JP5128074B2 - Operation method of organic waste treatment method system - Google Patents

Operation method of organic waste treatment method system Download PDF

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JP5128074B2
JP5128074B2 JP2006017168A JP2006017168A JP5128074B2 JP 5128074 B2 JP5128074 B2 JP 5128074B2 JP 2006017168 A JP2006017168 A JP 2006017168A JP 2006017168 A JP2006017168 A JP 2006017168A JP 5128074 B2 JP5128074 B2 JP 5128074B2
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composting
organic waste
compost
power generation
waste treatment
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JP2007197244A (en
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大治 石原
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IHI Inspection and Instrumentation Co Ltd
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    • 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
    • Y02ATECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A40/00Adaptation technologies in agriculture, forestry, livestock or agroalimentary production
    • Y02A40/10Adaptation technologies in agriculture, forestry, livestock or agroalimentary production in agriculture
    • Y02A40/20Fertilizers of biological origin, e.g. guano or fertilizers made from animal corpses
    • 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
    • Y02E20/00Combustion technologies with mitigation potential
    • Y02E20/12Heat utilisation in combustion or incineration of waste
    • 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
    • Y02TCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO TRANSPORTATION
    • Y02T10/00Road transport of goods or passengers
    • Y02T10/10Internal combustion engine [ICE] based vehicles
    • Y02T10/30Use of alternative fuels, e.g. biofuels
    • 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
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W30/00Technologies for solid waste management
    • Y02W30/40Bio-organic fraction processing; Production of fertilisers from the organic fraction of waste or refuse

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  • Control Of Vehicle Engines Or Engines For Specific Uses (AREA)
  • Incineration Of Waste (AREA)
  • Processing Of Solid Wastes (AREA)
  • Fertilizers (AREA)

Description

本発明は、有機廃棄物を発酵させた際に発生する臭気ガスを脱臭するとともに発電を行う有機廃棄物処理システムの運転方法に関する。   The present invention relates to a method for operating an organic waste treatment system that deodorizes odorous gas generated when organic waste is fermented and generates power.

養鶏場や養豚場において発生する家畜糞(糞尿を含む)、又は生ゴミ等の有機廃棄物を発酵させて堆肥化する技術において、処理過程で発生する排気ガスの悪臭対策は、大きな問題となっている。
例えば、水(あるいは薬液)洗浄法、オガ粉吸着法、微生物分解法等が知られているが、これらの脱臭方法は、水(薬液)処理を伴ったり、比較的広い敷地面積を必要としたりすることから、導入が困難な場合が多く、しかもアンモニア以外の臭気成分を除去することが難しい。
また、近年、臭気ガスを炉(脱臭炉)内で燃焼させて臭気成分を高温で熱分解する燃焼脱臭法が検討されているものの、燃焼装置及びその運転コストが高いため、普及は進んでいない。
そこで、特許文献1に示すように、コンポストを有する堆肥化装置から発生する臭気ガスを内燃機関(ディーゼルエンジン)に導入して燃料とともに燃焼させることにより、臭気成分を高温で熱分解し、同時に、その内燃機関を駆動源として発電を行うことにより、低コスト化を図ることができる有機廃棄物処理システムが提案されている。
特開2003−148186号公報
In the technology of fermenting and composting organic waste such as livestock dung (including manure) and raw garbage generated at poultry farms and pig farms, countermeasures against bad odors of exhaust gas generated during the treatment process become a major problem. ing.
For example, water (or chemical solution) cleaning methods, sawdust adsorption method, microbial decomposition method, etc. are known, but these deodorization methods involve water (chemical solution) treatment and require a relatively large site area. Therefore, it is often difficult to introduce, and it is difficult to remove odor components other than ammonia.
In recent years, a combustion deodorization method in which odor gas is burned in a furnace (deodorization furnace) to thermally decompose odor components at a high temperature has been studied. .
Therefore, as shown in Patent Document 1, by introducing odor gas generated from a composting apparatus having compost into an internal combustion engine (diesel engine) and burning it with fuel, the odor component is thermally decomposed at high temperature, An organic waste treatment system that can reduce costs by generating electric power using the internal combustion engine as a drive source has been proposed.
JP 2003-148186 A

ところで、上述した技術では、コンポストの容量が大型化すると、発生する臭気ガスの量も増してしまう。しかしながら、臭気ガスを燃焼させる内燃機関は、その処理能力が限られているので、大量の臭気ガスに対応するためには、内燃機関の台数を増やす必要がある。このため、有機廃棄物処理システムの装置コストが上昇してしまうという問題がある。   By the way, in the technique mentioned above, when the capacity | capacitance of compost becomes large, the quantity of the generated odor gas will also increase. However, since the internal combustion engine that burns odor gas has a limited processing capacity, it is necessary to increase the number of internal combustion engines in order to cope with a large amount of odor gas. For this reason, there exists a problem that the apparatus cost of an organic waste disposal system will rise.

