JP2006122897A - Drainage treatment apparatus and treatment system of turbid sewage - Google Patents

Drainage treatment apparatus and treatment system of turbid sewage Download PDF

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JP2006122897A
JP2006122897A JP2005278143A JP2005278143A JP2006122897A JP 2006122897 A JP2006122897 A JP 2006122897A JP 2005278143 A JP2005278143 A JP 2005278143A JP 2005278143 A JP2005278143 A JP 2005278143A JP 2006122897 A JP2006122897 A JP 2006122897A
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JP4403126B2 (en
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Hidenori Yamaguchi
英紀 山口
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PANATONE NIIGATA KK
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Abstract

<P>PROBLEM TO BE SOLVED: To provide the most suitable turbid sewage treatment system which enables the whole treatment in a site corresponding to the circumstance of the site in a small-scale site having a small amount of turbid sewage to be a treatment target. <P>SOLUTION: The turbid sewage treatment system comprises a drainage mechanism 1a of the turbid sewage which can individually be used as a drainage treatment apparatus, a solid-liquid separation mechanism 2a of the turbid sewage, a solidification treatment mechanism 3a and a compressor 4 served as each driving source, wherein the drainage mechanism of the turbid sewage includes a suction part 11 provided with a suction port which can ground and has a plane opening, and an air driving diaphragm pump part 13 provided with a check valve through which gravel can pass; the solid-liquid separation mechanism includes a sealed sedimentation tank 21 which can carry out flocculation treatment by air agitation; and the solidification treatment mechanism includes an agitator driven by an air motor 6 which agitates to mix flocculated sludge B and a neutral solidifying agent b. <P>COPYRIGHT: (C)2006,JPO&NCIPI

Description

本発明は、主として建設現場等で発生する汚濁泥水の処理システムに関するものである。   The present invention relates to a treatment system for contaminated mud water generated mainly at a construction site or the like.

建設現場で発生する汚濁泥水(土砂泥水)の処理は、基本的に固液分離をなし、固体ケーキは現場外に運搬廃棄し、浄水はそのまま再利用したり放水廃棄している。   The treatment of contaminated mud water (sediment mud water) generated at the construction site is basically solid-liquid separation, the solid cake is transported and discarded outside the site, and the purified water is reused as it is or discharged.

具体的には、汚濁泥水貯留箇所から水中サンドポンプによって汚濁泥水をくみ上げ、スクリーンによる一次固液分離を行い、固体部分は廃棄処分とし、更にスクリーンで分離されない汚濁泥水の凝集沈殿をなし、沈殿物をそのまま廃棄処分或いは圧力差を利用した二次固液分離を行い、分離固体部分を廃棄処理している(特許文献1,2)。そして特に前記の固体部分の廃棄は、現場外に運搬して廃棄するようにしている。   Specifically, the slurry mud water is pumped up from the polluted mud water storage site by an underwater sand pump, primary solid-liquid separation is performed with a screen, the solid part is disposed of, and the aggregated sediment of the polluted mud water that is not separated by the screen is formed. Is disposed as it is or is subjected to secondary solid-liquid separation utilizing a pressure difference, and the separated solid portion is disposed of (Patent Documents 1 and 2). In particular, the solid part is disposed of by being transported outside the site.

また建築現場の汚濁泥水(余剰泥水)の処理手段として、所定の縦穴に溜めた余剰泥水をポンプアップし、その余剰泥水に固化材及び減水剤を添加攪拌して半固化状態として処理する手段も知られている(特許文献3)。   In addition, as a means of treating the contaminated mud water (surplus mud water) at the construction site, there is also a means for pumping up the surplus mud water accumulated in a predetermined vertical hole, adding a solidifying material and a water reducing agent to the surplus mud water, and stirring and treating it as a semi-solidified state. Known (Patent Document 3).

特公平4−74041号公報。Japanese Patent Publication No. 4-74041. 特開平6−319916号公報。Japanese Patent Laid-Open No. 6-319916. 特開平10−296232号公報。Japanese Patent Laid-Open No. 10-296232.

前記した特許文献1,2で開示されている従前の汚濁泥水処理システムでは、掘削に泥水(掘削液)を多量に使用する現場や、大規模建設現場が対象であり、このため泥水処理システム全体が大規模にならざるを得なく、そのまま泥水使用量の少ない現場や、単に発生泥水を処理するだけの現場には対応できない。   The conventional polluted muddy water treatment systems disclosed in Patent Documents 1 and 2 are intended for sites where a large amount of muddy water (drilling fluid) is used for excavation and large-scale construction sites. However, it is unavoidable to be large-scale, and cannot respond to the site where the amount of muddy water used is small or the generated muddy water is simply treated.

