JPH07115906A - Extraction of drink and apparatus therefor - Google Patents

Extraction of drink and apparatus therefor

Info

Publication number
JPH07115906A
JPH07115906A JP27196493A JP27196493A JPH07115906A JP H07115906 A JPH07115906 A JP H07115906A JP 27196493 A JP27196493 A JP 27196493A JP 27196493 A JP27196493 A JP 27196493A JP H07115906 A JPH07115906 A JP H07115906A
Authority
JP
Japan
Prior art keywords
extraction
tank
concentration
liquid
flow rate
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
JP27196493A
Other languages
Japanese (ja)
Other versions
JP3377570B2 (en
Inventor
Shogo Yamaguchi
昇吾 山口
Yasushi Ito
靖史 伊藤
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.)
Mitsubishi Heavy Industries Ltd
Original Assignee
Mitsubishi Heavy Industries 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 Mitsubishi Heavy Industries Ltd filed Critical Mitsubishi Heavy Industries Ltd
Priority to JP27196493A priority Critical patent/JP3377570B2/en
Publication of JPH07115906A publication Critical patent/JPH07115906A/en
Application granted granted Critical
Publication of JP3377570B2 publication Critical patent/JP3377570B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Abstract

PURPOSE:To provide a drink extraction method capable of adjusting the average concentration of the total extracted liquid to a target concentration, decreasing the risk of the production of defective product and enabling the back-up of the defective product to another extraction tank and the processing to an acceptable product. CONSTITUTION:An extraction step to add water to an extraction raw material filled in an extraction tank and extract the extracted liquid containing an extract of an extracting raw material is finished in an extraction tank among plural extraction tanks 31. The extracted liquid is discharged, the weight and concentration of the extracted liquid are determined and transmitted to a controller 60, the concentration of the extracted liquid in the extraction tank 31 is compared with a preset target concentration value, the temperature and flow rate of water to be supplied to the extracting tank of the next extraction step and an extraction period are calculated and the calculation results are fed-back to the next extraction tank 31 to bring the concentration closer to the target concentration. Similar control is continued thereafter to adjust the average concentration of the total extracted liquid to the target concentration.

Description

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

【0001】[0001]

【産業上の利用分野】本発明は、抽出タンクに入れた抽
出原料に供給水を加えて抽出原料のエキスを含む抽出液
を抽出する飲料抽出方法及び装置に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a beverage extraction method and apparatus for extracting an extraction liquid containing an extract of an extraction raw material by adding feed water to the extraction raw material placed in an extraction tank.

【0002】[0002]

【従来の技術】従来の飲料抽出装置は、1個の大型タン
クに抽出原料を入れ、これに熱水を加え、一定時間保持
して、抽出原料のエキスを含む抽出液を抽出し、次いで
抽出液(飲料液)を排出し、その後、原料滓を洗浄水と
ともに流し出すようにしている。この従来例(必要なら
ば特公昭59−6684公報を参照されたい)を図4に
より説明する。
2. Description of the Related Art A conventional beverage extraction apparatus puts an extraction raw material in one large tank, adds hot water to it, holds it for a certain period of time, extracts an extraction liquid containing the extract of the extraction raw material, and then extracts it. The liquid (beverage liquid) is discharged, and then the raw material slag is poured out together with the washing water. This conventional example (refer to Japanese Patent Publication No. 59-6684 if necessary) will be described with reference to FIG.

【0003】6が抽出タンクで、抽出タンク6の天板
に、上面にコーヒー粉砕豆開閉バルブ1′付き供給ダク
ト1と、フィルター洗浄用スプレーノズル2と、タンク
洗浄用スプレーボール3及び抽出用スプレーノズル4と
を設け、抽出タンク6の下面開口部にフィルター5を設
け、これらフィルター洗浄用スプレーノズル2と、タン
ク洗浄用スプレーボール3と、抽出用スプレーノズル4
とに、開閉バルブ8、8′を介して温水供給管7を連結
している。
Reference numeral 6 designates an extraction tank, a top plate of the extraction tank 6, a supply duct 1 having a coffee ground bean opening / closing valve 1'on its upper surface, a filter cleaning spray nozzle 2, a tank cleaning spray ball 3 and an extraction spray. A nozzle 4 is provided, a filter 5 is provided at the lower opening of the extraction tank 6, a spray nozzle 2 for cleaning the filter, a spray ball 3 for cleaning the tank, and a spray nozzle 4 for the extraction.
A hot water supply pipe 7 is connected to and via open / close valves 8 and 8 '.

【0004】また抽出タンク6の下面開口部にコーヒー
豆粕排出管9を連結し、同コーヒー豆粕排出管9の先端
部に開閉バルブ10を介してコーヒー豆粕案内管11を
連結し、コーヒー豆粕排出管9の中間部にコーヒー抽出
液取出管12及びサンプル取出管13を連結し、コーヒ
ー抽出液取出管12の中途に所定の間隔をおいて一対の
開閉バルブ14、14′を介装し、開閉バルブ14、1
4′の間のコーヒー抽出液取出管12に蒸気供給管15
を連結し、蒸気供給管15の中途に操作バルブ16を設
け、操作バルブ16の両側に開閉バルブ17、17′を
設け、抽出タンク6の天板及び操作バルブ16に開閉バ
ルブ19を介して圧縮空気供給管18を連結している。
A coffee bean meal discharge pipe 9 is connected to the lower opening of the extraction tank 6, and a coffee bean meal guide pipe 11 is connected to the tip of the coffee bean meal discharge pipe 9 through an opening / closing valve 10 to make a coffee bean meal discharge pipe. A coffee extract liquid take-out pipe 12 and a sample take-out pipe 13 are connected to an intermediate portion of 9, and a pair of open / close valves 14 and 14 'are provided at predetermined intervals in the middle of the coffee extract liquid take-out pipe 12 to provide an open / close valve. 14, 1
The steam supply pipe 15 is connected to the coffee extract liquid extraction pipe 12 between 4 '.
The operation valve 16 is provided in the middle of the steam supply pipe 15, the opening / closing valves 17 and 17 'are provided on both sides of the operation valve 16, and the top plate of the extraction tank 6 and the operation valve 16 are compressed via the opening / closing valve 19. The air supply pipe 18 is connected.

【0005】また上記フィルター5の下側に手動ハンド
ル20により上下動するシャフト21を配装し、シャフ
ト21を上昇させることにより、フィルター5を抽出タ
ンク6の底部から浮き上がらせて、抽出タンク6の下面
開口部を解放状態にし、シヤフト21を下降させること
により、フィルター5を抽出タンク6の下面開口部に嵌
着させて、コーヒーの粉砕豆の流出阻止作用と濾過作用
とを行わせるようになっている。
A shaft 21 that moves up and down by a manual handle 20 is provided below the filter 5, and the shaft 21 is lifted to lift the filter 5 from the bottom of the extraction tank 6 and By opening the lower surface opening and lowering the shaft 21, the filter 5 is fitted into the lower surface opening of the extraction tank 6 so that the ground coffee beans are prevented from flowing out and the coffee is filtered. ing.

