated solution and dextrin (manufactured by Sanwa Starch Kogyo Co., Ltd., trade name: Sundeck # 30) are stirred and mixed, sterilized by heating at 80 degrees 20 minutes, and then a vacuum degree of 1330 to 1729 Pa, a heating temperature of 130 degrees, 120 The vacuum belt was dried at a temperature of 110 ° C. to obtain instant Oolong tea E (about 100 kg).
味の良い烏龍茶100kgに温水1900kgを投入し、75度30分の条件で中温抽出した。粗分離して得られた抽出液(ブリックス1.5程度、約1600kg)は、遠心分離にかけて液を清澄化後、濃縮機にて約25倍濃縮液(ブリックス約20、約100kg)を得た。この濃縮液とデキストリン(三和澱粉工業(株)製、商品名サンデック#70)を撹拌、混合し80度30分にて加熱殺菌した後、チャンバー内温度90度の条件で噴霧乾燥し、烏龍茶Fを得た(約100kg)。 1900 kg of warm water was added to 100 kg of oolong tea with good taste, and the medium temperature was extracted under the condition of 75 degrees 30 minutes. The extracted liquid (about Brix 1.5, about 1600 kg) obtained by rough separation was clarified by centrifuging, and then a concentrated liquid (Brix about 20, about 100 kg) was obtained with a concentrator. . This concentrated solution and dextrin (manufactured by Sanwa Starch Kogyo Co., Ltd., trade name: Sundeck # 70) are stirred and mixed, sterilized by heating at 80 ° C for 30 minutes, and then spray-dried at a chamber temperature of 90 ° C. F was obtained (about 100 kg).
各乾燥法の各烏龍茶濃縮液における烏龍茶エキス固形分とデキストリンの配合比率は1:1とした。 The blending ratio of oolong tea extract solids and dextrin in each oolong tea concentrate of each drying method was 1: 1.
各乾燥法にて得られたインスタント烏龍茶E、インスタント烏龍茶Fを2:3の重量割合で混合し、本発明のインスタント烏龍茶Gを得た。 Instant oolong tea E and instant oolong tea F obtained by each drying method were mixed at a weight ratio of 2: 3 to obtain instant oolong tea G of the present invention.
このインスタント烏龍茶Gを試飲したところ、香りの部分と味の部分とのバランスのとれた烏龍茶であった。 When this instant oolong tea G was sampled, it was oolong tea with a balanced fragrance and taste.
なお、前記ではインスタント烏龍茶E、インスタント烏龍茶Fを2:3の重量割合で混合して本発明のインスタント烏龍茶Gとしていたが、本願発明者等が更に追加試験を行ったところ、インスタント烏龍茶E、インスタント烏龍茶Fを重量割合で1〜3:9〜7の範囲で混合したインスタント烏龍茶であれば、香りの部分と味の部分とのバランスのとれた烏龍茶製品であることを確認できた。 In the above, Instant Oolong Tea E and Instant Oolong Tea F were mixed at a weight ratio of 2: 3 to obtain Instant Oolong Tea G of the present invention. However, when the present inventors conducted further tests, Instant Oolong Tea E, Instant If it was instant Oolong tea mixed Oolong tea F in the range of 1-3: 9-7 by weight ratio, it could be confirmed that it was an Oolong tea product with a balanced fragrance and taste.
90度50分の条件で麦茶100kg、温水2000kg投入し、高温抽出した。粗分離して得られた抽出液(ブリックス2.5程度、約1400kg)は、遠心分離にかけて液を清澄化後、濃縮機にて約20倍濃縮液(ブリックス約18、約100kg)を得た。 100 kg of barley tea and 2000 kg of warm water were added at 90 ° C. for 50 minutes, and high temperature extraction was performed. The extracted liquid (about Brix 2.5, about 1400 kg) obtained by rough separation was clarified by centrifugation and then a concentrated solution (Brix about 18, about 100 kg) was obtained with a concentrator. .
