JPH09276606A - Method of settling and filtering foul water and tank for settling and filtering sewage - Google Patents

Method of settling and filtering foul water and tank for settling and filtering sewage

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Publication number
JPH09276606A
JPH09276606A JP8941696A JP8941696A JPH09276606A JP H09276606 A JPH09276606 A JP H09276606A JP 8941696 A JP8941696 A JP 8941696A JP 8941696 A JP8941696 A JP 8941696A JP H09276606 A JPH09276606 A JP H09276606A
Authority
JP
Japan
Prior art keywords
settling
sewage
tank
filtration
sedimentation
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
JP8941696A
Other languages
Japanese (ja)
Inventor
Seiji Ishizuka
清治 石塚
Katashiro Satou
堅城 佐藤
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
SATO KATASHIRO
Original Assignee
SATO KATASHIRO
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by SATO KATASHIRO filed Critical SATO KATASHIRO
Priority to JP8941696A priority Critical patent/JPH09276606A/en
Publication of JPH09276606A publication Critical patent/JPH09276606A/en
Pending legal-status Critical Current

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Abstract

PROBLEM TO BE SOLVED: To demonstrate a high clarification performance with simple and small scaled equipment by introducing sewage into a settling and filtering tank, discharging sediment from a bottom and filtering sewage from which the sedi ment has been before being discharged as clarified water. SOLUTION: When foul water such as water from rivers and lakes is treated, the sewage is introduced into a settling and filtering tank 1 from an introducing hose 2 and flow rate is controlled by an introducing valve 2a. A precipitating and flocculating agent is added to the foul water so that flocculated sediment is formed from the sewage, and the sediment is allowed to settle and accumulate on a bottom of the settling and filtering tank 1. The sediment is discharged and separated through a sediment discharging outlet 3 and discharging timing and discharging quantity are controlled by opening and closing a discharging valve 3. Supernatant water after removal of the sediment is made to pass through a screen 4, 4' and filtered with the aid of flow of the foul water continuously introduced through the introducing hose 2 so that water from which fine solid polluting substances are removed is made to flow through a clarified water discharging outlet 5.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【発明の属する技術分野】この発明は、汚水に凝集沈降
剤を添加し、それに含まれる汚濁原因物質を沈降させ濾
過することにより汚水を浄化する場合に、汚水を一の沈
澱漕で連続的に浄化する沈澱濾過方法及びその沈澱濾過
漕に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to the addition of a flocculating settling agent to sewage, and when the sewage is purified by sedimenting and filtering the pollution-causing substances contained therein, the sewage can be continuously treated in one settling tank. TECHNICAL FIELD The present invention relates to a method for purifying a precipitate and a precipitate filtration tank.

【0002】[0002]

【従来の技術】汚水の浄化とは、河川若しくは湖水又は
土木現場の泥水等の汚濁原因物質となる泥土やヘドロ等
を汚水から分離することをいう。
2. Description of the Related Art Purifying sewage means separating mud, sludge, etc., which are pollutant-causing substances such as river or lake water or mud at civil engineering sites, from sewage.

【0003】従来は、凝集沈降剤を添加した汚水を沈澱
漕に一定時間静置し、汚濁原因物質が、その自重により
沈降するのを待って上水を排出し、その後沈澱漕の底に
残った沈殿物を回収していた。また、回収した沈殿物は
所定の処分場で焼却等の処分をするために、バキューム
車で吸引して処分場に運搬するか、遠心分離機で脱水後
トラック等で運搬していた。
Conventionally, sewage containing a flocculating settling agent is allowed to stand in a settling tank for a certain period of time, the pollutant is allowed to settle due to its own weight, and then the tap water is discharged, after which it remains at the bottom of the settling tank. The collected precipitate was collected. In addition, in order to dispose of the collected precipitates such as incineration at a predetermined disposal site, it was suctioned by a vacuum car and transported to the disposal site, or dehydrated by a centrifuge and then transported by a truck or the like.

【0004】[0004]

【発明が解決しようとする課題】しかし、凝集された汚
濁原因物質がその自重により沈澱するまでには長時間を
要し、また、沈澱漕の容積は長い滞留時間を確保するた
めに処理すべき汚水の量に応じて大きくする必要があっ
た。
However, it takes a long time for the flocculated pollutant to settle due to its own weight, and the volume of the settling tank should be treated to secure a long residence time. It had to be increased depending on the amount of dirty water.

