JP6542440B1 - Fine solid separation device - Google Patents

Fine solid separation device Download PDF

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JP6542440B1
JP6542440B1 JP2018134601A JP2018134601A JP6542440B1 JP 6542440 B1 JP6542440 B1 JP 6542440B1 JP 2018134601 A JP2018134601 A JP 2018134601A JP 2018134601 A JP2018134601 A JP 2018134601A JP 6542440 B1 JP6542440 B1 JP 6542440B1
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dirty water
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一博 前田
一博 前田
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一博 前田
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Abstract

【課題】シンプルな構造でありながら浄化レベルの高い処理水を排出できる微細固形物分離装置を提供する。
【解決手段】外部から処理タンク2内に汚水Wを導入する汚水導入管3と、汚水導入管3と処理タンク2内で連通する上下開口の汚水案内管5と、汚水案内管5の上方に所定の間隙で配設され汚水案内管5の上開口部から流出した汚水Wを整流する整流部8と、整流部8の上方に所定の間隙で配設され浮上した汚水の微細固形物をかき集める汚泥ワイパー13と、汚泥ワイパー13でかき集められた微細固形物を収容して処理タンク2外へ排出する汚泥シューター23と、処理タンク2内から浄化した液体Sを排出する排出管32と、汚水Wに気泡を混入するために汚水導入管3に連設したエアーポンプ49と、で構成した、ことを特徴とする。
【選択図】図1
An object of the present invention is to provide a fine solid separation device capable of discharging treated water having a high purification level while having a simple structure.
SOLUTION: A dirty water introduction pipe 3 for introducing dirty water W into the treatment tank 2 from the outside, a dirty water guide pipe 5 of upper and lower openings communicated with the dirty water introduction pipe 3 in the treatment tank 2, and above the dirty water guide pipe 5. A straightening unit 8 disposed at a predetermined gap and straightening the dirty water W flowing out from the upper opening of the dirty water guide pipe 5 and a fine solid of the dirty water disposed at the predetermined gap above the straightening unit 8 The sludge wiper 13, a sludge shooter 23 for containing fine solid matter collected by the sludge wiper 13 and discharging it out of the processing tank 2, a discharge pipe 32 for discharging the liquid S purified from the inside of the processing tank 2, dirty water W , And an air pump 49 connected to the dirty water introduction pipe 3 in order to mix air bubbles into the air pump.
[Selected figure] Figure 1

Description

この発明は、汚水を固形物と液体に分離する処理タンクからなる微細固形物分離装置に関する。   The present invention relates to a fine solids separation device comprising a treatment tank for separating waste water into solids and liquid.

従来、豚舎等の家畜により排出される糞尿等は、薬品を用いた簡易的な重力沈殿槽により固形物と液体に分離し、その後、曝気槽により汚水中の有機物を微生物により分解し消毒して河川等へ放流したり、再度別途の沈殿槽にて固形物と液体に分離して消毒した後に上澄液を河川等へ放流し、固形物は脱水機により完全な固形物の産業廃棄物として処理したり、汚染レベルにより肥料等として利用されている。   Conventionally, manure and urine excreted by livestock such as piggery are separated into solid and liquid by a simple gravity settling tank using chemicals, and then the organic matter in sewage is decomposed and disinfected by microorganisms by an aeration tank. After being discharged into rivers etc. or separated into solid and liquid in separate sedimentation tank and disinfected again, the supernatant liquid is discharged into rivers etc. Solids are dewatered as complete solid industrial waste Depending on the level of contamination, it is used as fertilizer.

しかしながら、大量に薬品を使用するなどしても浄化された液体中には薬品に反応することのない微細固形物が多数混入していたり、薬品が残存するなどして河川等への放流や肥料としての固形物の成分に問題を有していた。   However, even if a large amount of chemical is used, the purified liquid contains many fine solid substances that do not react to the chemical, or the chemical remains, resulting in discharge to rivers and the like, and fertilizer Had problems with the composition of the solid as.

また、従来の方法では重力沈殿槽を複数使用したり、曝気槽による微生物の生育のための好気的な条件を維持管理しなければならず、装置を設置するための広大な土地や装置の費用、運用費の面で問題を有していた。   In addition, in the conventional method, it is necessary to use a plurality of gravity sedimentation tanks and maintain aerobic conditions for the growth of microorganisms by the aeration tank, and it is necessary to use a large land or equipment for installing the equipment. There was a problem in terms of expenses and operating expenses.

このような状況において、例えば、特許文献1に係る糞尿浄化装置では、汚水中の大型の固形物を貯留槽で分離した後、抽出された液状物を沈殿分離させると共にオゾン供給手段で発生させたオゾンの気泡に固形物を付着させ浮上分離させ、更に、固形物をイオン交換フィルタの表面に付着させて分離し、しかも、固形物をプレフィルタと逆浸透濾過手段によって濾過分離することで1つの糞尿浄化装置で浄化レベルの高い処理水を排出することができるものとして開示されている。   In such a situation, for example, in the feces and urine purification apparatus according to Patent Document 1, after separating a large solid substance in sewage in a storage tank, the separated liquid substance is separated by precipitation and generated by an ozone supply means Solid matter is attached to bubbles of ozone and floated and separated, solid matter is adhered to the surface of ion exchange filter and separated, and solid matter is filtered and separated by prefilter and reverse osmosis filtration means. It is disclosed as what can be processed water with a high purification level by a manure purification apparatus.

特開2000−343099号公報JP 2000-343099 A

しかしながら、特許文献1に係る糞尿浄化装置は、1つの糞尿浄化装置で浄化レベルの高い処理水を排出できる点では優れているが、オゾン供給手段やイオン交換フィルタ、プレフィルタ等と言った消耗品や副資材の点数が多く、大型となり装置も複雑となって結果として高価な装置となってしまい、依然として運用費を廉価に抑えることには限界があった。   However, although the feces and urine purification apparatus according to Patent Document 1 is excellent in that treated water having a high purification level can be discharged by one manure and urine purification apparatus, consumables such as ozone supply means, ion exchange filters, prefilters, etc. In addition, the number of auxiliary materials is large, the size is large, and the apparatus is complicated. As a result, the apparatus becomes an expensive apparatus, and there is a limit to keep the operation cost inexpensive.

本願の発明者は、汚水中に薬品と反応することのない微細固形物が多数存在することに着目し、沈殿分離と共に気泡を付着させた微細固形物を気泡から分離されることなく水面まで浮上させて回収することで薬品を使用することなく簡易な装置で浄化レベルの高い処理水を排出できることを見出した。   The inventor of the present application has noted that there are many fine solid substances which do not react with chemicals in the sewage, and the fine solid substances to which bubbles are attached as well as precipitation and separation float to the water surface without being separated from the bubbles. It has been found that treated water having a high purification level can be discharged with a simple device without using chemicals by letting it be collected.

本発明は、以上のような事情に鑑みてなされたものであり、シンプルな構造でありながら浄化レベルの高い処理水を排出できる微細固形物分離装置を提供することにある。   The present invention has been made in view of the above circumstances, and it is an object of the present invention to provide a fine solid separation device capable of discharging treated water having a high purification level while having a simple structure.

以上のような目的を達成するために、本発明は以下のようなものを提供する。   In order to achieve the above objects, the present invention provides the following.

