JP6208041B2 - Solid-liquid separator - Google Patents

Solid-liquid separator Download PDF

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JP6208041B2
JP6208041B2 JP2014033579A JP2014033579A JP6208041B2 JP 6208041 B2 JP6208041 B2 JP 6208041B2 JP 2014033579 A JP2014033579 A JP 2014033579A JP 2014033579 A JP2014033579 A JP 2014033579A JP 6208041 B2 JP6208041 B2 JP 6208041B2
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JP2015157256A (en
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達也 千賀
達也 千賀
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Tsurumi Manufacturing Co Ltd
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Description

本発明は例えば、下水処理場、し尿処理場、畜産農業、食料品製造業、化学工業などの汚泥を含む排水の処理施設において発生する、液体中に含まれている汚泥の固形物、特に懸濁固形物(SS)を分離した固分と液分を各別に取り出すための装置に関するものである。   The present invention includes, for example, sludge solids contained in liquids, particularly suspensions generated in wastewater treatment facilities including sludge such as sewage treatment plants, human waste treatment plants, livestock agriculture, food manufacturing industries, and chemical industries. The present invention relates to an apparatus for separately taking out a solid content and a liquid content from which a turbid solid (SS) is separated.

現在、下水処理場、し尿処理場、畜産農業、食料品製造業、化学工業などの排水の処理場において発生する汚泥を含む排水即ち懸濁汚水は環境破壊の問題から、そのままでは排水することが出来ないことは周知のことであり、懸濁汚水に含まれる懸濁固形物(SS)を可能な限り除去した状態で処理することが課題となっている。   Currently, wastewater containing sludge generated in wastewater treatment plants such as sewage treatment plants, human waste treatment plants, livestock farming, food manufacturing industries, and chemical industries, ie suspended sewage, can be drained as it is due to environmental damage. What cannot be done is a well-known thing, and it has become a subject to process in the state which removed the suspended solid (SS) contained in suspended sewage as much as possible.

そのために、大と小および間隙保持用の直径の異なる各濾片を一組として、それら複数組を回転軸に挿嵌固定された積層濾体を排出方向へ向かって等間隔に複数配列させて、該積層濾体を同一方向に回転させて、相隣接する積層濾体の一方における送り濾片の外周縁が他方の積層濾体における間隙濾片の外周縁に接近した態様とし、この積層濾体の、送り濾片は前後に隣接する間隙濾片と向き合うように組み合わされており、各積層濾体の回転により、送り濾片は間隙濾片の細い隙間に食い込む形で回転することにより、濾過面の目詰りを防止している懸濁液を濾過する装置は公知である(例えば、特許文献1参照)。   For this purpose, a set of large and small filter pieces with different diameters for holding gaps is used as a set, and a plurality of stacked filter bodies in which the plurality of sets are inserted and fixed to the rotation shaft are arranged at equal intervals in the discharge direction. The laminated filter body is rotated in the same direction so that the outer peripheral edge of the feed filter piece in one of the adjacent laminated filter bodies approaches the outer peripheral edge of the gap filter piece in the other laminated filter body. The feed filter piece of the body is combined so as to face the front and rear adjacent gap filter pieces, and by rotating each laminated filter body, the feed filter piece rotates in a form that bites into the narrow gap of the gap filter piece, An apparatus for filtering a suspension that prevents clogging of the filtration surface is known (for example, see Patent Document 1).

また、別に背景技術として、ボルトとナットを用いてスペーサを取付けた固定リングを複数枚積層させて液体ガイド溝を構成し、その内周に遊動リングを配置し、スクリューコンベアを駆動させて遊動リングを偏心回転させることで汚泥水を固形分と水分に分離を行う装置も公知である(例えば、特許文献2参照)。   In addition, as another background art, a plurality of fixing rings with spacers attached using bolts and nuts are stacked to form a liquid guide groove, an idle ring is arranged on the inner periphery, and the screw conveyor is driven to idle ring. An apparatus that separates sludge water into solid content and moisture by rotating the shaft eccentrically is also known (see, for example, Patent Document 2).

特開平2−31807号公報JP-A-2-31807 特開平5−228695号公報JP-A-5-228695

しかしながら、前記特許文献1の懸濁液を濾過する装置においては、小径円板状濾片の細い隙間は食い込む形で回転する大径円板状濾片の厚さより僅かでも広くならなければならないが、大径円板状濾片が回転軸に完全固定されており同一軌道を回転するため、本来掻きださなければならない濾過脱水物のケーキが細い隙間で大径円板状濾片の厚みを除く領域が付着固形化し、濾過面の目詰りが発生することで懸濁液の固液分離ができなくなり、また、大・小径円板状濾片は0.2mm〜1mm程度の極く薄いものであるので、そのプレス加工やレーザー加工の際に加工歪や熱歪が生じるため、歪取りが必要であり、円板状濾片の径を大きくすると、歪の影響が顕著となり相隣接する小径円板状濾片の細かい隙間を構成する大径円板状濾片の両側面が接触干渉されて、積層濾体の回転軸トルクが増大することに加えて、大・小円板状濾片の摩耗が早まることとなり、更に、大径および小径円板状濾片を積層固定することで濾過溝を形成していることから、濾過溝の幅と位置の精度は両濾片の厚みと平坦度の精度および積層組立時の締付加減等に大きく影響されるので、組立時には細心の注意と調整が必要とされることから、組立には多くの労力と熟練が必要とされるという欠点があった。   However, in the apparatus for filtering the suspension of Patent Document 1, the narrow gaps of the small-diameter disk-shaped filter pieces must be slightly larger than the thickness of the large-diameter disk-shaped filter pieces that rotate in a biting manner. Since the large-diameter disc-shaped filter piece is completely fixed to the rotating shaft and rotates on the same track, the cake of the filtered dehydrated product that has to be scraped off naturally increases the thickness of the large-diameter disc-shaped filter piece through a narrow gap. The area to be removed is solidified and the filtration surface becomes clogged, making it impossible to separate the suspension from solid and liquid. Large and small-diameter disk-shaped filter pieces are extremely thin, about 0.2 mm to 1 mm. Therefore, since processing strain and thermal strain occur during the press processing and laser processing, it is necessary to remove the strain, and when the diameter of the disk-shaped filter piece is increased, the effect of strain becomes significant and the adjacent small diameter Of large-diameter disk-shaped filter pieces that form fine gaps in disk-shaped filter pieces In addition to increasing the rotating shaft torque of the laminated filter body due to contact interference on the side surfaces, wear of large and small disk-shaped filter pieces is accelerated, and large-diameter and small-diameter disk-shaped filter pieces are laminated. Since the filtration groove is formed by fixing, the accuracy of the width and position of the filtration groove is greatly affected by the thickness and flatness accuracy of both filter pieces and the reduction of tightening during stacking assembly. Since careful attention and adjustment are sometimes required, assembly has the drawback of requiring a lot of labor and skill.

