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JP2003199495A - Tea beverage and method of production for the same - Google Patents

Tea beverage and method of production for the same

Info

Publication number
JP2003199495A
JP2003199495A JP2001401219A JP2001401219A JP2003199495A JP 2003199495 A JP2003199495 A JP 2003199495A JP 2001401219 A JP2001401219 A JP 2001401219A JP 2001401219 A JP2001401219 A JP 2001401219A JP 2003199495 A JP2003199495 A JP 2003199495A
Authority
JP
Japan
Prior art keywords
filtration
tea
extract
filtering
tea beverage
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
JP2001401219A
Other languages
Japanese (ja)
Inventor
Kiyoshi Nemoto
潔 根本
Takeshi Inoue
剛 井上
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.)
Sapporo Breweries Ltd
Original Assignee
Sapporo Breweries 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 Sapporo Breweries Ltd filed Critical Sapporo Breweries Ltd
Priority to JP2001401219A priority Critical patent/JP2003199495A/en
Publication of JP2003199495A publication Critical patent/JP2003199495A/en
Pending legal-status Critical Current

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Abstract

<P>PROBLEM TO BE SOLVED: To provide tea beverage with low precipitation and excellent in flavor. <P>SOLUTION: The tea beverage is obtained by the following steps; an extraction step obtaining the extract solution from tea, a step removing the residual tea leaves of the extraction by centrifugal filtration, multiple filtrating steps for filtration of the liquid obtained by the centrifugal filtration, and the multiple filtrating steps comprises a preliminary surface filtration step using a filter paper or a filter cloth and a later filtration step filtrating substance with particle size ≤1 μm contained in the extraction liquid by utilizing a multi-layer filtration system. <P>COPYRIGHT: (C)2003,JPO

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【発明の属する技術分野】本発明は茶類飲料及びその製
造方法に関するもので、更に詳しくは、茶葉より抽出し
た茶抽出液に含まれる経時的に 析出沈殿する成分を濾
過して得られる茶類飲料とこれを製造するための濾過す
るる方法に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a tea beverage and a method for producing the same, and more specifically, teas obtained by filtering components of a tea extract extracted from tea leaves, which precipitate and precipitate with time. It relates to a beverage and a filtering method for producing the same.

【0002】[0002]

【従来の技術】お茶はわが国においては、古来より定着
した飲料であり、広く親しまれており、最近では、清涼
飲料として、缶あるいはペットボトルなどの容器に充填
されて販売され、若年層の間でも急速に普及しつつあ
る。
2. Description of the Related Art Tea has been a well-established beverage in Japan since ancient times and has been widely popular. Recently, it has been sold as a soft drink filled in containers such as cans and PET bottles, and is sold to young people. But it is spreading rapidly.

【0003】使用される茶葉として、緑茶、ウーロン茶
などが多く愛好されているが、この他、紅茶、ジャスミ
ン茶、プーアール茶等あらゆる茶が含まれる。これら緑
茶、ウーロン茶等の茶類飲料を製造するに当り、茶葉を
水又は湯等に浸漬して得られた抽出液は透明度を高める
ため、濾過を行う。ところが、この濾過の仕方によって
は、経時的に飲料中に含まれる微小な不溶性残渣及びカ
テキン、タンニン等が凝集沈殿し濁りを生ずることがあ
る。この沈殿物そのものは飲料の香味に影響するもので
はないが、近年、PETボトル等の透明容器が多くの飲
料製品に使用されており、消費者に無用な不快感を与え
る可能性がある。
As the tea leaves used, green tea, oolong tea, etc. are often favoured, but in addition to this, all teas such as black tea, jasmine tea, and Pu'er tea are included. In producing tea beverages such as green tea and oolong tea, the extract obtained by immersing tea leaves in water or hot water is filtered to enhance transparency. However, depending on the filtration method, minute insoluble residues and catechin, tannin, etc. contained in the beverage may aggregate and precipitate over time, resulting in turbidity. The precipitate itself does not affect the flavor of the beverage, but in recent years, transparent containers such as PET bottles have been used in many beverage products, which may cause unnecessary discomfort to consumers.