【0005】さらにバキューム車による処理において
は、沈澱漕が最低2漕以上なければ連続した吸引をする
ことができず、汚水処理設備として広い場所が必要であ
った。一方、沈殿物の運搬に際しては、バキューム車で
の吸引は、沈殿物とともに多くの水を吸引し、その運搬
及び処理場における最終処分には無駄な労力及び費用が
費やされ、処理場での再処理効率をも低下させる原因と
もなっていた。
Further, in the treatment by the vacuum vehicle, continuous suction cannot be performed unless the sedimentation tank is at least two tanks, and a wide space is required as a wastewater treatment facility. On the other hand, when transporting the sediment, suction with a vacuum car sucks a large amount of water together with the sediment, and wasteful labor and cost are spent on the transportation and final disposal at the treatment site, resulting in It was also a cause of lowering the reprocessing efficiency.

【0006】[0006]

【課題を解決するための手段】本願は上記課題に鑑みて
なされたものであり、凝集沈降剤を添加した汚水を沈澱
濾過漕に連続的に流入し、凝集反応生成物である沈澱物
を沈澱濾過漕の底面から排出し、一方、残された上水
は、汚水の流入及び浄化水の流出によって生じる沈澱漕
内の流れによって生じる水圧により強制的に濾過するこ
とにより、汚水を浄化する沈澱濾過方法及び沈澱濾過漕
を提供するものである。本願発明によれば、一度の処理
工程を経て浄化され、沈澱漕から連続的に流出される浄
化水はそのまま河川等に戻すことも工場等で再利用する
こともできる。このように、簡易かつ小規模な設備であ
りながら高い浄化処理能力及び浄化処理能率を発揮し、
汚水に含まれた汚濁原因物質のみを回収するといった上
記課題を解決するものである。
The present application has been made in view of the above-mentioned problems. Sewage containing a flocculating and precipitating agent is continuously flowed into a settling filtration tank to precipitate a flocculating reaction product, that is, a precipitate. The waste water discharged from the bottom of the filter tank, while the remaining clean water is forcibly filtered by the water pressure generated by the flow in the precipitation tank caused by the inflow of sewage water and the outflow of purified water, thereby purifying the sewage. A method and a settling filter are provided. According to the present invention, the purified water that has been purified through a single treatment step and that is continuously discharged from the settling tank can be directly returned to a river or the like or reused in a factory or the like. In this way, despite its simple and small-scale equipment, it exhibits high purification treatment capacity and purification treatment efficiency,
It solves the above-mentioned problem of collecting only the pollutant contained in the sewage.

【0007】[0007]

【発明の実施の形態】本願に係る汚水の沈澱濾過方法及
びその沈澱濾過漕を図面に基づいて説明する。
BEST MODE FOR CARRYING OUT THE INVENTION A sediment filtration method and a sediment filtration tank thereof according to the present invention will be described with reference to the drawings.

【0008】図1は、本願発明にかかる沈澱濾過方法及
び沈澱濾過漕を示したものである。処理すべき汚水は、
流入ホース2から沈澱漕1に流入され、その流量は流入
バルブ2aによって調節される。汚水は、その汚濁原因
物質の種類及び処理量によって連続的若しくは断続的又
は多量に若しくは少量づつ流入される。
FIG. 1 shows a precipitation filtration method and a precipitation filtration tank according to the present invention. Sewage to be treated is
It flows into the settling tank 1 from the inflow hose 2, and the flow rate is adjusted by the inflow valve 2a. Sewage is introduced continuously or intermittently or in large amounts or in small amounts depending on the type and treated amount of the pollutant causing substance.

【0009】本願にかかる沈澱濾過方法及び沈澱濾過漕
は、この流入量によってもその汚水処理能力を調節でき
るが、具体的には、250Kg/分〜6000Kg/分
までの処理が可能である。また、汚水に沈降凝集剤を添
加した後、最初の浄化水が得られるまでの時間は、使用
するポンプの能力にもよるが1分から3分という短時間
である。
The sedimentation filtration method and sedimentation filtration tank according to the present invention can control the sewage treatment capacity depending on the inflow amount, but specifically, the treatment up to 250 Kg / min to 6000 Kg / min is possible. Further, the time from the addition of the sedimentation coagulant to the sewage until the first purified water is obtained is a short time of 1 to 3 minutes depending on the capacity of the pump used.

