JP2005000896A - Method and apparatus for pressure feeding of dewatered sludge - Google Patents

Method and apparatus for pressure feeding of dewatered sludge Download PDF

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JP2005000896A
JP2005000896A JP2003170554A JP2003170554A JP2005000896A JP 2005000896 A JP2005000896 A JP 2005000896A JP 2003170554 A JP2003170554 A JP 2003170554A JP 2003170554 A JP2003170554 A JP 2003170554A JP 2005000896 A JP2005000896 A JP 2005000896A
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sludge
dewatered sludge
dewatered
pipe
pumping
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JP2003170554A
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JP4296854B2 (en
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Takashi Mori
孝志 森
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IHI Corp
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IHI Corp
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Abstract

<P>PROBLEM TO BE SOLVED: To reduce pressure loss in pressure feeding a dewatered sludge without requiring a lubricant. <P>SOLUTION: One end part of a tapered pipe 4 whose diameter in the intermediate part is smaller than that in the both ends by the predetermined dimensions is detachably connected to the downstream side of a discharge pipe 2 of a pressure feeding pump 1 for sludge. The other end part of the tapered pipe 4 is detachably connected to the upstream side end part of a duct 3 for dewatered sludge. A dewatered sludge 6 is discharged by the operation of the pressure feeding pump 1 for sludge through the discharge pipe 2. The dewatered sludge 6 is compressed by being passed through a tapered throttle part 4a of the tapered pipe 4, thus making the moisture content contained inside the dewatered sludge 6 to come on the surface of the dewatered sludge 6. The water came on the surface of the dewatered sludge 6 is mediated between the surface and the inner wall surface of the duct 3 for dewatered sludge, thereby smoothly performing pressure feeding of the dewatered sludge 6 inside the duct 3 for dewatered sludge. <P>COPYRIGHT: (C)2005,JPO&NCIPI

Description

【0001】
【発明の属する技術分野】
本発明は下水処理施設等にて汚泥圧送ポンプを用いて脱水汚泥を焼却炉等の目的地へ圧送する際に用いるための脱水汚泥の圧送方法及び装置に関するものである。
【0002】
【従来の技術】
下水処理場で発生する下水汚泥は、下水中に含まれる有機物が活性汚泥処理され、微生物の形で固定された後、この微生物やその死骸、排泄物、その他の微細な懸濁粒子が、無機凝集剤や高分子凝集剤等の所要の凝集剤により凝集、沈降させられたものである。したがって、上記下水汚泥は有機物を多く含んでいることから、一般的には、重力分離や浮上分離などを用いて濃縮した後、真空脱水機やベルトプレス等の加圧式の脱水装置、或いは、遠心分離機等の脱水装置を用いて含水率を80〜65%程度まで低下させてケーキ状の脱水汚泥(脱水ケーキ)とした後、焼却炉に送って焼却処理されることが多い。
