JP6141805B2 - Method and apparatus for concentrating sludge - Google Patents

Method and apparatus for concentrating sludge Download PDF

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JP6141805B2
JP6141805B2 JP2014145273A JP2014145273A JP6141805B2 JP 6141805 B2 JP6141805 B2 JP 6141805B2 JP 2014145273 A JP2014145273 A JP 2014145273A JP 2014145273 A JP2014145273 A JP 2014145273A JP 6141805 B2 JP6141805 B2 JP 6141805B2
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佐藤 進
佐藤  進
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Description

本発明は、ホッパー構造を有する汚泥濃縮槽における汚泥の濃縮方法およびその装置に関するものである。   The present invention relates to a sludge concentration method and apparatus in a sludge concentration tank having a hopper structure.

一般に、汚水・排水の浄化処理プロセスにおいて、発生する汚泥(スラリー)の処理には、曝気沈砂槽、原水ポンプ槽、流量調整槽、曝気槽、沈殿槽、散水ポンプ槽、消毒槽の順に処理槽を設け、沈殿槽から汚泥引き抜きポンプで引き抜かれた余剰汚泥を汚泥濃縮槽に導き、汚泥濃縮槽で処理された脱離液を流量調整槽に戻し、沈殿した濃縮汚泥を汚泥貯留槽に送って貯留し、その後搬出するようにしている。従来、この汚泥濃縮槽での固液分離の効率化を図るため、汚泥濃縮槽内に水路棒を垂直に設置し、この水路棒を横移動させ汚泥液中に水路を形成することにより懸濁粒子群の沈降速度を早めるようにした汚泥の濃縮方法およびその装置が提案されている(例えば、特許文献1および2参照。)。   Generally, in the purification process of sewage and wastewater, the treatment tanks are treated in the order of aeration sand tank, raw water pump tank, flow rate adjustment tank, aeration tank, precipitation tank, sprinkling pump tank, disinfection tank. The excess sludge extracted from the sedimentation tank by the sludge extraction pump is guided to the sludge concentration tank, the desorbed liquid treated in the sludge concentration tank is returned to the flow rate adjustment tank, and the precipitated concentrated sludge is sent to the sludge storage tank. It is stored and then removed. Conventionally, in order to improve the efficiency of solid-liquid separation in this sludge concentration tank, a water channel rod is installed vertically in the sludge concentration tank, and this water channel rod is moved laterally to form a water channel in the sludge liquid. There has been proposed a method and an apparatus for concentrating sludge so as to increase the sedimentation rate of particle groups (see, for example, Patent Documents 1 and 2).

特開2001−321800号公報JP 2001-321800 A 特開2003−200006号公報JP 2003-200006 A

特許文献1および2に記載の汚泥の濃縮方法およびその装置では、水路棒を水面上に露出させ、槽内で緩やかに回転させることにより水路(みずみち)を形成するようにしている。また、特許文献2に記載の汚泥の濃縮方法およびその装置では、槽内の中央部に縦方向に配置された回転軸に水路棒用固定翼を放射状に横向きに設け、この固定翼に水路棒を縦向きに設けて、回転軸をゆっくりと回転させ、水路を形成するようにしている。   In the sludge concentration method and apparatus described in Patent Documents 1 and 2, the water channel rod is exposed on the water surface and gently rotated in the tank to form a water channel. Further, in the sludge concentration method and apparatus described in Patent Document 2, the fixed wings for waterway rods are provided radially and horizontally on the rotating shaft arranged in the vertical direction at the center of the tank, and the waterway rods are provided on the fixed wings. Is provided in the vertical direction, and the rotating shaft is slowly rotated to form a water channel.

ところが、上記従来の汚泥の濃縮方法およびその装置では、水路棒上端を水面上に延長させているため、濃縮槽が大型化すると水路棒の長さを延ばし、しかも、配置する水路棒の数を増やさなければならず、水路棒の駆動装置が大型化しコストアップを招くという問題がある。また、水路棒の本数が多く、特に濃縮槽の中央部では、その密度が高くなるため、水路棒に汚泥中のし渣が絡みつき、水路(みずみち)の形成や濃縮効果の低減を生じる。このため、絡みついたし渣の除去、清掃等の作業を頻繁に行わなければならないという問題がある。   However, in the above conventional sludge concentration method and apparatus, since the upper end of the water channel rod is extended above the water surface, the length of the water channel rod is increased when the concentration tank is enlarged, and the number of water channel rods to be arranged is increased. There is a problem that the driving device for the waterway rod is enlarged and the cost is increased. In addition, since the number of waterway rods is large, especially in the central part of the concentration tank, the density becomes high, and the residue in the sludge is entangled with the waterway rods, resulting in the formation of waterways and the reduction of the concentration effect. For this reason, there is a problem that work such as entanglement, removal of residue and cleaning must be frequently performed.

本発明は上記課題を解決するためになされたもので、簡素な構成で、濃縮槽内の被処理液の固液分離を確実にかつ迅速に行うことができ、汚泥の濃縮性能の向上とコストダウンを図ることができる汚泥の濃縮方法およびその装置を提供することを目的とする。   The present invention has been made in order to solve the above-mentioned problems. With a simple configuration, the solid-liquid separation of the liquid to be treated in the concentration tank can be performed reliably and quickly, and the concentration performance and cost of sludge can be improved. An object of the present invention is to provide a method and apparatus for concentrating sludge that can be downed.

本発明の請求項1に係る汚泥の濃縮方法は、汚水または排水の浄化処理プロセスを構成するホッパー構造の汚泥濃縮槽であって、導入された被処理液を脱離液と濃縮汚泥とに固液分離する汚泥濃縮槽に、鉛直方向に配置された複数の棒材を配置し、これら棒材を回動させて被処理液中の棒材の進行方向後方側に負圧により液濃度の低い路を形成する低濃度液路形成手段を設けて構成するとともに、これら棒材の上端を、汚泥濃縮槽に導入される被処理液の水面下に常時没するよう短寸にカットして形成し、汚泥濃縮槽内の中央部には、濃縮汚泥引抜ポンプに連通された濃縮汚泥引き抜き管を配置して構成し、低濃度液路形成手段は、上端が濃縮汚泥引き抜き管から上方に突出して回転駆動装置に接続され、下端が濃縮汚泥引き抜き管から下方に延出されて底面に臨む回転軸を備えるとともに、棒材を、下端がこの回転軸の下部と連結され、円錐状底部の傾斜に沿って延びる接続部と、この接続部と連続し、上方に立ち上がる縦棒部とを有して構成し、固液分離処理時、棒材を回動させ、被処理液中に縦方向に液濃度の低い路を形成することを特徴とするものである。 A method for concentrating sludge according to claim 1 of the present invention is a hopper-structured sludge concentration tank that constitutes a purification process of sewage or waste water, and the introduced liquid to be treated is solidified into a desorbed liquid and a concentrated sludge. A plurality of rods arranged in the vertical direction are arranged in a sludge concentration tank for liquid separation, and these rods are rotated so that the liquid concentration is low due to negative pressure on the rear side in the traveling direction of the rods in the liquid to be treated. A low-concentration liquid path forming means is provided to form a path, and the upper ends of these rods are cut into short lengths so that they are always submerged under the surface of the liquid to be treated introduced into the sludge concentration tank. In the middle of the sludge concentration tank, a concentrated sludge extraction pipe communicating with the concentrated sludge extraction pump is arranged, and the low concentration liquid path forming means rotates with the upper end protruding upward from the concentrated sludge extraction pipe Connected to the drive unit, the lower end is below the concentrated sludge extraction pipe It has a rotating shaft that extends and faces the bottom surface, and the bar is connected to the lower end of the rotating shaft and extends along the inclination of the conical bottom, and is continuous with the connecting portion and upwards. It has a vertical bar portion that rises, and is characterized in that, during the solid-liquid separation process, the bar is rotated to form a path with a low liquid concentration in the liquid to be processed in the vertical direction.

