JPH10156391A - Treatment of phosphorus recovered from treated water of sewerage - Google Patents
Treatment of phosphorus recovered from treated water of sewerageInfo
- Publication number
- JPH10156391A JPH10156391A JP32063696A JP32063696A JPH10156391A JP H10156391 A JPH10156391 A JP H10156391A JP 32063696 A JP32063696 A JP 32063696A JP 32063696 A JP32063696 A JP 32063696A JP H10156391 A JPH10156391 A JP H10156391A
- Authority
- JP
- Japan
- Prior art keywords
- sludge
- phosphorus
- insoluble
- chloride
- treated water
- 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.)
- Granted
Links
Landscapes
- Removal Of Specific Substances (AREA)
- Treatment Of Sludge (AREA)
Abstract
Description
【0001】[0001]
【発明の属する技術分野】本発明は、下水処理場等の処
理水中に含有され、そのまま放流されている溶解性リン
を不溶性のリン化合物として汚泥ともに回収した後、汚
泥を緑農地等へ有機質肥料として再利用を図る場合、不
溶性リン化合物を再び溶解性リンに変化させると同時
に、汚泥中の重金属類を不溶性硫化物とする方法に関す
るものである。The present invention relates to a method for recovering soluble phosphorus contained in treated water from a sewage treatment plant or the like and being discharged as it is together with sludge as an insoluble phosphorus compound, and then transferring the sludge to green agricultural land or the like. The present invention relates to a method for converting an insoluble phosphorus compound into soluble phosphorus again while simultaneously converting heavy metals in sludge into insoluble sulfide.
【0002】[0002]
【従来の技術】下水処理場においては、流入する汚水の
懸濁物を沈降分離したのち、活性汚泥を用いて汚水中の
溶解性物質を基準値以下に浄化して公共水域に放流する
仕組みとなっている。しかし、活性汚泥法においては、
流入する全リン量を除去することは困難で、流入リン量
の約45〜50%が処理水に含まれ、公共水域へ放流さ
れているのが通常である。また、公共水域へは、農業排
水及び生活廃水などの汚水も直接流入し、水質汚濁及び
水質悪化が問題となっている状況下にあって、下水処理
場から排出される放流水も極力リン及び窒素などの栄養
素となる物質が少量であることが望まれる。一方、放流
水中に含まれるリンを減少させるため、流入汚水に硫酸
鉄、塩化鉄などの鉄塩、または、ポリ塩化アルミ、硫酸
アルミなどのアルミ塩類を添加して、汚水中の溶解性リ
ンを不溶性のリン酸化合物とした後、活性汚泥処理を行
い、不溶化したリンを汚泥に混入させて回収する方法も
実施されている。この方法で回収されたリンは不溶性で
あるため、汚泥をコンポスト化し、緑農地等へ施肥する
場合は、リンの肥効性が低下したものとなる。2. Description of the Related Art In a sewage treatment plant, after a suspended sediment of inflowing sewage is settled and separated, activated sludge is used to purify soluble substances in the sewage to a standard value or less and discharge the same to public waters. Has become. However, in the activated sludge method,
It is difficult to remove the total amount of inflowing phosphorus, and about 45 to 50% of the amount of inflowing phosphorus is usually contained in treated water and discharged to public waters. In addition, sewage such as agricultural wastewater and domestic wastewater flows directly into public waters, and water pollution and deterioration of water quality are becoming a problem. It is desirable that the amount of nutrients such as nitrogen be small. On the other hand, iron salts such as iron sulfate and iron chloride, or aluminum salts such as polyaluminum chloride and aluminum sulfate are added to the influent wastewater to reduce the amount of phosphorus contained in the wastewater. A method has also been practiced in which after an insoluble phosphoric acid compound is formed, an activated sludge treatment is performed, and the insolubilized phosphorus is mixed into the sludge and recovered. Since the phosphorus recovered by this method is insoluble, when composting sludge and applying it to green farmland or the like, the effectiveness of phosphorus is reduced.