【0004】そこで、従来は、一般的な遠心分離等の濾
過手段で抽出液を濾過した後、珪藻土濾過等の精密濾過
を行い、経時的に澱の原因となる成分を予め取除くこと
で対応していた。
[0004] Therefore, conventionally, after the extract is filtered by a general filtration means such as centrifugation, microfiltration such as diatomaceous earth filtration is carried out to remove the component causing the precipitation with time beforehand. Was.

【0005】[0005]

【発明が解決しようとする課題】しかしながら、経時的
な濁りの発生は生じなくなったものの、お茶本来の旨
み、まろやかさが薄らいでしまうと言う問題が生じてし
まうことがパネラーによる官能試験で明らかとなった。
However, although the occurrence of turbidity over time no longer occurs, it is clear from a sensory test by panelists that the problem that the original taste and mellowness of tea is faint occurs. became.

【0006】本発明は、上述した旨み、まろやかさとい
った茶類飲料に必要な要素を維持しつつ実質的に経時的
濁りの生じることのない茶飲料を提供するとともに、茶
抽出液の濾過を最適に行い、旨み、まろやかさの消失を
改善することのできる茶類飲料の製造方法を提供するこ
とを目的とする。
[0006] The present invention provides a tea beverage that does not substantially become cloudy over time while maintaining the above-mentioned umami and mellowness necessary for tea beverages and optimizes the filtration of the tea extract. It aims at providing the manufacturing method of the tea drink which can improve the disappearance of umami and mellowness.

【0007】[0007]

【課題を解決するための手段】本発明は上述した従来の
問題点を解決する方法であり、茶類飲料の製造工程にお
ける茶抽出液の濾過工程を改善したものである。
The present invention is a method for solving the above-mentioned conventional problems, and is an improvement of the process for filtering a tea extract in the process for producing a tea beverage.

【0008】先ず、本発明らは、茶抽出液に対して、
(1)ステンレスメッシュ(200メッシュ)による濾
過、(2)遠心分離機による濾過、(3)前記(2)を
施した後、更に、約1μmまでの濾過が可能なデプス
(層濾過)濾過方式フィルター(例えばカートリッジフ
ィルター)で濾過を行う、(4)前記(2)を施した
後、更に、精密濾過(珪素土濾過)を実施する、の4つ
の濾過方式の各々について、緑茶抽出液の濁度(吸光
度)、常温放置における経時的濁り状況について試験を
行った。なお、上記(1)の濾過については、約70μ
m程度の大きさの成分が除去され、(2)の濾過につい
ては、約10μm程度の成分が除去される。また、
(4)の方式では、0.5μm程度の成分が除去可能で
ある。
First, the present invention relates to a tea extract,
(1) Stainless steel mesh (200 mesh) filtration, (2) Centrifuge filtration, (3) After performing the above (2), depth (layer filtration) filtration method capable of further filtering up to about 1 μm Turbidity of the green tea extract for each of the four filtration methods: filtering with a filter (eg, cartridge filter), (4) performing the above (2), and then performing microfiltration (silicone earth filtration). Degree (absorbance) and turbidity with time at room temperature were tested. In addition, about the above (1) filtration, about 70μ
A component having a size of about m is removed, and in the filtration of (2), a component having a size of about 10 μm is removed. Also,
In the method of (4), a component of about 0.5 μm can be removed.

【0009】この試験は、煎茶10gを60℃300m
lの湯で抽出し、茶穀を網濾過して除去し、常温まで冷
却した抽出液を用いて各濾過を試み、最終的に1000
mlの製品液へと調合した。その後ガラス瓶に熱充填
し、オートクレーブにて殺菌し、常温で放置した。そし
て、濁度については、製造直後の製品液を700nmに
おける吸光度を調べることにより行い、沈殿状況につい
ては、1ヶ月放置、2ヶ月放置について観察した。
In this test, 10 g of green tea was used at 60 ° C. for 300 m
It was extracted with 1 l of hot water, the tea grains were removed by net filtration, and each filtration was tried using the extract cooled to room temperature.
Formulated into ml product solution. Then, the glass bottle was heat-filled, sterilized by an autoclave, and left at room temperature. The turbidity was measured by examining the absorbance of the product solution immediately after production at 700 nm, and the precipitation was observed for 1 month or 2 months.