また、特許文献2記載の固液分離装置においては、スクリューコンベアが汚泥水を流入口から排出口まで押し出すように分離を行う構成であるため、汚泥水の流入口側のスペーサが磨耗しやすく、都度部品交換を要するという欠点があった。   Further, in the solid-liquid separation device described in Patent Document 2, since the screw conveyor is configured to separate the sludge water so as to push the sludge water from the inlet to the outlet, the spacer on the inlet side of the sludge water is likely to wear, There was a drawback that parts had to be replaced each time.

そこで、本発明は前記問題点を鑑み、樹脂成型時に濾片に生じる歪みを抑制し、各濾片の組み立てを容易にすることが可能な固液分離装置を提供することを目的とする。   In view of the above problems, an object of the present invention is to provide a solid-liquid separation device that can suppress distortion generated in a filter piece during resin molding and facilitate the assembly of each filter piece.

本発明の請求項1に係る発明では、原液供給口と固分排出口および濾液排水口を有する懸濁汚水に含まれる固分と液分に分離濾過する固液分離装置において、各濾片間を所要間隔の濾過溝に保持するための間隔保持具を該濾片の表裏面に凸子として一体的に樹脂成型し凸子濾片を積層状に定着させ、該凸子濾片の凸子端面の凸設高さが一方の面を他方の面より高く構成するか、または表裏両面とも同一の高さに構成するとともに、前記各濾過溝内に揺動可能に濾過プレートを遊嵌して形成された各細隙を濾水流出溝として形成された積層濾体によって、懸濁汚水に含まれる懸濁微粒子の固分回収排出と懸濁微粒子の少ない液分排水とに効率よく分離濾過するように構成されていることを最も主要な特徴とする。 In the invention according to claim 1 of the present invention, in a solid-liquid separation device that separates and filters solid liquid and liquid contained in suspended sewage having a raw liquid supply port, a solid content discharge port, and a filtrate drain port, the integrally by fixing each Totsuko濾片that resin molding in layers apart retainer for retaining the filtration grooves of predetermined spacing as Totsuko on the front and back surfaces of the filtrate pieces of該凸Ko濾片Convex height of convex end surface is configured so that one surface is higher than the other surface, or both the front and back surfaces are the same height, and the filtration plate is loosely fitted in each filtration groove The separated filter formed as a drainage groove is used to efficiently separate the suspended solids contained in the suspended sewage into solids collected and discharged and the liquid wastewater containing less suspended particulates. The main feature is that it is configured to be filtered.

本発明の請求項1に記載の固液分離装置において、本発明の請求項2に係る発明は、前記凸子濾片の表裏面三箇所以上凸子を一体的に樹脂成型して凸設するよう構成されている。 In the solid-liquid separating apparatus according to claim 1 of the present invention, the invention of claim 2 of the present invention, the Totsuko than three places of front and back surfaces of the Totsuko濾片be integrally resin-molded convex It is configured to install .

本発明の請求項2に記載の固液分離装置において、本発明の請求項3に係る発明は、前記凸子濾片の凸子端面を環状に凸設するよう、表裏両面または一方の面の凸子端面の中央部に窪みが形成されている。   In the solid-liquid separation device according to claim 2 of the present invention, the invention according to claim 3 of the present invention is such that both the front and back surfaces or one surface of the convex filter piece are provided so as to project annularly. A depression is formed at the center of the end face of the convex.

本発明の請求項1ないし3のいずれか一項に記載の固液分離装置において、本発明の請求項4に係る発明は、前記濾片と一体成型された凸子よって各濾片間に揺動可能に遊嵌収容される小径濾過プレートと、該小径濾過プレートの外縁と対向配設される他方積層濾体の濾過溝の外縁より突出する揺動可能に濾過溝内に遊嵌収容された大径濾過プレートの2種類の濾過プレートと、前記凸子濾片、隣接対向する他方積層濾体の積層順位構成により対向する互いの濾過プレートの外縁同士が干渉しない積層順位で積層された、複数の積層濾体が懸濁汚水を受入れて固分と液分に分離濾過しながら固分排出口に移送するように、各積層濾体の中心に設けられた回転軸により駆動回転させながら、上下2段に分けて隣接対向配列された各積層濾体により、効率よく分離濾過するように構成されている。 In the solid-liquid separation device according to any one of claims 1 to 3 of the present invention, the invention according to claim 4 of the present invention, the濾片integrally molded Totsuko Thus between each濾片A small-diameter filtration plate that is swingably fitted and accommodated, and is loosely fitted and accommodated in the filter groove so as to swing from the outer edge of the filtration groove of the other laminated filter body disposed opposite to the outer edge of the small-diameter filtration plate. The two filter plates of the large-diameter filtration plate and the convex filter pieces were stacked in a stacking order so that the outer edges of the opposing filter plates do not interfere with each other due to the stacking order configuration of the other opposing filter body. While being rotated by a rotating shaft provided at the center of each laminated filter body, a plurality of laminated filter bodies receive suspended sewage and transfer it to a solids outlet while separating and filtering into solid and liquid components. , Each laminated filter body divided into two upper and lower stages and arranged adjacent to each other More, and is configured to efficiently separated filtration.

本発明の請求項4に記載の固液分離装置において、本発明の請求項5に係る発明は、前記積層濾体において、凸子濾片と大径濾過プレートには濾液孔および小径濾過プレートには濾液切欠孔をそれぞれ同心状に穿設し、該濾液孔および濾液切欠孔は積層後の上記両積層濾体内に濾液路を形成し、該濾液路の送液終端開口部は前記固液分離装置側壁の外側に付設された濾液室内に導通され、該濾液室下壁に濾液室排水口を開設するように構成されている。   In the solid-liquid separation device according to claim 4 of the present invention, the invention according to claim 5 of the present invention is that in the laminated filter body, the convex filter pieces and the large-diameter filtration plate include the filtrate holes and the small-diameter filtration plate. The filtrate notch holes are concentrically drilled, and the filtrate hole and the filtrate notch hole form a filtrate path in both the laminated filter bodies after the lamination, and the liquid-feed end opening of the filtrate path is the solid-liquid separation Conduction is made in a filtrate chamber attached to the outside of the apparatus side wall, and a filtrate chamber drainage port is opened on the lower wall of the filtrate chamber.

