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JP2019177351A5 - - Google Patents
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JP2019177351A5 - - Google Patents

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JP2019177351A5
JP2019177351A5 JP2018068478A JP2018068478A JP2019177351A5 JP 2019177351 A5 JP2019177351 A5 JP 2019177351A5 JP 2018068478 A JP2018068478 A JP 2018068478A JP 2018068478 A JP2018068478 A JP 2018068478A JP 2019177351 A5 JP2019177351 A5 JP 2019177351A5
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Prior art keywords
sludge
organic
dehydrating
coagulant
organic coagulant
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JP2018068478A
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JP6886426B2 (en
JP2019177351A (en
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有機性汚泥に高分子凝集剤を添加して前記有機性汚泥を凝集させる工程と、
前記凝集された汚泥を濃縮及び加圧脱水する工程と、
前記濃縮後又は前記加圧脱水後の汚泥に有機凝結剤を添加する工程と、
前記有機凝結剤が添加された汚泥を機械的に脱水する工程と、を含み、
前記有機凝結剤が添加された汚泥およびその脱水ろ液のうちの少なくとも一方のpHが6以上であり、前記濃縮及び加圧脱水された汚泥の蒸発残留物(TS)が40〜150g/Lであることを特徴とする有機性汚泥の脱水方法。
A step of adding a polymer flocculant to the organic sludge to coagulate the organic sludge;
A step of concentrating and pressure dehydrating the agglomerated sludge,
A step of adding an organic coagulant to the sludge after the concentration or after the pressure dehydration,
Mechanically dehydrating the sludge to which the organic coagulant has been added,
At least one of the sludge to which the organic coagulant is added and the dehydrated filtrate thereof has a pH of 6 or more, and the evaporation residue (TS) of the concentrated and pressurized dehydrated sludge is 40 to 150 g / L. A method for dehydrating organic sludge characterized by being present.
前記有機凝結剤は、pH4のカチオン度が5meq/g以上であることを特徴とする、請求項1に記載の有機性汚泥の脱水方法。   The method for dehydrating organic sludge according to claim 1, wherein the organic coagulant has a cation degree at pH 4 of 5 meq / g or more. 前記有機凝結剤は、25℃における原液の粘度が50mPa・s以上の液状であることを特徴とする、請求項1または2に記載の有機性汚泥の脱水方法。 The method for dehydrating organic sludge according to claim 1 or 2 , wherein the organic coagulant is a liquid having a stock solution viscosity at 25 ° C of 50 mPa · s or more. 前記有機凝結剤は、分子量が4000を超え150万以下であることを特徴とする、請求項1〜のいずれか1項に記載の有機性汚泥の脱水方法。 The organic coagulant is characterized by a molecular weight of 4000 to exceeding 1,500,000, method of dehydrating organic sludge of any one of claims 1-3. 前記有機凝結剤は、無希釈もしくは希釈倍率60倍以下に希釈した溶液として添加することを特徴とする、請求項1〜のいずれか1項に記載の有機性汚泥の脱水方法。 The organic coagulant is characterized by adding as a solution diluted to 60-fold undiluted or dilution, method of dehydrating organic sludge of any one of claims 1-4. 有機性汚泥に高分子凝集剤を添加して前記有機性汚泥を凝集させる凝集手段と、
前記凝集された汚泥を濃縮する濃縮手段と、
前記濃縮された汚泥を加圧脱水する加圧脱水手段と、
前記濃縮後又は前記加圧脱水後の汚泥に有機凝結剤を添加する有機凝結剤添加手段と、
前記有機凝結剤が添加された汚泥を機械的に脱水する脱水手段と、を含み、
前記有機凝結剤が添加された汚泥およびその脱水ろ液のうちの少なくとも一方のpHが6以上であり、前記濃縮及び加圧脱水された汚泥の蒸発残留物(TS)が40〜150g/Lであることを特徴とする有機性汚泥の脱水に用いる処理装置。
A flocculation means for flocculating the organic sludge by adding a polymer flocculant to the organic sludge,
Concentrating means for concentrating the agglomerated sludge,
Pressure dewatering means for dewatering the concentrated sludge under pressure,
An organic coagulant adding means for adding an organic coagulant to the sludge after the concentration or after the pressure dehydration,
Dewatering means for mechanically dehydrating the sludge to which the organic coagulant is added,
At least one of the sludge to which the organic coagulant is added and the dehydrated filtrate thereof has a pH of 6 or more, and the evaporation residue (TS) of the concentrated and pressurized dehydrated sludge is 40 to 150 g / L. A treatment device used for dehydration of organic sludge, which is characterized by being present.
前記濃縮・加圧脱水手段と前記有機凝結剤添加手段との間に設けられ、前記濃縮及び加圧脱水後の汚泥を分断して少なくともブロック状に形成する分断手段を有することを特徴とする、請求項に記載の有機性汚泥の脱水に用いる処理装置。 Characterized in that it has a dividing means which is provided between the concentration / pressure dewatering means and the organic coagulant addition means and divides the sludge after the concentration and pressure dewatering to form at least a block. A treatment apparatus used for dehydrating the organic sludge according to claim 6 .
JP2018068478A 2018-03-30 2018-03-30 Dehydration method of organic sludge and treatment equipment used for this Active JP6886426B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2018068478A JP6886426B2 (en) 2018-03-30 2018-03-30 Dehydration method of organic sludge and treatment equipment used for this

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2018068478A JP6886426B2 (en) 2018-03-30 2018-03-30 Dehydration method of organic sludge and treatment equipment used for this

Publications (3)

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JP2019177351A JP2019177351A (en) 2019-10-17
JP2019177351A5 true JP2019177351A5 (en) 2020-04-30
JP6886426B2 JP6886426B2 (en) 2021-06-16

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Family Cites Families (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS58223500A (en) * 1982-06-21 1983-12-26 Ebara Infilco Co Ltd Treatment of organic sludge
US4792406A (en) * 1988-05-23 1988-12-20 Nalco Chemical Company Method for dewatering a slurry using a twin belt press with cationic amine salts
JPH06343999A (en) * 1993-06-10 1994-12-20 Kubota Corp Sludge dewatering method
JPH06344000A (en) * 1993-06-10 1994-12-20 Kubota Corp Sludge dewatering method
JPH10230299A (en) * 1997-02-21 1998-09-02 Nippon Shokubai Co Ltd Dehydrating method of sludge
JP5882608B2 (en) * 2011-06-21 2016-03-09 水ing株式会社 Method and apparatus for dewatering organic sludge
JP2013233509A (en) * 2012-05-09 2013-11-21 Swing Corp Method and apparatus of dehydration of organic sludge

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