JP2006174711A - Method for producing tea paste - Google Patents

Method for producing tea paste Download PDF

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JP2006174711A
JP2006174711A JP2004368287A JP2004368287A JP2006174711A JP 2006174711 A JP2006174711 A JP 2006174711A JP 2004368287 A JP2004368287 A JP 2004368287A JP 2004368287 A JP2004368287 A JP 2004368287A JP 2006174711 A JP2006174711 A JP 2006174711A
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tea
tea leaves
paste
wet
producing
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Akikazu Yamamoto
明和 山本
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Kurita Water Industries Ltd
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Abstract

<P>PROBLEM TO BE SOLVED: To provide a method for producing tea paste by which wet tea leaves such as moisture-containing tea dregs can be smoothly crushed regardless of grain diameters of the tea leaves into paste. <P>SOLUTION: The method for producing tea paste comprises using wet tea leaves obtained through soaking tea leaves in a liquid such as warm water in advance, adding a dilute solution to the wet tea leaves in a regulation tank so as to have a prescribed moisture content, roughly crushing the tea leaves with a rough-crushing machine, and making the crushed tea leaves circulate in the regulation tank. Specifically, the dilute solution is introduced in the regulation tank 21 and a rough crushing machine 31 composed of a cutter pump or the like is driven so as to introduce the wet tea leaves through a tea-leaf passage 25 while making the dilute solution fluid, the wet tea leaves are crushed and circulated between the rough-crushing machine 31 and the regulation tank 21. <P>COPYRIGHT: (C)2006,JPO&NCIPI

Description

本発明は、茶葉に液体を加えて細かく破砕して茶ペーストを製造する方法に関し、特に茶滓から茶ペーストを製造する方法に関する。   The present invention relates to a method for producing a tea paste by adding a liquid to tea leaves and finely crushing, and more particularly to a method for producing a tea paste from teacups.

近年、廃棄物の再利用が促進され、茶飲料の製造過程で発生する茶滓についても再利用を目的とした種々の処理法が提案されている。例えば特許文献1には、茶滓を脱水し、遠赤外線を用いて乾燥させた後に粉砕することにより、茶滓から食品添加物を製造する方法が開示されている。この方法によれば、茶滓を脱水して遠赤外線を用いて乾燥させることで、茶滓の腐敗を防ぎ、また、アミノ酸やテアニン等の有用な成分の含有量を増加させることができるとされる。   In recent years, the reuse of waste has been promoted, and various treatment methods have been proposed for the purpose of reusing teacups generated in the production process of tea beverages. For example, Patent Document 1 discloses a method for producing a food additive from teacups by dehydrating the teacups, drying them using far infrared rays, and then pulverizing them. According to this method, the tea bowl is dehydrated and dried using far-infrared rays, thereby preventing the decay of the tea bowl and increasing the content of useful components such as amino acids and theanine. The

しかし、上記方法では茶滓の脱水濾液に茶葉の含有成分が移行するため、脱水によって茶滓から有用な成分が失われる上、脱水濾液の処理が必要になる。このため、本願発明者は先に、水分を含んだ状態の茶滓を破砕してペースト状として再利用する方法を提案している(特願2004−501023)。   However, in the above method, since the components contained in the tea leaves are transferred to the dehydrated filtrate of the tea bowl, useful components are lost from the tea bowl by dehydration, and the dehydrated filtrate needs to be processed. For this reason, the inventor of the present application has previously proposed a method of crushing a teacup containing water and reusing it as a paste (Japanese Patent Application No. 2004-501023).

ところで茶葉をペースト状にする方法としては、乾燥茶葉の微細化物に油脂や糖アルコール液等の液体を添加した混合物を所定の条件で磨砕して茶ペーストを製造する方法が提案されている(特許文献2)。特許文献2に記載された方法によれば、あらかじめ粒子径が1mm以下程度に破砕された茶葉の微細化物に液体を添加することにより、茶葉を磨砕する際の粉体の飛散を防止して茶葉を極めて細かくできる。   By the way, as a method for making tea leaves into a paste, a method has been proposed in which a mixture obtained by adding a liquid such as fat or sugar alcohol liquid to a refined dried tea leaf is ground under predetermined conditions to produce a tea paste ( Patent Document 2). According to the method described in Patent Document 2, by adding a liquid to a refined tea leaf that has been previously crushed to a particle size of about 1 mm or less, the powder is prevented from being scattered when grinding the tea leaf. Tea leaves can be made very fine.

しかし上記方法ではあらかじめ微細化した乾燥茶葉を用いることから、上記方法を茶滓に適用する場合には特許文献1に開示された方法と同様に茶滓を脱水乾燥させる必要がある。また、様々な大きさの茶片を含む茶葉を処理しようとすると、茶葉が磨砕装置に詰まるトラブルや磨砕処理に要する時間が長くなるといった問題を引き起こすおそれがある。
特開2003−111566号公報 特開2001−107号公報
However, since the above method uses dried tea leaves that have been refined in advance, when the above method is applied to teacups, it is necessary to dehydrate and dry the teacups as in the method disclosed in Patent Document 1. In addition, when trying to process tea leaves containing various sizes of tea pieces, there is a risk of causing problems such as trouble that the tea leaves are clogged in the grinding apparatus and a longer time required for the grinding process.
Japanese Patent Laid-Open No. 2003-111466 Japanese Patent Laid-Open No. 2001-107

本発明は上記課題に鑑みてなされたものであり、その目的は、茶葉の粒径に係らず品質が均質化された茶ペーストを簡易に製造できる茶ペーストの製造方法を提供することである。また、本発明は特に水分を含んだ茶滓のような湿潤茶葉を、茶葉の粒径や、茶の茎と葉の混合比率に係らずスムーズに破砕してペースト状にできる茶ペーストの製造方法を提供することを目的とする。   This invention is made | formed in view of the said subject, The objective is to provide the manufacturing method of the tea paste which can manufacture easily the tea paste in which quality was homogenized irrespective of the particle size of the tea leaf. In addition, the present invention is a method for producing a tea paste that can be crushed smoothly into a paste form, regardless of the particle size of tea leaves or the mixing ratio of tea stems and leaves. The purpose is to provide.

本発明は、茶葉をあらかじめ温水等の液体に浸漬することにより得られた湿潤茶葉を用い、調整槽で所定の含水率となるように湿潤茶葉に希釈液を添加した上で粗破砕機で粗破砕して調整槽に循環させる。より具体的には、本発明は以下を提供する。   The present invention uses wet tea leaves obtained by immersing tea leaves in a liquid such as warm water in advance, and after adding a diluent to the wet tea leaves so that the moisture content becomes a predetermined water content in the adjustment tank, Crush and circulate in the conditioning tank. More specifically, the present invention provides the following.

