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JP4547103B2 - Operation method of high pressure pump of filter press type dehydrator - Google Patents
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JP4547103B2 - Operation method of high pressure pump of filter press type dehydrator - Google Patents

Operation method of high pressure pump of filter press type dehydrator Download PDF

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JP4547103B2
JP4547103B2 JP2001114914A JP2001114914A JP4547103B2 JP 4547103 B2 JP4547103 B2 JP 4547103B2 JP 2001114914 A JP2001114914 A JP 2001114914A JP 2001114914 A JP2001114914 A JP 2001114914A JP 4547103 B2 JP4547103 B2 JP 4547103B2
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pressure pump
piston
stock solution
filter press
time
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JP2002306907A (en
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伸平 末松
雅夫 下田
大策 条辺
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Nippon Steel Engineering Co Ltd
Nippon Steel Plant Designing Corp
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Nittetsu Plant Designing Corp
Nippon Steel Engineering Co Ltd
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  • Control Of Positive-Displacement Pumps (AREA)

Description

【0001】
【発明の属する技術分野】
本発明は、浚渫及び下水汚泥、建設残土等を含むスラリー状の原液をフィルタープレスを用いて脱水してケーキを製造するフィルタープレス式脱水装置の高圧ポンプの運転方法に関する。
【0002】
【従来の技術】
従来、河川やダム等の浚渫による土砂、生活廃液を処理した下水汚泥、建設工事で発生する水を含む残土等からなる原液(スラリーともいう)から水を分離して減量化する方法として、フィルタープレス式脱水装置が各種の産業界で幅広く利用されている。
フィルタープレス式脱水装置は、最初に低圧大容量型の渦巻きポンプで、フィルタープレスの濾布内の濾室に原液を圧送して濾室に急速に充填し、その後、往復動型のシリンダーを有する高圧小容量ポンプ(以下高圧ポンプという)に切り替えて原液を圧送し、原液の濾過時間を短縮して濾過効率の向上を図っている。
しかし、この濾過工程における高圧ポンプの停止時期は、原液から水を濾過して製造されたケーキの水分量を大きく左右する。
特に、濾過により脱水処理されたケーキを埋め立て材や土壌改良材等に活用する場合は、ケーキに含まれる水分量を均一にすることが望まれており、フィルタープレス式脱水装置の高圧ポンプの停止時期を適正に制御することが重要となる。
従って、脱水処理されたケーキの水分含有量を均一にするため、高圧ポンプの停止時期(脱水処理の終了時期)を調整する方法として、ある設定した濾過圧力に達した後、低圧の渦巻きポンプによる原液の充填の開始から高圧ポンプの停止までの時間を一定時間として設定した設定時間を基準に、例えば作業員等が濾過(脱水)を終了するか、あるいは設定時間をタイマーで設定することで自動化し、濾過時間に到達してから脱水を終了することが行われている。
しかし、この運転方法では、図5に示すように、脱水する原液として、例えば、性状が変化して脱水がし易くなった原液Aの場合では、高圧ポンプを停止する脱水時間の設定値(脱水終了時間)より以前に、ケーキの累計濾水量が目標値に到達する。
更に、原液の性状が変化して濾過がし難くなった原液Cの場合では、脱水時間の設定値時点において、初期スラリーで性状の変化のない標準的な原液の特性を有する原液Bよりも累計濾水量が低くなるため、ケーキの水分含有量が高くなる傾向を示す。
即ち、性状が時間の経過と共に変化する原液を用いた場合、一定の設定時間による運転では、累計濾水量の変動を生じ、脱水処理されたケーキの水分含有量を均一にすることが困難である。
この対策として、特許第2936411号公報に記載されている方法がある。即ち、フィルタープレス式脱水装置に供給される原液の質量流量及び密度をリアルタイムで検出し、この検出値に基づいて、乾土分を演算により求め、その演算値である積算乾土分と予め設定した土粒子真比重とに基づいてケーキの含水比を計算し、このケーキの含水比をケーキの目標含水比と比較する。そして、脱水後のケーキの含水比が目標含水比を下回る場合は、フィルタープレスの運転を継続し、脱水後のケーキの含水比が目標含水比を上回る場合は、フィルタープレスの運転を停止することにより、脱水のケーキの含水比をコントロールし、ケーキの含水量を正確に把握して脱水効率の向上を図る方法である。
【0003】
【発明が解決しようとする課題】
しかしながら、特許第2936411号公報に記載された方法では以下のような問題があった。
汚泥、残土等は、その種類が多く、しかも、その性状が時間の経過と共に変化する原液の脱水に適用する場合、リアルタイムで脱水条件を設定するのに手間を要し、設定そのものも困難である。
例えば、浚渫汚泥の場合では、浚渫する場所によって、その性状である粘度や固体の含有粒子径、介在物の有無等に大きな差を生じ、極端な場合では、一日の内でも、朝、昼、夕方等で不規則的にその性状が大きく異なる。
