JPH07204697A - Combined heat and power supply device using waste - Google Patents
Combined heat and power supply device using wasteInfo
- Publication number
- JPH07204697A JPH07204697A JP288194A JP288194A JPH07204697A JP H07204697 A JPH07204697 A JP H07204697A JP 288194 A JP288194 A JP 288194A JP 288194 A JP288194 A JP 288194A JP H07204697 A JPH07204697 A JP H07204697A
- Authority
- JP
- Japan
- Prior art keywords
- waste
- gas
- fermentation
- tank
- heat
- 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
Links
Classifications
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E20/00—Combustion technologies with mitigation potential
- Y02E20/14—Combined heat and power generation [CHP]
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E50/00—Technologies for the production of fuel of non-fossil origin
- Y02E50/30—Fuel from waste, e.g. synthetic alcohol or diesel
Landscapes
- Purification Treatments By Anaerobic Or Anaerobic And Aerobic Bacteria Or Animals (AREA)
- Treatment Of Sludge (AREA)
- Control Of Eletrric Generators (AREA)
Abstract
(57)【要約】
【目的】 農業廃棄物などの廃棄物を有効に処理して有
益な熱電併給装置を得る。
【構成】 廃棄物原料を搾汁器13や調整槽16で処理
し、処理した成分を発酵槽17a,17bで発酵処理し
てガス成分と消化汚泥や消化廃液に分離する。消化汚泥
は浄化池18で浄化するとともに人工湿地を形成する。
ガス成分はガスタンク22に採取してガスエンジン23
の燃料として用い、ガスエンジンで発電機26を駆動し
て電力を発生させるとともに、ガスエンジン23の発酵
槽の加温源として用いる。
(57) [Abstract] [Purpose] To effectively treat waste such as agricultural waste to obtain a useful cogeneration system. [Structure] The waste raw material is processed in the juicer 13 and the adjusting tank 16, and the processed components are fermented in the fermentation tanks 17a and 17b to separate into gas components and digested sludge and digested waste liquid. The digested sludge is purified in the purification pond 18 and forms an artificial wetland.
The gas components are collected in the gas tank 22 and collected in the gas engine 23.
The fuel is used as a fuel for heating the generator 26 by the gas engine to generate electric power, and is also used as a heating source for the fermentation tank of the gas engine 23.
Description
【0001】[0001]
【産業上の利用分野】本発明は農業廃棄物等の発酵熱を
利用した廃棄物利用熱電併給装置に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a combined heat and power supply system utilizing waste heat utilizing fermentation heat of agricultural waste and the like.
【0002】[0002]
【従来の技術】図2は従来の排熱回収装置を示すもの
で、同図において1は農業廃棄物などの原料を貯蔵する
原料槽、2は硫黄成分除去用のバイオリアクタ、3は発
酵用バイオリアクタ、4は分離膜、5は脱硫器、6はガ
スホルダ、7は熱交換器、8は撹拌棒、9はガス燃焼
器、10(P)はポンプである。2. Description of the Related Art FIG. 2 shows a conventional exhaust heat recovery system. In the figure, 1 is a raw material tank for storing raw materials such as agricultural waste, 2 is a bioreactor for removing sulfur components, and 3 is for fermentation. Bioreactor, 4 is a separation membrane, 5 is a desulfurizer, 6 is a gas holder, 7 is a heat exchanger, 8 is a stirring rod, 9 is a gas combustor, and 10 (P) is a pump.
