JP2001224907A - Advanced treatment-correspondent flocculating, settling and rapid filtering device - Google Patents

Advanced treatment-correspondent flocculating, settling and rapid filtering device

Info

Publication number
JP2001224907A
JP2001224907A JP2000105644A JP2000105644A JP2001224907A JP 2001224907 A JP2001224907 A JP 2001224907A JP 2000105644 A JP2000105644 A JP 2000105644A JP 2000105644 A JP2000105644 A JP 2000105644A JP 2001224907 A JP2001224907 A JP 2001224907A
Authority
JP
Japan
Prior art keywords
chamber
coagulation
sedimentation
filtration
flocculating
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
JP2000105644A
Other languages
Japanese (ja)
Inventor
Toshikazu Shimodaira
利和 下平
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.)
Individual
Original Assignee
Individual
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 Individual filed Critical Individual
Priority to JP2000105644A priority Critical patent/JP2001224907A/en
Publication of JP2001224907A publication Critical patent/JP2001224907A/en
Pending legal-status Critical Current

Links

Abstract

PROBLEM TO BE SOLVED: To provide an advanced treatment-correspondent flocculating, settling and rapid filtering device miniaturized, inexpensive in equipment cost and operation cost and capable of carrying out stably advanced treatment of sewage, wastewater from a factory or the like and water purification of lakes and rivers with high efficiency. SOLUTION: The usual flocculating tank and the usual settling tank are combined into one, which is then partitioned into a flocculating chamber 1, a settling chamber 2 on the lateral side of the chamber 1 and a storage chamber 3 below the chamber 1. A slot part 5 communicating with the chamber 2 is provided in the lower part of the side surface of the camber 1. A partition plate 6 having communication holes 7 communicating with the chamber 3 is provided on the bottom surface of the chamber 1. A flow rectifying plate 8 projecting toward the chamber 2 is provided for rectifying the current flowing to the chamber 2. Any of a sand filtration chamber, a membrane filtration chamber, a biological membrane filtration chamber and an activated carbon adsorption filtration chamber is provided in the upper part of the chamber 2 for filtrating supernatant water of an upward current.

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】本発明は、汚水に含まれる浮
遊物質、溶解性有機物、栄養塩類、金属類等を処理する
技術に関する。特に、設備費、運転費が安価で、下水、
工場排水等の高度処理や湖沼・河川の水質浄化を安定し
た高い効率で行うことが可能な、コンパクト化を図った
高度処理対応型の凝集沈殿・急速ろ過装置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a technique for treating suspended substances, soluble organic substances, nutrients, metals and the like contained in sewage. In particular, equipment and operation costs are low, sewage,
The present invention relates to a compact, high-processing coagulation sedimentation / rapid filtration system capable of performing high-level treatment of factory wastewater and the like and purification of lakes and rivers with stable and high efficiency.

【0002】[0002]

【従来の技術】従来の技術で下水や工場排水の高度処理
や湖沼・河川の水質浄化を凝集沈殿・急速ろ過法で行う
ためには、通例、図2の処理フローに示すような施設が
必要となる。このような施設では、各処理槽が別個に設
置されているため、広い設置面積が必要、運転管理が煩
雑、イニシャル・ランニングコストが高い、という問題
点がある。
2. Description of the Related Art In order to perform advanced treatment of sewage and industrial wastewater and purification of lakes / marshes / rivers by a coagulation sedimentation / rapid filtration method, a facility as shown in the processing flow of FIG. Becomes In such a facility, since each processing tank is separately installed, there is a problem that a large installation area is required, operation management is complicated, and initial running costs are high.