【0010】凝集沈降剤の添加された汚水は、沈澱濾過
漕1に滞留している間にも凝集沈降物を生成し続け、そ
の自重で沈降して沈澱濾過漕1の底に堆積する。
The wastewater to which the flocculation-sedimentation agent has been added continues to form a flocculation sediment even while staying in the sedimentation filtration tank 1, and is settled by its own weight and deposited on the bottom of the sedimentation filtration tank 1.

【0011】上記堆積した凝集沈降物は、沈殿物排出口
3から排出して分離することができ、この排出の時期及
び排出量は、排出バルブ3の開閉によって調節すること
ができる。該沈澱物(凝集沈降反応における反応生成
物)の除去は、沈澱濾過漕内の沈澱物生成反応を進める
といった二次的な効果ももたらす。
The accumulated coagulated sediment can be discharged from the sediment discharge port 3 and separated, and the timing and amount of this discharge can be adjusted by opening and closing the discharge valve 3. The removal of the precipitate (reaction product in the coagulation-sedimentation reaction) also has a secondary effect of promoting the reaction of forming the precipitate in the precipitation filtration tank.

【0012】一方、沈殿物を除去した後の上水は流入ホ
ース2から連続的に流入される汚水の流れに押されて、
スクリーン4及びスクリーン4’を通過し濾過される。
このスクリーンの枚数、目の粗さ及びその間隔等は、浄
化する汚水の種類及び量により適宜設定できる。
On the other hand, the clean water after removing the precipitate is pushed by the flow of waste water continuously flowing from the inflow hose 2,
It is filtered through screen 4 and screen 4 '.
The number of screens, the roughness of the screen, the interval between the screens, and the like can be appropriately set depending on the type and amount of wastewater to be purified.

【0013】該スクリーン4,4’により細かい固形汚
濁原因物質が除去された浄化水は、浄化水流出口5から
流出される。該浄化水流出口5から流出される水量は、
流入ホース2から流入される汚水の量及び沈殿物排出口
3から排出される沈殿物の量に応じて調節することがで
きる。この流入・流出量の調節によって、沈澱濾過漕1
内の汚水の滞留時間及びスクリーン4にかかる水圧を調
節することができる。このように本願発明においては、
流入バルブ2a、浄化水流出バルブ5a及び沈殿物排出
バルブ3aの開閉及びスクリーン4の目の粗さ及び枚数
等を適当に組み合わせることによって、一の設備で多様
な汚濁原因物質の種類及び汚濁の程度に対応することが
できる。
Purified water from which fine solid pollution-causing substances have been removed by the screens 4 and 4'is discharged from the purified water outlet 5. The amount of water discharged from the purified water outlet 5 is
It can be adjusted according to the amount of sewage flowing in from the inflow hose 2 and the amount of sediment discharged from the sediment discharge port 3. By adjusting the inflow and outflow rates, the sedimentation filtration tank 1
The residence time of the dirty water inside and the water pressure on the screen 4 can be adjusted. Thus, in the present invention,
By appropriately opening and closing the inflow valve 2a, the purified water outflow valve 5a, and the sediment discharge valve 3a, and adjusting the roughness and the number of meshes of the screen 4, various kinds of pollution-causing substances and the degree of pollution can be obtained in one facility. Can correspond to.

【0014】第2図は、沈澱濾過漕1の底部から、沈降
した沈澱物を排出して除去する場合に排出された沈澱物
を、沈殿物排出口3に設けた沈殿物収集用袋6で収集す
る沈澱濾過方法及び沈澱濾過漕を表したものである。こ
の袋は、透水性のある素材を用い、交換可能とすること
が好ましい。この沈殿物収集用袋6により、沈澱物を袋
単位で取り扱うことができ、本願発明にかかる沈澱濾過
方法及び沈澱濾過漕は小規模処理にも大規模処理にも適
したものとなる。
FIG. 2 shows the precipitate discharged from the bottom of the settling tank 1 when the settling precipitate is discharged and removed by a bag 6 for collecting precipitates provided in the precipitate discharge port 3. 1 shows a precipitation filtration method and a precipitation filtration tank to be collected. This bag is preferably made of a water-permeable material and is replaceable. With this bag 6 for collecting precipitates, the precipitate can be handled in bags, and the precipitation filtration method and precipitation filtration tank according to the present invention are suitable for both small-scale processing and large-scale processing.