【0006】上記飲料抽出装置では、先ず開閉バルブ
1′を開いて、コーヒー粉砕豆を抽出タンク6内へ所定
量だけ収納し、次いで開閉バルブ17、17′、14′
を開き且つ操作バルブ16を切換えて、蒸気をコーヒー
抽出液取出管12、コーヒー豆粕排出管9及びフィルタ
ー5を介して抽出タンク6内へ導入し、抽出タンク6内
に収納したコーヒー粉砕豆を蒸して、予熱膨張させ、次
いで開閉バルブ8′を開いて、抽出用スプレーノズル4
から温水を予熱膨張したコーヒー粉砕豆の上面へ霧状に
満遍なく噴出させるとともに自然流下させる。
In the above beverage brewing apparatus, the opening / closing valve 1'is first opened to store a predetermined amount of ground coffee beans in the brewing tank 6, and then the opening / closing valves 17, 17 ', 14'.
Open and open the operation valve 16 to introduce steam into the extraction tank 6 through the coffee extract extraction pipe 12, the coffee bean lees discharge pipe 9 and the filter 5, and steam the ground coffee beans stored in the extraction tank 6. Preheat expansion, and then open / close valve 8'to open extraction spray nozzle 4
The hot water is sprayed evenly in the form of mist onto the upper surface of the ground coffee beans that have been preheated and allowed to flow naturally.

【0007】このときに得られるコーヒーをフィルター
5を介して抽出するとともに、この抽出液をコーヒー豆
粕排出管9と予め開いている開閉バルブ14、14′を
介してコーヒー抽出液取出管12から取り出す。そして
コーヒーの抽出作業を完了したら、手動ハンドル20を
回して、フィルター5を抽出タンク6の底部から浮き上
がらせ、次いで抽出タンク6にコーヒー豆の重量と同量
の水を投入するとともに開閉バルブ19を開き、圧縮空
気を抽出タンク6へ導入して加圧し、開閉バルブ10を
開いて、コーヒー豆粕排出管9及び案内管11を経て外
部へ一挙に廃棄し、さらに開閉バルブ8を開き、フィル
ター洗浄用スプレーノズル2及びタンク洗浄用スプレー
ボール3によりフィルター5及びタンク6等を洗浄し
て、一連のコーヒー抽出を完了する。
The coffee obtained at this time is extracted through the filter 5, and the extracted liquid is taken out through the coffee extracted liquid extraction pipe 12 through the coffee bean lees discharge pipe 9 and the opening / closing valves 14 and 14 'which are opened in advance. . When the coffee brewing operation is completed, the manual handle 20 is turned to lift the filter 5 from the bottom of the brewing tank 6, and then the brewing tank 6 is filled with water in an amount equal to the weight of the coffee beans and the open / close valve 19 is opened. Open, introduce compressed air into the extraction tank 6 and pressurize it, open the open / close valve 10 and discard it all at once through the coffee bean lees discharge pipe 9 and the guide pipe 11 and then open the open / close valve 8 to wash the filter. The filter 5, the tank 6, and the like are washed by the spray nozzle 2 and the tank cleaning spray ball 3, and a series of coffee extraction is completed.

【0008】[0008]

【発明が解決しようとする課題】前記図4に示す従来の
飲料抽出装置は、大型であり、この飲料抽出装置で一度
に大量の抽出を行うと、抽出原料に対する抽出条件(例
えば供給水温度、抽出時間、供給水量)に振れがあっ
て、目標とする抽出率(エキス濃度)が得られず、その
場合、抽出液濃度の修正が困難で、修正に手間がかか
り、フレーバーが飛んでしまったような場合には、修正
が不可能になる。
The conventional beverage extraction device shown in FIG. 4 is large in size, and when a large amount of extraction is performed at one time with this beverage extraction device, extraction conditions for the extraction raw material (for example, supply water temperature, The target extraction rate (extract concentration) could not be obtained due to fluctuations in the extraction time and the amount of water supplied. In that case, it was difficult to correct the concentration of the extract solution, and it took time to correct it, causing the flavor to fly. In such a case, the correction becomes impossible.

【0009】本発明は前記の問題点に鑑み提案するもの
であり、その目的とする処は、排出した抽出液全量の平
均濃度を目標濃度に調整することができる。また不良品
製造の虞れを少なくできるとともに、不良品を他の抽出
タンクでバックアップできて、容易に良品にすることが
できる飲料抽出方法及び装置を提供しようとする点にあ
る。
The present invention is proposed in view of the above problems, and the object thereof is to adjust the average concentration of the total amount of the extracted liquid to the target concentration. Another object of the present invention is to provide a beverage extraction method and apparatus that can reduce the risk of manufacturing defective products and can back up defective products with another extraction tank to easily make them good products.

【0010】[0010]

【課題を解決するための手段】上記の目的を達成するた
めに、本発明の飲料抽出方法は、抽出タンクに入れた抽
出原料に供給水を加えて抽出原料のエキスを含む抽出液
を抽出する抽出工程を複数の抽出タンクのうち一つの抽
出タンクで終わって、抽出液を排出し、抽出液の重量と
濃度とを計測して、制御装置へ送り、抽出タンクの抽出
液濃度値と予め設定されている目標濃度値とを比較し、
次の抽出工程の抽出タンクの供給水温度と流量、抽出時
間とを演算して、この演算結果を次の抽出タンクへフィ
ードバックして、目標濃度に近づけ、その後も同様の制
御を行って、排出した抽出液全量の平均濃度を目標濃度
に調整することを特徴としている。
In order to achieve the above-mentioned object, the beverage extraction method of the present invention adds feed water to the extraction raw material placed in the extraction tank to extract the extraction liquid containing the extract of the extraction raw material. Finish the extraction process with one of the multiple extraction tanks, discharge the extraction liquid, measure the weight and concentration of the extraction liquid, send it to the controller, and set the extraction liquid concentration value in the extraction tank in advance. Compared with the target concentration value,
Calculate the feed water temperature, flow rate, and extraction time of the extraction tank in the next extraction process, feed back the calculation result to the next extraction tank, bring it closer to the target concentration, and perform similar control thereafter to discharge. The feature is that the average concentration of all the extracted liquids is adjusted to the target concentration.

