JPS60222197A - Methane fermentation device - Google Patents

Methane fermentation device

Info

Publication number
JPS60222197A
JPS60222197A JP59078861A JP7886184A JPS60222197A JP S60222197 A JPS60222197 A JP S60222197A JP 59078861 A JP59078861 A JP 59078861A JP 7886184 A JP7886184 A JP 7886184A JP S60222197 A JPS60222197 A JP S60222197A
Authority
JP
Japan
Prior art keywords
methane fermentation
heat exchanger
temperature
temp
switching valve
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
JP59078861A
Other languages
Japanese (ja)
Inventor
Hiroshi Ouchi
大内 博志
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.)
Panasonic Holdings Corp
Original Assignee
Matsushita Electric Industrial Co 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 Matsushita Electric Industrial Co Ltd filed Critical Matsushita Electric Industrial Co Ltd
Priority to JP59078861A priority Critical patent/JPS60222197A/en
Publication of JPS60222197A publication Critical patent/JPS60222197A/en
Pending legal-status Critical Current

Links

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E50/00Technologies for the production of fuel of non-fossil origin
    • Y02E50/30Fuel from waste, e.g. synthetic alcohol or diesel

Abstract

PURPOSE:To effect satisfactory methane fermentation by changing automatically the temp. of the digesting liquid in a methane fermentation chamber by a heat exchanger in quick response with the change in the temp. of a methane fermentation device thereby controlling adequately the temp. of the digesting liquid in the methane fermentation chamber. CONSTITUTION:The heat exchanger 4 is disposed in the methane fermentation chamber 2 and a heat medium is passed through a piping route 3 including the heat exchanger 4. A control device 9 is so provided as to control the temp. of the heat medium in the route 3 by receiving the signal from a detector 5 which detects the temp. of the digesting liquid in the chamber 2. A selector valve 7 for feed water and a selector valve 8 for discharge which are changed over by the device 9 are provided to the route 3. The digesting liquid in the methane fermentation chamber is thus adequately controlled and the satisfactory methane fermentation is effected.

Description

【発明の詳細な説明】 産業上の利用分野 本発明は有機性廃棄物処理を目的とするメタン発酵装置
の改良に関するものである。
DETAILED DESCRIPTION OF THE INVENTION Field of the Invention The present invention relates to an improvement in a methane fermentation apparatus for the purpose of treating organic waste.

従来例の構成とその問題点 有機性廃棄物を処理するメタン発酵装置においては、3
6°C付近を適温とする中温菌を使ったもの入、so’
c付近を適温とする高温菌を使ったものとに分かれるが
、温度管理が比較的容易なことから中温菌を用いたメタ
ン発酵装置が一般的である。ところで、この中温菌は4
0’Qを越えると活動が極端に劣化し死滅してしまうこ
とが知られている。°しかじ、屋外に設置されたメタン
発酵装置は夏季の直射日光を受けた場合、メタン発酵槽
内の消化液の温度が40°C以上になる事が頻繁に生じ
る。このため、メタン発酵構内の中温菌を何らかの形で
適温の35°Cまで冷却してやる必要がある0 発明の目的 本発明はメタン発酵槽内の消化液の適切な温度調節を行
い、良好なメタン発酵を行なわせるメタン発酵装置を提
供するものである。
Conventional structure and its problems In a methane fermentation device that processes organic waste, 3
So', a container made with mesophilic bacteria that has an optimal temperature around 6°C.
There are two types of methane fermentation equipment: methane fermentation equipment that uses thermophilic bacteria with an optimal temperature around c, but methane fermentation equipment that uses mesophilic bacteria is common because temperature control is relatively easy. By the way, this mesophilic bacterium has 4
It is known that when the temperature exceeds 0'Q, the activity deteriorates extremely and the species die. However, if a methane fermentation device installed outdoors is exposed to direct sunlight in the summer, the temperature of the digestive fluid inside the methane fermentation tank often rises to 40°C or higher. For this reason, it is necessary to cool the mesophilic bacteria in the methane fermentation plant to an appropriate temperature of 35°C in some way. The purpose of the present invention is to provide a methane fermentation device that performs the following steps.

