JP2017205767A - Landfill treatment method of organic waste and pretreatment facility of organic waste - Google Patents

Landfill treatment method of organic waste and pretreatment facility of organic waste Download PDF

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JP2017205767A
JP2017205767A JP2017169306A JP2017169306A JP2017205767A JP 2017205767 A JP2017205767 A JP 2017205767A JP 2017169306 A JP2017169306 A JP 2017169306A JP 2017169306 A JP2017169306 A JP 2017169306A JP 2017205767 A JP2017205767 A JP 2017205767A
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organic waste
pretreatment
facility
waste
equipment
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太郎 滝本
Taro Takimoto
太郎 滝本
堀井 安雄
Yasuo Horii
安雄 堀井
誠 奥野
Makoto Okuno
誠 奥野
貴雄 楠田
Takao Kusuda
貴雄 楠田
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Kubota Environmental Service Co Ltd
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Abstract

PROBLEM TO BE SOLVED: To provide an inexpensive landfill treatment method of organic wastes capable of effectively shortening a period from closure to disuse of a controlled final disposal site.SOLUTION: In a landfill treatment method of organic wastes including a pretreatment step for performing biological treatment by air-diffusing and water-sprinkling to the organic wastes and a landfill step for performing the landfill treatment of the organic wastes after the pretreatment step, the completion of the pretreatment step is determined by a leachate measurement step for measuring the BOD and COD of the leachate collected from the organic wastes in the pretreatment step, a temperature measurement step for measuring the temperature of the organic wastes, and a completion determination step for performing the completion determination of the pretreatment step based on a BOD/COD ratio calculated from a measured result in the leachate measurement step, and the temperature of the organic wastes measured in the temperature measurement step.SELECTED DRAWING: Figure 3

Description

本発明は、有機性廃棄物の埋立処理方法及び前処理設備に関する。 The present invention relates to an organic waste landfill treatment method and pretreatment equipment .

最終処分場は、閉鎖つまり埋立終了した後、「一般廃棄物の最終処分及び産業廃棄物の最終処分に係る技術上の基準を定める命令」で法定された廃止基準を満たすことによって廃止することができる。   The final disposal site may be abolished after closing or landfilling and meeting the abolition standards stipulated by the “Order for Establishing Technical Standards for Final Disposal of General Waste and Final Disposal of Industrial Waste” it can.

しかし、浸出水等についての廃止基準は非常に厳しく、最終処分場の閉鎖から廃止までに要する期間が長期に渡ると、その期間の維持管理費の増大や跡地利用の制限等の問題が生じる。   However, the standards for abolition of leachate etc. are very strict, and if the period required from closure of the final disposal site to abolition is long, problems such as an increase in maintenance costs and restrictions on use of the site will arise during that period.

そこで、特許文献1には、最終処分場を閉鎖してから廃止するまでの期間を短縮するために、廃棄物層に空気を送り込んで、微生物による易分解性有機物の分解を促進させ、BODとCODとが廃止基準Aに達するまで、酸化剤を複数回に分けて廃棄物層に注入する最終処分場の廃止時期短縮方法が提案されている。   Therefore, in Patent Document 1, in order to shorten the period from the closing of the final disposal site until it is abolished, air is sent to the waste layer to promote the decomposition of easily decomposable organic substances by microorganisms, and BOD and Until the COD reaches the decommissioning standard A, a method for shortening the decommissioning time of the final disposal site in which the oxidizing agent is divided into a plurality of times and injected into the waste layer has been proposed.

また、特許文献2には、埋立前に廃棄物を機械的に洗浄することで、廃棄物に含まれる有機物や塩類を洗い出して廃棄物を安定化する方法や、埋立前に廃棄物に散水および通気して、廃棄物中の有機物や塩類、重金属等を洗い出し、或いは不溶化する方法が示されている。   Patent Document 2 discloses a method of stabilizing waste by washing organic matter and salts contained in the waste by mechanically washing the waste before landfill, A method is shown in which aeration is performed to wash out or insolubilize organic matter, salts, heavy metals, and the like in waste.

特開2005−224674号公報JP 2005-224673 A 特開2009−241053号公報JP 2009-241053 A

しかし、特許文献1に記載された方法を採用する場合、最終処分場に厚く埋立した廃棄物層に一様に空気を供給するのは容易ではないため、十分な給気設備を構築しない限り、廃止時期を効果的に短縮できないという問題があった。   However, when adopting the method described in Patent Document 1, it is not easy to uniformly supply air to the waste layer thickly landfilled at the final disposal site, so unless sufficient air supply equipment is constructed, There was a problem that the abolition time could not be shortened effectively.

また、特許文献2に記載された方法を採用する場合、廃棄物を最終処分場に搬入する前に外部で前処理する必要があり、前処理設備を構築する敷地の確保難という問題ばかりでなく、前処理によって発生する排水等を処理するための水処理設備等の費用が嵩むという問題があり、容易に前処理することができなかった。   In addition, when adopting the method described in Patent Document 2, it is necessary to pre-process waste before carrying it into the final disposal site, and not only the problem of securing a site for constructing pre-treatment facilities However, there is a problem that the cost of water treatment equipment for treating waste water generated by the pretreatment is increased, and the pretreatment cannot be easily performed.

そのため、現状、廃棄物は前処理されることなく最終処分場で直接埋立処理されている。特に最終処分場に搬入された有機性廃棄物、例えば熱灼減量が15%以上で括られる有機性汚泥は、通気性及び通水性が悪く、埋立層内で団粒構造となって内部が嫌気化し、BOD,COD,T−N等の発生源となり、浸出水処理設備への原水の水質悪化をもたらし、最終処分場の廃止時期の短縮の阻害要因となっている。このような有機性廃棄物には、有機性汚泥に限らず熱灼減量が15%未満の無機性汚泥や僅かでも有機物が含まれる焼却灰等が含まれる。   Therefore, at present, waste is directly landfilled at the final disposal site without being pretreated. In particular, organic waste brought to the final disposal site, for example, organic sludge with a thermal loss reduction of 15% or more, has poor air permeability and water permeability, and has an aggregate structure in the landfill layer, making the inside anaerobic It becomes a generation source of BOD, COD, TN, etc., brings about deterioration of the quality of raw water to the leachate treatment facility, and hinders the shortening of the abolition time of the final disposal site. Such organic waste includes not only organic sludge but also inorganic sludge having a thermal loss of less than 15%, incinerated ash containing even a small amount of organic matter, and the like.

本発明の目的は、上述した問題点に鑑み、特段の専用の敷地が確保できない場合であっても、管理型の最終処分場の閉鎖から廃止までの期間を効果的に短縮することができる安価な有機性廃棄物の埋立処理方法及び前処理設備を提供する点にある。 In view of the above-described problems, the object of the present invention is a low cost that can effectively shorten the period from closure to closure of a managed final disposal site even when a special dedicated site cannot be secured. It is the point which provides the landfill processing method and pre-processing equipment of an organic waste.

上述の目的を達成するため、本発明による有機性廃棄物の埋立処理方法の第一特徴構成は、特許請求の範囲の請求項1に記載した通り、有機性廃棄物の埋立処理方法であって、有機性廃棄物に散気及び散水して生物処理する前処理ステップと、前記前処理ステップの後に有機性廃棄物を埋立処理する埋立ステップと、を含み、前記前処理ステップの終了を、前記前処理ステップで有機性廃棄物から採取した浸出水のBOD及びCODを測定する浸出水測定ステップと、有機性廃棄物の温度を測定する測温ステップと、前記浸出水測定ステップの測定結果から求まるBOD/COD比と、前記測温ステップで測定された有機性廃棄物の温度とに基づいて前記前処理ステップの終了判定を行なう終了判定ステップと、により決定する点にある。 To achieve the above object, a first characteristic feature of the landfill method of the organic waste according to the present invention, as described in claim 1 of the appended claims, a landfill method of the organic waste A pretreatment step for performing biological treatment by aeration and sprinkling of organic waste, and a landfill step for landfilling organic waste after the pretreatment step, and ending the pretreatment step, It is obtained from the measurement result of the leachate measurement step for measuring the BOD and COD of leachate collected from the organic waste in the pretreatment step, the temperature measurement step for measuring the temperature of the organic waste, and the measurement result of the leachate measurement step. a BOD / COD ratio lies in that determined by the termination determination step that determines the termination of the pretreatment step on the basis of the temperature of the organic waste that is measured by the temperature measuring step.