【0010】表1はその試験結果を示す。Table 1 shows the test results.

【0011】[0011]

【表1】 表1に示すように、上記(2)の場合、700nmの吸光度
で0.06〜0.10であるのに対し、上記(3)の濾過方式を
行った場合には、700nmの吸光度が0.01〜0.03であっ
た。ちなみに、珪藻土濾過を施した場合には、700nmの
吸光度は0.001〜0.009であった。
[Table 1] As shown in Table 1, in the case of the above (2), the absorbance at 700 nm is 0.06 to 0.10, whereas when the filtration method of the above (3) is performed, the absorbance at 700 nm is 0.01 to 0.03. It was By the way, when the diatomaceous earth was filtered, the absorbance at 700 nm was 0.001 to 0.009.

【0012】なお、700nmの波長を用いるのは、7
00〜750nmの波長領域は赤外光であり、溶液の色
による影響を受けずに濁りの成分に作用できるからであ
る。
The wavelength of 700 nm is used by 7
This is because the wavelength region of 00 to 750 nm is infrared light and can act on the turbid component without being affected by the color of the solution.

【0013】表1の結果から解かるように、上記(1)
の濾過で得られた製品液は、吸光度の値は大きく、経時
的沈殿状況も多量であり、製品としては不適である。ま
た、(2)の濾過方式で得られた製品液も、吸光度はや
や大きく、また、経時的沈殿状況も2ヶ月後ではやや多
く、これも製品としては不向きである。
As can be seen from the results in Table 1, the above (1)
The product solution obtained by the filtration of No. 2 has a large absorbance value and a large amount of precipitation over time, and is not suitable as a product. Further, the product solution obtained by the filtration method of (2) also has a slightly high absorbance, and the precipitation state over time is slightly large after 2 months, which is also unsuitable as a product.

【0014】一方、(3)の濾過方式及び(4)の濾過
方式を用いた場合には、吸光度もきわめて小さく、経時
的沈殿も殆ど無く、商品として十分に満足できるもので
ある。
On the other hand, when the filtration method of (3) and the filtration method of (4) are used, the absorbance is extremely small and there is almost no precipitation over time, and the product is sufficiently satisfactory.

【0015】次に、各濾過方式により得られた製品液に
ついて官能評価試験を実施した。
Next, a sensory evaluation test was conducted on the product liquid obtained by each filtration method.

【0016】試験は、上記試験と同様に、煎茶10gを
60℃の300mlの湯で抽出し、網濾過後、常温まで
冷却した抽出液を用いて上記各濾過を行い、最終的に1
000mlの製品液へ調合した。その後、缶へ熱充填
し、オートクレーブにて殺菌し、1週間後に10名のパ
ネラーにて官能評価をした。表2はこの官能試験の結果
を示す。
In the test, as in the above test, 10 g of sencha was extracted with 300 ml of hot water at 60 ° C., filtered through a net, and then filtered using an extract cooled to room temperature, and finally 1
Formulated to 000 ml of product liquid. Then, the cans were heat-filled, sterilized by an autoclave, and one week later, sensory evaluation was conducted by 10 panelists. Table 2 shows the results of this sensory test.

【0017】[0017]

【表2】 上記試験結果によると、上記(1)〜(3)の濾過方式
は、上記(4)の濾過方式にくらべ官能評価が高く、1
μm程度の濾過を行って得られた抽出液サンプルでは、
旨み、まろやかな緑茶感が、ステンレス200メッシュ
濾過、遠心分離濾過を施したサンプル、即ち、精密濾過
を行わなかったサンプルと差がないことがわかった。
[Table 2] According to the above test results, the filtration methods of (1) to (3) have higher sensory evaluations than the filtration method of (4).
In the extract sample obtained by performing filtration of about μm,
It was found that the taste and mellow green tea feeling were not different from those of the sample that had been subjected to stainless 200 mesh filtration and centrifugal filtration, that is, the sample that had not been subjected to microfiltration.