性状が大きく変化する原液を脱水するには、原液の質量流量及び密度等のリアルタイムの測定に種々の計器類を必要とし、しかも、積算乾土分と予め設定した土粒子真比重とに基づいてケーキの含水比等を求めるのに時間と手間を要する。更に、フィルタープレス式脱水装置の運転を行う際、その操業に経験を必要とし、実用技術として汎用的でない等の問題がある。
【0004】
本発明はかかる事情に鑑みてなされたもので、フィルタープレス式脱水装置の測定機器等の装備を簡素化して、その運転を容易にすると共に、性状が時系列で変化し易い浚渫汚泥、下水汚泥、建設工事で発生する水を含む残土等を脱水した後のケーキの含水量を均一にすることができ、フィルタープレスの異常状態を容易に判別することができるフィルタープレス式脱水装置の高圧ポンプの運転方法を提供することを目的とする。
【0005】
【課題を解決するための手段】
前記目的に沿う本発明に係るフィルタープレス式脱水装置の高圧ポンプの運転方法は、フィルタープレス式脱水装置を用いた脱水の初期に、低圧ポンプにより原液を圧送し、この後に往復動型シリンダーを有する高圧ポンプから前記フィルタープレス式脱水装置に原液を圧送し、原液を脱水してケーキを製造するフィルタープレス式脱水装置の高圧ポンプの運転方法において、
原液を圧送する前記高圧ポンプのピストンの移動時間を予め設定しておき、設定された前記高圧ポンプのピストンの移動時間よりも該高圧ポンプのピストンの移動時間が長くなった時点で、前記高圧ポンプの運転を停止して脱水を完了し、更に、前記高圧ポンプのピストンの移動時間が長くなった後、前記高圧ポンプのピストンの移動時間が短くなった場合を異常状態と判定する。
この方法により、原液を供給する高圧ポンプのピストンの移動時間により、脱水ケーキの水分を決定するので、原液の粘度、あるいは固体の含有粒子径が時系列で変化しても、ケーキの水分を均一にすることができ、埋め立て材や土壌改良材等に活用することができる。
【0006】
ここで、本発明に係るフィルタープレス式脱水装置の高圧ポンプの運転方法において、前記高圧ポンプのピストンの移動時間を該ピストンの移動速度に変換し、前記高圧ポンプのピストンの移動時間が長くなった後、前記高圧ポンプのピストンの移動時間が短くなった場合を異常状態と判定する代わりに、前記高圧ポンプのピストンの移動速度が遅くなった後、前記高圧ポンプのピストンの移動速度が速くなった場合を異常状態と判定することもできる。
これにより、フィルタープレス式脱水装置の測定機器等の装備を簡素化して、経過時間によって性状が変化し易い浚渫残土、下水汚泥、建設工事で発生する水を含む残土等の脱水したケーキの含水量を均一にすることができ、その運転を容易にすることができる。
【0008】
そして、フィルタープレス式脱水装置の濾布の破損や濾過室のシール不良等に起因した異常を検知することができる。
【0009】
【発明の実施の形態】
続いて、添付した図面を参照しつつ、本発明を具体化した実施の形態につき説明し、本発明の理解に供する。
図1は本発明の一実施の形態に係るフィルタープレス式脱水装置の高圧ポンプの運転方法に適用されるフィルタープレス式脱水装置の全体図、図2は同高圧ポンプの概念図、図3は脱水時間と累計濾水量の関係を表すグラフ、図4は脱水時間とピストンの移動時間(移動速度)の関係を表すグラフである。
図1及び図2に示すように、本発明の一実施の形態に係るフィルタープレス式脱水装置の高圧ポンプの運転方法に用いられるフィルタープレス式脱水装置10は、原液(スラリーともいう)をフィルタープレス11に圧送(送給)する高圧ポンプ12と、この高圧ポンプ12に連通して高圧ポンプ12を往復作動する油圧ユニット13と、高圧ポンプ12に原液を供給する吸い込みポンプ14と、原液を供給する図示しない渦流式の低圧ポンプを有している。
更に、フィルタープレス11は、濾布を内張りした隣り合わせの濾過板によって形成される複数の濾過室15を有し、原液を濾過した濾過水を排水する図示しない濾過受け樋がフィルタープレス11の下方に配置されている。
【0010】
また、高圧ポンプ12は、往復動作を繰り返し、その往復端位置を検知する装置の一例であるリミットスイッチ21b、21cを備えたピストン21aを内蔵した油圧シリンダー21と、この油圧シリンダー21に連通した泥水ポンプ22及び23を設けている。
泥水ポンプ22には、ゴム膜22aで区画された油圧室24、ゴム膜22aとゴム膜22bで区画され、水と不凍液をいれた中間室25と、ゴム膜22bで区画され原液を吐出弁27及び吸入弁28の切り替えによって、吸入、あるいは吐出する原液の吸吐出室26を設けており、同様に、泥水ポンプ23にも、ゴム膜23aで区画された油圧室29、ゴム膜23aとゴム膜23bで区画された水と不凍液をいれた中間室30と、ゴム膜23bで区画され吐出弁32及び吸入弁33の切り替えによって、原液を吸入、あるいは吐出する原液の吸吐出室31を備えている。
なお、吐出弁27と吐出弁32を連結する配管34には、フィルタープレス11に原液を供給する泥水吐出管35が接続され、吸入弁28と吸入弁33を連結する配管36には、原液を吸引する泥水吸入管37が接続されている。
【0011】
次に、本発明の一実施の形態に係るフィルタープレス式脱水装置の高圧ポンプの運転方法についてフィルタープレス式脱水装置10を用いて説明する。
浚渫を行った際の汚泥を一次沈殿させ、発生した原液を渦流式の低圧ポンプを作動してフィルタープレス11の濾過室15に送給した。
その後、油圧ユニット13を運転して高圧ポンプ12の油圧シリンダー21のピストン21aを図2の矢印で示す方向に押し込む。
このピストン21aの押し込みによって、図2に示すように、泥水ポンプ22の油圧室24に、油圧が加えられる。この油圧力が中間室25に伝達されて中間室25を形成するゴム膜22bが吸吐出室26に押し出されて膨らみ、吸吐出室26に吸引されていた原液が、吐出弁27と配管34を介して押し出され、泥水吐出管35を経由してフィルタープレス11の濾過室15に圧送(送給)される。
一方、油圧シリンダー21のピストン21aが図の矢印方向に作動した場合、泥水ポンプ23は、吸引側になり、泥水ポンプ23に設けた油圧室29の油圧が抜かれ、ゴム膜23aが油圧室29側にへこむ。そして、中間室30を形成するゴム膜23bもへこんで、吸吐出室31に吸引力が発生する。
そして、吸吐出室31に発生する吸引力によって、原液は、泥水吸入管37から配管36を経由し、吸入弁33を介して吸吐出室31に吸引される。
【0012】
この油圧シリンダー21のピストン21aの動作は、往復動作であり、前記した矢印の方向と逆の方向の作動を交互に繰り返すため、泥水ポンプ22と泥水ポンプ23が、原液を交互に高圧で、しかも、連続してフィルタープレス11の濾過室15に送給することができる。