前処理ステップで生物処理が進むと有機性廃棄物の温度が上昇し、易分解性有機物が主体のBODは次第に低下するが、難分解性有機物が主体のCODはそれほどには低下しない。しかし、良好な好気性条件下で生物処理が進むと難分解性有機物が次第に分解されてCODが低下し、それに伴って有機性廃棄物の温度も低下する。そこで、浸出水測定ステップを実行して、定期的に浸出水のBOD及びCODを測定してBOD/COD比を算出するとともに、測温ステップで有機性廃棄物の温度を測定することにより、前処理の進捗の程度を把握することができる。終了判定ステップでは、浸出水のBOD/COD比と有機性廃棄物の温度に基づいて、難分解性有機物の分解の程度が把握され、予め設定された値に達すると前処理ステップを終了して、当該有機性廃棄物を最終的に埋立処理することができるようになる。When the biological treatment proceeds in the pretreatment step, the temperature of the organic waste rises and the BOD mainly composed of easily degradable organic substances gradually decreases, but the COD mainly composed of hardly decomposable organic substances does not decrease so much. However, when the biological treatment proceeds under good aerobic conditions, the hardly decomposable organic matter is gradually decomposed to reduce the COD, and the temperature of the organic waste is also lowered accordingly. Therefore, by performing the leachate measurement step, periodically measuring the BOD and COD of the leachate to calculate the BOD / COD ratio, and measuring the temperature of the organic waste in the temperature measurement step, The degree of processing progress can be grasped. In the end determination step, the degree of decomposition of the hardly decomposable organic matter is grasped based on the BOD / COD ratio of the leachate and the temperature of the organic waste, and when the preset value is reached, the pretreatment step is ended. The organic waste can finally be landfilled.

同第二の特徴構成は、同請求項2に記載した通り、上述の第一の特徴構成に加えて、前記終了判定ステップは、BOD/COD比が略1となり、有機性廃棄物の温度と外気の温度の温度差が20度以内になったときに、前記前処理ステップが終了したと判定する点にある。 In the second feature configuration, as described in claim 2, in addition to the first feature configuration described above, the end determination step has a BOD / COD ratio of approximately 1, and the temperature of the organic waste When the temperature difference between the outside air temperatures is within 20 degrees, it is determined that the preprocessing step is completed.

浸出水のBOD/COD比が略1になり、有機性廃棄物と外気の温度差が20度以内になったときに前処理が終了したと適切に判定できるようになる。When the BOD / COD ratio of the leachate becomes approximately 1, and the temperature difference between the organic waste and the outside air is within 20 degrees, it can be appropriately determined that the pretreatment has been completed.

本発明による有機性廃棄物の前処理設備の第一の特徴構成は、同請求項3に記載した通り、上述の第一または第二の特徴構成を備えた有機性廃棄物の埋立処理方法を実行するための有機性廃棄物の前処理設備であって、埋立処理前の有機性廃棄物を載置する載置設備と、前記載置設備に載置された有機性廃棄物に散気及び散水して生物処理するための散気設備と散水設備とを備えている点にある。The first characteristic configuration of the organic waste pretreatment facility according to the present invention is the organic waste landfill processing method having the first or second characteristic configuration described above. An organic waste pretreatment facility for carrying out the process, wherein the organic waste before the landfill treatment is placed on the organic waste placed on the placement equipment It is in the point provided with the aeration equipment and watering equipment for sprinkling water and treating it.

載置設備に載置された有機性廃棄物に、散水設備によって水分が供給されるとともに散気設備によって空気が供給されることによって、好気性環境下で微生物による有機物の予備的な分解処理が促進される。この良好な好気性環境によって効率的に難分解性有機物が易分解性有機物に分解されるようになり、最終処分場に埋め立てられた廃棄物に含まれる有機物が分解されるまでの時間が大幅に短縮されるようになる。Preliminary decomposition treatment of organic matter by microorganisms is performed in an aerobic environment by supplying moisture to the organic waste placed on the mounting equipment by the watering equipment and supplying air by the air diffusion equipment. Promoted. This good aerobic environment efficiently decomposes difficult-to-decompose organic matter into easily-decomposable organic matter, and greatly increases the time until the organic matter contained in the waste landfilled at the final disposal site is decomposed. It will be shortened.

して、散水によって廃棄物に含まれる浮遊性有機物や塩分等が洗い出しにより予め除去されるので、最終処分場に埋め立てられた廃棄物からの浸出水の汚濁の程度も改善され、最終処分場を閉鎖してから廃止するまでの期間を効果的に短縮できるようになる。 Their to, stray organic matter and salt or the like contained in the waste by water spray is previously removed by washing out, the degree of contamination of the leachate from the waste that is buried in landfills also be improved, the final disposal site It becomes possible to effectively shorten the period from closing to abolition.

同第二の特徴構成は、同請求項4に記載した通り、上述の第一の特徴構成に加えて、前記載置設備は、地表の一区画を仕切るように掘削された領域に一体に形成された側壁及び床版と、前記床版に配設される前記散気設備としての通気管を覆う通気部材とを備えて構成され、前記通気部材の上層に前記有機性廃棄物が載置されるように構成されている点にある。 In the second characteristic configuration, as described in claim 4, in addition to the first characteristic configuration described above, the installation equipment is integrally formed in a region excavated so as to partition a section of the ground surface. A side wall and a floor slab, and a ventilation member that covers a ventilation pipe as the air diffusion equipment disposed on the floor slab, and the organic waste is placed on an upper layer of the ventilation member. It is in the point which is constituted so that.

地表が掘削された一区画に側壁及び床版が一体に形成され、床版の上に散気設備としての通気管が配置され、その通気管が通気部材で覆われて載置設備が構築される。通気部材の上方に載置された有機性廃棄物及び種菌担持体には、通気管から供給された散気用空気が通気部材を介して一様に供給され、仮に有機性廃棄物が湿潤で通気のための抵抗が大きい場合でも、散気された空気は床版を通過して地中にリークするようなことなく有機性廃棄物に適切に供給され、円滑に生物処理が進むようになる。A side wall and a floor slab are integrally formed in a section where the ground surface is excavated, and a ventilation pipe as a diffuser is arranged on the floor slab, and the ventilation pipe is covered with a ventilation member to construct a mounting equipment. The The organic waste and inoculum support placed above the ventilation member are uniformly supplied with the air for aeration supplied from the ventilation pipe through the ventilation member, so that the organic waste is wet. Even when the resistance to ventilation is high, the diffused air is properly supplied to organic waste without passing through the floor slab and leaking into the ground, and the biological treatment proceeds smoothly. .

以上説明した通り、本発明によれば、特段の専用の敷地が確保できない場合であっても、管理型の最終処分場の閉鎖から廃止までの期間を効果的に短縮することができる安価な有機性廃棄物の埋立処理方法及び前処理設備を提供することができるようになった。 As described above, according to the present invention, even when a special dedicated site cannot be secured, an inexpensive organic material that can effectively shorten the period from the closure to the abolition of a managed final disposal site. It has become possible to provide a landfill treatment method and pretreatment equipment for radioactive waste.