請求項1に係る発明では、汚水を固形物と液体に分離する処理タンクかならる浄化装置であって、外部から処理タンク内に汚水を導入する汚水導入管と、前記汚水導入管と前記処理タンク内で連通する上下開口の汚水案内管と、前記汚水案内管の上方に所定の間隙で配設され前記汚水案内管の上開口部から流出した前記汚水を整流する整流部と、前記整流部の上方に所定の間隙で配設され浮上した前記汚水の微細固形物をかき集める汚泥ワイパーと、前記汚泥ワイパーでかき集められた前記微細固形物を収容して前記処理タンク外へ排出する汚泥シューターと、前記処理タンク内から浄化した液体を排出する排出管と、前記排出管と連通し前記処理タンクの液面の高さを微調整する水位調整部を有する水位調整容器と、前記汚水に気泡を混入するために前記処理タンク外において前記汚水導入管に連設したマイクロバブル発生装置と、で構成し、前記汚水導入管は、前記汚水案内管の内部に貫通して前記汚水案内管の前記内部において開口端が鉛直上方となるよう真上に湾曲して屈曲し、前記汚水案内管は、上端に上方に拡開した鍔を形成し、前記汚泥ワイパーは、前記処理タンクの鉛直中心軸を起点として水平方向に回動すると共に、前記整流部は、前記汚泥ワイパーの下方において同軸に連設し、前記整流部は、円錐状の整流下面と円柱状の整流側面からなる下端先鋭のコマ型に形成し、前記水位調整部は、前記排出管の上端部を前記水位調整容器の底部から突出するよう形成し、突出した部位の周側面を螺刻して円筒状の雄ネジ管とし、これに内側面を螺刻した円筒状の雌ネジ管を螺合可能に構成したことを特徴とする微細固形物分離装置を提供せんとする。
In the invention according to claim 1, the purification device comprises a treatment tank for separating the sewage into solid and liquid, and the sewage introduction pipe for introducing the sewage into the treatment tank from the outside, the sewage introduction pipe, and the treatment Upper and lower sewage guide pipes communicating within the tank, a straightening unit disposed at a predetermined gap above the dirty water guide pipe and straightening the dirty water flowing out from the upper opening of the dirty water guide pipe, and the straightening unit A sludge wiper which is disposed above the surface of the waste water so as to scrape the fine solid matter of the dirty water which is floated above the predetermined gap, and a sludge shooter which contains the fine solid matter scraped by the sludge wiper and discharges it out of the treatment tank; contamination and discharge pipe, and the water level adjusting container having a level adjusting unit for finely adjusting the height of the liquid surface of the treatment tank communicating with said discharge pipe, a bubble in the sewerage for discharging clarified liquid from the processing tank A microbubble generating apparatus and continuously to the wastewater feed pipe in the treatment tank outside in order, in constructed, the wastewater inlet tube, in the interior of the sewerage guide tube through the inside of the sewerage guide tube Curved and bent right up so that the open end is vertically upward, the dirty water guide pipe forms a weir that spreads upward at the upper end, and the sludge wiper starts from the vertical central axis of the processing tank While rotating in the horizontal direction, the flow straightening unit is coaxially connected below the sludge wiper, and the flow straightening unit is formed into a sharpened lower end pointed by a conical flow straight lower surface and a cylindrical flow straight side. The water level adjusting portion is formed such that the upper end portion of the discharge pipe protrudes from the bottom portion of the water level adjusting container, and the peripheral side surface of the protruding portion is screwed to form a cylindrical male screw pipe. Cylindrical female thread screwed on the side Providing cents to fine solids separation device, characterized in that to constitute a tube to be screwed.

請求項2に係る発明では、前記処理タンクの底部には、沈殿した汚泥を前記処理タンク外に排出する沈殿物排出管を備え、前記沈殿物排出管は、前記処理タンクの底部近傍から水平方向に伸延して上方に立設した前記沈殿物排出管の中途部に空気を送り込む空気導入管を連通連接したことを特徴とする請求項1に記載の微細固形物分離装置を提供せんとする。
In the invention according to claim 2, the bottom of the processing tank is provided with a sediment discharge pipe for discharging the deposited sludge to the outside of the processing tank, and the sediment discharge pipe is in the horizontal direction from near the bottom of the processing tank An apparatus for separating fine solids according to claim 1, wherein an air introduction pipe for feeding air to a middle portion of the sediment discharge pipe which is extended upward and set up upward is connected in communication .

請求項3に係る発明では、前記整流部は、前記整流側面の中途部に前記整流側面を囲繞する円環状の気泡破壊部を形成したことを特徴とする請求項2に記載の微細固形物分離装置を提供せんとする。
In the invention according to claim 3 , the fine solid separated matter according to claim 2, characterized in that the straightening unit forms an annular bubble breaking portion surrounding the straight side surface at a middle portion of the straight side surface. We will provide equipment.

請求項1記載の発明によれば、外部から処理タンク内に汚水を導入する汚水導入管と、汚水導入管と処理タンク内で連通する上下開口の汚水案内管と、汚水案内管の上方に所定の間隙で配設され汚水案内管の上開口部から流出した汚水を整流する整流部と、整流部の上方に所定の間隙で配設され浮上した汚水の微細固形物をかき集める汚泥ワイパーと、汚泥ワイパーでかき集められた微細固形物を収容して処理タンク外へ排出する汚泥シューターと、処理タンク内から浄化した液体を排出する排出管と、排出管と連通し処理タンクの液面の高さを微調整する水位調整部を有する水位調整容器と、汚水に気泡を混入するために処理タンク外において汚水導入管に連設したマイクロバブル発生装置と、で構成し、汚水導入管は、汚水案内管の内部に貫通して汚水案内管の内部において開口端が鉛直上方となるよう真上に湾曲して屈曲し、汚水案内管は、上端に上方に拡開した鍔を形成し、汚泥ワイパーは、処理タンクの鉛直中心軸を起点として水平方向に回動すると共に、整流部は、汚泥ワイパーの下方において同軸に連設し、整流部は、円錐状の整流下面と円柱状の整流側面からなる下端先鋭のコマ型に形成し、水位調整部は、排出管の上端部を水位調整容器の底部から突出するよう形成し、突出した部位の周側面を螺刻して円筒状の雄ネジ管とし、これに内側面を螺刻した円筒状の雌ネジ管を螺合可能に構成したことより、浮力のない固形物は汚水案内管の下開口部から処理タンクの下方へと沈殿し、気泡が付着した微細固形物は浮力によって汚水案内管の上開口部から流出しつつ上方の整流部によって微細固形物から気泡が分離することなく液面に浮上させることができるので微細固形物からなる汚泥を汚泥ワイパーにより効率よく回収でき、排出管を通して浄化レベルの高い処理水を取り出すことが可能となり、また、整流部は、円錐状の整流下面と円柱状の整流側面からなる下端先鋭のコマ型に形成したことより、汚水案内管の上開口部から流出した気泡が付着した微細固形物をまんべんなく放射状に整流させ液面に浮上させることができるので、微細固形物からの気泡の分離を安定的に防止することができる。また、汚水導入管は、汚水案内管の内部に貫通して汚水案内管の内部において開口端が鉛直上方となるよう真上に屈曲したことより、汚水中の浮力を有さない固形物は汚水案内管に沿って下降し、浮力を有する固形物や気泡が付着した微細固形物は汚水案内管に沿って上昇させることができ、また、汚水案内管は、上端に上方に拡開した鍔を形成したことより、汚水案内管の上開口部から流出した気泡が付着した微細固形物を上方の整流部に向けてまんべんなく確実に流出させることができるので、微細固形物からの気泡の分離を更に安定的に防止することができる。また、汚泥ワイパーは、処理タンクの鉛直中心軸を起点として水平方向に回動すると共に、整流部は、汚泥ワイパーの下方において同軸に連設したことより、汚泥ワイパーの回動を阻害することなく整流部を処理タンクの上部に垂設でき、しかも、整流部を鉛直中心軸に水平断面視同心円形状とすれば、たとえ整流部が汚泥ワイパーと同軸で回動しても整流部により処理タンク内の汚水を掻き乱すことなく整流作用を発揮させることができる。更に、マイクロバブル発生装置により、ほとんどすべての微細固形物に極小の気泡を付着させることができるので、浄化レベルの極めて高い処理水を取り出すことが可能となる。また、水位調整部の雄ネジ管に対する雌ネジ管の位置を上下することで水位調整容器内の水位、すなわち、処理タンクの液面高さを容易に微調整することができる。
According to the invention of claim 1, the sewage introduction pipe for introducing the sewage into the treatment tank from the outside, the sewage guide pipe of the upper and lower opening communicating with the sewage introduction pipe and the treatment tank, and the predetermined position above the sewage guide pipe A straightening unit disposed in the gap between the upper and the lower openings of the dirty water guide pipe, a sludge wiper disposed in a predetermined gap above the straightening unit, and collecting fine solids of the raised sewage; A sludge shooter that contains fine solids collected by the wiper and discharges it out of the treatment tank, a discharge pipe that discharges the purified liquid from the inside of the treatment tank, and the height of the liquid surface of the treatment tank in communication with the discharge pipe. It consists of a water level adjustment container that has a water level adjustment part that fine-tunes, and a micro bubble generator connected to the sewage introduction pipe outside the treatment tank to mix air bubbles into the sewage. Inside Inside the dirty water guide pipe, it bends and bends right up so that the open end is vertically upward inside the dirty water guide pipe, the dirty water guide pipe forms a weir that spreads upward at the upper end, and the sludge wiper While rotating in the horizontal direction starting from the vertical central axis, the straightening unit is coaxially connected below the sludge wiper, and the straightening unit is a sharpened lower end consisting of a conical straightening lower surface and a cylindrical straightening side The water level adjustment part is formed into a mold, the upper end of the discharge pipe is formed to project from the bottom of the water level adjustment container, and the peripheral side surface of the protruding part is screwed to form a cylindrical male screw pipe. Since the cylindrical female screw tube whose side is screwed is configured to be able to be screwed, solid material without buoyancy precipitates from the lower opening of the sewage guiding tube to the lower side of the treatment tank, and the fine particles with bubbles attached Solid matter flows out from the upper opening of the sewage guide tube by buoyancy Since it can be floated on the liquid surface without separating air bubbles from the fine solid by the straightening unit, sludge consisting of fine solid can be efficiently recovered by the sludge wiper, and treated water with high purification level is taken out through the discharge pipe In addition, since the straightening portion is formed in a sharpened lower end having a conical straightening lower surface and a cylindrical straightening side, it is possible to fine the air flowed out from the upper opening of the dirty water guide pipe Since the solid matter can be uniformly and radially rectified to float on the liquid surface, separation of air bubbles from the fine solid matter can be stably prevented. In addition, since the sewage introduction pipe penetrates into the inside of the sewage guide pipe and is bent upward so that the open end is vertically upward inside the sewage guide pipe, solid substances that do not have the buoyancy of the sewage become sewage. It is possible to move downward along the guide tube, and float solid solids and air bubbles attached fine solid matter can rise along the dirty water guide tube, and the dirty water guide tube also spreads the weir spread upward at the upper end. Since the fine solid matter which the bubbles which flowed out from the upper opening of the dirty water guide pipe can be made to flow out uniformly toward the upper straightening part reliably from having formed, separation of the bubble from the fine solid matter is further achieved. It can be prevented stably. Further, the sludge wiper rotates in the horizontal direction starting from the vertical central axis of the processing tank, and the rectifying unit is coaxially provided below the sludge wiper, without disturbing the rotation of the sludge wiper. If the flow straightening unit can be provided above the processing tank and the flow straightening unit has a concentric shape with a vertical central axis in horizontal cross sectional view, even if the flow straightening unit rotates coaxially with the sludge wiper, the flow straightening unit The rectification action can be exhibited without disturbing the waste water of the Furthermore, since the microbubble generating device makes it possible to attach minimal air bubbles to almost all the fine solid substances, it is possible to take out treated water having a very high purification level. Further, the water level in the water level adjusting container, that is, the liquid level height of the processing tank can be easily finely adjusted by moving the position of the female screw pipe relative to the male screw pipe of the water level adjusting portion.

