JPH06304571A - Treatment of waste water - Google Patents

Treatment of waste water

Info

Publication number
JPH06304571A
JPH06304571A JP5095908A JP9590893A JPH06304571A JP H06304571 A JPH06304571 A JP H06304571A JP 5095908 A JP5095908 A JP 5095908A JP 9590893 A JP9590893 A JP 9590893A JP H06304571 A JPH06304571 A JP H06304571A
Authority
JP
Japan
Prior art keywords
solid matter
waste water
membrane separation
mechanical
separation
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
JP5095908A
Other languages
Japanese (ja)
Inventor
Yuji Yasuda
雄二 保田
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.)
Mitsubishi Heavy Industries Ltd
Original Assignee
Mitsubishi Heavy Industries Ltd
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 Mitsubishi Heavy Industries Ltd filed Critical Mitsubishi Heavy Industries Ltd
Priority to JP5095908A priority Critical patent/JPH06304571A/en
Publication of JPH06304571A publication Critical patent/JPH06304571A/en
Pending legal-status Critical Current

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  • Separation Of Suspended Particles By Flocculating Agents (AREA)
  • Separation Using Semi-Permeable Membranes (AREA)

Abstract

PURPOSE:To eliminate a mixing device for mixing a mechanical separation residue with a membrane separation concentrate in a waste water treating method wherein solid matter in a waste water is removed by a mechanical separation device and a flocculant is injected into the separated liquid to treat it by membrane separation. CONSTITUTION:In a waste water treating device in which after solid matter in waste water 1 is removed by a mechanical separator 2, a flocculant 3 is injected into the separated liquid to flocculate the residual solid matter and colloid and a part of soluble materials and the formed flocs are separated by a membrane separation device, a membrane separation concentrate 7 contg. the flocs is circulated through the mechanical separator 2 to separate and concentrate them together with the solid matter in the waste water 1.

Description

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

【0001】[0001]

【産業上の利用分野】本発明は、各種廃水(産業廃水、
し尿、下水、浄化槽汚泥分離液などの生活系排水など)
の処理方法に関する。
BACKGROUND OF THE INVENTION The present invention relates to various wastewater (industrial wastewater,
Domestic wastewater such as human waste, sewage, septic tank sludge separation liquid, etc.)
Regarding the processing method of.

【0002】[0002]

【従来の技術】図3に従来の廃水処理方法を示す。廃水
1中の固形物の大半を遠心分離機などの機械的分離装置
2で除去した後、分離液に凝集剤(硫酸バンド(硫酸ア
ルミニウム)、高分子凝集剤などの有機、無機系凝縮
剤)3を凝集反応装置4において注入することにより、
分離液中に残留する固形物、コロイド、溶解性物質の一
部を凝集フロック中に取り込んだ後、凝集フロックを限
外濾過又は精密濾過の膜分離装置5で分離するものであ
る。機械的分離装置2からは分離残渣8、膜分離装置5
からは凝集フロックを含む濃縮液7が排出し、これらは
混合装置9で混合して汚泥処理装置10で処理される。
2. Description of the Related Art FIG. 3 shows a conventional wastewater treatment method. After removing most of the solids in the wastewater 1 with a mechanical separator 2 such as a centrifuge, the separated liquid is a flocculant (organic or inorganic condensing agent such as a sulfuric acid band (aluminum sulfate) or a polymer flocculant). By injecting 3 in the flocculation reactor 4,
The solid matter, colloid, and a part of the soluble substance remaining in the separated liquid are taken into the floc, and the floc is separated by the ultrafiltration or microfiltration membrane separation device 5. Separation residue 8 and membrane separation device 5 from the mechanical separation device 2.
The concentrated liquid 7 containing agglomerated flocs is discharged from the device, and these are mixed by the mixing device 9 and treated by the sludge treatment device 10.

【0003】[0003]

【発明が解決しようとする課題】前記の従来の廃水処理
方法では、図3に示すように、機械的分離残渣および膜
分離濃縮液という2つの排出系統を有することになり、
混合処理するための混合装置が必要となって装置構成が
複雑になるとともに、操作管理が煩雑になる。
The above-mentioned conventional wastewater treatment method has two discharge systems of a mechanical separation residue and a membrane separation concentrate, as shown in FIG.
A mixing device is required for the mixing process, which complicates the device configuration and complicates operation management.

【0004】本発明は、以上の問題点を解決することが
できる廃水処理方法を提供しようとするものである。
The present invention is intended to provide a wastewater treatment method capable of solving the above problems.