最終処分場の説明図Illustration of final disposal site (a)は最初に前処理設備が設置される最終処分場の平面図、(b)は同断面図、(c)は前処理設備が移設された最終処分場の平面図、(d)は同断面図、(e)はさらに前処理設備が移設された最終処分場の平面図、(f)は同断面図(A) is a plan view of the final disposal site where the pretreatment facility is first installed, (b) is a cross-sectional view thereof, (c) is a plan view of the final disposal site where the pretreatment facility is relocated, and (d) is a plan view of the final disposal site. The same sectional view, (e) is a plan view of the final disposal site where the pretreatment facility has been relocated, and (f) is the sectional view (a)、(b)は前処理設備の第一の実施形態の説明図(A), (b) is explanatory drawing of 1st embodiment of pre-processing equipment. 前処理設備に付随する設備の説明図Explanatory drawing of equipment attached to pretreatment equipment 掘削型の前処理設備の断面図Cross section of drilling type pretreatment equipment (a)〜(d)は通気管3Aの配管説明図(A)-(d) is piping explanatory drawing of 3 A of ventilation pipes. (a)〜(f)は前処理設備を構成する載置設備の平面形状の説明図(A)-(f) is explanatory drawing of the planar shape of the mounting equipment which comprises pre-processing equipment.

以下、本発明による埋立処理方法及び前処理設備の実施形態を説明する。
図1には、クローズドタイプ(「被覆型」とも呼ぶ。)の管理型最終処分場の構造が示されている。管理型最終処分場(以下、単に「最終処分場」と記す場合もある。)は、廃棄物の処理及び清掃に関する法律で定められる構造基準と維持管理基準に基づいて設置及び運営され、同法に定められた
1504496677862_0
の区分に従って埋立処分される。
Hereinafter, embodiments of a landfill processing method and pretreatment equipment according to the present invention will be described.
FIG. 1 shows the structure of a closed type (also referred to as “cover type”) managed final disposal site. Managed final disposal sites (hereinafter sometimes referred to simply as “final disposal sites”) are established and operated in accordance with the structural standards and maintenance management standards stipulated in the Waste Disposal and Cleaning Act. Stipulated in
1504496677862_0
Landfilled according to the classification of

管理型最終処分場100は、埋立地となる山間部の谷間や掘削地盤が堰堤101で仕切られ、埋立地の底面や斜面等にゴムシート等の難透水性の層または壁で構成される遮水工102が施され、さらに浸出水の集排水管103が敷設されている。   In the management-type final disposal site 100, the valleys and excavation grounds in the mountainous areas that are used as landfills are partitioned by dams 101, and the bottoms and slopes of the landfills are made of impervious layers or walls such as rubber sheets. A hydraulic work 102 is applied, and a leachate collecting and draining pipe 103 is laid.

堰堤101の外側に集排水管103を経由した浸出水の貯水池104が設けられ、ポンプで浸出水処理設備105に送水される。また、図には示していないが、雨水や地下水が浸出水に混入しないように、遮水工102の外側に地下水集排水管が設けられて調整池等に集水されている。   A leachate reservoir 104 is provided outside the dam 101 via a drainage pipe 103 and is fed to the leachate treatment facility 105 by a pump. Although not shown in the figure, a groundwater collection / drainage pipe is provided outside the impermeable work 102 so that rainwater and groundwater are not mixed into the leachate and collected in a regulating pond or the like.

最終処分場100は、不特定人が安易に進入できないように塀等で閉鎖されており、また埋立地から発生する様々な臭気ガスが外部に漏洩しないように、また雨水が滲入しないように被覆施設106で覆われている。被覆施設106は、鋼製の柱で骨組みが組まれ、金属製の板状体が配置されて外気と分離されている。被覆施設106の上方近傍にはガスを吸引するファン107が設けられ、ファン107で吸引されたガスは活性炭吸着装置等で臭気が除去され、無害化装置で無害化された後に大気解放される。   The final disposal site 100 is closed with eaves and the like so that unspecified people cannot enter easily, and it is covered so that various odorous gases generated from the landfill site do not leak to the outside and rainwater does not enter. Covered with facilities 106. The covering facility 106 is framed with steel columns, and a metal plate-like body is arranged to separate it from the outside air. A fan 107 that sucks gas is provided in the vicinity of the upper part of the coating facility 106, and the gas sucked by the fan 107 is deodorized by an activated carbon adsorbing device or the like, detoxified by a detoxifying device, and then released to the atmosphere.

尚、被覆施設106の構造として、ラーメン構造、アーチ構造、平面トラス構造、高剛性曲げ材と高引張強度のケーブルを組み合わせた自己釣合型のハイブリッド構造、スペースフレーム構造、シェル構造、空気支持構造、サスペンション構造等、公知の様々な支持構造が採用可能である。   In addition, the structure of the covering facility 106 includes a ramen structure, an arch structure, a flat truss structure, a self-balanced hybrid structure combining a high-rigidity bending material and a high tensile strength cable, a space frame structure, a shell structure, and an air support structure. Various known support structures such as suspension structures can be used.

トラックで搬入された有機性汚泥を含む様々な廃棄物は、敷地の端部から順に遮水工102の上に埋め立てられる。廃棄物108が一定量埋め立てられる度に覆土109が施され、さらにその上に新たな廃棄物108が埋め立てられ、上限に達すると最終覆土109が施される。   Various wastes including the organic sludge carried in by the truck are landed on the impermeable work 102 in order from the end of the site. Covering soil 109 is applied every time a certain amount of waste 108 is landfilled, and further new waste 108 is landfilled thereon, and when the upper limit is reached, final covering soil 109 is applied.

通常、このような管理型最終処分場100には、有機性汚泥、無機性汚泥、焼却灰、廃プラスチック、スラグ、コンクリートくず、ガラスくず、陶磁器くず、鉱滓、瓦礫くず等が搬入されて埋め立てられる。   Usually, such a management-type final disposal site 100 is filled with organic sludge, inorganic sludge, incinerated ash, waste plastic, slag, concrete scrap, glass scrap, ceramic scrap, slag, debris, etc. .

廃棄物108からの浸出水は、重力に従って遮水工102に達した後、遮水工102の傾斜によって浸出水集排水管103へと導かれ、浸出水集排水管103を経由して浸出水の貯水池104に導かれ、浸出水処理設備105で浄化処理された後に、下水処理場等に放流される。   The leachate from the waste 108 reaches the impermeable work 102 in accordance with gravity, and is then led to the leachate collection / drainage pipe 103 by the inclination of the impermeable work 102, and the leachate is discharged via the leachate collection / drainage pipe 103. , And after being purified by the leachate treatment facility 105, it is discharged to a sewage treatment plant or the like.

このような最終処分場100は最終覆土109が施されると閉鎖され、浸出水の性状、埋立層の温度、地盤沈降の状況等が所定の廃止基準に達するまで管理され、その後廃止される。   The final disposal site 100 is closed when the final cover 109 is applied, and is managed until the properties of the leachate, the temperature of the landfill layer, the ground subsidence condition, etc. reach predetermined abolition standards, and then abolished.

しかし、大量の有機性廃棄物が埋め立てられると、通気性が損なわれて微生物による有機物の分解が阻害され、長期にわたって廃止できない虞がある。そこで、本発明による前処理設備1が活用される。以下の説明では、有機性廃棄物とは、熱灼減量が15%以上で括られる有機性汚泥のみならず、熱灼減量が15%未満の無機性汚泥や僅かでも有機物が含まれる廃棄物をも包含する概念で使用する。   However, when a large amount of organic waste is landfilled, the air permeability is impaired and the decomposition of the organic matter by microorganisms is hindered, and there is a possibility that it cannot be abolished for a long time. Therefore, the pretreatment facility 1 according to the present invention is utilized. In the following explanation, organic waste includes not only organic sludge with a heat loss reduction of 15% or more, but also inorganic sludge with a heat loss reduction of less than 15% or waste containing a small amount of organic matter. It is used in a concept that also includes

図2(a)に示すように、最終処分場100の敷地内に前処理設備1が設置されている。当該前処理設備1は、最終処分場に埋め立てられる有機性廃棄物を生物学的に前処理する直置式の設備である。   As shown in FIG. 2A, the pretreatment facility 1 is installed in the site of the final disposal site 100. The pretreatment facility 1 is a direct installation facility that biologically pretreats organic waste landfilled in a final disposal site.