そして、濾過室15に送給された原液は、濾過板に内張りした濾布により、水分のみが濾過され、固形分と残留水とからなるケーキが生成する。
濾過された水は、濾水受け樋から系外に排出される。
【0013】
この高圧ポンプ12で、フィルタープレス11の濾過室15に送給されて、脱水される原液は、例えば、浚渫の表層部、あるいは中層、下層等によって、原液の粘度が異なったり、固体の含有粒子径、不純物である介在物の量や種類等が変化する。
図3に示すように、原液の脱水時間の経過に伴う累計濾水量を見ると、例えば、原液が、通常の脱水性を有する原液(性状の変化のない初期スラリー)Bの場合では、脱水時間の経過と共に、累計濾水量が増加するが、一定時間を過ぎると、累計濾水量の増加の傾向が変化(増加の割合が減少)し、その傾き(α0 )が急激に小さくなる。
しかし、砂泥等の性状が変化して脱水が極めて容易な原液(性状の変化後のスラリー)Aの場合では、脱水時間の経過と共に、累計濾水量は急激に増加するため、累計濾水量の減少変化(増加の割合が減少)が、原液Bより早い時期に起こる。このとき、その傾き(α2 )は小さくなる。
一方、性状が変化し、粘度や固形の含有粒子径が小さくなった脱水のし難い原液(性状変化後のスラリー)Cの場合では、脱水時間の経過と共に、累計濾水量は緩やかに増加するため、累計濾水量の減少変化(増加の割合が減少)が、原液Bより遅い時期に起こる。このとき、その傾き(α1 )は小さくなる。
従って、この累計濾水量の減少量が変化(増加の割合が減少)する点(傾き)を一定の値にすること、即ち濾水量の変化量を一定にして脱水を終了することが、原液を脱水する際、ケーキの濾過抵抗を一定にして脱水を終了することとなるため、ケーキ中の固体密度を一定にすることができる。
このため、上記したそれぞれの傾き(α0 )、傾き(α1 )、傾き(α2 )が同じとなる偏曲点を、一般に用いられている算出式により求めることで、ケーキ中の固体密度を一定にすることもできるが、原液の種類、その性状の変化が多い場合、条件の設定や運転に時間を要する。
【0014】
そこで、ケーキの濾過抵抗は、高圧で原液をフィルタープレス11の濾過室15に送給する泥水ポンプ22、23の抵抗となり、しかも、原液を送給する油圧シリンダー21のピストン21aの往復する動作の移動時間、又は往復する動作の移動速度に反映されることを利用する。
図4に示すように、油圧シリンダー21のピストン21aの往復動作の移動時間、又は移動速度は、原液をフィルタープレス11の濾過室15に送給する際、原液の送給の初期から中期では、移動時間が短く、あるいは移動速度が速くなるが、前記傾きが小さくなる末期では、ピストン21aの移動時間が急激に長く、あるいは、移動速度が急激に遅くなる。
即ち、砂泥等の脱水の容易な原液Aの場合、原液が性状変化しない通常の脱水性を有する原液Bの場合、性状の変化した粘度や固形の含有粒子径が小さく脱水のし難い原液Cの場合について、それぞれに油圧シリンダー21のピストン21aの移動時間を一定の設定値にして脱水を行い、ピストン21aの移動時間が設定値より長くなった時点で、脱水の終了を判定すること、又はそれぞれに油圧シリンダー21のピストン21aの移動速度を一定の設定値にして脱水を行い、ピストン21aの移動速度が設定値より遅くなった時点で、脱水の終了を判定することで、脱水によって生成したケーキの含水量を、それぞれ均一な値にすることができる。このピストン21aの往復動作、あるいは片側の押し出し動作の時間は、リミットスイッチ21b、21cに当接した所要時間を計測して求めることができる。
更に、油圧シリンダー21のピストン21aの移動時間毎に、予め前記したケーキの脱水率のデータを求めておき、この値を基に、原液の種類を選定して脱水率を決定し、フィルタープレス11を運転することもできる。
【0015】
また、本実施の形態に係るフィルタープレス式脱水装置の高圧ポンプの運転方法では、油圧シリンダー21のピストン21aの移動時間(移動速度)を管理するので、濾布の破損や濾過室15のシール不良等が発生した際、油圧シリンダー21のピストン21aの移動時間が急激に短くなったり、移動速度が速くなるため、この変化から前記した濾布の破損や濾過室15のシール不良等の異常を早期に検出することができる。即ち、高圧ポンプ12が備えた油圧シリンダー21のピストン21aの移動時間が長くなった後、油圧シリンダー21のピストン21aの移動時間が短くなった場合を異常状態として判定し、また高圧ポンプ12が備えた油圧シリンダー21のピストン21aの移動時間をピストン21aの移動速度に変換した場合、高圧ポンプ12が備えた油圧シリンダー21のピストン21aの移動速度が遅くなった後、油圧シリンダー21のピストン21aの移動速度が速くなった場合を異常状態として判定する。
そして、異常が検知された際、フィルタープレス11への原液の供給が非常停止され機器の破損及び作業場の保全を行うことができる。
このようにして脱水されて生成したケーキは、トラック等により搬送されて、埋め立て材や土壌改良材として利用される。
【0016】
【実施例】
次に、フィルタープレス式脱水装置の高圧ポンプの運転方法の実施例について説明する。
浚渫した固形分を30重量%を含む原液について、砂泥等の脱水の容易な原液Aと、原液が通常の脱水性を有する原液Bと、性状の変化した粘度や固形の含有粒子径が小さく脱水のし難い原液Cのそれぞれを用い、この原液を、渦流式の低圧ポンプを作動してフィルタープレスの濾過室に送給した後、油圧ユニットを介して作動長さ(移動距離)400mmのピストンを有する油圧シリンダーを作動して高圧ポンプを運転し、更に、フィルタープレスの濾過室に原液を圧送し、油圧シリンダーのピストンの移動時間の設定を30秒にした。
その結果、この高圧ポンプによって濾過室に原液を供給する際、脱水経過時間の初期から中期におけるピストンの移動時間(押し出しストローク)は3秒間であったが、脱水の末期では、油圧シリンダーのピストンの移動時間が30秒となり、油圧シリンダーの移動時間が設定値に到達したので、この時点で脱水を終了した。
そして、原液Aから生成したケーキ、原液Bから生成したケーキ、原液Cから生成したケーキをそれぞれ取り出して、各ケーキの水分含有量を測定した結果、原液Aのケーキ、原液Bのケーキ、原液Cのケーキのいずれも水分含有量が20重量%となり、均一にすることができた。
【0017】