【0018】以上の調査結果から、お茶抽出液(茶穀除
去、遠心分離濾過を実施したもの)を、約1μまでの含
有物質を濾過する濾過手段を介して濾過することによ
り、お茶本来の旨み、まろやかを損なわず、かつ、経時
的濁りを発生しない、茶類飲料を得ることができること
が確認された。また、1μ濾過により得られたお茶飲料
の濁度は、700nmの吸光度が0.01〜0.03であり、この吸
光度を有する お茶であれば、経時的濁りを生じないこ
とが確認された。したがって、上記(3)による濾過
(700nm吸光度で0.01〜0.03)が、沈殿の
発生を抑え、香味も優れた茶飲料を得ることのできる濾
過方法であるということができる。換言すれば、700
nm吸光度で0.01〜0.03の茶飲料は、濁度、経
時的な沈殿の観点から、また、香味においても、優れた
茶飲料であるということができる。
From the above survey results, it is possible to obtain the true flavor of tea by filtering the tea extract (the one from which tea grains have been removed and centrifugal separation filtration has been carried out) through a filtering means for filtering the contained substances up to about 1 μm. It was confirmed that it is possible to obtain a tea beverage that does not impair the mellowness and does not cause turbidity over time. The turbidity of the tea beverage obtained by 1 μ filtration had an absorbance at 700 nm of 0.01 to 0.03, and it was confirmed that tea having such an absorbance does not cause turbidity over time. Therefore, it can be said that the filtration according to the above (3) (0.01 to 0.03 at 700 nm absorbance) is a filtration method capable of suppressing the occurrence of precipitation and obtaining a tea beverage excellent in flavor. In other words, 700
It can be said that a tea beverage having an nm absorbance of 0.01 to 0.03 is an excellent tea beverage from the viewpoint of turbidity and precipitation over time, and also in terms of flavor.

【0019】次に、茶抽出液より700nm吸光度で
0.01〜0.03の茶飲料を得るための濾過工程につ
いて説明する。上述のように、700nm吸光度で0.
01〜0.03の茶飲料を得るには、約1μmまでの成
分を濾過することにより得ることができるが、茶抽出液
を、例えば、1μm程度まで濾過可能な濾材で一挙に濾
過しようとしても濾材がすぐに目詰りを起してしまうた
め、連続生産は不可能である。
Next, the filtration step for obtaining a tea beverage having an absorbance at 700 nm of 0.01 to 0.03 from the tea extract will be described. As described above, the absorbance at 700 nm was 0.
In order to obtain a tea beverage of 01 to 0.03, it is possible to obtain it by filtering components up to about 1 μm, but even if the tea extract is tried to be filtered all at once with a filter medium capable of filtering up to about 1 μm. Continuous production is not possible because the filter media will soon become clogged.

【0020】そこで、本発明においては、最適の濾過手
段を組み合わせて、最終的に約1μmまでの成分を濾過
する濾材を用いて、700nmにおける吸光度が0.0
1〜0.03を実現するようにした。
Therefore, in the present invention, an optimum filtration means is combined and a filter medium for finally filtering the components up to about 1 μm is used, and the absorbance at 700 nm is 0.0.
1 to 0.03 is realized.

【0021】本発明は、この濾過を達成する方法とし
て、複数段階濾過手段を用い、前段で濾紙もしくは濾布
による表面濾過手段を用い、後段で約1μまでの濾過を
可能にするデプス(層)濾過方式の濾過手段とで少なく
とも構成された複数段階濾過手段を用いることで達成す
ることができた。
In the present invention, as a method for achieving this filtration, a multi-stage filtration means is used, a surface filtration means with a filter paper or a filter cloth is used in the former stage, and a depth (layer) which enables filtration up to about 1 μ in the latter stage. This can be achieved by using a multi-stage filtration means that is at least configured with a filtration type filtration means.

【0022】なお、デプス(層)濾過方式とは、図1
(A)に示すように、濾材の表面及び濾材層内の網目に
より濾過を行うもので、濾紙や濾布のような表面濾過濾
材に比べて濾過面積が広い。この種の濾材の多くは濾材
表面の網目の大きさが粗く、濾材層の深さ方向に向かっ
て徐々に網目の大きさが細かくなるよう構成されてい
る。
The depth (layer) filtration system is shown in FIG.
As shown in (A), filtration is performed by the surface of the filter medium and the mesh in the filter medium layer, and has a wider filtration area than a surface filtration filter medium such as a filter paper or a filter cloth. Most of this kind of filter media have a coarse mesh size on the surface of the filter media, and the mesh size is gradually reduced in the depth direction of the filter media layer.

