JPS5955397A - Operating method of digestion tank - Google Patents

Operating method of digestion tank

Info

Publication number
JPS5955397A
JPS5955397A JP57167084A JP16708482A JPS5955397A JP S5955397 A JPS5955397 A JP S5955397A JP 57167084 A JP57167084 A JP 57167084A JP 16708482 A JP16708482 A JP 16708482A JP S5955397 A JPS5955397 A JP S5955397A
Authority
JP
Japan
Prior art keywords
sludge
heat
digestion tank
heating
gas
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
JP57167084A
Other languages
Japanese (ja)
Inventor
Ryoichi Morimine
森峰 亮一
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.)
Kubota Corp
Original Assignee
Kubota 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 Kubota Corp filed Critical Kubota Corp
Priority to JP57167084A priority Critical patent/JPS5955397A/en
Publication of JPS5955397A publication Critical patent/JPS5955397A/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

Landscapes

  • Treatment Of Sludge (AREA)

Abstract

PURPOSE:To maintain exactly the sludge in a digestion tank at a prescribed temp., by calculating the temp. and flow rate of the sludge charged into the digestion tank and the quantity of heat required for heating the sludge with a control device and heating the heating water with a boiler when the waste heat of a gas engine is short. CONSTITUTION:A control device 22 controls the operation of a gas engine according to the volume of the gas measured with a flowmeter 8 to maintain the output of a generator 10 always constant. Said device calculates the quantity of heat that can be recovered from the gas engine 9 and calculates the quantity of heat reguired for heatint the sludge from the temp. and flow rate of the charged sludge measured with a thermometer 23 and a sludge flowmeter 3 and the temp. of the sludge in a primary digestion tank 1 measured with a thermometer 24. The control device compares the results of the calculations, and when the quantity of the recovered heat is smaller than the quantity of the heat required for heating in a winter season or the like, the control device closes a selector valve 20 and opens selector valves 19, 21 to operate and control a hot water boiler 15 thereby making up the deficient quantity of heat.

Description

【発明の詳細な説明】 本発明は消化槽の運転方法に関する。[Detailed description of the invention] The present invention relates to a method for operating a digester.

下水、し尿、あるいは産業廃棄物等を処理するに際して
は、汚泥中の有機物を鎌気性細菌の作用で脱離液とガス
と消化汚泥とに分解消化する消化槽が用いられることが
多い。このような消化槽においては、消化槽内の汚泥の
温度を常に所定温度に維持する必要があり、このため従
来は、消化1n内で発生するメタンガス等の消化ガスを
燃料とする第1のボイラーと、灯油あるいは重油等を燃
料とする第2のボイラーとを用い、第1のボイラー、あ
るいは第1及び第2のボイラーにより蒸気を発生させて
この蒸気を消化槽内に直接供給していた。
When treating sewage, human waste, industrial waste, etc., a digestion tank is often used to decompose and digest organic matter in sludge into desorbed liquid, gas, and digested sludge through the action of sickling bacteria. In such a digestion tank, it is necessary to always maintain the temperature of the sludge in the digestion tank at a predetermined temperature, and for this reason, conventionally, a first boiler that uses digestion gas such as methane gas generated in the digestion tank as fuel has been used. and a second boiler that uses kerosene or heavy oil as fuel, and the first boiler or the first and second boilers generate steam and supply this steam directly into the digester.