【0003】[0003]
【発明が解決しようとする課題】近年、公共水域及び閉
鎖水域に窒素及びリンなどの栄養素を含む汚水が多量に
流入し、水生植物及び藻類微生物の異常増殖によっても
たらされる水質の悪化が問題となっている。これらの水
域の水質悪化の防止には、流入する汚水を削減させると
ともに、集約処理がなされている下水処理場からの放流
水中に含まれる窒素及びリンを極力減少させることが重
要である。しかしながら現在、下水処理場において実施
されている活性汚泥を用いる汚水処理方法では、流入す
るリンの全量を除去することは困難で、流入するリン量
の約45〜50%が処理水として放流されているのが通
常である。In recent years, a large amount of sewage containing nutrients such as nitrogen and phosphorus flows into public waters and closed waters, and the deterioration of water quality caused by abnormal growth of aquatic plants and algal microorganisms has become a problem. ing. In order to prevent the deterioration of water quality in these water areas, it is important to reduce inflowing sewage and to reduce nitrogen and phosphorus contained in effluent discharged from sewage treatment plants where intensive treatment is performed as much as possible. However, in the sewage treatment method using activated sludge currently being carried out in a sewage treatment plant, it is difficult to remove the entire amount of inflowing phosphorus, and about 45 to 50% of the amount of inflowing phosphorus is discharged as treated water. Is usually there.
【0004】一方、処理水の放流水域が、閉鎖水域であ
ったり、また、土水取水水域と併用する場合などでは、
下水処理工程で鉄塩またはアルミニウム塩類を添加し
て、不溶性リン化合物として放流水中の溶解性リンを除
去する方法が一部では実施されているが、この方法が実
施されている下水処理場で発生する汚泥を有機質肥料と
して再利用する場合は、汚泥中のリンが不溶性であるた
め、リンの肥効性が低下したものとなっている。On the other hand, when the treated water discharge water area is a closed water area, or when used together with a soil water intake water area,
In some sewage treatment processes, iron salts or aluminum salts are added to remove soluble phosphorus in the effluent as an insoluble phosphorus compound. When sludge is reused as an organic fertilizer, the phosphorus in the sludge is insoluble, so that the phosphorus fertilizing effect is reduced.
【0005】本発明者等は、これらの問題点に着目し、
下水処理場からの放流水中に含まれるリンを大幅に削減
させ、しかも回収したリンを可溶性に変化させ、汚泥を
緑農地等への有機質肥料として再利用する場合、リンの
肥効性を向上させるとともに汚泥中に含まれる重金属類
を不溶性の硫化物とする経済的な方法を提供しようとす
るものである。The present inventors have paid attention to these problems,
Significantly reduce the phosphorus contained in the effluent from the sewage treatment plant, and improve the fertilizing effect of phosphorus when the recovered phosphorus is changed to soluble and the sludge is reused as organic fertilizer for green farmland etc. Another object is to provide an economical method for converting heavy metals contained in sludge into insoluble sulfide.
【0006】[0006]
【課題を解決するための手段】下水処理場にて汚水を活
性汚泥を用いて浄化した処理水を最終沈殿池にて懸濁物
を沈降分離した上澄水には、流入リン量の約45〜50
%が含まれ、このまま放流されている。そして、放流水
中に含まれるリンの約60〜70%が溶解性のリン酸イ
オン(PO4-3 )である。この溶解性リンイオンを、不
溶性の化合物として凝集沈殿させ分離すれば、放流水中
のリンを大幅に削減させることが可能であることが容易
に予測される。溶解性リンイオンを不溶性化合物とする
方法として、カルシウム塩類、または、マグネシウム塩
類を添加する方法、及び鉄塩類、アルミニウム塩類を添
加する方法などがあるが、溶解性リン酸イオンとの反応
性及び取扱い性、そして、後述する処理方法を考慮する
と、塩化第一鉄(Fecl2 )及び塩化第二鉄(Fec
l3 )を用いる方法が最も適性である。Means for Solving the Problems The treated water obtained by purifying sewage using activated sludge at a sewage treatment plant is added to the supernatant water obtained by settling and separating a suspended substance in a final sedimentation basin. 50
% Is released as it is. Approximately 60 to 70% of the phosphorus contained in the effluent is soluble phosphate ions (PO4-3). It is easily predicted that if this soluble phosphorus ion is coagulated and precipitated as an insoluble compound and separated, the phosphorus in the effluent can be significantly reduced. As a method for converting soluble phosphorus ions into an insoluble compound, there are a method of adding calcium salts or magnesium salts, and a method of adding iron salts and aluminum salts. Considering the processing method described later, ferrous chloride (Fecl2) and ferric chloride (Fec2)
The method using l3) is the most suitable.