【0003】
このように、焼却処理を行うべく脱水汚泥を焼却炉へ送る場合には、脱水装置から回収される上記脱水汚泥が高い粘性を有することから、圧送ポンプを用いて脱水汚泥輸送管内を通して圧送するようにしている。
【0004】
この種の脱水汚泥の圧送に用いられるポンプとしては、たとえば、脱水汚泥を投入する汚泥受入ホッパの下部に接続した2本の圧送用シリンダ内のピストンを、それぞれ対応する2つの主油圧シリンダで交互に前進後退させることにより交互に吸入吐出作動ができるようにし、且つ上記汚泥受入ホッパ内に吸入吐出弁としての揺動管を揺動可能に設けて、一端を交互に上記各圧送用シリンダに連通するようにすると共に、他端を汚泥出口となる吐出管に接続させてあり、上記各圧送用シリンダの吸入吐出動作に同期して揺動管を切替作動させることにより、汚泥受入ホッパ内の脱水汚泥を上記各圧送用シリンダに交互に吸入した後、揺動管、吐出管を経て脱水汚泥輸送管内を下流側へ圧送できるようにしてなる往復動型のダブルピストン式の圧送ポンプが用いられている(たとえば、特許文献1参照)。
【0005】
ところで、上記脱水汚泥は、含水率が変動すると粘性が変化し、特に、含水率が低下すると粘性が高まるため、上記汚泥圧送ポンプの下流側に接続する脱水汚泥輸送管の途中に屈曲部が存在するような場合は、該屈曲部にて脱水汚泥の流通時の抵抗が高まり、このため脱水汚泥の圧送時における圧損が大となることが懸念される。
【0006】
上記ような脱水汚泥の圧送時における圧損を防止するためには、汚泥圧送管路中における脱水汚泥の流通を円滑に行わせるようにすればよいと考えられている。このような脱水汚泥の圧送管路中における流通を円滑に行なわせるための手法としては、たとえば、圧送ポンプの上流側に接続してある汚泥受入ホッパに受け入れられた脱水汚泥に、予め媒体油を添加しておくようにしたものがある。すなわち、脱水汚泥に媒体油を添加しておき、上記圧送ポンプにより圧送される脱水汚泥が搬送ラインを通過する際、上記添加されている媒体油が搬送ラインの内壁面に塗着されるようにして、この搬送ラインの内壁面に塗着された媒体油を該搬送ライン内を流通する脱水汚泥の潤滑油として作用させることにより、上記粘性を有する脱水汚泥の詰まりを防止して汚泥搬送を円滑に行わせるようにすることが提案されている(たとえば、特許文献2参照)。
【0007】
又、粘着性を有する加熱脱水汚泥の汚泥移送経路となるシュータの内壁面への付着、積層化を防止するための手法として、上記シュータの上部内壁に潤滑油を噴出させるための複数のノズルを設けて、該各ノズルより上記シュータの内壁に沿って潤滑油を噴射させることにより、該シュータの内壁面の全面に亘り潤滑油の皮膜を形成させ、これにより付着性のある脱水汚泥であっても付着を防止してスムーズに通過させるようにすることも提案されている(たとえば、特許文献3参照)。
【0008】
これらのことから、脱水汚泥の含水率が低下して粘度が上昇するときにも脱水汚泥圧送時の圧損の増大を防止できるようにするための対策としては、たとえば、汚泥圧送管路の屈曲部の直前位置に、潤滑剤注入装置を接続して潤滑油の如き潤滑剤を注入させ、これにより、汚泥圧送管路の屈曲部における内壁面と、その内側を流通する脱水汚泥の表面との間に上記潤滑剤を介在させるようにして、管内圧損の上昇を抑制するようにすることが考えられる。
【0009】
【特許文献1】
特開2003−63662号公報
【特許文献2】
特開平10−85794号公報
【特許文献3】
特開平11−165193号公報
【0010】
【発明が解決しようとする課題】
ところが、脱水汚泥の圧送時における圧損を防止するために、上記特許文献2及び特許文献3に示されたような潤滑油等の潤滑剤を注入する手法では、潤滑剤を消費するためランニングコストが嵩むという問題があると共に、潤滑剤注入装置を設ける必要があることから設備が複雑化して設備コストが嵩むという問題もある。
【0011】
そこで、本発明は、脱水汚泥の含水量が低下して該脱水汚泥の粘性が高まるような場合であっても、潤滑油等の潤滑剤を要することなく脱水汚泥圧送時の脱水汚泥輸送管内における汚泥の流通をスムーズに行わせることができて、圧損を低減させることができるようにする脱水汚泥の圧送方法及び装置を提供しようとするものである。
【0012】
【課題を解決するための手段】
本発明は、上記課題を解決するために、汚泥圧送ポンプより吐出させて圧送管路を通して目的地へ圧送される脱水汚泥を、圧送途中で圧縮することにより内部の水分を汚泥表面に滲出させて、該汚泥表面と管壁との間に水を発生させるようにして脱水汚泥を圧送する脱水汚泥の圧送方法、及び、汚泥圧送ポンプより吐出された脱水汚泥を圧送する圧送管路の途中位置に、上流側から縮径するようにした絞りを設け、該絞りで脱水汚泥を圧縮して内部に含まれている水分を脱水汚泥表面に滲出させて圧送させるようにしてなる構成を有する脱水汚泥の圧送装置とする。
【0013】
汚泥圧送ポンプの運転により脱水汚泥を圧送管路を通して下流側へ圧送するとき、脱水汚泥は上記圧送管路の途中で絞りを通過するときに圧縮される。この圧縮によって上記脱水汚泥の内部に含まれていた水分が脱水汚泥表面に滲出される。この一旦滲出された水は、脱水汚泥が上記絞りの下流側へ移行することにより圧縮状態が緩和されたとしても、脱水汚泥の表面部に存在するため、この水によって上記絞りよりも下流側の圧送管路内では、該圧送管路の内壁面と脱水汚泥の表面との間には、水が発生させられるようになる。このため、脱水汚泥の圧送管路内における流通がスムーズに行なわれるようになる。
【0014】