しかしながらこのような従来の運転方法においては、消
化ガスを汚泥の加温にのみ用いており、池に何ら利用さ
れていなかった。また冬ル」等の低温時には、消化ガス
を燃料とする第1のボイラーのみでは熱量が不足するの
で、灯油あるいは重油等を燃料とする第2のボイラーを
併用するが、0れら第1及び第2のボイラーにより蒸気
を発生させてこれらの蒸気を互いに独立に直接消化)凸
円iこ(j(8給していたので、汚泥を所定温度に維持
するにあたって第2のボイラーの制御が非常に困難であ
り、汚泥の温度を正確に一定にすることができなかった
。また運転はすべて人為的な判断により行なわれており
、人件費が高額になると共に、x−h’>作の恐れもあ
った。
However, in such a conventional operation method, the digestion gas is used only for heating the sludge, and is not used in the pond at all. In addition, at low temperatures such as in winter, the first boiler, which uses digestion gas as fuel, does not have enough heat, so a second boiler, which uses kerosene or heavy oil as fuel, is used in combination. Steam is generated by the second boiler and these steams are directly extinguished independently of each other) Convex circle i(j) It was difficult to maintain the temperature of the sludge, and it was not possible to keep the temperature of the sludge accurately constant.Furthermore, all operations were performed based on human judgment, resulting in high labor costs and the risk of x-h'> cropping. There was also.

本発明は上記の点に鑑み、消化ガスを汚泥の加温以外に
も有効に利用でき、しかも冬期等の低温時にも消化槽内
の汚泥を正確に所定温度に維持できる消化槽の、■朝方
法を得ることを目的とする。
In view of the above-mentioned points, the present invention has been developed to provide a digester system that can effectively utilize digestion gas for purposes other than heating sludge, and that can maintain the sludge in the digester at a predetermined temperature accurately even during low temperatures such as winter. The purpose is to obtain a method.

すなわち本発明にかかる消化槽の運転≠#右方法、消化
槽で発生する消化ガスによりガスエンジンを駆動して動
力を得ると共に、該ガスエンジンの廃熱により前記消化
槽内の汚泥を加温するための加温水を加熱し、制御装置
により、前記消化槽への投入汚泥の温度及び流量と前記
消化槽内の汚泥の温度とから該汚泥を所定温度にするた
めに必要な必要加温熱量を演算し、かつ前記加温水から
前記必要加温熱量が得られるように該加温水の温度を制
御し、さらに前記ガスエンジンの廃熱に不足分が生じた
時にはボイラーを制御して前記加温水を加熱することを
特徴とするものであり、消化ガスによりガスエンジンを
駆動するので、このガスエンジンにより例えば発電機を
駆動することにより電力を得ることができ、しかもこの
ガスエンジンの廃熱により加温水を介して汚泥を加温す
るので、従来のように消化ガスをボイラーの燃料として
用いてボイラーにより蒸気を発生させ、この蒸気を直接
消化槽内に低給して汚泥を加温する場合と比較して、汚
泥の加温に関して略同程度の熱効率を得ることができ、
全体としてエネルギーの点で非常に経済的である。また
冬期等の低温時にガスエンジンの廃熱に不足分が生じた
場合、ボイラーを運転制御してこのボイラーにより、ガ
スエンジンの廃熱で加熱された加mk水をさらに加熱し
、この加温水で汚泥を加温するので、加温水の温度を制
御するのは比較的容易でありかつ加温水に時[1υ的に
短かい温度変動があってもそれによる汚泥の温度変動は
ほとんどないことから、汚泥を正確に所定の温度に維持
できる。
That is, the operation of the digestion tank according to the present invention≠ #Right method, the digestion gas generated in the digestion tank drives a gas engine to obtain power, and the waste heat of the gas engine warms the sludge in the digestion tank. The control device calculates the amount of heating heat necessary to bring the sludge to a predetermined temperature from the temperature and flow rate of the sludge input into the digestion tank and the temperature of the sludge in the digestion tank. and controlling the temperature of the heated water so that the required amount of heating heat is obtained from the heated water, and further controls the boiler to increase the temperature of the heated water when there is a shortage in the waste heat of the gas engine. Since the gas engine is driven by the digestion gas, electric power can be obtained by driving a generator, for example, and the waste heat of the gas engine can also be used to generate heated water. Since the sludge is heated through the boiler, this method is compared to the conventional method in which digestion gas is used as boiler fuel to generate steam in the boiler, and this steam is directly fed into the digestion tank to heat the sludge. It is possible to obtain approximately the same thermal efficiency in heating sludge,
Overall it is very economical in terms of energy. In addition, if there is a shortage of waste heat from the gas engine during low temperatures such as in winter, the boiler is controlled to further heat the mk water heated by the gas engine's waste heat, and this heated water is used to Since the sludge is heated, it is relatively easy to control the temperature of the heated water, and even if there is a short temperature change of 1υ in the heated water, there is almost no change in the temperature of the sludge. Sludge can be accurately maintained at a predetermined temperature.

