JPH06194345A - Ethanol concentration measuring system - Google Patents
Ethanol concentration measuring systemInfo
- Publication number
- JPH06194345A JPH06194345A JP34408392A JP34408392A JPH06194345A JP H06194345 A JPH06194345 A JP H06194345A JP 34408392 A JP34408392 A JP 34408392A JP 34408392 A JP34408392 A JP 34408392A JP H06194345 A JPH06194345 A JP H06194345A
- Authority
- JP
- Japan
- Prior art keywords
- cell
- thermocouple
- ethanol concentration
- oscillator
- measurement
- 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.)
- Withdrawn
Links
Abstract
Description
【0001】[0001]
【産業上の利用分野】本発明は、エタノール発酵タンク
内のエタノールの濃度計測装置に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a device for measuring the concentration of ethanol in an ethanol fermentation tank.
【0002】[0002]
【従来の技術】エタノール発酵タンクのエタノール濃度
計測を行なうについては、種々の方法があり、生体物
質、微生物、抗体、細胞等の分子識別機能を利用する方
法、多孔質膜を介してサンプルされた気体中のエタノー
ル濃度を赤外線ガス分析計により分析する方法、又は近
赤外線方法などがある。2. Description of the Related Art There are various methods for measuring the ethanol concentration in an ethanol fermentation tank, including a method of utilizing the molecular recognition function of biological substances, microorganisms, antibodies, cells, etc., and sampling through a porous membrane. There is a method of analyzing the concentration of ethanol in the gas by an infrared gas analyzer, a near infrared method, or the like.
【0003】[0003]
【発明が解決しようとする課題】しかし、上述の分子識
別機能を利用する方法にあっては、センサを繰返し殺菌
(加熱消毒)する必要があり、このため耐久性に問題が
ありランニングコストが高くなるという問題がある。ま
た、赤外線ガス分析計による方法についても、上述の加
熱消毒に対する耐久性やランニングコストの問題の外、
発酵液中に糖が共存する場合に計測精度が悪くなるとい
う問題、あるいは、エタノール濃度校正データを適用対
象ごとに取得する必要があるという問題がある。更に
は、近赤外線方法にあっては、上述の濃度校正データの
取得の問題の外、発酵液に菌体等の懸濁成分を除去する
必要があり、更に装置全体のコスト及びランニングコス
ト(消費電力)が極めて高くなるという問題がある。However, in the method utilizing the above-mentioned molecular identification function, it is necessary to repeatedly sterilize (heat disinfect) the sensor, which causes a problem in durability and a high running cost. There is a problem of becoming. In addition, regarding the method using an infrared gas analyzer, in addition to the problems of durability and running cost against heat sterilization described above,
There is a problem that the measurement accuracy deteriorates when sugar coexists in the fermentation liquid, or that ethanol concentration calibration data needs to be acquired for each application target. Furthermore, in the near-infrared method, in addition to the problem of obtaining the concentration calibration data described above, it is necessary to remove suspended components such as bacterial cells in the fermentation liquid, and the cost of the entire device and running cost (consumption There is a problem that the electric power) becomes extremely high.
【0004】本発明は、上述の各方法における問題、す
なわち耐久性やランニングコスト、計測精度の悪化、エ
タノール濃度校正データの取得、更には装置全体のコス
トの問題を解決した新たなエタノール濃度計測装置の提
供を目的とする。The present invention is a new ethanol concentration measuring apparatus which solves the problems in the above-mentioned methods, namely, durability, running cost, deterioration of measurement accuracy, acquisition of ethanol concentration calibration data, and the cost of the entire apparatus. For the purpose of providing.