前記の濃縮液とデキストリン(三和澱粉工業(株)製、商品名サンデック#70)を撹拌、混合し80度30分にて加熱殺菌した後、チャンバー内温度80度の条件で噴霧乾燥し、インスタント麦茶Hを得た(約100kg)。 After stirring and mixing the concentrated solution and dextrin (manufactured by Sanwa Starch Co., Ltd., trade name Sandeck # 70) and sterilizing by heating at 80 degrees 30 minutes, spray drying under conditions of a chamber temperature of 80 degrees, Instant barley tea H was obtained (about 100 kg).
また前記濃縮液とデキストリン(三和澱粉工業(株)製、商品名サンデック#70)を撹拌、混合した後、ドラムドライヤにて乾燥粉末化し、インスタント麦茶Iを得た(約100kg)。 Further, the concentrated solution and dextrin (manufactured by Sanwa Starch Co., Ltd., trade name Sandeck # 70) were stirred and mixed, and then dried and powdered with a drum dryer to obtain instant barley tea I (about 100 kg).
各乾燥法の各麦茶濃縮液における麦茶エキス固形分とデキストリンの配合比率は1:1した。 The blending ratio of barley tea extract solids and dextrin in each barley tea concentrate of each drying method was 1: 1.
各乾燥法にて得られたインスタント麦茶H、インスタント麦茶Iを5:6の重量割合で混合し、本発明のインスタント麦茶Jを得た。 Instant barley tea H and instant barley tea I obtained by each drying method were mixed at a weight ratio of 5: 6 to obtain instant barley tea J of the present invention.
この実施例で原料に用いた麦茶を用いて通常の喫茶法にて得られた麦茶と、この実施例で得られたインスタント麦茶Jとを試飲したところ、ほとんど同様の風味であり、更に、インスタント麦茶Jの方が甘みと香りのバランスがよかった。 When tasting barley tea obtained by ordinary tea using the barley tea used as a raw material in this example and instant barley tea J obtained in this example, the taste was almost the same, and instant Barley tea J had a better balance between sweetness and aroma.
前記ではインスタント麦茶H、インスタント麦茶Iを5:6の重量割合で混合して本発明のインスタント麦茶Jとしていたが、本願発明者等が更に追加試験を行ったところ、インスタント麦茶H、インスタント麦茶Iを重量割合で5〜3:5〜7の範囲で混合したインスタント麦茶であれば、この実施例で原料に用いた麦茶を用いて通常の喫茶法にて得られた麦茶と、ほとんど同様の風味で喫飲でき、更に、好みの甘みと香りのバランスを持った麦茶製品になることを確認できた。 In the above, instant barley tea H and instant barley tea I were mixed at a weight ratio of 5: 6 to obtain instant barley tea J of the present invention. However, when the present inventors conducted additional tests, instant barley tea H and instant barley tea I were used. If it is instant barley tea mixed in the range of 5-3: 5-7 by weight ratio, it is almost the same flavor as barley tea obtained by ordinary tea using barley tea used as a raw material in this example. In addition, it was confirmed that it would be a barley tea product with a balance of sweetness and aroma of your choice.
焙じ度の異なるほうじ茶を組み合わせて本発明のほうじ龍茶を調製した。 The roasted tea of the present invention was prepared by combining roasted teas with different roasting degrees.
焙じ度の浅いほうじ茶100kgに温水2000kgを投入し、40度 45分の条件で低温抽出した。粗分離して得られた抽出液(ブリックス1.0程度、約1700kg)は、遠心分離にかけて液を清澄化後、濃縮機にて約20倍濃縮液(ブリックス約20、約85kg)を得た。この濃縮液とデキストリン(三和澱粉工業(株)製、商品名サンデック#30)を撹拌、混合し80度 30分にて加熱殺菌した後、真空度1330〜1729Pa、加熱温度130度、120度、110度の条件で真空ベルト乾燥し、インスタントほうじ茶Kを得た(約80kg)。 To 100 kg of roasted tea with a low roasting degree, 2000 kg of hot water was added and extracted at a low temperature under the condition of 40 degrees 45 minutes. The extract obtained by rough separation (about Brix 1.0, about 1700 kg) was clarified by centrifugation and then about 20 times concentrated solution (Brix about 20, about 85 kg) was obtained with a concentrator. . This concentrated solution and dextrin (manufactured by Sanwa Starch Kogyo Co., Ltd., trade name: Sundeck # 30) are stirred and mixed and sterilized by heating at 80 ° C. for 30 minutes, and then the degree of vacuum is 1330-1729 Pa, the heating temperature is 130 ° C., 120 ° The belt was dried under a condition of 110 ° C. to obtain instant Hojicha K (about 80 kg).