又、絞りとしてのテーパ状絞り部を形成したテーパ管を、圧送管路としての汚泥圧送ポンプの吐出管と脱水汚泥輸送管との間に着脱自在に取り付けるようにした構成とすることにより、口径の縮径率が異なる複数のテーパ管を用意しておくようにすれば、脱水汚泥の含水率の変化に伴う粘性の変化に伴って、該脱水汚泥の内部に含まれている水分を表面に滲出させるために要求される脱水汚泥の圧縮率が変化しても、該要求される脱水汚泥の圧縮率に対応した縮径率を備えたテーパ管を適宜選択して交換することで、含水率の異なる脱水汚泥の圧送時における圧損の防止を容易に図ることが可能になる。
【0015】
【発明の実施の形態】
以下、本発明の実施の形態を図面を参照して説明する。
【0016】
図1(イ)(ロ)は本発明の脱水汚泥の圧送方法及び装置の実施の一形態の概要を示すもので、汚泥圧送ポンプ1の吐出側に、圧送管路として、吐出管2と該吐出管2に接続して脱水汚泥を圧送するようにする脱水汚泥輸送管3が備えてある構成において、一例として、上記吐出管2と脱水汚泥輸送管3との接続部に、絞りとして、両端部を上記汚泥圧送ポンプ1の吐出管2及び脱水汚泥輸送管3の口径と同一の口径Dとし且つ中間部を両端部の口径Dよりも所要寸法小さい口径dとして両端部より中間部に向けて滑らかに縮径するテーパ状絞り部4aを備えた形状としてなるテーパ管4を介在させて、テーパ管4の一端部を吐出管2の下流側端部に着脱自在に接続し、該テーパ管4の他端部を、脱水汚泥輸送管3の上流側端部に着脱自在に接続する。
【0017】
上記汚泥圧送ポンプ1の吐出管2とテーパ管4の一端部との接続、及び、該テーパ管4の他端部と脱水汚泥輸送管3の上流側端部との接続は、たとえば、接続すべき端部同士にそれぞれフランジ部2a,4b及び3a,4bを形成しておき、互いに当接させた上記吐出管2とテーパ管4及びテーパ管4と脱水汚泥輸送管3のフランジ部2a,4b及び3a,4b同士を、ボルト・ナット5を用いて取り外し可能に連結させるようにすればよい。
【0018】
上記テーパ管4の両端部より中間部に向けて形成されるテーパ状絞り部4aの傾斜角度は、汚泥圧送用ポンプ1の吐出管2より所要圧力で吐出される脱水汚泥6を、上記テーパ管4に上流側端部より上記縮径するテーパ状絞り部4aに沿わせて中間部へ向けて進行させるときに、上記脱水汚泥6を圧縮して該脱水汚泥6中に含まれている水分を該脱水汚泥6の表面へ浮き出させることができるような傾斜角度として設定してある。更に、中間部へ向けて絞るように縮径した後は、下流側となる他端側へ拡径して脱水汚泥6を膨張させて下流側へ送るようにしてある。したがって、上記テーパ管4の長さ寸法、及び、両端部の口径Dに対する中間部の口径dの縮径率は、汚泥圧送ポンプ1の吐出圧力や、汚泥圧送ポンプ1の吐出管2の口径及び上記テーパ状絞り部4aに要求される傾斜角度に基いて適宜決定するようにすればよい。
【0019】
なお、7は汚泥圧送ポンプ1の吸入側に設けた汚泥受入ホッパである。
【0020】
上記構成としてある本発明の脱水汚泥の圧送方法及び装置により脱水汚泥6の圧送を行う場合には、汚泥受入ホッパ7に投入された脱水汚泥6を、汚泥圧送用ポンプ1の運転により該ポンプ1の吐出管2を経て吐出させるようにする。吐出管2を経て吐出された脱水汚泥6は、上記テーパ管4内に送り込まれて一端部側より他端部側へ通過させられるときに、該テーパ管4の上流側端部より中間部に向けて縮径するテーパ状絞り部4aで徐々に圧縮されることになる。
【0021】
ここで、凝集した汚泥に対する水の結合状態について調べてみると、汚泥に結合している水には、図2に示す如く、汚泥粒子6aの凝集物の周囲に存在する自由水8、汚泥粒子6aが凝集するときに周囲を汚泥粒子6aに囲まれることで形成される間隙(空隙)に取り込まれている間隙水9、凝集により互いに隣接する汚泥粒子6a同士の間に形成されている毛管状の隙間に取り込まれた毛管結合水10、個々の汚泥粒子6aの内部に取り込まれている内部保留水11、汚泥粒子6aの表面に結合している表面付着水12、汚泥粒子6a中等に含まれる塩類等の結晶に結合して含まれる結晶水(図示せず)等がある。これらの水は、その結合状態によって汚泥との離脱性(脱水性)の難易度が変化し、自由水8、間隙水9、毛管結合水10、表面付着水12、内部保留水11、結晶水の順に脱水がより困難になり、機械脱水では、自由水8や間隙水9、毛管結合水10の一部が脱水しているに過ぎない。このために、脱水汚泥6の内部にはかなりの量の水分が残留しており、脱水汚泥6を圧縮すると、該脱水汚泥6の内部に残存している水分の一部を、脱水汚泥6の表面へ浮き出させる(滲出させる)ことが可能となる。なお、脱水汚泥6を圧縮した際に該脱水汚泥6の表面に一旦浮き出された水は、その後、脱水汚泥6に対する圧縮を緩和させたとしても、上記脱水汚泥6の表面に浮き出されたままとなる。
【0022】
本発明では、上記脱水汚泥6を圧縮することにより内部の水が表面に浮き出る性質を利用し、上記浮き出された水により円滑に脱水汚泥輸送管3内を圧送させるようにしようとするものである。
【0023】
上記において、吐出管2からテーパ管4に送り込まれた脱水汚泥6が、テーパ状絞り部4aで徐々に圧縮されて行く過程で脱水汚泥6中に含まれる水分の一部を該脱水汚泥6の表面に滲出させると、この滲出した水は、脱水汚泥6の表面と脱水汚泥輸送管3の内壁面部との間に発生させられた状態となる。これにより脱水汚泥6は、内部から滲出した水で包まれた状態でテーパ管4内から脱水汚泥輸送管3内に移されるようにする。この際、テーパ管4の下流側端部で径が拡げられても、脱水汚泥6の表面に滲出した水は、脱水汚泥輸送管3の内壁面に沿って保持されたままとなる性質を利用して脱水汚泥輸送管3内を流通させることができるようにする。
【0024】