【0005】[0005]
【課題を解決するための手段】上述の目的を達成する本
発明は、発酵タンクに両端が接続されたサンプリング配
管に備えられたポンプと仕切弁と、このポンプと仕切弁
との間にあってサンプリング配管に連通され内部に超音
波振動子が配置された計測セルと、この計測セル内に一
端が挿入された熱電対と、この熱電対の他端に接続され
たエタノール濃度演算器と、この演算器と上記超音波振
動子との間に接続されたアンプと、上記計測セルが収納
され上記サンプリング配管が貫通する恒温槽と、この恒
温槽内に冷水又は温水を供給する冷却・加熱装置と、を
備えたことを特徴とする。Means for Solving the Problems The present invention that achieves the above-mentioned object is to provide a pump and a sluice valve provided in a sampling pipe whose both ends are connected to a fermentation tank, and a sampling pipe between the pump and the sluice valve. Measuring cell in which an ultrasonic transducer is placed inside, a thermocouple with one end inserted in the measuring cell, an ethanol concentration calculator connected to the other end of the thermocouple, and this calculator An amplifier connected between the ultrasonic transducer and the ultrasonic transducer, a thermostatic chamber in which the measurement cell is housed and the sampling pipe penetrates, and a cooling / heating device for supplying cold water or hot water into the thermostatic chamber, It is characterized by having.
【0006】[0006]
【作用】発酵タンクにバイパスを設けて恒温槽内を通
し、この恒温槽内に計測セルを備え、計測セル内にて超
音波振動子と熱電対とを備えているため、温度変化によ
り発酵液内の気泡の温度を抑制して精度を高めつつ、音
速の温度特性とエタノール濃度との関係により、エタノ
ール濃度を得ている。[Function] Since the fermentation tank is provided with a bypass to pass through the inside of the constant temperature tank, a measuring cell is provided in this constant temperature tank, and an ultrasonic vibrator and a thermocouple are provided in the measuring cell, so that the fermentation liquid changes depending on the temperature change. The ethanol concentration is obtained from the relationship between the temperature characteristic of the sound velocity and the ethanol concentration while suppressing the temperature of the bubbles in the inside to improve the accuracy.
【0007】[0007]
【実施例】ここで、図1を参照して本発明の実施例を説
明する。図1において、発酵タンク10には、その上下
にバイパス通路としてサンプリング配管1a,1b(以
下配管1a,1bという)が連通し、その配管1aには
仕切弁3が備えられ、配管1bにはポンプ2が備えら
れ、配管1a,1b間には計測セル5が介在・連通され
ている。この計測セル5内には熱電対6の一端が配置さ
れ、熱電対6の他端は電線にて演算器8に接続されてい
る。また、計測セル5内には、超音波振動子4が配置さ
れ、この超音波振動子4はアンプ7を介して、演算器8
に接続されている。また、計測セル5を中心に配管1
a,1bを含めて恒温槽9a内に貫通されており、この
恒温槽9aには配管により冷却・加熱装置9bがつなが
っている。EXAMPLE An example of the present invention will now be described with reference to FIG. In FIG. 1, a fermentation tank 10 is connected with sampling pipes 1a and 1b (hereinafter referred to as pipes 1a and 1b) as bypass passages above and below the fermentation tank 10. The pipe 1a is provided with a gate valve 3 and the pipe 1b is provided with a pump. 2 is provided, and the measuring cell 5 is interposed and communicated between the pipes 1a and 1b. One end of the thermocouple 6 is arranged in the measuring cell 5, and the other end of the thermocouple 6 is connected to the calculator 8 by an electric wire. In addition, an ultrasonic transducer 4 is arranged in the measuring cell 5, and the ultrasonic transducer 4 is connected to an arithmetic unit 8 via an amplifier 7.
It is connected to the. In addition, the piping 1 centered around the measurement cell 5
The thermostat 9a including a and 1b is penetrated, and a cooling / heating device 9b is connected to the thermostat 9a by piping.
