JPH01145390A - Temperature-controlling method for high-speed fermentation of organic material - Google Patents

Temperature-controlling method for high-speed fermentation of organic material

Info

Publication number
JPH01145390A
JPH01145390A JP30286087A JP30286087A JPH01145390A JP H01145390 A JPH01145390 A JP H01145390A JP 30286087 A JP30286087 A JP 30286087A JP 30286087 A JP30286087 A JP 30286087A JP H01145390 A JPH01145390 A JP H01145390A
Authority
JP
Japan
Prior art keywords
temperature
tank
temp
fermentation
treated
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
JP30286087A
Other languages
Japanese (ja)
Inventor
Masakatsu Kishida
岸田 正坦
Makoto Kitano
誠 北野
Seiji Kugimiya
釘宮 清治
Kazuo Nibu
丹生 一夫
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.)
NI TECHNO SALES KK
Nippon Steel Corp
Nippon Steel Plant Designing Corp
Original Assignee
NI TECHNO SALES KK
Nittetsu Plant Designing Corp
Nippon Steel Corp
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 NI TECHNO SALES KK, Nittetsu Plant Designing Corp, Nippon Steel Corp filed Critical NI TECHNO SALES KK
Priority to JP30286087A priority Critical patent/JPH01145390A/en
Publication of JPH01145390A publication Critical patent/JPH01145390A/en
Pending legal-status Critical Current

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Abstract

PURPOSE: To make it possible to maintain materials to be treated at optimum temp. for fermentation and to shorten the time for treatment, by heating materials to be treated inside a fermentation tank from the outside surface of the tank wall via the tank wall, and controlling the temp. of the inside surface of the tank wall.
CONSTITUTION: The materials 3 to be treated inside the tank 1 are indirectly heated by means of a heating device 2 of a uniform heating system such as a plane-shaped heater or a hot water jacket heater provided on the outside surface of the wall of the fermentation tank 1 via the tank wall. Then, the temperatures of the materials 3 to be treated and the inside wall surface are detected with a temp. detector 4 and a temp. detector 5 provided on the inside surface side of the tank wall respectively, and are transferred to temp. setting instruments 6, 7. These setting instruments have the upper and lower limit temp. set values respectively. The operation of the heating device 2 is stopped at the upper limit temp. set value T1 of the setting instrument 7 and the operation as mentioned above is performed at the lower limit temp. set value T2 of the setting instrument 7 until the temp. of the materials 3 to be treated reaches the upper limit temp. set value t1 of the setting instrument 6. Then, when the temp. of the materials 3 to be treated rises to or above the set value t1, the operation of the heating device 2 is stopped irrespective of any signals from the setting instrument 7 until this temp. reaches the lower limit temp. set value t2 of the setting instrument 6.
COPYRIGHT: (C)1989,JPO

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は有機物を高速発酵させるための加熱装置の温度
制御方法に関する。
DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to a temperature control method of a heating device for high-speed fermentation of organic substances.

〔従来の技術〕[Conventional technology]

従来、有機物の発酵法のうち、処理時間を短縮するため
の温度制御としては、発酵槽内にブロアー、温風ヒータ
ー等により温風吹込みを行い、温風量を変えることによ
って温度制御する方法、あるいは発酵熱により暖められ
た排気ガスを熱交換し、給気ガスを予熱することによっ
て発酵促進を行う方法がある。
Conventionally, in organic fermentation methods, temperature control to shorten processing time involves blowing hot air into the fermenter using a blower, hot air heater, etc., and controlling the temperature by changing the amount of hot air. There is a method of promoting fermentation by exchanging heat with exhaust gas warmed by fermentation heat and preheating supply gas.

〔発明が解決しようとする問題点〕[Problem that the invention seeks to solve]

しかし、前述した方法は次に示す欠点を有する。 However, the above-mentioned method has the following drawbacks.