【0011】前記飲料抽出方法において、抽出タンクの
抽出液濃度値を予め設定された目標濃度値と比較し、抽
出液の重量と濃度とより次の抽出工程の抽出タンクの供
給水温度と流量、抽出時間とを演算するときに、同供給
水温度と流量、抽出時間を予め設定された範囲内で行う
ようにしてもよい。前記飲料抽出方法において、供給水
温度、流量、抽出時間の3条件のうち2つの条件を先ず
固定し、残りの1条件を予め設定された範囲で変化さ
せ、それでも対応できないときには、上記2条件のうち
の1条件を変化させるようにしてもよい。
In the beverage extraction method, the concentration value of the extraction liquid in the extraction tank is compared with a preset target concentration value, and the weight and the concentration of the extraction liquid are used to determine the temperature and flow rate of the water supplied to the extraction tank in the next extraction step. When calculating the extraction time, the supply water temperature, the flow rate, and the extraction time may be set within a preset range. In the beverage extraction method, two conditions out of three conditions of the supply water temperature, the flow rate, and the extraction time are first fixed, and the remaining one condition is changed within a preset range. One of the conditions may be changed.

【0012】また本発明の飲料抽出装置は、共通の供給
水、洗浄水、抽出原料等の供給配管の分岐配管の下流側
に設けられた複数の抽出タンクと、同各抽出タンクで抽
出された抽出液を集めて送り出す共通の抽出液排出手段
とを有し、一つの抽出タンクで抽出工程が終わった後、
次の抽出タンクの抽出工程に順次移行する飲料抽出装置
において、前記各抽出タンク毎の供給水配管に設けられ
た供給水の流量制御手段及び温度制御手段と、同各抽出
タンク毎の抽出液出口部に設けられた抽出液重量検出手
段及び液濃度検出手段と、抽出工程にある任意の抽出タ
ンクの抽出液濃度値と予め設定されている目標濃度値と
を比較し次の抽出工程の抽出タンクの供給水温度と流
量、抽出時間とを演算してこの演算結果を次の抽出工程
の抽出タンクへ送って、排出した抽出液全量の平均濃度
を目標濃度に調整する制御装置とを具えている。
Further, the beverage extraction apparatus of the present invention is provided with a plurality of extraction tanks provided on the downstream side of the branch pipes of the common supply water, washing water, and the supply pipes for the extraction raw material, and the extraction tanks. Having a common extract discharge means for collecting and sending the extract, after the extraction process is completed in one extract tank,
In the beverage extraction device that sequentially shifts to the extraction process of the next extraction tank, the flow rate control means and temperature control means of the supply water provided in the supply water pipe for each extraction tank, and the extraction liquid outlet for each extraction tank Extraction liquid weight detection means and liquid concentration detection means provided in the section, and compares the extraction liquid concentration value of an arbitrary extraction tank in the extraction step with a preset target concentration value, and the extraction tank of the next extraction step The control device adjusts the supply water temperature, the flow rate, and the extraction time, sends the calculation result to the extraction tank in the next extraction step, and adjusts the average concentration of the discharged total amount of the extraction liquid to the target concentration. .

【0013】前記飲料抽出装置において、各抽出タンク
供給配管に流量制御手段として設けられた供給水の流量
調節計と流量調整弁と、供給水配管に供給水の温度制御
手段として設けられた熱交換機と同熱交換機出口の供給
水配管に取付けられた温度調節計と同温度調節計により
コントロールされる熱交換機の熱水配管に設けられた流
量調整弁と、各抽出タンク毎の抽出液出口部に抽出液重
量検出手段として設けられたロードセルを有するバッフ
ァタンクと、前記バッファタンクに液濃度検出手段とし
て設けられた液比重計、吸光濃度計、電気抵抗濃度計等
の濃度計と、抽出工程にある任意の抽出タンクの抽出液
濃度値を予め設定された目標濃度値と比較して抽出液の
重量と濃度より次の抽出工程の抽出タンクの供給水温度
と流量、抽出時間とを演算して供給水の流量調節計と熱
交換機出口の供給水配管に取付けられた温度調節計とに
指令を発して排出した抽出液全量の平均濃度を目標濃度
に調整する制御装置とを具えるようにしてもよい。
In the beverage brewing apparatus, a feed water flow rate controller and a flow rate adjusting valve provided as flow rate control means in each brewing tank supply pipe, and a heat exchanger provided in the supply water pipe as temperature control means of the feed water. And a temperature controller attached to the supply water pipe at the outlet of the heat exchanger, a flow rate adjustment valve provided in the hot water pipe of the heat exchanger controlled by the temperature controller, and an extraction liquid outlet for each extraction tank. In the extraction step, there is a buffer tank having a load cell provided as the extraction liquid weight detection means, a concentration meter such as a liquid densitometer, an absorption concentration meter, and an electrical resistance concentration meter provided in the buffer tank as the liquid concentration detection means. Compare the concentration value of the extraction liquid in any extraction tank with a preset target concentration value, and based on the weight and concentration of the extraction liquid, supply water temperature and flow rate of the extraction tank in the next extraction process, extraction time And a controller for adjusting the average concentration of the total amount of the extracted liquid discharged by issuing a command to the flow controller of the supply water and the temperature controller attached to the supply water pipe at the outlet of the heat exchanger. You may make it available.

【0014】[0014]

【作用】本発明の飲料抽出方法及び装置は前記のように
構成されており、抽出タンクに入れた抽出原料に供給水
を加えて抽出原料のエキスを含む抽出液を抽出する抽出
工程を複数の抽出タンクのうち一つの抽出タンクで終わ
って、抽出液を排出し、抽出液の重量と濃度とを計測し
て、制御装置へ送り、抽出タンクの抽出液濃度値と予め
設定されている目標濃度値とを比較し、次の抽出工程の
抽出タンクの供給水温度と流量、抽出時間とを演算し
て、この演算結果を次の抽出タンクへフィードバックし
て、目標濃度に近づけ、その後も同様の制御を行って、
排出した抽出液全量の平均濃度を目標濃度に調整する。
The beverage extraction method and apparatus of the present invention are configured as described above, and are provided with a plurality of extraction steps for adding the feed water to the extraction raw material placed in the extraction tank to extract the extraction liquid containing the extract of the extraction raw material. After ending with one of the extraction tanks, discharge the extraction liquid, measure the weight and concentration of the extraction liquid, send it to the control device, extract liquid concentration value of the extraction tank and the preset target concentration The value is compared, the supply water temperature and flow rate of the extraction tank in the next extraction process, the extraction time are calculated, and the calculation result is fed back to the next extraction tank to bring it closer to the target concentration, and thereafter the same. Control
Adjust the average concentration of all discharged extract to the target concentration.