本発明の請求項1に係る汚泥の濃縮方法では、汚水または排水の浄化処理プロセスを構成するホッパー構造の汚泥濃縮槽であって、導入された被処理液を脱離液と濃縮汚泥とに固液分離する汚泥濃縮槽に、鉛直方向に配置された複数の棒材を配置し、これら棒材を回動させて被処理液中の棒材の進行方向後方側に負圧により液濃度の低い路を形成する低濃度液路形成手段を設けて構成するとともに、これら棒材の上端を、汚泥濃縮槽に導入される被処理液の水面下に常時没するよう短寸にカットして形成し、汚泥濃縮槽内の中央部には、濃縮汚泥引抜ポンプに連通された濃縮汚泥引き抜き管を配置して構成し、低濃度液路形成手段は、上端が濃縮汚泥引き抜き管から上方に突出して回転駆動装置に接続され、下端が濃縮汚泥引き抜き管から下方に延出されて底面に臨む回転軸を備えるとともに、棒材を、下端がこの回転軸の下部と連結され、円錐状底部の傾斜に沿って延びる接続部と、この接続部と連続し、上方に立ち上がる縦棒部とを有して構成し、固液分離処理時、棒材を回動させ、被処理液中に縦方向に液濃度の低い路を形成することにより、固液分離処理時、棒材が回動すると、被処理液中で棒材の進行方向後方側に負圧部が発生し、この負圧部に高濃度の汚泥分に比較して比重の軽い液分が集まり被処理液中に縦方向に液濃度の低い路が形成される。比重の軽い液分は上昇して被処理液中の上側に固液分離した脱離液の層を形成するので、脱離液の層が短時間で形成され、作業効率が向上する。 In the sludge concentration method according to claim 1 of the present invention, the sludge concentration tank has a hopper structure that constitutes a purification process of sewage or waste water, and the introduced liquid to be treated is separated into a desorbed liquid and a concentrated sludge. A plurality of rods arranged in the vertical direction are arranged in a sludge concentration tank for liquid separation, and these rods are rotated so that the liquid concentration is low due to negative pressure on the rear side in the traveling direction of the rods in the liquid to be treated. A low-concentration liquid path forming means is provided to form a path, and the upper ends of these rods are cut into short lengths so that they are always submerged under the surface of the liquid to be treated introduced into the sludge concentration tank. In the middle of the sludge concentration tank, a concentrated sludge extraction pipe communicating with the concentrated sludge extraction pump is arranged, and the low concentration liquid path forming means rotates with the upper end protruding upward from the concentrated sludge extraction pipe Connected to the drive, the lower end is below the concentrated sludge extraction pipe And a rotating shaft that extends to the bottom surface and has a rod that is connected to the lower end of the rotating shaft and extends along the inclination of the conical bottom, and is continuous with the connecting portion. In the solid-liquid separation process, the rod is rotated to form a path with low liquid concentration in the vertical direction in the liquid to be treated during the solid-liquid separation process. When the bar rotates, a negative pressure part is generated in the processed liquid at the rear side in the direction of travel of the bar, and a liquid component having a lower specific gravity is collected in this negative pressure part than the high-concentration sludge. A path having a low liquid concentration is formed in the processing liquid in the vertical direction. The liquid having a low specific gravity rises and forms a separated liquid-liquid layer on the upper side of the liquid to be treated, so that the detached liquid layer is formed in a short time and the working efficiency is improved.

本発明の請求項2に係る汚泥の濃縮装置は、汚水または排水の浄化処理プロセスの一部を構成するホッパー構造の汚泥濃縮槽であって、導入された被処理液を脱離液と濃縮汚泥とに固液分離する汚泥濃縮槽に、縦方向に配置された複数の棒材を配置し、これら棒材を回動させて被処理液中の棒材の進行方向後方側に負圧により液濃度の低い路を形成する低濃度液路形成手段を設けて構成するとともに、これら棒材の上端を、汚泥濃縮槽に導入される被処理液の水面下に常時没するよう短寸にカットして形成し、汚泥濃縮槽内の中央部には、濃縮汚泥引抜ポンプに連通された濃縮汚泥引き抜き管を配置して構成し、低濃度液路形成手段は、上端が濃縮汚泥引き抜き管から上方に突出して回転駆動装置に接続され、下端が濃縮汚泥引き抜き管から下方に延出されて底面に臨む回転軸を備えるとともに、棒材を、下端がこの回転軸の下部と連結され、円錐状底部の傾斜に沿って延びる接続部と、この接続部と連続し、上方に立ち上がる縦棒部とを有して構成したことを特徴とするものである。 The sludge concentration apparatus according to claim 2 of the present invention is a sludge concentration tank having a hopper structure that constitutes a part of a purification process of sewage or waste water, wherein the introduced liquid to be treated is a desorbed liquid and concentrated sludge. A plurality of bars arranged in the vertical direction are arranged in a sludge concentrating tank that separates into solid and liquid, and these bars are rotated so that the liquid in the liquid to be treated is moved backward by the negative pressure in the direction of travel. A low-concentration liquid path forming means is provided to form a low-concentration path, and the upper ends of these rods are cut short so that they are always submerged under the surface of the liquid to be treated introduced into the sludge concentration tank. In the middle part of the sludge concentration tank, a concentrated sludge extraction pipe connected to the concentrated sludge extraction pump is arranged, and the low concentration liquid path forming means has an upper end upward from the concentrated sludge extraction pipe. Protruding and connected to the rotary drive, the lower end is from the concentrated sludge extraction tube A rotating shaft extending toward the bottom and facing the bottom surface, and a bar member connected to a lower end of the rotating shaft and extending along the inclination of the conical bottom, and continuous with the connecting portion, It is characterized by having a vertical bar portion that rises upward .