本発明は、上述した事情に鑑みてなされたもので、コンポストの容量を増やした場合であっても、内燃機関の台数を必要最低限に抑えることが可能な有機廃棄物処理システムの運転方法を提供することを目的とする。   The present invention has been made in view of the above-described circumstances, and provides a method for operating an organic waste treatment system capable of minimizing the number of internal combustion engines even when the capacity of compost is increased. The purpose is to provide.

本発明に係る有機廃棄物処理システムの運転方法では、上記課題を解決するために以下の手段を採用した。
本発明は、コンポスト容器内において有機廃棄物を発酵させて堆肥化する複数の堆肥化装置と、前記複数の堆肥化装置から発生する臭気ガスを燃料とともに燃焼して、脱臭及び発電を行う複数の脱臭発電装置と、を有する有機廃棄物処理方法システムの運転方法において、前記有機廃棄物の投入時期を前記複数の堆肥化装置毎に異ならせて臭気ガスの最大発生時を分散化させると共に、前記複数の堆肥化装置における臭気ガスの発生状態に応じて臭気ガスの送気量を前記複数の堆肥化装置毎に異ならせて前記複数の堆肥化装置から前記脱臭発電装置に向けて送気する臭気ガスの量を一定量に制御し、前記脱臭発電装置において発生した熱量を用いて加熱した空気を前記複数の堆肥化装置に導入することを特徴とする。
In the operation method of the organic waste treatment system according to the present invention, the following means are adopted in order to solve the above problems.
The present invention includes a plurality of composting apparatuses that ferment and compost organic waste in a compost container , and a plurality of odorous gases generated from the plurality of composting apparatuses together with fuel to perform deodorization and power generation. and deodorizing power generator, in an organic waste treatment method system method of operating with the poured timing of organic waste made different for each of the plurality of composting apparatus dispersing the time of maximum occurrence of odorous gas Rutotomoni, supplying air toward the air supply amount of odorous gas from said plurality of composting device of the plurality of composting apparatus made different for each said deodorizing power generating device according to the occurrence state of odorous gases in the plurality of composting device The amount of odor gas is controlled to a constant amount, and air heated by using the amount of heat generated in the deodorizing power generation device is introduced into the plurality of composting devices.

前記複数の堆肥化装置に対する前記有機廃棄物の投入時期が、前記有機廃棄物の発酵サイクル時間を前記複数の堆肥化装置の台数分に分けた時間に基づいて規定されるものでは、各堆肥化装置における臭気ガスの最大発生時を確実に分散化させることができる。
前記複数の堆肥化装置における臭気ガスの発生状態が、前記コンポスト容器内の温度に基づいて判断されるものでは、容易かつ確実に各堆肥化装置における臭気ガスの最大発生時を判断することができる。
堆肥化を進行させるべき堆肥化装置に対して前記加熱した空気を導入するものでは、良好な堆肥化が図られる。
In the case where the input timing of the organic waste with respect to the plurality of composting devices is defined based on the time obtained by dividing the fermentation cycle time of the organic waste into the number of the plurality of composting devices , each composting The maximum generation of odor gas in the apparatus can be reliably dispersed.
When the generation state of the odor gas in the plurality of composting apparatuses is determined based on the temperature in the compost container , it is possible to easily and surely determine the maximum generation time of the odor gas in each composting apparatus. .
Good composting can be achieved by introducing the heated air into a composting apparatus that should proceed with composting .

本発明によれば、有機廃棄物の投入時期を複数の堆肥化装置毎に異ならせることで、各堆肥化装置における臭気ガスの最大発生時を分散化させることができる。また、各堆肥化装置から送気される臭気ガスの量を一定量に調整するので、脱臭発電装置に過大な臭気ガスが送気されることが防止される。これにより、脱臭発電装置の処理能力を最低限度に抑えることが可能となる。すなわち、堆肥化装置が大容量化した場合であっても、必要最低限度の脱臭発電装置により臭気ガスの脱臭を行うことができるので、装置コストの抑制を図ることができる。さらに、脱臭発電装置において発生した熱量を用いて加熱した空気を複数の堆肥化装置に導入するので、良好な堆肥化が図られる。 According to the present invention, it is possible to disperse the maximum generation time of odor gas in each composting device by changing the input timing of the organic waste for each of the plurality of composting devices. Moreover, since the quantity of the odor gas sent from each composting apparatus is adjusted to a fixed quantity, it is prevented that an excessive odor gas is supplied to the deodorizing power generation apparatus . This makes it possible to minimize the processing capacity of the deodorizing power generation device. That is, even when the composting apparatus has a large capacity, the odor gas can be deodorized by the minimum required deodorizing power generation apparatus, so that the apparatus cost can be suppressed. Furthermore, since the air heated using the calorie | heat amount which generate | occur | produced in the deodorizing electric power generation apparatus is introduce | transduced into several composting apparatuses, favorable composting is achieved.