【0015】[0015]

【実施例】次に本発明の飲料抽出方法の実施に使用する
飲料抽出装置の一実施例を図1〜図3により説明する。
図1は同飲料抽出装置を示すブロック図、図2は同飲料
抽出装置の抽出タンク及び周辺機器を示す側面図、図3
は図2の抽出タンクの洗浄時の状態を示す説明図であ
る。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS Next, one embodiment of a beverage extracting device used for carrying out the beverage extracting method of the present invention will be described with reference to FIGS.
1 is a block diagram showing the beverage extraction device, FIG. 2 is a side view showing an extraction tank and peripheral devices of the beverage extraction device, FIG.
FIG. 4 is an explanatory diagram showing a state of the extraction tank of FIG. 2 during cleaning.

【0016】図1、図2において、50は共通の純水供
給配管、54は洗浄水配管、56は抽出原料等の供給配
管、53は純水を加熱する熱交換機用の熱源となる熱水
配管である。各配管から分岐された配管の下流に抽出タ
ンク31を主体とすn個の抽出タンク装置30が連結さ
れている。n個の抽出タンク装置30において、抽出さ
れた飲料は、共通の抽出液受け樋51に集められ、送出
配管52、ポンプ45を経て貯蔵タンク(図示せず)へ
送り出される。各抽出タンク装置30は、制御装置60
により制御され、一つの抽出タンク装置30の抽出が
終わった後、次の抽出タンク装置30の抽出工程に順
次移行してゆく。
In FIGS. 1 and 2, 50 is a common pure water supply pipe, 54 is a wash water pipe, 56 is a supply pipe for extraction raw materials and the like, and 53 is hot water which is a heat source for a heat exchanger for heating pure water. It is piping. The n extraction tank devices 30 mainly including the extraction tank 31 are connected downstream of the pipes branched from the respective pipes. In the n number of extraction tank devices 30, the extracted beverages are collected in a common extraction liquid receiving trough 51, and sent out to a storage tank (not shown) via a delivery pipe 52 and a pump 45. Each extraction tank device 30 includes a control device 60.
After the extraction of one extraction tank device 30 is completed, the process is sequentially shifted to the extraction process of the next extraction tank device 30.

【0017】純水の流量制御手段として、各抽出タンク
31に純水を供給する配管50の分岐配管に純水の供給
停止用電磁弁46と流量調節計36と流量調整弁40と
が設けられている。また純水の温度制御手段として、純
水供給配管50の分岐配管に熱交換機38が設けられ、
熱交換機38出口の純水供給配管50に温度調節計37
が取付けられており、温度調節計37が熱水配管53に
取付けられた流量調整弁39をコントロールすることに
より、熱水の流量が調整されて、純水の温度が変わる。
熱水配管53にも、各抽出タンク装置30毎に電磁弁4
7が設けられており、無用のときには、熱水の供給が停
止される。
As a means for controlling the flow rate of pure water, a solenoid valve 46 for stopping the supply of pure water, a flow rate controller 36 and a flow rate adjusting valve 40 are provided in a branch pipe of a pipe 50 for supplying pure water to each extraction tank 31. ing. A heat exchanger 38 is provided in a branch pipe of the pure water supply pipe 50 as a pure water temperature control means.
The temperature controller 37 is connected to the pure water supply pipe 50 at the outlet of the heat exchanger 38.
The temperature controller 37 controls the flow rate adjusting valve 39 attached to the hot water pipe 53 to adjust the flow rate of the hot water and change the temperature of the pure water.
The hot water pipe 53 also has a solenoid valve 4 for each extraction tank device 30.
7 is provided, and the supply of hot water is stopped when it is not needed.

【0018】抽出原料粒等の供給配管56には、各抽出
タンク装置30毎に計量供給機57が設けられ、制御装
置60からの指令により、一定量の抽出原料粒等が決ま
ったタイミングで抽出原料粒等が抽出タンク31へ供給
される。洗浄水配管54にも、各抽出タンク装置30毎
に電磁弁48が設けられ、抽出タンク31内の洗浄水配
管54先端には、ノズル55が取付けられている。抽出
工程が完了し、抽出液が排出された後、制御装置60か
らの指令により、図3に示すように抽出タンク31の底
部59が出口配管、電磁弁41、原料粕排出樋70とと
もに、駆動装置(図示せず)により上方へ押し上げら
れ、電磁弁48が開き、ノズル55から洗浄水が吹き出
し、原料粕が洗い出されて、底部59に取付けられてい
るフィルタ58が洗浄される。49は底部59及び配管
に溜まった洗浄水を流し出すために洗浄時だけ開く電磁
弁である。
A metering feeder 57 is provided for each extraction tank device 30 in the supply pipe 56 for the extraction raw material grains and the like, and a fixed amount of the extraction raw material grains or the like is extracted at a predetermined timing according to a command from the control device 60. Raw material grains and the like are supplied to the extraction tank 31. An electromagnetic valve 48 is also provided for each extraction tank device 30 in the cleaning water pipe 54, and a nozzle 55 is attached to the tip of the cleaning water pipe 54 in the extraction tank 31. After the extraction process is completed and the extraction liquid is discharged, the bottom 59 of the extraction tank 31 is driven together with the outlet pipe, the solenoid valve 41, and the raw material lees discharge gutter 70 according to a command from the control device 60, as shown in FIG. It is pushed upward by a device (not shown), the electromagnetic valve 48 is opened, washing water is blown out from the nozzle 55, the raw meal is washed out, and the filter 58 attached to the bottom 59 is washed. Reference numeral 49 is a solenoid valve that opens only during cleaning in order to flush the cleaning water accumulated in the bottom 59 and the pipe.

【0019】抽出タンク31内では、抽出タンク31に
入れた抽出原料粒に温められた純水が加えられて、抽出
原料粒のエキスを含む抽出液が抽出された後、制御装置
60からの指令により、電磁弁41が開いて、抽出液が
下部の抽出液重量検出手段であるバッファタンク32へ
流入する。抽出液の流入が完了した後、ロードセル33
がバッファタンク32を含めた全体の重さを計測し、制
御装置60においてバッファタンク32及び付属品の重
量を差引くことにより、抽出液の重量が算定、記録され
る。バッファタンク32は、抽出タンク31の抽出液排
出配管からも、下部の抽出液受け樋51からも、機械的
な結合が絶たれているので、これらの配管との接続によ
る重量計測への影響は全く無い。
In the extraction tank 31, after warmed pure water is added to the extraction raw material grains put in the extraction tank 31 to extract the extraction liquid containing the extract of the extraction raw material grains, a command from the control device 60 is given. As a result, the solenoid valve 41 is opened, and the extract flows into the buffer tank 32, which is the extract weight detecting means below. After the inflow of the extract is completed, the load cell 33
Measures the total weight including the buffer tank 32, and the controller 60 subtracts the weights of the buffer tank 32 and accessories to calculate and record the weight of the extract. The buffer tank 32 is mechanically disconnected from the extraction liquid discharge pipe of the extraction tank 31 and from the extraction liquid receiving trough 51 at the lower part, so that the connection with these pipes does not affect the weight measurement. Not at all.