本発明の請求項2に係る汚泥の濃縮装置では、汚水または排水の浄化処理プロセスの一部を構成するホッパー構造の汚泥濃縮槽であって、導入された被処理液を脱離液と濃縮汚泥とに固液分離する汚泥濃縮槽に、縦方向に配置された複数の棒材を配置し、これら棒材を回動させて被処理液中の棒材の進行方向後方側に負圧により液濃度の低い路を形成する低濃度液路形成手段を設けて構成するとともに、これら棒材の上端を、汚泥濃縮槽に導入される被処理液の水面下に常時没するよう短寸にカットして形成し、汚泥濃縮槽内の中央部には、濃縮汚泥引抜ポンプに連通された濃縮汚泥引き抜き管を配置して構成し、低濃度液路形成手段は、上端が濃縮汚泥引き抜き管から上方に突出して回転駆動装置に接続され、下端が濃縮汚泥引き抜き管から下方に延出されて底面に臨む回転軸を備えるとともに、棒材を、下端がこの回転軸の下部と連結され、円錐状底部の傾斜に沿って延びる接続部と、この接続部と連続し、上方に立ち上がる縦棒部とを有して構成したことにより、固液分離処理時、棒材が回動すると、被処理液中で棒材の進行方向後方側に負圧部が発生し、この負圧部に高濃度の汚泥分に比較して比重の軽い液分が集まり被処理液中に縦方向に液濃度の低い路が形成される。比重の軽い液分は上昇して被処理液中の上側に固液分離した脱離液の層を形成するので、脱離液の層が短時間で形成され、これにより汚泥の濃縮性能が向上する。また、棒材の寸法を短くすることができるので、コストダウンを図ることができる。 The sludge concentration apparatus according to claim 2 of the present invention is a sludge concentration tank having a hopper structure that constitutes a part of a purification process of sewage or wastewater, wherein the introduced liquid to be treated is a desorbed liquid and concentrated sludge. A plurality of bars arranged in the vertical direction are arranged in a sludge concentrating tank that separates into solid and liquid, and these bars are rotated so that the liquid in the liquid to be treated is moved backward by the negative pressure in the direction of travel. A low-concentration liquid path forming means is provided to form a low-concentration path, and the upper ends of these rods are cut short so that they are always submerged under the surface of the liquid to be treated introduced into the sludge concentration tank. In the middle part of the sludge concentration tank, a concentrated sludge extraction pipe connected to the concentrated sludge extraction pump is arranged, and the low concentration liquid path forming means has an upper end upward from the concentrated sludge extraction pipe. Protruding and connected to a rotary drive, the lower end is a concentrated sludge extraction tube A rotating shaft extending downward and facing the bottom surface is provided, and the bar is connected to the lower end of the rotating shaft and extends along the inclination of the conical bottom, and is continuous with the connecting portion. By having a vertical bar part that rises upward, when the bar rotates during the solid-liquid separation process, a negative pressure part is generated on the rear side in the traveling direction of the bar in the liquid to be processed. A liquid component having a lighter specific gravity than the high-concentration sludge component gathers in the negative pressure portion, and a path with a low liquid concentration is formed in the liquid to be treated. The liquid with a low specific gravity rises to form a separated liquid-liquid layer on the upper side of the liquid to be treated, so that the detached liquid layer is formed in a short time, which improves the sludge concentration performance. To do. Further, since the dimensions of the bar can be shortened, the cost can be reduced.

本発明の請求項3に係る汚泥の濃縮装置は、棒材の上端を被処理液の設計水位の略半分の高さに設定したことを特徴とするものである。 The sludge concentration apparatus according to claim 3 of the present invention is characterized in that the upper end of the bar is set to a height approximately half the design water level of the liquid to be treated.

本発明の請求項4に係る汚泥の濃縮装置は、棒材間を補強材で連結するとともに、濃縮汚泥引き抜き管の外周に環状部材を遊嵌しこの環状部材と棒材とを接続して構成したガイドを備えたことを特徴とするものである。   The sludge concentrating device according to claim 4 of the present invention is configured by connecting the rod members with a reinforcing material, loosely fitting an annular member on the outer periphery of the concentrated sludge extraction pipe, and connecting the annular member and the rod member. It is characterized by having a guide.

本発明の請求項1に係る汚泥の濃縮方法は、汚水または排水の浄化処理プロセスを構成するホッパー構造の汚泥濃縮槽であって、導入された被処理液を脱離液と濃縮汚泥とに固液分離する汚泥濃縮槽に、鉛直方向に配置された複数の棒材を配置し、これら棒材を回動させて被処理液中の棒材の進行方向後方側に負圧により液濃度の低い路を形成する低濃度液路形成手段を設けて構成するとともに、これら棒材の上端を、汚泥濃縮槽に導入される被処理液の水面下に常時没するよう短寸にカットして形成し、汚泥濃縮槽内の中央部には、濃縮汚泥引抜ポンプに連通された濃縮汚泥引き抜き管を配置して構成し、低濃度液路形成手段は、上端が濃縮汚泥引き抜き管から上方に突出して回転駆動装置に接続され、下端が濃縮汚泥引き抜き管から下方に延出されて底面に臨む回転軸を備えるとともに、棒材を、下端がこの回転軸の下部と連結され、円錐状底部の傾斜に沿って延びる接続部と、この接続部と連続し、上方に立ち上がる縦棒部とを有して構成し、固液分離処理時、棒材を回動させ、被処理液中に縦方向に液濃度の低い路を形成するようにしたので、濃縮槽内の被処理液の固液分離を確実にかつ迅速に行うことができ、汚泥の濃縮性能を向上させることができる。 A method for concentrating sludge according to claim 1 of the present invention is a hopper-structured sludge concentration tank that constitutes a purification process of sewage or waste water, and the introduced liquid to be treated is solidified into a desorbed liquid and a concentrated sludge. A plurality of rods arranged in the vertical direction are arranged in a sludge concentration tank for liquid separation, and these rods are rotated so that the liquid concentration is low due to negative pressure on the rear side in the traveling direction of the rods in the liquid to be treated. A low-concentration liquid path forming means is provided to form a path, and the upper ends of these rods are cut into short lengths so that they are always submerged under the surface of the liquid to be treated introduced into the sludge concentration tank. In the middle of the sludge concentration tank, a concentrated sludge extraction pipe communicating with the concentrated sludge extraction pump is arranged, and the low concentration liquid path forming means rotates with the upper end protruding upward from the concentrated sludge extraction pipe Connected to the drive unit, the lower end is below the concentrated sludge extraction pipe It has a rotating shaft that extends and faces the bottom surface, and the bar is connected to the lower end of the rotating shaft and extends along the inclination of the conical bottom, and is continuous with the connecting portion and upwards. It has a vertical bar part that rises, and at the time of solid-liquid separation processing, the bar is rotated to form a low liquid concentration path in the vertical direction in the liquid to be processed. Solid-liquid separation of the liquid to be treated can be performed reliably and quickly, and the sludge concentration performance can be improved.