本発明の請求項1または2のいずれか一項に記載の固液分離装置において、本発明の請求項6に係る発明は、前記積層濾体の始端開口部を懸濁汚水の原液供給口とし、終端開口部を固分排出口として、スクリューブレードの外径が濾過プレートの内径よりも大きく凸子濾片または濾片の内径より小さく形成されたスクリューコンベアを前記積層濾体の中心孔に嵌装するように構成されている。   In the solid-liquid separator according to any one of claims 1 and 2, the invention according to claim 6 of the present invention is characterized in that the starting end opening of the laminated filter body is a stock solution supply port of suspended sewage. A screw conveyor having a terminal opening as a solid outlet and an outer diameter of the screw blade larger than an inner diameter of the filter plate and smaller than an inner diameter of the filter piece is fitted into the center hole of the laminated filter body. It is configured to wear.

本発明の請求項1の発明に係る固液分離装置によれば、固液分離装置において、各濾片間を所要間隔の濾過溝に保持するための間隔保持具を該濾片の表裏面に凸子として一体的に樹脂成型することで、濾片の金型を調整するのみで精度よく積層可能な濾片を構成することが可能となAccording to the solid-liquid separation device of the first aspect of the present invention, in the solid-liquid separation device, the interval holders for holding the gaps between the filter pieces in the filtration grooves having the required intervals are provided on the front and back surfaces of the filter pieces. by integrally resin-molded as Totsuko, that Do is possible to form accurately stackable濾片only adjusting the mold濾片.

また、本発明の請求項1に基づいた請求項2の発明に係る固液分離装置によれば、前記濾片の表裏面の三箇所以上に凸子を一体的に樹脂成型した濾片を凸子濾片として構成されているので、多数枚の濾片を安定して積層可能となるとともに、凸子を形成することで、他方の凸子濾片との当接面積を小さくすることが可能となり、樹脂成型時における冷却時間の差異によって凸子濾片の各部位が収縮することにより生じる歪みを凸子で吸収し、管理する事ができるので、凸子を形成することで濾片全体の歪みを抑制する事が可能となり、さらに、凸子濾片の凸子端面の凸設高さが表裏両面とも同一に構成されているならば、凸子の高さが均一化されることで樹脂成型時における冷却時間が凸子の表裏両面とも同じとなり、冷却時に濾片が収縮することにより生じる応力により表面側の凸子が曲がろうとするが、同様に裏面側の凸子も曲がろうとするので、凸子の表面、裏面で互いに曲がりが相殺され、濾片に生じる歪みをより抑制する事が可能となり、かつ組み立て時において、凸子濾片の表面、裏面の向きに関係無く回転軸へ挿嵌することが可能となり、例えば固液分離装置を駆動させる事で凸子濾片の表面側の凸子が磨耗したとしても、凸子濾片を裏返して裏面の凸子を利用する事が可能となる効果を有している。   Further, according to the solid-liquid separation device according to the second aspect of the present invention based on the first aspect of the present invention, the filter pieces formed by integrally resin-molding the protrusions on the front and back surfaces of the filter pieces are convex. Since it is configured as a sub filter piece, it is possible to stably stack a large number of filter pieces, and by forming a convex, it is possible to reduce the contact area with the other convex filter piece The distortion generated by the contraction of each part of the convex filter piece due to the difference in the cooling time during resin molding can be absorbed and managed by the convex part, so by forming the convex part, the entire filter piece It is possible to suppress distortion, and if the convex height of the convex end face of the convex filter piece is the same on both the front and back surfaces, the height of the convex can be made uniform and the resin can be made uniform. The cooling time at the time of molding is the same on both the front and back sides of the convex, and the filter piece shrinks during cooling The convex on the front side tends to bend due to the stress caused by the stress, but the convex on the back side also tends to bend. It is possible to further suppress and at the time of assembly, it is possible to insert into the rotating shaft regardless of the direction of the front and back surfaces of the convex filter piece, for example, by driving the solid-liquid separation device Even if the protrusion on the front surface side of the piece is worn, it has an effect that it is possible to turn the protrusion filter piece over and use the protrusion on the back surface.

さらに、本発明の請求項2に基づいた請求項3の発明に係る固液分離装置によれば、凸子濾片の凸子端面を環状に凸設するよう、表裏両面または一方の面の凸子端面の中央部に窪みが形成されているので、凸子の当接面積が小さくなり、樹脂成型時において窪みの内側と外側を均等に冷却されるので、凸子部分も含め凸子濾片全体の冷却時間が均一化され、凸子濾片の各部位の冷却時間の差異によって生じる歪みの発生をより効果的に防止することが可能となる効果を有している。   Furthermore, according to the solid-liquid separation device according to the third aspect of the present invention based on the second aspect of the present invention, both the front and back surfaces or one of the convex surfaces is provided so as to project the convex end surface of the convex filter piece in an annular shape. Since the depression is formed in the center of the end face, the contact area of the protrusion is reduced, and the inside and outside of the depression are cooled evenly during resin molding. The entire cooling time is made uniform, and it is possible to more effectively prevent the occurrence of distortion caused by the difference in cooling time of each part of the convex filter piece.