このように、脱水汚泥6の圧送時に、該脱水汚泥6の表面と脱水汚泥輸送管3の内壁面との間には水を発生させることができるようにしてあるため、この水の存在によって圧送される脱水汚泥6が脱水汚泥輸送管3内壁面へ付着するのを未然に防止することができる。このため、脱水汚泥6の含水率が50%程度まで低下して粘性が大となった場合であっても、脱水汚泥6の圧送をスムーズに行なわせることができて、脱水汚泥6の圧送時における圧損を低減することができる。しかも、上記脱水汚泥6の圧送時に該脱水汚泥6の表面と脱水汚泥輸送管3の内壁面との間に発生させられる水は、汚泥圧送ポンプ1より吐出される脱水汚泥6をテーパ管4のテーパ状絞り部4aで圧縮することによって発生させられるものであるため、外部からの供給は不要である。したがって、従来のように、潤滑油の如き潤滑剤を使用して脱水汚泥圧送時の圧損の低減を図る場合に比してランニングコスト及び設備コストの低減を図ることが可能になる。
【0025】
更に、上記テーパ管4は、汚泥圧送ポンプ1の吐出管2と脱水汚泥輸送管3との間に着脱自在に取り付けてあるため、脱水汚泥6の含水率が変化することに伴って圧縮率を変化させて常に内部の水分を表面に浮き出させるようにする場合には、両端部の口径Dに対する中間部の口径dの縮径率が異なる複数のテーパ管4を用意しておくようにする。このようにすれば、圧送すべき脱水汚泥6の含水率に応じて該脱水汚泥6の内部の水分を滲出させるために要求される圧縮率に対応できる縮径率を備えたテーパ管4を適宜選択して交換することができて、含水率の異なる脱水汚泥6の圧送時における圧損の防止を容易に図ることが可能になる。
【0026】
なお、本発明は上記実施の形態のみに限定されるものではなく、テーパ管4は、必要に応じて両端部口径Dに対する中間部口径dの縮径率の異なるものに容易に交換できるよう、汚泥圧送ポンプ1及び脱水汚泥輸送管3とは別体とすることが望ましいが、汚泥圧送用ポンプ1内の吐出管2の途中位置に絞りとしてテーパ状絞り部を設けて脱水汚泥6を圧縮するようにしたり、脱水汚泥輸送管3の上流部に絞りとしてテーパ状の絞り部を設けるようにしてもよい。又、上記テーパ管4は、中間部に向けて両端部から同様の傾斜を有するテーパ状絞り部4aを備えたものとして示したが、上流側となる一端側から中間部にかけての傾斜角度と、下流側となる他端部から中間部にかけての傾斜角度が相違する形状としてもよく、更には、テーパ状絞り部4aの途中で傾斜角度が変化する形状のものとしてもよい。更に、汚泥圧送ポンプ1は、往復動型のダブルピストン式以外の形式のものであってもよいこと、その他本発明の要旨を逸脱しない範囲内において種々変更を加え得ることは勿論である。
【0027】
【発明の効果】
以上述べた如く、本発明によれば、以下の如き優れた効果を発揮する。
(1) 汚泥圧送ポンプより吐出させて圧送管路を通して目的地へ圧送される脱水汚泥を、圧送途中で圧縮することにより内部の水分を汚泥表面に滲出させて、該汚泥表面と管壁との間に水を発生させるようにして脱水汚泥を圧送する脱水汚泥の圧送方法、及び、汚泥圧送ポンプより吐出された脱水汚泥を圧送する圧送管路の途中位置に、上流側から縮径するようにした絞りを設け、該絞りで脱水汚泥を圧縮して内部に含まれている水分を脱水汚泥表面に滲出させて圧送させるようにしてなる構成を有する脱水汚泥の圧送装置としてあるので、脱水汚泥の圧送時に、絞りよりも下流側の圧送管路内では、該圧送管路の内壁面と脱水汚泥の表面との間に水を発生させた状態にて脱水汚泥の流通を行なわせることができることから、脱水汚泥の含水率が低下して粘度が高まったとしても、該脱水汚泥の圧送をスムーズに行わせることができて、脱水汚泥の圧送時における圧損を低減することができる。
(2) 上記脱水汚泥の圧送時に該脱水汚泥の表面と圧送管路の内壁面との間に発生させる水は、脱水汚泥を、絞りを通過させることにより圧縮することによって該脱水汚泥の内部より滲出させて供給できる。このため、外部からの水の供給は不要であることから、潤滑油の如き潤滑剤を使用して脱水汚泥圧送時の圧損の低減を図る場合に比してランニングコスト及び設備コストの低減を図ることが可能になる。
(3) 絞りとしてのテーパ状絞り部を形成したテーパ管を、圧送管路としての汚泥圧送ポンプの吐出管と脱水汚泥輸送管との間に着脱自在に取り付けるようにした構成とすることにより、口径の縮径率が異なる複数のテーパ管を用意しておくようにすれば、脱水汚泥の含水率の変化に伴う粘性の変化に伴って、該脱水汚泥の内部に含まれている水分を表面に滲出させるために要求される脱水汚泥の圧縮率が変化しても、該要求される脱水汚泥の圧縮率に対応した縮径率を備えたテーパ管を適宜選択して交換することで、含水率の異なる脱水汚泥の圧送時における圧損の防止を容易に図ることが可能になる。
【図面の簡単な説明】
【図1】本発明の脱水汚泥の圧送方法及び装置の実施の一形態を示すもので、(イ)は概略側面図、(ロ)は要部を拡大して示す図である。
【図2】汚泥と水の結合状態を模式的に示す図である。
【符号の説明】
1 汚泥圧送ポンプ
2 吐出管(圧送管路)
3 脱水汚泥輸送管(圧送管路)
4 テーパ管(絞り)
4a テーパ状絞り部(絞り)
6 脱水汚泥
[0001]
BACKGROUND OF THE INVENTION
The present invention relates to a dewatered sludge pumping method and apparatus for use in pumping dewatered sludge to a destination such as an incinerator using a sludge pump in a sewage treatment facility or the like.