しかも前記システムは、分離固形分の現場外廃棄が必要となり、更なる産業廃棄物を生じさせ、二次処理が必要となる。   In addition, the system requires off-site disposal of the separated solids, generates additional industrial waste, and requires secondary treatment.

また特許文献3記載の汚濁泥水に直接固化材を添加する処理手段では、泥水が半固形状態のままであり、当然そのままでは廃棄することができずに再度の処理が必要となる。   Moreover, in the processing means which adds a solidification material directly to the polluted mud described in Patent Document 3, the mud remains in a semi-solid state, and naturally it cannot be discarded as it is, and a re-treatment is required.

また従前手段における泥水の汲み上げには、水中サンドポンプを採用しているもので、汲み上げには相応の深さが必要であり、処理のために予め泥水を貯留する箇所(カマ場、縦穴)を現場に設けておかなければならない。しかも泥水の全てがポンプで汲み上げられて処理させるものではなく、最終的には手作業となってしまうか、汲み上げずにそのまま土砂で埋めてしまう処置を講じている。   In addition, the submerged sand pump is used for pumping up the muddy water in the conventional means, and a suitable depth is required for pumping up. It must be established on site. In addition, not all of the muddy water is pumped up and processed, and eventually, it is a manual operation or a measure is taken to bury it without any pumping.

従って従前手段では、現場で発生した泥水をそのままの状態で処理することができなく、一旦貯留箇所に溜めるという煩雑な作業が必要であるという問題や、残存泥水処理の問題がある。   Therefore, the conventional means cannot treat the muddy water generated in the field as it is, and there is a problem that a complicated work of temporarily storing the muddy water in the storage location is required and a problem of residual muddy water treatment.

そこで本発明は処理対象の泥水量が少ない小規模現場において、当該現場での全処理が容易に成し得る最適な処理システム並びに前記システムに採用される泥水排水処理装置を提案したものである。   Accordingly, the present invention proposes an optimum treatment system that can easily perform all treatments at a small-scale site where the amount of muddy water to be treated is small, and a mud drainage treatment device employed in the system.

本発明(請求項2)に係る汚濁泥水排水システムは、排水処理装置として単独使用が可能な汚濁泥水の排水機構と、汚濁泥水の固液分離機構と、固化処理機構と、前記排水機構及び固液分離機構の駆動源となるコンプレッサーとで構成され、汚濁泥水の排水機構は、接地可能な平面開口の吸引口を備えた吸引部、及び砂利が通過可能な逆止弁を備えた空気駆動のダイヤフラムポンプ部とからなり、固液分離機構は、空気攪拌による凝集処理可能な適宜容量の沈殿槽を備えたもので、固化処理機構は、凝集汚泥と中性固化剤を攪拌混合する攪拌機を備えたものである。   A polluted mud drainage system according to the present invention (Claim 2) includes a polluted mud water drainage mechanism that can be used alone as a wastewater treatment device, a solid-liquid separation mechanism of polluted mud water, a solidification treatment mechanism, the drainage mechanism, It consists of a compressor that serves as the drive source for the liquid separation mechanism, and the drainage mechanism for contaminated mud water is an air-driven unit equipped with a suction part with a flat-surfaced suction port that can be grounded and a check valve through which gravel can pass. It consists of a diaphragm pump unit, the solid-liquid separation mechanism is equipped with a sedimentation tank of an appropriate capacity that can be coagulated by air stirring, and the solidification processing mechanism is equipped with a stirrer that stirs and mixes the coagulated sludge and the neutral solidifying agent. It is a thing.

而して排水機構において、ダイヤフラムポンプ部の作動(コンプレッサーによる作動)によって、吸引部から泥水の吸引をするもので、特に吸引口の接地によって地表面の泥水も全て吸引することができ、吸引泥水を適宜箇所に排出することで、前記排水機構は単独で地表面泥水の排出装置として使用できる。しかも吸引に際して砂利を吸い込んでも何ら支障なくそのまま吸引排出できる。   Thus, in the drainage mechanism, the operation of the diaphragm pump part (operation by the compressor) sucks muddy water from the suction part. In particular, all the muddy water on the ground surface can be sucked by the grounding of the suction port. By properly discharging to a place, the drainage mechanism can be used alone as a ground surface mud drainage device. Moreover, even if gravel is sucked during suction, it can be sucked and discharged as it is without any trouble.