【0005】[0005]

【課題を解決するための手段】本発明の廃水処理方法
は、廃水中の固形物を機械的分離装置によって除去した
後、分離液に凝集剤を注入して残留する固形物、コロイ
ドおよび溶解性物質の一部を凝集フロック化し、これを
膜分離によって分離する廃水処理方法において、凝集フ
ロックを含む膜分離濃縮液を機械的分離装置に循環させ
ることを特徴とする。
According to the method for treating wastewater of the present invention, a solid matter in a wastewater is removed by a mechanical separator, and then a coagulant is injected into the separated liquid to leave a residual solid matter, colloid and solubility. A wastewater treatment method in which a part of a substance is flocculated and separated by membrane separation is characterized in that a membrane separation concentrate containing agglomerated flocs is circulated through a mechanical separation device.

【0006】[0006]

【作用】本発明においては、前記のように、膜分離濃縮
液を機械的分離装置に循環し、廃水中の固形物と凝集フ
ロックを混合処理することにより、従来必要であった混
合装置が省略され、かつ、操作管理が簡略化される。ま
た、膜分離濃縮液中の凝集フロックも機械的分離装置で
濃縮されるので、発生する汚泥(機械的分離残渣および
凝集フロック)全体が減容化される。
In the present invention, as described above, the membrane separation concentrated liquid is circulated through the mechanical separation device, and the solid matter in the waste water and the floc floc are mixed, so that the mixing device which has been conventionally required is omitted. And the operation management is simplified. Further, the flocs in the membrane separation concentrate are also concentrated by the mechanical separator, so that the volume of sludge (mechanical separation residue and flocs) generated is reduced.

【0007】本発明では、以上の通り、廃水の原液中の
固形物と凝集フロックを機械的分離装置で混合処理する
ことにより、装置構成、操作管理が簡略化されるが、本
発明に係る廃水処理方法の成否を決める要素として、機
械的分離装置における本来の目的である原液中の固形物
の分離濃縮機能を、従来方法と同等程度に維持すること
ができるか否かがあげられる。凝集フロックは保水性が
強いためにきわめて難脱水性であり、これを廃水と混合
することによる悪影響がある可能性がある。そこで、こ
の点を下記の実験によって検討した。
According to the present invention, as described above, the solid composition and coagulation flocs in the undiluted solution of waste water are mixed and processed by the mechanical separation apparatus, so that the apparatus configuration and operation management are simplified. The factor that determines the success or failure of the treatment method is whether or not the original purpose of the mechanical separation device, that is, the function of separating and concentrating the solid matter in the stock solution, can be maintained at the same level as the conventional method. Aggregated flocs are extremely difficult to dehydrate due to their strong water retention, and there is a possibility that they may be adversely affected by mixing them with wastewater. Therefore, this point was examined by the following experiment.

【0008】(1)実験試料(対象液)……浄化槽汚泥
(Aし尿処理場に搬入するものをサンプリング)、SS
濃度12300ppm 、 (2)実験装置、条件……機械的分離(回分遠心分離
器、遠心回転数3000rpm 、10分)、凝集剤(硫酸
バンド、注入率300ppm 、pH6.5NaOHで調整、薬品
混和はジャーテスタで実施、攪拌翼回転数150rpm 、
混和時間5分)、膜分離(図2に示すN2 が供給される
原液貯槽と膜透過部との間に循環ポンプにより循環液を
循環させる膜分離試験装置を使用、膜種類限外濾過膜、
分画分子量40000、材質ポリアクリルニトリル、透
過圧力2kg/cm2 、液温20〜22℃)、 (3)実験方法……浄化槽汚泥を回分遠心器で分離濃縮
し、固形物を排除した後、分離液にジャーテスタで凝集
剤を注入、その後混合液を膜分離する。膜分離では、1
/10まで濃縮し、この濃縮液と浄化槽汚泥を容量比
1:10で混合後、再度回分遠心器で分離濃縮する。凝
集フロック(膜分離濃縮液)を混合しない場合とした場
合について回分遠心器での濃縮液SS濃度を比較した。 (4)実験結果……凝集フロックを混合しない場合の濃
縮液SS濃度42100ppm 、混合した場合42700
ppm で両者ほとんど差はない。したがって、凝集フロッ
クを混合しても本来の機械的分離装置の分離濃縮機能に
支障はないことが確認された。
(1) Experimental sample (target liquid): septic tank sludge (Sampling the one that is carried into A human waste treatment plant), SS
Concentration 12300ppm, (2) Experimental equipment, conditions ... Mechanical separation (batch centrifuge, centrifugal rotation speed 3000 rpm, 10 minutes), coagulant (sulfuric acid band, injection rate 300ppm, pH 6.5 adjusted with NaOH, chemical mixture is jar) Conducted with a tester, stirring blade rotation speed 150 rpm,
Mixing time 5 minutes) Membrane separation (uses a membrane separation tester that circulates the circulating liquid by a circulation pump between the stock solution storage tank to which N 2 is supplied and the membrane permeation section shown in FIG. 2), ultrafiltration membrane ,
Fractional molecular weight 40,000, material polyacrylonitrile, permeation pressure 2 kg / cm 2 , liquid temperature 20-22 ° C), (3) Experimental method …… After separating and concentrating septic tank sludge with a batch centrifuge to remove solids, A coagulant is injected into the separated liquid with a jar tester, and then the mixed liquid is subjected to membrane separation. 1 for membrane separation
Concentrate to / 10, mix the concentrate with the septic tank sludge at a volume ratio of 1:10, and then separate and concentrate again with a batch centrifuge. The concentration of the concentrated solution SS in the batch centrifuge was compared when the flocculation flocs (membrane separation concentrated solution) were not mixed. (4) Experimental results: Concentrated solution SS concentration of 42100 ppm without mixing floc, 42700 with mixing
At ppm, there is almost no difference between the two. Therefore, it was confirmed that even if the flocculation flocs were mixed, the original separation and concentration function of the mechanical separation device was not hindered.