(1) 茶葉を液体に浸漬させて得られた湿潤茶葉を、攪拌機を備えた調整槽に導入して希釈液と混合し固形物濃度を調整して希釈茶葉を得る濃度調整工程と、前記濃度調整工程で得られた希釈茶葉を前記調整槽から送り出し粗破砕機を通過させて粗破砕する粗破砕工程と、前記粗破砕工程の粗破砕機を通過した粗破砕茶葉を前記濃度調整工程の調整槽に循環させる循環工程と、を含む茶ペーストの製造方法。   (1) A concentration adjusting step for obtaining a diluted tea leaf by introducing a wet tea leaf obtained by immersing the tea leaf in a liquid into a regulating tank equipped with a stirrer and mixing the diluted tea leaf with a diluent to obtain a diluted tea leaf; Adjusting the concentration adjustment step for the rough crushing step of sending the diluted tea leaves obtained in the adjustment step from the adjustment tank and passing through the coarse crusher for rough crushing, and the coarse crushing tea leaves passing through the rough crusher in the rough crushing step A method for producing a tea paste, comprising a circulation step of circulating in a tank.

ここで「湿潤茶葉」とは、生茶葉又は製茶が温水等の液体に1分間以上、好ましくは3〜5分間浸漬されることにより得られるもので、含水率78〜85重量%、好ましくは80〜83重量%の水分を含む。なお、液体に浸漬される「茶葉」は飲食に供される茶葉であり、飲食用に加工された「製茶」のみならず、茶樹から採取され実質的に加工されていない茶葉である「生茶葉」も含むものとする。また「製茶」とは、生茶葉が蒸熱製法、釜炒製法及び発酵等の公知の方法で加工された茶葉を意味し、乾燥された「乾燥茶葉」を含む。生茶葉が採取される茶樹の品種や、製茶を製造する加工法に特に制限はない。   Here, “wet tea leaves” are obtained by immersing fresh tea leaves or tea in a liquid such as warm water for 1 minute or more, preferably 3 to 5 minutes, and a moisture content of 78 to 85% by weight, preferably 80%. Contains ~ 83 wt% moisture. The “tea leaves” immersed in the liquid are tea leaves used for eating and drinking, and not only “tea making” processed for eating and drinking, but also “raw tea leaves” that are tea leaves collected from tea trees and not processed substantially. Is also included. The term “tea making” means tea leaves obtained by processing raw tea leaves by known methods such as steaming, kettle making, and fermentation, and includes dried “dried tea leaves”. There are no particular restrictions on the tea tree varieties from which fresh tea leaves are collected and the processing method for producing tea.

希釈液は、湿潤茶葉と希釈液との混合物(「希釈茶葉」と称する)の固形物濃度が5〜10重量%、好ましくは7〜8重量%となるように湿潤茶葉に混合される。希釈茶葉は、調整槽を経て粗破砕機を通過することにより粗破砕機で大まかに破砕され、調整槽に循環されることで次第に細かく破砕される。このため本発明によれば、湿潤茶葉に粒径が大きい葉片や、葉脈、葉柄、及び茎等の管状体が含まれる場合でも、漸次これらを細片化できるため、破砕機のトラブルを防止して、粒径が整った茶ペーストを得ることができる。   The diluted solution is mixed with the wet tea leaf so that the solid concentration of the mixture of the wet tea leaf and the diluted solution (referred to as “diluted tea leaf”) is 5 to 10% by weight, preferably 7 to 8% by weight. Diluted tea leaves are roughly crushed by the coarse crusher by passing through the coarse crusher through the adjustment tank, and gradually and finely crushed by being circulated to the adjustment tank. For this reason, according to the present invention, even when the wet tea leaves include leaf pieces having a large particle diameter and tubular bodies such as veins, petioles, and stems, these can be gradually broken down, thereby preventing troubles in the crusher. Thus, a tea paste with a uniform particle size can be obtained.

(2) 前記濃度調整工程において、あらかじめ希釈液を前記調整槽に導入して流動化させた状態で前記湿潤茶葉を導入する(1)に記載の茶ペーストの製造方法。   (2) In the said density | concentration adjustment process, the manufacturing method of the tea paste as described in (1) which introduce | transduces the said wet tea leaf in the state which introduce | transduced the diluent into the said adjustment tank and fluidized.

湿潤茶葉は、茶葉が水分を吸収しているため、植物組織が軟化して破砕され易いが、流動性が低い。そこで(2)記載の方法に従い、希釈液をあらかじめ調整槽に導入して流動化させた状態で湿潤茶葉を調整槽に少量ずつ導入することにより、あらかじめ流動化された希釈液の慣性を利用して湿潤茶葉の流動を促進できる。このため、湿潤茶葉が調整槽内に停滞することを防止し、かつ、希釈茶葉を粗破砕機に送り出して粗破砕機から調整槽に循環させるためのエネルギー消費を低減できる。   Since wet tea leaves absorb moisture, the wet tea leaves tend to be softened and crushed, but have low fluidity. Therefore, according to the method described in (2), the wet tea leaves are introduced into the adjustment tank little by little in a state where the dilution liquid is introduced into the adjustment tank in advance and fluidized, thereby utilizing the inertia of the previously fluidized dilution liquid. And can promote the flow of wet tea leaves. For this reason, it is possible to prevent the wet tea leaves from staying in the adjustment tank, and to reduce energy consumption for sending the diluted tea leaves to the coarse crusher and circulating them from the coarse crusher to the adjustment tank.

調整槽内には、希釈液をあらかじめ調整槽の容量の半量程度導入し、攪拌機で流動性を与えながら、湿潤茶葉を調整槽に保持された希釈液に対して1/4〜1/2倍ずつ、5〜10分程度をかけて調整槽に導入することが好ましい。調整槽には、調整槽内の流体物の固形物濃度が7〜8重量%の範囲となるように、適宜、希釈液を追加添加してもよい。   About half of the volume of the adjustment tank is introduced into the adjustment tank in advance, and the wet tea leaves are ¼ to 1/2 times the dilution liquid held in the adjustment tank while providing fluidity with a stirrer. It is preferable to introduce into the adjustment tank over about 5 to 10 minutes. A diluent may be added to the adjustment tank as appropriate so that the solid concentration of the fluid in the adjustment tank is in the range of 7 to 8% by weight.