中程度の焙じ度のほうじ茶100kgに温水2000kgを投入し、65度 30分の条件で中温抽出した。粗分離して得られた抽出液(ブリックス1.5程度、約1600kg)は、遠心分離にかけて液を清澄化後、濃縮機にて約20倍濃縮液(ブリックス約16、約100kg)を得た。この濃縮液とデキストリン(三和澱粉工業(株)製、商品名サンデック#70)を撹拌、混合し80度30分にて加熱殺菌した後、チャンバー内温度90度の条件で噴霧乾燥し、インスタントほうじ茶Lを得た(約80kg)。 Hot water 2000 kg was added to medium-roasted roasted tea 100 kg and extracted at a medium temperature under the condition of 65 degrees 30 minutes. The extracted liquid (about Brix 1.5, about 1600 kg) obtained by rough separation was clarified by centrifuging, and then the concentrated liquid (Brix about 16, about 100 kg) was obtained with a concentrator. . This concentrated solution and dextrin (manufactured by Sanwa Starch Kogyo Co., Ltd., trade name: Sundeck # 70) are stirred, mixed, heat sterilized at 80 degrees 30 minutes, spray-dried at a chamber temperature of 90 degrees, and instant Hojicha L was obtained (about 80 kg).
焙じ度の高いほうじ茶100kgに温水2000kgを投入し、90度 20分の条件で高温抽出した。粗分離して得られた抽出液(ブリックス1.5程度、約1600kg)は、遠心分離にかけて液を清澄化後、濃縮機にて約 倍濃縮液(ブリックス約16、約80kg)を得た。この濃縮液とデキストリン(三和澱粉工業(株)製、商品名サンデック#70)を撹拌、混合した後、ドラムドライヤにて乾燥粉末化し、インスタントほうじ茶Mを得た(約80kg)。 Hot water 2000 kg was added to 100 kg of roasted tea with high roasting degree, and high temperature extraction was performed at 90 ° C. for 20 minutes. The extract obtained by rough separation (Brix 1.5, about 1600 kg) was subjected to centrifugal separation to clarify the liquid, and then an about double concentrate (Brix about 16, 80 kg) was obtained using a concentrator. This concentrated solution and dextrin (manufactured by Sanwa Starch Kogyo Co., Ltd., trade name Sandeck # 70) were stirred and mixed, and then dried and powdered with a drum dryer to obtain instant hojicha M (about 80 kg).
各乾燥法の各ほうじ茶濃縮液におけるほうじ茶エキス固形分とデキストリンの配合比率は1:1とした。 The mixing ratio of hojicha extract solids and dextrin in each hojicha concentrate of each drying method was 1: 1.
各乾燥法にて得られたインスタントほうじ茶K、インスタントほうじ茶L、インスタントほうじ茶Mを2:3:3の重量割合で混合し、本発明のインスタントほうじ茶Nを得た。 Instant Hojicha K, Instant Hojicha L, and Instant Hojicha M obtained by each drying method were mixed at a weight ratio of 2: 3: 3 to obtain Instant Hojicha N of the present invention.
インスタントほうじ茶Nは、香りの部分と味の部分とのバランスのとれたほうじ茶であることを確認できた。 It was confirmed that the instant roasted green tea N was a roasted green tea with a balanced fragrance and taste.