汚濁泥水を処理するには、前記排水機構で吸引した汚濁泥水を、固液分離機構の沈殿槽に溜め、凝集剤を添加し、且つ空気攪拌を行った後静置して、上澄み浄水はそのまま下水等に廃棄する。凝集沈殿物は、次の固化処理機構の攪拌機に送り込む。攪拌機においては無機質の中性固化剤を添加して攪拌し、凝集沈殿物を固化させ、固化物は土壌と何ら変わりの無い無害物なので、そのまま現場において再利用することができる。   In order to treat the contaminated mud water, the mud water sucked by the drainage mechanism is stored in the settling tank of the solid-liquid separation mechanism, the flocculant is added, and after agitation with air, it is allowed to stand, and the supernatant purified water remains as it is. Dispose of in sewage. The agglomerated precipitate is sent to a stirrer of the next solidification processing mechanism. In the stirrer, an inorganic neutral solidifying agent is added and stirred to solidify the aggregated precipitate. Since the solidified product is harmless to the soil, it can be reused as it is.

また本発明(請求項3)に係る汚濁泥水排水システムは、前記(請求項1)の汚濁泥水処理システムにおいて、固定処理機構の攪拌機をエアモータ駆動としたもので、各機構の全ての駆動をコンプレッサーによる駆動にしたことを特徴とするものである。   Further, the polluted mud drainage system according to the present invention (Claim 3) is the polluted mud waste water treatment system of (Claim 1), wherein the agitator of the fixed processing mechanism is driven by an air motor, and all the driving of each mechanism is a compressor. It is characterized by having been driven by.

従ってエンジン駆動のコンプレッサーを処理現場に持ち込むことで、当該現場での汚濁泥水の処理が可能となるものである。   Therefore, by bringing an engine-driven compressor to the treatment site, it is possible to treat the contaminated mud water at the site.

また本発明(請求項4)は、前記発明において、固液分離機構の沈殿槽を密封槽とし、水分排出管及び固形分排出管に適宜な開閉弁を備えてなることを特徴としたものである。   The present invention (Claim 4) is characterized in that, in the above invention, the precipitation tank of the solid-liquid separation mechanism is a sealed tank, and the moisture discharge pipe and the solid content discharge pipe are provided with appropriate on-off valves. is there.

而して密封状態で空気攪拌を行うこと沈殿槽内が高圧状態となり、開閉弁を開放すると、沈殿槽内圧力で固液分離物の槽外搬送がなされ、攪拌空気の有効利用となるものである。   Thus, when the air is stirred in a sealed state, the inside of the settling tank becomes a high pressure state, and when the on-off valve is opened, the solid-liquid separation is transported outside the tank by the pressure inside the settling tank, and the stirring air is effectively used. is there.

更に本発明(請求項5)は、排水機構と固液分離処理機構の間、又は固液分離処理機構と固化処理機構との間或いは双方の搬送管に、エアジェットポンプ(搬送力付与機構)を介装することを特徴としたもので、各機構間の搬送管路が長くなっても、コンプレッサーの高圧空気を利用しての長距離搬送を実現できるものである。   Further, according to the present invention (Claim 5), an air jet pump (conveying force applying mechanism) is provided between the drainage mechanism and the solid-liquid separation processing mechanism, or between the solid-liquid separation processing mechanism and the solidification processing mechanism, or in both the conveying pipes. It is characterized in that long-distance conveyance using the high-pressure air of the compressor can be realized even if the conveyance pipeline between the mechanisms becomes long.

本発明は、前記の構成の通りであり、使用現場に対応して各機構の必要処理能力を備えたものを選択組み合わせることで、全体の処理システムを最適な規模とすることができ、且つ全て現場処理可能とし、現場外に搬出する二次廃棄物を発生させないものである。   The present invention is configured as described above, and the entire processing system can be set to an optimum scale by selecting and combining those having the necessary processing capacity of each mechanism corresponding to the use site. It enables on-site processing and does not generate secondary waste to be carried out of the site.

また空気作動のダイヤフラムポンプを排水機構に採用したことによって、泥水汲み上げ用の貯留穴を掘削する必要が無く、ポンプ位置から離れた泥水箇所でも掃除機のように吸水口を操作することで地表面の泥水の排出が可能であり、更に残水が存在しなくともポンプの故障が生じない等の機器の保守が容易である。   In addition, by adopting an air-operated diaphragm pump in the drainage mechanism, it is not necessary to dig a storage hole for pumping up muddy water, and the surface of the ground can be operated by operating the water intake port like a vacuum cleaner at a muddy water location away from the pump position. The muddy water can be discharged, and the maintenance of the equipment such as the pump does not fail even if there is no residual water is easy.