茶ペーストの製造方法は、回分式又は連続式のどちらとしてもよく、回分式とする場合は調整槽に一定量の希釈液及び湿潤茶葉を導入した時点で希釈液及び湿潤茶葉の調整槽への導入を停止し、粗破砕工程と循環工程のみを継続する。そして、調整槽内の流体物の平均粒径及び固形物濃度が所定値となったら、粗破砕工程及び循環工程を継続しながら、調整槽内から粗破砕茶葉を取り出す。一方、連続式では希釈液又は/及び湿潤茶葉を連続的又は間欠的に調整槽に導入して濃度調整工程を継続しながら、調整槽内の流体物の平均粒径及び固形物濃度が所定範囲内の値となったら、調整槽から送出される粗破砕物の一部を循環させながら排出する。   The method for producing the tea paste may be either a batch type or a continuous type. In the case of a batch type, when a certain amount of dilution liquid and wet tea leaves are introduced into the adjustment tank, the dilution liquid and wet tea leaves are added to the adjustment tank. Stop the introduction and continue only the coarse crushing process and the circulation process. And if the average particle diameter and solid substance density | concentration of the fluid in a adjustment tank become a predetermined value, a rough crushing tea leaf will be taken out from the adjustment tank, continuing a rough crushing process and a circulation process. On the other hand, in the continuous type, the average particle diameter and solid matter concentration of the fluid in the adjustment tank are within a predetermined range while continuously introducing the diluent or / and wet tea leaves into the adjustment tank continuously or intermittently. When the value is within the range, a part of the coarsely crushed material sent from the adjustment tank is circulated and discharged.

(3) 前記濃度調整工程において、前記湿潤茶葉の含水率を測定し前記希釈液の量を制御する(1)又は(2)に記載の茶ペーストの製造方法。   (3) In the said density | concentration adjustment process, the moisture content of the said wet tea leaf is measured, and the manufacturing method of the tea paste as described in (1) or (2) which controls the quantity of the said dilution liquid.

調整槽に導入される湿潤茶葉の含水率は種々の要因により変動し、特に湿潤茶葉として茶滓を用いる場合は変動幅が大きいため、湿潤茶葉の含水率に応じて希釈液の添加量を制御することが好ましい。   The moisture content of the wet tea leaves introduced into the adjustment tank varies depending on various factors. Especially when using teacups as wet tea leaves, the fluctuation range is large, so the amount of diluent added is controlled according to the moisture content of the wet tea leaves. It is preferable to do.

(4) 近赤外分光法による非接触式含水率計を用いて前記湿潤茶葉の含水率を測定する(3)に記載の茶ペーストの製造方法。   (4) The method for producing a tea paste according to (3), wherein the moisture content of the wet tea leaf is measured using a non-contact moisture meter by near infrared spectroscopy.

湿潤茶葉の含水率の測定手段は、特に限定されないが、近赤外分光法を利用した非接触式の含水率計を用いれば、調整槽に導入される湿潤茶葉の含水率を簡易かつ迅速に算出できる。このため(4)では、簡易、迅速、かつ高精度で希釈液の添加量を制御できる。   The means for measuring the moisture content of the wet tea leaves is not particularly limited, but if a non-contact moisture meter using near infrared spectroscopy is used, the moisture content of the wet tea leaves introduced into the adjustment tank can be easily and quickly determined. It can be calculated. For this reason, in (4), the addition amount of the diluent can be controlled simply, quickly, and with high accuracy.

(5) 前記濃度調整工程において前記湿潤茶葉に添加剤を添加する(1)から(4)のいずれかに記載の茶ペーストの製造方法。   (5) The method for producing a tea paste according to any one of (1) to (4), wherein an additive is added to the wet tea leaves in the concentration adjusting step.

濃度調整工程では、湿潤茶葉に酸化防止剤等の添加剤を添加することにより、製造される茶ペーストの品質の保持又は/及び均質化を図ることもできる。特に好ましい添加剤としては、抗菌や抗酸化等の作用を有するポリフェノール類、及び抗酸化作用を有するビタミンCが挙げられ、これらを単独又は組み合わせて使用してよい。特に、ポリフェノール類としてカテキン類を添加するようにすれば、茶ペーストの品質保持を図るだけでなく、茶ペーストのカテキン含有量を調整することにより品質の均質化を図ることができる。また、希釈液として抗酸化性ガスを含む抗酸化水を使用することで、湿潤茶葉の希釈と添加剤の添加を兼ねることができる。   In the concentration adjusting step, the quality of the tea paste produced can be maintained or / and homogenized by adding an additive such as an antioxidant to the wet tea leaves. Particularly preferred additives include polyphenols having antibacterial and antioxidant effects, and vitamin C having an antioxidant action, and these may be used alone or in combination. In particular, if catechins are added as polyphenols, not only the quality of the tea paste can be maintained, but also the quality can be homogenized by adjusting the catechin content of the tea paste. Further, by using an antioxidant water containing an antioxidant gas as a diluent, it is possible to both dilute wet tea leaves and add additives.

ここで、「抗酸化性ガス」とは、酸素を還元する作用を有するガス、例えば水素ガスや一酸化炭素ガスのような還元性ガス、及び不活性ガスを意味する。本明細書において「不活性ガス」とは、化学反応の中でも特に酸化反応を起こしにくい気体を意味し、ヘリウム、アルゴンなどの希ガス族元素に限らず、窒素ガス及び炭酸ガスを含む。「抗酸化水」とはこうした抗酸化性ガスを含む水を意味し、特に好適な例として炭酸水、窒素含有水、及び水素含有水が挙げられる。   Here, the “antioxidant gas” means a gas having an action of reducing oxygen, for example, a reducing gas such as hydrogen gas or carbon monoxide gas, and an inert gas. In the present specification, “inert gas” means a gas that hardly causes an oxidation reaction among chemical reactions, and is not limited to a rare gas group element such as helium or argon, but includes nitrogen gas and carbon dioxide gas. “Antioxidant water” means water containing such an antioxidant gas, and particularly preferred examples include carbonated water, nitrogen-containing water, and hydrogen-containing water.

添加剤の添加量としては、ポリフェノール類については、希釈茶葉のポリフェノール類濃度が0.4〜0.8重量%となる範囲が好ましく、ビタミンCについては、希釈茶葉に対して0.05〜0.1重量%が好ましい。また、抗酸化水については、抗酸化性ガスを10〜100mg/L程度含むことが好ましく、さらにpHが3〜5であることが好ましい。   As the addition amount of the additive, for polyphenols, a range in which the concentration of polyphenols in diluted tea leaves is 0.4 to 0.8% by weight is preferable, and for vitamin C, 0.05 to 0 with respect to diluted tea leaves. .1% by weight is preferred. Moreover, about antioxidant water, it is preferable that antioxidant gas is contained about 10-100 mg / L, and it is more preferable that pH is 3-5.

(6) 前記濃度調整工程において、前記調整槽にマイクロバブル発生手段を設け抗酸化性ガスを吹き込む(1)から(5)のいずれかに記載の茶ペーストの製造方法。   (6) The method for producing a tea paste according to any one of (1) to (5), wherein in the concentration adjustment step, microbubble generation means is provided in the adjustment tank and an antioxidant gas is blown.