なお、前記ではインスタントほうじ茶K、インスタントほうじ茶L、インスタントほうじ茶Nを2:3:3の重量割合で混合して本発明のインスタントほうじ茶Nとしていたが、本願発明者等が更に追加試験を行ったところ、インスタントほうじ茶K、インスタントほうじ茶L、インスタントほうじ茶Mを重量割合で1〜3:8〜3:1〜4の範囲で混合したインスタントほうじ茶であれば、香りの部分と味の部分とのバランスのとれたほうじ茶製品となることを確認できた。 In the above, Instant Hojicha K, Instant Hojicha L, and Instant Hojicha N were mixed at a weight ratio of 2: 3: 3 to obtain Instant Hojicha N of the present invention. , Instant Hojicha K, Instant Hojicha L, Instant Hojicha M are mixed in a weight ratio of 1-3: 8-3: 1-4. It was confirmed that it was a tahoe tea product.
ハーブを原料として乾燥方法を組み合わせて本発明のインスタントハーブティーを調製した。 The instant herbal tea of the present invention was prepared by combining drying methods using herbs as raw materials.
ハイビスカスのホール・粉砕100kgに温水2000kgを投入し、40度55分の条件で低温抽出した。粗分離して得られた抽出液(ブリックス2.0程度、約1700kg)は、遠心分離にかけて液を清澄化後、濃縮機にて約20倍濃縮液(ブリックス約20、約170kg)を得た。この濃縮液とデキストリン(三和澱粉工業(株)製、商品名サンデック#30)を撹拌、混合し80度30分にて加熱殺菌した後、真空度1330〜1729Pa、加熱温度130度、120度、110度の条件で真空ベルト乾燥し、ハイビスカスパウダーを得た(約70kg)。 2,000 kg of hot water was added to 100 kg of hibiscus holes and ground, and extracted at a low temperature under the condition of 40 degrees 55 minutes. The extract (brix 2.0, about 1700 kg) obtained by rough separation was clarified by centrifugation, and then a concentrated solution (brix about 20, about 170 kg) was obtained with a concentrator. . This concentrated solution and dextrin (manufactured by Sanwa Starch Kogyo Co., Ltd., trade name: Sundeck # 30) are stirred and mixed and sterilized by heating at 80 ° C for 30 minutes, and then a vacuum of 1330 to 1729 Pa, a heating temperature of 130 ° C, and 120 ° C. The belt was dried under a condition of 110 degrees to obtain a hibiscus powder (about 70 kg).
ローズヒップのホール・粗砕100kgに温水2000kgを投入し、90度55分の条件で高温抽出した。粗分離して得られた抽出液(ブリックス2.5程度、約1600kg)は、遠心分離にかけて液を清澄化後、濃縮機にて約20倍濃縮液(ブリックス約22、約180kg)を得た。この濃縮液とデキストリン(三和澱粉工業(株)製、商品名サンデック#70)を撹拌、混合した後、ドラムドライヤにて乾燥粉末化し、ローズヒップパウダーを得た(約100kg)。 Hot water 2000 kg was put into a rose hip hole / crushed 100 kg and extracted at a high temperature of 90 degrees 55 minutes. The extracted liquid (about Brix 2.5, about 1600 kg) obtained by rough separation was clarified by centrifuging, and then the concentrated liquid (Brix about 22, about 180 kg) was obtained with a concentrator. . This concentrated solution and dextrin (manufactured by Sanwa Starch Co., Ltd., trade name: Sundeck # 70) were stirred and mixed, and then dried and powdered with a drum dryer to obtain a rosehip powder (about 100 kg).
各乾燥法のハイビスカスパウダー、ローズヒップパウダーにおけるハイビスカスエキス、ローズヒップエキスの固形分とデキストリンの配合比率は約1:1とした。 The mixing ratio of the solid content and dextrin of the hibiscus extract and rosehip extract in each drying method was about 1: 1.
各乾燥法にて得られたハイビスカスパウダー、ローズヒップパウダーを2:3の重量割合で混合し、本発明のインスタントハーブティーを得た。 The hibiscus powder and rosehip powder obtained by each drying method were mixed at a weight ratio of 2: 3 to obtain the instant herbal tea of the present invention.