請求項2記載の発明によれば、処理タンクの底部には、沈殿した汚泥を処理タンク外に排出する沈殿物排出管を備え、沈殿物排出管は、処理タンクの底部近傍から水平方向に伸延して上方に立設した沈殿物排出管の中途部に空気を送り込む空気導入管を連通連接したことより、沈殿物排出管の内部に充填した汚泥を空気の浮力によって上方へと移動させて外部へ排出することができる。
According to the invention of claim 2, the bottom of the processing tank is provided with a sediment discharge pipe for discharging the deposited sludge to the outside of the processing tank, and the sediment discharge pipe extends horizontally from the vicinity of the bottom of the processing tank Since the air introduction pipe for feeding air to the middle part of the sediment discharge pipe erected upward is connected and connected, the sludge filled in the inside of the sediment discharge pipe is moved upward by the buoyancy of the air to the outside Can be discharged into

請求項3記載の発明によれば、整流部は、整流側面の中途部に整流側面を囲繞する円環状の気泡破壊部を形成したことより、液面に影響を及ぼす程度の大きな気泡を気泡破壊部に衝突させて破壊することができる。
According to the third aspect of the present invention, since the straightening unit forms an annular bubble breaking portion surrounding the straight side surface at the middle portion of the straight side surface, it can break large bubbles that affect the liquid level. It can be destroyed by colliding with a part .

本実施形態に係る微細固形物分離装置の各構成を同一断面内に簡略的に配設した説明図である。It is explanatory drawing which arrange | positioned simply each structure of the fine-solids separation apparatus which concerns on this embodiment in the same cross section. 本実施形態に係る微細固形物分離装置の平面図である。It is a top view of the fine-solids separation device concerning this embodiment. (a)は汚水案内管と整流部を示す説明用斜視図で、(b)は整流側面に気泡破壊部を形成した整流部の説明用斜視図である。(A) is a perspective view for description which shows a sewage guide pipe and a rectification part, (b) is a perspective view for explanation of the rectification part which formed the bubble destruction part in the rectification side. 本実施形態に係る微細固形物分離装置が用いられる全体構成例を示す図である。BRIEF DESCRIPTION OF THE DRAWINGS It is a figure which shows the example of whole structure in which the fine-solids separation apparatus which concerns on this embodiment is used. (a)は汚泥シューターの簡易斜視図で、(b)はその簡易側面図である。(A) is a simplified perspective view of a sludge shooter, and (b) is a simplified side view thereof. (a)は水位調整部を構成する可変プレートの正面図で、(b)は基準プレートの正面図で、(c)は水位調整容器にガイド支柱で基準プレートを固定した正面図である。(A) is a front view of the variable plate which comprises a water level adjustment part, (b) is a front view of a reference plate, (c) is a front view which fixed the reference plate to the water level adjustment container by the guide support | pillar. (a)は図2におけるA−A線断面図において可変プレートを下降させた図で、(b)は可変プレートを少し上昇させた図で、(c)は可変プレートを更に上昇させた図である。(A) is a diagram in which the variable plate is lowered in the cross-sectional view along the line A-A in FIG. 2, (b) is a diagram in which the variable plate is slightly raised, and (c) is a diagram in which the variable plate is further raised is there. (a)は他の水位調整部を構成する雄ネジ管と雌ネジ管の斜視図で、(b)は図2におけるA−A線断面図に準じて雌ネジ管を下降させた図で、(c)は雌ネジ管を上昇させた図である。(A) is a perspective view of a male screw pipe and a female screw pipe that constitute another water level adjustment unit, and (b) is a drawing in which the female screw pipe is lowered according to the sectional view taken along line A-A in FIG. (C) is the figure which raised the internal thread pipe.

本発明に係る微細固形物分離装置の要旨は、汚水を固形物と液体に分離する処理タンクかならる浄化装置であって、外部から処理タンク内に汚水を導入する汚水導入管と、汚水導入管と処理タンク内で連通する上下開口の汚水案内管と、汚水案内管の上方に所定の間隙で配設され汚水案内管の上開口部から流出した汚水を整流する整流部と、整流部の上方に所定の間隙で配設され浮上した汚水の微細固形物をかき集める汚泥ワイパーと、汚泥ワイパーでかき集められた微細固形物を収容して処理タンク外へ排出する汚泥シューターと、処理タンク内から浄化した液体を排出する排出管と、汚水に気泡を混入するために汚水導入管に連設したエアーポンプと、で構成したことを特徴とする。すなわち、シンプルな構造でありながら浄化レベルの高い処理水を排出できる微細固形物分離装置の提供を図ろうとするものである。   The gist of the fine solid matter separation device according to the present invention is a purification device consisting of a treatment tank for separating sewage into solid and liquid, and a sewage introduction pipe for introducing sewage into the treatment tank from the outside, and sewage introduction Pipes and communicating pipes in the treatment tank; a straightening unit disposed at a predetermined gap above the dirty water guide pipes and rectifying the dirty water flowing out from the upper opening of the dirty water guide pipes; A sludge wiper which is disposed at a predetermined gap above and picks up the fine solid matter of surfaced sludge which has floated up, a sludge shooter which contains the fine solid matter scraped by the sludge wiper and discharges it out of the treatment tank, and purification from within the treatment tank It is characterized in that it comprises an exhaust pipe for discharging the liquid and an air pump connected to the sewage introduction pipe in order to mix air bubbles into the sewage. That is, it is an object of the present invention to provide a fine solid separation device capable of discharging treated water having a high purification level while having a simple structure.

以下、本発明に係る微細固形物分離装置の実施形態について図面を参照しながら説明する。また、本説明中において左右同一又は左右対称の構造や部品については、原則として同一の符号を付し、左右何れか一方のみを説明して、他方については説明を適宜省略する。   Hereinafter, an embodiment of a fine solid separation device according to the present invention will be described with reference to the drawings. Further, in the present description, the same symbols are attached in principle to the structures or parts which are the same in left and right or in left and right symmetry, and only one of the left and right is explained, and the explanation is omitted suitably for the other.