【0015】また、沈殿物収集用袋6が透水性のある素
材とすれば、沈殿物に含まれた余分な水分を沈澱物を排
出する際に取り除くことができ、沈殿物とともに多量の
水分を吸引してしまうバキューム車による処理に比し
て、その運搬及び処理場における最終処分には無駄な労
力及び費用を軽減することができる。
Further, if the sediment collecting bag 6 is made of a water-permeable material, excess water contained in the sediment can be removed when the sediment is discharged, and a large amount of water can be removed together with the sediment. Wasteful labor and cost for the transportation and the final disposal at the treatment plant can be reduced as compared with the treatment by the vacuum car which sucks.

【0016】図3は、沈殿物排出口3から沈澱物を排出
した後の汚水を一又は二以上のスクリーンによって濾過
する沈澱濾過漕を表したものである。上述のように、こ
のスクリーンの枚数及び目の粗さ等は処理する汚水の種
類、量に応じて設定することができ、流入ホース2側か
ら浄化水流出口5側に向かってその目の粗さを小さくし
ていくことによって、より効率的な処理が可能となる。
さらに、目詰まりをしたスクリーンを交換することによ
り、一定の処理能率を保つことができる。
FIG. 3 shows a precipitation filter tank for filtering the wastewater after discharging the precipitate from the precipitate discharge port 3 through one or more screens. As described above, the number of screens and the roughness of the screen can be set according to the type and amount of waste water to be treated, and the roughness of the screen from the inflow hose 2 side toward the purified water outlet 5 side. By making the value smaller, more efficient processing becomes possible.
Furthermore, by replacing the clogged screen, a constant processing efficiency can be maintained.

【0017】本願にかかる沈澱濾過方法及び沈澱濾過漕
の浄化能力を具体的に示す。下記の濃度計量試験は、河
川水の水質調査について(株)室蘭試験分析センター
(北海道知事登録の計量証明事業所)が行ったものであ
る。
The precipitation filtration method and the purification capacity of the precipitation filtration tank according to the present application will be specifically described. The following concentration measurement test was conducted by Muroran Test Analysis Center Co., Ltd. (measurement certification office registered with the Governor of Hokkaido) for water quality survey of river water.

【0018】表1に原水の計量結果を示す。Table 1 shows the measurement results of raw water.

【0019】[0019]

【表1】 表2に本願にかかる汚水の沈澱濾過方法及びその沈澱濾
過漕によって処理した後の計量結果を示す。
[Table 1] Table 2 shows the sediment filtration method for wastewater according to the present application and the measurement results after treatment with the sediment filtration tank.

【0020】[0020]

【表2】 上掲の表の結果によれば本願の処理によって、汚水原水
に含まれる浮遊物質量は665mg/lから4mg/l
にまで減少されている。この差は、肉眼でも認識できる
程度の顕著なものである。
[Table 2] According to the results in the table above, the amount of suspended solids contained in the sewage raw water was 665 mg / l to 4 mg / l due to the treatment of the present application.
Has been reduced to. This difference is so remarkable that it can be visually recognized.

【0021】図4はスクリーン4の一実施例を示す。本
実施例は、金網の間に透水マットを挟んだ簡便なもので
あり、処理する汚水量が少ない場合や沈澱濾過漕に使用
できる場所に制限がある場合に適している。
FIG. 4 shows an embodiment of the screen 4. This embodiment is a simple one in which a water-permeable mat is sandwiched between wire nets, and is suitable when the amount of waste water to be treated is small or where the place where it can be used for a sedimentation filtration tank is limited.

【0022】図5に示した沈澱濾過漕1の一実施例は、
排出する沈殿物が沈殿物排出口3に集まるように、沈澱
濾過漕の底面を傾斜させたものである。生成される凝集
沈澱物の塊の大きさや状態に応じて傾斜の角度及び沈殿
物排出口3の大きさを設定することができる。
One embodiment of the precipitation filter tank 1 shown in FIG.
The bottom of the sedimentation filtration tank is inclined so that the sediment to be discharged is collected in the sediment discharge port 3. The angle of inclination and the size of the precipitate discharge port 3 can be set according to the size and state of the lump of the aggregated precipitate generated.