本発明の請求項2に係る汚泥の濃縮装置は、汚水または排水の浄化処理プロセスの一部を構成するホッパー構造の汚泥濃縮槽であって、導入された被処理液を脱離液と濃縮汚泥とに固液分離する汚泥濃縮槽に、縦方向に配置された複数の棒材を配置し、これら棒材を回動させて被処理液中の棒材の進行方向後方側に負圧により液濃度の低い路を形成する低濃度液路形成手段を設けて構成するとともに、これら棒材の上端を、汚泥濃縮槽に導入される被処理液の水面下に常時没するよう短寸にカットして形成し、汚泥濃縮槽内の中央部には、濃縮汚泥引抜ポンプに連通された濃縮汚泥引き抜き管を配置して構成し、低濃度液路形成手段は、上端が濃縮汚泥引き抜き管から上方に突出して回転駆動装置に接続され、下端が濃縮汚泥引き抜き管から下方に延出されて底面に臨む回転軸を備えるとともに、棒材を、下端がこの回転軸の下部と連結され、円錐状底部の傾斜に沿って延びる接続部と、この接続部と連続し、上方に立ち上がる縦棒部とを有して構成したので、濃縮槽内の被処理液の固液分離を確実にかつ迅速に行うことができ、汚泥の濃縮性能を向上させることができる。また、棒材の寸法を短くすることができ、コストダウンを図ることができる。 The sludge concentration apparatus according to claim 2 of the present invention is a sludge concentration tank having a hopper structure that constitutes a part of a purification process of sewage or waste water, wherein the introduced liquid to be treated is a desorbed liquid and concentrated sludge. A plurality of bars arranged in the vertical direction are arranged in a sludge concentrating tank that separates into solid and liquid, and these bars are rotated so that the liquid in the liquid to be treated is moved backward by the negative pressure in the direction of travel. A low-concentration liquid path forming means is provided to form a low-concentration path, and the upper ends of these rods are cut short so that they are always submerged under the surface of the liquid to be treated introduced into the sludge concentration tank. In the middle part of the sludge concentration tank, a concentrated sludge extraction pipe connected to the concentrated sludge extraction pump is arranged, and the low concentration liquid path forming means has an upper end upward from the concentrated sludge extraction pipe. Protruding and connected to the rotary drive, the lower end is from the concentrated sludge extraction tube A rotating shaft extending toward the bottom and facing the bottom surface, and a bar member connected to a lower end of the rotating shaft and extending along the inclination of the conical bottom, and continuous with the connecting portion, Since it has a vertical bar portion that rises upward, solid-liquid separation of the liquid to be treated in the concentration tank can be performed reliably and quickly, and the sludge concentration performance can be improved. Moreover, the dimension of a bar can be shortened and cost reduction can be aimed at.

図1は、浄化処理プロセスの一部を構成する汚泥濃縮槽において本発明の一実施例に係る汚泥の濃縮方法に用いられる濃縮装置を示す全体説明図である。(実施例1)FIG. 1 is an overall explanatory view showing a concentrating device used in a sludge concentrating method according to an embodiment of the present invention in a sludge concentrating tank constituting a part of a purification treatment process. (Example 1) 図2の(A)、(B)はそれぞれ、図1の汚泥の濃縮装置の縦断面図および上方から見た説明図である。2 (A) and 2 (B) are a longitudinal sectional view and an explanatory view as seen from above of the sludge concentrator in FIG. 1, respectively. 図3の(A)、(B)はそれぞれ、図1の汚泥の濃縮装置の棒材の挙動を示す説明図である。3 (A) and 3 (B) are explanatory views showing the behavior of the bar of the sludge concentrator in FIG. 1, respectively.

濃縮槽内の被処理液の固液分離を確実にかつ迅速に行うことができ、汚泥の濃縮性能の向上とコストダウンを図るという目的を、汚水または排水の浄化処理プロセスの一部を構成する汚泥濃縮槽であって、導入された被処理液を脱離液と濃縮汚泥とに固液分離する汚泥濃縮槽に、鉛直方向に配置された複数の棒材を配置し、これら棒材を回動させて被処理液中の棒材の進行方向後方側に負圧により液濃度の低い路を形成する低濃度液路形成手段を設けて構成するとともに、これら棒材の上端を、汚泥濃縮槽に導入される被処理液の水面下に常時没するよう短寸にカットして形成し、汚泥濃縮槽内の中央部には、汚泥引抜ポンプに連通された汚泥引き抜き管を配置して構成し、低濃度液路形成手段を、上端が汚泥引き抜き管から上方に突出して回転駆動装置に接続され、下端が汚泥引き抜き管から下方に延出されて底面に臨む回転軸と、この回転軸の下部と接続部を介して連結された棒材とを備えて構成し、棒材の上端を被処理液の設計水位の略半分の高さに設定したことにより実現した。   A part of the purification process of sewage or waste water, with the purpose of ensuring solid-liquid separation of the liquid to be treated in the concentration tank reliably and promptly, and improving sludge concentration performance and cost reduction. A sludge concentration tank is a sludge concentration tank that solid-liquid separates the liquid to be treated into separated liquid and concentrated sludge, and a plurality of bars arranged in the vertical direction are arranged. A low-concentration liquid passage forming means for forming a low-concentration liquid passage is formed on the rear side in the traveling direction of the bar material in the liquid to be treated by a negative pressure, and the upper end of the bar material is a sludge concentration tank. The sludge extraction pipe connected to the sludge extraction pump is arranged at the center of the sludge concentration tank. The low-concentration liquid path forming means, the upper end protrudes upward from the sludge extraction pipe A rotating shaft connected to the rolling drive device, the lower end of the rotating shaft extending downward from the sludge extraction pipe and facing the bottom surface, and a bar connected to the lower part of the rotating shaft via a connecting portion, This was realized by setting the upper end of the material to approximately half the design water level of the liquid to be treated.