【0003】[0003]

【発明が解決しようとする課題】本発明は、上述の問題
点に鑑みてなされたものであり、目的とするところは、
設備費、運転費が安価で、下水、工場排水等の高度処理
や湖沼・河川の水質浄化を安定した高い効率で行うこと
が可能な、コンパクト化を図った高度処理対応型の凝集
沈殿・急速ろ過装置を提供するにある。
SUMMARY OF THE INVENTION The present invention has been made in view of the above-mentioned problems, and has as its object the following:
Low cost coagulation sedimentation and rapid processing with high efficiency and low cost of equipment and operation, stable and high efficiency of advanced treatment of sewage and industrial wastewater and purification of lakes / marshes / rivers. Providing filtration equipment.

【0004】[0004]

【課題を解決するための手段】上述の目的を達成するた
めの手段として、請求項1、2、3に記載の発明を用い
る。
Means for Solving the Problems As means for achieving the above object, the inventions according to claims 1, 2 and 3 are used.

【0005】すなわち、従来の凝集槽と沈殿槽を合体さ
せ、凝集室の側方を沈殿室、下方を貯留室として区画
し、前記凝集室の側面下方に前記沈殿室と連通するスロ
ット部,前記凝集室の底面に前記貯留室と連通する連通
口を有する仕切り板、及び前記沈殿室の方向に突き出し
た整流板を設けたことを特徴とする凝集沈殿装置。
That is, a conventional coagulation tank and a sedimentation tank are combined, a side of the coagulation chamber is defined as a sedimentation chamber, and a lower part is defined as a storage chamber, and a slot communicating with the sedimentation chamber is provided below a side surface of the coagulation chamber. A coagulation sedimentation apparatus comprising: a partition plate having a communication port communicating with the storage chamber on the bottom surface of the coagulation chamber; and a rectifying plate protruding toward the sedimentation chamber.

【0006】請求項1に記載の凝集沈殿装置の凝集室を
上下に区画し、上段を急速攪拌凝集室、下段を緩速攪拌
凝集室とし、上下段の境は連通口を有する仕切り板とし
たことを特徴とする凝集沈殿装置。
The coagulation chamber of the coagulation settling apparatus according to claim 1 is divided into upper and lower sections, the upper section is a rapid stirring and coagulation chamber, the lower section is a slow stirring and coagulation chamber, and the boundary between the upper and lower sections is a partition plate having a communication port. A coagulation sedimentation apparatus characterized by the above-mentioned.

【0007】請求項1に記載の凝集沈殿装置の沈殿室の
上方に、該沈殿室の上澄み水を上向き流でろ過する砂ろ
過室、膜ろ過室、生物ろ過室、活性炭吸着ろ過室のいず
れかを設けたことを特徴とする凝集沈殿・急速ろ過装
置。
[0007] Any one of a sand filtration chamber, a membrane filtration chamber, a biological filtration chamber, and an activated carbon adsorption filtration chamber for filtering the supernatant water of the sedimentation chamber by an upward flow above the sedimentation chamber of the coagulation sedimentation apparatus according to claim 1. A coagulation sedimentation / rapid filtration device characterized by having a filter.

【0008】[0008]

【発明の実施の形態】次に本発明の好適実施例の形態を
図1に基づいて詳述する。図1は高度処理対応型凝集沈
殿・急速ろ過装置の概略縦断面図である。図1に示すよ
うに当該装置は、凝集室1、沈殿室2、貯留室3、ろ過
室4から構成されている。凝集室1の底面は連通口7を
有する仕切り板6であり、これによって凝集室1と貯留
室3は隔てられている。仕切り板6の端は沈殿室2の方
向に突き出した整流板8に連なっている。凝集室1の上
段の急速攪拌凝集室9と下段の緩速攪拌凝集室10は連
通口12を有する仕切り板11によって隔てられてい
る。沈殿室2の上方には上澄み水を上向き流でろ過する
ろ過室4が設けられている。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS Next, a preferred embodiment of the present invention will be described in detail with reference to FIG. FIG. 1 is a schematic longitudinal sectional view of a coagulation sedimentation / rapid filtration device capable of advanced treatment. As shown in FIG. 1, the apparatus includes a flocculation chamber 1, a sedimentation chamber 2, a storage chamber 3, and a filtration chamber 4. The bottom surface of the coagulation chamber 1 is a partition plate 6 having a communication port 7, which separates the coagulation chamber 1 from the storage chamber 3. The end of the partition plate 6 is connected to a straightening plate 8 protruding in the direction of the sedimentation chamber 2. The upper stage rapid stirring / aggregating chamber 9 and the lower stage slow stirring / aggregating chamber 10 are separated by a partition plate 11 having a communication port 12. Above the sedimentation chamber 2, a filtration chamber 4 for filtering the supernatant water by an upward flow is provided.