以下、図面を参照して、本発明に係る有機廃棄物処理システムの運転方法の一実施形態について説明する。
以下の図面において、各部材の認識を容易とするために、各部材の縮尺を適宜変更している。また、以下の説明では、コンポスト容器を略してコンポストと呼んでいる。
Hereinafter, an embodiment of a method for operating an organic waste treatment system according to the present invention will be described with reference to the drawings.
In the following drawings, the scale of each member is appropriately changed in order to facilitate recognition of each member. In the following description, the compost container is abbreviated as compost.

図1は、本実施形態に係る有機廃棄物処理システムSの概略構成を示す図である。
有機廃棄物処理システムSは、畜糞(有機廃棄物)Fを発酵させて堆肥化させる複数の堆肥化装置10(10a,10b)、畜糞Fの発酵により発生した臭気ガスGを燃焼して脱臭するとともに発電を行う複数の脱臭発電装置20(20a〜20c)、臭気ガスGを堆肥化装置10から脱臭発電装置20に送気するガス送管30、有機廃棄物処理システムSの運転を制御する制御装置40等を備えて構成される。
FIG. 1 is a diagram showing a schematic configuration of an organic waste treatment system S according to the present embodiment.
The organic waste treatment system S burns and deodorizes a plurality of composting apparatuses 10 (10a, 10b) that ferment and compost livestock feces (organic waste) F, and the odor gas G generated by the fermentation of livestock feces F. A plurality of deodorizing power generation devices 20 (20a to 20c) that generate power together with them, a gas feed pipe 30 that feeds the odor gas G from the composting device 10 to the deodorization power generation device 20, and a control that controls the operation of the organic waste treatment system S The apparatus 40 is provided.

堆肥化装置10としては、例えば、畜糞Fを連続的に好気性醗酵させる連続式醗酵機が用いられる。
図2は、堆肥化装置10の概略構成を示した図である。
堆肥化装置10(10a,10b)は、例えば、約30m程度の容量のコンポスト11、コンポスト11の上部に形成される畜糞Fの投入口12、コンポスト11内において畜糞Fを常時あるいは定期的に攪拌する攪拌機13、コンポスト11内に外部から空気Xを供給するための送風管15、送風管15の途中部位に設置される空気加熱用の電気ヒータ14及び給気ブロア16等を含んで構成される。
As the composting apparatus 10, for example, a continuous fermenter for continuously aerobic fermentation of livestock feces F is used.
FIG. 2 is a diagram showing a schematic configuration of the composting apparatus 10.
The composting apparatus 10 (10a, 10b) is, for example, compost 11 having a capacity of about 30 m 3 , an input 12 for livestock feces F formed on the upper part of the compost 11, and livestock feces F in the compost 11 at regular or regular intervals. It comprises a stirrer 13 for stirring, a blower pipe 15 for supplying air X into the compost 11 from the outside, an electric heater 14 for air heating installed in the middle of the blower pipe 15, an air supply blower 16, and the like. The

攪拌機13の内部は、中空状態とされており、また、攪拌機13の下部には複数の通気孔13kが形成されている。これにより、攪拌機13の上部に接続された送風管15から攪拌機13内に供給された空気Xがコンポスト11内に供給されるようになっている。   The inside of the agitator 13 is in a hollow state, and a plurality of vent holes 13k are formed in the lower part of the agitator 13. Thereby, the air X supplied into the stirrer 13 from the blower pipe 15 connected to the upper part of the stirrer 13 is supplied into the compost 11.

そして、コンポスト11内において畜糞Fが醗酵されると、臭気成分(アンモニア、メチルメルカプタン、硫化メチル、二硫化メチル等)を含む気体(以下、臭気ガスG)が、コンポスト11の容量の約10〜30%程度の量だけ発生する。
なお、コンポスト11の上部空間には、コンポスト11内で発生する臭気ガスGの温度を検出する温度センサ42が設けられる。
Then, when livestock feces F are fermented in the compost 11, a gas containing odor components (ammonia, methyl mercaptan, methyl sulfide, methyl disulfide, etc.) (hereinafter referred to as odor gas G) is about 10 to 10 times the capacity of the compost 11. It occurs only in the amount of about 30%.
A temperature sensor 42 that detects the temperature of the odor gas G generated in the compost 11 is provided in the upper space of the compost 11.

図1に戻り、各コンポスト11a,11bの上部には、ガス送管31a,31bが接続されている。ガス送管31a,31bは、一旦ガス送管32に連結された後に、再度ガス送管33(33a〜33c)に分岐して、複数の脱臭発電装置20a〜20cに連結される。
なお、ガス送管32には、排風ブロア34が設けられている。また、ガス送管31a,31bには、それぞれ臭気ガスGの流量を調整する制御弁35a,35bが設けられている。
これにより、コンポスト11a,11b内で発生した臭気ガスGは、排風ブロア34の駆動によって、ガス送管31a,31b,32,33a〜33cを介して複数の脱臭発電装置20a〜20cに送られる。更に、各制御弁35a,35bの開度により、各コンポスト11a,11bから脱臭発電装置20a〜20cに送られる臭気ガスGを調整することが可能となっている。
Returning to FIG. 1, gas feed pipes 31a and 31b are connected to the upper portions of the composts 11a and 11b. The gas feed pipes 31a and 31b are once connected to the gas feed pipe 32, and then branch again to the gas feed pipes 33 (33a to 33c) to be connected to the plurality of deodorizing power generation devices 20a to 20c.
The gas feed pipe 32 is provided with an exhaust blower 34. Further, control valves 35a and 35b for adjusting the flow rate of the odor gas G are provided in the gas feed pipes 31a and 31b, respectively.
Thus, the odor gas G generated in the composts 11a and 11b is sent to the plurality of deodorizing power generation devices 20a to 20c through the gas feed pipes 31a, 31b, 32, and 33a to 33c by driving the exhaust blower 34. . Furthermore, the odor gas G sent from each compost 11a, 11b to the deodorizing power generation devices 20a-20c can be adjusted by the opening degree of each control valve 35a, 35b.