【0023】また、表面濾過方式の濾材は、図1(B)
に示すように、濾材の表面の網目で濾過を行うものであ
り、表面に濾過物が堆積してくると、背圧が高まり、網
目の大きさが拡大し、微細成分の濾過性能が低下する
(5μm程度の大きさの成分は十分濾過可能)。従っ
て、約1μmの微細成分の濾過を長時間継続するために
は層濾過方式の濾材を併用する方が好ましい。
The filter material of the surface filtration system is shown in FIG.
As shown in Fig. 2, the filtration is performed with the mesh on the surface of the filter medium, and when the filtration material is deposited on the surface, the back pressure increases, the size of the mesh increases, and the filtration performance of fine components decreases. (A component with a size of about 5 μm can be sufficiently filtered). Therefore, in order to continue the filtration of the fine component of about 1 μm for a long time, it is preferable to use the filter material of the layer filtration method together.

【0024】本発明の濾過の程度は、前記表1でみる
と、1ヶ月後、2ヶ月後の沈殿が、珪藻土濾過の「全く
なし」に対して「無し」のレベルであり、珪藻土濾過に
比べて若干濁りが感じられる程度で、ペットボトル等の
容器に入った状態では、識別し難い。
As to the degree of filtration of the present invention, as shown in Table 1 above, the precipitation after one month and after two months was at a level of "none" to "no" at the time of diatomaceous earth filtration. In comparison, it is slightly turbid, and is difficult to identify when it is in a container such as a plastic bottle.

【0025】以上のように、上記課題は、茶葉の抽出液
を濾過して得られた700nmの吸光度が0.01〜0.03の茶
類飲料によって解決される。
As described above, the above problems can be solved by a tea beverage having an absorbance at 700 nm of 0.01 to 0.03 obtained by filtering an extract of tea leaves.

【0026】また、約1ミクロンまでの大きさの物質を
濾過する濾過手段を採用することにより上記吸光度を有
する茶類飲料を得ることが可能となる。
Further, it is possible to obtain a tea beverage having the above-mentioned absorbance by adopting a filtering means for filtering a substance having a size of up to about 1 micron.

【0027】また、上記茶類飲料は、茶葉より抽出した
抽出液を茶穀除去と遠心分離濾過を行った後、抽出液に
含まれる約1ミクロンまでの大きさの物質を濾過して得
られた抽出液を用いて調合を行う製造ことにより得るこ
とができる。
The above tea beverage is obtained by removing tea grains from an extract extracted from tea leaves and centrifuging and filtering, and then filtering substances contained in the extract up to about 1 micron in size. It can be obtained by manufacturing using the extracted liquid.

【0028】また、茶葉よりその抽出液を得るための抽
出工程と、前記抽出液を茶穀除去及び遠心分離濾過を施
す工程と、遠心分離濾過を施した抽出液を濾過する複数
段階濾過工程を有し、前記複数段階濾過工程は、濾紙若
しくは濾布を用いた前段表面濾過工程と前記抽出液に含
まれる約1ミクロンまでの大きさの物質を濾過する層濾
過方式の後段濾過工程とからなる茶類飲料の製造方法に
よって、連続工程で本発明の茶類飲料を製造することが
できる。
Further, an extraction step for obtaining the extract from tea leaves, a step of removing the tea grains and centrifugal filtration of the extract, and a multi-step filtration step of filtering the extract subjected to centrifugal filtration The multi-step filtration step comprises a pre-stage surface filtration step using a filter paper or a filter cloth, and a post-stage filtration step of a layer filtration system for filtering substances contained in the extract up to about 1 micron in size. The tea beverage of the present invention can be manufactured in a continuous process by the method for manufacturing a tea beverage.

【0029】[0029]

【発明の実施の形態】次に、本発明の茶類飲料の製造方
法の実施形態を図2の工程図に従って説明する。
BEST MODE FOR CARRYING OUT THE INVENTION Next, an embodiment of the method for producing a tea beverage of the present invention will be described with reference to the process chart of FIG.