【0003】農業廃棄物、主として養豚糞尿から発生す
るメタンガスは各家庭の家事に利用されているところも
ある。最近、畜産振興で多量の豚を飼育しており、糞尿
処理で河川のBODを高めている。今後は土地も糞尿に
よる酸性化が増大し、河川水の水質の基準設定も見直し
をせまられている。糞尿を集中的に処理する、農業廃棄
物処理場が必要となっている。現状では処理場を設置し
ても廃棄物を発酵させてコンポストにする程度である。
多少進んだ状態はメタン発酵槽(バイオリアクタ)を利
用し、ガス発生を行い、ガスホルダにガス貯蔵し、メタ
ンガスとしてガスエンジンを駆動し発電を行っているか
温水加熱のみである。他方バイオリアクタはメタン菌の
作用で有機物が分解されメタンとCo2が発生する。メ
タン菌の活性度は周囲温度と大きな影響を持ち通常37
℃前後で発酵を促進する中温発酵を採用している。発生
したメタンガスを燃料とし温水を作り、各リアクタに分
配し、撹拌で各部の温度を均一に保持している。発生す
るメタンガスは所内加温に使用されるのみでその他の動
力には利用できない。[0003] Agricultural wastes, mainly methane gas generated from pig manure, are also used for household chores. Recently, a large number of pigs have been raised for the promotion of livestock and the BOD of rivers has been increased by treating manure. In the future, the acidification of land will increase due to excrement, and the standard setting for water quality of river water is being reviewed. There is a need for an agricultural waste treatment plant that treats manure intensively. At present, even if a treatment plant is set up, the waste is fermented to compost.
In a slightly advanced state, a methane fermentation tank (bioreactor) is used to generate gas, store gas in a gas holder, drive a gas engine as methane gas to generate electricity, or only hot water heating. On the other hand, in the bioreactor, organic matter is decomposed by the action of methane bacteria to generate methane and Co 2 . The activity of methane bacteria has a large effect on the ambient temperature and is usually 37.
The medium temperature fermentation that promotes fermentation at around ℃ is adopted. The generated methane gas is used as a fuel to produce hot water, which is distributed to each reactor and the temperature of each part is kept uniform by stirring. The generated methane gas is used only for heating the plant and cannot be used for other power sources.
【0004】農業廃棄物利用で経済性を検討する場合、
生産品がコンポストから生産される肥料(固体)のみで
は、プラント内で使用する電力料金費用が全費用の15
%にもなり、運営状態は向上しない。コンポストの価格
は¥26円kg程度で1日当たりの投入量が13.5m
3とした場合1日当たりの生産量は5,000kg程度
であり、プラントの経済性は成立しない。農業廃棄物の
処理料金が加算されれば経済性は良くなる。その上廃棄
物に含まれる有機物の高度利用が大切である。プラント
の発生熱を有効利用することで所内動力を賄うことと発
生する熱をバイオリアクタの加温用に利用することであ
る。その上発生する脱離液を所内動力を使用せずBOD
を10mg/リットル程度まで下げて、河川放流するこ
とである。When considering the economic efficiency of utilizing agricultural waste,
If only fertilizer (solid) produced from compost is used as the product, the cost of electricity used in the plant is 15% of the total cost.
%, And the operating condition does not improve. The price of the compost is about 26 yen kg, and the input amount per day is 13.5m.
When set to 3 , the daily production is about 5,000 kg, and the economic efficiency of the plant is not established. The economic efficiency will improve if the processing fee for agricultural waste is added. In addition, it is important to make advanced use of organic substances contained in waste. It is to cover the power in the plant by effectively using the heat generated by the plant and to use the generated heat for heating the bioreactor. The desorbed liquid generated on the BOD
Is reduced to about 10 mg / liter and discharged into the river.
【0005】[0005]
【発明が解決しようとする課題】脱離液を動力と高分子
膜を利用せずに無動力で処理するには比較的広い面積を
必要とする。脱離液の処理は今後の課題であり、最も初
歩的な方法は浄化池にホテイアオイ等の水草を発生さ
せ、植物にBODを吸収さす方法である。浄化池のBO
D除去等は80%以下であり、再度の浄化を必要とす
る。浄化池の下流に人工湿地を施し、水草及び魚類を飼
い、放流可能なBODまで下げる。当プラントは大変有
益であり、離村集落、又は離島等での村落形成の有力な
目玉となる。電力の供給はインフラストラクチャの基本
であり、発生メタンガスの有効利用としてエンジン発電
機を利用したコージエネ、発電がプラントの経済評価を
向上さす、有力な点である。A relatively large area is required for treating the desorbed liquid without power and without using a polymer membrane. Treatment of the desorbed liquid is an issue for the future, and the most basic method is to generate aquatic plants such as water hyacinth in the purification pond to absorb BOD in the plant. BO of purification pond
D removal and the like is 80% or less and requires re-purification. An artificial wetland will be provided downstream of the purification pond, where weeds and fish will be kept and lowered to a BOD where it can be released. This plant is very useful and will be an important feature of village formation in remote villages or remote islands. Electricity supply is the basis of infrastructure, and cogeneration using engine generators as effective use of generated methane gas, and power generation are important points that improve the economic evaluation of the plant.