【0009】次に本発明の作用を処理手順に添って説明
する。
Next, the operation of the present invention will be described along with the processing procedure.

【0010】間欠的に一定量の汚水14が急速攪拌凝
集室9に流入する。 急速攪拌凝集室9では、攪拌機13により攪拌流を起
こし、定量的に注入される凝集剤15と混合し、凝集反
応によりフロックを形成させる。 前記に伴い、急速攪拌凝集室9の混合液は、仕切り
板11の連通口12より緩速攪拌凝集室10に移流し、
連通口12を介して起こる攪拌流によって穏やかに攪拌
され、フロックの成長が図られる。 緩速攪拌凝集室10でフロックが成長し重くなった汚
泥質は、凝集室1の底面の連通口7を介して、貯留室3
に沈降する。 一方、緩速攪拌凝集室10の混合液は、前記に伴
い、下方のスロット部5を通って沈殿室2に移流する。 前記の流入が停止すると、沈殿室2に移流した混合
液中の汚泥質は重力により沈降し、整流板8によって斜
壁16に添って貯留室3へ沈降する汚泥と凝集室1の底
面上へ返送される汚泥とに区分けされる。この時の返送
される汚泥の量的比率は、整流板8の角度θによって調
整する。 前記で凝集室1の底面上へ返送された汚泥は、連通
口7を介して貯留室3へ沈降する汚泥と凝集室1に残留
する汚泥とにふるい分けられる。この時の貯留室3へ沈
降する汚泥の量的比率は、連通口7の開口率による。 凝集室1に残留した汚泥の一部は、凝集室1の攪拌流
によって巻き上げられ、凝集室1内で浮遊する。この巻
き上げられ浮遊する汚泥の量は、凝集室1に返送され残
留した汚泥の量と攪拌流の強さによる。 一方前記に伴い、沈殿室2の上部の上澄み水は押し
上げられ、上向き流でろ過室4に移流する。▲10▼ろ
過室4では、ろ過層の種類によってろ過、吸着、生物学
的処理等の処理が行われた後、自然水流で越流せき17
より流出する。
A certain amount of sewage 14 intermittently flows into the rapid stirring / coagulation chamber 9. In the rapid stirring coagulation chamber 9, a stirring flow is generated by the stirrer 13, mixed with the coagulant 15 injected quantitatively, and flocs are formed by the coagulation reaction. Along with the above, the liquid mixture in the rapid stirring and aggregation chamber 9 is transferred from the communication port 12 of the partition plate 11 to the slow stirring and aggregation chamber 10,
The mixture is gently agitated by the agitation flow generated through the communication port 12, and the floc grows. The sludge whose floc has grown and becomes heavier in the slow stirring flocculation chamber 10 is stored in the storage chamber 3 through the communication port 7 on the bottom surface of the flocculation chamber 1.
Settles down. On the other hand, the liquid mixture in the slow stirring and aggregation chamber 10 is transferred to the sedimentation chamber 2 through the lower slot 5 as described above. When the inflow is stopped, the sludge in the mixed solution transferred to the sedimentation chamber 2 is settled by gravity, and the sludge settles into the storage chamber 3 along the sloping wall 16 by the rectifying plate 8 and the bottom of the flocculation chamber 1. It is classified into sludge returned. The quantitative ratio of the returned sludge at this time is adjusted by the angle θ of the current plate 8. The sludge returned to the bottom of the coagulation chamber 1 is sieved into the sludge settling into the storage chamber 3 through the communication port 7 and the sludge remaining in the coagulation chamber 1. The quantitative ratio of the sludge settling in the storage chamber 3 at this time depends on the opening ratio of the communication port 7. Part of the sludge remaining in the flocculation chamber 1 is wound up by the stirring flow of the flocculation chamber 1 and floats in the flocculation chamber 1. The amount of the sludge that is rolled up and floated depends on the amount of sludge returned to the coagulation chamber 1 and remaining and the strength of the stirring flow. On the other hand, along with the above, the supernatant water in the upper part of the sedimentation chamber 2 is pushed up and flows upward to the filtration chamber 4. {Circle around (10)} In the filtration chamber 4, after filtration, adsorption, biological treatment, and the like are performed depending on the type of the filtration layer, the water overflows with natural water.
More outflow.