[0002]
[Prior art]
The sewage sludge generated at the sewage treatment plant is treated with activated sludge from organic matter contained in the sewage and fixed in the form of microorganisms, and then these microorganisms, their dead bodies, excrement, and other fine suspended particles are inorganic. It is agglomerated and precipitated by a required aggregating agent such as an aggregating agent or a polymer aggregating agent. Therefore, since the sewage sludge contains a large amount of organic matter, it is generally concentrated using gravity separation, flotation separation, etc., and then pressurized dehydration equipment such as a vacuum dehydrator or a belt press, or a centrifugal separator. In many cases, the moisture content is reduced to about 80 to 65% using a dehydrating device such as a separator to form a cake-like dewatered sludge (dehydrated cake), and then sent to an incinerator for incineration.
[0003]
Thus, when dehydrated sludge is sent to an incinerator for incineration, the dehydrated sludge recovered from the dehydrator has a high viscosity, so that it is pumped through the dehydrated sludge transport pipe using a pump. I have to.
[0004]
As a pump used for the pumping of this kind of dewatered sludge, for example, the pistons in the two pumping cylinders connected to the lower part of the sludge receiving hopper for feeding the dewatered sludge are alternately switched by two corresponding main hydraulic cylinders. The suction / discharge operation can be performed alternately by moving forward and backward, and a swing pipe as a suction / discharge valve is swingably provided in the sludge receiving hopper, and one end communicates with each of the pressure feeding cylinders alternately. In addition, the other end is connected to a discharge pipe serving as a sludge outlet, and the dewatering in the sludge receiving hopper is performed by switching the oscillating pipe in synchronization with the suction and discharge operation of each of the pressure feeding cylinders. Reciprocating double-piston type pistons that allow sludge to be alternately sucked into the above-mentioned cylinders for pumping, and then pumped down the dewatered sludge transport pipe through the swing pipe and discharge pipe. Feed pump is used (e.g., see Patent Document 1).
[0005]
By the way, the viscosity of the dewatered sludge changes when the water content varies, and particularly when the water content decreases, the viscosity increases. Therefore, there is a bent portion in the middle of the dewatered sludge transport pipe connected to the downstream side of the sludge pump. In such a case, there is a concern that the resistance at the time of circulation of the dewatered sludge increases at the bent portion, and therefore, the pressure loss at the time of pressure feeding of the dehydrated sludge increases.
[0006]
In order to prevent such pressure loss during dewatered sludge pumping, it is considered that the dewatered sludge can be smoothly distributed in the sludge pumping line. As a method for smoothly circulating such dewatered sludge in the pressure feed line, for example, medium oil is previously applied to the dewatered sludge received in the sludge receiving hopper connected to the upstream side of the pressure feed pump. Some have been added. That is, medium oil is added to the dewatered sludge, and when the dehydrated sludge pumped by the pressure pump passes through the transport line, the added medium oil is applied to the inner wall surface of the transport line. Then, the medium oil applied to the inner wall surface of the transfer line is allowed to act as lubricating oil for the dehydrated sludge that circulates in the transfer line, thereby preventing clogged dehydrated sludge having the above-mentioned viscosity and smoothing the sludge transfer. Has been proposed (see, for example, Patent Document 2).
[0007]
In addition, as a technique for preventing adhesion and lamination of the shooter serving as a sludge transfer path for the heated dehydrated sludge having adhesiveness, a plurality of nozzles for jetting lubricating oil to the upper inner wall of the shooter are provided. And a lubricant film is formed over the entire inner wall surface of the shooter by spraying the lubricant oil from the nozzles along the inner wall of the shooter. It has also been proposed to prevent the sticking and allow it to pass smoothly (see, for example, Patent Document 3).
[0008]
Therefore, as a measure for preventing an increase in pressure loss during dewatered sludge pumping even when the moisture content of the dewatered sludge decreases and the viscosity increases, for example, a bent portion of a sludge pumping pipeline A lubricant injection device is connected to a position immediately before the injection of a lubricant such as lubricating oil, so that the space between the inner wall surface at the bent portion of the sludge pressure feeding line and the surface of the dewatered sludge flowing inside the sludge It is conceivable to suppress the increase in the pressure loss in the pipe by interposing the above-mentioned lubricant.
[0009]
[Patent Document 1]
Japanese Patent Laid-Open No. 2003-63662 [Patent Document 2]
JP-A-10-85794 [Patent Document 3]
Japanese Patent Laid-Open No. 11-165193
[Problems to be solved by the invention]
However, in order to prevent pressure loss at the time of dewatered sludge pumping, in the method of injecting a lubricant such as lubricating oil as shown in Patent Document 2 and Patent Document 3 above, the running cost is low because the lubricant is consumed. In addition to the problem that it is bulky, there is also a problem that the equipment becomes complicated and the equipment cost increases because it is necessary to provide a lubricant injection device.
[0011]
Therefore, the present invention is a case where the water content of the dewatered sludge is reduced and the viscosity of the dewatered sludge is increased. It is an object of the present invention to provide a dewatered sludge pressure-feeding method and apparatus that can smoothly distribute sludge and reduce pressure loss.