本発明の実施形態に係る微細固形物分離装置1は、図1、図2、図3(a)に示すように、外部から処理タンク2内に汚水Wを導入する汚水導入管3と、汚水導入管3と処理タンク2内で連通する上下開口の汚水案内管5と、汚水案内管5の上方に所定の間隙で配設され汚水案内管5の上開口部から流出した汚水Wを整流する整流部8と、整流部8の上方に所定の間隙で配設され浮上した汚水の微細固形物をかき集める汚泥ワイパー13と、汚泥ワイパー13でかき集められた微細固形物を収容して処理タンク2外へ排出する汚泥シューター23と、処理タンク2内から浄化した液体(処理水)Sを排出する排出管32と、汚水Wに気泡を混入するために汚水導入管3に連設したエアーポンプ49と、で構成している。   The fine solid matter separation device 1 according to the embodiment of the present invention, as shown in FIG. 1, FIG. 2 and FIG. 3 (a), is a sewage introduction pipe 3 for introducing sewage W into the treatment tank 2 from the outside, The dirty water guide pipe 5 of the upper and lower opening which communicates in the introduction pipe 3 and the treatment tank 2 and a predetermined gap above the dirty water guide pipe 5 are used to rectify the dirty water W flowing out from the upper opening of the dirty water guide pipe 5 Rectifying portion 8, sludge wiper 13 disposed at a predetermined gap above the rectifying portion 8 and scraping the fine solid matter of sludge that has floated up, containing the fine solid matter scraped by the sludge wiper 13 outside the treatment tank 2 And a discharge pipe 32 for discharging the liquid (treated water) S purified from the inside of the treatment tank 2, and an air pump 49 connected to the waste water introduction pipe 3 for mixing air bubbles in the waste water W , Consists of.

また、整流部8は、下端先鋭の円錐状に形成し、汚水案内管5は、上端において上方に拡開した鍔6を形成している。   Further, the flow straightening unit 8 is formed in a conical shape with a sharp lower end, and the dirty water guide pipe 5 forms a weir 6 expanded upward at the upper end.

更に、汚泥ワイパー13は、処理タンク2の鉛直中心軸Gを起点として水平方向に回動すると共に、整流部8は、汚泥ワイパー13の下方において同軸に連設している。   Furthermore, the sludge wiper 13 rotates in the horizontal direction starting from the vertical central axis G of the processing tank 2, and the rectifying unit 8 is coaxially connected below the sludge wiper 13.

このように構成することで、浮力のない固形物は汚水案内管5の下開口部から処理タンク2の下方へと沈殿し、気泡が付着した微細固形物は浮力によって汚水案内管5の上開口部から流出し、気泡が付着した微細固形物が気泡と分離することなくまんべんなく放射状に整流され液面Hに浮上させることができ、微細固形物等からなる汚泥を汚泥ワイパー13により回収することで排出管32を通して浄化レベルの高い処理水Sを取り出すことが可能となる。   By configuring in this way, solid material without buoyancy precipitates from the lower opening of the sewage guiding tube 5 to the lower part of the treatment tank 2, and fine solid matter with attached air bubbles floats on the upper opening of the sewage guiding tube 5 by buoyancy. The fine solid matter which has flowed out from the part and can adhere to the bubbles can be uniformly rectified radially without separating it from the bubbles and can rise to the liquid level H, and the sludge consisting of the fine solid matter is recovered by the sludge wiper 13 It is possible to take out the treated water S having a high purification level through the discharge pipe 32.

このような微細固形物分離装置1は、汚水レベルが高い場合、例えば、図4に示すように、豚舎からの糞尿等を固形物と液状物に分離する簡易的な重力沈殿槽の後段に配置し、微細固形物分離装置1の後段に曝気槽を配置し、曝気槽の後段に最終の簡易的な重力沈殿槽を設置して河川等へ放出させるたりするものである。   Such a fine solid separation device 1 is disposed at the latter stage of a simple gravity sedimentation tank that separates manure and the like from a piggery into solid and liquid as shown in FIG. 4, for example, when the sewage level is high. Then, an aeration tank is disposed downstream of the fine solid separation device 1, and a final simple gravity settling tank is disposed downstream of the aeration tank to be discharged to a river or the like.

また、簡易的な重力沈殿槽や微細固形物分離装置1、最終の簡易的な重力沈殿槽等から排出される汚泥は脱水機に投入され、固形物なった状態で肥料等へと活用される。 In addition, the sludge discharged from the simple gravity settling tank, the fine solid separation device 1, the final simple gravity settling tank, etc. is input to the dehydrator and is used as fertilizer in the solid state. Ru.

なお、本実施形態に係る微細固形物分離装置1は、上述の構成に限定されるものではなく、汚水レベルや外部環境等により如何なる構成であってもよく、本発明の要旨の範囲内において種々の変形・変更が可能である。   In addition, the fine solid matter separation device 1 according to the present embodiment is not limited to the above-described configuration, and may have any configuration depending on the level of the sewage, the external environment, etc. It is possible to change and change

また、本実施形態の微細固形物分離装置1では、エアーポンプ49として後述するマイクロバブル発生装置49aを用いることで微細固形物の約90%を除去できるため薬品を使用する必要がなく、従って、曝気槽における微生物の管理も容易となり、更に、最終の重力沈殿槽で無害化する手間を省くことができるため、消耗品や副資材にかかる費用が抑えられ、更に、運用費を廉価に抑えることが可能となる。   Further, in the fine solid matter separation device 1 of the present embodiment, about 90% of the fine solid matter can be removed by using a microbubble generation device 49a described later as the air pump 49, and therefore, it is not necessary to use chemicals. The management of the microorganisms in the aeration tank is also facilitated, and further, the time and effort required to render it harmless in the final gravity settling tank can be omitted, so that the cost for consumables and auxiliary materials can be reduced, and the operation cost can be reduced. Is possible.

しかも、回収された固形物(微細固形物を含む)にも、薬品が含まれないため、脱水機により完全な固形物とした後、安全な肥料等として利用することができる。   In addition, since the collected solid (including fine solid) also contains no medicine, it can be used as a safe fertilizer after it is completely solidified by a dehydrator.

次に、本実施形態に係る微細固形物分離装置1の各部の構成について、図面を用いて具体的に詳述する。   Next, the configuration of each part of the fine solid matter separation device 1 according to the present embodiment will be specifically described in detail using the drawings.

まず、図1に示すように、微細固形物分離装置1の本体を構成する処理タンク2は、下半部を下端先鋭の円錐状に形成し、上半部を上部開口の円筒状に形成した大型容器として形成している。   First, as shown in FIG. 1, in the processing tank 2 constituting the main body of the fine solid matter separating device 1, the lower half portion is formed in a conical shape at the lower end tip and the upper half portion is formed in a cylindrical shape of the upper opening It is formed as a large container.

また、処理タンク2の下半部の中途部には汚水導入管3が配設され、処理タンク2の外部においてエアーポンプ49を連設し、エアーポンプ49には原水として浄水Jが導入され、汚水Wと共に気泡を混入した原水が混合されるよう構成し、循環水ではなく清浄な浄水Jを導入することで浄化能力の向上を図っている。   In the middle of the lower half of the treatment tank 2, a sewage introduction pipe 3 is disposed, an air pump 49 is connected to the outside of the treatment tank 2, and clean water J is introduced into the air pump 49 as raw water. Raw water mixed with air bubbles is mixed with the dirty water W, and the purification capacity is improved by introducing clean clean water J instead of circulating water.

なお、本実施形態では循環水ではなく清浄な浄水Jを導入しているが、循環水の導入を排除するものでないことは言うまでもない。   In addition, in this embodiment, although not the circulating water but the clean purified water J is introduced, it is needless to say that the introduction of the circulating water is not excluded.

また、本実施形態ではエアーポンプ49として数μm〜約50μmの極小の気泡を発生させることができるマイクロバブル発生装置49a(株式会社ニクニ製:MBG25N15PE−1BH)を用いている。   Further, in the present embodiment, as the air pump 49, a micro-bubble generating device 49a (manufactured by Nikuni Co., Ltd .: MBG25N15PE-1BH) capable of generating micro bubbles of several μm to about 50 μm is used.