次に本発明システムの実施形態について説明する。図1は本発明システムの第一実施形態で、この汚濁汚泥排水システムは、排水処理装置として単独使用が可能な汚濁泥水排水機構1と、汚濁泥水の固液分離機構2と、固化処理機構3と、駆動部(コンプレッサー)4とで構成される。   Next, an embodiment of the system of the present invention will be described. FIG. 1 shows a first embodiment of the system of the present invention. This polluted sludge drainage system includes a polluted mud drainage mechanism 1 that can be used alone as a wastewater treatment device, a solid-liquid separation mechanism 2 of polluted mud water, and a solidification treatment mechanism 3. And a drive unit (compressor) 4.

汚濁泥水の排水機構1は、吸引部11と、吸引ホース12と、ポンプ部13と、排出ホース14とからなる。   The polluted muddy water drainage mechanism 1 includes a suction part 11, a suction hose 12, a pump part 13, and a discharge hose 14.

吸引部11は、一般の掃除機の吸引部と同様な接地可能な平面開口の吸引口を備えたもので、吸引ホース12でポンプ部13と接続されている。   The suction part 11 includes a suction opening with a flat opening that can be grounded, similar to the suction part of a general vacuum cleaner, and is connected to the pump part 13 by a suction hose 12.

ポンプ部(ダイヤフラムポンプ)13は、駆動ダイヤフラム131でポンプ室132の容積を変化させるもので、ポンプ室132の出入り口に逆止弁133を備えてなる。特にポンプ駆動は駆動部4のコンプレッサーからの高圧空気で行うものであり、また逆止弁133は、砂利が通過可能なボール弁や煽り弁を採用したものである。   The pump unit (diaphragm pump) 13 is a drive diaphragm 131 that changes the volume of the pump chamber 132, and includes a check valve 133 at the entrance and exit of the pump chamber 132. In particular, the pump is driven by high-pressure air from the compressor of the drive unit 4, and the check valve 133 employs a ball valve or a swing valve through which gravel can pass.

また排出ホース14は、ポンプ部13の排出口に連結され、次の固液分離機構(沈殿槽)2に汚濁泥水Aを放出するようにしているものである。   The discharge hose 14 is connected to the discharge port of the pump unit 13 and discharges the contaminated mud water A to the next solid-liquid separation mechanism (precipitation tank) 2.

固液分離機構2は、駆動部4のコンプレッサーと接続して空気攪拌可能な構造とした適宜容量(使用対象の現場の泥水発生量に対応する容量)の沈殿槽を備えると共に、凝集剤aを供給するようにしたものである。   The solid-liquid separation mechanism 2 is provided with a sedimentation tank of an appropriate capacity (capacity corresponding to the amount of muddy water generated on the site to be used) connected to the compressor of the drive unit 4 so as to be able to stir the air, and the coagulant a It is to be supplied.

固化処理機構3は、固化剤bと凝集汚泥Bを攪拌混合する攪拌機であり、攪拌機は、前記の固液分離機構2の処理能力に対応する処理能力を備えていれば良いもので、具体的には2軸攪拌羽根を備え、別置発電機(エンジン駆動)5から電力供給を受け、攪拌羽根用モータを駆動させてなるものである。   The solidification processing mechanism 3 is a stirrer that stirs and mixes the solidifying agent b and the coagulated sludge B, and the stirrer only needs to have a processing capacity corresponding to the processing capacity of the solid-liquid separation mechanism 2. Is provided with a biaxial agitating blade, which is supplied with electric power from a separate generator (engine drive) 5 and drives the agitating blade motor.

而して建設現場に、排水機構1、沈殿槽(固液分離機構)2、攪拌機(固化処理機構)3、エンジン駆動のコンプレッサー(駆動部)4、エンジン駆動の発電機5を持ち込むことで汚濁泥水処理システムを構築することができるものである。   Thus, it is contaminated by bringing the drainage mechanism 1, the sedimentation tank (solid-liquid separation mechanism) 2, the stirrer (solidification processing mechanism) 3, the engine-driven compressor (drive unit) 4 and the engine-driven generator 5 to the construction site. A muddy water treatment system can be constructed.