また、高圧ポンプによって濾過室に原液を送給し、高圧ポンプの運転をピストンの移動速度を133.3mm/秒(400mm/3秒)で行ったが、末期で、高圧ポンプの油圧シリンダーのピストンの移動速度が、一旦16mm/秒(400mm/25秒)に低下した後、再び16mm/秒を超えたため、異常と判断して運転を停止し、点検を行った結果、濾過室の濾布の破損を確認することができた。
【0018】
以上、本発明の実施の形態を説明したが、本発明は、上記した形態に限定されるものでなく、要旨を逸脱しない条件の変更等は全て本発明の適用範囲である。
例えば、油圧シリンダーのピストンの位置検出は、リミットスイッチの他に、光センサー、磁気センサー等の一般に用いられているものを採用でき、検出された位置から移動時間や移動速度を算出する演算装置についてもコンピュータ等を用いることができる。
更に、累計濾水量の増加の傾向(増加の割合)が変化するのを利用して、その傾きが急激に小さく変化する偏曲点をコンピュータに入力しておき、蓄積されたデータから、この蓄積されたデータに対応する原液を選定して脱水の処理時間を設定することもできる。
【0019】
【発明の効果】
請求項1、2記載のフィルタープレス式脱水装置の高圧ポンプの運転方法においては、フィルタープレス式脱水装置を用いた脱水の初期に、低圧ポンプにより原液を圧送し、この後に往復動型シリンダーを有する高圧ポンプからフィルタープレス式脱水装置に原液を圧送し、原液を脱水してケーキを製造するフィルタープレス式脱水装置の運転方法において、原液を圧送する高圧ポンプのピストンの移動時間を予め設定しておき、設定された高圧ポンプのピストンの移動時間よりも高圧ポンプのピストンの移動時間が長くなった時点で、高圧ポンプの運転を停止して脱水を完了するので、フィルタープレス式脱水装置の測定機器等の装備を簡素化して、その運転を容易にすると共に、性状が時系列で変化し易い浚渫残土、下水汚泥、建設工事で発生する水を含む残土等の脱水した後のケーキの含水量を均一にすることができる。
【0021】
そして、高圧ポンプのピストンの移動時間が長くなった後、高圧ポンプのピストンの移動時間が短くなった場合を異常状態と判定するので、濾布の破損や濾過室のシール不良等の異常を検出でき、脱水装置の運転を安定して行うことができる。更に、作業場の安全及び環境の保全を行うことができる。
【0022】
請求項記載のフィルタープレス式脱水装置の高圧ポンプの運転方法においては、高圧ポンプのピストンの移動速度が遅くなった後、高圧ポンプのピストンの移動速度が速くなった場合を異常状態と判定するので、濾布の破損や濾過室のシール不良等の異常を正確に検出でき、脱水装置の運転をより安定して行うことができる。
【図面の簡単な説明】
【図1】本発明の一実施の形態に係るフィルタープレス式脱水装置の高圧ポンプの運転方法に適用されるフィルタープレス式脱水装置の全体図である。
【図2】同高圧ポンプの概念図である。
【図3】脱水時間と累計濾水量の関係を表すグラフである。
【図4】脱水時間とピストンの移動時間の関係を表すグラフである。
【図5】従来の原液の脱水方法における脱水時間と累計濾水量の関係を表すグラフである。
【符号の説明】
10:フィルタープレス式脱水装置、11:フイルタープレス、12:高圧ポンプ、13:油圧ユニット、14:吸い込みポンプ、15:濾過室、21:油圧シリンダー、21a:ピストン、21b:リミットスイッチ、21c:リミットスイッチ、22:泥水ポンプ、22a:ゴム膜、22b:ゴム膜、23:泥水ポンプ、23a:ゴム膜、23b:ゴム膜、24:油圧室、25:中間室、26:吸吐出室、27:吐出弁、28:吸入弁、29:油圧室、30:中間室、31:吸吐出室、32:吐出弁、33:吸入弁、34:配管、35:泥水吐出管、36:配管、37:泥水吸入管
[0001]
BACKGROUND OF THE INVENTION
The present invention relates to a method for operating a high-pressure pump of a filter press type dehydrator for producing a cake by dewatering a slurry stock solution containing dredging, sewage sludge, construction residual soil, and the like using a filter press.
[0002]
[Prior art]
Conventionally, as a method of separating and reducing the amount of water from undiluted liquids (also called slurries) consisting of soil and sand from rivers and dams, sewage sludge treated from domestic wastewater, residual soil containing water generated during construction work, etc. Press dehydrators are widely used in various industries.
The filter press-type dewatering device is a low-pressure, large-capacity centrifugal pump that first feeds the stock solution into the filter chamber in the filter cloth of the filter press, quickly fills the filter chamber, and then has a reciprocating cylinder. By switching to a high-pressure small-capacity pump (hereinafter referred to as a high-pressure pump), the stock solution is pumped, and the filtration time of the stock solution is shortened to improve the filtration efficiency.
However, the stop timing of the high-pressure pump in this filtration step greatly affects the moisture content of the cake produced by filtering water from the stock solution.