脱臭発電装置20(20a〜20c)は、臭気ガスGを燃料とともに燃焼することによって、高温(約1000℃)で熱分解して脱臭する燃焼機関21と、燃焼機関21を駆動源とする発電機22とを含んで構成される。
燃焼機関21としては、例えば、ディーゼル機関やガスタービン等が用いられる。適用される燃焼機関の種類やその特性については、畜糞Fの処理量や設置スペース等の周囲環境等に応じて定められる。
例えば、総排気量1000ccのディーゼル機関を用いた場合には、堆肥化装置10において発生する臭気ガスGを給気口から毎分約1m程度取り込んで灯油等の燃料とともに燃焼させることにより脱臭する。なお、臭気ガスGとともに空気を燃焼機関21に導入してもよい。
The deodorizing power generation apparatus 20 (20a to 20c) includes a combustion engine 21 that thermally decomposes and deodorizes at a high temperature (about 1000 ° C.) by burning the odor gas G together with fuel, and a generator using the combustion engine 21 as a drive source. 22.
For example, a diesel engine or a gas turbine is used as the combustion engine 21. The type of combustion engine to be applied and its characteristics are determined according to the amount of livestock feces F treated, the surrounding environment such as the installation space, and the like.
For example, when a diesel engine with a total displacement of 1000 cc is used, deodorization is achieved by taking about 1 m 3 of odor gas G generated in the composting apparatus 10 from the air inlet and burning it with fuel such as kerosene. . Note that air may be introduced into the combustion engine 21 together with the odor gas G.

制御装置40は、有機廃棄物処理システムSの運転を制御するものであって、攪拌機13、電気ヒータ14、給気ブロア16等を制御して、畜糞Fの発酵サイクルを促進させる。また、燃焼機関21を制御して、臭気ガスGの脱臭(燃焼)と発電を行う。
また、制御装置40は、コンポスト11に設けた温度センサ42からの情報を演算処理し、その演算結果等に基づいて制御弁35の開度を制御する。
The control device 40 controls the operation of the organic waste treatment system S, and controls the stirrer 13, the electric heater 14, the air supply blower 16, and the like to promote the fermentation cycle of the livestock feces F. Further, the combustion engine 21 is controlled to deodorize (combust) the odor gas G and generate power.
In addition, the control device 40 performs calculation processing on information from the temperature sensor 42 provided in the compost 11 and controls the opening degree of the control valve 35 based on the calculation result and the like.

なお、本実施形態に係る有機廃棄物処理システムSにおいては、比較的小型の脱臭発電装置20が3台設置されている。このように比較的小型の脱臭発電装置20を複数台設置することによって、単一の大型の脱臭発電装置を設置する場合と比較して、有機廃棄物処理システムSのランニングコスト及びイニシャルコスト(装置コスト)を抑えることができ、また、余剰な電力を発電しなくて済むというメリットがある。   In the organic waste treatment system S according to this embodiment, three relatively small deodorizing power generation devices 20 are installed. By installing a plurality of relatively small deodorizing power generation devices 20 in this way, the running cost and initial cost (device) of the organic waste treatment system S are compared with the case of installing a single large deodorizing power generation device. Cost), and there is an advantage that it is not necessary to generate surplus power.

次に、このように構成された本実施形態に係る有機廃棄物処理システムSの運転方法ついて説明する。
図3は、有機廃棄物処理システムSの運転方法を説明するための図である。
まず、堆肥化装置10aのコンポスト11a内に畜糞Fを投入する。コンポスト11a内に投入された畜糞Fは、コンポスト11a内において、攪拌機13によって、空気Xと共に攪拌され貯留されることによって、醗酵し堆肥化される。具体的には、コンポスト11a内の畜糞Fは、約6時間から18時間経過した時点で、大量かつ高温(約70℃)の臭気ガスGを発生する。そして、約24時間経過すると、醗酵、堆肥化が完了する。
Next, an operation method of the organic waste treatment system S according to the present embodiment configured as described above will be described.
FIG. 3 is a diagram for explaining an operation method of the organic waste treatment system S.
First, livestock dung F is thrown into the compost 11a of the composting apparatus 10a. The animal manure F thrown into the compost 11a is fermented and composted by being stirred and stored together with the air X by the stirrer 13 in the compost 11a. Specifically, the livestock excretion F in the compost 11a generates a large amount of high temperature (about 70 ° C.) odor gas G when about 6 to 18 hours have passed. And after about 24 hours, fermentation and composting are completed.