【0007】下水処理水が最終沈殿池へ入る前工程にお
いて、処理水に塩化第一鉄または塩化第二鉄を添加する
と、溶解性リン酸イオンは、リン酸第一鉄(Fe3(P
o4)2 )またはリン酸第二鉄(FePo4) を生成
し、最終沈殿池で処理液中に含まれる汚泥とともに沈殿
する。通常は、最終沈殿池汚泥は最初沈殿池汚泥と混合
され、濃縮工程を経て汚泥調質された後、脱水機を用い
て固液分離される。固液分離された脱水汚泥を緑農地等
への有機質肥料として再利用する場合、汚泥に含まれる
重金属類、特に最も多く含まれる亜鉛などが少ないこと
が重要となる。[0007] When ferrous chloride or ferric chloride is added to the treated water in a process before the sewage treated water enters the final sedimentation basin, the soluble phosphate ion becomes ferrous phosphate (Fe3 (P
o4) 2) or ferric phosphate (FePo4) is generated and sedimented in the final sedimentation tank together with the sludge contained in the treatment liquid. Usually, the final sedimentation tank sludge is first mixed with the sedimentation tank sludge, subjected to sludge conditioning through a concentration step, and then subjected to solid-liquid separation using a dehydrator. When the dewatered sludge separated into solid and liquid is reused as an organic fertilizer for green farmland and the like, it is important that the sludge contains a small amount of heavy metals, particularly zinc, which is most frequently contained.
【0008】本発明者は、汚泥中に含まれる重金属類、
特に亜鉛を除去する方法として、濃縮汚泥に塩化第二鉄
と次亜塩素酸ソーダを添加して溶出させて分離除去する
方法を開発しており、この方法で処理することによっ
て、汚泥中の亜鉛は大幅に除去されたものとなる。しか
し、この方法で処理した脱水汚泥中にも重金属類及び亜
鉛が塩化物の形で少量残存するため、この残存する金属
塩化物を不溶性の硫化物としておくことが重要である。
以上記述したように、下水処理場から排出される放流水
から溶解性リンを回収し、しかも重金属類、特に亜鉛の
除去を行なった脱水汚泥は、不溶性のリン酸鉄化合物と
残留した少量の重金属塩化物及び亜鉛塩化物を含む組織
となっている。The present inventor has proposed that heavy metals contained in sludge,
In particular, as a method for removing zinc, a method has been developed to add ferric chloride and sodium hypochlorite to concentrated sludge and elute it to separate and remove it.By treating with this method, zinc in sludge is removed. Is largely removed. However, heavy metals and zinc also remain in the form of chlorides in small amounts in the dewatered sludge treated by this method, and it is important to convert the remaining metal chlorides into insoluble sulfides.
As described above, dehydrated sludge obtained by recovering soluble phosphorus from effluent discharged from a sewage treatment plant and removing heavy metals, particularly zinc, is insoluble iron phosphate compound and a small amount of residual heavy metal. It has a structure containing chloride and zinc chloride.