希釈液として抗酸化水を用いる場合は、あらかじめ水に抗酸化性ガスを溶解させることにより調製された抗酸化水を調整槽に導入してもよいが、抗酸化性ガスを含まない水道水等を希釈液として用い、調整槽にマイクロバブル発生手段を設けることにより、抗酸化性ガスを微細気泡化させて調整槽内の流体物に添加してもよい。本発明では、調整槽内には粗破砕された茶葉が循環されて保持されるため、抗酸化性ガスのマイクロバブルが茶葉に付着して溶解効率が向上するとともに、茶葉の表面の酸素が還元されることで酸化防止及び好気性微生物の増殖防止効果を高くできる。   When using antioxidant water as a diluting solution, antioxidant water prepared by dissolving an antioxidant gas in water in advance may be introduced into the adjustment tank, but tap water that does not contain antioxidant gas, etc. May be used as a diluting solution, and microbubble generation means may be provided in the adjustment tank to make the antioxidant gas into fine bubbles and added to the fluid in the adjustment tank. In the present invention, since the roughly crushed tea leaves are circulated and held in the adjustment tank, antioxidant gas microbubbles adhere to the tea leaves to improve dissolution efficiency, and oxygen on the surface of the tea leaves is reduced. As a result, the effect of preventing oxidation and the growth of aerobic microorganisms can be enhanced.

(7) 前記循環工程から前記濃度調整工程の調整槽に循環され平均粒径1000〜5000μmの固形物を含む前記粗破砕茶葉を、前記調整槽から排出して微破砕してペースト状の茶ペーストを得るペースト化工程をさらに含む(1)から(6)のいずれかに記載の茶ペーストの製造方法。   (7) The coarsely crushed tea leaves that are circulated from the circulation step to the adjustment tank of the concentration adjustment step and contain solid matter having an average particle diameter of 1000 to 5000 μm are discharged from the adjustment tank and finely crushed to give a paste-like tea paste The method for producing a tea paste according to any one of (1) to (6), further including a pasting step for obtaining the above.

本発明では、粗破砕された粗破砕茶葉をさらに細かく破砕するペースト化工程を設けることで、茶ペーストの使用用途に応じて異なる粒径の茶ペーストを製造できる。特に、ペースト化工程において、カッタ付きの攪拌羽根を備えるインライン型のミルつきポンプによる微破砕処理と、砥石を備える磨砕機による湿式磨砕処理と、をこの順で行なう2段階処理を行なうと、粒径が100μm以下に微細化された滑らかな茶ペーストを得ることができる。   In the present invention, by providing a pasting step for further finely crushing roughly crushed coarsely crushed tea leaves, tea pastes with different particle sizes can be produced according to the intended use of the tea paste. In particular, in the pasting step, when performing a two-stage process in which a fine crushing process by an inline-type pump with a mill equipped with a stirring blade with a cutter and a wet crushing process by a grinder equipped with a grindstone are performed in this order, A smooth tea paste having a particle size of 100 μm or less can be obtained.

(8) 前記ペースト化工程で得られた茶ペーストを滅菌する滅菌工程をさらに含む(7)に記載の茶ペーストの製造方法。   (8) The method for producing a tea paste according to (7), further including a sterilization step of sterilizing the tea paste obtained in the pasting step.

滅菌工程で茶ペーストを滅菌することにより製造された茶ペーストの保存性を高めることができる。滅菌工程で用いられる滅菌方法は特に限定されないが、短時間で簡易かつ確実に滅菌できる加熱滅菌を用いることが好ましい。特に、滅菌工程の前段で湿式磨砕処理を行なって茶ペーストを摩擦熱で30〜70℃程度に加温した後、速やかに滅菌工程を実施することにより、加熱に必要なエネルギー量を低減でき、好ましい。   The preservability of the tea paste produced by sterilizing the tea paste in the sterilization process can be improved. The sterilization method used in the sterilization step is not particularly limited, but it is preferable to use heat sterilization that can be sterilized easily and reliably in a short time. In particular, the amount of energy required for heating can be reduced by carrying out a wet grinding process before the sterilization process and heating the tea paste to about 30-70 ° C. with frictional heat, and then quickly performing the sterilization process. ,preferable.

(9) 前記滅菌工程で滅菌された茶ペーストを無菌状態で包装容器に充填する充填工程をさらに含む(8)に記載の茶ペーストの製造方法。   (9) The method for producing a tea paste according to (8), further including a filling step of filling the packaging container in a sterile state with the tea paste sterilized in the sterilization step.

本発明では滅菌工程で滅菌された茶ペーストは、無菌条件下で滅菌された包装容器に充填する。滅菌された茶ペーストを包装容器に充填することでさらに保存性を高めることができる。   In the present invention, the tea paste sterilized in the sterilization process is filled in a packaging container sterilized under aseptic conditions. Preservability can be further enhanced by filling the packaging container with sterilized tea paste.

(10) 前記湿潤茶葉は茶滓である(1)から(9)のいずれかに記載の茶ペーストの製造方法。   (10) The method for producing a tea paste according to any one of (1) to (9), wherein the wet tea leaves are teacups.

湿潤茶葉としては、煎茶、玉露、番茶、紅茶、及びウーロン茶等の乾燥茶葉を温水に浸漬して茶飲料を製造することにより得られる茶滓を用いることが好ましい。茶滓には、製茶の60〜80%程度のポリフェノール類が残存する一方、カフェイン量が低減されている。このため茶滓から製造された茶滓ペーストは、ポリフェノール類により保存性が高められる一方、カフェインが低減されていることから幅広い用途に再利用できる。   As the wet tea leaves, it is preferable to use tea bowls obtained by immersing dry tea leaves such as sencha, gyokuro, bancha, black tea, and oolong tea in hot water to produce a tea beverage. In the tea bowl, polyphenols of about 60 to 80% of tea are left, while the amount of caffeine is reduced. For this reason, teacup paste produced from teacups can be reused for a wide range of uses because caffeine is reduced while preservability is enhanced by polyphenols.

本発明によれば、あらかじめ液体に浸漬して軟化させた湿潤茶葉を循環しながら破砕することで、繊維の絡みつき等による破砕トラブルを防止し、茶葉を徐々に細片化して粒径が整った茶ペーストを得ることができる。また本発明によれば、簡易な構成の装置で品質が均質化された茶ペーストを効率よく製造できるため、高品質の茶ペーストを安価に提供できる。   According to the present invention, the wet tea leaves that have been softened by immersing in a liquid in advance are crushed while circulating, thereby preventing crushing troubles due to fiber entanglement and the like, and the tea leaves are gradually fragmented to prepare the particle size. Tea paste can be obtained. Further, according to the present invention, a tea paste whose quality is homogenized can be efficiently produced with an apparatus having a simple configuration, so that a high quality tea paste can be provided at low cost.

以下、図面を参照して本発明について具体的に説明する。図1は、本発明に係る茶ペーストの製造方法を実施するための茶ペースト製造装置(以下、単に「製造装置」)11の模式図である。   Hereinafter, the present invention will be specifically described with reference to the drawings. FIG. 1 is a schematic view of a tea paste manufacturing apparatus (hereinafter simply referred to as “manufacturing apparatus”) 11 for carrying out the method of manufacturing a tea paste according to the present invention.