そしてポンプ部13を作動させ、現場における汚濁泥水Aが溜まっている箇所に吸引部11の吸引口をあてがうと、ポンプ部13の作動によって、汚濁泥水Aが吸引部11から吸引され、吸引ホース12を通過してポンプ部13のポンプ室132を通過し排出ホース14を通って沈殿槽(固液分離機構)2に排出される。   And if the pump part 13 is operated and the suction port of the suction part 11 is assigned to the place where the polluted mud water A is collected in the field, the dirty mud water A is sucked from the suction part 11 by the action of the pump part 13, and the suction hose 12 , Passes through the pump chamber 132 of the pump unit 13, passes through the discharge hose 14, and is discharged to the precipitation tank (solid-liquid separation mechanism) 2.

前記の汚濁泥水Aの給排水においては、吸引口の接地によって地表面の泥水も全て吸引することができ、また小砂利等を吸引しても、そのまま支障なく沈殿槽2まで運ぶことができるので、従前の水中サンドポンプのような残存泥水が発生したり、目詰まりしたり、小砂利吸引によってポンプが故障・破損するようなことがない。   In the supply and drainage of the above-mentioned contaminated mud water A, all the mud on the ground surface can be sucked by the grounding of the suction port, and even if small gravel is sucked, it can be carried as it is to the sedimentation tank 2 without any trouble. Residual mud like conventional submersible sand pumps is not generated, clogged, or pumps fail or break due to small gravel suction.

尚前記の排水機構は、コンプレッサー(駆動部)4との組み合わせによって、独立した泥水排水装置として使用することができ、建築現場以外の競技場や野球場等の緊急グランド排水機器として採用することができる。   The drainage mechanism can be used as an independent muddy drainage device in combination with the compressor (drive unit) 4 and can be used as an emergency ground drainage device for stadiums and baseball fields other than construction sites. it can.

沈殿槽(固液分離機構)2に所定量の汚濁泥水Aが溜められと、凝集剤aを添加し、且つコンプレッサー(駆動部)4から沈殿槽2内に高圧空気を吹き入れて、汚濁泥水Aと凝集剤aを攪拌混合し、所定時間静置する。そうすると沈殿槽2において、汚濁泥水Aは沈殿物Bと上澄み浄水Cに分離するので、上澄み浄水Cはそのまま下水に廃棄したり現場で再利用し、沈殿物Bは攪拌機(固化処理機構)3に投入する。   When a predetermined amount of polluted mud water A is accumulated in the sedimentation tank (solid-liquid separation mechanism) 2, flocculant a is added, and high-pressure air is blown into the sedimentation tank 2 from the compressor (drive unit) 4. A and the aggregating agent a are mixed with stirring and allowed to stand for a predetermined time. Then, in the sedimentation tank 2, the polluted mud water A is separated into the sediment B and the supernatant purified water C. Therefore, the supernatant purified water C is discarded as it is into the sewage or reused at the site, and the sediment B is sent to the stirrer (solidification mechanism) 3 throw into.

攪拌機(固化処理機構)3に沈殿物Bが投入されると、攪拌機3に更に無機質の中性固化剤を適宜量添加して攪拌する。所定時間(固化剤の内容にもよるが数分程度)攪拌すると沈殿物Bは固化物Dとなり、この固化物Dは、中性であり土壌と何ら変わりの無い無害物であるので、そのまま現場において廃棄することができる。   When the precipitate B is put into the stirrer (solidification mechanism) 3, an appropriate amount of an inorganic neutral solidifying agent is further added to the stirrer 3 and stirred. When stirring for a predetermined time (depending on the content of the solidifying agent, about several minutes), the precipitate B becomes a solidified material D, and this solidified material D is neutral and harmless to the soil. Can be discarded.

従って前記の実施形態の汚濁泥水処理システムは、所定の処理を行う各機構並びに駆動源を、現場で必要とする作業形態や処理能力に合わせて組み合わせて構築するもので、小規模現場でも容易に適用でき、且つ全て現場処理が可能であり、現場から搬出しなければならない二次廃棄物を発生させない利点を有する。   Therefore, the contaminated mud water treatment system of the above embodiment is constructed by combining each mechanism for performing a predetermined treatment and a driving source in accordance with a work form and processing capacity required on the site, and can be easily used on a small site. It can be applied and all can be processed on site, and has the advantage of not generating secondary waste that must be transported from the site.