また、本発明の請求項1ないし3のいずれか一項に基づいた請求項4の発明に係る固液分離装置によれば、前記濾片と一体成型された凸子或いは濾片間の回転軸に嵌装された別体のスペーサによって各濾片間に揺動可能に遊嵌収容される小径濾過プレートと、該小径濾過プレートの外縁と対向配設される他方積層濾体の濾過溝の外縁より突出する揺動可能に濾過溝内に遊嵌収容された大径濾過プレートの2種類の濾過プレートと、前記凸子濾片或いはスペーサを介装させた各濾片を、隣接対向する他方積層濾体の積層順位構成により対向する互いの濾過プレートの外縁同士が干渉しない積層順位で積層された、複数の積層濾体が懸濁汚水を受入れて固分と液分に分離濾過しながら固分排出口に移送するように、各積層濾体の中心に設けられた回転軸により駆動回転させながら、上下2段に分けて隣接対向配列された各積層濾体により、効率よく分離濾過するように構成されているので、凸子濾片の固液分離装置を駆動させることで凸子濾片の交換が必要となった場合でも、凸子濾片に形成された凸子の高さが凸子濾片の表面、裏面ともに同一であれば表裏の向きに関係なく凸子濾片の交換が容易に可能であり、作業性を向上させることが可能となる。   Further, according to the solid-liquid separation device according to the invention of claim 4 based on any one of claims 1 to 3 of the present invention, a convex element integrally formed with the filter piece or a rotating shaft between the filter pieces. A small-diameter filtration plate that is swingably fitted and accommodated between the filter pieces by a separate spacer fitted to the filter, and an outer edge of the filtration groove of the other laminated filter body disposed opposite to the outer edge of the small-diameter filtration plate Two types of filtration plates, a large-diameter filtration plate that is loosely accommodated in the filtration groove so as to be able to swing further, and each of the filter pieces interposing the convex filter pieces or spacers are adjacent to each other. A plurality of laminated filter bodies, which are stacked in a stacking order in which the outer edges of the opposing filter plates do not interfere with each other due to the stacking order configuration of the filter bodies, receive suspended sewage and separate the solids and liquids while filtering them. Provided at the center of each laminated filter body to be transferred to the discharge port Since it is configured to efficiently separate and filter by the laminated filter bodies that are adjacently arranged in two separate stages while being driven and rotated by the rotating shaft, the solid-liquid separation device for the convex filter pieces is driven. Even if it is necessary to replace the convex filter piece, if the height of the convex element formed on the convex filter piece is the same on both the front and back surfaces, the convex part will be The subfilter piece can be easily replaced, and the workability can be improved.

本発明の請求項4に基づいた請求項5の発明に係る固液分離装置によれば、凸子濾片と大径濾過プレートには濾液孔および小径濾過プレートには濾液切欠孔をそれぞれ同心状に穿設し、該濾液孔および濾液切欠孔は積層後の上記両積層濾体内に濾液路を形成し、該濾液路の送液終端開口部は前記固液分離装置側壁の外側に付設された濾液室内に導通され、該濾液室下壁に濾液室排水口を開設するように構成されているので、濾液路のない積層濾体の場合よりも、濾液路経由の濾液室下壁の濾液室排水口からの排水が加わることから、濾過溝内で揺動回転する大径および小径濾過プレートの濾液分離能力が向上されることで、濾液分離機能の向上と含水率の低い濾過脱水物のケーキが回収し得るという効果を有している。   According to the solid-liquid separator according to the invention of claim 5 based on claim 4 of the present invention, the convex filter pieces and the large-diameter filtration plate have concentric filtrate holes, and the small-diameter filter plate has concentric filtrate notches. The filtrate hole and the filtrate notch hole form a filtrate path in the two laminated filter bodies after lamination, and a liquid feed terminal opening of the filtrate path is provided outside the side wall of the solid-liquid separator. Since it is connected to the filtrate chamber and is configured to open a filtrate chamber drain on the lower wall of the filtrate chamber, the filtrate chamber on the lower wall of the filtrate chamber via the filtrate path is more than in the case of a laminated filter body without a filtrate path. Since drainage from the drainage port is added, the filtrate separation capacity of the large and small diameter filtration plates that swing and rotate in the filtration groove is improved. Has the effect that can be recovered.

請求項1または2のいずれか一項に基づいた請求項6の発明に係る固液分離装置によれば、前記積層濾体の始端開口部を懸濁汚水の原液供給口とし、終端開口部を固分排出口として、スクリューブレードの外径が濾過プレートの内径よりも大きく凸子濾片の内径より小さく形成されたスクリューコンベアを前記積層濾体の中心孔に嵌装するように構成されているので、懸濁汚水は始端開口部から終端開口部へ押し出されることとなり、始端開口部側の凸子が非常に磨耗しやすくなるが、凸子濾片に形成された凸子の高さが凸子濾片の表面、裏面ともに同一に構成されているならば、凸子濾片を裏返して取り付けて使用することが可能となる。   According to the solid-liquid separator according to the invention of claim 6 based on any one of claims 1 and 2, the starting end opening of the laminated filter body is used as a stock solution supply port for suspended sewage, and the end opening is formed. As the solid content outlet, a screw conveyor formed so that the outer diameter of the screw blade is larger than the inner diameter of the filter plate and smaller than the inner diameter of the convex filter piece is fitted into the center hole of the laminated filter body. Therefore, suspended sewage is pushed out from the opening at the start end to the end opening, and the protrusion on the start end opening side is very easily worn, but the height of the protrusion formed on the protrusion filter piece is convex. If the front and back surfaces of the sub filter piece are configured identically, the convex filter piece can be mounted upside down and used.