【0020】バッファタンク32には、液濃度検出手段
としてのバッファタンク32内のセンサ35により、液
の特性を検出する濃度計34(液比重計、または吸光濃
度計、或いは電気抵抗濃度計等)が設けられている。制
御装置60は、各抽出タンク31に投入する純水や洗浄
水、抽出原料の投入のタイミングに応じて電磁弁46、
47、48及び計量供給機57に順番に指令を発すると
もに、前記計測調節計の信号を受けて、抽出工程にある
任意の抽出タンク31から排出される抽出液の濃度値を
予め設定された目標濃度値と比較し、同抽出液の重量と
濃度より次の抽出工程の抽出タンク31の供給水温度と
流量、抽出時間とを演算して、この演算結果を流量調節
計36と温度調節計37に伝え、電磁弁41を開くタイ
ミングを指示して、排出した抽出液全量の平均濃度を目
標濃度に調整する。
In the buffer tank 32, a densitometer 34 (a liquid densitometer, an absorption densitometer, an electric resistance densitometer, or the like) for detecting the characteristics of the liquid by a sensor 35 in the buffer tank 32 as a liquid concentration detecting means. Is provided. The control device 60 controls the solenoid valve 46, depending on the timing of charging the pure water, the cleaning water, and the extraction raw material to be supplied to each extraction tank 31,
47, 48 and the metering and supplying device 57 are sequentially issued, and the concentration value of the extraction liquid discharged from an arbitrary extraction tank 31 in the extraction step is preset in response to the signal from the measurement controller. The temperature and flow rate of the water supplied to the extraction tank 31 in the next extraction step and the extraction time are calculated based on the weight and concentration of the extract, and the calculated results are calculated as the flow rate controller 36 and the temperature controller 37. Then, the timing for opening the solenoid valve 41 is instructed to adjust the average concentration of all the discharged extract to the target concentration.

【0021】次に前記図1〜図3に示す飲料抽出装置の
作用を具体的に説明する。共通の純水、熱水、洗浄水、
抽出原料粒等の供給配管の分岐配管の下流にn個の抽出
タンク装置30が設けられ、一つの抽出タンク装置30
(例えば抽出タンク装置30)の抽出作業が完了した
後、次の抽出タンク装置30(例えば抽出タンク装置
30)の抽出工程が始まるように順次抽出作業を行い、
抽出タンク装置30において抽出された飲料が共通の抽
出液受け樋51に集められて、貯蔵タンクへ送り出され
る。
Next, the operation of the beverage extraction device shown in FIGS. 1 to 3 will be specifically described. Common pure water, hot water, wash water,
N extraction tank devices 30 are provided downstream of the branch pipe of the supply pipe for the extraction raw material particles and the like, and one extraction tank device 30 is provided.
After the extraction work of (for example, the extraction tank device 30) is completed, the extraction work is sequentially performed so that the extraction process of the next extraction tank device 30 (for example, the extraction tank device 30) starts.
The beverages extracted in the extraction tank device 30 are collected in the common extraction liquid receiving trough 51 and sent to the storage tank.

【0022】そして抽出工程の最初には、制御装置60
からの指令により計量供給機57が作動し、抽出原料の
規定量分が抽出タンク31内に堆積する。抽出タンク
31への純水供給は、制御装置60からの指令により
電磁弁46が開くことにより開始される(このとき、抽
出タンク31の底部は、下がって、抽出タンク31下
部は、気密を保持し、排出配管の電磁弁41は、閉じら
れた状態にある)。
At the beginning of the extraction process, the controller 60
In response to a command from the metering device 57, the metering and supplying device 57 operates, and a specified amount of the extraction raw material is accumulated in the extraction tank 31. The pure water supply to the extraction tank 31 is started by opening the electromagnetic valve 46 in response to a command from the control device 60 (at this time, the bottom of the extraction tank 31 is lowered and the lower portion of the extraction tank 31 is kept airtight. However, the solenoid valve 41 of the discharge pipe is in a closed state).

【0023】制御装置60より抽出タンク31への純
水流量の目標濃度値が流量調節計36に伝えられ、流量
調節計36と流量調整弁40とにより、純水流量がコン
トロールされる。また制御装置60は、熱交換機38出
口の純水の温度調節計37に指示して、熱交換機38の
熱水配管53に設けられた流量調整弁39を作動させ、
熱水の流量を調節することにより、純水の温度を規定温
度に近づけるようにコントロールする。純水供給時間
は、抽出タンク31の容量と純水流量とから算出さ
れ、抽出タンク31が満杯となったとき、電磁弁46
が閉じられる。
The target concentration value of the pure water flow rate to the extraction tank 31 is transmitted from the control device 60 to the flow rate controller 36, and the pure water flow rate is controlled by the flow rate controller 36 and the flow rate adjusting valve 40. Further, the control device 60 instructs the temperature controller 37 of the pure water at the outlet of the heat exchanger 38 to operate the flow rate adjusting valve 39 provided in the hot water pipe 53 of the heat exchanger 38,
By controlling the flow rate of hot water, the temperature of pure water is controlled to approach the specified temperature. The pure water supply time is calculated from the capacity of the extraction tank 31 and the pure water flow rate, and when the extraction tank 31 is full, the solenoid valve 46 is supplied.
Is closed.

【0024】ここで、抽出原料粒或いは抽出原料葉から
エキスを抽出するため、一定時間保持された後、制御装
置60からの指令により、電磁弁41が開き、抽出液が
下方のバッファタンク32に流下する。またバッファ
タンク32では、後述するように重量が計量され、液
濃度が検出された後、電磁弁42が開かれ、抽出液が抽
出液受け樋51に流下し、ポンプ45により貯蔵タンク
へ排出される。
Here, in order to extract the extract from the extraction raw material grain or the extraction raw material leaf, after being held for a certain period of time, the solenoid valve 41 is opened by a command from the control device 60, and the extraction liquid is stored in the lower buffer tank 32. Run down. In the buffer tank 32, the weight is measured as described later, and after the liquid concentration is detected, the electromagnetic valve 42 is opened, the extraction liquid flows down into the extraction liquid receiving trough 51, and is discharged to the storage tank by the pump 45. It

【0025】一方、抽出液を送り出した抽出タンク3
1では、洗浄水配管54の電磁弁48が開き、タンク底
部59が持ち上げられ、ノズル55から洗浄水が吹出
し、原料の抽出粕が排出樋70に流れ出し、同時に抽出
タンク31の内側、フィルタ58、配管等が洗浄され
る。洗浄が完了した後、電磁弁48が閉じ、底部59が
下がり、タンク下部が密閉され、次の抽出に備える。
On the other hand, the extraction tank 3 which has sent out the extraction liquid
In 1, the electromagnetic valve 48 of the cleaning water pipe 54 is opened, the tank bottom 59 is lifted, the cleaning water is blown out from the nozzle 55, the extracted rame of the raw material flows out into the discharge gutter 70, and at the same time, the inside of the extraction tank 31 and the filter 58, The piping etc. are cleaned. After the cleaning is completed, the solenoid valve 48 is closed, the bottom 59 is lowered, and the lower part of the tank is sealed to prepare for the next extraction.