以下、図面に示す実施例により本発明を説明する。本発明の一実施例に係る汚泥の濃縮装置2は、図1に示すように、浄化処理プロセスの一部を構成する汚泥濃縮槽10に設置される。図1の浄化処理プロセスに基づく浄化処理システムSでは、曝気沈砂槽3、原水ポンプ槽4、流量調整槽5、曝気槽6、沈殿槽7、散水ポンプ槽8、消毒槽9の順に処理槽を設け、沈殿槽7から汚泥引き抜きポンプ12で引き抜かれた余剰汚泥Lslを汚泥濃縮槽10に導き、汚泥濃縮槽10で処理された脱離液Lspを脱離液管13を通じて流量調整槽5に戻し、沈殿した濃縮汚泥Slgを汚泥貯留槽11に送って貯留し、その後搬出するようにしている。この浄化処理システムSでは、流入した汚水は、曝気沈砂槽3、原水ポンプ槽4、流量調整槽5の順に砂やし渣が除去され、曝気槽6で生物処理され汚濁物質が酸化分解される(工程S−1参照)。曝気槽6で酸化分解された被処理液は沈殿槽7で処理水と汚泥に固液分離後に、散水ポンプ槽8を経て消毒槽9に導かれ塩素消毒後に放流されるようになっている(工程S−2参照)。そして、曝気槽6で生物処理の過程で発生した余剰汚泥は、沈殿槽7から汚泥濃縮槽10に送られ、汚泥濃縮槽10で濃縮後に汚泥貯留槽11から搬出するようになっている(工程S−3参照)。本実施例では、処理される被処理液の汚水として、生活排水等を対象にしている。   Hereinafter, the present invention will be described with reference to embodiments shown in the drawings. As shown in FIG. 1, the sludge concentration apparatus 2 according to one embodiment of the present invention is installed in a sludge concentration tank 10 constituting a part of the purification treatment process. In the purification treatment system S based on the purification treatment process of FIG. 1, the treatment tanks are arranged in the order of the aeration sedimentation tank 3, the raw water pump tank 4, the flow rate adjustment tank 5, the aeration tank 6, the precipitation tank 7, the watering pump tank 8, and the disinfection tank 9. The excess sludge Lsl extracted from the sedimentation tank 7 by the sludge extraction pump 12 is guided to the sludge concentration tank 10, and the desorbed liquid Lsp treated in the sludge concentration tank 10 is returned to the flow rate adjusting tank 5 through the desorbed liquid pipe 13. The concentrated sludge Slg that has been precipitated is sent to and stored in the sludge storage tank 11 and then discharged. In this purification treatment system S, sand and residue are removed from the inflowing sewage in the order of the aeration sedimentation tank 3, the raw water pump tank 4, and the flow rate adjustment tank 5, and are biologically treated in the aeration tank 6 to oxidize and decompose pollutants. (Refer process S-1). The liquid to be treated that has been oxidatively decomposed in the aeration tank 6 is separated into treated water and sludge in the sedimentation tank 7 and then led to the disinfection tank 9 through the watering pump tank 8 and discharged after chlorine disinfection ( Step S-2). Then, surplus sludge generated in the course of biological treatment in the aeration tank 6 is sent from the sedimentation tank 7 to the sludge concentration tank 10, and is carried out from the sludge storage tank 11 after being concentrated in the sludge concentration tank 10 (process). S-3). In the present embodiment, domestic wastewater or the like is targeted as the sewage of the liquid to be treated.

汚泥濃縮槽10には、図2の(A)、(B)に示すように、上部開口10Bの下側に取り付けられた支持台16上に濃縮汚泥引き抜きポンプ14が設けられる。濃縮汚泥引き抜きポンプ14には、濃縮汚泥引き抜き管15が接続される。濃縮汚泥引き抜き管15は、このポンプ14から下方に垂直に延長され、下端15Aが汚泥濃縮槽10の、中央が次第に狭まる円錐状底部(底面)10Aの中心部10Cに臨んで配置される。支持台16と濃縮汚泥引き抜き管15との間には、上端が支持台16の下面に取り付けられ、下端が濃縮汚泥引き抜き管15の下部に連結され、濃縮汚泥引き抜き管15に空気を供給する濃縮汚泥引き抜きポンプ空気管17が設けられる。   In the sludge concentration tank 10, as shown in FIGS. 2A and 2B, a concentrated sludge extraction pump 14 is provided on a support base 16 attached to the lower side of the upper opening 10B. A concentrated sludge extraction pump 15 is connected to the concentrated sludge extraction pump 14. The concentrated sludge extraction pipe 15 is vertically extended downward from the pump 14, and the lower end 15 </ b> A is disposed facing the central portion 10 </ b> C of the conical bottom portion (bottom surface) 10 </ b> A whose center is gradually narrowed. Concentration for supplying air to the concentrated sludge extraction pipe 15 between the support base 16 and the concentrated sludge extraction pipe 15 is attached to the lower surface of the support base 16 and the lower end is connected to the lower part of the concentrated sludge extraction pipe 15. A sludge extraction pump air pipe 17 is provided.

汚泥濃縮槽10には、汚泥の濃縮装置2が設けられる。この濃縮装置2は、上部開口部10Bの上側に取り付けられた架台21と、この架台21上に設置された無段変速機付きモータ(駆動装置)22と、この無段変速機付きモータ22の出力軸と連結されたウオーム減速機(駆動装置)23と、このウオーム減速機23の出力側に連結され、出力側から濃縮汚泥引き抜きポンプ14と濃縮汚泥引き抜き管15とを貫通し、下端24Aが濃縮汚泥引き抜き管15から下方に延出されて底部10Aの中心部10Cに臨む金属製棒状の回転軸24とを備えて構成される。   The sludge concentration tank 10 is provided with a sludge concentration device 2. The concentrating device 2 includes a gantry 21 attached to the upper side of the upper opening 10B, a motor (driving device) 22 with a continuously variable transmission installed on the gantry 21, and a motor 22 with a continuously variable transmission. A worm speed reducer (drive device) 23 connected to the output shaft, connected to the output side of the worm speed reducer 23, penetrates the concentrated sludge extraction pump 14 and the concentrated sludge extraction pipe 15 from the output side, and a lower end 24A A metal rod-like rotary shaft 24 extending downward from the concentrated sludge extraction tube 15 and facing the center portion 10C of the bottom portion 10A is provided.