【0011】[0011]

【発明の効果】従来より、混合液中にフロック形成の核
となるSS分がある程度含まれていた方が、凝集沈殿の
効果が高いことが知られている。本発明の凝集沈殿装置
は前述の作用に示すように、自然水流と重力沈降によ
り、ポンプを使うことなく一定量の汚泥を混合液中に返
送することができ、返送された汚泥は凝集室の攪拌流に
よって巻き上げられ、混合液中に一定濃度で浮遊し、フ
ロック形成の核となる。これにより、凝集沈殿の効果
が高く、汚濁成分やSS分等の除去率が高い、凝集剤
の使用量を低減することができる、その分、汚泥の発
生量が少ない、という利点が生じる。
It has been known that the effect of flocculation and sedimentation is higher when the mixed solution contains a certain amount of SS, which is a nucleus for floc formation. As described above, the coagulation sedimentation device of the present invention can return a certain amount of sludge to the mixed solution without using a pump by natural water flow and gravity sedimentation. It is wound up by the agitated flow and floats at a constant concentration in the mixed solution, forming a core of floc formation. As a result, there are advantages that the effect of coagulation and sedimentation is high, the removal rate of polluting components and SS content is high, the amount of coagulant used can be reduced, and the amount of generated sludge is correspondingly small.

【0012】また、凝集室の底面上の沈積汚泥と貯留室
の汚泥の、混合液中からの凝集剤の摂取や、混合液中へ
の凝集剤の放出により、混合液中の凝集剤濃度の安定化
が図られるとともに、凝集剤の無駄な使用を抑える効果
がある。
In addition, the coagulant concentration in the mixed liquid is reduced by ingesting the coagulant from the mixed liquid and releasing the coagulant into the mixed liquid of the sediment sludge on the bottom surface of the coagulation chamber and the sludge in the storage chamber. It has the effect of stabilizing and suppressing wasteful use of the flocculant.