【0023】図6は、沈澱濾過漕1が組立式である場合
の実施例を示す。漏水しないようにパネルの外縁に、パ
ッキンとなるゴム等の樹脂を施した5枚のパネルをボル
ト及び図7に示したU字型クリップボルトによって掛止
することによって、簡易に組み立てることができる。こ
のU字型クリップボルトとは、図7図に示すようにX−
Y面に略U字の形に形成されたU字部分に連なるクラン
ク部が、Z軸方向に折れ曲がっているボルトである。こ
のU字クリップボルト及びボルトによって前記各パネル
が簡易に固定できるのである。さらに、この組立式沈澱
濾過漕には、上述した流入ホース2、沈殿物排出口3、
浄化水流出口5及びスクリーン4を適宜設けることがで
きる。
FIG. 6 shows an embodiment in which the settling filtration tank 1 is of an assembly type. By assembling five panels, which are made of resin such as rubber, as a packing, on the outer edges of the panels so as not to leak water, by the bolts and the U-shaped clip bolt shown in FIG. 7, it is possible to easily assemble. This U-shaped clip bolt is, as shown in FIG.
A crank portion connected to a U-shaped portion formed in a substantially U-shape on the Y surface is a bolt bent in the Z-axis direction. The U-shaped clip bolts and bolts allow the panels to be easily fixed. Further, in this assembly type sedimentation filtration tank, the inflow hose 2, the sediment discharge port 3,
The purified water outlet 5 and the screen 4 can be appropriately provided.

【0024】[0024]

【発明の効果】上述の通り本願は、凝集沈降剤を添加し
た汚水を連続的に沈澱濾過漕に流入し、沈降した沈殿物
のみを排出し、その上水を濾過することによって連続的
に汚水を浄化することができる。この連続的な処理によ
り、凝集沈降のために汚水を貯える設備を必要とせず、
汚水の量に拘わらず一の沈澱濾過漕によって全体の浄化
処理ができる。 また、汚水を連続的に沈澱濾過漕の一
端から流入し、沈澱濾過漕の多端から浄化水を流出する
ことにより、沈澱濾過漕内に方向性のある流れを生じさ
せ、この流れによって汚水を強制的に濾過し、その浄化
能率を向上させる。
Industrial Applicability As described above, according to the present invention, wastewater to which a flocculating settling agent is added is continuously flown into a sedimentation filtration tank, only the sedimented sediment is discharged, and the water is filtered to continuously produce the wastewater. Can be purified. This continuous treatment does not require a facility for storing wastewater for coagulation sedimentation,
Regardless of the amount of sewage, the entire settling process can be done with a single settling filter. In addition, sewage is continuously introduced from one end of the settling filter tank, and purified water is discharged from the other end of the settling filter tank to generate a directional flow in the settling filter tank. To improve its purification efficiency.

【0025】沈澱濾過漕の底部から沈降した凝集反応生
成物である沈澱物のみを交換可能な袋等によって収集す
ることにより、その搬送及び再処理にかかる労力及び費
用を節約することができる。
By collecting only the precipitate, which is the agglutination reaction product settled from the bottom of the settling filter tank, in a replaceable bag or the like, it is possible to save the labor and cost involved in its transportation and reprocessing.

【0026】スクリーンや透水袋の種類や数は、汚水の
種類及び汚濁の程度に併せて選択設定できるため、一の
沈澱漕でどのような汚水処理についても、例えば工場排
水、下水、河川若しくは湖水又は海水、土木建築現場の
泥土・汚水、野菜などの洗い水、生コンプラントなどの
洗い水及びし尿等の様々な汚水の浄化に対応できる。さ
らに、本願発明は、簡易かつコンパクトな設備であり、
スクリーン及び透水袋についても取り外し可能としたこ
とから、設備全体を組立式とすることができ、分解及び
組立にも場所を選ばず運搬や保管には好適なものであ
る。
The type and number of screens and water-permeable bags can be selected and set in accordance with the type of wastewater and the degree of pollution. Therefore, for any wastewater treatment with a single settling tank, for example, factory wastewater, sewage, river or lake water. Alternatively, it can be used to purify seawater, mud and sewage in civil engineering and construction sites, washing water for vegetables, washing water for raw plants and various sewage such as night soil. Furthermore, the present invention is a simple and compact facility,
Since the screen and the water-permeable bag are also removable, the entire equipment can be assembled, and it is suitable for transportation and storage regardless of location for disassembly and assembly.