【0009】以上説明したように、本発明では機械的分
離装置における分離濃縮機能に何ら支障を来すことな
く、従来必要とされた機械的分離残渣と膜分離濃縮液を
混合処理するための混合装置が省略され、かつ、操作管
理が簡略化されると共に、発生する汚泥(機械的分離残
渣および凝集フロック)全体が減容化される。
As described above, according to the present invention, the mechanical separation residue and the membrane separation concentrate, which have been conventionally required, can be mixed without causing any trouble in the separation and concentration function of the mechanical separation device. The device is omitted, the operation and management is simplified, and the volume of sludge (mechanical separation residue and coagulated flocs) generated is reduced.

【0010】[0010]

【実施例】本発明の一実施例を、図1によって説明す
る。廃水1中の固形物の大半は、遠心分離機などの機械
的分離装置2で除去され、分離液に凝集剤(硫酸バンド
(硫酸アルミニウム)、高分子凝縮剤などの有機、無機
系凝縮剤)3を凝集反応装置4において注入することに
より、分離液中に残留する固形物、コロイド、および溶
解性物質の一部を凝集フロック中に取り込む。その上で
凝集フロックを限外濾過又は精密濾過の膜分離装置5で
分離し、処理水6を系外に排出する。一方、膜分離装置
5で分離された凝集フロックを含む濃縮液7は、前記機
械的分離装置2に循環され、ここで廃水中の固形物と共
に凝集フロックが分離混和される。この固形物と凝集フ
ロックが濃縮された機械的分離残渣(汚泥)8は、汚泥
処理装置10で処理される。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENT An embodiment of the present invention will be described with reference to FIG. Most of the solid matter in the wastewater 1 is removed by a mechanical separator 2 such as a centrifuge, and a coagulant (organic or inorganic condensing agent such as a sulfuric acid band (aluminum sulfate) or a polymer condensing agent) is added to the separated liquid. By injecting 3 in the flocculation reactor 4, a part of the solid matter, colloid, and soluble substance remaining in the separated liquid is taken into floc floc. Then, flocculated flocs are separated by the ultrafiltration or microfiltration membrane separation device 5, and the treated water 6 is discharged to the outside of the system. On the other hand, the concentrated liquid 7 containing agglomerated flocs separated by the membrane separator 5 is circulated to the mechanical separator 2 where the agglomerated flocs are separated and mixed with the solid matter in the wastewater. The mechanical separation residue (sludge) 8 in which the solid matter and the flocculated flocs are concentrated is treated by a sludge treatment device 10.

【0011】「作用」欄で説明したように、前記廃水中
の固形物と前記膜分離装置5で分離された凝集フロック
は、機械的分離装置2において充分に分離濃縮されるこ
とになる。
As described in the section "Operation", the solid flocs in the waste water and the floc aggregates separated by the membrane separator 5 are sufficiently separated and concentrated in the mechanical separator 2.