【0008】上述の構成において、配管1a,1bのバ
イパスは発酵液サンプル用に設けられており、発酵タン
ク10中の発酵液はポンプ2により計測セル5に供給さ
れる。計測セル5中に供給された発酵液は、熱電対6に
よりその温度が計測されると共に、振動子4から超音波
が送波され計測セル5内にて反射波が受信される。演算
器6からは超音波振動子4の送波信号がアンプ7を介し
て送られ、演算器6には振動子4の受信信号及び熱電対
6の温度信号が入力される。In the above structure, the bypasses of the pipes 1a and 1b are provided for the fermentation liquid sample, and the fermentation liquid in the fermentation tank 10 is supplied to the measuring cell 5 by the pump 2. The temperature of the fermented liquid supplied into the measuring cell 5 is measured by the thermocouple 6, and ultrasonic waves are transmitted from the vibrator 4 and reflected waves are received in the measuring cell 5. The transmission signal of the ultrasonic transducer 4 is sent from the calculator 6 through the amplifier 7, and the reception signal of the transducer 4 and the temperature signal of the thermocouple 6 are input to the calculator 6.
【0009】かかる計測において、菌体が発生する気泡
が計測に支障となり、その精度低下をもたらすが、菌体
が活性となる温度域を外した温度範囲に発酵液温度を設
定することにより気泡の発生を抑制することができる。
恒温槽9aはそのためのもので、冷却・加熱装置9bよ
り恒温槽9a内に冷水又は温水を供給し、発酵液温度を
気泡の発生がなくなる温度域に設定し、計測精度の向上
を図っている。発酵液温度を上述の温度域に設定し、温
度を変化させつつ発酵液の温度信号と超音波振動子4に
よる送波及び受波の時間間隔を数回にわたって行なう。
演算器8では、音速演算を行なった後、温度特性と音速
とによりエタノール濃度を求めている。なお、発酵液の
エタノール濃度nE については、次式(数1)により表
わされる。In such a measurement, the bubbles generated by the bacterial cells hinder the measurement and bring about a decrease in accuracy. However, by setting the temperature of the fermentation solution to a temperature range outside the temperature range in which the bacterial cells become active, Occurrence can be suppressed.
The constant temperature bath 9a is for that purpose, and cold water or hot water is supplied from the cooling / heating device 9b into the constant temperature bath 9a to set the temperature of the fermented liquid to a temperature range in which bubbles are not generated, thereby improving the measurement accuracy. . The temperature of the fermented liquid is set to the above-mentioned temperature range, and the temperature signal of the fermented liquid and the time intervals of transmission and reception by the ultrasonic oscillator 4 are performed several times while changing the temperature.
The calculator 8 calculates the speed of sound and then determines the ethanol concentration from the temperature characteristics and the speed of sound. The ethanol concentration n E of the fermentation broth is expressed by the following equation (Equation 1).
【数1】 [Equation 1]
【0010】なお、上記ポンプ2は、発酵タンク10よ
り計測セル5へ発酵液を供給する働きを行うと共に、仕
切弁3を閉としてポンプ2を駆動することにより、発酵
液を加圧することができ、このポンプ2による発酵液の
加圧によっても気泡の発生を抑制できる。こうして、エ
タノール濃度の高精度で迅速な計測が連続的に可能とな
った。The pump 2 serves to supply the fermented liquid from the fermentation tank 10 to the measuring cell 5, and the fermented liquid can be pressurized by driving the pump 2 with the sluice valve 3 closed. The generation of bubbles can also be suppressed by pressurizing the fermentation liquid by the pump 2. In this way, highly accurate and rapid measurement of ethanol concentration became possible continuously.
【0011】[0011]
【発明の効果】以上説明したように本発明によれば、菌
体による気泡発生が抑制され、かつ発酵液の音速の温度
特性を求めることができるため、発酵液への前処理が不
要になり、更に、共存する菌体、糖分等の影響を殆ど受
けることなく迅速なる高精度エタノール濃度計測が低コ
ストで可能となる。As described above, according to the present invention, the generation of bubbles due to bacterial cells can be suppressed, and the temperature characteristic of the sonic velocity of the fermentation broth can be obtained. Therefore, the pretreatment of the fermentation broth becomes unnecessary. In addition, rapid and highly accurate ethanol concentration measurement can be performed at low cost without being affected by coexisting bacterial cells and sugars.