【0026】以上、抽出タンク装置30の抽出工程に
ついて説明したが、これは抽出タンク装置30、抽出
タンク装置30・・・抽出タンク装置n30について
も同様である。次に制御装置60の制御方式、即ち、初
めの抽出タンク装置30から排出される抽出液の濃度
を予め設定された目標濃度値と比較し、その結果を次の
抽出タンク装置30の制御にフィードバックして、供
給水温度と流量、抽出時間を算出して、抽出条件を上記
の供給水配管の温度調節計と流量調節計とに指示し、抽
出時間を決め、次々に同様のフィードバック制御をして
複数個の抽出タンク装置30から排出した抽出液全量の
平均濃度を目標濃度に調整する制御方式を説明する。
Although the extraction process of the extraction tank device 30 has been described above, the same applies to the extraction tank device 30, the extraction tank device 30, ... The extraction tank device n30. Next, the control method of the control device 60, that is, the concentration of the extraction liquid discharged from the first extraction tank device 30 is compared with a preset target concentration value, and the result is fed back to the control of the next extraction tank device 30. Then, calculate the supply water temperature, flow rate, and extraction time, indicate the extraction conditions to the temperature controller and the flow controller of the supply water pipe, determine the extraction time, and perform similar feedback control one after another. A control method for adjusting the average concentration of all the extraction liquid discharged from the plurality of extraction tank devices 30 to the target concentration will be described.

【0027】バッファタンク32を支えているロード
セル33は、抽出タンク31より排出された抽出液の
重量を計量して、計量値を制御装置60に伝える。バッ
ファタンク32に設けられている濃度計34は、液濃
度を検出し、検出値を制御装置60に伝える。制御装置
60では、バッファタンク32内の抽出液の重量、濃
度を予め設定された目標濃度値と比較演算し、同抽出液
の濃度の目標濃度値に対するバラツキを補正するよう
に、次の抽出タンク31への純水温度と流量、抽出時
間を算出して、抽出条件を抽出タンク31の純水配管
の流量調節計36と温度調節計37とに指示すると同時
に抽出タンク31の抽出保持時間を決める。
The load cell 33 supporting the buffer tank 32 measures the weight of the extraction liquid discharged from the extraction tank 31 and transmits the measured value to the control device 60. The densitometer 34 provided in the buffer tank 32 detects the liquid concentration and transmits the detected value to the control device 60. The control device 60 compares and calculates the weight and concentration of the extract in the buffer tank 32 with a preset target concentration value, and corrects the variation of the concentration of the extract with respect to the target concentration value. The temperature and flow rate of pure water to 31 and the extraction time are calculated, and the extraction conditions are instructed to the flow controller 36 and the temperature controller 37 of the pure water piping of the extraction tank 31, and at the same time the extraction holding time of the extraction tank 31 is determined. .

【0028】以上の条件で抽出タンク31から排出さ
れた抽出液は、バッファタンク32に溜まり、同様に
排出抽出液の重量を計量して計量値を制御装置60に伝
え、バッファタンクに設けられている濃度計34は、
液濃度を検出し、検出値を制御装置60に伝える。制御
装置60では、バッファタンク32とバッファタンク
32内の抽出液の重量と、濃度から抽出液濃度の平均
を演算し、この値を目標濃度値と比較し、タンクとタ
ンクの合計の抽出液濃度と目標濃度値との差を算出
し、この差を補正するように、次の抽出タンク31へ
の純水温度と流量、抽出時間を算出して、抽出条件を抽
出タンク31の純水配管の流量調節計36と温度調節
計375とに指示すると同時に抽出タンク31の抽出
保持時間を決める。
The extraction liquid discharged from the extraction tank 31 under the above conditions is accumulated in the buffer tank 32, and similarly, the weight of the discharged extraction liquid is measured and the measured value is transmitted to the control device 60, which is provided in the buffer tank. The densitometer 34
The liquid concentration is detected and the detected value is transmitted to the control device 60. In the control device 60, the weight of the extraction liquid in the buffer tank 32 and the extraction liquid in the buffer tank 32, and the average of the extraction liquid concentration are calculated from the concentration, and this value is compared with the target concentration value, and the total extraction liquid concentration of the tank and the tank is calculated. And the target concentration value are calculated, and the pure water temperature and flow rate to the next extraction tank 31 and the extraction time are calculated so as to correct this difference, and the extraction conditions are set to the pure water piping of the extraction tank 31. At the same time as instructing the flow rate controller 36 and the temperature controller 375, the extraction holding time of the extraction tank 31 is determined.

【0029】以下同様に、抽出タンクn31まで抽出液
全量の濃度が目標濃度となるように、各抽出タンク装置
での抽出液平均濃度の成績をフィードバックしては次の
抽出タンクの抽出条件を決めるようにして、平均の抽出
液濃度をできるだけ目標濃度に近づけるように調整す
る。抽出液濃度と抽出条件の関係とは、予め試験により
検証して置く。
Similarly, the extraction condition of the next extraction tank is determined by feeding back the results of the average concentration of the extraction liquid in each extraction tank device so that the concentration of the total extraction liquid up to the extraction tank n31 will be the target concentration. In this way, the average extract concentration is adjusted so as to be as close to the target concentration as possible. The relationship between the extract concentration and the extraction conditions should be verified in advance by a test.

【0030】また抽出液濃度を目標濃度に近づけるよう
に調整する方法として、次の抽出工程の抽出タンクの供
給水温度と、流量、抽出時間の3条件を同時に変更し、
初期抽出タンク装置30の条件からできるだけ近い値
をとりながら修正、調整する方法をとる。さらに制御装
置60に、抽出タンクの供給水温度と流量、抽出時間の
3条件の上下限を設定できる機能を付加し、その範囲で
飲料の種類により、どの条件を優先するかを決め、他の
2条件を固定して、優先する条件を変化させ、それでも
たりない場合には、次の条件を変化させる方法により、
抽出液濃度と目標濃度を近づけるように調整することも
できる。
Further, as a method for adjusting the concentration of the extraction liquid so as to be close to the target concentration, the three conditions of the feed water temperature of the extraction tank, the flow rate and the extraction time in the next extraction step are simultaneously changed,
A method of correcting and adjusting while taking a value as close as possible to the condition of the initial extraction tank device 30 is adopted. Furthermore, the control device 60 is provided with a function for setting the upper and lower limits of the three conditions of the supply water temperature and flow rate of the extraction tank and the extraction time, and which condition is given priority in that range depending on the type of beverage, and other By fixing the two conditions and changing the priority condition, if it is still not enough, by changing the next condition,
It is also possible to adjust the extract concentration and the target concentration so that they are close to each other.