製造装置11は、調整槽21と、粗破砕機31と、微破砕機41と、磨砕機51と、滅菌機61と、充填機71と、を備える。調整槽21と粗破砕機31とは第1接続管35で、粗破砕機31と微破砕機41とは第2接続管45で、微破砕機41と磨砕機51とは第3接続管55で、磨砕機51と滅菌機61とは第4接続管65で、滅菌機61と充填機71とは第5接続管75で、それぞれ相互に直列接続されている。   The production apparatus 11 includes an adjustment tank 21, a rough crusher 31, a fine crusher 41, a grinder 51, a sterilizer 61, and a filling machine 71. The adjustment tank 21 and the rough crusher 31 are the first connection pipe 35, the rough crusher 31 and the fine crusher 41 are the second connection pipe 45, and the fine crusher 41 and the grinder 51 are the third connection pipe 55. Thus, the attritor 51 and the sterilizer 61 are connected to each other in series by a fourth connecting pipe 65, and the sterilizer 61 and the filling machine 71 are connected to each other in series by a fifth connecting pipe 75.

調整槽21と粗破砕機31とは循環路36でも接続されており、第1接続管35は調整槽21の出口側と粗破砕機31の入口側とに接続され、循環路36は調整槽21の入口側と粗破砕機31の出口側とに接続されている。調整槽21には攪拌機23が設けられ、茶葉路25、希釈液路26及び添加剤路27がさらに接続され、添加剤路27には添加剤貯槽22が接続されている。   The adjustment tank 21 and the coarse crusher 31 are also connected by a circulation path 36, the first connecting pipe 35 is connected to the outlet side of the adjustment tank 21 and the inlet side of the rough crusher 31, and the circulation path 36 is connected to the adjustment tank. The inlet side of 21 and the outlet side of the rough crusher 31 are connected. The adjustment tank 21 is provided with a stirrer 23, a tea leaf path 25, a diluent path 26 and an additive path 27 are further connected, and the additive path 27 is connected to an additive storage tank 22.

粗破砕機31は、筒状の筐体30の内部にカッタ付きの回転羽根(以下「破砕羽根」)32と、その背面に設けられたスリットが形成された板34と、圧送用の回転羽根(以下「移送羽根」)33とを備えるカッタポンプである。微破砕機41は、筐体40内部に破砕羽根42及び破砕ミル43を備えるインラインミルポンプで構成されている。微破砕機41の破砕羽根42の背面にはスリットが形成された板44が設けられている。   The rough crusher 31 includes a rotating blade (hereinafter referred to as “crushing blade”) 32 with a cutter inside a cylindrical housing 30, a plate 34 provided with a slit provided on the back surface thereof, and a rotating blade for pressure feeding. (Hereinafter referred to as “transfer blade”) 33. The fine crusher 41 is configured by an in-line mill pump including a crushing blade 42 and a crushing mill 43 inside the housing 40. A plate 44 having slits is provided on the back surface of the crushing blade 42 of the fine crusher 41.

次に、本発明の第1実施態様として、上記の製造装置11を用い、湿潤茶葉としての茶滓を破砕してペースト状の茶滓ペーストを製造する方法について説明する。   Next, as a first embodiment of the present invention, a method for producing a paste-like teacup paste by crushing teacups as wet tea leaves using the production apparatus 11 will be described.

まず、希釈液として炭酸水を希釈液路26からあらかじめ調整槽21に導入する。調整槽21内の液量が一定量に達したら、攪拌機23を稼動する。次に、粗破砕機31を稼動させることにより調整槽21から送り出された炭酸水を、循環路36を介して調整槽21に循環させて流動化させる。このようにして、炭酸水を流動化させた状態で茶葉路25から茶滓を調整槽21に導入する。茶滓は、調整槽21内に導入されることで流動状態にある炭酸水と攪拌混合され、炭酸水との接触によって茶滓表面の酸素が除去され、雑菌の増殖が抑制される。   First, carbonated water as a diluent is introduced into the adjustment tank 21 from the diluent path 26 in advance. When the amount of liquid in the adjustment tank 21 reaches a certain amount, the stirrer 23 is operated. Next, the carbonated water sent out from the adjustment tank 21 by operating the rough crusher 31 is circulated and fluidized in the adjustment tank 21 via the circulation path 36. In this manner, the tea bowl is introduced from the tea leaf path 25 into the adjustment tank 21 in a state where the carbonated water is fluidized. The teacup is stirred and mixed with carbonated water in a fluidized state by being introduced into the adjustment tank 21, and oxygen on the surface of the teacup is removed by contact with the carbonated water, so that the growth of germs is suppressed.

調整槽21には、湿潤茶葉の導入に先立って調整槽21の容量の半量の希釈液を導入し、所定量の湿潤茶葉を5〜10分程度かけて漸次、調整槽21に供給することが好ましい。調整槽21には、槽内の流体物(希釈茶葉と粗破砕茶葉の混合物)の固形物濃度が5〜10重量%、好ましくは7〜8重量%となるよう、適宜、希釈液又は/及び湿潤茶葉を添加して濃度調整を行なう。このように、あらかじめ調整槽21内に導入された炭酸水を流動化させ、調整槽21内の流体物の固形物濃度を所定範囲内とすることにより、調整槽21内の流体物をスムーズに粗破砕機31に送出できる。   Prior to the introduction of the wet tea leaves, a half amount of the diluted liquid is introduced into the adjustment tank 21, and a predetermined amount of the wet tea leaves are gradually supplied to the adjustment tank 21 over about 5 to 10 minutes. preferable. In the adjustment tank 21, a dilute solution and / or an appropriate amount so that the solid matter concentration of the fluid (mixture of diluted tea leaves and coarsely crushed tea leaves) in the tank is 5 to 10% by weight, preferably 7 to 8% by weight. Add wet tea leaves to adjust the concentration. As described above, the carbonated water introduced into the adjustment tank 21 in advance is fluidized, and the solid matter concentration of the fluid in the adjustment tank 21 is set within a predetermined range, so that the fluid in the adjustment tank 21 is smoothed. It can be sent to the rough crusher 31.