【0013】更に、本発明の凝集沈殿・急速ろ過装置
は、凝集沈殿処理後、沈殿室の上方で上向き流のろ過処
理を行うことにより、上向き流で均一にろ過すること
ができる(ろ過面に汚濁分均等負荷)、前段で凝集沈
殿を行っているので浮遊物の電荷が中和され、吸着除去
の効果もあり、ろ過効率が高い、貯留室で発生したス
カムは上方の凝集室に浮上するため、又ろ過室のろ材層
に付着した凝集フロックは重力により貯留室に沈降する
ため、ろ材層の目詰まりが少なく、長期間の使用が可能
である、ろ材層を洗浄する場合は、上方からの通水
(高圧水の使用可)により、ろ材層に付着した凝集フロ
ックが脱離し貯留室へ重力沈降し、効果的に洗浄するこ
とができる、前記の脱離した凝集フロックを更に除
去したい場合は、ろ過層の上方からの洗浄水の流下によ
って、前段の凝集室へ逆流させ、再度凝集沈殿処理がで
き効率的である、という利点を生じる。
Further, the coagulation sedimentation / rapid filtration device of the present invention can perform an upward flow filtration treatment above the sedimentation chamber after the coagulation sedimentation treatment, so that the filtration can be performed uniformly by the upward flow. (Equivalent load of pollutants), flocculation and sedimentation in the previous stage neutralizes the charge of suspended matter, has the effect of adsorption and removal, has high filtration efficiency, and scum generated in the storage chamber floats to the upper flocculation chamber. Therefore, flocculated floc adhering to the filter medium layer in the filtration chamber settles in the storage chamber due to gravity, so the filter medium layer is less clogged and can be used for a long period of time. When the flocculated floc adhering to the filter medium layer is desorbed by passing water (use of high-pressure water) and sedimented by gravity into the storage chamber, it can be effectively washed. Is from above the filtration layer The stream of wash water, to flow back to the previous stage of agglomeration chamber, it is efficient can flocculation process again produces the advantage.

【0014】また、本発明の凝集沈殿・急速ろ過装置
は、従来の急速攪拌凝集槽、緩速攪拌凝集槽、沈殿槽、
ろ過槽、貯留槽の5つが統合されているため、設置ス
ペースが少ない、移送ポンプ等の移送設備を必要とし
ない、運転管理が容易、という利点がある。
Further, the coagulation sedimentation / rapid filtration apparatus of the present invention comprises a conventional rapid stirring coagulation tank, a slow stirring coagulation tank, a sedimentation tank,
Since the filtration tank and the storage tank are integrated, there are advantages in that the installation space is small, transfer equipment such as a transfer pump is not required, and operation management is easy.

【0015】以上により、設備費、運転費が安価で、下
水、工場排水等の高度処理や湖沼・河川の水質浄化を安
定した高い効率で行うことが可能な、コンパクト化を図
った高度処理対応型の凝集沈殿・急速ろ過装置を提供す
ることができる。
[0015] As described above, the equipment cost and the operating cost are low, and the advanced treatment for downsizing, which can perform the advanced treatment of sewage and factory drainage and the purification of the water quality of lakes, rivers and rivers with high efficiency, is realized. It is possible to provide a coagulation sedimentation / rapid filtration device of a mold type.

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

【図1】本発明の実施例を示す、高度処理対応型凝集沈
殿・急速ろ過装置の概略縦断面図である。
FIG. 1 is a schematic longitudinal sectional view of a coagulation sedimentation / rapid filtration device capable of advanced treatment, showing an embodiment of the present invention.

【図2】従来の技術を示す、凝集沈殿・急速ろ過施設の
処理フローである。
FIG. 2 is a process flow of a coagulation sedimentation / rapid filtration facility showing a conventional technique.

【符号の説明】[Explanation of symbols]

1・・・凝集室 2・・・沈殿室 3・・・貯留室 4・・・ろ過室 5・・・スロット部 6・・・仕切り板 7・・・連通口 8・・・整流板 9・・・急速攪拌凝集室 10・・・緩速攪拌凝
集室 11・・・仕切り板 12・・・連通口 13・・・攪拌機 14・・・汚水 15・・・凝集剤 16・・・斜壁 17・・・越流せき
DESCRIPTION OF SYMBOLS 1 ... Coagulation room 2 ... Sedimentation room 3 ... Storage room 4 ... Filtration room 5 ... Slot part 6 ... Partition plate 7 ... Communication port 8 ... Rectification plate 9. ··· Fast stirring flocculation chamber 10 ··· Slow stirring flocculation chamber 11 ··· Partition plate 12 ··· Communication port 13 ··· Stirrer 14 ··· Sewage 15 ··· Flocculant 16 ··· Sloping wall ... Overflow cough