[0012]
[Means for Solving the Problems]
In order to solve the above-mentioned problems, the present invention allows dehydrated sludge discharged from a sludge pump to be pumped to a destination through a pumping pipeline, and compresses the sludge in the middle of pumping to exude moisture inside the sludge. , A method of pumping dewatered sludge by pumping dehydrated sludge so as to generate water between the sludge surface and the pipe wall, and a midway position of a pumping line for pumping dewatered sludge discharged from the sludge pump. A dewatered sludge having a configuration in which a throttle is provided that is reduced in diameter from the upstream side, and the dewatered sludge is compressed by the throttle so that moisture contained therein is exuded to the surface of the dehydrated sludge and pumped. A pumping device is used.
[0013]
When the dewatered sludge is pumped downstream through the pumping pipeline by operating the sludge pump, the dewatered sludge is compressed when passing through the throttle in the middle of the pumping pipeline. By this compression, moisture contained in the dehydrated sludge is oozed out on the surface of the dehydrated sludge. Even if the dewatered sludge is reduced in the compressed state due to the dewatered sludge moving to the downstream side of the throttle, the water that has been leached is present on the surface of the dewatered sludge. In the pressure feed line, water is generated between the inner wall surface of the pressure feed line and the surface of the dewatered sludge. For this reason, the distribution of the dewatered sludge in the pressure-feed pipeline is smoothly performed.
[0014]
In addition, by adopting a configuration in which a taper pipe formed with a tapered throttle part as a throttle is detachably attached between a discharge pipe of a sludge pressure feed pump as a pressure feed line and a dewatered sludge transport pipe, If a plurality of taper pipes with different diameter reduction ratios are prepared, the moisture contained in the dewatered sludge is changed on the surface as the viscosity changes due to the change in the moisture content of the dewatered sludge. Even if the compression rate of the dewatered sludge required for leaching changes, the water content can be changed by appropriately selecting and replacing a taper tube having a reduced diameter corresponding to the required dewatered sludge compression rate. Therefore, it is possible to easily prevent pressure loss at the time of pumping dewatered sludge having different sizes.
[0015]
DETAILED DESCRIPTION OF THE INVENTION
Hereinafter, embodiments of the present invention will be described with reference to the drawings.
[0016]
FIGS. 1 (a) and 1 (b) show an outline of an embodiment of a dewatered sludge pressure feeding method and apparatus according to the present invention. The discharge pipe 2 and the pressure pipe are connected to the discharge side of the sludge pressure feed pump 1 as a pressure feed line. In the configuration provided with the dewatered sludge transport pipe 3 that is connected to the discharge pipe 2 and pumps the dehydrated sludge, as an example, the connecting portion between the discharge pipe 2 and the dewatered sludge transport pipe 3 is provided with both ends as a throttle. The diameter is the same as the diameter of the discharge pipe 2 and the dewatered sludge transport pipe 3 of the sludge pump 1 and the middle part has a diameter d smaller than the diameter D of both ends, and is directed from both ends toward the middle part. One end of the taper tube 4 is detachably connected to the downstream end of the discharge pipe 2 through a taper tube 4 having a shape with a tapered throttle portion 4a that smoothly reduces the diameter. The other end of the tube can be attached to and detached from the upstream end of the dewatered sludge transport pipe 3 To continue.
[0017]
The connection between the discharge pipe 2 of the sludge pump 1 and one end of the taper pipe 4 and the connection between the other end of the taper pipe 4 and the upstream end of the dewatered sludge transport pipe 3 are, for example, connected. Flange portions 2a, 4b and 3a, 4b are respectively formed at the power ends, and the discharge pipe 2, taper pipe 4, taper pipe 4, and flange portions 2a, 4b of the dewatered sludge transport pipe 3 are in contact with each other. And 3a and 4b may be detachably connected using bolts and nuts 5.
[0018]
The inclination angle of the tapered throttle portion 4a formed from both ends of the taper tube 4 toward the intermediate portion is such that the dewatered sludge 6 discharged from the discharge tube 2 of the sludge pressure pump 1 at a required pressure is used as the taper tube. 4, when the dewatered sludge 6 is compressed toward the intermediate portion along the tapered throttle portion 4 a that is reduced in diameter from the upstream end, the water contained in the dewatered sludge 6 is reduced. The inclination angle is set so that it can be raised on the surface of the dewatered sludge 6. Further, after the diameter is reduced so as to be squeezed toward the intermediate portion, the diameter is increased to the other end side which is the downstream side, and the dewatered sludge 6 is expanded and sent to the downstream side. Therefore, the length dimension of the taper pipe 4 and the reduction ratio of the diameter d of the middle part with respect to the diameter D of both ends are determined by the discharge pressure of the sludge pump 1 and the diameter of the discharge pipe 2 of the sludge pump 1. What is necessary is just to determine suitably based on the inclination-angle requested | required of the said taper-shaped aperture | diaphragm | squeeze part 4a.
[0019]
A sludge receiving hopper 7 is provided on the suction side of the sludge pump 1.
[0020]
When the dewatered sludge 6 is pumped by the dewatered sludge pressure feeding method and apparatus of the present invention having the above-described configuration, the dewatered sludge 6 introduced into the sludge receiving hopper 7 is transferred to the pump 1 by the operation of the sludge pump 1. It is made to discharge through the discharge pipe 2 of this. When the dewatered sludge 6 discharged through the discharge pipe 2 is fed into the taper pipe 4 and passed from the one end side to the other end side, the dewatered sludge 6 is moved from the upstream end of the taper pipe 4 to the intermediate portion. The taper is gradually compressed by the tapered throttle portion 4a that is reduced in diameter.