また、汚水導入管3は処理タンク2の内部に水平に引き込まれ、処理タンク2の鉛直中心軸Gに軸心を有する汚水案内管5の側壁の中途部において水密に貫通しており、汚水案内管5の内部において開口端が鉛直上方となるよう真上に屈曲し、汚水中の浮力を有さない固形物は汚水案内管5に沿って下降し、浮力を有する固形物や気泡が付着した微細固形物は汚水案内管5に沿って上昇する。   In addition, the dirty water introduction pipe 3 is drawn horizontally into the inside of the treatment tank 2 and penetrates watertightly in the middle part of the side wall of the dirty water guide pipe 5 having an axial center on the vertical central axis G of the treatment tank 2 Inside the pipe 5, the open end is bent upwards so that the open end is vertically upward, and the solid without buoyancy in the sewage descends along the sewage guide pipe 5, and the solid with solidity and air bubbles adhere The fine solids rise along the sewage guiding tube 5.

汚水案内管5は、上下開口の円筒状に形成し、上端部周縁を外側に折曲して上方に拡開させることで図3(a)に示すように、平面視円環状の鍔6を形成しており、下降する固形物は汚水案内管5の下開口部から処理タンク2の底部へと沈殿し、上昇する微細固形物等は上開口部から流出する。   The dirty water guide pipe 5 is formed in the cylindrical shape of the upper and lower opening, and the upper end portion peripheral edge is bent outward and expanded upward as shown in FIG. The falling solids are deposited from the lower opening of the sewage guiding tube 5 to the bottom of the treatment tank 2, and the rising fine solids and the like flow out from the upper opening.

また、汚水案内管5の上方には所定の間隙で下端先鋭の円錐状に形成したコマ型(図3(a)参照)の整流部8を配設しており、具体的には円錐状の整流下面9と円柱状の整流側面10とを備え、汚水案内管5と同様に処理タンク2の鉛直中心軸Gが軸心となるよう配設しており、上端面の中心部には後述するモータ17のモータ軸18を連接している。   Further, above the dirty water guide pipe 5, there is disposed a straight section (see FIG. 3 (a)) having a predetermined gap formed in a conical shape at the lower end tip (see FIG. 3 (a)). It has a straight lower surface 9 and a straight cylindrical side surface 10, and is disposed so that the vertical central axis G of the processing tank 2 is the same as the dirty water guide pipe 5, and it will be described later The motor shaft 18 of the motor 17 is connected.

なお、汚水案内管5の上開口部から流出する汚水Wを安定的に整流して浮上させるには、鍔6の外径が整流部8の外径と同一であるか小径であることが望ましい。   In addition, in order to stably rectify and float the sewage W flowing out from the upper opening of the sewage guide pipe 5, it is desirable that the outer diameter of the weir 6 be equal to or smaller than the outer diameter of the flow straightening unit 8. .

また、鍔6の傾斜角度と整流下面9の傾斜角度は略5°〜略45°の範囲で同一に形成し、特に35°±10°の傾斜角度とすることで整流効果を顕著に現出させることができ、鍔6の傾斜角度と整流下面9の傾斜角度との誤差は±3°以内が望ましい。   Further, the inclination angle of the weir 6 and the inclination angle of the rectifying lower surface 9 are formed identically in the range of approximately 5 ° to approximately 45 °, and in particular, the rectification effect appears notably by setting the inclination angle of 35 ° ± 10 °. The difference between the inclination angle of the weir 6 and the inclination angle of the rectifying lower surface 9 is preferably within ± 3 °.

なお、本実施形態では鍔6と整流下面9との間隙を略30mmとして構成しているが、この間隙は処理タンク2の大きさや汚水Wの種類、外部環境等によって適宜最適な条件とすることができる。   In the present embodiment, the gap between the weir 6 and the straight lower surface 9 is approximately 30 mm, but this gap should be appropriately optimized depending on the size of the treatment tank 2, the type of waste water W, the external environment, etc. Can.

また、図3(b)に示すように、整流部8の中途部には整流側面10を囲繞する円環状の気泡破壊部11を形成することもでき、液面Hに影響を及ぼす程度の大きな気泡を気泡破壊部11に衝突させて破壊する役割を果たす。   Further, as shown in FIG. 3B, an annular bubble destruction portion 11 surrounding the rectification side surface 10 can be formed in the middle portion of the rectification portion 8, and a large degree that affects the liquid level H can be formed. It plays a role of colliding the air bubble with the air bubble destruction part 11 and destroying it.

また、図1、図2に示すように、整流部8の上端面に連接するモータ軸18の中途部には、ステー14とブレード15からなる水平方向に回動する汚泥ワイパー13を突設し、モータ17を制御することで汚泥ワイパー13がモータ軸18、すなわち鉛直中心軸Gを軸心として液面H近傍の汚泥をかき集めることができる。   Further, as shown in FIGS. 1 and 2, a horizontally rotating sludge wiper 13 consisting of a stay 14 and a blade 15 is provided in the middle of the motor shaft 18 connected to the upper end face of the flow straightening unit 8. By controlling the motor 17, the sludge wiper 13 can scrape the sludge in the vicinity of the liquid level H with the motor shaft 18, that is, the vertical central axis G as an axis.

具体的には、ステー14は水平片と垂直片からなる断面視逆L字状で、処理タンク2の円筒状の上半部の内壁に接触しない程度、すなわち、上半部の半径よりも若干だけ短尺に形成すると共に、ブレード15は弾性部材で形成し、整流部8の整流側面10と処理タンク2の内壁との間に近接して収まる程度の横長で長方形状に形成している。   Specifically, the stay 14 has a reverse L-shape in cross-sectional view consisting of a horizontal piece and a vertical piece, and does not come in contact with the inner wall of the cylindrical upper half of the processing tank 2, that is, slightly smaller than the radius of the upper half. The blade 15 is formed of an elastic member, and is formed in a rectangular shape having a width enough to be close to be fitted between the straightening side surface 10 of the straightening unit 8 and the inner wall of the processing tank 2.

また、汚泥ワイパー13は、ステー14を構成するL字の鉛直片においてボルト等にてブレード15の上端縁を咬止し、ステー14に対してブレード15を垂設することで構成される。   Further, the sludge wiper 13 is configured by locking the upper end edge of the blade 15 with a bolt or the like in the L-shaped vertical piece that constitutes the stay 14, and hanging the blade 15 against the stay 14.

なお、本実施形態では汚泥ワイパー13を処理タンク2の略半径程度の長さとしてアナログ時計の如く形成しているが、例えば、処理タンク2の略直径程度としてその中心に鉛直中心軸Gを位置させたり、鉛直中心軸Gを軸心として平面視十字状に形成する等、本発明の要旨の範囲内において種々の変形・変更が可能である。   In the present embodiment, the sludge wiper 13 is formed as an approximate length of the radius of the processing tank 2 like an analog watch, but for example, the vertical central axis G is positioned at the center as an approximate diameter of the processing tank 2 Various modifications and changes are possible within the scope of the subject matter of the present invention, such as forming a vertical center axis G as an axis and forming a cross shape in plan view.

モータ17は、処理タンク2の対向する上端に架設した基礎架台20の上に取付架台21を架設し、モータ軸18が鉛直下方となるように取付架台21に固定している。   The motor 17 has a mounting base 21 mounted on a base 20 mounted on the opposing upper end of the processing tank 2 and is fixed to the mounting base 21 so that the motor shaft 18 is vertically downward.

具体的には、基礎架台20は、処理タンク2の円筒状の上半部の直径程度の長さの2本の角棒からなり、これらを所定間隔の平行に配設して処理タンク2の上端に架設し、更に、取付架台21は、基礎架台20に直交して跨ぐ短尺の2本の角棒からなり、これらを所定間隔の平行に配設して基礎架台20上に架設し、モータ17をボルト等により取付架台21に螺合して固定している。   Specifically, the foundation frame 20 is composed of two square bars having a length about the diameter of the cylindrical upper half of the processing tank 2, and these are disposed in parallel at a predetermined interval to provide The mounting base 21 is constructed at the upper end, and further, the mounting base 21 is formed of two short rectangular bars straddling the base base 20 at right angles, which are arranged in parallel at a predetermined interval to be bridged on the base base 20 Reference numeral 17 is screwed and fixed to the mounting base 21 with a bolt or the like.