図3(a),(b)に示すように、前処理設備1は、載置設備2と、散気設備3と、散水設備4とを備えている。載置設備2は最終処分場100に設営され、埋立処理前の有機性廃棄物を種菌担持体とともに載置する設備である。散気設備3は載置設備2に載置された有機性廃棄物に散気するための設備でブロワーファンBと通気管3A等を備えている。散水設備4は載置設備2に載置された有機性廃棄物に散水するための設備で、レインガンまたは散水台車で構成され、それぞれホースを介して水源に接続されている。   As shown in FIGS. 3A and 3B, the pretreatment facility 1 includes a mounting facility 2, an air diffusion facility 3, and a watering facility 4. The placement facility 2 is a facility that is installed in the final disposal site 100 and places the organic waste before the landfill process together with the inoculum support. The diffuser facility 3 is a facility for diffusing the organic waste placed on the placement facility 2 and includes a blower fan B and a vent pipe 3A. The watering facility 4 is a facility for watering the organic waste placed on the placing facility 2 and is composed of a rain gun or a watering trolley, and each is connected to a water source via a hose.

詳述すると、載置設備2は、地表の一区画を仕切るように配置される複数の側壁部材5と、側壁部材5で仕切られた領域に配置される通気抑制部材7と通気部材6を備えて構成されている。側壁部材5として土嚢、フレキシブルコンテナバッグ、玉石を充填した蛇かご等が好適に用いられる。   More specifically, the mounting facility 2 includes a plurality of side wall members 5 arranged so as to partition a section of the ground surface, and a ventilation suppressing member 7 and a ventilation member 6 arranged in a region partitioned by the side wall member 5. Configured. As the side wall member 5, a sandbag, a flexible container bag, a snake basket filled with cobblestone, or the like is preferably used.

複数のシート状の通気抑制部材7が地表を覆うように敷設され、その上部に散気設備3としての通気管3Aが配設され、砕石等で構成される通気部材6が通気管3Aを被覆するように、側壁部材5の面一まで充填されている。通気抑制部材7は樹脂製シートを用いるのが好ましいが金属板状体を用いてもよい。   A plurality of sheet-like ventilation control members 7 are laid so as to cover the ground surface, and a ventilation pipe 3A as a diffuser 3 is disposed on the top, and a ventilation member 6 made of crushed stone or the like covers the ventilation pipe 3A. Thus, the side wall member 5 is filled to the same level. The airflow suppression member 7 is preferably a resin sheet, but may be a metal plate.

通気管3Aの管壁には多数の細孔が形成され、基端側がブロワーファンBに接続された給気管3Bに接続されている。通気管3Aは金属製パイプまたは塩化ビニル等の樹脂製パイプで構成され、フランジ接合することで所望の長さが確保されている。給気管3Bも同様に金属製パイプまたは樹脂製パイプで構成され、側壁部材5との取り合い部等ではフレキシブル管が用いられている。尚、樹脂製パイルを用いる場合には、フランジ接合に替えて接着材で接合するTS接合を採用することも可能である。   A large number of pores are formed in the pipe wall of the vent pipe 3A, and the base end side is connected to the air supply pipe 3B connected to the blower fan B. The vent pipe 3A is composed of a metal pipe or a resin pipe such as vinyl chloride, and a desired length is secured by flange joining. Similarly, the air supply pipe 3B is formed of a metal pipe or a resin pipe, and a flexible pipe is used at a joint portion with the side wall member 5 or the like. In addition, when using resin-made pile, it is also possible to employ | adopt TS joining joined with an adhesive instead of flange joining.

通気管3Aの細孔が有機性廃棄物で目詰まりしないように通気部材6が設けられ、通気管3Aから供給される空気の地中へのリークを抑制するために通気抑制部材7が配置されている。載置設備2は重機を用いて搬入され、組み立てられる。   The ventilation member 6 is provided so that the pores of the ventilation pipe 3A are not clogged with organic waste, and the ventilation suppression member 7 is arranged to suppress leakage of air supplied from the ventilation pipe 3A into the ground. ing. The mounting equipment 2 is carried in and assembled using heavy equipment.

このような載置設備2に載置された有機性廃棄物10と種菌担持体11に、散水設備4によって水分が供給されるとともに散気設備3によって空気が供給されることによって、良好な好気性環境下で微生物による有機物の予備的な分解処理が促進され、効率的に難分解性有機物が易分解性有機物に分解されるようになり、前処理後に最終処分場に埋め立てられた廃棄物に含まれる有機物が最終的に分解されるまでの時間が大幅に短縮されるようになる。   By supplying water to the organic waste 10 and the inoculum support 11 mounted on the mounting equipment 2 by the watering equipment 4 and air by the air diffusion equipment 3, a favorable condition is obtained. Preliminary decomposition treatment of organic substances by microorganisms is promoted in the aerobic environment, and the hard-to-decompose organic substances are efficiently decomposed into easily-decomposable organic substances. The time until the contained organic matter is finally decomposed is greatly reduced.

また、散水によって廃棄物に含まれる濁質性有機物や塩分等が予め除去されるので、最終処分場に埋め立てられた廃棄物からの浸出水の汚濁の程度も改善され、最終処分場を閉鎖してから廃止するまでの期間を効果的に短縮できるようになる。このような前処理設備1は最終処分場100に設営されるので、周辺住民の反発等で取得困難な前処理設備を構築するための敷地も確保する必要が無くなる。   In addition, turbid organic substances and salt contained in the waste are removed in advance by watering, so the degree of contamination of leachate from the waste landfilled in the final disposal site is improved and the final disposal site is closed. It will be possible to effectively shorten the period until it is abolished. Since such a pretreatment facility 1 is set up in the final disposal site 100, it is not necessary to secure a site for constructing a pretreatment facility that is difficult to obtain due to repulsion of neighboring residents.

載置設備2からの浸出水は、通気抑制部材7の隙間から地面に浸透して、最終処分場100の遮水工102に設けられた集排水管103を介して最終処分場100の浸出水として貯水池104に集水され、最終処分場の浸出水処理設備105で浄化処理されるようになる。つまり、載置設備2からの浸出水が最終処分場に放流されるように構成されていればよく、地中に浸透するように放流されていてもよいし、浸出水を貯水池104に導く導水路が形成されていてもよい。   The leachate from the mounting facility 2 penetrates into the ground through the gap of the ventilation control member 7 and is leached from the final disposal site 100 through the drainage pipe 103 provided in the water shielding work 102 of the final disposal site 100. The water is collected in the reservoir 104 and purified by the leachate treatment facility 105 at the final disposal site. In other words, the leachate from the mounting facility 2 may be configured to be discharged to the final disposal site, may be discharged so as to penetrate into the ground, and may be introduced to guide the leachate to the reservoir 104. A water channel may be formed.

通気部材6が側壁部材5の面一まで充填されているため、前処理が終了した有機性汚泥を載置設備2から除去する際に、側壁部材5の上端を目途にバックホーやドーザ装置等の重機を操作すればよいので、載置設備2を破損すること無く容易に作業を行なえるようになる。   Since the ventilation member 6 is filled to the same level as the side wall member 5, when removing the organic sludge after the pretreatment from the mounting equipment 2, the backhoe, the dozer device, etc. Since it is only necessary to operate the heavy machinery, the work can be easily performed without damaging the mounting equipment 2.