発明の構成 本発明のメタン発酵装置は、メタン発酵槽と、このメタ
ン発酵槽内に配置した熱交換器と、この熱交換器を含む
配管経路と、前記メタン発酵槽内の消化液の温度を検知
する検知器と、前記検知器の信号を受けて前記配管経路
の熱媒体の温度を制御する制御装置と、前記配管経路に
設けられ前記制御装置より切換えられる給水切換弁およ
び排水切換弁とから構成され、前記消化液の適切な温度
調節を行い、効率的なメタン発酵を行うものである。
Structure of the Invention The methane fermentation apparatus of the present invention includes a methane fermentation tank, a heat exchanger disposed in the methane fermentation tank, a piping path including the heat exchanger, and a temperature control system for the digestive fluid in the methane fermentation tank. A detector for detecting, a control device for controlling the temperature of the heat medium in the piping route in response to a signal from the detector, and a water supply switching valve and a drainage switching valve that are provided in the piping route and are switched by the control device. It is designed to appropriately control the temperature of the digestive fluid and perform efficient methane fermentation.

実施例の説明 以下本発明の一実施例を添付図面を参照しながら説明す
る。
DESCRIPTION OF THE EMBODIMENTS An embodiment of the present invention will now be described with reference to the accompanying drawings.

図において、1は中温菌を含むメタン発酵を行う消化液
、2は前記消化液1を収納するメタン発酵槽、3は管内
に熱媒体が流れる配管経路、4は配管経路3の一部を構
成する熱交換器で、メタン発酵槽2内に配置され、前記
消化液1の温度を上下させるものである。5は消化液1
の温度を検知するサーミスタよりなる検知器、6は配管
経路3の一部にあって熱交換器4に熱媒体を供給するポ
ンプ、7は熱交換器4への熱媒体を切換える電磁式の給
水切換弁、8は熱交換器4からの熱媒体を切換える電磁
式の排水切換弁、9は検知器6により検知された消化液
1の温度に応じて動作する制御装置で、熱交換器4への
熱媒体を温水又は冷水に切換えるように給水切換弁1お
よび排水切換弁8を制御する。1oはメタン発酵槽2の
発酵ガスを燃焼して配管経路3の一部を加熱し温水の熱
媒体を得るガスボイラーで、メタン発酵槽2とのガス配
管を省略している。11は冷水の熱媒体を供給する給水
器で、給水切換弁7に接続されている。
In the figure, 1 is a digestive fluid that performs methane fermentation containing mesophilic bacteria, 2 is a methane fermentation tank that stores the digestive fluid 1, 3 is a piping path through which a heat medium flows, and 4 is a part of the piping path 3. This heat exchanger is placed inside the methane fermentation tank 2 and raises and lowers the temperature of the digestive fluid 1. 5 is digestive fluid 1
6 is a pump that is part of the piping route 3 and supplies the heat medium to the heat exchanger 4; 7 is an electromagnetic water supply that switches the heat medium to the heat exchanger 4; A switching valve 8 is an electromagnetic drainage switching valve that switches the heat medium from the heat exchanger 4; 9 is a control device that operates according to the temperature of the digestive fluid 1 detected by the detector 6; The water supply switching valve 1 and the drain switching valve 8 are controlled to switch the heat medium to hot water or cold water. 1o is a gas boiler that burns fermentation gas from the methane fermentation tank 2 to heat a part of the piping route 3 to obtain a hot water heat medium, and the gas piping with the methane fermentation tank 2 is omitted. A water supply device 11 supplies a heat medium of cold water, and is connected to the water supply switching valve 7.

第2図において、12は検知器6からの電圧信号が例え
ば38°C以上を示した時にONになる高温比較器、1
3は前記高温比較器13により駆動され、ポンプ6、給
水切換弁7および排水切換弁8を制御する第1のリレー
、14は検知器6が例えば36°C以下を示した時にO
Nになる低温比較器、15は前記低温比較器14により
駆動されポンプ6およびガスボイラー1oを制御する第
2のリレー、16は制御用トランス、ゴ7は前記制御用
トランス16にて降圧された電圧を直流に変換し以降の
制御回路に直流電圧を供給する直流定電圧電源である。
In FIG. 2, 12 is a high temperature comparator that turns ON when the voltage signal from the detector 6 indicates, for example, 38°C or higher;
3 is a first relay which is driven by the high temperature comparator 13 and controls the pump 6, water supply switching valve 7 and drain switching valve 8; 14 is a first relay which is turned on when the detector 6 indicates a temperature below 36°C
15 is a second relay that is driven by the low temperature comparator 14 and controls the pump 6 and the gas boiler 1o; 16 is a control transformer; and GO 7 is a voltage lowered by the control transformer 16. It is a DC constant voltage power supply that converts voltage to DC and supplies DC voltage to subsequent control circuits.

次に第1図、第2図を参照しながらメタン発酵装置の詳
細な説明を行う。
Next, a detailed explanation of the methane fermentation apparatus will be given with reference to FIGS. 1 and 2.