以下、本発明の一実施例を図面に基づいて説明する。図
において、(1)は−火消化種、(2)は二次消化槽で
あり、−火消化檜(1)には汚泥流量計(3)を介して
汚泥が投入され、この−火消化種(1)内の汚泥は汚泥
循環ポンプ(4)により二重管式の加温用熱交換器(5
)を介して循環せしめられる。−火消化+1; (1)
で所定期間処理された汚泥は二次消化ire (2)に
低給され、この二次消化槽(2)で所定期間処理された
後、消化汚イ尼は汚泥引抜ポンプ(6)により脱水設備
(図示せず)に送られ、脱111液は水処理施設(図示
せず)に送られる。Iju記−火消上槽(1)及び二次
消化゛ 槽(2)の内部で発生したメタンガス等の消化
ガスは、ガスタンク(7)に1庁留され、ガスタンク(
7)からガス流↓よ計(8)を介してガスエンジン(9
)にfJI= =Qiされる。
Hereinafter, one embodiment of the present invention will be described based on the drawings. In the figure, (1) is the fire extinguisher, (2) is the secondary digestion tank, - the fire extinguisher (1) is fed with sludge via a sludge flow meter (3), and the - fire extinguisher is The sludge in seed (1) is transferred to a double-pipe heating heat exchanger (5) by a sludge circulation pump (4).
). -Fire extinguishing +1; (1)
The sludge that has been treated for a predetermined period of time is fed to the secondary digestion tank (2), and after being treated for a predetermined period of time in this secondary digestion tank (2), the digested sludge is transferred to dewatering equipment using a sludge extraction pump (6). (not shown) and the de-111 liquid is sent to a water treatment facility (not shown). Digestion gas such as methane gas generated inside the upper fire extinguishing tank (1) and the secondary fire extinguishing tank (2) is stored in the gas tank (7), and is stored in the gas tank (7).
Gas flow from 7) through meter (8) to gas engine (9
) is given fJI==Qi.