図4に示すように、載置設備2は、有機性廃棄物の前処理中に次に前処理する有機性廃棄物を前処理中の有機性廃棄物とは異なる領域に載置できるように複数に区画されていることが好ましく、前処理中の有機性廃棄物で育成された菌の一部が次に前処理する有機性廃棄物に種菌として供給可能に構成されていることが好ましい。   As shown in FIG. 4, the placement facility 2 can place the organic waste to be pretreated next in the area different from the organic waste being pretreated during the pretreatment of the organic waste. It is preferable to be divided into a plurality of sections, and it is preferable that a part of the bacteria grown with the organic waste being pretreated can be supplied as an inoculum to the organic waste to be pretreated next.

複数に区画された載置設備2(2A,2B)の一区画2Aに有機性廃棄物及び種菌担持体を載置して生物処理している間に、新たに搬入された有機性廃棄物を他の区画2Bに載置しておき、一区画2Aで前処理が終了するとその種菌が繁殖した有機性廃棄物を埋立地に埋め立て、その一部を他の区画2Bの有機性廃棄物に種菌として使い、区画2Aにさらに新たに搬入された有機性廃棄物を載置することで、無駄な時間が無くなり連続的に有機性廃棄物を前処理することができるようになる。初期の種菌担持体は山林等から採取した腐葉土等を用いればよく、その後は直前の前処理対象物を種汚泥として再利用できる。   While the organic waste and the inoculum support are placed on the section 2A of the sectioned installation equipment 2 (2A, 2B) and biologically treated, the newly introduced organic waste is removed. Placed in the other section 2B, when the pretreatment is completed in one section 2A, the organic waste in which the inoculum has propagated is buried in the landfill, and a part of the organic waste is inoculated into the organic waste in the other section 2B. As a result, by placing the newly introduced organic waste in the section 2A, the wasteful time is eliminated and the organic waste can be continuously pretreated. As the initial inoculum support, humus or the like collected from a forest or the like may be used, and then the immediately preceding pretreatment target can be reused as seed sludge.

上述したレインガンや散水台車にホースを介して接続される水源として、最終処分場100に設置された水処理装置である浸出水処理設備105で処理された処理水を用いることが好ましく、ポンプ等の給水設備によってレインガンや散水台車に給水されるように構成することが好ましい。   As a water source connected to the above-mentioned rain gun or sprinkler truck via a hose, it is preferable to use treated water treated in the leachate treatment facility 105 which is a water treatment device installed in the final disposal site 100, such as a pump. It is preferable that the water gun is configured to supply water to a rain gun or a watering truck.

水処理装置105で処理された処理水は、下水処理場に放流可能な程度に浄化されているため、前処理設備での有機性廃棄物の洗浄や湿潤状態の維持に好適に用いることができ、上水の使用量を抑制することができる。   The treated water treated by the water treatment device 105 is purified to such an extent that it can be discharged into a sewage treatment plant, and therefore can be suitably used for cleaning organic waste in a pretreatment facility and maintaining a wet state. The amount of clean water used can be suppressed.

上述したように、最終処分場100は外気遮断型であるので、前処理設備1で発生するガスを処理するための別途の装置を設ける必要が無い。   As described above, since the final disposal site 100 is an outside air blocking type, it is not necessary to provide a separate device for processing the gas generated in the pretreatment facility 1.

図4に示すように、前処理設備1(載置設備2)の近傍に、複数種の廃棄物を種類ごとに収容する廃棄物収容設備20と、前処理前の有機性廃棄物に何れかの廃棄物を混合する混合設備30と、トラックで搬入された廃棄物を受け入れる展開検査場40が設けられていることが好ましい。   As shown in FIG. 4, either the waste storage facility 20 for storing a plurality of types of wastes for each type or the organic waste before the pretreatment in the vicinity of the pretreatment facility 1 (mounting facility 2). It is preferable that a mixing facility 30 for mixing the waste and a development inspection place 40 for receiving the waste carried in the truck are provided.

トラックで搬入された廃棄物が有機性汚泥以外の適法な廃棄物である場合には、搬入された廃棄物は展開検査場40に投下されて、予め区分けされた廃棄物収容設備20に種類毎に区分けしてストックされる。廃棄物収容設備20は、例えば、焼却灰の収容部、廃プラスチックの収容部、スラグやコンクリートくずの収容部、ガラスくずや陶磁器くずの収容部等に区分けされている。   When the waste carried in the truck is a legal waste other than organic sludge, the carried-in waste is dropped into the development inspection site 40, and is sorted into the waste storage equipment 20 classified in advance. Stocked in two categories. The waste storage facility 20 is divided into, for example, an incineration ash storage section, a waste plastic storage section, a slag and concrete scrap storage section, a glass scrap and a ceramic scrap storage section, and the like.

トラックで搬入された廃棄物が有機性汚泥である場合に、展開検査場40に投下された有機性汚泥は、重機を用いて混合設備30で廃プラスチックやスラグやコンクリートくずと混合された後に、載置設備2に載置される。載置設備2に載置される廃棄物の体積が過大にならないよう、混合する廃棄物量の量は体積比で20%以下であることが好ましい。   When the waste carried in the truck is organic sludge, the organic sludge dropped on the development inspection site 40 is mixed with waste plastic, slag and concrete scraps in the mixing facility 30 using heavy equipment. It is mounted on the mounting facility 2. It is preferable that the amount of waste to be mixed is 20% or less in volume ratio so that the volume of waste placed on the placement facility 2 does not become excessive.

最終処分場に持ち込まれる有機性汚泥に、それ以外の他の廃棄物、例えば焼却灰、廃プラスチック、スラグ、コンクリートくず、ガラスくず、陶磁器くず、鉱滓、瓦礫くず等を混合した後に前処理すれば、仮に含水率の高い有機性汚泥等であっても前処理設備1で前処理される際に通気性及び通水性が確保されるようになるので前処理が促進され、埋立後であっても、一様に生物処理が進行するようになる。このような他の廃棄物は元々最終処分場に埋め立てられるものであるため、これらによって最終処分場の埋立容量が減容化されるということもない。   If organic sludge brought to the final disposal site is mixed with other waste such as incineration ash, waste plastic, slag, concrete scrap, glass scrap, ceramic scrap, slag, debris scrap, etc. Even if it is organic sludge with a high water content, pretreatment is promoted when pretreatment is performed in the pretreatment facility 1, so that pretreatment is promoted and even after landfill. The biological treatment will progress uniformly. Since such other waste is originally landfilled in the final disposal site, it does not reduce the landfill capacity of the final disposal site.

尚、廃棄物収容設備20、混合設備30及び展開検査場40を前処理設備1の近傍に設置して、前処理設備1の移設とともに移設することが困難な場合には、埋立領域以外のスペースに固定設置し、混合設備30で混合された後の有機性廃棄物が重機で前処理設備1まで搬送されるように構成してもよい。   In addition, when it is difficult to install the waste storage facility 20, the mixing facility 30, and the development inspection site 40 in the vicinity of the pretreatment facility 1 and relocate the pretreatment facility 1, a space other than the landfill area The organic waste after being fixedly installed and mixed in the mixing facility 30 may be transported to the pretreatment facility 1 by a heavy machine.

さらに、有機性汚泥等有機性廃棄物の含水率が約85%よりも高い場合には、pHに影響を与えることがないヤシ殻系の水分調整剤で含水率を下げ、生物処理時に通気性が阻害されないように調整することが好ましい。   Furthermore, when the moisture content of organic waste such as organic sludge is higher than about 85%, the moisture content is reduced with a coconut shell-type moisture regulator that does not affect the pH, and air permeability during biological treatment It is preferable to adjust so that is not inhibited.

尚、載置設備2の大きさは特に限定されることはなく、最終処分場の規模によって適宜設定すればよい。本実施形態では深さ1m程度で40m×20m角の2区画が形成されている。   In addition, the magnitude | size of the mounting equipment 2 is not specifically limited, What is necessary is just to set suitably according to the scale of the final disposal site. In the present embodiment, two sections of 40 m × 20 m square with a depth of about 1 m are formed.