消化液1が中温菌の活動に適当な温度(36°C)であ
れば、制御装置9はいずれの機器にも信号を送らず、ポ
ンプ6やガスボイラー1oは停止状態であり、従って配
管経路3内にはいずれの熱媒体も流れない。
If the temperature of the digestive fluid 1 is appropriate for the activity of mesophilic bacteria (36°C), the control device 9 will not send a signal to any equipment, the pump 6 and the gas boiler 1o will be in a stopped state, and therefore the piping route will be No heat medium flows inside the chamber.

次に夏季の直射日光等により、また、外気の高温の影響
を受けて消化液が温度上昇し、例えば38°C以上にな
ったことを検知器5が検知したならば、制御装置9内の
高温比較器12がOFF状態からON状態になり、第1
のリレー13をON切換弁7はボイラー1o側から給水
器11側へ、また、排水切換弁8はボイラー1o側から
排水側へそれぞれ配管経路が切換わる0そして給水器1
1から熱交換器4内に冷水が流れ、メタン発酵槽2内の
消化液1の液温を下げ始め排水切換弁8から放出される
。消化液1が例えば366Cに達すると、高温比較器1
2は再びOFF状態に戻り、リレー13をOFF l、
、ポンプ6は停止し、給水切換弁7、排水切換弁8もO
FFとなり、配管経路3はガスボイラー1o側に戻る。
Next, if the detector 5 detects that the temperature of the digestive fluid has increased due to direct sunlight in summer or the influence of high temperature outside air, for example, 38°C or higher, the controller 9 The high temperature comparator 12 changes from the OFF state to the ON state, and the first
The switching valve 7 switches the piping route from the boiler 1o side to the water supply device 11 side, and the drain switching valve 8 switches the piping route from the boiler 1o side to the drain side.
1 flows into the heat exchanger 4 and begins to lower the temperature of the digestive fluid 1 in the methane fermentation tank 2 and is discharged from the drainage switching valve 8. When the digestive fluid 1 reaches, for example, 366C, the high temperature comparator 1
2 returns to the OFF state and turns off the relay 13.
, the pump 6 is stopped, and the water supply switching valve 7 and drainage switching valve 8 are also closed.
It becomes FF, and the piping route 3 returns to the gas boiler 1o side.

次に外気の温度が低下し、それにつれて消化液1の温度
が例えば35°Cを下回ったことを検知器5が検知した
場合、制御装置9内の低温比較器14がOFF状態から
ON状態になる。これにより第2のリレー15を働らか
せポンプ6を駆動させると同時にガスボイラー10も駆
動させて発酵ガスを燃焼させる。この燃焼によシ温水を
作り、その温水を熱媒体として、給水切換弁7を経由し
てポンプ6から熱交換器4に送って、消化液1を加温す
る。熱交換器4により加温を終えた熱媒体は排水切換弁
8を経由してガスボイラー1oに戻される。戻された水
はガスボイラー1oにより加温されて再び熱交換器4に
供給され、消化液1の加温を行う。加温が継続され、消
化液1の液温が例えば36°Cを越えたことを検知器5
が検知したならば、低温比較器14はOFFに戻り、リ
レー15もOFFになり、ポンプ6およびガスボイラー
10は停止され、加温は終了する。
Next, when the temperature of the outside air decreases and the detector 5 detects that the temperature of the digestive fluid 1 falls below, for example, 35°C, the low temperature comparator 14 in the control device 9 changes from the OFF state to the ON state. Become. As a result, the second relay 15 is operated to drive the pump 6, and at the same time, the gas boiler 10 is also driven to combust the fermentation gas. Hot water is produced by this combustion, and the hot water is sent as a heat medium from the pump 6 to the heat exchanger 4 via the water supply switching valve 7 to heat the digestive fluid 1. The heat medium that has been heated by the heat exchanger 4 is returned to the gas boiler 1o via the drainage switching valve 8. The returned water is heated by the gas boiler 1o and supplied to the heat exchanger 4 again, where the digestive fluid 1 is heated. The detector 5 detects that the temperature of the digestive fluid 1 has exceeded 36°C due to continued heating.
If detected, the low temperature comparator 14 returns to OFF, the relay 15 also turns OFF, the pump 6 and the gas boiler 10 are stopped, and heating ends.

なお、実施例では、熱媒体として水を用い、またこれを
ガスボイラーで加温したが、必ずしもこの例に限られる
ものでないことはあきらかである。
In addition, although water was used as a heat medium and was heated by a gas boiler in the example, it is clear that the present invention is not necessarily limited to this example.