【0030】[茶抽出]先ず、煎茶10gを60℃で3
00mlの湯で抽出する(第1工程)。
[Tea Extraction] First, 10 g of green tea is mixed at 60 ° C. for 3 days.
Extract with 00 ml of hot water (first step).

【0031】[茶穀除去]次に、メッシュスクリーン等
の網濾過で茶穀を除去する(第2工程)。
[Removal of Tea Grains] Next, the tea grains are removed by mesh filtration using a mesh screen or the like (second step).

【0032】[冷却]次に、20℃〜30℃に速やかに
冷却する(第3工程)。
[Cooling] Next, the temperature is rapidly cooled to 20 ° C. to 30 ° C. (third step).

【0033】[遠心分離]次に、冷却後の茶類抽出液を
遠心分離機により10μm程度までの濁り成分(略10
μm以上の成分)を除去する(第4工程)。
[Centrifugation] Next, the cooled tea extract is subjected to a turbid component (about 10 μm) with a centrifuge.
components (μm or more) are removed (fourth step).

【0034】[濾布濾過]次に、第1濾過として、濾布
による表面濾過を行い、1〜5μm程度までの成分を濾
過する(第5工程)。
[Filtration with a filter cloth] Next, as the first filtration, surface filtration with a filter cloth is performed to filter components up to about 1 to 5 μm (fifth step).

【0035】[濾紙濾過]次に、第2段濾過として、濾
紙による表面濾過を行い、1〜3μm程度までの濁り成
分を除去する(第6工程)。
[Filtration with Filter Paper] Next, as the second stage filtration, surface filtration with filter paper is performed to remove turbid components up to about 1 to 3 μm (sixth step).

【0036】[デプス(層)濾過]次に、第3段濾過と
して、プラスチックフィルムを使用した層(デプス)濾
過方式の一種であるカートリジフィルタにより、約1μ
mまでの濁り成分を除去する(第7工程)。
[Depth (layer) filtration] Next, as the third stage filtration, about 1 μm was obtained by a Cartridge filter which is a kind of layer (depth) filtration method using a plastic film.
Turbid components up to m are removed (7th step).

【0037】[調合]次に、濁り成分除去した抽出液を
製品と同様酸化防止剤等を添加し、濃度調整等を行い、
調合し、最終的に1000mlの緑茶飲料を得た(第8
工程)。
[Preparation] Next, the extract from which the turbid components have been removed is added with an antioxidant and the like as in the case of the product to adjust the concentration,
It was mixed to finally obtain 1000 ml of green tea beverage (No. 8).
Process).

【0038】本実施形態により得られた茶飲料は、既
に、表1及び表2で示される1μmカートリッジフィル
タを使用したサンプルとして使用されたものであり、表
1及び表2に示されるように、遠心分離濾過してそのま
ま調合したサンプルと、遠心分離濾過の代わりにステン
レス200メッシュの網濾過(70μm程度の濁り成分
を濾過)を施し、調合したサンプルと比較しても、濁
度、経時的沈殿状況に関しても優れ、また官能評価につ
いて高い評価が得られている。
The tea beverage obtained according to the present embodiment has already been used as a sample using the 1 μm cartridge filter shown in Tables 1 and 2, and as shown in Tables 1 and 2, Centrifugal filtration and blended sample as it is, and stainless steel 200 mesh screen filtration (filtration of turbid components of about 70 μm) was performed instead of centrifugal filtration, and even when compared to the blended sample, turbidity and precipitation over time The situation is excellent, and the sensory evaluation is highly evaluated.

【0039】以上のように、本実施形態において、遠心
分離機、濾布濾過と濾紙濾過からなる前段濾過、及びカ
ートリッジフィルタ(1μm)による後段濾過を組み合
わせることにより、700nmにおける吸光度が0.0
1〜0.03である茶飲料を連続工程で製造することが
可能となる。
As described above, in the present embodiment, the absorbance at 700 nm is 0.0 by combining the centrifugal separator, the pre-stage filtration consisting of filter cloth filtration and filter paper filtration, and the post-stage filtration by the cartridge filter (1 μm).
It becomes possible to manufacture tea beverages of 1 to 0.03 in a continuous process.