前処理期間は有機性廃棄物の組成や由来によって様々であるが、数週間から十数週間の範囲である。   The pretreatment period varies depending on the composition and origin of the organic waste, but ranges from several weeks to several tens of weeks.

前処理後の有機性汚泥を効率的に埋立処理できるように、上述した前処理設備1は組立及び分解が容易に行なえるように構成されており、埋立処理の進捗に伴なって最終処分場100内での前処理設備1の設営位置が埋立処理後の領域を含めて移動可能に構成されている。   The pretreatment facility 1 described above is configured so that it can be easily assembled and disassembled so that the organic sludge after pretreatment can be efficiently landfilled. The installation position of the pretreatment facility 1 in 100 is configured to be movable including the area after the landfill process.

埋立処理後の領域に前処理設備を設営することができると、最終処分場100に前処理設備1の設営のための専用の敷地を確保する必要が無くなるので、限られた領域の最終処分場に効率的に廃棄物を埋め立てることができるようになる。尚、最終処分場100に前処理設備1の設営のための専用の敷地が確保されていてもよい。   If pre-treatment facilities can be set up in the area after landfill processing, it is not necessary to secure a dedicated site for setting up the pre-treatment equipment 1 in the final disposal site 100, so a final disposal site in a limited area It becomes possible to landfill waste efficiently. Note that a dedicated site for setting up the pretreatment facility 1 may be secured in the final disposal site 100.

図2(a)に示すように、埋立初期には廃棄物搬入路12の近傍に前処理設備1が設置され、廃棄物搬入路からトラックで搬入された廃棄物が、前処理設備1の近傍で展開され、前処理設備1の載置設備2に載置されるように構成されている。前処理設備1で前処理された有機性廃棄物は、重機によって奥側の埋立領域R1から順に埋め立てられるように搬送される。   As shown in FIG. 2 (a), the pretreatment facility 1 is installed in the vicinity of the waste carry-in path 12 at the initial stage of landfill, and the waste carried by the truck from the waste carry-in path is near the pretreatment facility 1. And is configured to be mounted on the mounting facility 2 of the pretreatment facility 1. The organic waste pretreated by the pretreatment facility 1 is transported by a heavy machine so as to be landfilled in order from the rear landfill area R1.

図2(c)に示すように、奥側の埋立領域R1が埋め立てられると、当該奥側の埋立領域R1に新たな前処理設備1が設置され、廃棄物搬入路12からトラックで搬入された廃棄物が、新たな前処理設備1の近傍で展開され、新たな前処理設備1の載置設備2に載置される。前処理設備1で前処理された有機性廃棄物は、重機によって手前側の埋立領域R2に埋め立てられるように搬送される。   As shown in FIG. 2 (c), when the backside landfill area R1 is landfilled, a new pretreatment facility 1 is installed in the backside landfill area R1 and is carried by a truck from the waste carry-in path 12 The waste is developed in the vicinity of the new pretreatment facility 1 and placed on the placement facility 2 of the new pretreatment facility 1. The organic waste pretreated by the pretreatment facility 1 is conveyed by a heavy machine so as to be buried in the landfill area R2 on the near side.

図2(e)に示すように、手前側の埋立領域R2が埋め立てられると、当該手前側の埋立領域R2に新たな前処理設備1が設置され、廃棄物搬入路からトラックで搬入された廃棄物が、新たな前処理設備1の近傍で展開され、新たな前処理設備1の載置設備2に載置される。前処理設備1で前処理された有機性廃棄物は、重機によって奥側の埋立領域R1に埋め立てられるように搬送される。このようなプロセスを繰り返すことによって、効率的に埋立処理が実行される。   As shown in FIG. 2 (e), when the landfill area R2 on the near side is landfilled, a new pretreatment facility 1 is installed in the landfill area R2 on the near side, and the waste carried in by truck from the waste carry-in path An object is developed in the vicinity of the new pretreatment facility 1 and placed on the placement facility 2 of the new pretreatment facility 1. The organic waste pretreated by the pretreatment facility 1 is transported by a heavy machine so as to be buried in the landfill area R1 on the back side. By repeating such a process, the landfill process is efficiently performed.

このような前処理設備1は、埋立作業の動線を妨げない位置に設置されることが好ましく、移設時に搬入される廃棄物の処理を継続して行えるように、移設前の前処理設備1とは異なる新たな前処理設備1を設営し、新たな前処理設備1の設営後に移設前の前処理設備1を撤去することが好ましい。   Such a pretreatment facility 1 is preferably installed at a position that does not hinder the flow of landfill work, and the pretreatment facility 1 before the relocation so that the waste carried in at the time of relocation can be continuously processed. It is preferable to set up a new pretreatment facility 1 different from that and remove the pretreatment facility 1 before the relocation after the new pretreatment facility 1 is installed.

即ち、上述した前処理設備1によって、管理型の最終処分場に埋め立てられる有機性廃棄物を生物学的に前処理する有機性廃棄物の前処理方法が実行される。   In other words, the organic waste pretreatment method for biologically pretreating the organic waste buried in the management-type final disposal site is executed by the pretreatment facility 1 described above.

具体的に、埋立処理前の有機性廃棄物を載置する載置設備と、前記載置設備に載置された有機性廃棄物に散気及び散水して予備的に生物処理するための散気設備と散水設備とを含む有機性廃棄物の前処理設備を最終処分場に設営する設営ステップと、有機性廃棄物を予備的に生物処理する前処理ステップと、前処理が終了した有機性廃棄物を埋立処理する埋立ステップとを備え、前処理ステップと埋立ステップとが繰り返される。前処理ステップでは、有機性廃棄物からの浸出水が最終処分場に放流されるように構成されることが好ましい。   Specifically, a placement facility for placing organic waste before landfill treatment, and a dispersion for preliminarily biological treatment by aeration and sprinkling of the organic waste placed on the placement facility. Organic waste pre-treatment facilities including gas facilities and sprinkling facilities at the final disposal site, pre-treatment steps for pre-biological treatment of organic waste, and organic after pre-treatment A landfill step for landfilling the waste, and the pretreatment step and the landfill step are repeated. The pretreatment step is preferably configured so that leachate from the organic waste is discharged to the final disposal site.

また、載置設備が複数の領域に区画され、一区画で有機性廃棄物を前処理しながら、他区画に次に前処理する有機性廃棄物を載置し、前処理中の有機性廃棄物で育成された菌の一部を次に前処理する有機性廃棄物に種菌として供給する種菌育成供給ステップがさらに含まれる。   In addition, the loading equipment is divided into multiple areas, and organic waste to be pretreated next is placed in another compartment while pretreating organic waste in one compartment, and organic waste being pretreated There is further included an inoculum growth and supply step of supplying a part of the bacteria grown on the product as an inoculum to the organic waste to be pretreated next.

さらに設営ステップで設営された前処理設備を解体する解体ステップをさらに含み、埋立処理の進捗に伴なって最終処分場内の異なる位置で設営ステップが再度実行され、既設の前処理設備に対して解体ステップが実行されることが好ましい。   In addition, it further includes a dismantling step for dismantling the pretreatment equipment constructed in the construction step, and the construction step is re-executed at a different location in the final disposal site as the landfilling progresses, and dismantling the existing pretreatment equipment Preferably the steps are performed.