【0009】この脱水汚泥に、別途硫化鉄と塩酸によっ
て生成させた硫化水素を反応させると、不溶性のリン酸
鉄化合物は、硫化鉄と可溶性のリン酸を生成する。一
方、重金属類塩化物及び亜鉛塩化物は、不溶性の硫化物
になる。そして、硫化鉄と塩酸より硫化水素を生成させ
た残渣は、塩化第一鉄となっているので、この塩化第一
鉄は放流水中から溶解性リン酸イオンを回収するために
循環利用することができる。When the dehydrated sludge is separately reacted with hydrogen sulfide generated by iron sulfide and hydrochloric acid, the insoluble iron phosphate compound generates iron sulfide and soluble phosphoric acid. On the other hand, heavy metal chlorides and zinc chlorides become insoluble sulfides. Since the residue from the production of hydrogen sulfide from iron sulfide and hydrochloric acid is ferrous chloride, this ferrous chloride can be recycled to recover soluble phosphate ions from the effluent. it can.
【0010】[0010]
【発明の実施の形態】従来、溶解性リンを不溶性塩とし
て凝集沈殿分離する場合、溶解性リン濃度が希薄である
ものは回収が困難であるといわれている。そして、下水
処理場から排出される放流水中のリン濃度も、数ppm
〜数十ppmで希薄であるので、放流水に鉄塩を添加し
て凝集沈殿分離する方法は、非常に回収率の低いものと
なる。しかし、下水処理場工程において、最終沈殿池へ
入る前の処理水中には、曝気槽からの汚泥粒子が多量に
含まれているので、最終沈殿池に入る直前に鉄塩を添加
することによって、生成したリン酸鉄は、汚泥粒子に付
着または凝集フロックを生成したりして、共沈し、効率
良く沈降分離することが可能となる。DESCRIPTION OF THE PREFERRED EMBODIMENTS Conventionally, it is said that when soluble phosphorus is subjected to coagulation precipitation and separation as an insoluble salt, those having a low soluble phosphorus concentration are difficult to recover. And the concentration of phosphorus in the effluent discharged from the sewage treatment plant is also several ppm.
Since it is diluted at a concentration of about several tens of ppm, the method of adding an iron salt to the effluent for coagulation, sedimentation and separation has a very low recovery rate. However, in the sewage treatment plant process, the treated water before entering the final sedimentation basin contains a large amount of sludge particles from the aeration tank, so by adding an iron salt immediately before entering the final sedimentation basin, The generated iron phosphate adheres to sludge particles or generates flocculated floc, coprecipitates, and can be efficiently settled and separated.
【0011】更に、従来は沈降しなかった汚泥微粒子
も、塩化鉄による凝集フロックを生成し、沈降分離する
ことができるようになり、放流水の水質向上ともなる。
この様に、鉄塩を添加して回収したリン酸鉄は不溶性で
あるので、脱水汚泥を有機質肥料として利用する場合
は、リンの肥料効果が低いものとなっているので、可溶
性のリン化合物に変える必要がある。また、汚泥中の重
金属類及び亜鉛を塩化第二鉄と次亜塩素酸ソーダを用い
て処理した脱水汚泥は、可溶性の金属塩化物となってい
るので、不溶性化合物としなければ除去効果が減少する
こととなる。Furthermore, sludge fine particles which have not settled conventionally can also form flocculated flocks of iron chloride and can be settled and separated, thereby improving the quality of the discharged water.
In this way, the iron phosphate added and recovered is insoluble, so when dewatered sludge is used as an organic fertilizer, the fertilizer effect of phosphorus is low. I need to change. In addition, dehydrated sludge obtained by treating heavy metals and zinc in sludge with ferric chloride and sodium hypochlorite is a soluble metal chloride, so the removal effect is reduced unless it is made an insoluble compound. It will be.