[0021]
Here, when examining the binding state of water to the agglomerated sludge, as shown in FIG. 2, free water 8 and sludge particles existing around the agglomerates of the sludge particles 6a are included in the water bound to the sludge. The pore water 9 taken in the gap (gap) formed by surrounding the sludge particles 6a when the 6a agglomerates, and the capillaries formed between the sludge particles 6a adjacent to each other by agglomeration Capillary binding water 10 taken into the gap, internal retained water 11 taken into the individual sludge particles 6a, surface adhering water 12 bound to the surface of the sludge particles 6a, sludge particles 6a, etc. There is water of crystallization (not shown) that is contained in crystals such as salts. These waters vary in the degree of difficulty in separating (dehydrating) from sludge depending on their binding state, and include free water 8, pore water 9, capillary-bonded water 10, surface adhering water 12, internal reserve water 11, and crystal water. In this order, dehydration becomes more difficult, and in the mechanical dehydration, only a part of the free water 8, the interstitial water 9, and the capillary combined water 10 is dehydrated. For this reason, a considerable amount of water remains inside the dewatered sludge 6. When the dewatered sludge 6 is compressed, a part of the water remaining in the dewatered sludge 6 is removed from the dewatered sludge 6. It can be raised (exuded) on the surface. It should be noted that when the dewatered sludge 6 is compressed, the water that once floated on the surface of the dewatered sludge 6 remains floating on the surface of the dewatered sludge 6 even if the compression on the dewatered sludge 6 is eased thereafter. Become.
[0022]
In the present invention, the dewatered sludge 6 is compressed to take advantage of the property that the water inside floats to the surface, and the inside of the dewatered sludge transport pipe 3 is smoothly pumped by the raised water. .
[0023]
In the above, a part of the water contained in the dewatered sludge 6 in the process of the dewatered sludge 6 sent from the discharge pipe 2 to the taper pipe 4 being gradually compressed by the tapered throttle portion 4a. When exuded on the surface, the exuded water is generated between the surface of the dehydrated sludge 6 and the inner wall surface of the dehydrated sludge transport pipe 3. As a result, the dewatered sludge 6 is transferred from the taper pipe 4 into the dewatered sludge transport pipe 3 in a state of being wrapped with water oozed from the inside. At this time, even if the diameter is expanded at the downstream end of the taper pipe 4, the water that has oozed out on the surface of the dewatered sludge 6 is retained along the inner wall surface of the dewatered sludge transport pipe 3. Thus, the dewatered sludge transport pipe 3 can be circulated.
[0024]
In this way, when the dewatered sludge 6 is pumped, water can be generated between the surface of the dewatered sludge 6 and the inner wall surface of the dewatered sludge transport pipe 3. It is possible to prevent the dewatered sludge 6 to be adhered to the inner wall surface of the dewatered sludge transport pipe 3 in advance. For this reason, even when the water content of the dewatered sludge 6 is reduced to about 50% and the viscosity becomes large, the dewatered sludge 6 can be smoothly pumped. The pressure loss in can be reduced. Moreover, the water generated between the surface of the dewatered sludge 6 and the inner wall surface of the dewatered sludge transport pipe 3 during the pumping of the dewatered sludge 6 causes the dewatered sludge 6 discharged from the sludge pressure pump 1 to flow through the taper tube 4. Since it is generated by compressing with the tapered throttle portion 4a, supply from the outside is not necessary. Accordingly, it is possible to reduce the running cost and the equipment cost as compared with the conventional case where a lubricant such as lubricating oil is used to reduce the pressure loss at the time of dewatered sludge pumping.
[0025]
Further, since the taper pipe 4 is detachably attached between the discharge pipe 2 of the sludge pump 1 and the dewatered sludge transport pipe 3, the compression rate is reduced as the moisture content of the dewatered sludge 6 changes. In the case where the internal moisture is always made to float on the surface by changing, a plurality of taper tubes 4 having different diameter reduction ratios of the diameter d of the middle part with respect to the diameter D of both ends are prepared. In this way, the taper tube 4 having a diameter reduction rate that can correspond to the compression rate required for exuding the moisture inside the dewatered sludge 6 according to the water content of the dewatered sludge 6 to be pumped is appropriately selected. It can be selected and replaced, and it is possible to easily prevent pressure loss during the pressure-feeding of the dewatered sludge 6 having different moisture contents.
[0026]
In addition, this invention is not limited only to the said embodiment, The taper pipe | tube 4 can be easily replaced | exchanged for what has the diameter reduction ratio of the intermediate part diameter d with respect to both-ends diameter D as needed easily. Although it is desirable to make it separate from the sludge pressure pump 1 and the dewatered sludge transport pipe 3, the tapered sludge 6 is provided as a throttle in the middle of the discharge pipe 2 in the sludge pressure pump 1 to compress the dewatered sludge 6. Alternatively, a tapered throttle portion may be provided at the upstream portion of the dewatered sludge transport pipe 3 as a throttle. Moreover, although the said taper pipe | tube 4 was shown as what was equipped with the taper-shaped aperture | diaphragm | squeeze part 4a which has the same inclination from both ends toward an intermediate part, the inclination angle from the one end side used as an upstream to an intermediate part, It may have a shape in which the inclination angle from the other end portion on the downstream side to the intermediate portion is different, or may have a shape in which the inclination angle changes in the middle of the tapered throttle portion 4a. Furthermore, the sludge pump 1 may be of a type other than the reciprocating double piston type, and other various modifications may be made without departing from the scope of the present invention.