なお、本実施形態では省略しているが、実際にはモータ17に減速機を付加して適切な回転数に制御できるよう構成している。   Although omitted in the present embodiment, a reduction gear is actually added to the motor 17 so that it can be controlled to an appropriate rotational speed.

また、処理タンク2の上半部の上方、すなわち、整流部8の整流側面10の側方には汚泥シューター23を配設しており、汚泥シューター23により汚泥ワイパー13でかき集められた微細固形物を収容して処理タンク2外へ排出される。   Further, a sludge shooter 23 is disposed above the upper half of the treatment tank 2, that is, on the side of the straightening side surface 10 of the flow straightening unit 8, and the fine solid collected by the sludge wiper 13 by the sludge shooter 23. To be discharged out of the processing tank 2.

具体的には、汚泥シューター23は、シューター部24と案内部27とで構成しており、図2、図5(a)、(b)に示すようにシューター部24は側面視略逆直角三角形状で平面視略長方形状の上方開口の箱体に形成しており、一側面を処理タンク2の内壁に固定して処理タンク2の内壁も含めて箱体をなしている。   Specifically, the sludge shooter 23 is composed of a shooter portion 24 and a guide portion 27. As shown in FIGS. 2, 5 (a) and 5 (b), the shooter portion 24 is a substantially reverse rectangular triangle in a side view. It is formed in a box in the form of an upper opening substantially rectangular in plan view, and one side is fixed to the inner wall of the processing tank 2 to form a box including the inner wall of the processing tank 2.

また、整流部8の整流側面10の近傍に位置するシューター部24の先端は、整流側面10の外形に倣って内側に凹状のシューター湾曲部25を形成している。   Further, the tip of the shooter portion 24 located in the vicinity of the straightening side surface 10 of the straightening unit 8 forms a concave shooter curved portion 25 inward according to the outer shape of the straightening side surface 10.

また、シューター部24の一側面をなす処理タンク2の下端縁近傍には、外部と連通する汚泥回収管26を処理タンク2の外壁に連通連接しており、回収された汚泥を外部に排出することができる。   In the vicinity of the lower end of the processing tank 2 forming one side of the shooter portion 24, a sludge collection pipe 26 communicating with the outside is connected to the outer wall of the processing tank 2 and the collected sludge is discharged to the outside. be able to.

また、案内部27は、主案内部28と副案内部29とで構成し、主案内部28は三角形状の平板からなり、一辺をシューター部24の開口端辺と同一の長さに形成してシューター部24の一方の開口端部に接続し、全体を下方へ傾斜させた状態で異なる他の一辺を処理タンク2の内壁に接続している。   The guide portion 27 is composed of a main guide portion 28 and a sub guide portion 29. The main guide portion 28 is formed of a triangular flat plate, and one side is formed to have the same length as the open end side of the shooter portion 24. The other side is connected to the inner wall of the processing tank 2 while being connected to one open end of the shooter portion 24 and the whole is inclined downward.

また、副案内部29は、略三角形状の平板からなり、主案内部28の更に他の一辺に同長さの副案内部29の一辺を連接し、全体を主案内部28よりも更に下方へ傾斜させている。   Further, the sub guide portion 29 is formed of a substantially triangular flat plate, one side of the sub guide portion 29 having the same length is connected to the other side of the main guide portion 28 and the whole is further below the main guide portion 28 It is inclined to.

また、整流部8の整流側面10の近傍に位置する副案内部29の他の一辺は、整流側面10の外形に倣って内側に凹状の案内湾曲部30を形成している。   Further, the other side of the sub guide portion 29 located in the vicinity of the straightening side surface 10 of the straightening unit 8 forms a concave guide curved portion 30 inward according to the outer shape of the straightening side surface 10.

このような汚泥シューター23は、シューター部24の開口部が液面Hよりも若干だけ上方に露出するよう配設され、液面近傍を回動する汚泥ワイパー13によりかき集められた微細固形物等からなる汚泥をシューター部24に収容する際、整流された液面Hが乱れたりせず、汚泥を効率よく収容するために案内部27が重要な役割を果たす。   The sludge shooter 23 is disposed such that the opening of the shooter portion 24 is exposed slightly above the liquid level H, and the fine solid collected from the sludge wiper 13 rotating around the liquid level is used. When housing the sludge in the shooter portion 24, the rectified liquid level H is not disturbed, and the guide portion 27 plays an important role in storing the sludge efficiently.

なお、本実施形態では案内部27を主案内部28と副案内部29とで構成しているが、副案内部29を形成せず主案内部28のみで構成してもよい。   In addition, although the guide part 27 is comprised by the main guide part 28 and the subguide part 29 in this embodiment, you may comprise only the main guide part 28 without forming the subguide part 29. FIG.

また、本実施形態では案内部27を平板で形成しているが、案内部27の下部側を密閉空間となるような立体構造、すなわち、案内部27の下側が凹状とならないよう形成し、浮上する微細固形物等が可能な限り滞留しないよう形成することもできる。   Further, in the present embodiment, the guide portion 27 is formed of a flat plate, but a three-dimensional structure in which the lower side of the guide portion 27 is a sealed space, that is, the lower side of the guide portion 27 is not concaved It can also be formed so as not to stay as fine as possible.

このように、汚水導入管3を通して汚水案内管5に導入された汚水は、下降して処理タンク2の底部に沈殿するものと、上昇して液面Hに到達するものとに二分されるため、汚水案内管5の外部で処理タンク2の中央部近傍の液体は微細固形物等をほとんど含まない浄化レベルの高い処理水Sが占有することになる。   As described above, the sewage introduced into the sewage guide pipe 5 through the sewage introduction pipe 3 is divided into one falling down and settling in the bottom of the processing tank 2 and one rising up and reaching the liquid level H. The liquid in the vicinity of the central portion of the treatment tank 2 outside the dirty water guide pipe 5 is occupied by the treated water S having a high purification level which hardly contains fine solid matter and the like.

このような状況を可能とするのは、微細固形物に付着した気泡が整流部8の作用により分離しないためであり、特に、気泡の生成をマイクロバブル発生装置49aで行うことで顕著となり、また、処理タンク2内に導入する浄水Jを循環使用させることなく常に清浄な浄水Jを導入すれば、更に浄化レベルの高い処理水Sを精製することができる。   Such a situation is made possible because the bubbles attached to the fine solid matter are not separated by the action of the flow straightening unit 8, and in particular, the generation of the bubbles becomes remarkable by the microbubble generator 49a, and If the clean water J is always introduced without circulating the clean water J introduced into the treatment tank 2, the treated water S having a high purification level can be further purified.

また、図1に示すように、処理水Sは、排出管32によって処理タンク2の外部に排出されるが、本実施形態では排出管32から放出される処理水Sは水位調整容器34を介して最終排出移管32aから排出されるよう構成している。   Further, as shown in FIG. 1, the treated water S is discharged to the outside of the treatment tank 2 by the discharge pipe 32, but in the present embodiment, the treated water S discharged from the discharge pipe 32 is via the water level adjustment container 34. Emissions from the final emissions transfer 32a.

具体的には、排出管32は、処理タンク2の略中央部において汚水案内管5の近傍に開口部を鉛直下方として配設し、その直後で処理タンク2の上半部の壁面に向けて水平となるよう屈曲して処理タンク2外に露出し、更に、鉛直上方に屈曲して水位調整容器34へと連通するよう形成している。   Specifically, the discharge pipe 32 is disposed in the vicinity of the dirty water guide pipe 5 at a substantially central portion of the processing tank 2 with the opening vertically downward, and immediately thereafter, toward the wall surface of the upper half of the processing tank 2 It is bent so as to be horizontal and exposed to the outside of the processing tank 2, and further bent vertically upward so as to communicate with the water level adjusting container 34.

水位調整容器34は、上述のように循環させることなく処理タンク2内に導入される浄水Jの単位時間当たりの水量と、排出される処理水Sの水量とのバランスにより処理タンク2の液面Hの高さを微調整するものであり、処理タンク2の上部側の外壁と共に上方開口で略矩形箱状に形成され、内部に水位調整部35を配設している。   The water level adjustment container 34 has the liquid level of the processing tank 2 by the balance between the water quantity per unit time of the purified water J introduced into the processing tank 2 without circulating as described above and the water quantity of the processing water S discharged. The height H is finely adjusted, and is formed in a substantially rectangular box shape at the upper opening together with the outer wall on the upper side of the processing tank 2, and the water level adjusting portion 35 is disposed inside.