また特に排水機構として、ダイヤフラムポンプを採用することで、水中サンドポンプを採用している従前手段が抱えている問題を解消したものである。   Moreover, the problem which the conventional means which employ | adopted the submerged sand pump is eliminated by employ | adopting a diaphragm pump as a drainage mechanism especially.

また図3は本発明システムの第二実施形態で、第一実施形態と同様に排水処理装置として単独使用が可能な汚濁泥水排水機構1aと、汚濁泥水の固液分離機構2a、固化処理機構3aと、駆動部(コンプレッサー4及び高圧空気を分配する開閉弁制御部41)4aとで構成される。   FIG. 3 shows a second embodiment of the system of the present invention. As in the first embodiment, a contaminated mud drainage mechanism 1a that can be used alone as a wastewater treatment apparatus, a solid-liquid separation mechanism 2a, and a solidification treatment mechanism 3a. And a drive unit (compressor 4 and on-off valve control unit 41 for distributing high-pressure air) 4a.

汚濁泥水の排水機構1aは、吸引部11と、吸引ホース12と、ポンプ部13と、排出ホース14と、搬送力付与機構15とからなる。   The polluted mud drainage mechanism 1 a includes a suction part 11, a suction hose 12, a pump part 13, a discharge hose 14, and a conveyance force applying mechanism 15.

吸引部11、吸引ホース12、ポンプ部13、排出ホース14の構成は第一実施形態と同様であり、特に搬送力付与機構15は、コンプレッサー4の高圧空気を搬送方向に噴出することで、搬送物(汚濁泥水A)を固液分離機構2aに押し出すと共に、高圧空気の噴射によってポンプ部13側の汚濁泥水Aを吸引する所謂ジェットポンプ構造を採用したものである。   The structure of the suction part 11, the suction hose 12, the pump part 13, and the discharge hose 14 is the same as that of the first embodiment. In particular, the transport force imparting mechanism 15 transports high-pressure air from the compressor 4 in the transport direction. A so-called jet pump structure is employed in which an object (polluted mud water A) is pushed out to the solid-liquid separation mechanism 2a and the mud mud water A on the pump unit 13 side is sucked by injection of high-pressure air.

固液分離機構2aは、駆動部4aのコンプレッサー4と接続して空気攪拌可能な構造とした適宜容量(使用対象の現場の泥水発生量に対応する容量)の沈殿槽21を備えると共に、凝集剤aを供給するようにしたもので、特に沈殿槽21は、密封構造として開閉弁22,23を介装して上澄み浄水Cの排出管24及び沈殿物Bの排出管25を連結したものである。特に沈殿物Bの排出管25は、次の固化処理機構3aに接続したものであり、排出管25が長くなる場合には、前記した搬送力付与機構を介設するようにしても良い。   The solid-liquid separation mechanism 2a includes a sedimentation tank 21 having an appropriate capacity (capacity corresponding to the amount of muddy water generated on the site of use) connected to the compressor 4 of the drive unit 4a and having a structure capable of stirring air, and a coagulant. In particular, the sedimentation tank 21 is formed by connecting the discharge pipe 24 of the supernatant clean water C and the discharge pipe 25 of the sediment B through the on-off valves 22 and 23 as a sealing structure. . In particular, the discharge pipe 25 for the precipitate B is connected to the next solidification processing mechanism 3a, and when the discharge pipe 25 becomes long, the above-described transport force applying mechanism may be interposed.

固化処理機構3aは、第一実施形態と同様に、固化剤bと凝集汚泥Bを攪拌混合する攪拌機であるが、その攪拌羽根の回転駆動源として、特にコンプレッサー4からの高圧空気で作動するエアモータ6を採用したものである。   The solidification processing mechanism 3a is a stirrer that stirs and mixes the solidifying agent b and the coagulated sludge B as in the first embodiment, and an air motor that operates with high-pressure air from the compressor 4 as a rotational drive source of the stirring blades. 6 is adopted.