【0031】[0031]

【発明の効果】本発明の飲料抽出方法及び装置は前記の
ように構成されており、抽出タンクに入れた抽出原料粒
に供給水を加えて抽出原料粒のエキスを含む抽出液を抽
出する抽出工程を複数の抽出タンクのうち一つの抽出タ
ンクで終わって、抽出液を排出し、抽出液の重量と濃度
とを計測して、制御装置へ送り、抽出タンクの抽出液濃
度値と予め設定されている目標濃度値とを比較し、次の
抽出工程の抽出タンクの供給水温度と流量、抽出時間と
を演算して、この演算結果を次の抽出タンクへフィード
バックして、目標濃度に近づけ、その後も同様の制御を
行うので、排出した抽出液全量の平均濃度を目標濃度に
容易に調整することができる。
EFFECT OF THE INVENTION The beverage extraction method and apparatus of the present invention is configured as described above, and extraction is performed by adding the feed water to the extraction raw material granules contained in the extraction tank to extract the extraction liquid containing the extract of the extraction raw material granules. The process is completed in one of the plurality of extraction tanks, the extraction liquid is discharged, the weight and concentration of the extraction liquid are measured, sent to the control device, and the extraction liquid concentration value of the extraction tank is preset. Compared with the target concentration value, the feed water temperature and flow rate of the extraction tank of the next extraction process, the extraction time is calculated, and the calculation result is fed back to the next extraction tank to approach the target concentration, Since the same control is performed thereafter, the average concentration of all the discharged extract can be easily adjusted to the target concentration.

【0032】また特定の抽出タンクにおける抽出濃度が
目標値より外れていた場合でも、複数の抽出タンクの抽
出液全量の抽出濃度に与える影響が抽出タンクの数で割
った値になるので、不良品製造の虞れを少なくできると
ともに、不良品を他の抽出タンクでバックアップでき
て、容易に良品にすることができる。
Even if the extraction concentration in a particular extraction tank is out of the target value, the effect of the total extraction liquid in a plurality of extraction tanks on the extraction concentration is a value divided by the number of extraction tanks. The risk of manufacturing can be reduced, and defective products can be backed up by another extraction tank, so that they can be easily made into good products.

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

【図1】本発明の飲料抽出方法の実施に使用する飲料抽
出装置の一実施例を示すブロック図である。
FIG. 1 is a block diagram showing an embodiment of a beverage extraction device used for implementing the beverage extraction method of the present invention.

【図2】同飲料抽出装置の抽出タンク及び周辺機器を示
す側面図である。
FIG. 2 is a side view showing an extraction tank and peripheral devices of the beverage extraction device.

【図3】図2の抽出タンクの洗浄時の状態を示す説明図
である。
FIG. 3 is an explanatory diagram showing a state of the extraction tank of FIG. 2 during cleaning.

【図4】従来の飲料抽出装置を示す縦断側面図である。FIG. 4 is a vertical sectional side view showing a conventional beverage extraction device.

【符号の説明】[Explanation of symbols]

30 抽出タンク装置 31 抽出タンク 32 バッファタンク 33 抽出液重量検出手段(ロードセル) 34 液濃度検出手段(濃度計) 36、40 流量制御手段(流量調節計) 37 温度制御手段(温度調節計) 38 温度制御手段(熱交換器) 39 温度制御手段(流量調節計) 50 純水供給配管 51 抽出液受け樋 60 制御装置 30 Extraction tank device 31 Extraction tank 32 Buffer tank 33 Extraction liquid weight detection means (load cell) 34 Liquid concentration detection means (concentration meter) 36, 40 Flow rate control means (flow rate controller) 37 Temperature control means (temperature controller) 38 Temperature Control means (heat exchanger) 39 Temperature control means (flow rate controller) 50 Pure water supply pipe 51 Extraction liquid receiving trough 60 Control device

Claims (5)