本発明の実施例1における多重円板式の固液分離装置の縦断面図である。It is a longitudinal cross-sectional view of the multiple disk type solid-liquid separator in Example 1 of this invention. 図1のX−X線矢視方向の断面図である。It is sectional drawing of the XX arrow direction of FIG. 本発明の実施例1の積層濾体の、(a)は正面図、(b)はその縦断側面図である。(A) is a front view of the laminated filter body of Example 1 of this invention, (b) is the vertical side view. 本発明の実施例1の複数の積層濾体の、隣接態様を示した要部拡大側面図である。It is the principal part expanded side view which showed the adjacent aspect of the some laminated filter body of Example 1 of this invention. 本発明の実施例1の積層濾体を構成する大径濾過プレートの、(a)は正面図、(b)はその縦断側面図である。(A) is a front view of the large diameter filtration plate which comprises the laminated filter body of Example 1 of this invention, (b) is the vertical side view. 本発明の実施例1の積層濾体を構成する小径濾過プレートの、(a)は正面図、(b)はその縦断側面図である。BRIEF DESCRIPTION OF THE DRAWINGS (a) of the small diameter filtration plate which comprises the laminated filter body of Example 1 of this invention is a front view, (b) is the vertical side view. 本発明の実施例1の積層濾体を構成する凸子濾片の、(a)は正面図、(b)は(a)の縦断側面図で凸子の凸設高さを表裏面で同一にしたもので、(c)は(a)の縦断側面図で凸子の凸設高さを一方の面を他方の面より高く構成したものである。(A) is a front view of the convex filter piece constituting the laminated filter body of Example 1 of the present invention, (b) is a vertical side view of (a), and the convex height of the convex is the same on the front and back surfaces. (C) is a longitudinal side view of (a) in which the convex height of the convex is configured such that one surface is higher than the other surface. 本発明の実施例1の別実施形態における複数の積層濾体の、隣接態様を示した要部拡大側面図である。It is the principal part enlarged side view which showed the adjacent aspect of the some laminated filter body in another embodiment of Example 1 of this invention. 本発明の実施例1を基にした実施例2における固液分離装置の縦断面図である。It is a longitudinal cross-sectional view of the solid-liquid separator in Example 2 based on Example 1 of this invention. 図8のX−X線矢視方向の断面図である。It is sectional drawing of the XX arrow direction of FIG. 本発明の実施例2の積層濾体の、(a)は正面図、(b)はそのA−A断面図である。(A) of the laminated filter body of Example 2 of this invention is a front view, (b) is the AA sectional drawing. 本発明の実施例2の複数の積層濾体の、隣接態様を示した要部拡大側面図である。It is the principal part enlarged side view which showed the adjacent aspect of the some laminated filter body of Example 2 of this invention. 本発明の実施例2の積層濾体を構成する大径濾過プレートの、(a)は正面図、(b)はその縦断側面図である。(A) of the large diameter filtration plate which comprises the laminated filter body of Example 2 of this invention is a front view, (b) is the vertical side view. 本発明の実施例2の積層濾体を構成する小径濾過プレートの、(a)は正面図、(b)はその縦断側面図である。(A) of the small diameter filtration plate which comprises the laminated filter body of Example 2 of this invention is a front view, (b) is the vertical side view. 本発明の実施例2の積層濾体を構成する凸子濾片の、(a)は正面図、(b)は(a)のA−A断面図で凸子5tの凸設高さを表裏面で同一にしたもので、(c)は(a)のA−A断面図で凸子5Tの凸設高さを一方の面を他方の面より高く構成したものである。(A) of the convex filter piece which comprises the laminated filter body of Example 2 of this invention is a front view, (b) is AA sectional drawing of (a), and represents the convex installation height of the convex 5t. It is the same on the back surface, and (c) is a cross-sectional view taken along the line AA of (a), in which the height of the protrusion 5T is configured so that one surface is higher than the other surface. 本発明の実施例3におけるスクリュー式の固液分離装置の縦断側面図である。It is a vertical side view of the screw-type solid-liquid separator in Example 3 of this invention. 図16のX−X線矢視方向の拡大断面図である。It is an expanded sectional view of the XX arrow direction of FIG. 本発明の実施例3のスクリューコンベアの回転により濾過プレートが偏心回転する状態を例示した要部縦断側面図である。It is a principal part vertical side view which illustrated the state which a filtration plate rotates eccentrically by rotation of the screw conveyor of Example 3 of this invention. 本発明の実施例3の別実施形態におけるスクリューコンベアの回転により濾過プレートが偏心回転する状態を例示した要部縦断側面図である。It is a principal part longitudinal side view which illustrated the state which the filtration plate rotates eccentrically by rotation of the screw conveyor in another embodiment of Example 3 of this invention.

以下、本発明の懸濁汚水に含まれる固分と液分に分離濾過する固液分離装置において、各濾片間を所要間隔の濾過溝に保持するための間隔保持具を該濾片の表裏面に凸子として一体的に樹脂成型するか、或いは別体のスペーサとして各濾片間に介装させながら各濾片を積層状に定着させ、前記各濾過溝内に揺動可能に濾過プレートを遊嵌して形成された各細隙を濾水流出溝として形成された積層濾体によって、懸濁汚水に含まれる懸濁微粒子の固分回収排出と懸濁微粒子の少ない液分排水とに効率よく分離濾過するように構成される実施形態として、以下の如く本願発明の実施例に基づき、図面を参照して詳細に説明するが、この実施例の形態により本発明が限定されるものではない。   Hereinafter, in the solid-liquid separation device for separating and filtering the solid content and the liquid content contained in the suspended sewage of the present invention, an interval holder for holding the interval between the filter pieces in a filtration groove of a required interval is shown on the filter piece. The resin plate is integrally molded as a convex on the back surface, or each filter piece is fixed in a laminated manner while being interposed between the filter pieces as a separate spacer, and the filter plate is swingable in each filter groove With the laminated filter formed as a drainage groove, each slit formed by loosely fitting is used to collect and discharge suspended solids contained in the suspended sewage and to drain the liquid with less suspended particulates. Embodiments configured to efficiently separate and filter will be described in detail with reference to the drawings based on examples of the present invention as follows. However, the present invention is not limited to the embodiments. Absent.