駆動部4aは、所定の能力を備えたコンプレッサー4と、コンプレッサーの高圧空気を各機構に分配制御する開閉弁制御部41を備えたもので、特に汚濁泥水排水機構1aと、固液分離機構2a、固化処理機構3aは、必ずしも同時運転を行うものではない。即ち固液分離機構2aにおける沈殿時間の間には、汚濁泥水排水機構1aは作動せずに、前回処理時の沈殿物を処理するために固化処理機構3aを作動させるのみで良いし、沈殿槽21が空いた状態(余裕がある状態)で汚濁泥水排水機構1aを動作させるものである。従って各機構の動作時間や必要能力を考慮してコンプレッサー容量や開閉弁制御部41の動作を決定すれば良い。   The drive unit 4a includes a compressor 4 having a predetermined capacity, and an on-off valve control unit 41 for distributing and controlling the high-pressure air of the compressor to each mechanism. In particular, the contaminated mud drainage mechanism 1a and the solid-liquid separation mechanism 2a The solidification processing mechanism 3a does not necessarily perform simultaneous operation. That is, during the sedimentation time in the solid-liquid separation mechanism 2a, the contaminated mud drainage mechanism 1a does not operate, it is only necessary to operate the solidification processing mechanism 3a in order to process the precipitate during the previous treatment, The polluted mud drainage mechanism 1a is operated in a state in which 21 is empty (with a margin). Therefore, the compressor capacity and the operation of the on-off valve control unit 41 may be determined in consideration of the operation time and required capacity of each mechanism.

而して前記第二実施形態の各機構を建設現場に持ち込んで、汚濁泥水処理システムを構築し、第一実施形態と同様に、ポンプ部13を作動させて現場における汚濁泥水Aを沈殿槽21に排出する。   Thus, each mechanism of the second embodiment is brought to the construction site to construct a contaminated mud water treatment system, and similarly to the first embodiment, the pump unit 13 is operated and the polluted mud water A at the site is set in the sedimentation tank 21. To discharge.

沈殿槽21に所定量の汚濁泥水Aが溜められと、凝集剤aを添加し、且つコンプレッサー4から沈殿槽21内に高圧空気を吹き入れて、汚濁泥水Aと凝集剤aを攪拌混合し、所定時間静置する。そうすると沈殿槽21において、汚濁泥水Aは沈殿物Bと上澄みの浄水Cに分離する。特に沈殿槽21は密閉構造となっているので、開閉弁22,23を選択的に開放することで、沈殿槽21内の圧力によって沈殿物B又は上澄みの浄水Cが圧力放出されることになり、攪拌空気の有効利用が図られるものである。   When a predetermined amount of polluted mud water A is stored in the settling tank 21, flocculant a is added, and high-pressure air is blown into the settling tank 21 from the compressor 4 to stir and mix the polluted mud water A and the flocculant a. Let stand for a predetermined time. Then, in the sedimentation tank 21, the polluted mud water A is separated into the sediment B and the supernatant purified water C. In particular, since the sedimentation tank 21 has a sealed structure, by selectively opening the on-off valves 22 and 23, the sediment B or the supernatant water C is released by the pressure in the sedimentation tank 21. Thus, effective use of the stirring air is achieved.

また固化処理機構3では第一実施形態と同様に、沈殿物Bの固化処理が行われるが、特にエアモータ6による駆動を行うようにしたもので、第一実施形態のように発電機を現場に持ち込む必要がなくなる利点がある。勿論第二実施形態も第一実施形態同様に所定の処理を行う各機構並びに駆動源を、現場で必要とする作業形態や処理能力に合わせて組み合わせて構築するもので、小規模現場でも容易に適用でき、且つ全て現場処理が可能であり、現場から搬出しなければならない二次廃棄物を発生させない利点を有することは当然である。   Further, in the solidification processing mechanism 3, as in the first embodiment, the solidification processing of the precipitate B is performed. In particular, the solidification processing mechanism 3 is driven by the air motor 6, and the generator is installed on the site as in the first embodiment. There is an advantage that it is not necessary to bring it in. Of course, the second embodiment is constructed by combining each mechanism and drive source for performing predetermined processing in accordance with the work form and processing capability required at the site, similarly to the first embodiment, and is easy even at a small site. Naturally, it has the advantage that it can be applied and all can be processed in the field and does not generate secondary waste that must be carried out of the field.

本発明の第一実施形態の全体の説明図。BRIEF DESCRIPTION OF THE DRAWINGS General explanatory drawing of 1st embodiment of this invention. 同ポンプ部の断面図。Sectional drawing of the pump part. 本発明の第二実施形態の全体の説明図。Explanatory drawing of the whole 2nd embodiment of this invention.