さらに、この汚泥の濃縮装置2は、この回転軸24の下端24Aと濃縮汚泥引き抜き管15の下端15Aとの間で、下端が回転軸24に連結され円錐状底部10Aの傾斜に沿って折曲された折曲部とこの折曲部と連続し上方に直線状に垂直に立ち上がる縦棒部とを有する金属製棒材25(25A〜25C)を、回転軸24の周方向に互いに等間隔で複数本(本実施例では3本)設けて構成される。これら棒材25A〜25Cには、上下の2箇所にこれら棒材25A〜25Cを横方向に連結して補強する環状補強パイプ(補強材)26A、26Bが設けられる。また、補強パイプ26A、26B間には、棒材25A〜25Cを回転軸24を中心に円滑に回動させるガイド27が設けられる。ガイド27は、濃縮汚泥引き抜き管15の外周に遊嵌された環状部材28と、この環状部材28と棒材25A〜25Cとを接続して連結する連結部材29とを備えて構成される。ガイド27は、棒材25A〜25Cまたは回転軸24に外力が加わっても、環状部材28の内面が濃縮汚泥引き抜き管15の外面に規制されるので、回転軸24の揺れを阻止し、軸芯を常時垂直方向に保つようになっている。低濃度液路形成手段は、無段変速機付きモータ22とウオーム減速機23と回転軸24と棒材25A〜25Cとを備えて構成される。   Further, the sludge concentrating device 2 is bent between the lower end 24A of the rotary shaft 24 and the lower end 15A of the concentrated sludge extraction pipe 15 with the lower end connected to the rotary shaft 24 along the inclination of the conical bottom portion 10A. Metal bars 25 (25A to 25C) each having a bent portion and a vertical rod portion that is continuous with the bent portion and rises vertically in a straight line are arranged at equal intervals in the circumferential direction of the rotary shaft 24. A plurality (three in this embodiment) are provided. These bar members 25A to 25C are provided with annular reinforcing pipes (reinforcing members) 26A and 26B that connect and reinforce these bar members 25A to 25C in two lateral directions. A guide 27 is provided between the reinforcing pipes 26 </ b> A and 26 </ b> B to smoothly rotate the rods 25 </ b> A to 25 </ b> C around the rotation shaft 24. The guide 27 includes an annular member 28 loosely fitted on the outer periphery of the concentrated sludge extraction pipe 15, and a connecting member 29 that connects and connects the annular member 28 and the rods 25A to 25C. Even if an external force is applied to the rods 25A to 25C or the rotating shaft 24, the guide 27 restricts the swinging of the rotating shaft 24 and prevents the rotating shaft 24 from shaking because the inner surface of the annular member 28 is regulated by the outer surface of the concentrated sludge extraction pipe 15. Is always kept in the vertical direction. The low concentration liquid path forming means includes a motor 22 with a continuously variable transmission, a worm speed reducer 23, a rotating shaft 24, and rods 25A to 25C.

ところで、本実施例に係る汚泥の濃縮装置2は、棒材25A〜25Cの上端30を、汚泥濃縮槽10に導入される被処理液の水面L1下に常時没するよう短寸にカットして形成される。より具体的には、棒材25A〜25Cの上端30を被処理液の設計水位L1の略半分の高さとなるように、あるいは略半分の高さより若干高くなるように設定している。すなわち、汚泥濃縮槽10では、処理時間の経過とともに、設計水位L1の略半分の高さから上側に高濃度の汚泥分に比較して比重の軽い脱離液Lspの層が、下側に高濃度の汚泥分が含まれる比較的比重の重い高濃度汚泥液Lthのが形成され、底部10Aに濃縮汚泥が堆積されるようになっている。このため、棒材25A〜25Cの上端30は面L1上に露出することはなく、脱離液Lspの層内に位置するかその層の下側で近くに位置するようになっている。つまり、脱離液Lspの層は処理時間に応じてその厚さが変化するのに対して棒材25A〜25Cの上端30の高さは一定となっている。 By the way, the sludge concentrating device 2 according to the present embodiment cuts the upper ends 30 of the rods 25A to 25C into a short length so as to be always submerged under the water surface L1 of the liquid to be treated introduced into the sludge concentrating tank 10. It is formed. More specifically, the upper ends 30 of the rods 25A to 25C are set so as to be approximately half the height of the design water level L1 of the liquid to be treated or slightly higher than approximately half the height. That is, in the sludge concentration tank 10, as the treatment time elapses, the layer of the desorbed liquid Lsp having a lighter specific gravity compared to the high-concentration sludge from the height of approximately half of the design water level L1 to the lower side increases. A layer of high-concentration sludge liquid Lth having a relatively heavy specific gravity containing sludge content is formed, and concentrated sludge is deposited on the bottom 10A. Therefore, the upper end 30 of the bar 25A~25C is never exposed on the water surface L1, it adapted to close the lower side of either the layer positioned in a layer of releasing liquid Lsp. That is, the thickness of the upper end 30 of the rods 25A to 25C is constant while the thickness of the layer of the desorbing liquid Lsp changes according to the processing time.

汚泥の濃縮装置2は、無段変速機付きモータ22が回転駆動され、このモータ22の出力がウオーム減速機23により減速されて、回転軸24に出力されると、回転軸24は棒材25A〜25Cを被処理液中でゆっくりと回動させるようになっている。本実施例では、例えば、ウオーム減速機23が1:30の減速出力で、回転軸24へ出力する回転数は0.074〜0.11rpmとなっている。棒材25A〜25Cが被処理液中でゆっくり回動すると、図3の(A)に示すように、被処理液中の棒材25(25A〜25C)の進行方向後方側に負圧により液濃度の低い路P1が形成されるようになっている。ここでいう、液濃度が低いとは、高濃度の汚泥分に比較して負圧部に比重の軽い液分が集まることをいい、液濃度の低い路P1が形成されるとは、棒材25(25A〜25C)の進行方向後方側に棒材25に沿って縦方向(垂直方向)に比重の軽い液分が集まり、この比重の軽い液分が縦方向に形成されることをいう。すなわち、棒材25(25A〜25C)の進行方向後方側に液濃度の低い路P1が形成されると、この路P1に集まった液濃度の低い液、つまり、汚泥分の少ない液はより比重の軽い方へと移動し、上方への流れが生じ、水路(みずみち)が形成される。棒材25(25A〜25C)の上端30より上方側または上端30が位置するレベルには、脱離液Lspの層が形成されているので、路P1を上昇する液濃度の低い液は脱離液Lspに合流され、脱離液Lspの層の形成が迅速化される。   In the sludge concentrating device 2, when the motor 22 with a continuously variable transmission is rotationally driven and the output of the motor 22 is decelerated by the worm speed reducer 23 and output to the rotating shaft 24, the rotating shaft 24 becomes the bar 25A. ˜25C is slowly rotated in the liquid to be treated. In this embodiment, for example, the worm speed reducer 23 has a 1:30 reduction output, and the rotation speed output to the rotary shaft 24 is 0.074 to 0.11 rpm. When the rods 25A to 25C rotate slowly in the liquid to be treated, as shown in FIG. 3A, the liquid is caused by a negative pressure on the rear side in the traveling direction of the rods 25 (25A to 25C) in the liquid to be treated. A path P1 having a low concentration is formed. Here, the low liquid concentration means that a liquid component having a light specific gravity is collected in the negative pressure part as compared with a high concentration sludge component, and that the path P1 having a low liquid concentration is formed is a bar. 25 (25A to 25C) means that a liquid component having a low specific gravity gathers in the longitudinal direction (vertical direction) along the rod 25 on the rear side in the traveling direction, and the liquid component having a low specific gravity is formed in the vertical direction. That is, when the path P1 having a low liquid concentration is formed on the rear side in the traveling direction of the bar 25 (25A to 25C), the liquid having a low liquid concentration collected in the path P1, that is, the liquid having a small amount of sludge is more specific gravity. It moves to the lighter side, and an upward flow is generated, and a water channel is formed. Since the layer of the desorbing liquid Lsp is formed at the level above the upper end 30 of the rod 25 (25A to 25C) or at the level where the upper end 30 is located, the liquid with a low liquid concentration rising on the path P1 is desorbed. The formation of the layer of the desorption liquid Lsp is accelerated by joining the liquid Lsp.