水位調整部35は、図6(a)、(b)、(c)に示すように、可変プレート36と基準プレート38、及び2つのガイド支柱40とで構成し、可変プレート36は、矩形板状に形成し下方に横長の楕円状の調整孔37を穿設している。   As shown in FIGS. 6 (a), (b) and (c), the water level adjustment unit 35 is composed of a variable plate 36, a reference plate 38, and two guide columns 40, and the variable plate 36 is a rectangular plate. A horizontally long elliptical adjustment hole 37 is formed at the lower side.

基準プレート38は、図6(b)に示すように、可変プレート36よりも若干だけ大きな矩形板状に形成し中央部に矩形状の基準孔39を穿設して水位調整容器34に固定されており、ガイド支柱40は、図6(c)に示すように、基準プレート38との間で可変プレート36を水密に挟持するものであり、基準プレート38と所定の間隙で水位調整容器34の壁面に密着当接する略角柱状に形成している。   As shown in FIG. 6 (b), the reference plate 38 is formed in a rectangular plate shape slightly larger than the variable plate 36, and a rectangular reference hole 39 is formed in the center and fixed to the water level adjustment container 34. As shown in FIG. 6C, the guide post 40 sandwiches the variable plate 36 with the reference plate 38 in a watertight manner, and the guide post 40 of the water level adjustment container 34 with a predetermined gap with the reference plate 38. It is formed in a substantially prismatic shape in close contact with the wall surface.

従って、図7(a)に示すように、可変プレート36を下方に位置させると調整孔37は基準プレート38の下側の基準孔39と連通し、また、図7(b)、(c)に示すように可変プレート36を上昇させることで調整孔37と基準孔39とが連通する高さt(水位調整容器34の水位)を可変することができ、すなわち、図1に示す処理タンク2の液面H高さを微調整できることになる。   Accordingly, as shown in FIG. 7 (a), when the variable plate 36 is positioned downward, the adjustment hole 37 communicates with the lower reference hole 39 of the reference plate 38, and FIGS. 7 (b) and 7 (c). The height t (the water level of the water level adjusting container 34) at which the adjustment hole 37 and the reference hole 39 communicate can be varied by raising the variable plate 36 as shown in FIG. The liquid level H height of can be finely adjusted.

なお、本実施形態の水位調整部35は上述のように構成しているが、例えば、水位調整容器34に連接する排出管32の上端部を水位調整容器34の底部から突出するよう形成し、突出した部位を図8(a)に示すように周側面を螺刻した円筒状の雄ネジ管41とし、これに内側面を螺刻した円筒状の雌ネジ管42を螺合可能に構成し、図8(b)、(c)に示すように雄ネジ管41に対する雌ネジ管42の位置を上下することで水位調整容器34内の水位t、すなわち、処理タンク2の液面H高さを微調整できるよう構成してもよい。   In addition, although the water level adjustment part 35 of this embodiment is comprised as mentioned above, it forms so that the upper end part of the discharge pipe 32 connected with the water level adjustment container 34 may be protruded from the bottom part of the water level adjustment container 34, As shown in FIG. 8 (a), the protruding portion is a cylindrical male screw tube 41 whose peripheral side is screwed, and a cylindrical female screw tube 42 whose internal side is screwed is constituted so as to be screwable. As shown in FIGS. 8 (b) and 8 (c), the water level t in the water level adjustment container 34, that is, the liquid level H of the processing tank 2 is increased by moving the position of the female screw pipe 42 relative to the male screw pipe 41. It may be configured to be able to fine-tune the

なお、本実施形態では可変プレート36や雌ネジ管42の上下動作を手動式として説明しているが、水位の調整方法や構造は本実施形態に限定されるものではなく、例えば、浄水Jの単位時間当たりの水量や排出される処理水Sの水量を電気的に検出すると共に処理タンク2の液面H高さをセンサー等で検出して可変プレート36や雌ネジ管42の位置を自動制御したり等することもできる。   In the present embodiment, the vertical movement of the variable plate 36 and the female screw tube 42 is described as a manual operation, but the method and structure for adjusting the water level is not limited to this embodiment. The amount of water per unit time and the amount of treated water S being discharged are electrically detected, and the height of the liquid surface H of the processing tank 2 is detected by a sensor or the like to automatically control the positions of the variable plate 36 and the female screw tube 42 You can also do things like

また、処理タンク2の底部に沈殿した汚泥は、図1に示すように沈殿物排出管44に流出し、脱水機等の外部装置へと排出される。   The sludge deposited on the bottom of the processing tank 2 flows out to the precipitate discharge pipe 44 as shown in FIG. 1 and is discharged to an external device such as a dehydrator.

具体的には、沈殿物排出管44は、処理タンク2の底部近傍から水平方向に伸延して端部にバルブ45を配設すると共にバルブ45の直前で上方に立設し、その中途部に空気導入管46を連通連接している。   Specifically, the precipitate discharge pipe 44 extends in the horizontal direction from the vicinity of the bottom of the processing tank 2 and arranges the valve 45 at the end and stands upward just in front of the valve 45, The air introduction pipe 46 is connected in communication.

空気導入管46はソレノイドバルブ47等を端部に備え、手動操作、又は自動操作により沈殿物排出管44の内部に空気を送り込むことができ、沈殿物排出管44の内部に充填した汚泥を空気の浮力によって上方へと移動させて外部へ排出できるよう構成している。   The air introduction pipe 46 has a solenoid valve 47 and the like at its end, and air can be fed into the inside of the sediment discharge pipe 44 by manual operation or automatic operation, and the sludge filled in the inside of the sediment discharge pipe 44 is air It is configured to be moved upward by the buoyancy of and discharged to the outside.

また、バルブ45は沈殿物排出管44の内部に滞留した汚泥等を除去するために配設されており、非定期で解放され汚泥の除去作業を行うことができる。   Further, the valve 45 is disposed to remove sludge and the like staying inside the sediment discharge pipe 44, and can be released irregularly to perform the sludge removal operation.

以上、説明したように本実施形態に係る微細固形物分離装置1は、外部から処理タンク2内に汚水を導入する汚水導入管3と、汚水導入管3と処理タンク2内で連通する上下開口の汚水案内管5と、汚水案内管5の上方に所定の間隙で配設され汚水案内管5の上開口部から流出した汚水を整流する整流部8と、整流部8の上方に所定の間隙で配設され浮上した汚水の微細固形物をかき集める汚泥ワイパー13と、汚泥ワイパー13でかき集められた微細固形物を収容して処理タンク2外へ排出する汚泥シューター23と、処理タンク2内から浄化した液体を排出する排出管32と、汚水に気泡を混入するために汚水導入管3に連設したエアーポンプ49と、で構成したことより、浮力のない固形物は汚水案内管5の下開口部から処理タンク2の下方へと沈殿し、気泡が付着した微細固形物は浮力によって汚水案内管5の上開口部から流出しつつ上方の整流部8によって微細固形物から気泡が分離することなく液面Hに浮上させることができるので微細固形物からなる汚泥を汚泥ワイパー13により効率よく回収でき、排出管32を通して浄化レベルの高い処理水を取り出すことが可能となる。   As described above, the fine solid matter separation device 1 according to this embodiment includes the sewage introduction pipe 3 for introducing sewage into the treatment tank 2 from the outside, and the upper and lower openings communicating with the sewage introduction pipe 3 in the treatment tank 2. And a straightening unit 8 disposed at a predetermined gap above the dirty water guide tube 5 and straightening the dirty water flowing out from the upper opening of the dirty water guide tube 5; and a predetermined gap above the straightening unit 8 Sludge wiper 13 for scraping and collecting fine solid matter of sewage that has been surfaced, sludge shooter 23 for containing fine solid matter scraped by sludge wiper 13 and discharging it out of treatment tank 2, and purification from inside treatment tank 2 The solid material without buoyancy comes from the lower opening of the sewage guiding pipe 5 by comprising the exhaust pipe 32 for discharging the liquid and the air pump 49 connected to the sewage introduction pipe 3 for mixing air bubbles into the sewage. Processing tank 2 from the department The fine solid that has precipitated downward and has bubbles attached flows out from the upper opening of the dirty water guide tube 5 by buoyancy, and floats up on the liquid level H without bubbles being separated from the fine solids by the upper straightening unit 8 Therefore, sludge composed of fine solid matter can be efficiently recovered by the sludge wiper 13, and treated water with a high purification level can be taken out through the discharge pipe 32.