ここで、茶葉路25に近赤外線分光法を利用した非接触式の含水率計(図示せず)を設ければ、調整槽21に導入される湿潤茶葉の含水率を迅速に測定し、濃度調整に必要な希釈液の添加量を速やかに求めて希釈水の添加量を高い精度で制御できる。また、添加剤貯槽22からビタミンC、ポリフェノール類、ソルビン酸等の酸化防止剤や防腐剤を添加剤として添加してもよい。ポリフェノール類の一種であるカテキンは、元来、茶葉に含まれ抗酸化や抗菌等の作用を備える成分であり、添加剤としてカテキンを添加することで、調整槽21に導入される湿潤茶葉(特に成分変動の大きい茶滓)のカテキン含有量を調整して製造される茶ペーストの品質を均質化できることから、添加剤として特に好ましい。   Here, if a non-contact type moisture content meter (not shown) using near-infrared spectroscopy is provided in the tea leaf path 25, the moisture content of the wet tea leaf introduced into the adjustment tank 21 is quickly measured, and the concentration It is possible to quickly determine the addition amount of the diluent necessary for the adjustment and control the addition amount of the dilution water with high accuracy. Moreover, you may add antioxidants and preservatives, such as vitamin C, polyphenols, and sorbic acid, from the additive storage tank 22 as an additive. Catechin, which is a kind of polyphenols, is a component that is originally contained in tea leaves and has antioxidation and antibacterial effects, and wet tea leaves introduced into the adjustment tank 21 by adding catechins as additives (particularly, Since the quality of the tea paste produced by adjusting the catechin content of tea bowl) having a large component variation can be homogenized, it is particularly preferable as an additive.

本実施態様では、希釈液として抗酸化水である炭酸水を用い、あらかじめ炭酸を溶解させた炭酸水を調整槽21に導入しているが、調整槽21にマイクロバブル発生手段(図示せず)を備え付け、微細化した炭酸ガスを調整槽21内に送り込み、水道水等の希釈液に溶解させてもよい。破砕茶葉は希釈液に比して粘性が高く、マイクロバブルの保持効果が高いため、調整槽21内の流体物に循環された破砕茶葉が含まれる状態でマイクロバブルを吹き込むことが好ましい。抗酸化性ガスの吹き込み量は、希釈液に対して1〜10容量%程度とすることが好ましい。   In this embodiment, carbonated water that is antioxidant water is used as the diluent, and carbonated water in which carbonic acid is dissolved in advance is introduced into the adjustment tank 21. Microbubble generating means (not shown) is added to the adjustment tank 21. The refined carbon dioxide gas may be fed into the adjustment tank 21 and dissolved in a diluent such as tap water. Since the crushed tea leaves are higher in viscosity than the diluted liquid and have a high microbubble retention effect, it is preferable to blow the microbubbles in a state where the crushed tea leaves are contained in the fluid in the adjustment tank 21. The blowing amount of the antioxidant gas is preferably about 1 to 10% by volume with respect to the diluent.

調整槽21では、上述した濃度調整工程が行なわれ、必要に応じて添加剤の添加や抗酸化性ガスの吹込みにより、湿潤茶葉の成分調整や品質保持処理が併せて行なわれる。次いで、調整槽21から送出された希釈液と湿潤茶葉との混合物(希釈茶葉)が第1接続管35を介して粗破砕機31に導入され粗破砕工程で粗破砕される。具体的には、粗破砕機31は破砕羽根32を有することから、粗破砕機31の筐体30内部に導入された希釈茶葉は筐体30内部を移動することにより破砕羽根32で破砕される。なお、破砕羽根32の後方にスリット付きの板34が設けられており、希釈茶葉はこの板34に堰き止められる形で破砕される。こうして粗破砕された茶滓(粗破砕茶葉)は、移送羽根33により粗破砕機31から送り出し、循環路36を介して調整槽21に循環させる。   In the adjustment tank 21, the above-described concentration adjustment step is performed, and as necessary, the adjustment of the wet tea leaf components and the quality maintenance process are performed by adding an additive or blowing an antioxidant gas. Next, the mixture (diluted tea leaves) of the diluted liquid and wet tea leaves sent out from the adjustment tank 21 is introduced into the rough crusher 31 through the first connection pipe 35 and is roughly crushed in the rough crushing step. Specifically, since the rough crusher 31 has crushing blades 32, diluted tea leaves introduced into the case 30 of the rough crusher 31 are crushed by the crushing blades 32 by moving inside the case 30. . In addition, the board 34 with a slit is provided behind the crushing blade | wing 32, and a diluted tea leaf is crushed in the form dammed by this board 34. The roughly crushed tea cake (coarse crushed tea leaves) is sent out from the coarse crusher 31 by the transfer blade 33 and circulated to the adjustment tank 21 through the circulation path 36.

本実施態様では調整槽21には、粗破砕及び循環工程を経て循環された粗破砕茶葉と茶葉路25から導入される未処理の湿潤茶葉(茶滓)とが導入され、循環処理がされることにより、固形物濃度が次第に増加するとともに、固形物の粒径が次第に小さくなる。調整槽21をバッチ式で用いる場合は、調整槽21内の流体物量が所定値になった時点で茶滓の導入を停止し、流体物量の固形物濃度が上記範囲内となるように希釈液の導入量を停止又は継続しながら、粗破砕工程及び循環工程を継続し、調整槽21内の流体物の粒径が概ね均質化した時点で、循環路36の途中に接続した第2接続管45から、調整槽21内の流体物を微破砕機41に送る。   In this embodiment, roughly crushed tea leaves that have been circulated through the coarse crushing and circulation process and untreated wet tea leaves (tea bowls) introduced from the tea leaf path 25 are introduced into the adjustment tank 21 and subjected to a circulation treatment. As a result, the solid concentration gradually increases, and the particle size of the solid gradually decreases. When the adjustment tank 21 is used in a batch system, the introduction of the teacup is stopped when the amount of the fluid in the adjustment tank 21 reaches a predetermined value, and the diluent is adjusted so that the solid substance concentration of the fluid quantity is within the above range. The second connecting pipe connected in the middle of the circulation path 36 when the coarse crushing process and the circulation process are continued while the introduction amount of the fluid is stopped or continued, and the particle size of the fluid in the adjustment tank 21 is substantially homogenized. From 45, the fluid in the adjustment tank 21 is sent to the fine crusher 41.

微破砕機41には、破砕羽根42の後方にスリット付きの板44が設けられており、粗破砕茶葉はこの板44に堰き止められる形でさらに細かく破砕される。板44のスリットの大きさは、500〜2000μm程度が好ましく、微破砕機41内部での繊維等の詰まりを防止するため、微破砕機41への粗破砕茶葉の導入速度は、粗破砕機31への希釈茶葉の導入速度に比して小さくする。   The fine crusher 41 is provided with a plate 44 with slits behind the crushing blade 42, and the coarsely crushed tea leaves are further finely crushed in a form that is dammed up by this plate 44. The size of the slit of the plate 44 is preferably about 500 to 2000 μm. In order to prevent clogging of fibers and the like inside the fine crusher 41, the introduction speed of the coarsely crushed tea leaves into the fine crusher 41 is set at the rough crusher 31. Reduce compared to the rate of introduction of diluted tea leaves.