【0006】本発明は、上述の問題点に鑑みてなされた
もので、その目的は農業廃棄物などの廃棄物を有効に処
理して有益な熱電併給装置を提供することである。The present invention has been made in view of the above problems, and an object thereof is to effectively treat waste such as agricultural waste to provide a useful combined heat and power supply device.
【0007】[0007]
【課題を解決するための手段】上記目的を達成するため
に、本発明の廃棄物利用熱電併給装置は、廃棄物に含ま
れる固液成分を発酵させてガス成分と消化汚泥を成生す
る発酵手段と、前記ガス成分を処理して貯蔵するガス貯
蔵手段と、前記消化汚泥を処理して人工湿地を得る手段
と、前記ガス貯蔵手段によって貯蔵されたガス成分を動
力源とする発電手段によって、構成したことを特徴とす
る。In order to achieve the above object, the waste heat utilization cogeneration system of the present invention is a fermentation for fermenting a solid-liquid component contained in a waste to produce a gas component and digested sludge. Means, a gas storage means for processing and storing the gas component, a means for processing the digested sludge to obtain an artificial wetland, and a power generation means using the gas component stored by the gas storage means as a power source, It is characterized by being configured.
【0008】さらに、本発明の廃棄物利用併給装置は、
廃棄物原料を処理する原料処理手段と、前記発酵手段に
よって得られた消化廃液を処理する手段と、前記発電手
段によって発生した熱を用いて前記発酵手段に加温する
加温手段を、有することを特徴とする。Further, the waste utilization combined supply apparatus of the present invention is
Having a raw material processing means for processing a waste raw material, a means for processing a digestion waste liquid obtained by the fermentation means, and a heating means for heating the fermentation means by using heat generated by the power generation means. Is characterized by.
【0009】[0009]
【作用】処理された廃棄物原料は発酵槽で発酵処理され
ガス成分と消化汚泥および消化廃液に分離される。ガス
成分は発電機エンジンの燃料として使用し、エンジンの
排熱は発酵槽の加温源として使用する。The treated waste material is fermented in the fermenter and separated into gas components, digested sludge and digested waste liquid. The gas component is used as the fuel for the generator engine, and the exhaust heat of the engine is used as the heating source for the fermenter.
【0010】[0010]
【実施例】以下に本発明の実施例を図1を参照しながら
説明する。DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS An embodiment of the present invention will be described below with reference to FIG.
【0011】図1は本発明の実施例による廃棄物利用熱
電併給装置を示すもので、同図において11はスクリー
ン、12は原料槽、13は搾汁機、14は堆肥施設、1
5は水槽、16は調整槽である。ここで、原料槽12に
はスクリーン11を通して原料が収納され、この原料は
搾汁器13によって搾汁された後に固体成分は堆肥施設
14に導かれるとともに、液体成分は調整槽16に導か
れる。調整槽16では搾汁器13からの液体成分に水槽
16からの水が添加される。FIG. 1 shows a combined heat and power supply system using waste according to an embodiment of the present invention. In FIG. 1, 11 is a screen, 12 is a raw material tank, 13 is a juicer, 14 is a composting facility, and 1 is a composting facility.
Reference numeral 5 is a water tank, and 16 is an adjusting tank. Here, the raw material is stored in the raw material tank 12 through the screen 11, and after the raw material is squeezed by the squeezing device 13, the solid component is introduced to the compost facility 14 and the liquid component is introduced to the adjusting tank 16. In the adjusting tank 16, water from the water tank 16 is added to the liquid component from the juicer 13.
【0012】また、図1において17aは一次発酵槽、
17bは二次発酵槽、18は浄化池、19は人工湿地、
20は天日乾燥床、21は脱硫装置、22はガスホルダ
としてのガスタンク、23はガスエンジン、24a,2
4bは熱交換器、25はマフラー、26は発電機であ
る。Further, in FIG. 1, 17a is a primary fermenter,
17b is a secondary fermentation tank, 18 is a purification pond, 19 is an artificial wetland,
20 is a sun drying bed, 21 is a desulfurization device, 22 is a gas tank as a gas holder, 23 is a gas engine, and 24a, 2a.