符号の説明Explanation of symbols

1,1a 排水機構
11 吸引部
12 吸引ホース
13 ポンプ部
131 駆動ダイヤフラム
132 ポンプ室
133 逆止弁
14 排出ホース
15 搬送力付与機構
2,2a 固液分離機構
21 沈殿槽
22,23 開閉弁
24,25 排出管
3,3a 固化処理機構(攪拌機)
4,4a 駆動部(コンプレッサー)
41 開閉弁制御部
5 発電機
6 エアモータ
A 汚濁泥水
B 沈殿物(凝集汚泥)
C 上澄み浄水
D 固化物
a 凝集剤
b 固化剤
DESCRIPTION OF SYMBOLS 1,1a Drainage mechanism 11 Suction part 12 Suction hose 13 Pump part 131 Drive diaphragm 132 Pump chamber 133 Check valve 14 Discharge hose 15 Conveying force giving mechanism 2,2a Solid-liquid separation mechanism 21 Sedimentation tanks 22, 23 On-off valves 24, 25 Discharge pipe 3, 3a Solidification mechanism
4,4a Drive unit (compressor)
41 On-off valve controller 5 Generator 6 Air motor A Polluted mud water B Precipitate (aggregated sludge)
C supernatant water purification D solidified product a flocculant b solidifying agent

Claims (5)

接地可能な平面開口の吸引口を備えた吸引部、及び砂利が通過可能な逆止弁を備えた空気駆動のダイヤフラムポンプ部とで構成したことを特徴とする汚濁泥水排水装置。   A polluted mud drainage device comprising a suction part having a suction opening with a flat opening that can be grounded and an air-driven diaphragm pump part having a check valve through which gravel can pass. 平面開口の吸引口を有する吸引部、及び砂利が通過可能な逆止弁を備えた空気駆動のダイヤフラムポンプ部とからなる汚濁泥水の排水機構と、空気攪拌による凝集処理可能な適宜容量の沈殿槽を備えた汚濁泥水の固液分離処理機構と、前記排水機構及び固液分離機構の駆動源となるコンプレッサーと、凝集汚泥と中性固化剤を攪拌混合する攪拌機を備えた固化処理機構で構成してなる汚濁泥水処理システム。   A drainage mechanism of polluted mud water comprising a suction part having a suction port with a flat opening and an air-driven diaphragm pump part equipped with a check valve through which gravel can pass, and a settling tank of an appropriate capacity capable of coagulation treatment by air stirring The solid-liquid separation processing mechanism including the sludge sludge water, the compressor as a driving source of the drainage mechanism and the solid-liquid separation mechanism, and the solidification processing mechanism equipped with a stirrer for stirring and mixing the coagulated sludge and the neutral solidifying agent. Contaminated mud water treatment system. 平面開口の吸引口を有する吸引部、及び砂利が通過可能な逆止弁を備えた空気駆動のダイヤフラムポンプ部とからなる汚濁泥水の排水機構と、空気攪拌による凝集処理可能な適宜容量の沈殿槽を備えた汚濁泥水の固液分離処理機構と、凝集汚泥と中性固化剤を攪拌混合するエアモータ駆動の攪拌機を備えた固化処理機構と、前記各機構の駆動源となるコンプレッサーとで構成してなる汚濁泥水処理システム。   A drainage mechanism of polluted mud water comprising a suction part having a suction port with a flat opening and an air-driven diaphragm pump part equipped with a check valve through which gravel can pass, and a settling tank of an appropriate capacity capable of coagulation treatment by air stirring The solid-liquid separation processing mechanism comprising the sludge sludge water, the solidification processing mechanism equipped with an air motor-driven stirrer that stirs and mixes the coagulated sludge and the neutral solidifying agent, and the compressor that is the drive source of each of the mechanisms. Become a polluted mud water treatment system. 固液分離機構の沈殿槽を密封槽とし、水分排出管及び固形分排出管に適宜な開閉弁を備えてなる請求項3記載の汚濁泥水処理システム。   The polluted mud water treatment system according to claim 3, wherein the settling tank of the solid-liquid separation mechanism is a sealed tank, and the water discharge pipe and the solid content discharge pipe are provided with appropriate on-off valves. 排水機構と固液分離処理機構の間、又は固液分離処理機構と固化処理機構との間或いは双方の搬送管に、エアジェットポンプによる搬送力付与機構を介装してなる請求項3又は4記載の汚濁泥水処理システム。   5. A transport force applying mechanism using an air jet pump is interposed between the drainage mechanism and the solid-liquid separation processing mechanism, or between the solid-liquid separation processing mechanism and the solidification processing mechanism, or both. The contaminated mud water treatment system described.
JP2005278143A 2004-10-01 2005-09-26 Polluted mud drainage treatment device and polluted mud waste water treatment system Expired - Fee Related JP4403126B2 (en)

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