さらにまた、前処理ステップで有機性廃棄物から採取した浸出水のBOD及びCODを測定する浸出水測定ステップと、有機性廃棄物の温度を測定する測温ステップと、前記浸出水測定ステップの測定結果から求まるBOD/COD比と、測温ステップで測定された有機性廃棄物の温度とに基づいて前処理ステップの終了判定を行なう終了判定ステップが実行されることがより好ましい。   Furthermore, the leachate measurement step for measuring BOD and COD of leachate collected from the organic waste in the pretreatment step, the temperature measurement step for measuring the temperature of the organic waste, and the measurement of the leachate measurement step It is more preferable that an end determination step for determining the end of the pretreatment step based on the BOD / COD ratio obtained from the result and the temperature of the organic waste measured in the temperature measurement step is executed.

前処理ステップで生物処理が進むと有機性廃棄物の温度が上昇し、易分解性有機物が主体のBODは次第に低下するが、難分解性有機物が主体のCODはそれほどには低下しない。しかし、良好な好気性条件下で生物処理が進むと難分解性有機物が次第に分解されてCODが低下し、それに伴って有機性廃棄物の温度も低下する。   When the biological treatment proceeds in the pretreatment step, the temperature of the organic waste rises and the BOD mainly composed of easily degradable organic substances gradually decreases, but the COD mainly composed of hardly decomposable organic substances does not decrease so much. However, when the biological treatment proceeds under good aerobic conditions, the hardly decomposable organic matter is gradually decomposed to reduce the COD, and the temperature of the organic waste is also lowered accordingly.

そこで、浸出水測定ステップを実行して、定期的に浸出水のBOD及びCODを測定してBOD/COD比を算出するとともに、測温ステップで有機性廃棄物の温度を測定することにより、前処理の進捗の程度を把握することができる。終了判定ステップでは、浸出水のBOD/COD比と有機性廃棄物の温度に基づいて、難分解性有機物の分解の程度が把握され、予め設定された値に達すると前処理ステップを終了して、当該有機性廃棄物を最終的に埋立処理することができるようになる。具体的に、浸出水のBOD/COD比が略1になり、有機性廃棄物と外気の温度差が20度以内になったときに前処理が終了したと判定することができる。   Therefore, by performing the leachate measurement step, periodically measuring the BOD and COD of the leachate to calculate the BOD / COD ratio, and measuring the temperature of the organic waste in the temperature measurement step, The degree of processing progress can be grasped. In the end determination step, the degree of decomposition of the hardly decomposable organic matter is grasped based on the BOD / COD ratio of the leachate and the temperature of the organic waste, and when the preset value is reached, the pretreatment step is ended. The organic waste can finally be landfilled. Specifically, it can be determined that the pretreatment has been completed when the BOD / COD ratio of the leachate is approximately 1, and the temperature difference between the organic waste and the outside air is within 20 degrees.

以下に本発明の前処理設備の別実施形態を説明する。
上述の実施形態では、最終処分場で移設可能な直置式の前処理設備を説明したが、移設に不向きな掘削式の前処理設備を最終処分場に設置してもよい。この場合には、埋立領域と重複しない位置であって、埋立の動線の妨げとならない位置に設置することが好ましい。
Another embodiment of the pretreatment facility of the present invention will be described below.
In the above-described embodiment, the direct-type pretreatment facility that can be transferred at the final disposal site has been described. However, an excavation type pretreatment facility that is not suitable for transfer may be installed at the final disposal site. In this case, it is preferable to install it at a position that does not overlap the landfill area and does not hinder the flow of landfill.

図5に示すように、掘削式の前処理設備1は、最終処分場の地表の一区画を仕切るように掘削された領域に一体に形成された側壁15及び床版17と、通気部材6とを備えた載置設備2と、散気設備3と、散水設備4とを備えて構成されている。   As shown in FIG. 5, the excavation type pretreatment facility 1 includes a side wall 15 and a floor slab 17 integrally formed in a region excavated so as to partition a section of the surface of the final disposal site, a ventilation member 6, and the like. Is equipped with the mounting equipment 2, the air diffusion equipment 3, and the watering equipment 4.

載置設備2の側壁15及び床版17は十分な強度を確保するために鉄筋コンクリートで構成され、床版17には浸出水を逃がすためのドレン孔18が形成されている。図3(a)と同様に、床版17には散気設備としての通気管3Aが配置され、通気管3Aを被覆する通気部材6が充填されている。   The side wall 15 and the floor slab 17 of the mounting facility 2 are made of reinforced concrete in order to ensure sufficient strength, and the floor slab 17 is formed with a drain hole 18 for allowing leachate to escape. Similar to FIG. 3A, the floor slab 17 is provided with a ventilation pipe 3A as a diffuser and filled with a ventilation member 6 that covers the ventilation pipe 3A.

載置設備2の上面に有機性廃棄物が種菌担持体とともに載置されて前処理される。床版17が非通気性のコンクリートであるため別途の通気抑制部材を設ける必要はない。また、重機による有機性廃棄物の載置作業や除去作業が容易になるように、側壁15及び通気部材6の上面は地表と略面一に構成されている。   Organic waste is placed on the upper surface of the mounting facility 2 together with the inoculum support and pretreated. Since the floor slab 17 is made of non-breathable concrete, it is not necessary to provide a separate air flow suppressing member. Further, the upper surfaces of the side wall 15 and the ventilation member 6 are substantially flush with the ground surface so that the organic waste can be easily placed and removed by heavy machinery.

持ち込まれた廃棄物を検査する展開検査場を備える場合には、廃棄物収容設備及び混合設備とともに、掘削式の前処理設備1を展開検査場の近傍に設置することが好ましく、検査が完了した廃棄物を速やかに混合して前処理設備1に載置できる。   When equipped with a deployment inspection site that inspects the waste brought in, it is preferable to install the excavated pretreatment facility 1 in the vicinity of the deployment inspection site together with the waste storage facility and the mixing facility, and the inspection has been completed. Waste can be quickly mixed and placed on the pretreatment facility 1.

散水装置4としてレインガンや散水台車に代えて、前処理設備1の近傍に設置した固定型のスプリンクラーを用いてもよい。   Instead of a rain gun or a watering cart as the watering device 4, a fixed sprinkler installed near the pretreatment facility 1 may be used.

最終処分場が外気遮断型でなく露天型である場合には、発生ガスの大気解放が許容されているため、前処理設備1に特段のガス処理設備を設置する必要はない。しかし、前処理中の有機性廃棄物に雨水が混入すると、前処理に支障を来すため、前処理設備1に覆蓋設備を設けることが好ましい。   When the final disposal site is not an outside air blocking type but an open-air type, it is not necessary to install special gas processing equipment in the pretreatment facility 1 because the released gas is allowed to be released into the atmosphere. However, if rainwater is mixed into the organic waste during the pretreatment, the pretreatment is hindered. Therefore, it is preferable to provide a cover facility in the pretreatment facility 1.

図3(a)に示した通気管3Aの構成は非常にシンプルで施工も容易であるが、通気管3Aを介して有機性廃棄物に供給される散気量は一様である必要があり、通気管3Aが受ける圧損が異なると散気量がばらついて、均質な前処理に支障を来す虞がある。   The configuration of the vent pipe 3A shown in FIG. 3A is very simple and easy to construct, but the amount of air diffused supplied to the organic waste through the vent pipe 3A needs to be uniform. If the pressure loss experienced by the vent pipe 3A is different, the amount of diffused air varies, and there is a risk of hindering homogeneous pretreatment.

そこで、載置設備に載置された有機性廃棄物に均等に散気するために様々な構成を採用することができる。例えば、図6(a)に示すように、中心点で点対称に通気管3Aを配置し、中心点に給気管3Bを接続すれば、略均等に散気できるようになる。例えば、図6(b)に示すように、給気管3Bから通気管3Aに供給される空気の供給箇所が対称となるように多点設定してもよい。   Therefore, various configurations can be adopted in order to evenly diffuse the organic waste placed on the placement facility. For example, as shown in FIG. 6A, if the vent pipe 3A is arranged point-symmetrically at the center point and the air supply pipe 3B is connected to the center point, the air can be diffused substantially evenly. For example, as shown in FIG. 6B, multiple points may be set so that the supply points of the air supplied from the supply pipe 3B to the ventilation pipe 3A are symmetrical.