微破砕機41では、粗破砕茶葉がさらに細かく破砕され、平均粒径が500μm以下となった微破砕茶葉が得られる。本実施態様では、微破砕茶葉は回転砥石を備える湿式ミルのような磨砕機51で磨際され、平均粒径が50〜100μmの茶滓ペーストが得られる。摩砕機51によるペースト化処理では、摩擦熱により微破砕茶葉が加熱され、温度が20〜40℃程度上昇する。そこで、本発明ではこの茶滓ペーストを滅菌機61に送り、滅菌機で60〜95℃、好ましくは85〜90℃で30分以上、又は140℃で2分間、加熱滅菌する滅菌工程を行なう。滅菌された茶滓ペースト滅菌機61の後段に設けられた充填機71を用い、滅菌された包装容器に充填する。このように、茶滓ペーストを滅菌し、さらに包装容器に充填することで、長期間保存でき、茶滓ペーストの搬送及び保管を容易とする。   In the fine crusher 41, the coarsely crushed tea leaves are further finely crushed to obtain finely crushed tea leaves having an average particle size of 500 μm or less. In this embodiment, the finely crushed tea leaves are ground by a grinder 51 such as a wet mill equipped with a rotating grindstone to obtain a teacup paste having an average particle size of 50 to 100 μm. In the pasting process by the grinder 51, the finely crushed tea leaves are heated by frictional heat, and the temperature rises by about 20 to 40 ° C. Therefore, in the present invention, the tea paste is sent to the sterilizer 61, and a sterilization step is performed in which the sterilization is performed by heat sterilization at 60 to 95 ° C, preferably 85 to 90 ° C for 30 minutes or more, or 140 ° C for 2 minutes. A sterilized packaging container is filled using a filling machine 71 provided at the subsequent stage of the sterilized teacup paste sterilizer 61. Thus, by sterilizing the teacup paste and further filling the packaging container, it can be stored for a long period of time, and the teacup paste can be easily transported and stored.

なお製造装置11内には、粗破砕茶葉を貯留する粗破砕茶葉貯槽、微破砕茶葉を貯留する微破砕茶葉貯槽、茶滓ペーストを貯留するペースト貯槽等(いずれも図示せず)を設けてもよい。この場合、粗破砕茶葉貯槽は第2接続管45と接続し、微破砕茶葉貯槽は第3接続管55、ペースト貯層は第4接続管65とそれぞれ接続する。このような貯槽を設けることにより、様々な粒径に破砕されたスラリ又はペースト状物を取り出すことができる。なお各貯槽には、内部に抗酸化性ガスを充填することで、各貯槽の貯留物の品質劣化を防止することが好ましい。   The manufacturing apparatus 11 may include a roughly crushed tea leaf storage tank for storing roughly crushed tea leaves, a finely crushed tea leaf storage tank for storing finely crushed tea leaves, a paste storage tank for storing teacup paste, and the like (none of which are shown). Good. In this case, the roughly crushed tea leaf storage tank is connected to the second connection pipe 45, the finely crushed tea leaf storage tank is connected to the third connection pipe 55, and the paste reservoir is connected to the fourth connection pipe 65. By providing such a storage tank, slurry or paste-like material crushed into various particle sizes can be taken out. In addition, it is preferable to prevent the quality deterioration of the storage of each storage tank by filling each storage tank with an antioxidant gas.

[実施例]
実施例として、図1に示す製造装置11を用いた実験を行なった。調整槽21は容量250Lとし、粗破砕機31としてカッタポンプ(コマツゼノア株式会社製)、微破砕機41としてインラインミル(特殊機化工業株式会社製)、磨砕機51として砥石を有する超微粒磨砕機(商品名「スーパーマスコロイダー」、増幸産業株式会社製)、滅菌機61として加熱滅菌機、充填機71としてバッグインボックス(B.I.B)式無菌充填機を用いた。
[Example]
As an example, an experiment using the manufacturing apparatus 11 shown in FIG. 1 was performed. The adjustment tank 21 has a capacity of 250 L, a cutter pump (manufactured by Komatsu Zenoah Co., Ltd.) as the coarse crusher 31, an in-line mill (manufactured by Koki Kogyo Co., Ltd.) as the fine crusher 41, and an ultrafine grinder having a grindstone as the grinder 51. (Trade name “Supermass colloider” manufactured by Masuko Sangyo Co., Ltd.), a heat sterilizer as the sterilizer 61, and a bag-in-box (BIB) type aseptic filler as the filling machine 71 were used.

調整槽21にはあらかじめ、希釈液として炭酸水(炭酸濃度0.01容積%、pH4)100Lを入れ、粗破砕機31を稼動させて希釈液を流動させた状態で、茶葉として煎茶を原料とする緑茶飲料の製造過程で発生した茶滓(含水率80重量%)100Lを5〜10分かけて導入した。調整槽21には希釈液路26から炭酸水を適宜、追加添加しながら調整槽21内の流体物を供給速度50L/分で粗破砕機31に送り、粗破砕機31で粗破砕して調整槽21に循環させた。茶滓及び希釈液の調整槽21への供給は、茶滓導入量100kg、希釈液導入量120Lとなった時点で停止し、さらに20分間の粗破砕及び循環処理を行なった。上記処理により固形物濃度9重量%、平均粒径2000μmの粗破砕茶葉が得られた。   The adjustment tank 21 is charged with 100 L of carbonated water (carbonic acid concentration 0.01 vol%, pH 4) as a diluent in advance, and the crude crusher 31 is operated to flow the diluent. 100 L of tea bowl (moisture content of 80% by weight) generated in the manufacturing process of green tea beverage was introduced over 5 to 10 minutes. While adjusting the addition of carbonated water from the dilution liquid passage 26 to the adjustment tank 21 as appropriate, the fluid in the adjustment tank 21 is sent to the rough crusher 31 at a supply rate of 50 L / min, and is roughly crushed by the rough crusher 31 It was circulated in the tank 21. The supply of the teacup and diluent to the adjustment tank 21 was stopped when the teacup introduction amount reached 100 kg and the dilution solution introduction amount 120 L, and further coarse crushing and circulation treatment for 20 minutes were performed. By the above treatment, roughly crushed tea leaves having a solid concentration of 9% by weight and an average particle size of 2000 μm were obtained.

次に、粗破砕茶葉を調整槽21から粗破砕機31に送り、さらに供給速度5L/分で微破砕機41を通過させ、平均粒径500μmの微破砕茶葉とした。これを磨砕機51に供給速度2L/分で供給し、平均粒径50μm、温度45℃の茶滓ペーストを得た。得られた茶滓ペーストは、滅菌機61で85℃、30分間加熱し、定量サニタリーポンプを介して無菌条件下、計量充填機71によりビニール製の包装容器に充填した。   Next, the coarsely crushed tea leaves were sent from the adjustment tank 21 to the coarsely pulverized machine 31 and further passed through the finely pulverized machine 41 at a supply rate of 5 L / min to obtain finely crushed tea leaves having an average particle diameter of 500 μm. This was supplied to the grinder 51 at a supply rate of 2 L / min to obtain a tea paste having an average particle size of 50 μm and a temperature of 45 ° C. The obtained teacup paste was heated at 85 ° C. for 30 minutes with a sterilizer 61, and filled into a vinyl packaging container with a metering filler 71 under aseptic conditions via a quantitative sanitary pump.