次に、堆肥化装置10bのコンポスト11b内に畜糞Fを投入する。堆肥化装置10bに畜糞Fを投入する時期は、堆肥化装置10aのコンポスト11aから大量の高温の臭気ガスGを発生する時期とする。すなわち、堆肥化装置10aに畜糞Fが投入されてから約12時間が経過した時点で、堆肥化装置10bに畜糞Fが投入される。
そして、コンポスト11b内に投入された畜糞Fも、堆肥化装置10aの場合と同様に、投入から約6時間から18時間経過した時点で大量の高温の臭気ガスGを発生し、約24時間経過することで醗酵、堆肥化が完了する。
Next, livestock feces F are put into the compost 11b of the composting apparatus 10b. The period when the animal manure F is introduced into the composting apparatus 10b is a period when a large amount of high temperature odor gas G is generated from the compost 11a of the composting apparatus 10a. That is, when about 12 hours have passed since the livestock feces F were put into the composting apparatus 10a, the livestock feces F were put into the composting apparatus 10b.
And the livestock manure F thrown into the compost 11b also generates a large amount of hot odor gas G when about 6 to 18 hours have passed since the feed, as in the case of the composting apparatus 10a, and about 24 hours have passed. This completes fermentation and composting.

そして、堆肥化装置10aにおける畜糞Fの醗酵、堆肥化が完了(コンポスト11a内に畜糞Fが投入されてから24時間経過時)した時点で、新たな畜糞Fをコンポスト11a内に畜糞Fが投入する。
同様に、堆肥化装置10bにおける畜糞Fの醗酵、堆肥化が完了(コンポスト11b内に畜糞Fが投入されてから24時間経過時)した時点で、新たな畜糞Fをコンポスト11b内に畜糞Fが投入する。
すなわち、約12時間毎に堆肥化装置10a,10bに交互に畜糞Fを投入する。これにより、図3に示すように、常に堆肥化装置10a,10bにおける畜糞Fの醗酵サイクルが重ならないようにすることができる。
そして、この醗酵過程において発生した臭気ガスGは、排風ブロア34の駆動によってガス送管31,32,33を介して脱臭発電装置20に送られる。
Then, when the fermentation and composting of the livestock feces F in the composting apparatus 10a is completed (24 hours after the livestock feces F are put into the compost 11a), the new livestock feces F are put into the compost 11a. To do.
Similarly, when the fermentation and composting of the livestock feces F in the composting apparatus 10b is completed (24 hours after the livestock feces F are put into the compost 11b), the new livestock feces F are put into the compost 11b. throw into.
That is, the animal manure F is alternately put into the composting apparatuses 10a and 10b about every 12 hours. Thereby, as shown in FIG. 3, the fermentation cycle of the livestock feces F in the composting apparatuses 10a and 10b can always be prevented from overlapping.
The odor gas G generated in the fermentation process is sent to the deodorizing power generation device 20 through the gas feed pipes 31, 32 and 33 by driving the exhaust blower 34.

なお、堆肥化装置10a,10bにおける畜糞Fの醗酵サイクルは、コンポスト11a,11bに設けた温度センサ42a,42bにより計測される。温度センサ42a,42bの計測結果は、制御装置40に送られる。
そして、制御装置40は、堆肥化装置10a,10bの温度が所定温度以上となっている場合には、堆肥化装置10a,10bに連結されたガス送管31a,31bに設けた制御弁35a,35bを開放する。
In addition, the fermentation cycle of livestock dung F in the composting apparatuses 10a and 10b is measured by temperature sensors 42a and 42b provided in the composts 11a and 11b. The measurement results of the temperature sensors 42a and 42b are sent to the control device 40.
And when the temperature of the composting apparatuses 10a and 10b is equal to or higher than the predetermined temperature, the control device 40 controls the control valves 35a and 31b provided in the gas feed pipes 31a and 31b connected to the composting apparatuses 10a and 10b. Open 35b.