すなわち、温風を直接槽内に送り込む加熱においては、
微生物に必要な空気量、水分蒸発に必要な空気量に対し
て10倍以上の加熱用空気量が必要となり、排気ガスの
脱臭対策に莫大な設備費と運転費が必要となる。又、温
風吹込み方式では、伝熱効果を上げるためには槽の下方
ないしは撹拌羽根に吹出口を設け、温風を吹出す方式が
必要となるが、温度制御のために温風量を変化させるこ
とにより吹出口の目詰りの問題がさけられず、長期間の
安定操業が出来ない。
In other words, when heating by sending hot air directly into the tank,
The amount of air for heating is required to be ten times more than the amount of air required for microorganisms and the amount of air required for water evaporation, and a huge amount of equipment and operating costs are required to deodorize the exhaust gas. In addition, in the hot air blowing method, in order to increase the heat transfer effect, it is necessary to install a blower outlet below the tank or on the stirring blade to blow out hot air, but in order to control the temperature, it is necessary to change the amount of hot air. As a result, the problem of clogging of the air outlet cannot be avoided, making stable operation for a long period of time impossible.

又、排気ガスを熱交換し給気ガスを予熱する方式では、
発酵最適温度迄に長時間を必要とし、期待する効果が得
られない。
In addition, in the method of preheating the supply gas by exchanging heat with the exhaust gas,
It takes a long time to reach the optimum temperature for fermentation, and the desired effect cannot be obtained.

〔問題点を解決するための手段〕[Means for solving problems]

本発明の要旨は、発酵槽槽壁の外面に加熱装置を設け、
槽壁を介して加熱する間接加熱方式の発酵槽において、
槽壁の内面温度を検知し、槽壁の内面温度の上限設定温
度(T+)で加熱を停止し、下限設定温度(T2)で加
熱運転をする制御を行うことにより各種有機物を発酵最
適温度に維持することを特徴とする有機物を高速発酵さ
せるための温度制御方法である。槽内処理物の温度を検
知し、槽内処理物温度が槽内処理物温度の上限設定温度
(t1)以上に上昇後は強制的に加熱を停止させること
、あるいは槽内処理物の温度を検知し、槽内処理物温度
が槽内処理物温度の上限設定温度(1+)以上に上昇後
は、槽内処理物温度が下限設定温度(t2)以下になる
迄強制的に加熱を停止させることは好ましい。また、前
記槽壁の内面温度の上限設定温度(T1)を100℃以
下、下限設定温度(T2)を40℃以上とすること、前
記槽内処理物温度の上限設定値(t1)を90℃以下と
すること、前記槽内処理物温度の下限設定値(h)を4
0℃以上とすることはいずれも好ましい。
The gist of the present invention is to provide a heating device on the outer surface of the fermenter tank wall,
In an indirect heating fermenter that heats through the tank wall,
By detecting the inner temperature of the tank wall, heating is stopped at the upper limit set temperature (T+) of the inner temperature of the tank wall, and heating operation is performed at the lower limit set temperature (T2), various organic substances are brought to the optimum temperature for fermentation. This is a temperature control method for high-speed fermentation of organic matter, which is characterized by maintaining the temperature. The temperature of the material to be processed in the tank is detected, and when the temperature of the material to be processed in the tank rises above the upper limit temperature (t1) of the temperature of the material to be processed in the tank, heating is forcibly stopped or the temperature of the material to be processed in the tank is lowered. When the temperature of the processed material in the tank rises above the upper limit set temperature (1+) of the temperature of the processed material in the tank, the heating is forcibly stopped until the temperature of the processed material in the tank falls below the lower limit set temperature (t2). That's good. Further, the upper limit set temperature (T1) of the inner surface temperature of the tank wall is set to 100°C or lower, the lower limit set temperature (T2) is set to 40°C or higher, and the upper limit set value (t1) of the temperature of the material to be treated in the tank is set to 90°C. The lower limit setting value (h) of the temperature of the material to be treated in the tank shall be 4.
It is preferable that the temperature is 0°C or higher.