次に、本発明に係る汚泥の濃縮方法について、上記実施例に係る汚泥の濃縮装置2の作用に基づいて説明する。本実施例に係る汚泥の濃縮装置2は、汚泥濃縮槽10に曝気槽6から汚泥引き抜きポンプ12で引き抜かれた余剰汚泥Lslが導かれ、設計水位L1に達すると、汚泥引き抜きポンプ12の稼働は停止する。無段変速機付きモータ22は常時稼働しており、ウオーム減速機23を介して回転駆動力が回転軸24に出力されると、回転軸24は棒材25A〜25Cを被処理液中でゆっくりと回動させる。このとき、棒材25A〜25Cの進行方向後方側に負圧により液濃度の低い路P1が形成される。この路P1では、液濃度が低く比重の軽い液分は上昇して被処理液中の上側に流出する。このため、被処理液中には、固液分離した脱離液Lspの層が形成され、しかも、液濃度の低い路P1からは絶えず液濃度が低く比重の軽い液分が上方に供給されるので、脱離液Lspの層が短時間で形成され、しかも、その層は厚さを急速に増してゆく。このため、汚泥濃縮槽10では、脱離液Lspと濃縮汚泥の分離を管時間で行うことができ、作業効率が向上する。また、棒材25A〜25Cは常に水面L1下に没しているので、水面L1に乱流を起こす虞がなく、脱離液Lspの形成に影響を与えにくい。   Next, the sludge concentration method according to the present invention will be described based on the action of the sludge concentration apparatus 2 according to the above embodiment. In the sludge concentration apparatus 2 according to the present embodiment, when the excess sludge Lsl extracted from the aeration tank 6 by the sludge extraction pump 12 is guided to the sludge concentration tank 10 and reaches the design water level L1, the operation of the sludge extraction pump 12 is performed. Stop. The motor 22 with a continuously variable transmission is always in operation, and when a rotational driving force is output to the rotating shaft 24 via the worm reducer 23, the rotating shaft 24 slowly moves the rods 25A to 25C in the liquid to be processed. And rotate. At this time, a path P1 having a low liquid concentration is formed by the negative pressure on the rear side in the traveling direction of the rods 25A to 25C. In this path P1, the liquid component having a low liquid concentration and a low specific gravity rises and flows out to the upper side in the liquid to be treated. For this reason, a layer of the desorbed liquid Lsp separated into solid and liquid is formed in the liquid to be treated, and a liquid component having a low liquid concentration and a low specific gravity is constantly supplied upward from the path P1 having a low liquid concentration. Therefore, the layer of the desorbing liquid Lsp is formed in a short time, and the thickness of the layer increases rapidly. For this reason, in the sludge concentration tank 10, separation of the desorbed liquid Lsp and the concentrated sludge can be performed in a pipe time, and the working efficiency is improved. Further, since the rods 25A to 25C are always submerged below the water surface L1, there is no possibility of causing turbulent flow on the water surface L1, and the formation of the desorbed liquid Lsp is hardly affected.

なお、上記実施例では、棒材25を回転軸24の周方向に等間隔で3本設けているが、これに限られるものではなく、3本以上としてもよい。また、棒材25を、回転軸24に対して二重、三重と多重に設けるようにしてもよい。   In the above embodiment, three rods 25 are provided at equal intervals in the circumferential direction of the rotating shaft 24, but the present invention is not limited to this, and three or more rods may be provided. Further, the bar 25 may be provided in double, triple and multiple with respect to the rotating shaft 24.

次に、上記実施例に係る汚泥の濃縮装置2の構造を実質的に備えた濃縮装置で実証試験を行った。その実証試験の結果を以下に示す。
1.実証試験の条件
本濃縮試験装置の実証試験は、表1に示す関東地方の実処理施設で行った。実証試験では余剰汚泥、濃縮汚泥、脱離液等を1回/週の頻度で採水して分析し、汚泥の濃縮性能を確認した。表2では、実験NO.と実験条件の関係を示す。
Next, a verification test was conducted with a concentration device substantially including the structure of the sludge concentration device 2 according to the above example. The results of the verification test are shown below.
1. Verification Test Conditions The verification test of the concentration test apparatus was conducted at an actual treatment facility in the Kanto region shown in Table 1. In the verification test, surplus sludge, concentrated sludge, desorbed liquid, etc. were sampled and analyzed once a week to confirm the sludge concentration performance. In Table 2, experiment NO. And the relationship between the experimental conditions.

Figure 0006141805
Figure 0006141805

Figure 0006141805
Figure 0006141805

2.実証試験の調査結果
実証試験期間に採取した(1)余剰汚泥、(2)引抜汚泥、(3)脱離液の水質分析を行った。分析項目は、汚泥はpHとMLSS、MLVSSの3項目、脱離液はpHとBOD、SSの3項目である。汚泥濃縮槽における汚泥の濃縮状況について表3に示す。表4には、脱離液の性状を示す。
2. Investigation results of demonstration test Water quality analysis of (1) surplus sludge, (2) extracted sludge, and (3) desorbed liquid collected during the demonstration test period was conducted. The analysis items are three items of sludge, pH, MLSS, and MLVSS, and the desorption solution is three items of pH, BOD, and SS. Table 3 shows the state of sludge concentration in the sludge concentration tank. Table 4 shows the properties of the desorbed liquid.

Figure 0006141805
Figure 0006141805

Figure 0006141805
Figure 0006141805

RUN1(汚泥濃縮装置なし)では、余剰汚泥濃度4,380mg/Lの汚泥が、汚泥濃縮後の汚泥濃度で7,490mg/Lとなり、濃縮倍率では1.71倍であった。
一方、汚泥濃縮装置を付けたRUN2では、余剰汚泥濃度7,230mg/Lの汚泥が、汚泥濃縮後の汚泥濃度で26,530mg/Lとなり、濃縮倍率では、3.68倍となった。
脱離液の性状では、RUN1とRUN2では大きな差異は見られず、両方とも良好な脱離液が得られた。
こうした実施設での実証試験結果から、本実施例に係る汚泥の濃縮装置を設置した場合は、脱離液の悪化を生じないで、汚泥濃縮槽での引き抜き汚泥濃度を高めて、汚泥の濃縮倍率を高くする効果が大きいことが判明した。これにより、本濃縮装置により汚泥の濃縮効果が高まることが確認された。
In RUN1 (without a sludge concentrator), the sludge with an excess sludge concentration of 4,380 mg / L was 7,490 mg / L after the sludge concentration, and the concentration factor was 1.71 times.
On the other hand, in RUN2 with a sludge concentrator, the sludge with an excess sludge concentration of 7,230 mg / L was 26,530 mg / L after the sludge concentration, and the concentration factor was 3.68 times.
There was no significant difference between RUN1 and RUN2 in terms of the properties of the desorbed solution, and good desorbed solutions were obtained for both.
From the results of demonstration tests at these facilities, when the sludge concentration device according to this example was installed, the sludge concentration in the sludge concentration tank was increased and the sludge concentration was increased without causing deterioration of the desorbed liquid. It was found that the effect of increasing the magnification was great. Thereby, it was confirmed that the concentration effect of sludge increases by this concentration apparatus.