すなわち、例えば、堆肥化装置10aにおいて高温の臭気ガスGが発生している場合(コンポスト11aに畜糞Fを投入後、6時間から18時間経過時まで)には、ガス送管31aの制御弁35aを開放することでコンポスト11a内の臭気ガスGを脱臭発電装置20に送気する。一方、堆肥化装置10bでは臭気ガスGの発生は殆どないのでガス送管31bの制御弁35bを遮蔽しておく等、適宜制御する。
逆に、堆肥化装置10bにおいて高温の臭気ガスGが発生している場合(コンポスト11bに畜糞Fを投入後、6時間から18時間経過時まで)には、ガス送管31bの制御弁35bを開放することでコンポスト11b内の臭気ガスGを脱臭発電装置20に送気する。一方、堆肥化装置10aでは臭気ガスGの発生は殆どないのでガス送管31aの制御弁35aを遮蔽しておく等、適宜制御する。
That is, for example, when high-temperature odor gas G is generated in the composting apparatus 10a (from 6 hours to 18 hours after the livestock feces F are introduced into the compost 11a), the control valve 35a of the gas feed pipe 31a. The odor gas G in the compost 11a is sent to the deodorizing power generation device 20 by opening the. On the other hand, in the composting apparatus 10b, since odor gas G is hardly generated, the control valve 35b of the gas feed pipe 31b is shielded, for example.
On the contrary, when high temperature odor gas G is generated in the composting apparatus 10b (from 6 hours to 18 hours after the livestock feces F are put into the compost 11b), the control valve 35b of the gas feed pipe 31b is turned on. By opening, the odor gas G in the compost 11 b is sent to the deodorizing power generation apparatus 20. On the other hand, in the composting apparatus 10a, since odor gas G is hardly generated, the control valve 35a of the gas feed pipe 31a is appropriately controlled, for example.

これにより、脱臭発電装置20(20a〜20c)には、常に略一定の臭気ガスGが送気されるように調整される。
そして、臭気ガスGは、脱臭発電装置20の燃焼機関21に燃料とともに供給され、燃焼機関21によって、燃焼され脱臭されることで、排気ガスYとされる。なお、排気ガスYは、不図示の触媒等を介してクリーンガスとされた後、有機廃棄物処理システムSの外部に排気される。
そして、脱臭発電装置20において発電された電力Eは、例えば、有機廃棄物処理システムSの攪拌機13、電気ヒータ14、給気ブロア16及び排風ブロア34等に送られ消費される。
Thereby, it adjusts so that the substantially constant odor gas G may always be sent to the deodorizing electric power generation apparatus 20 (20a-20c).
The odor gas G is supplied to the combustion engine 21 of the deodorizing power generation apparatus 20 together with the fuel, and is burned and deodorized by the combustion engine 21, so that the exhaust gas Y is obtained. The exhaust gas Y is made clean gas via a catalyst (not shown) and then exhausted to the outside of the organic waste treatment system S.
Then, the electric power E generated in the deodorizing power generation apparatus 20 is sent to and consumed by, for example, the stirrer 13, the electric heater 14, the air supply blower 16, and the exhaust air blower 34 of the organic waste treatment system S.

このように、本実施形態に係る有機廃棄物処理システムSの運転方法においては、複数の堆肥化装置10から脱臭発電装置20に送られる臭気ガスGの流量を略一定に制御することができる。このため、堆肥化装置10を大容量化した場合でも、必要最低限の処理能力を備える脱臭発電装置20を用意すればよいこととなる。
すなわち、脱臭発電装置20の臭気ガスGの処理能力を、複数の堆肥化装置10からの臭気ガスGの合計発生量に対応させる必要はなくなる。これにより、設備コストの上昇を最低限度に抑えることができる。
Thus, in the operating method of the organic waste treatment system S according to the present embodiment, the flow rate of the odor gas G sent from the plurality of composting apparatuses 10 to the deodorizing power generation apparatus 20 can be controlled to be substantially constant. For this reason, even when the capacity of the composting apparatus 10 is increased, it is only necessary to prepare the deodorizing power generation apparatus 20 having a necessary minimum processing capacity.
That is, it is not necessary to make the processing capacity of the odor gas G of the deodorizing power generation apparatus 20 correspond to the total amount of odor gas G generated from the plurality of composting apparatuses 10. Thereby, the raise of an installation cost can be suppressed to the minimum.

図4は、堆肥化装置10(コンポスト11)の合計容量に対する脱臭発電装置20の設置台数の関係を示す図である。
従来の有機廃棄物処理システムでは、堆肥化装置10のコンポスト11の合計容量を増大させた場合には、その増加率に合わせて脱臭発電装置20の台数も増やす必要があった。例えば、コンポスト11の合計容量が2倍(発生する最大臭気ガス量が2倍)となった場合には、脱臭発電装置20の台数も約2倍にする必要があった。
一方、本実施形態の有機廃棄物処理システムSにおいては、コンポスト11の合計容量が2倍となった場合であっても、発生する最大臭気ガス量は2倍とはならないので、脱臭発電装置20の台数を2倍にする必要はない。例えば、コンポスト11の合計容量を、20m2(10m2×2台)から40m2(20m2×2台)にした場合には、脱臭発電装置20の台数を2台から3台(1.5倍の台数)に増やすだけで対応可能である。
このように、有機廃棄物処理システムSにおいては、堆肥化装置10の容量を増大させたとしても、脱臭発電装置20の台数増加を最低限度に抑えることができる。
FIG. 4 is a diagram showing the relationship of the number of installed deodorizing power generation apparatuses 20 with respect to the total capacity of the composting apparatus 10 (compost 11).
In the conventional organic waste treatment system, when the total capacity of the compost 11 of the composting apparatus 10 is increased, it is necessary to increase the number of deodorizing power generation apparatuses 20 in accordance with the increase rate. For example, when the total capacity of the compost 11 is doubled (the maximum amount of generated odor gas is doubled), the number of deodorizing power generation apparatuses 20 needs to be doubled.
On the other hand, in the organic waste treatment system S of the present embodiment, even if the total capacity of the compost 11 is doubled, the generated maximum odor gas amount is not doubled. There is no need to double the number of units. For example, when the total capacity of the compost 11 is changed from 20 m2 (10 m2 × 2 units) to 40 m2 (20 m2 × 2 units), the number of deodorizing power generation devices 20 is increased from 2 to 3 (1.5 times the number). It is possible to cope with it simply by increasing it.
Thus, in the organic waste treatment system S, even if the capacity of the composting apparatus 10 is increased, the increase in the number of deodorizing power generation apparatuses 20 can be suppressed to the minimum.