【0027】汚水の浄化処理においては、環境への配慮
から除去した汚濁原因物質の処理及び採取した水の還元
は重要な課題である。本願発明にかかる汚水の沈澱濾過
方法及び沈澱濾過漕によれば、一の連続した処理過程で
汚濁原因物質のみを迅速かつ完全に除去し、採取した汚
水は浄化水として河川等に戻すことができる。
In the purification treatment of sewage water, the treatment of the pollution-causing substance removed in consideration of the environment and the reduction of the collected water are important issues. ADVANTAGE OF THE INVENTION According to the settling filtration method and settling tank of the wastewater according to the present invention, only the pollutant-causing substance can be quickly and completely removed in one continuous process, and the collected wastewater can be returned as purified water to a river or the like. .

【図面の簡単な説明】[Brief description of drawings]

【図1】 本願に係る汚水の沈澱濾過漕を示したもので
ある。
FIG. 1 shows a settling filtration tank for wastewater according to the present invention.

【図2】 沈殿物排出口に沈殿物収集用袋を設けた沈澱
濾過漕の一実施例を示す。
FIG. 2 shows an example of a sedimentation filtration tank having a sediment collection bag provided at a sediment discharge port.

【図3】 スクリーンを設けた沈澱濾過漕の一実施例を
示す。
FIG. 3 shows an example of a precipitation filtration tank provided with a screen.

【図4】 スクリーンの一実施例を示す。FIG. 4 shows an example of a screen.

【図5】 底面が傾斜している沈澱濾過漕の一実施例を
示す。
FIG. 5 shows an example of a settling filter tank with a sloping bottom.

【図6】 組立式の沈澱濾過漕の一実施例を示す。FIG. 6 shows an example of an assembly-type sedimentation filtration tank.

【図7】 組立式沈澱濾過漕の各パネルを掛止するU字
クリップボルトを示す。
FIG. 7 shows a U-shaped clip bolt for hooking each panel of the assembly-type sedimentation filtration tank.

Claims (16)