【図1】本発明の一実施例に係る構成図。FIG. 1 is a configuration diagram according to an embodiment of the present invention.
1a,1b 配管 2 ポンプ 3 仕切弁 4 振動子 5 計測セル 6 熱電対 7 アンプ 8 演算器 9a 恒温槽 9b 冷却・加熱装置 10 発酵タンク 1a, 1b Piping 2 Pump 3 Gate valve 4 Transducer 5 Measuring cell 6 Thermocouple 7 Amplifier 8 Computing unit 9a Constant temperature bath 9b Cooling / heating device 10 Fermentation tank
Claims (1)
ング配管に備えられたポンプと仕切弁と、 このポンプと仕切弁との間にあってサンプリング配管に
連通され内部に超音波振動子が配置された計測セルと、 この計測セル内に一端が挿入された熱電対と、 この熱電対の他端に接続されたエタノール濃度演算器
と、 この演算器と上記超音波振動子との間に接続されたアン
プと、 上記計測セルが収納され上記サンプリング配管が貫通す
る恒温槽と、 この恒温槽内に冷水又は温水を供給する冷却・加熱装置
と、 を備えたエタノール濃度計測装置。1. A measurement in which a pump and a sluice valve are provided in a sampling pipe whose both ends are connected to a fermentation tank, and an ultrasonic transducer is arranged inside the pump and the sluice valve and communicated with the sampling pipe. A cell, a thermocouple with one end inserted in the measuring cell, an ethanol concentration calculator connected to the other end of the thermocouple, and an amplifier connected between the calculator and the ultrasonic transducer. An ethanol concentration measuring device comprising: a thermostatic chamber in which the measuring cell is housed and through which the sampling pipe penetrates; and a cooling / heating device for supplying cold water or hot water into the thermostatic chamber.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP34408392A JPH06194345A (en) | 1992-12-24 | 1992-12-24 | Ethanol concentration measuring system |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP34408392A JPH06194345A (en) | 1992-12-24 | 1992-12-24 | Ethanol concentration measuring system |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH06194345A true JPH06194345A (en) | 1994-07-15 |
Family
ID=18366524
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP34408392A Withdrawn JPH06194345A (en) | 1992-12-24 | 1992-12-24 | Ethanol concentration measuring system |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH06194345A (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US6874355B2 (en) * | 2001-03-08 | 2005-04-05 | Abb Ab | Method and device for monitoring and controlling a process |
CN103865714A (en) * | 2014-03-06 | 2014-06-18 | 江南大学 | Method of brewing yellow rice wine by using low-intensity batch-type ultrasonic-assisted treatment |
CN108300627A (en) * | 2018-01-18 | 2018-07-20 | 江南大学 | A kind of semi liquid state fermentation system of self feed back |
-
1992
- 1992-12-24 JP JP34408392A patent/JPH06194345A/en not_active Withdrawn
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US6874355B2 (en) * | 2001-03-08 | 2005-04-05 | Abb Ab | Method and device for monitoring and controlling a process |
US6874356B2 (en) * | 2001-03-08 | 2005-04-05 | Abb Ab | Method and device for monitoring and controlling a process |
CN103865714A (en) * | 2014-03-06 | 2014-06-18 | 江南大学 | Method of brewing yellow rice wine by using low-intensity batch-type ultrasonic-assisted treatment |
CN108300627A (en) * | 2018-01-18 | 2018-07-20 | 江南大学 | A kind of semi liquid state fermentation system of self feed back |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
A300 | Withdrawal of application because of no request for examination |
Free format text: JAPANESE INTERMEDIATE CODE: A300 Effective date: 20000307 |