また、整流部8は、下端先鋭の円錐状に形成したことより、汚水案内管5の上開口部から流出した気泡が付着した微細固形物をまんべんなく放射状に整流させ液面Hに浮上させることができるので、微細固形物からの気泡の分離を安定的に防止することができる。   In addition, since the straightening unit 8 is formed in a conical shape at the lower end point, it is possible to uniformly straighten the fine solid matter to which the air bubbles flowing out from the upper opening of the dirty water guide pipe 5 adhere to rise to the liquid level H. Since it can be done, the separation of air bubbles from the fine solid can be stably prevented.

また、汚水案内管5は、上端に上方に拡開した鍔6を形成したことより、汚水案内管5の上開口部から流出した気泡が付着した微細固形物を上方の整流部8に向けてまんべんなく確実に流出させることができるので、微細固形物からの気泡の分離を更に安定的に防止することができる。   Further, since the dirty water guide pipe 5 is formed with the weir 6 expanded upward at the upper end, the fine solid with bubbles attached from the upper opening of the dirty water guide pipe 5 is directed toward the straightening part 8 above. Since the liquid can be surely drained evenly, it is possible to more stably prevent the separation of air bubbles from the fine solid.

更に、汚泥ワイパー13は、処理タンク2の鉛直中心軸Gを起点として水平方向に回動すると共に、整流部8は、汚泥ワイパー13の下方において同軸に連設したことより、汚泥ワイパー13の回動を阻害することなく整流部8を処理タンク2の上部に垂設でき、しかも、整流部8を鉛直中心軸Gに水平断面視同心円形状とすれば、たとえ整流部8が汚泥ワイパー13と同軸で回動しても整流部8により処理タンク2内の汚水を掻き乱すことなく整流作用を発揮させることができる。   Furthermore, the sludge wiper 13 rotates in the horizontal direction starting from the vertical central axis G of the processing tank 2, and the rectifying unit 8 is coaxially connected below the sludge wiper 13, so that the sludge wiper 13 rotates. If the flow straightening unit 8 can be provided above the processing tank 2 without blocking the movement, and if the flow straightening unit 8 has a concentric shape with a vertical central axis G in horizontal sectional view, then the flow straightening unit 8 is coaxial with the sludge wiper 13 Even if it rotates, the rectification | straightening function can be exhibited by the rectification | straightening part 8, without disturbing the waste water in the processing tank 2. As shown in FIG.

しかも、エアーポンプ49は、マイクロバブル発生装置49aであることより、ほとんどすべての微細固形物に極小の気泡を付着させることができるので、浄化レベルの極めて高い処理水を取り出すことが可能となる。   In addition, since the air pump 49 is a micro-bubble generating device 49a, it is possible to adhere minimal air bubbles to almost all the fine solid substances, so it is possible to take out treated water having a very high purification level.

以上、本発明の本実施形態に係る微細固形物分離装置の好ましい実施形態について説明したが、本発明は特定の実施形態に限定されるものではなく、種々の変形・変更が可能である。   As mentioned above, although the preferable embodiment of the fine-solids separation apparatus based on this embodiment of this invention was described, this invention is not limited to a specific embodiment, A various deformation | transformation and change are possible.

H 液面
S 浄化した液体(処理水)
W 汚水
G 鉛直中心軸
1 微細固形物分離装置
2 処理タンク
3 汚水導入管
5 汚水案内管
6 鍔
8 整流部
13 汚泥ワイパー
23 汚泥シューター
32 排出管
49 エアーポンプ
49a マイクロバブル発生装置
H Liquid Level S Purified Liquid (Treated Water)
W Sewage G Vertical central axis 1 Fine solid separation device 2 Treatment tank 3 Sewage introduction pipe 5 Sewage guide pipe 6 鍔 8 Rectification section 13 Sludge wiper 23 Sludge shooter 32 Discharge pipe 49 Air pump 49a Micro bubble generator

Claims (3)

汚水を固形物と液体に分離する処理タンクかならる浄化装置であって、
外部から処理タンク内に汚水を導入する汚水導入管と、
前記汚水導入管と前記処理タンク内で連通する上下開口の汚水案内管と、
前記汚水案内管の上方に所定の間隙で配設され前記汚水案内管の上開口部から流出した前記汚水を整流する整流部と、
前記整流部の上方に所定の間隙で配設され浮上した前記汚水の微細固形物をかき集める汚泥ワイパーと、
前記汚泥ワイパーでかき集められた前記微細固形物を収容して前記処理タンク外へ排出する汚泥シューターと、
前記処理タンク内から浄化した液体を排出する排出管と、
前記排出管と連通し前記処理タンクの液面の高さを微調整する水位調整部を有する水位調整容器と、
前記汚水に気泡を混入するために前記処理タンク外において前記汚水導入管に連設したマイクロバブル発生装置と、で構成し、
前記汚水導入管は、前記汚水案内管の内部に貫通して前記汚水案内管の前記内部において開口端が鉛直上方となるよう真上に湾曲して屈曲し、前記汚水案内管は、上端に上方に拡開した鍔を形成し、
前記汚泥ワイパーは、前記処理タンクの鉛直中心軸を起点として水平方向に回動すると共に、前記整流部は、前記汚泥ワイパーの下方において同軸に連設し、
前記整流部は、円錐状の整流下面と円柱状の整流側面からなる下端先鋭のコマ型に形成し
前記水位調整部は、前記排出管の上端部を前記水位調整容器の底部から突出するよう形成し、突出した部位の周側面を螺刻して円筒状の雄ネジ管とし、これに内側面を螺刻した円筒状の雌ネジ管を螺合可能に構成したことを特徴とする微細固形物分離装置。
It is a purifier that is a processing tank that separates sewage into solids and liquid,
Sewage introduction pipe for introducing sewage into the treatment tank from the outside,
Upper and lower opening dirty water guide pipes communicating with the dirty water introduction pipe in the treatment tank;
A straightening unit disposed above the dirty water guide pipe with a predetermined gap and straightening the dirty water flowing out from the upper opening of the dirty water guide pipe;
A sludge wiper which is disposed at a predetermined gap above the flow straightening unit and which collects fine solid matter of the floated water;
A sludge shooter that contains the fine solid matter collected by the sludge wiper and discharges it out of the treatment tank;
A discharge pipe for discharging the purified liquid from the processing tank;
A water level adjusting container having a water level adjusting portion in communication with the discharge pipe for finely adjusting the level of the liquid surface of the processing tank;
And a micro-bubble generator connected to the sewage introduction pipe outside the treatment tank for mixing air bubbles into the sewage.
The dirty water introduction pipe penetrates the inside of the dirty water guide pipe, and is bent upward and bent so that the open end is vertically upward inside the dirty water guide pipe, and the dirty water guide pipe is upward at the upper end Form an expanded cocoon,
The sludge wiper rotates in the horizontal direction starting from the vertical central axis of the processing tank, and the straightening unit is coaxially connected below the sludge wiper,
The straightening unit is formed in a tip-shaped top-piece-shaped, lower end including a conical straight lower surface and a cylindrical straight side surface .
The water level adjusting portion is formed such that the upper end portion of the discharge pipe protrudes from the bottom portion of the water level adjusting container, and the peripheral side surface of the protruding portion is threaded to form a cylindrical male screw pipe. What is claimed is: 1. A fine solid separation device characterized in that a screwed cylindrical female screw tube is configured to be screwable .
前記処理タンクの底部には、沈殿した汚泥を前記処理タンク外に排出する沈殿物排出管を備え、前記沈殿物排出管は、前記処理タンクの底部近傍から水平方向に伸延して上方に立設した前記沈殿物排出管の中途部に空気を送り込む空気導入管を連通連接したことを特徴とする請求項1に記載の微細固形物分離装置。 The bottom of the processing tank is provided with a sediment discharge pipe for discharging the deposited sludge to the outside of the processing tank, and the sediment discharge pipe extends horizontally from the vicinity of the bottom of the processing tank and stands upward 2. The fine solids separation device according to claim 1, wherein an air introduction pipe for feeding air to a middle portion of the sediment discharge pipe is connected in communication . 前記整流部は、前記整流側面の中途部に前記整流側面を囲繞する円環状の気泡破壊部を形成したことを特徴とする請求項2に記載の微細固形物分離装置。
The minute solid separation device according to claim 2, wherein the straightening unit has an annular bubble breaking portion surrounding the straight side surface at a middle portion of the straight side surface.
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