本発明の実施例1の多重円板式の固液分離装置10Tについて、図1ないし図7を用いて説明すると、固液分離装置10Tの上部に懸濁汚水の原液を供給する原液供給口11を開設すると共に、下部には固液分離された濾液を固液分離装置10Tの外に排水する濾液排水口13を開設し、固液分離装置10Tの側面部には固液分離された固分の濾過脱水物のケーキを固液分離装置10Tの外に排出回収する固分排出口12が開設されており、前記原液供給口11と固分排出口12との間に、図1に示すように該固分排出口12の排出方向へ昇り勾配状の等間隔で上下2段に対向配列された複数の積層濾体1が配設されており、図3および図5ないし図7に示すように該積層濾体1を構成する複数の凸子濾片5の表裏面の3箇所以上に、中央に窪みRが設けられた凸子5tを一体的に樹脂成型し、該凸子5tは一方の面側の凸子を他方の面側の凸子より高く凸設することも可能であるが、望ましくは同じ高さで凸設され、凸子5t端面を当接させて濾過溝Sを形成させながら、各濾過溝S内を交互に大径濾過プレート2と小径濾過プレート3を軸方向に移動可能なように介装させ、凸子濾片5と、大径濾過プレート2あるいは小径濾過プレート3の細隙を濾水流出溝Gとし、具体的には円形の一部を平面状にカットしたDカットあるいはキー(図示せず)等の係止機能を有した、図2に示されるように固液分離装置10Tの正面側側壁10fおよび背面側側壁10rの外側に設けられた軸受9によって軸支されると共に、該正面側側壁10fの外側に設けられた駆動伝達具8(例えばウォームギヤー等)によって回転駆動される回転軸4と同調回転するように、該回転軸4の係止形状に嵌るように中心に軸孔が穿設された直径の異なる凸子濾片5、大径濾過プレート2、小径濾過プレート3を、例えば(ア)先ず回転軸4外周に凸子濾片5を挿入させて、(イ)次に先に挿入した凸子濾片5の凸子5tが大径濾過プレート2の凸子遊嵌孔2hに嵌るように該大径濾過プレート2を回転軸4に挿入させ、(ウ)次に凸子濾片5を回転軸4に挿入させて凸子濾片5の裏面側の凸子5t端面と、先の凸子濾片5の表面側の凸子5t端面同士を衝合させて濾過溝Sを形成し、先に挿入した大径濾過プレート2を保持し、(エ)次に小径濾過プレート3の凸子切欠孔3hを凸子5tに嵌るように該小径濾過プレート3を回転軸4に挿入させて、(オ)次の凸子濾片5を回転軸4に挿入させて凸子5t端面と、先の凸子5t端面同士を当接させて濾過溝Sを形成させて、小径濾過プレート3を保持し、上記(ア)から(オ)の手順を繰返すことで形成された複数の積層濾体1を、図4に示すように相隣接する積層濾体1の一方の積層濾体1における大径濾過プレート2の外周縁を他方の積層濾体1の濾過溝S内に突入させて他方の凸子濾片5の凸子5tと小径濾過プレート3の外周縁に接近した態様とし、処理液中に含まれる回収微粒子を効率よく回収するように固液分離装置10Tの供給側側壁10sと排出側側壁10dに付設されたシール部材7の要部外縁を、該固分排出口12側終端の上下2段と原液供給口11側始端の下段の積層濾体1の凸子濾片5外周縁に僅かな隙間を隔てて近接対向し、望ましくは該シール部材7の外縁部に摺動抵抗の少ないブラシを付設することでより一層シール機能を向上し得ると共に回転軸4のトルク増加を抑制し、大径濾過プレート2および小径濾過プレート3は、該濾過溝S内を軸方向に揺動しながら該回転軸4と同調回転できるように構成されている。   The multi-disc type solid-liquid separator 10T according to the first embodiment of the present invention will be described with reference to FIGS. 1 to 7. A stock solution supply port 11 for supplying a stock solution of suspended sewage to the upper part of the solid-liquid separator 10T is provided. At the bottom, a filtrate outlet 13 for draining the solid-liquid separated filtrate out of the solid-liquid separator 10T is opened at the bottom, and the solid content separated by solid-liquid separation is provided on the side surface of the solid-liquid separator 10T. A solid content outlet 12 for discharging and collecting the cake of the filtered dehydrated product outside the solid-liquid separator 10T is provided, and the gap between the stock solution supply port 11 and the solid content outlet 12 is as shown in FIG. A plurality of laminated filter bodies 1 arranged in two upper and lower stages at equal intervals rising in the upward direction toward the discharge direction of the solid content discharge port 12 are arranged, as shown in FIGS. 3 and 5 to 7. In three or more places on the front and back surfaces of the plurality of convex filter pieces 5 constituting the laminated filter body 1, It is possible to integrally mold the protrusions 5t provided with the ridges R, and the protrusions 5t can be provided so that the protrusions on one surface side are higher than the protrusions on the other surface side. Are protruded at the same height, and the large-diameter filtration plate 2 and the small-diameter filtration plate 3 can be moved in the axial direction alternately in the respective filtration grooves S while the end faces of the protrusions 5t are brought into contact with each other to form the filtration grooves S. D is obtained by interposing the convex filter piece 5 and the slit of the large-diameter filtration plate 2 or the small-diameter filtration plate 3 as a drainage drainage groove G, specifically, by cutting a circular portion into a flat shape. As shown in FIG. 2, the bearing 9 provided on the outside of the front side wall 10f and the rear side wall 10r of the solid-liquid separator 10T has a locking function such as a cut or key (not shown). And a drive transmission tool 8 (for example, provided outside the front side wall 10f) A convex filter piece 5 having a different diameter and having a shaft hole formed in the center so as to be fitted into the locking shape of the rotary shaft 4 so as to rotate synchronously with the rotary shaft 4 that is rotationally driven by a form gear, etc. For example, (a) First, the convex filter piece 5 is inserted into the outer periphery of the rotary shaft 4, and (b) the convex element 5t of the convex filter piece 5 inserted first is large. The large-diameter filtration plate 2 is inserted into the rotary shaft 4 so as to fit in the convex free-insertion holes 2h of the radial filter plate 2, and (c) next, the convex filter piece 5 is inserted into the rotary shaft 4 and the convex filter is inserted. The large-diameter filtration plate 2 inserted first is formed by abutting the end surface of the protrusion 5t on the back side of the piece 5 and the end surface of the protrusion 5t on the surface side of the protrusion piece 5 to form a filtration groove S. (D) Next, the small-diameter filtration plate 3 is inserted into the rotary shaft 4 so that the convex notch hole 3h of the small-diameter filtration plate 3 fits into the convex 5t. Then, (e) the next convex filter piece 5 is inserted into the rotary shaft 4, the end face of the convex 5t and the end face of the previous convex 5t are brought into contact with each other to form a filtration groove S, and the small diameter filtration plate 3, and a plurality of laminated filter bodies 1 formed by repeating the procedures (a) to (e) described above are used as one laminated filter body 1 of adjacent laminated filter bodies 1 as shown in FIG. In which the outer peripheral edge of the large-diameter filtration plate 2 is inserted into the filtration groove S of the other laminated filter body 1 so as to be close to the convex elements 5t of the other convex filter piece 5 and the outer peripheral edge of the small-diameter filtration plate 3; The outer edge of the main part of the seal member 7 attached to the supply side wall 10s and the discharge side wall 10d of the solid-liquid separator 10T so as to efficiently recover the collected fine particles contained in the processing liquid is connected to the solid content outlet 12 side. A slight gap at the outer periphery of the convex filter piece 5 of the laminated filter body 1 at the upper and lower ends of the end and the lower end of the starting end on the stock solution supply port 11 side A large-diameter filtration plate which is opposed to each other at a distance and desirably can be further improved by attaching a brush having a low sliding resistance to the outer edge portion of the seal member 7 while suppressing an increase in torque of the rotating shaft 4. 2 and the small-diameter filtration plate 3 are configured to be able to rotate in synchronization with the rotary shaft 4 while swinging in the filtration groove S in the axial direction.

また、図8に示すように凸子5tを凸子濾片5に一体的に樹脂成型するのではなく、例えば濾片6の次に別体のスペーサ6sを回転軸に挿入し、スペーサ6sの外周部分に位置するように大径濾過プレート2もしくは小径濾過プレート3を挿嵌して構成することも可能であり、また濾片6の平面状に複数個スペーサを取り付けて各濾片間を所要間隔の濾過溝に保持するための間隔保持具として構成することも可能である。   Further, as shown in FIG. 8, the convex element 5t is not integrally molded with the convex filter piece 5, but, for example, a separate spacer 6s is inserted into the rotating shaft next to the filter piece 6, and the spacer 6s The large-diameter filtration plate 2 or the small-diameter filtration plate 3 can be inserted and configured so as to be located in the outer peripheral portion, and a plurality of spacers are attached to the flat surface of the filter piece 6 so that each filter piece is required. It is also possible to configure as an interval holder for holding in the interval filtration grooves.