このガスエンジン(9)はs 屯m Of)を駆動して
4力を発生させる。このガスエンジン(9)の排気ガス
は冷房用のヒートポンプ(1ツ及び誹ガス用熟交換器(
6)を介して大気に放出さR’Ls顕だ冷却水はエンジ
ン冷却水ポンプα、b*こより、;a +治用熱交換器
(i4を介して循環せしめられる。すυは温水ボイラー
であり、この温水・ト、イラー0痒にはオイルクンク頭
から灯油あるいは重油等の燃料が供給される。f5iJ
記加殖用熱交換器(5)を通過する前記−火消化種(1
)の汚泥を加温するための温水は、温水循環ポンプθの
により、加温用熱交換器(5)から温水流量810樽、
排ガス用熱交F(器@、及び;晃熱用熱交換器θ局を介
して加温用熱交換器(5)に戻る流路を循環せしめられ
るか、あるいは廃熱用熱交換訝α荀を通過した後に前記
温水ボイラー(IQを介して加温用熱交換器(5)に戻
る流路を循環せしめられる7、この2つの流路の切換は
、切換弁0〔→◇により行なうことができる。弼は制御
装置uであり、この制御装置■は、−火消化種(1)へ
の投入汚泥の温度を計測する温1=を計は〉からの信号
と、前記汚泥流J後針(3)からの信号と、−吹消化タ
ンク(1)内の汚泥の温度を計θ11する温度計(ハ)
からの信号と、前記加BAH用熱交換器(5)から流出
した加温水の温度を計測する温度計に)からの信号と、
前記温水流量計(至)からの信゛す″と、!″iiJ記
′ザス流fJ計(8)からの信号とが電気的に入力され
、へn記ザスエンジン(9)とエンジン冷却水ポンプク
1Mと温水ボイラーθ0とに制御信号を出力し、また図
示していrlいが切換弁(II〜Qυにも制御信号を出
力する。
This gas engine (9) drives the s ton m Of) to generate four forces. The exhaust gas of this gas engine (9) is used as a cooling heat pump (1) and a heat exchanger (1) for cooling.
6) R'Ls discharged to the atmosphere through the engine cooling water pumps α, b*, ;a + therapeutic heat exchanger (i4) is circulated. Yes, fuel such as kerosene or heavy oil is supplied from the oil tank head to this hot water, to, and irra 0 itch.f5iJ
The fire-extinguishing species (1) passing through the heat exchanger (5)
) The hot water for heating the sludge is supplied from the heating heat exchanger (5) by the hot water circulation pump θ at a flow rate of 810 barrels,
The exhaust gas heat exchanger F (and; the flow path returning to the heating heat exchanger (5) via the cooling heat exchanger θ station is circulated, or the waste heat heat exchanger α After passing through the hot water boiler (IQ), the water is circulated through a flow path that returns to the heating heat exchanger (5) via the hot water boiler (IQ).Switching between these two flow paths can be performed by a switching valve 0 [→◇]. 2 is the control device u, and this control device The signal from (3) and the thermometer (c) that measures the temperature of the sludge in the blowing and digestion tank (1) θ11
and a signal from a thermometer that measures the temperature of the heated water flowing out from the BAH heat exchanger (5),
The signal from the hot water flow meter (to) and the signal from the Sass flow fJ meter (8) are electrically input, and the signal from the Sass engine (9) and the engine cooling water are inputted electrically. A control signal is output to the pump tank 1M and the hot water boiler θ0, and a control signal is also output to the switching valves (II to Qυ, not shown).

制御値@に)は、ガス流量計(8)により計測されるガ
ス量に応じてガスエンジン(9)の稼動状態を制御し、
ガスエンジン(9)を常にフル稼動させて発電機(1(
)の出力を常に一定にする。
The control value @) controls the operating state of the gas engine (9) according to the amount of gas measured by the gas flow meter (8),
The gas engine (9) is always running at full capacity and the generator (1 (
) output is always constant.

またガスエンジン(9)より回収し得る熱量を演算する
と共に、温度計に)及び汚泥流量計(3)により計測さ
れる投入汚泥の温度及び流量と、温度計(ハ)により計
測される一火消化禮(1)内の汚泥の温度とから、汚泥
循環ポンプ(4)により循環せしめられる汚泥を加温す
るに必要な熱Uを演算する。そしてこれらの演算結果を
比較し、例えば夏ル」等で回収熱量が必要加湿熱H1よ
りも多い場合には、ヒートポンプOυに送ることのでき
る余剰エネルギーを演算してヒートポンプαυを運転し
かつ制御すると共に、エンジン冷却水ポンプα;1を制
御して冷却水以を調節し、回収熱量が必要加温熱量と等
しくなるようにする。また例えば冬季等で回収熱力天が
必要加温熱量よりも少ない場合には、切換弁(ホ)を閉
じると共に切換弁01020を開き、温水ボイラー(ハ
)を運転しかつ制御1して不足の熱風を浦なう。
In addition, the amount of heat that can be recovered from the gas engine (9) is calculated, as well as the temperature and flow rate of the input sludge measured by the thermometer) and sludge flow meter (3), and the temperature and flow rate of the input sludge measured by the thermometer (c). The heat U required to heat the sludge circulated by the sludge circulation pump (4) is calculated from the temperature of the sludge in the digester (1). Then, these calculation results are compared, and if the amount of recovered heat is greater than the required humidification heat H1, for example in the summer, the surplus energy that can be sent to the heat pump Oυ is calculated and the heat pump αυ is operated and controlled. At the same time, the engine cooling water pump α;1 is controlled to adjust the amount of cooling water so that the amount of recovered heat is equal to the required amount of heating heat. For example, in winter, when the recovered heat energy is less than the required heating heat amount, the switching valve (E) is closed and the switching valve 01020 is opened, the hot water boiler (C) is operated, and the hot water boiler is controlled by control 1. Ura now.