【0040】なお、上述の濾布濾過と濾紙濾過の順序は
入れ替えることは可能である。
The order of the filter cloth filtration and the filter paper filtration can be exchanged.

【実施例】以下に、本発明の茶飲料の製造工場に適用複
数の製造工場において採用された具体的な製造工程の例
を示す。 (実施例1) ニーダ(茶抽出)→分離スクリーン→40メッシュスト
レーナ→冷却→遠心分離→濾布濾過→濾紙濾過→カート
リッジフィルタ(製品名:ポリプロクリーン(キュノ株
式会社製)→調合タンク (実施例2) ニーダ(茶抽出)→分離スクリーン→40メッシュスト
レーナ→冷却→遠心分離→濾紙濾過→濾布濾過→カート
リッジフィルタ(製品名:ポリプロクリーン(キュノ株
式会社製)→調合タンク 以上の実施例1、2の製造工程で得られた茶飲料は、い
ずれも、表1及び表2に「1μmカートリッジフィル
タ」として示される濁度、経時的沈殿状態、及び香味に
関し優れた品質を有するものであった。
EXAMPLES Below, examples of specific manufacturing processes adopted in a plurality of manufacturing factories applied to the tea beverage manufacturing factories of the present invention will be shown. (Example 1) Kneader (tea extraction)-> Separation screen-> 40 mesh strainer->Cooling->Centrifugation-> Filter cloth filtration-> Filter paper filtration-> Cartridge filter (Product name: Polyproclean (manufactured by Cuno Co., Ltd.)-> Preparation tank (Example) 2) Kneader (tea extraction) → Separation screen → 40 mesh strainer → Cooling → Centrifugation → Filter paper filtration → Filter cloth filtration → Cartridge filter (Product name: Polyproclean (manufactured by Cuno Co., Ltd.) → Mixing tank Each of the tea beverages obtained in the production process of No. 2 had excellent quality regarding the turbidity, the precipitation state over time, and the flavor shown in Tables 1 and 2 as “1 μm cartridge filter”.

【0041】なお、ここで使用したカートリッジフィル
タ(製品名:ポリプロクリーン)は、濾過特性の異なる
多種類のポリプロピレン製不織布を積層した中空の円筒
状濾材で構成されており、円筒表面より上記不織布層を
通過して得られた濾過液が中空部に出力される。
The cartridge filter (product name: polyproclean) used here is composed of a hollow cylindrical filter medium in which various types of polypropylene nonwoven fabrics having different filtration characteristics are laminated, and the nonwoven fabric layer is formed from the cylindrical surface. The filtrate obtained after passing through is output to the hollow portion.

【0042】[0042]

【発明の効果】以上詳述したところから明らかなよう
に、本発明の茶飲料の製造方法によれば、沈殿の発生が
少なく、香味の優れた茶飲料を得ることができる。そし
て、得られた茶飲料は顧客の要求を満たすことのできる
優れた品質の商品として提供できる。
EFFECTS OF THE INVENTION As is clear from the above description, according to the method for producing a tea beverage of the present invention, it is possible to obtain a tea beverage having less flavor and excellent flavor. Then, the obtained tea beverage can be provided as an excellent quality product that can satisfy the customer's requirements.

【図面の簡単な説明】[Brief description of drawings]

【図1】濾過材及び濾過機構を説明する図である。
(A)はデプスフィルターの説明図、(B)は表面濾過
フィルターの説明図である。
FIG. 1 is a diagram illustrating a filtering material and a filtering mechanism.
(A) is an explanatory view of a depth filter, (B) is an explanatory view of a surface filtration filter.

【図2】本発明による茶飲料製造方法の工程図を示す図
である。
FIG. 2 is a diagram showing a process chart of a method for producing a tea beverage according to the present invention.