以上、図面を参照しながら本発明に係る有機廃棄物処理システム及び方法の好適な実施形態について説明したが、本発明は上記実施形態に限定されないことは言うまでもない。上述した実施形態において示した各構成部材の諸形状や組み合わせ等は一例であって、本発明の主旨から逸脱しない範囲において設計要求等に基づき種々変更可能である。   As mentioned above, although preferred embodiment of the organic waste disposal system and method concerning this invention was described referring drawings, it cannot be overemphasized that this invention is not limited to the said embodiment. Various shapes, combinations, and the like of the constituent members shown in the above-described embodiments are examples, and various modifications can be made based on design requirements and the like without departing from the gist of the present invention.

例えば、図5に示すように、脱臭発電装置20からの廃熱H(燃焼機関21のラジエター廃熱)を利用して空気Xを加熱し、その加熱空気をエア送管50及び送風管15を介して堆肥化装置10(コンポスト11)に導入することで、畜糞Fの醗酵を促進するようにしてもよい。これにより、電気ヒータ14を用いなくとも、畜糞Fの醗酵を促進することができる。また、堆肥化装置10のランニングコストを低減することができる。
この際、脱臭発電装置20から堆肥化装置10a,10bへの送風管15に制御弁52a,52bを設け、この制御弁52a,52bの開閉を堆肥化装置10a,10bにおける畜糞Fの醗酵サイクルに対応させることが好ましい。すなわち、畜糞Fの醗酵を促進したい堆肥化装置10にのみ加熱空気が送られるように制御弁52a,52bを約12時間毎に交互に開閉する。
なお、制御弁52a,52bの開閉と制御弁35a,35bの開閉とは、必ずしも同時期である必要はなく、制御弁52a,52bは、醗酵サイクルの初期段階(例えば畜糞Fの投入から12時間まで)において開放されるようにすることが好ましい。
For example, as shown in FIG. 5, the air X is heated using waste heat H (radiator waste heat of the combustion engine 21) from the deodorizing power generation device 20, and the heated air is sent to the air feed pipe 50 and the blower pipe 15. It may be made to promote fermentation of livestock feces F by introducing into composting device 10 (compost 11). Thereby, even if it does not use the electric heater 14, fermentation of livestock feces F can be accelerated | stimulated. Moreover, the running cost of the composting apparatus 10 can be reduced.
At this time, the control valves 52a and 52b are provided in the blower pipe 15 from the deodorizing power generation apparatus 20 to the composting apparatuses 10a and 10b, and the opening and closing of the control valves 52a and 52b is used for the fermentation cycle of livestock feces F in the composting apparatuses 10a and 10b. It is preferable to make it correspond. That is, the control valves 52a and 52b are alternately opened and closed about every 12 hours so that the heated air is sent only to the composting apparatus 10 that wants to promote the fermentation of livestock feces F.
Note that the opening and closing of the control valves 52a and 52b and the opening and closing of the control valves 35a and 35b are not necessarily in the same period, and the control valves 52a and 52b are in the initial stage of the fermentation cycle (for example, 12 hours from the introduction of the livestock feces F). It is preferable to be opened at (1).

上述した実施形態では、堆肥化装置10を2台設けた場合について説明したが、それ以上であってもよい。この場合には、各堆肥化装置10の発酵サイクルを約12時間毎にずらす場合に限らない。3台の場合には、発酵サイクルを約8時間毎にずらすようにしてもよい。
また、上述した実施形態では、各堆肥化装置10の発酵サイクルが約24時間の場合について説明したが、これは一例であって、24時間よりも短い場合や長い場合であってもよい。
In the above-described embodiment, the case where two composting apparatuses 10 are provided has been described. In this case, it is not restricted to shifting the fermentation cycle of each composting apparatus 10 about every 12 hours. In the case of three units, the fermentation cycle may be shifted about every 8 hours.
Moreover, although embodiment mentioned above demonstrated the case where the fermentation cycle of each composting apparatus 10 was about 24 hours, this is an example, Comprising: The case where it is shorter or longer than 24 hours may be sufficient.