〔作 用〕[For production]

加熱方法を槽内に温風を吹き込む方式でなく槽壁外面か
らの槽壁を介した間接加熱としているので、加熱のため
の空気は全く必要とせず、槽からの排気ガス量は微生物
に必要な空気量もしくは蒸発水分を排出するに必要な空
気量のいずれが大きい方の必要最小風量とすることが出
来、排気ガスの脱臭対策が大幅に軽減出来る。
Since the heating method is indirect heating from the outside of the tank wall through the tank wall instead of blowing hot air into the tank, no air is required for heating, and the amount of exhaust gas from the tank is necessary for microorganisms. The required minimum air volume can be set to the larger of the amount of air needed to discharge evaporated water or the amount of air required to discharge evaporated moisture, and the measures taken to deodorize the exhaust gas can be significantly reduced.

更に温度制御は槽壁の内面温度と処理物温度とによって
加熱装置の作動・停止をさせるだけの簡単な方式として
いる。
Furthermore, temperature control is a simple method in which the heating device is activated and stopped depending on the inner surface temperature of the tank wall and the temperature of the processed material.

又、有機物が投入される発酵槽においては、投入直後の
有機物温度を最適発酵温度迄数時間で上昇させ得る能力
を持つ加熱装置を用いた場合:は、温度上昇後は発酵最
適温度である40”〜90’Cに処理物温度を制御する
ことによって短期間で高速発酵を行わせることが可能で
ある。
In addition, in the fermenter where organic matter is added, if a heating device is used that has the ability to raise the temperature of the organic matter immediately after input to the optimum fermentation temperature in several hours, the temperature will reach the optimum fermentation temperature after the temperature rises. By controlling the temperature of the processed material to ~90'C, it is possible to perform high-speed fermentation in a short period of time.

〔実施例〕〔Example〕

以下、本発明の方法を図に示す一実施例に基づいて説明
する。
Hereinafter, the method of the present invention will be explained based on an embodiment shown in the drawings.

第1図に本発明の実施に使用する装置例のブロック図で
ある。温度検出器4は発酵槽1に投入された処理物3の
温度を検出し、温度設定器6に送る。また、温度検出器
5は発酵槽1の槽壁の外面に設けられた面状ヒーター又
は温水ジャケットヒーター等の均一加熱方式の加熱装置
2によって加熱される槽壁の内面側に取りつけられ、槽
壁内面の温度を検出し、温度設定器7に送る。温度設定
器6,7は各々上限温度設定値、下限温度設定値を持ち
、加熱装W2の運転停止を行う加熱装置運転操作器8を
制御する。
FIG. 1 is a block diagram of an example of a device used to implement the present invention. The temperature detector 4 detects the temperature of the processed material 3 put into the fermenter 1 and sends it to the temperature setting device 6. Further, the temperature detector 5 is attached to the inner surface of the tank wall heated by the uniform heating type heating device 2 such as a planar heater or hot water jacket heater provided on the outer surface of the tank wall of the fermenter 1. The temperature of the inner surface is detected and sent to the temperature setting device 7. The temperature setters 6 and 7 each have an upper limit temperature set value and a lower limit temperature set value, and control a heating device operating device 8 that stops the operation of the heating device W2.

制御方法は、槽内処理物温度が温度設定器6の上限温度
設定値t1になる迄は、温度設定器7の上限温度設定値
TIで加熱装置2の運転を停止し、温度設定器7の下限
温度設定値T2で加熱装置2の運転を行う。そして槽内
処理物温度が温度設定器6の上限温度設定値11以上に
上昇した時には、槽内処理物温度が温度設定器6の下限
温度設定値t2になる迄、温度設定器7からの信号に関
係なく加熱装置2の運転を停止する。
The control method is to stop the operation of the heating device 2 at the upper limit temperature setting value TI of the temperature setting device 7 until the temperature of the processed material in the tank reaches the upper limit temperature setting value t1 of the temperature setting device 6, and The heating device 2 is operated at the lower limit temperature set value T2. When the temperature of the processed material in the tank rises to the upper limit temperature setting value 11 of the temperature setting device 6 or higher, the signal from the temperature setting device 7 continues until the temperature of the processed material in the tank reaches the lower limit temperature setting value t2 of the temperature setting device 6. The operation of the heating device 2 is stopped regardless of the situation.