In particular, when the cake dehydrated by filtration is used as a landfill or soil improvement material, it is desired that the amount of water contained in the cake be uniform, and the high-pressure pump of the filter press dehydrator is stopped. It is important to control the timing appropriately.
Therefore, in order to make the moisture content of the dehydrated cake uniform, as a method of adjusting the stop time of the high pressure pump (end time of the dehydration treatment), after reaching a set filtration pressure, a low pressure centrifugal pump is used. Based on the set time set as the fixed time from the start of filling the stock solution to the stop of the high-pressure pump, for example, the operator finishes filtration (dehydration) or automates by setting the set time with a timer Then, after reaching the filtration time, the dehydration is terminated.
However, in this operation method, as shown in FIG. 5, for example, in the case of a stock solution A whose properties have changed and has become easy to be dehydrated, as a stock solution to be dehydrated, a set value (dehydration time) for stopping the high-pressure pump is obtained. Prior to the end time), the cumulative drainage of the cake reaches the target value.
Furthermore, in the case of the stock solution C in which the properties of the stock solution have changed and it has become difficult to filter, at the time of the set value of the dehydration time, the total amount is higher than that of the stock solution B having the standard stock solution characteristics with no change in properties at the initial slurry. Since the amount of drainage decreases, the moisture content of the cake tends to increase.
That is, when a stock solution whose properties change over time is used, the operation with a certain set time causes a change in the total drainage amount, making it difficult to make the water content of the dehydrated cake uniform. .
As a countermeasure, there is a method described in Japanese Patent No. 2936411. That is, the mass flow rate and density of the stock solution supplied to the filter press type dehydrator are detected in real time, and the dry soil content is calculated based on the detected value, and the calculated dry soil content is set in advance. The moisture content of the cake is calculated based on the true specific gravity of the soil particles, and the moisture content of the cake is compared with the target moisture content of the cake. When the moisture content of the cake after dehydration is lower than the target moisture content, the operation of the filter press is continued, and when the moisture content of the cake after dehydration exceeds the target moisture content, the operation of the filter press is stopped. Thus, the water content ratio of the dehydrated cake is controlled, and the water content of the cake is accurately grasped to improve the dewatering efficiency.
[0003]
[Problems to be solved by the invention]
However, the method described in Japanese Patent No. 2936411 has the following problems.
There are many types of sludge, residual soil, etc., and when applied to the dehydration of a stock solution whose properties change over time, it takes time and effort to set the dehydration conditions in real time. .
For example, in the case of dredged sludge, the viscosity, solid particle size, presence or absence of inclusions, etc., vary greatly depending on the dredging location. In the evening, the properties vary irregularly.
In order to dehydrate a stock solution whose properties greatly change, various instruments are required for real-time measurement of the mass flow rate and density of the stock solution, and based on the accumulated dry soil content and the true specific gravity of the soil particles set in advance. It takes time and effort to obtain the moisture content of the cake. Furthermore, when the filter press type dehydrating apparatus is operated, there is a problem that it requires experience for the operation and is not general-purpose as a practical technique.
[0004]
The present invention has been made in view of such circumstances, and simplifies the equipment such as the measuring equipment of the filter press type dehydrating device, facilitates its operation, and dredged sludge and sewage sludge whose properties are easily changed in time series. Of the high pressure pump of the filter press type dehydrator that can make the moisture content of the cake after dewatering residual soil including water generated in construction work uniform and can easily identify the abnormal state of the filter press The purpose is to provide a driving method.
[0005]
[Means for Solving the Problems]
The operation method of the high-pressure pump of the filter press type dehydrator according to the present invention in accordance with the above object is that the stock solution is pumped by a low pressure pump at the initial stage of dehydration using the filter press type dehydrator, and then has a reciprocating cylinder. In the operation method of the high pressure pump of the filter press type dehydrator that pumps the stock solution from the high pressure pump to the filter press type dehydrator and dehydrates the stock solution to produce a cake,
The movement time of the piston of the high-pressure pump for pumping the stock solution is set in advance, and when the movement time of the piston of the high-pressure pump becomes longer than the set movement time of the piston of the high-pressure pump, the high-pressure pump The operation is stopped and the dehydration is completed . Further, after the moving time of the piston of the high-pressure pump becomes long, the moving time of the piston of the high-pressure pump becomes short.
With this method, the moisture content of the dehydrated cake is determined by the travel time of the piston of the high-pressure pump that supplies the stock solution. Therefore, even if the viscosity of the stock solution or the particle size of the solid changes over time, the moisture content of the cake remains uniform. And can be used for landfills, soil improvement materials and the like.
[0006]
Here, in the operation method of the high pressure pump of the filter press type dehydrator according to the present invention, the moving time of the piston of the high pressure pump is converted into the moving speed of the piston, and the moving time of the piston of the high pressure pump becomes longer. After that, instead of determining that the moving time of the piston of the high-pressure pump is shortened, the moving speed of the piston of the high-pressure pump is increased after the moving speed of the piston of the high-pressure pump is decreased. The case can also be determined as an abnormal state .
This simplifies the equipment such as the measuring equipment of the filter press-type dewatering device, and the water content of dewatered cake, such as dredged soil, sewage sludge, and soil containing water generated during construction work, whose properties are likely to change over time Can be made uniform, and the operation thereof can be facilitated.
[0008]
Then, it is possible to detect anomalies caused by breakage of the filter cloth of the filter press type dehydrator, poor sealing of the filtration chamber, or the like.
[0009]
DETAILED DESCRIPTION OF THE INVENTION
Next, embodiments of the present invention will be described with reference to the accompanying drawings for understanding of the present invention.
FIG. 1 is an overall view of a filter press dehydrator applied to a method for operating a high pressure pump of a filter press dehydrator according to an embodiment of the present invention, FIG. 2 is a conceptual diagram of the high pressure pump, and FIG. FIG. 4 is a graph showing the relationship between time and accumulated drainage amount, and FIG. 4 is a graph showing the relationship between dehydration time and piston moving time (moving speed).