───────────────────────────────────────────────────── フロントページの続き (72)発明者 井上 剛 神奈川県厚木市緑ヶ丘五丁目1番1号 サ ッポロビール飲料株式会社飲料開発研究所 内 Fターム(参考) 4B027 FB13 FC02 FC05 FE08 FP74 FP85    ─────────────────────────────────────────────────── ─── Continued front page    (72) Inventor Tsuyoshi Inoue             5-1-1 Midorigaoka, Atsugi City, Kanagawa Prefecture             Beverage Development Laboratory Co., Ltd.             Within F term (reference) 4B027 FB13 FC02 FC05 FE08 FP74                       FP85

Claims (4)

【特許請求の範囲】[Claims] 【請求項1】 茶葉の抽出液を濾過して得られた700
nmの吸光度が0.01〜0.03の茶類飲料。
1. 700 obtained by filtering an extract of tea leaves
A tea drink with an absorbance of 0.01 to 0.03 at nm.
【請求項2】 約1ミクロンまでの大きさの物質を濾過
する濾過手段により得られた請求項1に記載の茶類飲
料。
2. A tea beverage according to claim 1 obtained by filtration means for filtering substances up to about 1 micron in size.
【請求項3】 茶葉より抽出した抽出液を茶穀除去と遠
心分離濾過を行った後、抽出液に含まれる約1ミクロン
までの大きさの物質を濾過して得られた抽出液を用いて
調合を行う茶類飲料の製造方法。
3. An extract obtained by extracting tea grains from an extract extracted from tea leaves, centrifuging and filtering, and then filtering substances contained in the extract up to about 1 micron in size. A method for producing a tea beverage, which comprises mixing.
【請求項4】 茶葉よりその抽出液を得るための抽出工
程と、前記抽出液より茶穀および不溶性残渣を分離除去
する工程と、茶穀および不溶性残渣を分離除去した抽出
液を濾過する複数段階濾過工程を有し、前記複数段階濾
過工程は、濾紙若しくは濾布を用いた前段表面濾過工程
と前記抽出液に含まれる約1ミクロンまでの大きさの物
質を濾過する層濾過方式の後段濾過工程とからなる茶類
飲料の製造方法。
4. An extraction step for obtaining an extract of tea leaves, a step of separating and removing tea grains and insoluble residues from the extract, and a plurality of steps of filtering the extract from which tea grains and insoluble residues have been separated and removed. The multi-stage filtration process includes a pre-stage surface filtration process using a filter paper or a filter cloth and a post-stage filtration process of a layer filtration system for filtering substances contained in the extract up to about 1 micron in size. A method for producing a tea beverage comprising:
JP2001401219A 2001-12-28 2001-12-28 Tea beverage and method of production for the same Pending JP2003199495A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
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Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2001401219A JP2003199495A (en) 2001-12-28 2001-12-28 Tea beverage and method of production for the same

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Publication Number Publication Date
JP2003199495A true JP2003199495A (en) 2003-07-15

Family

ID=27640081

Family Applications (1)

Application Number Title Priority Date Filing Date
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Country Status (1)

Country Link
JP (1) JP2003199495A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2005122779A1 (en) * 2004-06-21 2005-12-29 Biobud Co., Ltd. Green tea extract having an improved taste and manufacturing method thereof
WO2009019876A1 (en) * 2007-08-08 2009-02-12 Kao Corporation Method for production of tea extract
JP2009153487A (en) * 2007-12-27 2009-07-16 Kao Corp Method for producing tea extract
JP2017504317A (en) * 2013-12-18 2017-02-09 ネステク ソシエテ アノニム Method for improving the clarity and coolness attributes of green tea and reducing bitterness and astringency

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2005122779A1 (en) * 2004-06-21 2005-12-29 Biobud Co., Ltd. Green tea extract having an improved taste and manufacturing method thereof
WO2009019876A1 (en) * 2007-08-08 2009-02-12 Kao Corporation Method for production of tea extract
JP2009153487A (en) * 2007-12-27 2009-07-16 Kao Corp Method for producing tea extract
JP2017504317A (en) * 2013-12-18 2017-02-09 ネステク ソシエテ アノニム Method for improving the clarity and coolness attributes of green tea and reducing bitterness and astringency
US10820606B2 (en) 2013-12-18 2020-11-03 Societe Des Produits Nestle S.A. Methods for increasing the clarity and refreshing attributes and reducing the bitterness and astringency of green tea

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