【0012】従って、本実施例では、機械的分離残渣と
膜分離濃縮液とを混合処理するための混合装置を省略す
ることができ、かつ、操作管理を簡略化することがで
き、また、発生する汚泥を減容化することができる。
Therefore, in the present embodiment, the mixing device for mixing the mechanical separation residue and the membrane separation concentrate can be omitted, and the operation management can be simplified, and the generation can be prevented. The volume of sludge to be used can be reduced.

【0013】[0013]

【発明の効果】以上説明したように、本発明は廃水中の
固形物を機械的分離装置によって除去した後、分離液に
凝集剤を注入して残留する固形物、コロイドおよび溶解
性物質の一部を凝集フロック化し、これを膜分離によっ
て分離する廃水処理方法において、凝集フロックを含む
膜分離濃縮液を機械的分離装置に循環させることによ
り、従来必要であった混合装置を省略することができ、
かつ、操作を簡略化することができる。また、凝集フロ
ックも廃水中の固形物と共に機械的分離装置で分離濃縮
されるので、発生汚泥を減容化することができる。
As described above, according to the present invention, after the solid matter in the wastewater is removed by the mechanical separation device, a coagulant is injected into the separated liquid to remove the residual solid matter, colloid and soluble substances. In a wastewater treatment method in which a portion is flocculated and separated by membrane separation, by circulating a membrane separation concentrate containing floc through a mechanical separation device, a mixing device that was conventionally required can be omitted. ,
In addition, the operation can be simplified. Further, since the floc of flocs is separated and concentrated by the mechanical separation device together with the solid matter in the wastewater, the volume of the generated sludge can be reduced.

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

【図1】本発明の一実施例の系統図である。FIG. 1 is a system diagram of an embodiment of the present invention.

【図2】本発明の効果確認のために用いられた膜分離試
験装置の系統図である。
FIG. 2 is a system diagram of a membrane separation test device used for confirming the effect of the present invention.

【図3】従来の廃水処理方法の系統図である。FIG. 3 is a system diagram of a conventional wastewater treatment method.

【符号の説明】[Explanation of symbols]

1 廃水 2 機械的分離装置 3 凝集剤 4 凝集反応装置 5 膜分離装置 6 処理水 7 膜分離濃縮液 8 機械的分離残渣 10 汚泥処理装置 1 Wastewater 2 Mechanical Separation Device 3 Coagulant 4 Coagulation Reaction Device 5 Membrane Separation Device 6 Treated Water 7 Membrane Separation Concentrated Liquid 8 Mechanical Separation Residue 10 Sludge Treatment Device

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 廃水中の固形物を機械的分離装置によっ
て除去した後、分離液に凝集剤を注入して残留する固形
物、コロイドおよび溶解性物質の一部を凝集フロック化
し、これを膜分離によって分離する廃水処理方法におい
て、凝集フロックを含む膜分離濃縮液を機械的分離装置
に循環させることを特徴とする廃水処理方法。
1. After removing the solid matter in the wastewater by a mechanical separation device, a coagulant is injected into the separated liquid to coagulate and flocculate a part of the remaining solid matter, colloid and soluble substances, and to form a membrane. In the wastewater treatment method of separating by separation, a membrane separation concentrate containing coagulated flocs is circulated through a mechanical separation device.
JP5095908A 1993-04-22 1993-04-22 Treatment of waste water Pending JPH06304571A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP5095908A JPH06304571A (en) 1993-04-22 1993-04-22 Treatment of waste water

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP5095908A JPH06304571A (en) 1993-04-22 1993-04-22 Treatment of waste water

Publications (1)

Publication Number Publication Date
JPH06304571A true JPH06304571A (en) 1994-11-01

Family

ID=14150397

Family Applications (1)

Application Number Title Priority Date Filing Date
JP5095908A Pending JPH06304571A (en) 1993-04-22 1993-04-22 Treatment of waste water

Country Status (1)

Country Link
JP (1) JPH06304571A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007524501A (en) * 2003-06-24 2007-08-30 カロロ エンジニアーズ, ピー・シー Wastewater treatment method and wastewater treatment system
JP2018075544A (en) * 2016-11-10 2018-05-17 王子ホールディングス株式会社 Apparatus and method for treating water

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007524501A (en) * 2003-06-24 2007-08-30 カロロ エンジニアーズ, ピー・シー Wastewater treatment method and wastewater treatment system
JP2018075544A (en) * 2016-11-10 2018-05-17 王子ホールディングス株式会社 Apparatus and method for treating water

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