【特許請求の範囲】[Claims] 【請求項1】 抽出タンクに入れた抽出原料に供給水を
加えて抽出原料のエキスを含む抽出液を抽出する抽出工
程を複数の抽出タンクのうち一つの抽出タンクで終わっ
て、抽出液を排出し、抽出液の重量と濃度とを計測し
て、制御装置へ送り、抽出タンクの抽出液濃度値と予め
設定されている目標濃度値とを比較し、次の抽出工程の
抽出タンクの供給水温度と流量、抽出時間とを演算し
て、この演算結果を次の抽出タンクへフィードバックし
て、目標濃度に近づけ、その後も同様の制御を行って、
排出した抽出液全量の平均濃度を目標濃度に調整するこ
とを特徴とした飲料抽出方法。
1. The extraction step of adding the feed water to the extraction raw material placed in the extraction tank to extract the extraction liquid containing the extract of the extraction raw material is completed in one of the plurality of extraction tanks, and the extraction liquid is discharged. Then, measure the weight and concentration of the extract, send it to the control unit, compare the extract tank concentration value with the preset target concentration value, and supply water to the extract tank for the next extraction step. The temperature, the flow rate, and the extraction time are calculated, and the calculation result is fed back to the next extraction tank to bring it closer to the target concentration, and then the same control is performed.
A beverage extraction method, characterized in that the average concentration of all discharged extract is adjusted to a target concentration.
【請求項2】 前記抽出タンクの抽出液濃度値を予め設
定された目標濃度値と比較し、抽出液の重量と濃度とよ
り次の抽出工程の抽出タンクの供給水温度と流量、抽出
時間とを演算するときに、同供給水温度と流量、抽出時
間を予め設定された範囲内で行うことを特徴とした請求
項1記載の飲料抽出方法。
2. The extraction liquid concentration value of the extraction tank is compared with a preset target concentration value, and the weight and concentration of the extraction liquid are used to determine the feed water temperature and flow rate of the extraction tank in the next extraction step, and the extraction time. The beverage extraction method according to claim 1, wherein the temperature of the supplied water, the flow rate, and the extraction time are calculated within a preset range when the calculation is performed.
【請求項3】 供給水温度、流量、抽出時間の3条件の
うち2つの条件を先ず固定し、残りの1条件を予め設定
された範囲で変化させ、それでも対応できないときに
は、上記2条件のうちの1条件を変化させることを特徴
とする請求項2記載の飲料抽出方法。
3. Two of the three conditions of supply water temperature, flow rate, and extraction time are fixed first, and the remaining one condition is changed within a preset range. 3. The beverage extraction method according to claim 2, wherein one of the conditions is changed.
【請求項4】 共通の供給水、洗浄水、抽出原料等の供
給配管の分岐配管の下流側に設けられた複数の抽出タン
クと、同各抽出タンクで抽出された抽出液を集めて送り
出す共通の抽出液排出手段とを有し、一つの抽出タンク
で抽出工程が終わった後、次の抽出タンクの抽出工程に
順次移行する飲料抽出装置において、前記各抽出タンク
毎の供給水配管に設けられた供給水の流量制御手段及び
温度制御手段と、同各抽出タンク毎の抽出液出口部に設
けられた抽出液重量検出手段及び液濃度検出手段と、抽
出工程にある任意の抽出タンクの抽出液濃度値と予め設
定されている目標濃度値とを比較し次の抽出工程の抽出
タンクの供給水温度と流量、抽出時間とを演算してこの
演算結果を次の抽出工程の抽出タンクへ送って、排出し
た抽出液全量の平均濃度を目標濃度に調整する制御装置
とを具えていることを特徴とした飲料抽出装置。
4. A plurality of extraction tanks provided on the downstream side of a branch pipe of a common supply pipe for supply water, washing water, extraction raw materials, and the like, and a common for collecting and delivering the extraction liquid extracted in each extraction tank. In the beverage extraction device that has the extract liquid discharging means, and the extraction process is completed in one extraction tank, and then sequentially proceeds to the extraction process in the next extraction tank, provided in the supply water pipe for each of the extraction tanks. Flow rate control means and temperature control means of the supply water, extraction liquid weight detection means and liquid concentration detection means provided at the extraction liquid outlet of each extraction tank, and extraction liquid of any extraction tank in the extraction process The concentration value and the preset target concentration value are compared, the temperature of the supply water of the extraction tank in the next extraction process, the flow rate, and the extraction time are calculated, and the calculation result is sent to the extraction tank in the next extraction process. , The average of all discharged extract A beverage extraction device comprising: a control device for adjusting the concentration to a target concentration.
【請求項5】 前記各抽出タンク供給配管に流量制御手
段として設けられた供給水の流量調節計と流量調整弁
と、供給水配管に供給水の温度制御手段として設けられ
た熱交換機と同熱交換機出口の供給水配管に取付けられ
た温度調節計と同温度調節計によりコントロールされる
熱交換機の熱水配管に設けられた流量調整弁と、各抽出
タンク毎の抽出液出口部に抽出液重量検出手段として設
けられたロードセルを有するバッファタンクと、前記バ
ッファタンクに液濃度検出手段として設けられた液比重
計、吸光濃度計、電気抵抗濃度計等の濃度計と、抽出工
程にある任意の抽出タンクの抽出液濃度値を予め設定さ
れた目標濃度値と比較して抽出液の重量と濃度より次の
抽出工程の抽出タンクの供給水温度と流量、抽出時間と
を演算して供給水の流量調節計と熱交換機出口の供給水
配管に取付けられた温度調節計とに指令を発して排出し
た抽出液全量の平均濃度を目標濃度に調整する制御装置
とを具えていることを特徴とした請求項4記載の飲料抽
出装置。
5. The same heat as a flow rate controller and a flow rate control valve of supply water provided as flow rate control means in each of the extraction tank supply pipes, and a heat exchanger provided as supply water temperature control means in the supply water pipes. The temperature controller attached to the feed water pipe at the outlet of the exchanger, the flow rate adjusting valve provided in the hot water pipe of the heat exchanger controlled by the temperature controller, and the weight of the extract at the extract outlet of each extraction tank A buffer tank having a load cell provided as detection means, a concentration meter such as a liquid densitometer, an absorption concentration meter, and an electrical resistance concentration meter provided as liquid concentration detection means in the buffer tank, and any extraction in the extraction step The concentration value of the extraction liquid in the tank is compared with a preset target concentration value, and the temperature and flow rate of the supply water and the extraction time of the extraction tank in the next extraction process are calculated from the weight and concentration of the extraction liquid to calculate the flow rate of the supply water. It is characterized by including a volume controller and a temperature controller attached to the feed water pipe at the outlet of the heat exchanger, and a controller for issuing an instruction to adjust the average concentration of the total amount of the extracted liquid to a target concentration. The beverage extraction device according to claim 4.
JP27196493A 1993-10-29 1993-10-29 Beverage extraction method and apparatus Expired - Fee Related JP3377570B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP27196493A JP3377570B2 (en) 1993-10-29 1993-10-29 Beverage extraction method and apparatus

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP27196493A JP3377570B2 (en) 1993-10-29 1993-10-29 Beverage extraction method and apparatus

Publications (2)

Publication Number Publication Date
JPH07115906A true JPH07115906A (en) 1995-05-09
JP3377570B2 JP3377570B2 (en) 2003-02-17

Family

ID=17507268

Family Applications (1)

Application Number Title Priority Date Filing Date
JP27196493A Expired - Fee Related JP3377570B2 (en) 1993-10-29 1993-10-29 Beverage extraction method and apparatus

Country Status (1)

Country Link
JP (1) JP3377570B2 (en)

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2011135829A (en) * 2009-12-28 2011-07-14 Kirin Beverage Corp Method for producing coffee extract
JP2013248166A (en) * 2012-05-31 2013-12-12 Asahi Soft Drinks Co Ltd Extractor and mixed extract manufacturing method
CN103920305A (en) * 2014-04-23 2014-07-16 柳秦桥 Tank group type countercurrent cordyceps extracting method
KR101496270B1 (en) * 2013-10-24 2015-02-26 강민환 Mass water-supply apparatus for manufacturing coffee extraction by water-drip method
KR101528301B1 (en) * 2014-02-11 2015-06-11 이용현 Multi-drop type apparatus for extraction of dutch coffee
CN117050814A (en) * 2023-09-20 2023-11-14 东莞奇易香料有限公司 Preparation method of spice composition

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2011135829A (en) * 2009-12-28 2011-07-14 Kirin Beverage Corp Method for producing coffee extract
JP2013248166A (en) * 2012-05-31 2013-12-12 Asahi Soft Drinks Co Ltd Extractor and mixed extract manufacturing method
KR101496270B1 (en) * 2013-10-24 2015-02-26 강민환 Mass water-supply apparatus for manufacturing coffee extraction by water-drip method
KR101528301B1 (en) * 2014-02-11 2015-06-11 이용현 Multi-drop type apparatus for extraction of dutch coffee
CN103920305A (en) * 2014-04-23 2014-07-16 柳秦桥 Tank group type countercurrent cordyceps extracting method
CN117050814A (en) * 2023-09-20 2023-11-14 东莞奇易香料有限公司 Preparation method of spice composition

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