As shown in FIGS. 1 and 2, a filter press dehydrator 10 used in a method for operating a high pressure pump of a filter press dehydrator according to an embodiment of the present invention uses a stock solution (also called slurry) as a filter press. 11, a high-pressure pump 12 that pumps (feeds) the oil, a hydraulic unit 13 that communicates with the high-pressure pump 12 and reciprocates the high-pressure pump 12 , a suction pump 14 that supplies the stock solution to the high-pressure pump 12 , and a feed A vortex-type low-pressure pump (not shown) is included.
Furthermore, the filter press 11 has a plurality of filtration chambers 15 formed by adjacent filter plates lined with a filter cloth, and a filtration receptacle (not shown) for draining filtered water obtained by filtering the stock solution is located below the filter press 11. Has been placed.
[0010]
The high pressure pump 12 repeats a reciprocating operation, and a hydraulic cylinder 21 including a piston 21a having limit switches 21b and 21c, which is an example of a device for detecting a reciprocating end position, and muddy water communicating with the hydraulic cylinder 21. Pumps 22 and 23 are provided.
The muddy water pump 22 has a hydraulic chamber 24 partitioned by a rubber film 22a, an intermediate chamber 25 partitioned by a rubber film 22a and a rubber film 22b, filled with water and antifreeze liquid, and a stock solution partitioned by a rubber film 22b and a discharge valve 27. In addition, a suction and discharge chamber 26 for a stock solution to be sucked or discharged is provided by switching the suction valve 28. Similarly, the muddy water pump 23 has a hydraulic chamber 29, a rubber film 23a and a rubber film partitioned by a rubber film 23a. An intermediate chamber 30 containing water and antifreeze liquid partitioned by 23b, and a suction / discharge chamber 31 of the raw liquid for sucking or discharging the stock solution by switching between the discharge valve 32 and the suction valve 33 partitioned by the rubber film 23b. .
A muddy water discharge pipe 35 for supplying the stock solution to the filter press 11 is connected to the pipe 34 connecting the discharge valve 27 and the discharge valve 32, and the stock solution is connected to the pipe 36 connecting the suction valve 28 and the suction valve 33. A mud suction pipe 37 for suction is connected.
[0011]
Next, a method for operating the high-pressure pump of the filter press dehydrator according to the embodiment of the present invention will be described using the filter press dehydrator 10.
The sludge produced during dredging was primarily precipitated, and the generated stock solution was fed to the filter chamber 15 of the filter press 11 by operating a vortex low-pressure pump.
Thereafter, the hydraulic unit 13 is operated to push the piston 21a of the hydraulic cylinder 21 of the high-pressure pump 12 in the direction indicated by the arrow in FIG.
By pushing the piston 21a, hydraulic pressure is applied to the hydraulic chamber 24 of the muddy water pump 22, as shown in FIG. This oil pressure is transmitted to the intermediate chamber 25, and the rubber film 22 b forming the intermediate chamber 25 is pushed into the suction / discharge chamber 26 to swell, and the stock solution sucked into the suction / discharge chamber 26 passes through the discharge valve 27 and the pipe 34. It is extruded through the muddy water discharge pipe 35 and is pumped (supplied) to the filtration chamber 15 of the filter press 11.
On the other hand, when the piston 21a of the hydraulic cylinder 21 operates in the direction of the arrow in the figure, the muddy water pump 23 is on the suction side, the hydraulic pressure in the hydraulic chamber 29 provided in the muddy water pump 23 is released, and the rubber film 23a is on the hydraulic chamber 29 side. Dent. Then, the rubber film 23 b forming the intermediate chamber 30 is also dented and a suction force is generated in the suction / discharge chamber 31.
Then, due to the suction force generated in the suction / discharge chamber 31, the stock solution is sucked into the suction / discharge chamber 31 via the suction valve 33 via the pipe 36 from the muddy water suction pipe 37.
[0012]
The operation of the piston 21a of the hydraulic cylinder 21 is a reciprocating operation, and since the operation in the direction opposite to the direction of the arrow is alternately repeated, the muddy water pump 22 and the muddy water pump 23 alternately supply the stock solution at a high pressure. , Can be continuously fed to the filtration chamber 15 of the filter press 11.
And only the water | moisture content is filtered from the undiluted | stock solution sent to the filtration chamber 15 with the filter cloth lined on the filter board, The cake which consists of solid content and residual water produces | generates.
The filtered water is discharged out of the system from the drainage receptacle.
[0013]
The stock solution that is fed to the filtration chamber 15 of the filter press 11 by this high-pressure pump 12 and dehydrated has different viscosity depending on the surface layer portion, middle layer, lower layer, etc. The diameter, the amount and type of inclusions that are impurities, and the like change.
As shown in FIG. 3, when the accumulated drainage amount with the passage of the dehydration time of the stock solution is viewed, for example, in the case where the stock solution is a stock solution B having an ordinary dehydration property (initial slurry having no change in properties) B, the dehydration time over, although total drainage amount increases, it fixed the time after which, the tendency of increase in the total drainage volume change (rate of increase is reduced), and the inclination (alpha 0) is abruptly reduced.
However, in the case of undiluted solution (slurry after property change) A that changes its properties such as sand and mud, the accumulated drainage amount increases rapidly with the passage of the dehydration time. The decrease change (decrease in the rate of increase) occurs earlier than the stock solution B. At this time, the inclination (α 2 ) becomes small.
On the other hand, in the case of undiluted stock solution (slurry after property change) C whose properties have changed and viscosity and solid content particle size have become small, the cumulative drainage amount gradually increases with the passage of the dehydration time. , The decrease change of the accumulated drainage amount (the rate of increase decreases) occurs later than the stock solution B. At this time, the inclination (α 1 ) becomes small.
Therefore, it is necessary to set the point (slope) at which the amount of decrease in the accumulated drainage amount changes (decrease in the rate of increase) to a constant value, that is, to end the dehydration with the amount of change in the drainage amount constant. At the time of dehydration, the filtration resistance of the cake is made constant and the dehydration is terminated, so that the solid density in the cake can be made constant.