【特許請求の範囲】[Claims] 【請求項1】 汚水を浄化するための沈澱濾過方法にお
いて、 汚水を沈澱濾過漕に流入し、 前記沈澱濾過漕の底部から沈降した沈澱物を排出し、 該沈殿物を除去した後の汚水を濾過し、 該濾過後の浄化水を、前記沈澱濾過漕から流出させる汚
水の沈澱濾過方法。
1. A method of settling filtration for purifying sewage, comprising injecting sewage into a settling filter tank, discharging a precipitate that has settled from the bottom of the settling filter tank, and removing the sewage after removing the precipitate. A method for precipitating filtration of sewage, which comprises filtering and purifying purified water after the filtration from the precipitation filtration tank.
【請求項2】 汚水を浄化するための沈澱濾過方法にお
いて、 汚水に凝集沈降剤を添加し、 該凝集沈降剤添加後の汚水を沈澱濾過漕に流入し、 前記沈澱濾過漕の底部から沈降した沈澱物を排出し、 該沈殿物を除去した後の汚水を濾過し、 該濾過後の浄化水を、前記沈澱濾過漕から流出させる汚
水の沈澱濾過方法。
2. A sedimentation filtration method for purifying sewage, comprising adding a coagulating sedimentation agent to sewage, flowing the sewage after the addition of the coagulation sedimentation agent into a sedimentation filtration tank, and sedimenting from the bottom of the sedimentation filtration tank. A method of settling filtration of wastewater, wherein the precipitate is discharged, the wastewater after removing the precipitate is filtered, and the purified water after the filtration is allowed to flow out from the settling tank.
【請求項3】 前記汚水を沈澱濾過漕に流入する過程に
おいて、前記汚水の流入量を調節して流入する、請求項
1記載又は請求項2記載の汚水の沈澱濾過方法。
3. The method for sedimentation filtration of wastewater according to claim 1 or 2, wherein, in the process of flowing the wastewater into the sedimentation filtration tank, the inflowing amount of the wastewater is adjusted to flow in.
【請求項4】 前記沈澱濾過漕の底部から、沈降した沈
澱物を排出する過程において、 該排出された沈澱物を、交換可能な、透水性のある袋で
収集する、請求項1乃至請求項3記載の沈澱濾過方法。
4. The method according to claim 1, wherein in the process of discharging the sedimented sediment from the bottom of the sedimentation filtration tank, the discharged sediment is collected in a replaceable, water-permeable bag. The precipitation filtration method described in 3 above.
【請求項5】 前記沈澱濾過漕の底部から、沈降した沈
澱物を排出して除去した後の汚水を濾過する過程におい
て、 該沈殿物を除去した後の汚水を交換可能な、一又は二以
上のスクリーンによって濾過する、請求項1乃至請求項
4記載の沈澱濾過方法。
5. One or more replaceable sewage water after removing the precipitate in the process of filtering the sewage after discharging and removing the sedimented sediment from the bottom of the sedimentation filtration tank. The method of settling filtration according to any one of claims 1 to 4, wherein the filtration is performed using the screen of claim 1.
【請求項6】 汚水を浄化するための沈澱濾過漕におい
て、 汚水を沈澱濾過漕に流入させる手段と、 前記沈澱濾過漕の底部に設けられ、沈降した沈澱物を沈
澱濾過漕から排出する手段と、 該沈殿物を除去した後の汚水を濾過する手段と、 該濾過後の浄化水を沈澱濾過漕から流出させる手段と、
からなる沈澱濾過漕。
6. A settling filter for purifying sewage, a means for causing sewage to flow into the settling tank, and a means provided at the bottom of the settling filter for discharging settled precipitate from the settling tank. A means for filtering the wastewater after removing the precipitate, a means for causing the purified water after the filtration to flow out from the precipitation filter tank,
Settling filter tank consisting of.
【請求項7】 汚水を浄化するための沈澱濾過漕におい
て、 汚水に凝集沈降剤を添加する手段と、 該凝集沈降剤が添加された汚水を沈澱濾過漕に流入させ
る手段と、 前記沈澱濾過漕の底部に設けられ、沈降した沈澱物を沈
澱濾過漕から排出する手段と、 該沈殿物を除去した後の汚水を濾過する手段と、 該濾過後の浄化水を沈澱濾過漕から流出させる手段と、
からなる沈澱濾過漕。
7. A sedimentation filtration tank for purifying sewage, a means for adding a coagulation-sedimentation agent to sewage, a means for flowing sewage to which the coagulation-sedimentation agent has been added into the sedimentation filtration tank, and the sedimentation filtration tank Means for discharging the sedimented sediment from the sedimentation filtration tank, a means for filtering the sewage after removing the sediment, and a means for discharging the purified water after the filtration from the sedimentation filtration tank. ,
Settling filter tank consisting of.
【請求項8】 前記汚水を沈澱濾過漕に流入させる手段
が、該流入量について調節可能であることを特徴とする
請求項6又は請求項7記載の沈澱濾過漕。
8. The settling filter according to claim 6 or 7, wherein the means for causing the waste water to flow into the settling filter is adjustable with respect to the inflow amount.
【請求項9】 前記沈降した沈澱物を沈澱濾過漕から排
出する手段が、 前記排出させた沈殿物を収集するための容器又は袋を有
することを特徴とする請求項6乃至請求項8記載の沈澱
濾過漕。
9. The method according to claim 6, wherein the means for discharging the settled precipitate from the settling filtration tank has a container or a bag for collecting the discharged precipitate. Settling filter.
【請求項10】 前記排出させた沈殿物を収集するため
の容器又は袋が、透水性を有する材質からなる請求項9
記載の沈澱濾過漕。
10. The container or bag for collecting the discharged precipitate is made of a water-permeable material.
The settling filter described.
【請求項11】 前記排出させた沈殿物を収集するため
の容器又は袋が、交換可能であることを特徴とする請求
項9又は請求項10記載の沈澱濾過漕。
11. The precipitation filtration tank according to claim 9 or 10, wherein a container or bag for collecting the discharged precipitate is replaceable.
【請求項12】 前記沈殿物を除去した後の汚水を濾過
する手段が、一又は二以上のスクリーンを有することを
特徴とする請求項6乃至請求項11記載の沈澱濾過漕。
12. The precipitation filter tank according to claim 6, wherein the means for filtering the wastewater after removing the precipitate has one or more screens.
【請求項13】 前記スクリーンが、交換可能であるこ
とを特徴とする請求項12記載の沈澱濾過漕。
13. The settling filter according to claim 12, wherein the screen is replaceable.
【請求項14】 前記汚水を浄化するための沈澱濾過漕
の底面が、沈降した沈殿物が前記排出手段に集まるよう
に、傾斜している請求項6乃至請求項13記載の沈澱濾
過漕。
14. The settling filter tank according to claim 6, wherein the bottom surface of the settling filter tank for purifying the sewage is inclined so that the settled sediment collects at the discharge means.
【請求項15】 前記汚水を浄化するための沈澱濾過漕
が組立式である請求項6乃至請求項14記載の沈澱濾過
漕。
15. The settling filter according to claim 6, wherein the settling filter for purifying the wastewater is an assembly type.
【請求項16】 前記汚水を浄化するための沈澱濾過漕
が、 4枚以上のパネルと、 前記パネルを掛止する複数のボルトと、 前記パネルを掛止する複数のピンと、から組立てること
ができ、 前期パネルの外縁には漏水を防止するためのゴム等の樹
脂が施され、 前記ピンがクランク部分とU字部分を有するピンであ
る、 請求項15記載の沈澱濾過漕。
16. A sedimentation filter tank for purifying the sewage can be assembled from four or more panels, a plurality of bolts for locking the panels, and a plurality of pins for locking the panels. The sedimentation filter tank according to claim 15, wherein a resin such as rubber is applied to an outer edge of the first panel to prevent water leakage, and the pin is a pin having a crank portion and a U-shaped portion.
JP8941696A 1996-04-11 1996-04-11 Method of settling and filtering foul water and tank for settling and filtering sewage Pending JPH09276606A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP8941696A JPH09276606A (en) 1996-04-11 1996-04-11 Method of settling and filtering foul water and tank for settling and filtering sewage