本実施形態に係る有機廃棄物処理システムSの概略構成を示す図である。It is a figure which shows schematic structure of the organic waste processing system S which concerns on this embodiment. 堆肥化装置10の概略構成を示した図である。It is the figure which showed schematic structure of the composting apparatus. 有機廃棄物処理システムSの運転方法を説明するための図である。It is a figure for demonstrating the operating method of the organic waste disposal system. 堆肥化装置10の合計容量に対する脱臭発電装置20の設置台数の関係を示す図である。It is a figure which shows the relationship of the installation number of the deodorizing electric power generation apparatus 20 with respect to the total capacity | capacitance of the composting apparatus. 有機廃棄物処理システムSの変形例を示す概略構成図である。It is a schematic block diagram which shows the modification of the organic waste disposal system.

符号の説明Explanation of symbols

S…有機廃棄物処理システム
F…畜糞
X…空気
G…臭気ガス
Y…排気ガス
H…廃熱
10(10a,10b)…堆肥化装置
11(11a,11b)…コンポスト
20…脱臭発電装置
21…燃焼機関
22…発電機
30…ガス送管
31(31a,31b)…ガス送管
32…ガス送管
33(33a〜33c)…ガス送管
34…排風ブロア
35(35a,35b)…制御弁
40…制御装置
42(42a,42b)…温度センサ
50…エア送管
52a,52b…制御弁



S ... Organic waste treatment system F ... Livestock excrement X ... Air G ... Odor gas Y ... Exhaust gas H ... Waste heat 10 (10a, 10b) ... Composting device 11 (11a, 11b) ... Compost 20 ... Deodorizing power generation device 21 ... Combustion engine 22 ... Generator 30 ... Gas feed pipe 31 (31a, 31b) ... Gas feed pipe 32 ... Gas feed pipe 33 (33a-33c) ... Gas feed pipe 34 ... Exhaust air blower 35 (35a, 35b) ... Control valve DESCRIPTION OF SYMBOLS 40 ... Control apparatus 42 (42a, 42b) ... Temperature sensor 50 ... Air feed pipe 52a, 52b ... Control valve



Claims (4)

コンポスト容器内において有機廃棄物を発酵させて堆肥化する複数の堆肥化装置と、
前記複数の堆肥化装置から発生する臭気ガスを燃料とともに燃焼して、脱臭及び発電を行う複数の脱臭発電装置と、
を有する有機廃棄物処理方法システムの運転方法において、
前記有機廃棄物の投入時期を前記複数の堆肥化装置毎に異ならせて臭気ガスの最大発生時を分散化させると共に、
前記複数の堆肥化装置における臭気ガスの発生状態に応じて臭気ガスの送気量を前記複数の堆肥化装置毎に異ならせて前記複数の堆肥化装置から前記脱臭発電装置に向けて送気する臭気ガスの量を一定量に制御し、
前記脱臭発電装置において発生した熱量を用いて加熱した空気を前記複数の堆肥化装置に導入することを特徴とする有機廃棄物処理方法システムの運転方法。
A plurality of composting devices that ferment and compost organic waste in a compost container ;
A plurality of deodorizing power generation devices for performing deodorization and power generation by burning odorous gas generated from the plurality of composting devices together with fuel;
In the operation method of the organic waste treatment method system having
The poured timing of organic waste made different for each of the plurality of composting apparatus dispersing the time of maximum occurrence of odorous gas Rutotomoni,
Supplying air toward the air supply amount of odorous gas from said plurality of composting device of the plurality of composting apparatus made different for each said deodorizing power generating device according to the occurrence state of odorous gases in the plurality of composting device Control the amount of odor gas to a certain amount,
An operating method of an organic waste treatment method system, wherein air heated using an amount of heat generated in the deodorizing power generation device is introduced into the plurality of composting devices .
前記複数の堆肥化装置に対する前記有機廃棄物の投入時期は、前記有機廃棄物の発酵サイクル時間を前記複数の堆肥化装置の台数分に分けた時間に基づいて規定されることを特徴とする請求項1に記載の有機廃棄物処理方法システムの運転方法。 The input timing of the organic waste to the plurality of composting apparatuses is defined based on a time obtained by dividing the fermentation cycle time of the organic waste into the number of the plurality of composting apparatuses. Item 4. A method for operating the organic waste treatment method system according to Item 1. 前記複数の堆肥化装置における臭気ガスの発生状態は、前記コンポスト容器内の温度に基づいて判断されることを特徴とする請求項1又は請求項2に記載の有機廃棄物処理方法システムの運転方法。 The operating state of the organic waste treatment method system according to claim 1 or 2, wherein the generation state of odor gas in the plurality of composting apparatuses is determined based on a temperature in the compost container . . 堆肥化を進行させるべき堆肥化装置に対して前記加熱した空気を導入することを特徴とする請求項1から請求項3のうちいずれか一項に記載の有機廃棄物処理方法システムの運転方法。 The operating method of the organic waste processing method system according to any one of claims 1 to 3 , wherein the heated air is introduced into a composting apparatus that is to proceed with composting .
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