[0027]
【The invention's effect】
As described above, according to the present invention, the following excellent effects are exhibited.
(1) The dehydrated sludge discharged from the sludge pump and pumped to the destination through the pumping line is compressed in the middle of the pumping to exude moisture from the sludge surface. In order to reduce the diameter from the upstream side to the midway position of the dewatering sludge pumping method that pumps dehydrated sludge so that water is generated in between, and the dewatered sludge discharged from the sludge pump Since the dewatered sludge has a structure configured to compress the dehydrated sludge with the squeeze and exude the moisture contained therein to the surface of the dehydrated sludge and pump it, During pumping, dewatered sludge can be circulated in a state where water is generated between the inner wall surface of the pumped pipe and the surface of the dewatered sludge in the pumped line downstream of the throttle. Water content of dewatered sludge Even if the rate decreases and the viscosity increases, the dewatered sludge can be pumped smoothly, and the pressure loss during the dewatered sludge pumping can be reduced.
(2) The water generated between the surface of the dewatered sludge and the inner wall surface of the pressure-feed pipeline during the pumping of the dewatered sludge is compressed from the inside of the dewatered sludge by compressing the dewatered sludge by passing through a throttle. Can be exuded and supplied. For this reason, since supply of water from the outside is unnecessary, the running cost and the equipment cost are reduced as compared with the case of using a lubricant such as lubricating oil to reduce the pressure loss at the time of dewatered sludge pumping. It becomes possible.
(3) By adopting a configuration in which the tapered pipe formed with the tapered throttle section as the throttle is detachably attached between the discharge pipe of the sludge pressure feed pump as the pressure feed pipe and the dewatered sludge transport pipe, If a plurality of tapered pipes with different diameter reduction ratios are prepared, the moisture contained in the dewatered sludge is removed from the surface as the viscosity changes due to the change in the moisture content of the dewatered sludge. Even if the compression rate of the dewatered sludge required for leaching is changed, the taper tube having a diameter reduction rate corresponding to the required dewatered sludge compression rate is appropriately selected and replaced, so that It is possible to easily prevent pressure loss during the pumping of dewatered sludge having different rates.
[Brief description of the drawings]
FIG. 1 shows an embodiment of a dewatered sludge pumping method and apparatus according to the present invention. FIG. 1 (a) is a schematic side view, and FIG.
FIG. 2 is a diagram schematically showing a combined state of sludge and water.
[Explanation of symbols]
1 Sludge pressure pump 2 Discharge pipe (pressure line)
3 Dewatered sludge transport pipe (pressure feed line)
4 Taper tube (diaphragm)
4a Tapered diaphragm (diaphragm)
6 Dewatered sludge

Claims (3)

汚泥圧送ポンプより吐出させて圧送管路を通して目的地へ圧送される脱水汚泥を、圧送途中で圧縮することにより内部の水分を汚泥表面に滲出させて、該汚泥表面と管壁との間に水を発生させるようにして脱水汚泥を圧送することを特徴とする脱水汚泥の圧送方法。The dehydrated sludge discharged from the sludge pump and pumped to the destination through the pressure pipe is compressed in the middle of the pumping so that the moisture inside the sludge exudes and the water between the sludge surface and the pipe wall A method for pumping dehydrated sludge, characterized in that dehydrated sludge is pumped in such a manner as to generate water. 汚泥圧送ポンプより吐出された脱水汚泥を圧送する圧送管路の途中位置に、上流側から縮径するようにした絞りを設け、該絞りで脱水汚泥を圧縮して内部に含まれている水分を脱水汚泥表面に滲出させて圧送させるようにしてなることを特徴とする脱水汚泥の圧送装置。A throttle that is reduced in diameter from the upstream side is provided in the middle of the pumping pipeline for pumping the dewatered sludge discharged from the sludge pump, and the dewatered sludge is compressed by the throttle to reduce the moisture contained inside. A dewatered sludge pumping device characterized in that the dewatered sludge is exuded on the surface and pumped. 絞りとしてのテーパ状絞り部を形成したテーパ管を、圧送管路としての汚泥圧送ポンプの吐出管と脱水汚泥輸送管との間に着脱自在に取り付けるようにした請求項2記載の脱水汚泥の圧送装置。3. The dewatered sludge pressure feed according to claim 2, wherein a taper pipe formed with a taper-shaped restrictor as a restrictor is detachably attached between a discharge pipe of a sludge pressure feed pump as a pressure feed line and a dehydrated sludge transport pipe. apparatus.
JP2003170554A 2003-06-16 2003-06-16 Method and apparatus for pumping dewatered sludge Expired - Fee Related JP4296854B2 (en)

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Cited By (2)

* Cited by examiner, † Cited by third party
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JP2007050374A (en) * 2005-08-19 2007-03-01 Sumitomo Osaka Cement Co Ltd Method for transporting sludge with low water content, transporting device therefor, and cement production equipment
JP2009297703A (en) * 2008-05-13 2009-12-24 Mitsubishi Heavy Industries Environment & Chemical Engineering Co Ltd Method and apparatus for transporting organic dewatered sludge

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
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JP2009297703A (en) * 2008-05-13 2009-12-24 Mitsubishi Heavy Industries Environment & Chemical Engineering Co Ltd Method and apparatus for transporting organic dewatered sludge

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