発明の効果 本発明のメタン発酵装置は、メタン発酵槽内の消化液の
温度状態を検知器により絶えず検知し、メタン発酵槽内
の消化液の液温か高温になろうとした場合は制御装置を
作動して熱交換器を冷却器として作用させ消化液の温度
上昇を抑制し、一方消化液が低温になろうとする場合は
制御装置が作動して熱交換器を加温器に切換え消化液の
温度低下も抑制するものである。したがって温度の変化
に対しても熱交換器で自動的に速やかな対応を取ること
が出来、良好なメタン発酵に寄与するものである。また
自動運転であるので手間が省けるものであり、きわめて
実用的である。
Effects of the Invention The methane fermentation device of the present invention constantly detects the temperature state of the digestive fluid in the methane fermentation tank using a detector, and activates the control device when the temperature of the digestive fluid in the methane fermentation tank becomes too hot. The heat exchanger acts as a cooler and suppresses the temperature rise of the digestive fluid.If the digestive fluid is about to drop to a low temperature, the control device operates and switches the heat exchanger to a warmer to lower the temperature of the digestive fluid. It also suppresses the decline. Therefore, the heat exchanger can automatically and quickly respond to changes in temperature, contributing to good methane fermentation. Also, since it is automatic, it saves time and effort, making it extremely practical.

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

第1図は本発明の一実施例を示すメタン発酵装置の断面
図、第2図は同装置の制御回路図である。 2・・・・・・メタン発酵槽、3・・・山配管経路、4
・・・・・・熱交換器、5・・・・・・検知器、ア、・
・・・・・給水切換弁、8・・・・・・排水切換弁、9
・・・・・・制御装置。 代理人の氏名 弁理士 中 尾 敏 男 ほか1名第1
FIG. 1 is a sectional view of a methane fermentation device showing an embodiment of the present invention, and FIG. 2 is a control circuit diagram of the device. 2...Methane fermentation tank, 3...Mountain piping route, 4
...Heat exchanger, 5...Detector, a...
...Water supply switching valve, 8...Drainage switching valve, 9
······Control device. Name of agent: Patent attorney Toshio Nakao and 1 other person No. 1
figure

Claims (1)

【特許請求の範囲】[Claims] メタン発酵槽と、このメタン発酵槽内に配置した熱交換
器と、この熱交換器を含む配管経路と、前記メタン発酵
槽内の消化液の温度を検知する検知器と、前記検知器の
信号を受けて前記配管経路の熱媒体の温度を制御する制
御装置と、前記配管経路に設けられ前記制御装置により
切換えられる給水切換弁および排水切換弁とから構成さ
れるメタン発酵装置。
A methane fermentation tank, a heat exchanger placed in the methane fermentation tank, a piping route including the heat exchanger, a detector for detecting the temperature of the digestive fluid in the methane fermentation tank, and a signal from the detector. A methane fermentation device comprising: a control device for controlling the temperature of a heat medium in the piping route based on the received water; and a water supply switching valve and a drainage switching valve that are provided in the piping route and are switched by the control device.
JP59078861A 1984-04-19 1984-04-19 Methane fermentation device Pending JPS60222197A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP59078861A JPS60222197A (en) 1984-04-19 1984-04-19 Methane fermentation device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP59078861A JPS60222197A (en) 1984-04-19 1984-04-19 Methane fermentation device

Publications (1)

Publication Number Publication Date
JPS60222197A true JPS60222197A (en) 1985-11-06

Family

ID=13673605

Family Applications (1)

Application Number Title Priority Date Filing Date
JP59078861A Pending JPS60222197A (en) 1984-04-19 1984-04-19 Methane fermentation device

Country Status (1)

Country Link
JP (1) JPS60222197A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH02277599A (en) * 1989-04-19 1990-11-14 Nippon Ham Kk Production of gaseous methane by fermentation of domestic animal dung
JP2013071110A (en) * 2011-09-29 2013-04-22 Mitsubishi Rayon Co Ltd Biological treatment apparatus and biological treatment method
JP2014188485A (en) * 2013-03-28 2014-10-06 Sumitomo Heavy Ind Ltd Anaerobic treatment method

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH02277599A (en) * 1989-04-19 1990-11-14 Nippon Ham Kk Production of gaseous methane by fermentation of domestic animal dung
JP2013071110A (en) * 2011-09-29 2013-04-22 Mitsubishi Rayon Co Ltd Biological treatment apparatus and biological treatment method
JP2014188485A (en) * 2013-03-28 2014-10-06 Sumitomo Heavy Ind Ltd Anaerobic treatment method

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