For this reason, the solid density in the cake is obtained by obtaining the inflection points at which the respective inclinations (α 0 ), inclinations (α 1 ), and inclinations (α 2 ) are the same, using a commonly used calculation formula. However, it takes time to set conditions and to operate when there are many changes in the type and properties of the stock solution.
[0014]
Therefore, the filtration resistance of the cake is the resistance of the muddy water pumps 22 and 23 for feeding the stock solution to the filtration chamber 15 of the filter press 11 at a high pressure, and the piston 21a of the hydraulic cylinder 21 for feeding the stock solution reciprocates. It is utilized that it is reflected in the moving time or the moving speed of the reciprocating motion.
As shown in FIG. 4, the moving time or moving speed of the reciprocating operation of the piston 21 a of the hydraulic cylinder 21 is as follows: from the initial stage to the middle stage of feeding the stock solution when feeding the stock solution to the filtration chamber 15 of the filter press 11. Although the movement time is short or the movement speed is high, at the end when the inclination is small, the movement time of the piston 21a is abruptly long or the movement speed is abruptly slowed.
That is, in the case of a stock solution A that is easily dehydrated, such as sand and mud, in the case of a stock solution B that has a normal dehydration property in which the properties of the stock solution do not change, the stock solution C that is difficult to dehydrate due to a small change in viscosity or a solid-containing particle size. In this case, the dehydration is performed by setting the moving time of the piston 21a of the hydraulic cylinder 21 to a predetermined set value, and the end of dehydration is determined when the moving time of the piston 21a becomes longer than the set value, or The dehydration is performed by setting the moving speed of the piston 21a of the hydraulic cylinder 21 to a constant set value, and when the moving speed of the piston 21a becomes slower than the set value, the end of the dehydration is determined to generate the dehydration. The water content of the cake can be made uniform. The time of the reciprocating operation of the piston 21a or the pushing operation on one side can be obtained by measuring the required time of contact with the limit switches 21b and 21c.
Further, for each moving time of the piston 21a of the hydraulic cylinder 21, the cake dehydration rate data described above is obtained in advance, and based on this value, the type of stock solution is selected to determine the dehydration rate, and the filter press 11 You can also drive.
[0015]
Further, in the operation method of the high pressure pump of the filter press type dehydrator according to the present embodiment, the moving time (moving speed) of the piston 21a of the hydraulic cylinder 21 is managed, so that the filter cloth is damaged or the filter chamber 15 has a poor seal. When the above occurs, the moving time of the piston 21a of the hydraulic cylinder 21 is shortened rapidly or the moving speed is increased. Therefore, the change such as the breakage of the filter cloth and the sealing failure of the filter chamber 15 is caused early due to this change. Can be detected. That is, after the movement time of the piston 21a of the hydraulic cylinder 21 provided in the high-pressure pump 12 becomes longer, the case where the movement time of the piston 21a of the hydraulic cylinder 21 becomes shorter is determined as an abnormal state. When the moving time of the piston 21a of the hydraulic cylinder 21 is converted into the moving speed of the piston 21a, the moving speed of the piston 21a of the hydraulic cylinder 21 provided in the high-pressure pump 12 becomes slow, and then the moving of the piston 21a of the hydraulic cylinder 21 The case where the speed is increased is determined as an abnormal state.
And when abnormality is detected, supply of the undiluted | stock solution to the filter press 11 is stopped urgently, damage to an apparatus and maintenance of a workplace can be performed.
The cake thus dehydrated is transported by a truck or the like and used as a landfill material or a soil improvement material.
[0016]
【Example】
Next, an embodiment of a method for operating the high pressure pump of the filter press type dehydrator will be described.
For a stock solution containing 30% by weight of crushed solids, a stock solution A that is easily dewatered, such as sand and mud, a stock solution B in which the stock solution has a normal dehydration property, a viscosity whose properties have changed, and a solid-containing particle size are small. Each of the undiluted undiluted concentrates C was used, and this undiluted solution was supplied to the filter chamber of the filter press by operating a vortex low-pressure pump, and then a piston having an operating length (movement distance) of 400 mm via a hydraulic unit. The high-pressure pump was operated by operating the hydraulic cylinder having No., and the stock solution was pumped into the filtration chamber of the filter press, and the moving time of the piston of the hydraulic cylinder was set to 30 seconds.
As a result, when the stock solution was supplied to the filtration chamber by this high-pressure pump, the piston travel time (push-out stroke) from the beginning to the middle of the dehydration elapsed time was 3 seconds, but at the end of the dehydration, the piston of the hydraulic cylinder Since the moving time was 30 seconds and the moving time of the hydraulic cylinder reached the set value, dehydration was terminated at this point.
And the cake produced | generated from the stock solution A, the cake produced | generated from the stock solution B, the cake produced | generated from the stock solution C were taken out, respectively, As a result of measuring the moisture content of each cake, the cake of the stock solution A, the cake of the stock solution B, the stock solution C All of the cakes had a water content of 20% by weight and could be made uniform.
[0017]
In addition, the stock solution was fed to the filtration chamber by a high pressure pump, and the high pressure pump was operated at a piston moving speed of 133.3 mm / second (400 mm / 3 second). After moving to 16 mm / sec (400 mm / 25 sec) and again exceeding 16 mm / sec, it was judged abnormal and the operation was stopped. Damage could be confirmed.
[0018]
Although the embodiments of the present invention have been described above, the present invention is not limited to the above-described embodiments, and all changes in conditions and the like that do not depart from the gist are within the scope of the present invention.
For example, for the detection of the position of the piston of a hydraulic cylinder, in addition to the limit switch, commonly used devices such as an optical sensor and a magnetic sensor can be adopted, and an arithmetic unit that calculates the movement time and movement speed from the detected position Also, a computer or the like can be used.