このように、消化ガスによりガスエンジン(9)を11
mするので、例えば本実施例のようにこのガスエンジン
(9)で発E、 (13,α()を駆動することにより
電力を得ることができ、この?a力を処jm場等で有効
に利用できる。またガスエンジン(9)の排気ガス及び
冷却水により排ガス用熱交換器(2)及び廃熱用熱交換
器Q4)を介して加温水を加熱し、この加温水により加
温用熱交換器(5)を介して一次d3化タンク(1)の
汚泥を加温するので、従来のように消化−)ガスを燃料
とするボイラーにより蒸気をノη生させて、この蒸気を
一次消化槽内に直接共紀vる場合と比較して、汚泥の加
温に関して略同程度の熱効率が得られる。したがって、
全体としてエネルギーを有効に利用でき、非常に経済的
である。また制御装置に)により運転を全自動化でき、
人件費の削減及び誤操作の防止を実現できる。また本実
施例のように、夏期等の高温時に、回収熱量が必要加温
熱量を越えた場合、ヒートポンプαのを運転制卸して回
収熱量の余剰分により冷房を行なうようにすれば、従来
のように余剰の消化ガスを何ら利用することなく燃焼さ
せて廃棄していたのと比べて、非゛7;τに経済的であ
る。また冬期等の低温時に、回収熱量が必要加温熱量よ
りも少なくなった場合、ガスエンジン(9)の廃熱によ
り加熱された加温水を温水ボイラー(lieによりさら
に加熱するので、加温水の温度を比1咬的容易に制御で
き、しかもこの加温水により一次消化i’l (1)の
汚泥を加温するので、加温水に時間的に短かい温度変動
があっても汚泥の温度変動はほとんどないことから、汚
泥を正確に所定温惇二に維持できる。
In this way, the gas engine (9) is
Therefore, for example, as in this embodiment, electric power can be obtained by generating electricity with this gas engine (9) and driving (13, α(), and this power can be used effectively in a processing field, etc. In addition, heated water is heated by the exhaust gas and cooling water of the gas engine (9) via the exhaust gas heat exchanger (2) and the waste heat heat exchanger Q4), and this heated water is used for heating purposes. Since the sludge in the primary d3 conversion tank (1) is heated via the heat exchanger (5), steam is generated using a boiler fueled with digestion gas and this steam is used in the primary Compared to the case where the sludge is directly injected into the digester, approximately the same thermal efficiency can be obtained in terms of heating the sludge. therefore,
Overall, energy can be used effectively and it is very economical. In addition, the operation can be fully automated using the control device).
It is possible to reduce labor costs and prevent operational errors. Furthermore, as in this embodiment, when the amount of recovered heat exceeds the required amount of heating heat during high temperatures such as in summer, the heat pump This method is significantly more economical than the method in which surplus digestion gas was burned and disposed of without any use. In addition, when the amount of heat recovered is less than the amount of heating heat required during low temperatures such as winter, the heated water heated by the waste heat of the gas engine (9) is further heated by the hot water boiler (lie), so the temperature of the heated water is increased. can be controlled relatively easily, and since the heated water heats the sludge of the primary digestion i'l (1), even if there is a short temporal temperature change in the heated water, the sludge temperature will not fluctuate. Since there is almost no sludge, the sludge can be accurately maintained at a predetermined temperature.