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP8941696A JPH09276606A (en) 1996-04-11 1996-04-11 Method of settling and filtering foul water and tank for settling and filtering sewage

Publications (1)

Publication Number Publication Date
JPH09276606A true JPH09276606A (en) 1997-10-28

Family

ID=13970059

Family Applications (1)

Application Number Title Priority Date Filing Date
JP8941696A Pending JPH09276606A (en) 1996-04-11 1996-04-11 Method of settling and filtering foul water and tank for settling and filtering sewage

Country Status (1)

Country Link
JP (1) JPH09276606A (en)

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2000051611A (en) * 1998-08-10 2000-02-22 Tsurumi Mfg Co Ltd Apparatus for granulating and dewatering suspension
WO2010011489A3 (en) * 2008-07-22 2010-05-06 Trans Terra Corporation Primary equalization settling tank
WO2011087936A3 (en) * 2010-01-12 2011-11-17 Trans Terra Corporation Self-cleaning influent feed system for a wastewater treatment plant
US8398864B2 (en) 2008-07-22 2013-03-19 Trans Terra Corporation Screened decanter assembly for a settling tank
JP2014087799A (en) * 2014-01-17 2014-05-15 Ecoscience:Kk Polluted water purification system
CN104707374A (en) * 2013-12-12 2015-06-17 林淑琴 Industrial purifying pool
CN106039777A (en) * 2014-10-14 2016-10-26 刘伟 Sewage sediment device for protecting environment

Cited By (13)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2000051611A (en) * 1998-08-10 2000-02-22 Tsurumi Mfg Co Ltd Apparatus for granulating and dewatering suspension
WO2010011489A3 (en) * 2008-07-22 2010-05-06 Trans Terra Corporation Primary equalization settling tank
CN102105401A (en) * 2008-07-22 2011-06-22 特兰斯特拉公司 Primary equalization settling tank
US7972505B2 (en) 2008-07-22 2011-07-05 Trans Terra Corporation Primary equalization settling tank
US8398864B2 (en) 2008-07-22 2013-03-19 Trans Terra Corporation Screened decanter assembly for a settling tank
US8225942B2 (en) 2008-07-22 2012-07-24 Trans Terra Corporation Self-cleaning influent feed system for a wastewater treatment plant
GB2489143A (en) * 2010-01-12 2012-09-19 Trans Terra Corp Self-cleaning influent feed system for a wastewater treatment plant
WO2011087936A3 (en) * 2010-01-12 2011-11-17 Trans Terra Corporation Self-cleaning influent feed system for a wastewater treatment plant
GB2489143B (en) * 2010-01-12 2016-11-02 Trans Terra Corp Self-cleaning influent feed system for a wastewater treatment plant
CN104707374A (en) * 2013-12-12 2015-06-17 林淑琴 Industrial purifying pool
JP2014087799A (en) * 2014-01-17 2014-05-15 Ecoscience:Kk Polluted water purification system
CN106039777A (en) * 2014-10-14 2016-10-26 刘伟 Sewage sediment device for protecting environment
CN106039777B (en) * 2014-10-14 2017-12-29 惠州市合新科技有限公司 Sewage precipitation device for environmental protection

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