こうして得た本発明のインスタントハーブティーは、香りの部分と味の部分とのバランスのとれたハーブティーであることを確認できた。 It was confirmed that the instant herbal tea of the present invention thus obtained was a herbal tea in which a fragrance portion and a taste portion were balanced.
なお、前記ではハイビスカスパウダー、ローズヒップパウダーを2:3の重量割合で混合し、本発明のインスタントハーブティーとしていたが、本願発明者等が更に追加試験を行ったところ、ハイビスカスパウダー、ローズヒップパウダーを重量割合で1〜4:9〜6の範囲で混合したインスタントハーブティーであれば、香りの部分と味の部分とのバランスのとれた製品となることを確認できた。 In the above, hibiscus powder and rosehip powder were mixed at a weight ratio of 2: 3 to obtain the instant herbal tea of the present invention. However, when the present inventors conducted further tests, hibiscus powder and rosehip powder were used. It was confirmed that the instant herbal tea mixed in a weight ratio of 1 to 4: 9 to 6 was a product with a balanced fragrance portion and taste portion.
以上、この発明の好ましい実施形態、実施例を説明したが本発明はこれらに限られるものではなく、特許請求の範囲の記載から把握される技術的範囲において種々の形態に変更可能である。 As mentioned above, although preferable embodiment and the Example of this invention were described, this invention is not limited to these, In the technical range grasped | ascertained from description of a claim, it can change into a various form.
Claims (2)
前記原料について、15℃より高く40℃以下の温度範囲である低温領域における抽出温度で前記抽出工程を行い、
前記低温領域における抽出温度で前記抽出工程を行う前記原料と同一の原料について、40℃より高く80℃以下の温度範囲である中間温度領域における抽出温度で前記抽出工程を行い、
前記低温領域における抽出温度で前記抽出工程を行う前記原料と同一の原料について、80℃より高く100℃を越えない温度範囲である高温領域における抽出温度で前記抽出工程を行う
ことにより、前記同一の原料について複数の異なる温度範囲でそれぞれ前記抽出工程を行い、
前記低温領域で行った抽出工程で得た低温抽出液について真空ベルト乾燥法により乾燥を行い、
前記中間温度領域で行った抽出工程で得た中温抽出液について噴霧乾燥法により乾燥を行い、
前記高温領域で行った抽出工程で得た高温抽出液についてドラムドライヤ法により乾燥を行い、
前記異なる3種の乾燥方法による乾燥工程を終えた前記同一の原料からなる乾燥粉末を各乾燥工程で得た乾燥粉末ごとにそれぞれ混合及び/又は造粒した後、前記異なる3種の乾燥方法による3種のものの配合比率を調整して前記異なる3種の乾燥方法による3種のものを混合して
インスタント茶を製造する方法。 An extraction process for obtaining an extract from a raw material, a drying process for dry-pulverizing the extract, and a method for producing instant tea through a subsequent mixing and / or granulation process,
About the raw material, the extraction step is performed at an extraction temperature in a low temperature range that is higher than 15 ° C. and lower than or equal to 40 ° C.,
Wherein for the same raw material and the raw material to perform the extraction process in the extraction temperature in the low temperature range, performs the extraction process in the extraction temperature in the intermediate temperature region is a temperature range of 80 ° C. or less higher than 40 ° C.,
For the same raw material as the raw material that performs the extraction step at the extraction temperature in the low temperature region, the extraction step is performed at an extraction temperature in a high temperature region that is higher than 80 ° C. and does not exceed 100 ° C.
By performing the extraction step in a plurality of different temperature ranges for the same raw material ,
For the low temperature extract obtained in the extraction step performed in the low temperature region, drying by a vacuum belt drying method,
The intermediate temperature extract obtained in the extraction step performed in the intermediate temperature range is dried by spray drying,
For the high-temperature extract obtained in the extraction step performed in the high-temperature region is dried by a drum dryer method,
After mixing and / or granulating the dry powder made of the same raw material after the drying step by the three different drying methods for each dry powder obtained in each drying step, the three different drying methods are used. method for producing instant tea by mixing one of the three by the three different drying methods by adjusting the mixing ratio of the three things.
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