Furthermore, using the fact that the trend of increase in cumulative drainage (rate of increase) changes, the inflection point whose slope changes rapidly and small is input to the computer, and this accumulated data is stored from the accumulated data. It is also possible to set a dehydration processing time by selecting a stock solution corresponding to the obtained data.
[0019]
【The invention's effect】
In the operation method of the high-pressure pump of the filter press type dehydrator according to claim 1 or 2, in the initial stage of dehydration using the filter press type dehydrator, the stock solution is pumped by a low pressure pump, and thereafter a reciprocating cylinder is provided. In the operation method of the filter press type dehydrator that pumps the stock solution from the high pressure pump to the filter press dehydrator and dehydrates the stock solution to produce a cake, the moving time of the piston of the high pressure pump that pumps the stock solution is set in advance. When the moving time of the piston of the high-pressure pump becomes longer than the set moving time of the piston of the high-pressure pump, the operation of the high-pressure pump is stopped and the dehydration is completed. Simplified equipment, making it easy to operate, dredged soil, sewage sludge, construction work whose properties are easy to change over time It can be made uniform water content of the cake after the dehydration of such waste soil containing water generated.
[0021]
And, if the moving time of the piston of the high-pressure pump becomes long after the moving time of the piston of the high-pressure pump becomes long, it is judged as an abnormal state, so that abnormalities such as breakage of the filter cloth and poor sealing of the filtration chamber are detected. And the operation of the dehydrator can be performed stably. In addition, the workplace can be safe and the environment can be protected.
[0022]
In the operation method of the high-pressure pump of the filter press type dehydrator according to claim 2, it is determined that an abnormal state occurs when the moving speed of the piston of the high-pressure pump increases after the moving speed of the piston of the high-pressure pump becomes slow. Therefore, it is possible to accurately detect abnormality such as breakage of the filter cloth and defective sealing of the filtration chamber, and the operation of the dehydrating apparatus can be performed more stably.
[Brief description of the drawings]
FIG. 1 is an overall view of a filter press dehydrator applied to a method of operating a high pressure pump of a filter press dehydrator according to an embodiment of the present invention.
FIG. 2 is a conceptual diagram of the high-pressure pump.
FIG. 3 is a graph showing the relationship between the dehydration time and the accumulated drainage amount.
FIG. 4 is a graph showing the relationship between dehydration time and piston movement time.
FIG. 5 is a graph showing the relationship between the dewatering time and the accumulated drainage amount in the conventional stock solution dewatering method.
[Explanation of symbols]
10: filter press type dehydrator, 11: filter press, 12: high pressure pump, 13: hydraulic unit, 14: suction pump, 15: filtration chamber, 21: hydraulic cylinder, 21a: piston, 21b: limit switch, 21c: limit Switch, 22: Muddy water pump, 22a: Rubber membrane, 22b: Rubber membrane, 23: Muddy water pump, 23a: Rubber membrane, 23b: Rubber membrane, 24: Hydraulic chamber, 25: Intermediate chamber, 26: Suction / discharge chamber, 27: Discharge valve, 28: suction valve, 29: hydraulic chamber, 30: intermediate chamber, 31: suction / discharge chamber, 32: discharge valve, 33: suction valve, 34: piping, 35: muddy water discharge tube, 36: piping, 37: Mud suction pipe

Claims (2)

フィルタープレス式脱水装置を用いた脱水の初期に、低圧ポンプにより原液を圧送し、この後に往復動型シリンダーを有する高圧ポンプから前記フィルタープレス式脱水装置に原液を圧送し、原液を脱水してケーキを製造するフィルタープレス式脱水装置の高圧ポンプの運転方法において、
原液を圧送する前記高圧ポンプのピストンの移動時間を予め設定しておき、設定された前記高圧ポンプのピストンの移動時間よりも該高圧ポンプのピストンの移動時間が長くなった時点で、前記高圧ポンプの運転を停止して脱水を完了し、
更に、前記高圧ポンプのピストンの移動時間が長くなった後、前記高圧ポンプのピストンの移動時間が短くなった場合を異常状態と判定することを特徴とするフィルタープレス式脱水装置の高圧ポンプの運転方法。
At the initial stage of dehydration using a filter press type dehydrator, the stock solution is pumped by a low pressure pump, and then the stock solution is pumped from the high pressure pump having a reciprocating cylinder to the filter press type dehydrator to dehydrate the stock solution and cake. In the operation method of the high pressure pump of the filter press type dehydrator for producing
The movement time of the piston of the high-pressure pump that pumps the stock solution is set in advance, and when the movement time of the piston of the high-pressure pump becomes longer than the set movement time of the piston of the high-pressure pump, the high-pressure pump Stop driving and complete dehydration ,
Furthermore, after the moving time of the piston of the high-pressure pump becomes long, it is determined as an abnormal state when the moving time of the piston of the high-pressure pump becomes short. Method.
請求項1記載のフィルタープレス式脱水装置の高圧ポンプの運転方法において、前記高圧ポンプのピストンの移動時間を該ピストンの移動速度に変換し、前記高圧ポンプのピストンの移動時間が長くなった後、前記高圧ポンプのピストンの移動時間が短くなった場合を異常状態と判定する代わりに、前記高圧ポンプのピストンの移動速度が遅くなった後、前記高圧ポンプのピストンの移動速度が速くなった場合を異常状態と判定することを特徴とするフィルタープレス式脱水装置の高圧ポンプの運転方法。In the operation method of the high pressure pump of the filter press type dehydrator according to claim 1, after converting the moving time of the piston of the high pressure pump into the moving speed of the piston, the moving time of the piston of the high pressure pump becomes long, Instead of determining that the movement time of the piston of the high-pressure pump is shortened as an abnormal state, the movement speed of the piston of the high-pressure pump is increased after the movement speed of the piston of the high-pressure pump is decreased. A method of operating a high-pressure pump of a filter press dehydrator characterized by determining an abnormal state .
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JP2010051909A (en) * 2008-08-29 2010-03-11 Parker Engineering Kk Anomaly detection method of filter cloth of filter press and filter press
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