なお上記実施例においては、夏期等の高温時にヒートポ
ンプ/1】)を運転して回収熱量の余剰分により冷房を
行なうようにしたが、必ずしもこのようにする必要はな
く、例えば回収熱(2)の余剰分を脱水処理後の消化汚
泥の乾燥等に用いてもよい。
In the above embodiment, the heat pump/1]) is operated during high temperatures such as summer to perform air conditioning using the surplus of recovered heat, but it is not necessary to do this, for example, when the recovered heat (2) The surplus may be used for drying the digested sludge after dehydration treatment.

以上説明したように、本発明にかかる消化槽の運転方接
によれば、消化ガスによりガスエンジンをQIjし、こ
のガスエンジンの廃熱により加温水を介して汚泥を加温
するので、ガスエンジンの動力を例えば発電等に有効に
利用121)、従来のように消化ガスを汚泥の加温にの
み利用していた場合と比較して非常に経済的である。ま
た冬期等の低温時に、ガスエンジンの廃熱により加熱し
た加温水をボイラーによりさらに力旧;:、1% l、
、この加温水によって汚泥を加lk(するので、汚泥の
温度を正確に所定温度に維持し得る。また制御装置によ
り運転を自動化したので、人件費を削減し得ると共に誤
操作の恐れがない。
As explained above, according to the operating method of the digestion tank according to the present invention, the gas engine is QIjed by the digestion gas, and the waste heat of the gas engine is used to heat the sludge via the heated water. The power of the engine can be effectively used for power generation, etc.121), which is very economical compared to the conventional case where the digestion gas is used only for heating the sludge. In addition, during low temperatures such as winter, the heated water heated by the waste heat of the gas engine is further heated by the boiler.
The heated water is used to heat the sludge, so the temperature of the sludge can be accurately maintained at a predetermined temperature.Also, since the operation is automated by a control device, labor costs can be reduced and there is no risk of erroneous operation.

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

図面は本発明の一実施例を示す消化(aのぴ転系統のブ
ロック図である。 (1)・・・−火消化種、(2)・・・二次dj化化種
(3)・・・汚泥流量計、(5)・・・加温用熱交換器
、(9)・・・ガスエンジン、θQ・・・排ガス用熱交
換器、0→・・・13J熱用熱交換):d、θ瞳・・・
温水ボイラー、θQ・・・オイルタンク、θtO−aυ
・・・切換弁、(イ)・・・制御装置、+23(ハ)・
・・温度d1代理人 寺本義弘
The drawing is a block diagram of a piston system of a fire extinguisher (a) showing an embodiment of the present invention. ...Sludge flow meter, (5)...Heating heat exchanger, (9)...Gas engine, θQ...Exhaust gas heat exchanger, 0→...13J heat exchange): d, θ pupil...
Hot water boiler, θQ...oil tank, θtO-aυ
...Switching valve, (A) ...Control device, +23 (C).
... Temperature d1 agent Yoshihiro Teramoto

Claims (1)

【特許請求の範囲】[Claims] 1、 消化槽で発生する消化ガスによりガスエンジンを
駆動して動力を得ると共に、該ガスエンジンの廃熱によ
り前記消化槽内の汚泥を加温するための加温水を加熱し
、制御装置により、前記消化槽への投入汚泥の温度及び
流量と前記消化槽内の汚泥の温度とから該汚泥を所定温
度にするために必要な必要加温熱量を演算し、かつ前記
加温水から1)1記必要加温熱量が得られるように該加
温水の温度を制御し、さらに前記ガスエンジンの虎熱に
不足分が生じた時にはボイラーを制御して前記加温水を
加熱することを特徴とする消化槽の運転Eを方法。
1. The digestion gas generated in the digestion tank drives a gas engine to obtain power, and the waste heat of the gas engine heats heated water for heating the sludge in the digestion tank, and the control device: From the temperature and flow rate of the sludge input into the digestion tank and the temperature of the sludge in the digestion tank, calculate the necessary amount of heating heat necessary to bring the sludge to a predetermined temperature, and from the heated water 1) 1. A digestion tank characterized in that the temperature of the heated water is controlled so as to obtain the required amount of heating heat, and further, when the heat of the gas engine is insufficient, the boiler is controlled to heat the heated water. How to drive E.
JP57167084A 1982-09-24 1982-09-24 Operating method of digestion tank Pending JPS5955397A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP57167084A JPS5955397A (en) 1982-09-24 1982-09-24 Operating method of digestion tank