2 汚泥の濃縮装置
10 汚泥濃縮槽
25A〜25C 棒材
30 棒材上端
P1 液濃度の低い路
L1 被処理液の水面
Lsp 脱離液
2 Sludge Concentrator 10 Sludge Concentration Tank 25A-25C Bar 30 Upper end of Bar P1 Low liquid concentration path L1 Water level of liquid to be treated Lsp Desorbed liquid

Claims (4)

汚水または排水の浄化処理プロセスを構成するホッパー構造の汚泥濃縮槽であって、導入された被処理液を脱離液と濃縮汚泥とに固液分離する汚泥濃縮槽に、鉛直方向に配置された複数の棒材を配置し、これら棒材を回動させて被処理液中の棒材の進行方向後方側に負圧により液濃度の低い路を形成する低濃度液路形成手段を設けて構成するとともに、
これら棒材の上端を、汚泥濃縮槽に導入される被処理液の水面下に常時没するよう短寸にカットして形成し、
汚泥濃縮槽内の中央部には、濃縮汚泥引抜ポンプに連通された濃縮汚泥引き抜き管を配置して構成し、
低濃度液路形成手段は、上端が濃縮汚泥引き抜き管から上方に突出して回転駆動装置に接続され、下端が濃縮汚泥引き抜き管から下方に延出されて底面に臨む回転軸を備えるとともに、
棒材を、下端がこの回転軸の下部と連結され、円錐状底部の傾斜に沿って延びる接続部と、この接続部と連続し、上方に立ち上がる縦棒部とを有して構成し、
固液分離処理時、棒材を回動させ、被処理液中に縦方向に液濃度の低い路を形成することを特徴とする汚泥の濃縮方法。
It is a sludge concentration tank with a hopper structure that constitutes a purification process for sludge or wastewater, and is disposed vertically in a sludge concentration tank that separates the liquid to be treated into a detachment liquid and a concentrated sludge. A plurality of bar members are arranged, and a low-concentration liquid path forming means for forming a low-concentration liquid channel by negative pressure is provided on the rear side in the traveling direction of the bar members in the liquid to be treated. And
The upper ends of these bars are cut into short lengths so that they are always submerged under the surface of the liquid to be treated introduced into the sludge concentration tank,
In the central part of the sludge concentration tank, a concentrated sludge extraction pipe connected to the concentrated sludge extraction pump is arranged and configured.
The low-concentration liquid path forming means includes a rotating shaft that protrudes upward from the concentrated sludge extraction pipe and is connected to the rotary drive device, and has a lower end that extends downward from the concentrated sludge extraction pipe and faces the bottom surface.
The bar has a lower end connected to the lower part of the rotating shaft and has a connecting part extending along the inclination of the conical bottom, and a vertical bar part that is continuous with the connecting part and rises upward.
A method for concentrating sludge, characterized in that, during solid-liquid separation treatment, a rod is rotated to form a path with a low liquid concentration in the longitudinal direction in the liquid to be treated.
汚水または排水の浄化処理プロセスの一部を構成するホッパー構造の汚泥濃縮槽であって、導入された被処理液を脱離液と濃縮汚泥とに固液分離する汚泥濃縮槽に、縦方向に配置された複数の棒材を配置し、これら棒材を回動させて被処理液中の棒材の進行方向後方側に負圧により液濃度の低い路を形成する低濃度液路形成手段を設けて構成するとともに、
これら棒材の上端を、汚泥濃縮槽に導入される被処理液の水面下に常時没するよう短寸にカットして形成し
汚泥濃縮槽内の中央部には、濃縮汚泥引抜ポンプに連通された濃縮汚泥引き抜き管を配置して構成し、
低濃度液路形成手段は、上端が濃縮汚泥引き抜き管から上方に突出して回転駆動装置に接続され、下端が濃縮汚泥引き抜き管から下方に延出されて底面に臨む回転軸を備えるとともに、
棒材を、下端がこの回転軸の下部と連結され、円錐状底部の傾斜に沿って延びる接続部と、この接続部と連続し、上方に立ち上がる縦棒部とを有して構成したことを特徴とする汚泥の濃縮装置。
A sludge concentrating tank with a hopper structure that forms part of the purification process of sewage or wastewater, and in the longitudinal direction, into the sludge concentrating tank that separates the liquid to be treated into separated liquid and concentrated sludge. A low-concentration liquid path forming means that arranges a plurality of arranged bars and rotates these bars to form a path with low liquid concentration by negative pressure on the rear side in the traveling direction of the bars in the liquid to be treated. While providing and configuring,
The upper ends of these bars are cut into short lengths so that they are always submerged under the surface of the liquid to be treated introduced into the sludge concentration tank ,
In the central part of the sludge concentration tank, a concentrated sludge extraction pipe connected to the concentrated sludge extraction pump is arranged and configured.
The low-concentration liquid path forming means includes a rotating shaft that protrudes upward from the concentrated sludge extraction pipe and is connected to the rotary drive device, and has a lower end that extends downward from the concentrated sludge extraction pipe and faces the bottom surface.
The bar has a lower end connected to the lower part of the rotating shaft and has a connection part extending along the inclination of the conical bottom part, and a vertical bar part that is continuous with the connection part and rises upward. A sludge concentrator.
材の上端を被処理液の設計水位の略半分の高さに設定したことを特徴とする請求項2に記載の汚泥の濃縮装置。 The sludge concentrating device according to claim 2, wherein the upper end of the bar is set to a height substantially half of the design water level of the liquid to be treated. 棒材間を補強材で連結するとともに、濃縮汚泥引き抜き管の外周に環状部材を遊嵌しこの環状部材と棒材とを接続して構成したガイドを備えたことを特徴とする請求項3に記載の汚泥の濃縮装置。   4. The guide according to claim 3, further comprising a guide configured by connecting the rod members with a reinforcing material, loosely fitting an annular member around the outer periphery of the concentrated sludge extraction pipe, and connecting the annular member and the rod member. The sludge concentration apparatus as described.
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