また、図6(c)に示すように、給気管3Bと接続される各通気管3Aの上流側に定流量弁を設けると、各通気管3Aに供給される給気量を一定に制御できる。さらに、図6(d)に示すように、給気管3Bと接続される各通気管3Aの上流側に電磁弁を設けて、一定時間間隔で順番に一つの電磁弁のみを開放し他の電磁弁を閉塞するような制御を繰り返すと、電磁弁が開放された通気管3Aに供給される給気量が増すので通気管3Aの末端まで十分な空気を送ることができるようになる。通気管3Aをグループに分けてグループ単位で同様の制御を行なってもよい。例えば端から偶数番目の通気管3Aのグループと奇数番目の通気管3Aのグループとに分け、グループ単位で電磁弁の開閉制御を行なうような態様が例示できる。   Further, as shown in FIG. 6C, if a constant flow valve is provided upstream of each ventilation pipe 3A connected to the air supply pipe 3B, the amount of air supplied to each ventilation pipe 3A can be controlled to be constant. . Further, as shown in FIG. 6 (d), an electromagnetic valve is provided on the upstream side of each ventilation pipe 3A connected to the air supply pipe 3B, and only one electromagnetic valve is opened in order at regular time intervals, and the other electromagnetic valves are opened. If the control for closing the valve is repeated, the amount of air supplied to the vent pipe 3A with the solenoid valve opened increases, so that sufficient air can be sent to the end of the vent pipe 3A. The vent pipe 3A may be divided into groups and the same control may be performed in units of groups. For example, it is possible to exemplify a mode in which the opening / closing control of the solenoid valve is performed in units of groups by dividing into even-numbered ventilation pipes 3A groups and odd-numbered ventilation pipes 3A groups.

載置設備2の平面形状は図7(a)に示すような矩形に限るものではなく、図7(c)に示すような三角形であってもよいし、図7(e)に示すような円形であってもよい。何れの場合でも載置設備を2つの区画に区分けすれば、一方の区画で有機性廃棄物を前処理している期間に搬入された新たな有機性廃棄物を他方の区画に載置することができ、連続的に前処理を実行することができるようになる。   The planar shape of the mounting equipment 2 is not limited to the rectangle as shown in FIG. 7A, but may be a triangle as shown in FIG. 7C, or as shown in FIG. It may be circular. In any case, if the mounting equipment is divided into two sections, the new organic waste brought in during the period of pretreatment of organic waste in one section will be placed in the other section. And pre-processing can be executed continuously.

また、図7(b),(d),(f)に示すように、載置設備2を3つの区画(2A,2B,2C)に区分けしてもよく、それ以上の区画に区分してもよい。最終処分場に搬入される有機性廃棄物を段階的に前処理できるようになり、前処理作業がより効率的に行なえるようになる。   In addition, as shown in FIGS. 7B, 7D, and 7F, the mounting facility 2 may be divided into three sections (2A, 2B, 2C), or divided into more sections. Also good. Organic waste carried into the final disposal site can be pretreated in stages, so that pretreatment work can be performed more efficiently.

上述した実施形態は、何れも本発明の一例であり、該記載により本発明が限定されるものではなく、各部の具体的な構成は本発明の作用効果が奏される範囲で適宜変更設計可能であることはいうまでもない。   Each of the above-described embodiments is an example of the present invention, and the present invention is not limited by the description, and the specific configuration of each part can be appropriately changed and designed within the range where the effects of the present invention are exhibited. Needless to say.

1:前処理設備
2:載置設備
3:散気設備
3A:通気管
3B:給気管
4:散水設備
5:側壁部材
6:通気部材(砕石)
7:通気抑制部材(シート)
1: Pretreatment equipment 2: Mounting equipment 3: Aeration equipment 3A: Ventilation pipe 3B: Air supply pipe 4: Sprinkling equipment 5: Side wall member 6: Ventilation member (crushed stone)
7: Ventilation suppression member (sheet)

Claims (4)

有機性廃棄物の埋立処理方法であって、
有機性廃棄物に散気及び散水して生物処理する前処理ステップと、
前記前処理ステップの後に有機性廃棄物を埋立処理する埋立ステップと、
を含み、
前記前処理ステップの終了を、
前記前処理ステップで有機性廃棄物から採取した浸出水のBOD及びCODを測定する浸出水測定ステップと、
有機性廃棄物の温度を測定する測温ステップと、
前記浸出水測定ステップの測定結果から求まるBOD/COD比と、前記測温ステップで測定された有機性廃棄物の温度とに基づいて前記前処理ステップの終了判定を行なう終了判定ステップと、
により決定する有機性廃棄物の埋立処理方法。
A method for landfill treatment of organic waste,
A pretreatment step in which organic waste is diffused and sprinkled with water to be biologically treated;
A landfill step for landfilling organic waste after the pretreatment step;
Including
The end of the pre-processing step,
Leachate measurement step for measuring BOD and COD of leachate collected from organic waste in the pretreatment step;
A temperature measuring step for measuring the temperature of the organic waste;
An end determination step for determining the end of the pretreatment step based on the BOD / COD ratio obtained from the measurement result of the leachate measurement step and the temperature of the organic waste measured in the temperature measurement step;
Landfill treatment method for organic waste determined by
前記終了判定ステップは、BOD/COD比が略1となり、有機性廃棄物の温度と外気の温度の温度差が20度以内になったときに、前記前処理ステップが終了したと判定する請求項1記載の有機性廃棄物の埋立処理方法。The said completion | finish determination step determines with the said pre-processing step having been complete | finished when BOD / COD ratio will be substantially 1 and the temperature difference of the temperature of organic waste and the temperature of external air is less than 20 degree | times. The method for landfill treatment of organic waste according to 1. 請求項1または2記載の有機性廃棄物の埋立処理方法を実行するための有機性廃棄物の前処理設備であって、An organic waste pretreatment facility for executing the organic waste landfill treatment method according to claim 1,
埋立処理前の有機性廃棄物を載置する載置設備と、前記載置設備に載置された有機性廃棄物に散気及び散水して生物処理するための散気設備と散水設備とを備えている有機性廃棄物の前処理設備。Installation equipment for placing organic waste before landfill treatment, and aeration equipment and watering equipment for aerating and sprinkling organic waste placed on the above-mentioned placement equipment for biological treatment Equipped with organic waste pretreatment equipment.
前記載置設備は、地表の一区画を仕切るように掘削された領域に一体に形成された側壁及び床版と、前記床版に配設される前記散気設備としての通気管を覆う通気部材とを備えて構成され、前記通気部材の上層に前記有機性廃棄物が載置されるように構成されている請求項3記載の有機性廃棄物の前処理設備。The installation equipment includes a side wall and a floor slab integrally formed in a region excavated so as to partition a section of the surface of the earth, and a ventilation member that covers a ventilation pipe as the air diffusion equipment disposed on the floor slab The organic waste pretreatment facility according to claim 3, wherein the organic waste is placed on an upper layer of the ventilation member.
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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH10249300A (en) * 1997-03-18 1998-09-22 Hazama Gumi Ltd Waste disposal site
JP2006281006A (en) * 2005-03-31 2006-10-19 Fujita Corp Method of treating incineration ash, method of sprinkling water to incineration ash layer, and sprinkler for incineration ash
JP2009241053A (en) * 2008-03-12 2009-10-22 Fujita Corp Waste pretreatment method
JP2013027833A (en) * 2011-07-29 2013-02-07 Kajima Corp Waste stabilization method
JP2015116515A (en) * 2013-12-17 2015-06-25 クボタ環境サ−ビス株式会社 Organic waste pretreatment equipment, organic waste pretreatment method, and organic waste landfilling treatment method

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