本発明は、食品添加物等として利用できる茶ペーストの製造に用いることができ、特に茶滓をペースト状にするために利用できる。   INDUSTRIAL APPLICABILITY The present invention can be used for producing a tea paste that can be used as a food additive or the like, and in particular, can be used to make a tea cake into a paste.

本発明を実施するために用いられる茶ペースト製造装置の模式図である。It is a schematic diagram of the tea paste manufacturing apparatus used in order to implement this invention.

符号の説明Explanation of symbols

11 茶ペースト製造装置
21 調整槽
23 攪拌機
31 粗破砕機
41 微破砕機
51 磨砕機
61 滅菌機
71 充填機
DESCRIPTION OF SYMBOLS 11 Tea paste production apparatus 21 Adjustment tank 23 Stirrer 31 Coarse crusher 41 Fine crusher 51 Grinding machine 61 Sterilizer 71 Filling machine

Claims (10)

茶葉を液体に浸漬させて得られた湿潤茶葉を、攪拌機を備えた調整槽に導入して希釈液と混合し固形物濃度を調整して希釈茶葉を得る濃度調整工程と、
前記濃度調整工程で得られた希釈茶葉を前記調整槽から送り出し粗破砕機を通過させて粗破砕する粗破砕工程と、
前記粗破砕工程の粗破砕機を通過した粗破砕茶葉を前記濃度調整工程の調整槽に循環させる循環工程と、を含む茶ペーストの製造方法。
A concentration adjusting step for obtaining a diluted tea leaf by introducing a wet tea leaf obtained by immersing the tea leaf in a liquid into a regulating tank equipped with a stirrer and mixing with a diluent to adjust a solid concentration,
A coarse crushing step of sending the diluted tea leaves obtained in the concentration adjustment step from the adjustment tank and roughly crushing them through a coarse crusher,
A circulation step of circulating the coarsely crushed tea leaves that have passed through the coarse crusher in the coarse crushing step to the adjustment tank in the concentration adjusting step.
前記濃度調整工程において、あらかじめ希釈液を前記調整槽に導入して流動化させた状態で前記湿潤茶葉を導入する請求項1に記載の茶ペーストの製造方法。   2. The method for producing a tea paste according to claim 1, wherein in the concentration adjustment step, the wet tea leaves are introduced in a state in which a diluent is introduced into the adjustment tank and fluidized in advance. 前記濃度調整工程において、前記湿潤茶葉の含水率を測定し前記希釈液の量を制御する請求項1又は2に記載の茶ペーストの製造方法。   The method for producing a tea paste according to claim 1 or 2, wherein, in the concentration adjustment step, the moisture content of the wet tea leaves is measured to control the amount of the diluted solution. 近赤外分光法による非接触式含水率計を用いて前記湿潤茶葉の含水率を測定する請求項3に記載の茶ペーストの製造方法。   The method for producing a tea paste according to claim 3, wherein the moisture content of the wet tea leaf is measured using a non-contact moisture meter according to near infrared spectroscopy. 前記濃度調整工程において前記湿潤茶葉に添加剤を添加する請求項1から4のいずれかに記載の茶ペーストの製造方法。   The method for producing a tea paste according to any one of claims 1 to 4, wherein an additive is added to the wet tea leaves in the concentration adjusting step. 前記濃度調整工程において、前記調整槽にマイクロバブル発生手段を設け抗酸化性ガスを吹き込む請求項1から5のいずれかに記載の茶ペーストの製造方法。   The method for producing a tea paste according to any one of claims 1 to 5, wherein in the concentration adjusting step, microbubble generating means is provided in the adjusting tank and an antioxidant gas is blown. 前記循環工程から前記濃度調整工程の調整槽に循環され平均粒径1000〜5000μmの固形物を含む前記粗破砕茶葉を、前記調整槽から排出して微破砕してペースト状の茶ペーストを得るペースト化工程をさらに含む請求項1から6のいずれかに記載の茶ペーストの製造方法。   Paste which is circulated from the circulation step to the adjustment tank of the concentration adjustment step and which contains the coarsely crushed tea leaves containing solids having an average particle size of 1000 to 5000 μm is discharged from the adjustment tank and finely crushed to obtain a paste-like tea paste The manufacturing method of the tea paste in any one of Claim 1 to 6 which further includes a conversion process. 前記ペースト化工程で得られた茶ペーストを滅菌する滅菌工程をさらに含む請求項7に記載の茶ペーストの製造方法。   The method for producing a tea paste according to claim 7, further comprising a sterilization step of sterilizing the tea paste obtained in the pasting step. 前記滅菌工程で滅菌された茶ペーストを無菌状態で包装容器に充填する充填工程をさらに含む請求項8に記載の茶ペーストの製造方法。   The method for producing a tea paste according to claim 8, further comprising a filling step of filling the packaging container in a sterile state with the tea paste sterilized in the sterilization step. 前記湿潤茶葉は茶滓である請求項1から9のいずれかに記載の茶ペーストの製造方法。   The method for producing a tea paste according to any one of claims 1 to 9, wherein the wet tea leaves are teacups.
JP2004368287A 2004-12-20 2004-12-20 Method for producing tea paste Pending JP2006174711A (en)

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Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2008056434A1 (en) * 2006-11-07 2008-05-15 Kao Corporation Method for production of beverage
JP2011217641A (en) * 2010-04-07 2011-11-04 Nepuree Corp Method of processing tea leaves and tea-leaf processed product obtained by the same
JPWO2010041651A1 (en) * 2008-10-10 2012-03-08 住友ベークライト株式会社 Semiconductor device
CN114104352A (en) * 2021-12-15 2022-03-01 安徽省绿发生态农业有限公司 System is recycled to supporting tea milli of using of tea processing

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2008056434A1 (en) * 2006-11-07 2008-05-15 Kao Corporation Method for production of beverage
JP2008113621A (en) * 2006-11-07 2008-05-22 Kao Corp Method for producing beverage
JPWO2010041651A1 (en) * 2008-10-10 2012-03-08 住友ベークライト株式会社 Semiconductor device
JP5532258B2 (en) * 2008-10-10 2014-06-25 住友ベークライト株式会社 Semiconductor device
JP2011217641A (en) * 2010-04-07 2011-11-04 Nepuree Corp Method of processing tea leaves and tea-leaf processed product obtained by the same
CN114104352A (en) * 2021-12-15 2022-03-01 安徽省绿发生态农业有限公司 System is recycled to supporting tea milli of using of tea processing

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