前記実施例1に基づいて、例えば図9ないし図15を用いて説明すると、前記積層濾体1において、図12ないし図14に示すように凸子濾片5と大径濾過プレート2には濾液孔15および小径濾過プレート3には濾液切欠孔16をそれぞれ同心状に穿設し、図9ないし図11に示すように該濾液孔15および濾液切欠孔16は積層後の上記積層濾体1内に濾液路14を形成し、該濾液路6の送液終端開口部は前記固液分離装置10Tの背面側側壁10rの外側に付設された濾液室17内に導通され、該濾液室17下壁に濾液室排水口18を開設するように構成されている。   For example, referring to FIGS. 9 to 15 based on the first embodiment, in the laminated filter body 1, as shown in FIGS. The hole 15 and the small-diameter filtration plate 3 are concentrically formed with a filtrate notch 16, respectively. As shown in FIGS. 9 to 11, the filtrate hole 15 and the filtrate notch 16 are formed in the laminated filter body 1 after lamination. The filtrate passage 14 is formed, and the liquid feed terminal opening of the filtrate passage 6 is electrically connected to the filtrate chamber 17 provided outside the back side wall 10r of the solid-liquid separator 10T, and the lower wall of the filtrate chamber 17 The filtrate chamber drain port 18 is opened.

本発明の実施例3のスクリュー式の固液分離装置10Sについて、図16ないし図18を用いて説明すると、原動機23によって駆動されることで回転するスクリューコンベア22が積層濾体1の中心孔21に嵌装されており、スクリューコンベア22の回転に伴い、外径が凸子濾片5・・5の内径より小さく、濾過プレート19・・19の内径より大きく構成されたスクリューブレード22Bが回転することで、凸子濾片5・・5の外側に形成された座部20・・20の表裏面の3箇所以上に、望ましくは同じ高さで一体的に樹脂成型されて凸設される凸子5t同士が当接されて構成される凸子濾片5・・5の各積層間に遊嵌される濾過プレート19・・19の内周部にスクリューブレード22Bの外縁が摺接して偏心回転させ、原液供給口11から筒状の積層濾体1内へ送り込まれた懸濁汚水の原液は、スクリューブレード22Bに沿って旋回しながら軸方向へ前進し、凸子濾片5・・5の各積層間と濾過プレート19・・19により形成された濾水流出溝Gから濾過された濾水を流出し、脱水されて含水比の低くなった固分は前方の吐出圧調整弁24を押し出すことで固分排出口12から順次排出されるよう構成されている。   A screw-type solid-liquid separator 10S according to the third embodiment of the present invention will be described with reference to FIGS. 16 to 18. A screw conveyor 22 that is rotated by being driven by a prime mover 23 has a central hole 21 of the laminated filter body 1. As the screw conveyor 22 rotates, the screw blade 22B having an outer diameter smaller than the inner diameter of the convex filter pieces 5 ·· 5 and larger than the inner diameter of the filter plates 19 ·· 19 rotates. Thus, the protrusions that are formed by resin molding integrally at the same height, preferably at three or more locations on the front and back surfaces of the seat portions 20... 20 formed outside the convex filter pieces 5. The outer edge of the screw blade 22B is in sliding contact with the inner peripheral portion of the filter plate 19,... 19 that is loosely fitted between the stacks of the convex filter pieces 5,. And supply the stock solution The stock solution of the suspended sewage sent from 11 into the cylindrical laminated filter body 1 advances in the axial direction while swirling along the screw blade 22B, and is filtered between the laminated layers of the convex filter pieces 5. The filtered water flows out from the filtered water outflow groove G formed by the plates 19... 19, and the solid content that has been dehydrated and has a low water content ratio is discharged by pushing the discharge pressure regulating valve 24 ahead. The outlet 12 is sequentially discharged.

また、図19に示すように凸子5tを凸子濾片5に一体的に樹脂成型するのではなく、例えば濾片6の座部20・・20にそれぞれ別体のスペーサ6sを設け、ボルト等によりスペーサ6sを固定することで、各濾片間を所要間隔の濾過溝に保持するための間隔保持具として構成することも可能である。   In addition, as shown in FIG. 19, the convex 5t is not integrally molded with the convex filter piece 5. Instead, for example, separate spacers 6s are provided on the seats 20. By fixing the spacer 6s by, for example, it is also possible to configure as an interval holder for holding between the filter pieces in a filtration groove having a required interval.

1 積層濾体
2 小径濾過プレート
3 大径濾過プレート
5 凸子濾片
5t 凸子
6 濾片
6s スペーサ
10T 固液分離装置(多重円板式)
10S 固液分離装置(スクリュー式)
11 原液供給口
12 固分排出口
13 濾液排水口
14 濾液路
15 濾液孔
16 濾液切欠孔
17 濾液室
18 濾液室排水口
19 濾過プレート
21 中心孔
22 スクリューコンベア
22B スクリューブレード
G 濾水流出溝
R 窪み
S 濾過溝
DESCRIPTION OF SYMBOLS 1 Laminated filter body 2 Small diameter filtration plate 3 Large diameter filtration plate 5 Convex filter piece 5t Convex piece 6 Filter piece 6s Spacer 10T Solid-liquid separator (Multiple disk type)
10S solid-liquid separator (screw type)
11 Stock solution supply port 12 Solid content discharge port 13 Filtrate drain port 14 Filtrate passage 15 Filtrate hole 16 Filtrate cutout hole 17 Filtrate chamber 18 Filtrate chamber drain port 19 Filtration plate 21 Center hole 22 Screw conveyor 22B Screw blade G Filtrate outflow groove R S Filtration groove

Claims (6)