ここで、各温度設定器6.7の上限、下限温度設定値は
、有機物を発酵最適温度に維持する値とするべきであり
、処理物温度すなわち温度設定器6の下限設定値t、は
菌を死滅させない90℃以下、下限設定値t2は発酵菌
の最も活動する40“C以上、及び槽壁の内面温度すな
わち温度設定器7の上限設定値T1は100″C以下、
下限設定値T2は40℃以上とすることが望ましい。
Here, the upper and lower limit temperature set values of each temperature setter 6.7 should be values that maintain the organic matter at the optimum temperature for fermentation, and the temperature of the processed material, that is, the lower limit set value t of the temperature setter 6, The lower limit setting value t2 is 40"C or more where fermentation bacteria are most active, and the upper limit setting value T1 of the temperature setting device 7 is 100"C or less.
It is desirable that the lower limit setting value T2 is 40° C. or higher.

又、本実施例に示した、処理物温度に関する温度検出器
4及び温度設定器6は省略じた方式でももちろん良い。
Furthermore, it is of course possible to omit the temperature detector 4 and temperature setting device 6 related to the temperature of the processed material shown in this embodiment.

〔発明の効果] 以上の説明から明らかなように、本発明の温度制御方法
は槽内処理物の温度に応じ、槽の内壁面温度を制御する
ことによって槽内処理物温度を投入直後をも含め常時発
酵に最適な温度に維持することが出来る為、約1日間と
いう短期間で堆肥あるいは飼料とすることが出来る。
[Effects of the Invention] As is clear from the above explanation, the temperature control method of the present invention can control the temperature of the material to be processed in the tank even immediately after inputting the tank by controlling the temperature of the inner wall surface of the tank according to the temperature of the material to be processed in the tank. Since the temperature can be maintained at the optimum temperature for fermentation at all times, it can be turned into compost or feed in a short period of about one day.

【図面の簡単な説明】[Brief explanation of the drawing]

第1図は本発明を実施するための装置例を示すブロック
図である。 l・・・発酵槽、2・・・加熱装置、3・・・処理物、
4゜5・・・温度検出器、6.7・・・温度設定器、8
・・・加熱装置運転操作器。 代理人 弁理士 秋 沢 政 光 他1名
FIG. 1 is a block diagram showing an example of a device for implementing the present invention. 1... Fermentation tank, 2... Heating device, 3... Processed material,
4゜5...Temperature detector, 6.7...Temperature setting device, 8
...Heating device operation controller. Agent: Patent attorney Masamitsu Akizawa and 1 other person

Claims (6)