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】凝集室の側方を沈殿室、下方を貯留室とし
て区画し、前記凝集室の側面下方に前記沈殿室と連通す
るスロット部、前記凝集室の底面に前記貯留室と連通す
る連通口を有する仕切り板、及び前記沈殿室の方向に突
き出した整流板を設けたことを特徴とする凝集沈殿装
置。
1. A coagulation chamber is divided into a sedimentation chamber and a lower part thereof is defined as a storage chamber. A slot portion communicating with the sedimentation chamber is formed below a side surface of the coagulation chamber, and a bottom surface of the coagulation chamber is communicated with the storage chamber. A coagulating sedimentation apparatus comprising: a partition plate having a communication port; and a rectifying plate protruding toward the sedimentation chamber.
【請求項2】請求項1に記載の凝集沈殿装置の凝集室を
上下に区画し、上段を急速攪拌凝集室、下段を緩速攪拌
凝集室とし、前記上段と下段の境は連通口を有する仕切
り板としたことを特徴とする凝集沈殿装置。
2. The coagulation chamber of the coagulation sedimentation apparatus according to claim 1, wherein the coagulation chamber is divided into upper and lower sections, the upper section is a rapid stirring coagulation chamber, the lower section is a slow stirring coagulation chamber, and a boundary between the upper and lower sections has a communication port. A coagulation sedimentation device characterized by using a partition plate.
【請求項3】請求項1に記載の凝集沈殿装置の沈殿室の
上方に、該沈殿室の上澄み水を上向き流でろ過する砂ろ
過室、膜ろ過室、生物ろ過室、活性炭吸着ろ過室のいず
れかを設けたことを特徴とする凝集沈殿・急速ろ過装
置。
3. A sand filtration chamber, a membrane filtration chamber, a biological filtration chamber, and an activated carbon adsorption filtration chamber for filtering the supernatant water of the sedimentation chamber by an upward flow above the sedimentation chamber of the coagulation sedimentation apparatus according to claim 1. A coagulation sedimentation / rapid filtration device characterized by any one of the above.
JP2000105644A 2000-02-18 2000-02-18 Advanced treatment-correspondent flocculating, settling and rapid filtering device Pending JP2001224907A (en)

Priority Applications (1)

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Applications Claiming Priority (1)

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Publications (1)

Publication Number Publication Date
JP2001224907A true JP2001224907A (en) 2001-08-21

Family

ID=18618949

Family Applications (1)

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Country Status (1)

Country Link
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JP2014161823A (en) * 2013-02-27 2014-09-08 Amanasu Shinwa Kk Purifier
CN106007233A (en) * 2016-07-20 2016-10-12 皖西学院 Efficient industrial sewage treatment device
CN109292886A (en) * 2018-10-31 2019-02-01 南京合茂自动化科技有限公司 Apparatus for recovering metal in a kind of electroplating wastewater
CN111533385A (en) * 2020-05-20 2020-08-14 肖兴魁 Method and equipment for separating granular ore waste
CN115304185A (en) * 2022-08-08 2022-11-08 青岛尚禹环保设备科技有限公司 Ultrafiltration membrane filtration equipment

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101580292B (en) * 2009-06-03 2011-06-15 中国科学院兰州化学物理研究所 Water-distribution anti-disturbance floc precipitation reverse separation device
JP2014161823A (en) * 2013-02-27 2014-09-08 Amanasu Shinwa Kk Purifier
CN106007233A (en) * 2016-07-20 2016-10-12 皖西学院 Efficient industrial sewage treatment device
CN109292886A (en) * 2018-10-31 2019-02-01 南京合茂自动化科技有限公司 Apparatus for recovering metal in a kind of electroplating wastewater
CN111533385A (en) * 2020-05-20 2020-08-14 肖兴魁 Method and equipment for separating granular ore waste
CN115304185A (en) * 2022-08-08 2022-11-08 青岛尚禹环保设备科技有限公司 Ultrafiltration membrane filtration equipment

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