4b is a heat exchanger, 25 is a muffler, and 26 is a generator.
【0013】図1の装置において、一次発酵槽17aで
は、調整槽16から導かれた液体を発酵させる。一次発
酵過程において、消化汚泥は浄化池18に導かれ、発生
ガスは脱硫装置21に導かれるとともに、消化廃液は天
日乾燥床20に導かれる。浄化池18では、消化汚泥に
希釈水を加えて浄化した後、人口湿地に導き放流する。
一次発酵槽17a内の消化廃液は天日乾燥床20に導
き、残液は液体肥料にする。In the apparatus of FIG. 1, in the primary fermentation tank 17a, the liquid introduced from the adjusting tank 16 is fermented. In the primary fermentation process, the digested sludge is guided to the purification pond 18, the generated gas is guided to the desulfurization device 21, and the digested waste liquid is guided to the sun drying bed 20. In the purification pond 18, diluted water is added to the digested sludge to purify it, and then the digested sludge is guided to an artificial wetland and discharged.
The digestion waste liquid in the primary fermentation tank 17a is led to the sun drying bed 20, and the residual liquid is used as liquid fertilizer.
【0014】一次発酵槽17aで一次発酵した液体を二
次発酵槽17bに導き、さらに消化廃液は天日乾燥床2
0に導く。二次発酵で発生したガスは脱硫装置に送出す
る。脱硫装置21では送入されたガスを脱硫してガスタ
ンク22に送出する。The liquid that has undergone primary fermentation in the primary fermentation tank 17a is introduced into the secondary fermentation tank 17b, and the digested waste liquid is further dried in the sun drying bed 2
Lead to 0. The gas generated in the secondary fermentation is sent to the desulfurizer. The desulfurization device 21 desulfurizes the fed gas and sends it to the gas tank 22.
【0015】ガスエンジン23はガスタンクから供給さ
れるガスを燃料として動作し、発電機26を駆動する。
また、ガスエンジン23は熱交換器24aによって冷却
されるとともに、排気ガスは熱交換器24bとマフラー
25を通して排出される。一次発酵槽17aと二次発酵
槽17b内の液体を、それぞれ、熱交換器24aと24
bを通して加温する。The gas engine 23 operates using the gas supplied from the gas tank as fuel, and drives the generator 26.
The gas engine 23 is cooled by the heat exchanger 24a, and the exhaust gas is discharged through the heat exchanger 24b and the muffler 25. The liquids in the primary fermenter 17a and the secondary fermenter 17b are respectively transferred to the heat exchangers 24a and 24a.
Heat through b.
【0016】廃棄物処理に必要な所内動力を下記の補機
に限定する。The internal power required for waste treatment is limited to the following auxiliary machines.
【0017】 原水ポンプ:0.75kw:1台:0.75kw ガス撹拌ポンプ:0.75kw:4台:3.0kw 搾汁機:2.2kw:2台:4.4kw プラント内照明:0.3kw:3台:0.9kw 従って、合計電力は9.05kwとなる。Raw water pump: 0.75kw: 1 unit: 0.75kw Gas stirring pump: 0.75kw: 4 units: 3.0kw Juicing machine: 2.2kw: 2 units: 4.4kw Illumination in plant: 0. 3kw: 3 units: 0.9kw Therefore, the total power is 9.05kw.