【特許請求の範囲】[Claims] (1)発酵槽槽壁の外面に加熱装置を設け、槽壁を介し
て加熱する間接加熱方式の発酵槽において、槽壁の内面
温度を検知し、槽壁の内面温度の上限設定温度(T_1
)で加熱を停止し、下限設定温度(T_2)で加熱運転
をする制御を行うことにより各種有機物を発酵最適温度
に維持することを特徴とする有機物を高速発酵させるた
めの温度制御方法。
(1) In a fermenter using an indirect heating method in which a heating device is installed on the outer surface of the tank wall and heats through the tank wall, the inner temperature of the tank wall is detected and the upper limit set temperature (T_1
) A temperature control method for high-speed fermentation of organic substances, characterized in that various organic substances are maintained at the optimum temperature for fermentation by controlling heating operation to be stopped at a lower limit set temperature (T_2).
(2)槽内処理物の温度を検知し、槽内処理物温度が槽
内処理物温度の上限設定温度(t_1)以上に上昇後は
強制的に加熱を停止させる特許請求の範囲第1項に記載
の有機物を高速発酵させるための温度制御方法。
(2) The temperature of the material to be processed in the tank is detected, and heating is forcibly stopped after the temperature of the material to be processed in the tank rises above the upper limit temperature (t_1) of the temperature of the material to be processed in the tank.Claim 1 A temperature control method for high-speed fermentation of organic matter as described in .
(3)槽内処理物の温度を検知し、槽内処理物温度が槽
内処理物温度の上限設定温度(t_1)以上に上昇後は
、槽内処理物温度が下限設定温度(t_2)以下になる
迄強制的に加熱を停止させる特許請求の範囲第1項に記
載の有機物を高速発酵させるための温度制御方法。
(3) The temperature of the processed material in the tank is detected, and after the temperature of the processed material in the tank rises above the upper limit set temperature (t_1) of the temperature of the processed material in the tank, the temperature of the processed material in the tank is lower than the lower limit set temperature (t_2). 2. A temperature control method for high-speed fermentation of an organic substance according to claim 1, wherein heating is forcibly stopped until the temperature reaches 100.
(4)前記槽壁の内面温度の上限設定温度(T_1)を
100℃以下、下限設定温度(T_2)を40℃以上と
した特許請求の範囲第1項、第2項、または第3項に記
載の有機物を高速発酵させるための温度制御方法。
(4) According to claim 1, 2, or 3, the upper limit set temperature (T_1) of the inner surface temperature of the tank wall is 100°C or lower, and the lower limit set temperature (T_2) is 40°C or higher. A temperature control method for high-speed fermentation of the described organic matter.
(5)前記槽内処理物温度の上限設定値(t_1)を9
0℃以下とした特許請求の範囲第2項または第3項に記
載の有機物を高速発酵させるための温度制御方法。
(5) Set the upper limit setting value (t_1) of the temperature of the material to be treated in the tank to 9
A temperature control method for high-speed fermentation of an organic substance according to claim 2 or 3, wherein the temperature is 0° C. or lower.
(6)前記槽内処理物温度の下限設定値(t_2)を4
0℃以上とした特許請求の範囲第3項に記載の有機物を
高速発酵させるための温度制御方法。
(6) Set the lower limit set value (t_2) of the temperature of the material to be processed in the tank to 4
A temperature control method for high-speed fermentation of an organic substance according to claim 3, wherein the temperature is set to 0°C or higher.
JP30286087A 1987-11-30 1987-11-30 Temperature-controlling method for high-speed fermentation of organic material Pending JPH01145390A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP30286087A JPH01145390A (en) 1987-11-30 1987-11-30 Temperature-controlling method for high-speed fermentation of organic material

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP30286087A JPH01145390A (en) 1987-11-30 1987-11-30 Temperature-controlling method for high-speed fermentation of organic material

Publications (1)

Publication Number Publication Date
JPH01145390A true JPH01145390A (en) 1989-06-07

Family

ID=17913965

Family Applications (1)

Application Number Title Priority Date Filing Date
JP30286087A Pending JPH01145390A (en) 1987-11-30 1987-11-30 Temperature-controlling method for high-speed fermentation of organic material

Country Status (1)

Country Link
JP (1) JPH01145390A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20160308476A1 (en) * 2013-11-29 2016-10-20 Arcelik Anonim Sirketi Household appliance with multiple synchronous motors and control circuit thereof
JP2019154260A (en) * 2018-03-08 2019-09-19 有限会社サズカブルーアンドリサーチ Temperature control device and method for storage tank

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20160308476A1 (en) * 2013-11-29 2016-10-20 Arcelik Anonim Sirketi Household appliance with multiple synchronous motors and control circuit thereof
JP2019154260A (en) * 2018-03-08 2019-09-19 有限会社サズカブルーアンドリサーチ Temperature control device and method for storage tank

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