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP57167084A JPS5955397A (en) 1982-09-24 1982-09-24 Operating method of digestion tank

Publications (1)

Publication Number Publication Date
JPS5955397A true JPS5955397A (en) 1984-03-30

Family

ID=15843109

Family Applications (1)

Application Number Title Priority Date Filing Date
JP57167084A Pending JPS5955397A (en) 1982-09-24 1982-09-24 Operating method of digestion tank

Country Status (1)

Country Link
JP (1) JPS5955397A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2018065088A (en) * 2016-10-19 2018-04-26 ゼネック株式会社 Biogas generating device and biogas electric power generating system using the same
JP2021013927A (en) * 2020-11-05 2021-02-12 ゼネック株式会社 Biogas generating device and biogas electric power generating system using the same
JP2021041365A (en) * 2019-09-13 2021-03-18 愛知電機株式会社 Biogas power generation system

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2018065088A (en) * 2016-10-19 2018-04-26 ゼネック株式会社 Biogas generating device and biogas electric power generating system using the same
JP2021041365A (en) * 2019-09-13 2021-03-18 愛知電機株式会社 Biogas power generation system
JP2021013927A (en) * 2020-11-05 2021-02-12 ゼネック株式会社 Biogas generating device and biogas electric power generating system using the same

Similar Documents

Publication Publication Date Title
JP6159383B2 (en) Sewage sludge drying system
JP6059849B2 (en) Heating heat source or electric production system utilizing waste heat at medium and low temperatures, and control method thereof
JP2007205187A (en) Heat recovery system attached to boiler-steam turbine system
CN207849549U (en) A kind of heat network system for electric heat storage peak regulation
Palenzuela et al. Operational improvements to increase the efficiency of an absorption heat pump connected to a multi-effect distillation unit
JPS5955397A (en) Operating method of digestion tank
CN203962198U (en) A kind of diesel generator hot and cold water chp system
JPS5925640B2 (en) Organic waste processing equipment
JP2018527699A (en) Fuel cell system
JP2020153613A (en) Energy supply system
JPH044572A (en) Vapor generator of fuel cell power generation system
JPS5955396A (en) Operating method of digestion tank
JP5153177B2 (en) Fuel cell device
JPS5955398A (en) Operating method of digestion tank
JPH09147885A (en) Thermal power generation system for fuel cell
CN112344310A (en) Superheated steam boiler device for offshore heavy oil development and operation method thereof
RU2383629C2 (en) Method of utilisation of heat of exhaust gases of process aggregates
JPS57180079A (en) Temperature controller for fuel cell
CN218677218U (en) Combined heat and power system based on coupling of fuel cell and heat pump
JP6299383B2 (en) Cogeneration system
CN219177981U (en) A closed system for distributed photovoltaic energy storage high-efficient heat supply refrigeration
JPS5952142A (en) Air conditioning method utilizing waste heat of air compressor
JPH06215784A (en) Fuel cell generating facilities
RU2793306C1 (en) Method of use of heat of cold air from axial blower of blast furnace and system of air heaters
JP7335798B2 (en) FUEL CELL SYSTEM AND FUEL CELL SYSTEM OPERATING METHOD