【0018】原料投入13.5m3/日の場合発生する
ガス量は412m3/日であり発生熱量は5400キロ
カロリ/Nm3として2224.8メガカロリ/日とな
る。この発生ガスを利用してガスエンジン/38PS2
台の発生電力は最大48kwの出力を発生させ、18時
から23時までの夜間電力の供給には十分な規模であ
る。一方所内動力は昼間の利用で8kw程度であり、エ
ンジン1台の駆動で十分である。他方排熱回収について
は熱量18メガカロリ/hが可能な温水熱交換器を設置
し、温水温度65℃を得る場合12,000リットル/
hの容量を持つ。バイオリヤクタ内に供給する加温水は
発酵槽容量100m34基への供給は周囲温度を冬期の
25℃に仮定しても40リットル/分程度で十分であ
る。通常は30℃以上の周囲温度であり、自然発酵でリ
アクタ内の温度は保持される。発酵期間が25日間に仮
定しているが高温発酵50℃〜55℃にも対応可能な排
熱回収の熱量を持つ。When the raw material is charged at 13.5 m 3 / day, the amount of gas generated is 412 m 3 / day, and the amount of heat generated is 5400 kilocalorie / Nm 3 and 2224.8 megacalorie / day. Gas engine / 38PS2 using this generated gas
The generated power of the table generates a maximum output of 48 kW, which is a sufficient scale for supplying nighttime power from 18:00 to 23:00. On the other hand, the power in the office is about 8 kW for daytime use, and it is sufficient to drive one engine. On the other hand, for waste heat recovery, if a hot water heat exchanger capable of generating a heat of 18 megacalories / hour is installed to obtain a hot water temperature of 65 ° C, 12,000 liters /
It has a capacity of h. Pressurized hot water fed into the Baioriyakuta is supplied to the fermentor capacity 100 m 3 4 group is sufficient at 40 liters / minute extent even assuming an ambient temperature of winter 25 ° C.. The ambient temperature is usually 30 ° C. or higher, and the temperature in the reactor is maintained by natural fermentation. It is assumed that the fermentation period is 25 days, but it has a heat quantity for exhaust heat recovery that can cope with high temperature fermentation of 50 ° C to 55 ° C.
【0019】農業廃棄物処理を自立経済システムとして
離村集落又は離島に適応する場合下記の項目が基本であ
る。When the agricultural waste treatment is applied to a remote village or island as an independent economic system, the following items are basic.
【0020】(1)経済自立型プロジェクトである。(1) It is an economically independent project.
【0021】(2)近代設備はきわめて現地加工が高
い。(2) Modern equipment requires extremely high local processing.
【0022】(3)農村集落を形成する土地があれば食
糧供給の自立を可能とする。(3) If there is land that forms a rural village, the food supply can be made independent.
【0023】(4)農産物として加工製品を生産可能に
する、例えばタンパク質産品、ハム、燻製等を含む。(4) Including a protein product, ham, smoked product, etc., which enables the production of processed products as agricultural products.
【0024】(5)村落集合に電力供給を基本とする、
今回の設計例で40家族に800Wの容量まで各家庭に
供給可能である。電灯照明、扇風機、冷蔵庫、テレビ等
は十分な容量である。(5) Power is basically supplied to the village set,
With this design example, it is possible to supply 40 families with a capacity of 800 W to each home. Electric lights, fans, refrigerators, TVs, etc. have sufficient capacity.
【0025】(6)メタンガス発生で農業廃棄物は自然
環境に還元される形で処理され、高濃度BODは河川水
を汚さない。(6) Agricultural wastes are processed in the form of being returned to the natural environment by generation of methane gas, and high concentration BOD does not pollute river water.
【0026】(7)現地人の労働力をプラント建設に利
用可能である。特にタンクの構築、基礎ブロック等には
レンガ及びコンクリート、ブロック製品で構成する。配
管についても低圧であり配管加工も現地化できる。(7) The local labor force can be used for plant construction. Especially for building tanks and foundation blocks, bricks, concrete and block products will be used. The piping is also low pressure and the piping processing can be localized.
【0027】(8)現地にて高度な技術伝達を必要とせ
ず、エンジン発電機の運転技術のみである。(8) It does not require high-level technical transmission on site, only the engine generator operation technology.
【0028】[0028]
【発明の効果】本発明は、上述の如くであって、農業廃
棄物などの廃棄物を発酵処理し、ガス成分と消化汚泥や
消化排液に分離させ、ガス成分を発電機エンジンの燃料
として利用するとともに、その他の成分で人口湿地を形
成したり肥料として用いるものであるから、有益な熱電
併給装置を得ることが出来る。Industrial Applicability The present invention is as described above, in which waste such as agricultural waste is fermented and separated into a gas component and digested sludge or digested effluent, and the gas component is used as fuel for a generator engine. Since it is used and forms an artificial wetland with other components and is used as a fertilizer, a useful combined heat and power supply device can be obtained.