原液供給口と固分排出口および濾液排水口を有し、懸濁汚水に含まれる固分と液分に分離濾過する固液分離装置において、各濾片間を所要間隔の濾過溝に保持するための間隔保持具を該濾片の表裏面に凸子として一体的に樹脂成型し凸子濾片を積層状に定着させ、該凸子濾片の凸子端面の凸設高さが一方の面を他方の面より高く構成するか、または表裏両面とも同一の高さに構成するとともに、前記各濾過溝内に揺動可能に濾過プレートを遊嵌して形成された各細隙を濾水流出溝として形成された積層濾体によって、懸濁汚水に含まれる懸濁微粒子の固分回収排出と懸濁微粒子の少ない液分排水とに効率よく分離濾過するように構成されていることを特徴とする固液分離装置。 In a solid-liquid separation device that has a stock solution supply port, a solid content discharge port, and a filtrate drainage port, and separates and filters the solid content and liquid content contained in suspended sewage, each filter piece is held in a filtration groove at a required interval integrally by fixing each Totsuko濾片that resin molding in layers as Totsuko the front and back surfaces of the filtrate pieces apart retainer for, convex設高of Totsuko end face of the Totsuko濾片 Each surface is configured to be higher than the other surface, or both the front and back surfaces are configured to have the same height, and each slit formed by loosely fitting a filter plate in each filter groove so as to be swingable. It is configured to efficiently separate and filter solid particulates collected and suspended in suspended sewage and liquid wastewater with few suspended particulates by means of a laminated filter formed as a drainage groove. A solid-liquid separator characterized by. 請求項1に記載の固液分離装置において、前記凸子濾片の表裏面の三箇所以上に凸子を一体的に樹脂成型して凸設するよう構成されていることを特徴とする固液分離装置。 The solid-liquid separator according to claim 1, wherein the protrusion is integrally formed by resin molding at three or more positions on the front and back surfaces of the protrusion filter piece. Separation device. 請求項2に記載の固液分離装置において、前記凸子濾片の凸子端面を環状に凸設するよう、表裏両面または一方の面の凸子端面の中央部に窪みが形成されていることを特徴とする固液分離装置。   3. The solid-liquid separation device according to claim 2, wherein a depression is formed in a center portion of the front and rear surfaces or one end of the convex end surface so as to project the convex end surface of the convex filter piece in an annular shape. A solid-liquid separator characterized by. 請求項1ないし3のいずれか一項に記載の固液分離装置において、前記濾片と一体成型された凸子よって各濾片間に揺動可能に遊嵌収容される小径濾過プレートと、該小径濾過プレートの外縁と対向配設される他方積層濾体の濾過溝の外縁より突出する揺動可能に濾過溝内に遊嵌収容された大径濾過プレートの2種類の濾過プレートと、前記凸子濾片、隣接対向する他方積層濾体の積層順位構成により対向する互いの濾過プレートの外縁同士が干渉しない積層順位で積層された、複数の積層濾体が懸濁汚水を受入れて固分と液分に分離濾過しながら固分排出口に移送するように、各積層濾体の中心に設けられた回転軸により駆動回転させながら、上下2段に分けて隣接対向配列された各積層濾体により、効率よく分離濾過するように構成されていることを特徴とする固液分離装置。 In the solid-liquid separation device according to any one of claims 1 to 3, a small diameter filtration plate swingably loosely fitted accommodated in the濾片integrally molded Totsuko Thus between each濾片, Two types of filtration plates, a large-diameter filtration plate that is loosely accommodated in the filtration groove so as to protrude from the outer edge of the filtration groove of the other laminated filter body disposed opposite to the outer edge of the small-diameter filtration plate, the Totsuko濾片, outer ends of the filtration plate of each other facing the lamination order structure of the adjacent opposite other laminated濾体are laminated in lamination order not to interfere, accept a plurality of stacked濾体is suspended sewage solid Each stack arranged adjacent to each other in two upper and lower stages while being driven and rotated by a rotating shaft provided at the center of each stacked filter body so as to be transferred to a solid content outlet while being separated and separated into a liquid and a liquid. Configured to efficiently separate and filter by filter Solid-liquid separator, characterized by being. 請求項4に記載の固液分離装置であって、前記積層濾体において、凸子濾片と大径濾過プレートには濾液孔および小径濾過プレートには濾液切欠孔をそれぞれ同心状に穿設し、該濾液孔および濾液切欠孔は積層後の上記両積層濾体内に濾液路を形成し、該濾液路の送液終端開口部は前記固液分離装置側壁の外側に付設された濾液室内に導通され、該濾液室下壁に濾液室排水口を開設するように構成したことを特徴とする固液分離装置。   5. The solid-liquid separator according to claim 4, wherein, in the laminated filter body, a convex hole and a large-diameter filtration plate are concentrically drilled with a filtrate hole and a small-diameter filtration plate with a concentric hole. The filtrate hole and the filtrate notch hole form a filtrate path in both the laminated filter bodies after lamination, and the liquid feed end opening of the filtrate path is connected to the filtrate chamber attached outside the side wall of the solid-liquid separator. A solid-liquid separator characterized in that a filtrate chamber drain port is opened in the lower wall of the filtrate chamber. 請求項1または2のいずれか一項に記載の固液分離装置において、記積層濾体の始端開口部を懸濁汚水の原液供給口とし、終端開口部を固分排出口として、スクリューブレードの外径が濾過プレートの内径よりも大きく凸子濾片または濾片の内径より小さく形成されたスクリューコンベアを前記積層濾体の中心孔に嵌装するように構成されていることを特徴とする固液分離装置。 In the solid-liquid separating apparatus according to any one of claims 1 or 2, the starting end opening of the front Symbol laminated濾体the solution feed port of the suspension sewage, the terminating opening as the solid fraction outlet, screw blades The outer diameter of the filter plate is larger than the inner diameter of the filter plate, and the screw conveyor formed smaller than the inner diameter of the filter piece or the filter piece is configured to be fitted into the center hole of the laminated filter body. Solid-liquid separator.
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CN108126394A (en) * 2018-01-03 2018-06-08 辜晓林 A kind of filter cylinder for livestock and poultry excrement solid-liquid seperator
CN114857864B (en) * 2022-04-29 2024-04-26 茅台学院 Garbage disposal device for environmental protection engineering

Family Cites Families (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0710440B2 (en) * 1992-02-21 1995-02-08 アムコン株式会社 Solid-liquid separation device
JP3734557B2 (en) * 1996-02-07 2006-01-11 株式会社鶴見製作所 Solid-liquid separator
JP4600343B2 (en) * 2006-04-24 2010-12-15 株式会社Ihi Multiple disk dehydrator
JP5854958B2 (en) * 2012-09-19 2016-02-09 株式会社鶴見製作所 Solid-liquid separator
KR101902612B1 (en) * 2012-10-11 2018-09-28 히사미쓰 세이야꾸 가부시키가이샤 Skin patch

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