【図1】本発明の実施例による廃棄物利用熱電併給装置
のブロック図。FIG. 1 is a block diagram of a combined heat and power supply system using waste according to an embodiment of the present invention.
【図2】従来の排熱回収装置の構成図。FIG. 2 is a configuration diagram of a conventional exhaust heat recovery device.
12…原料槽 13…搾汁機 16…調整槽 17a…一次発酵槽 17b…二次発酵槽 18…浄化池 19…人工湿地 20…天日乾燥床 21…脱硫装置 22…ガスタンク 23…エンジン 24a,24b…熱交換器 26…発電機 12 ... Raw material tank 13 ... Juice machine 16 ... Adjusting tank 17a ... Primary fermentation tank 17b ... Secondary fermentation tank 18 ... Purification pond 19 ... Artificial wetland 20 ... Sun drying floor 21 ... Desulfurization apparatus 22 ... Gas tank 23 ... Engine 24a, 24b ... Heat exchanger 26 ... Generator
Claims (2)
ガス成分と消化汚泥を成生する発酵手段と、 前記ガス成分を処理して貯蔵するガス貯蔵手段と、 前記消化汚泥を処理して人工湿地を得る手段と、 前記ガス貯蔵手段によって貯蔵されたガス成分を動力源
とする発電手段によって、構成したことを特徴とする、
廃棄物利用熱電併給装置。1. A fermentation means for fermenting a solid-liquid component contained in waste to produce a gas component and digested sludge, a gas storage device for treating and storing the gas component, and treating the digested sludge. A means for obtaining an artificial wetland, and a power generation means using a gas component stored by the gas storage means as a power source,
Combined heat and power equipment using waste.
原料を処理する原料処理手段と、前記発酵手段によって
得られた消化廃液を処理する手段と、前記発電手段によ
って発生した熱を用いて前記発酵手段に加温する加温手
段を、有することを特徴とする、廃棄物利用熱電併給装
置。2. The apparatus according to claim 1, further comprising a raw material processing means for processing a waste raw material, a means for processing a digestion waste liquid obtained by the fermentation means, and the heat generated by the power generation means. A combined heat and power supply device using waste, comprising a heating means for heating the fermentation means.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP288194A JPH07204697A (en) | 1994-01-17 | 1994-01-17 | Combined heat and power supply device using waste |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP288194A JPH07204697A (en) | 1994-01-17 | 1994-01-17 | Combined heat and power supply device using waste |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH07204697A true JPH07204697A (en) | 1995-08-08 |
Family
ID=11541706
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP288194A Pending JPH07204697A (en) | 1994-01-17 | 1994-01-17 | Combined heat and power supply device using waste |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH07204697A (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH10235317A (en) * | 1997-02-27 | 1998-09-08 | Ebara Corp | Anaerobic digestion treatment of livestock excretion |
| JP2002310419A (en) * | 2001-04-12 | 2002-10-23 | Meidensha Corp | Thermal decomposition facility by gas engine power generation facility using digestive gas |
| CN109987767A (en) * | 2019-04-22 | 2019-07-09 | 左可华 | A kind of split type sewage-treatment plant of medium heating purification |
| JP2020006305A (en) * | 2018-07-06 | 2020-01-16 | 東京瓦斯株式会社 | Gas production equipment |
-
1994
- 1994-01-17 JP JP288194A patent/JPH07204697A/en active Pending
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH10235317A (en) * | 1997-02-27 | 1998-09-08 | Ebara Corp | Anaerobic digestion treatment of livestock excretion |
| JP2002310419A (en) * | 2001-04-12 | 2002-10-23 | Meidensha Corp | Thermal decomposition facility by gas engine power generation facility using digestive gas |
| JP2020006305A (en) * | 2018-07-06 | 2020-01-16 | 東京瓦斯株式会社 | Gas production equipment |
| CN109987767A (en) * | 2019-04-22 | 2019-07-09 | 左可华 | A kind of split type sewage-treatment plant of medium heating purification |
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