【0012】このような目的を達成するためには、脱水
汚泥と硫化水素を反応させれば、リン酸鉄は可溶性のリ
ン酸となり、金属塩化物は不溶性の硫化物となる。そし
て、硫化鉄と塩酸の反応によって硫化水素と塩化第一鉄
が生成するので、塩化第一鉄はリン酸の回収薬剤として
循環使用する。上記の作用を化学式を用いて記述すると
以下の通りである。In order to achieve the above object, if dehydrated sludge is reacted with hydrogen sulfide, iron phosphate becomes soluble phosphoric acid, and metal chloride becomes insoluble sulfide. Then, since hydrogen sulfide and ferrous chloride are generated by the reaction between iron sulfide and hydrochloric acid, ferrous chloride is circulated and used as a collecting agent for phosphoric acid. The above action is described using a chemical formula as follows.
【0013】[0013]
【化1】 Embedded image
【0014】[0014]
【化2】 Embedded image
【0015】[0015]
【化3】 Embedded image
【0016】[0016]
【化4】 Embedded image
【0017】[0017]
【実施例】本発明を実施するためのフローを示すと図1
の通りである。図1において、初沈・曝気槽・終沈は、
下水処理場の汚水処理工程を示すもので、流入汚水Aは
活性汚泥を用いたこの工程を経て処理放流Bされる。こ
の処理工程中、初沈から初沈汚泥が、終沈から余剰汚泥
が発生し、この両者を合わせて重力濃縮され、混合生汚
泥となる。DESCRIPTION OF THE PREFERRED EMBODIMENTS FIG. 1 shows a flow for carrying out the present invention.
It is as follows. In Fig. 1, the initial settling, aeration tank, and final settling are
This shows a sewage treatment process in a sewage treatment plant, and inflow sewage A is treated and discharged B through this process using activated sludge. During this treatment step, initial sludge is generated from the initial settling, and excess sludge is generated from the final settling. Both of them are concentrated by gravity to form mixed raw sludge.
【0018】この混合生汚泥に塩化第二鉄と次亜塩素酸
ソーダを添加し、汚泥中の重金属類、特に亜鉛化合物を
溶出させる。溶出処理を行なった汚泥をアルカリ剤を用
いてPH調整を行ない、脱水機を用いて脱水操作を行な
い、重金属類、特に亜鉛含有量を削減させた脱水ケーキ
と、溶出分離した重金属類及び亜鉛を多く含有した脱水
ろ液を得る。Ferric chloride and sodium hypochlorite are added to the mixed raw sludge to elute heavy metals, particularly zinc compounds, in the sludge. The pH of the sludge that has been subjected to the elution treatment is adjusted using an alkali agent, and a dehydration operation is performed using a dehydrator. Heavy metals, particularly a dehydrated cake having a reduced zinc content, and heavy metals and zinc that have been eluted and separated are separated. A dehydrated filtrate containing a large amount is obtained.
【0019】脱水ケーキには、別途硫化鉄と塩酸によっ
て発生させた硫化水素を通じて、脱水ケーキに含まれる
重金属類及び亜鉛を不溶性の硫化物とすると同時に、リ
ン酸鉄を可溶性のリン酸に変える。この硫化操作を行な
った脱水ケーキをアルカリ剤で中和し、肥料及びコンポ
スト化等の対応が容易なものとする。In the dewatered cake, heavy metals and zinc contained in the dewatered cake are converted into insoluble sulfides and iron phosphate is converted into soluble phosphoric acid through hydrogen sulfide separately generated by iron sulfide and hydrochloric acid. The dewatered cake subjected to the sulfidation operation is neutralized with an alkali agent to facilitate handling of fertilizer and composting.
【0020】一方、分離した重金属類及び亜鉛を多く含
む脱水ろ液は、アルカリ剤で中和し、溶解している重金
属類及び亜鉛を水酸化物として析出、沈殿させたのち、
脱水して重金属類及び亜鉛を多量に含む脱水ケーキを分
離回収する。この操作で発生する分離水は、清澄となる
ので、濃縮槽へ返送し、濃縮分離水と合わせて処理す
る。また、硫化鉄と塩酸を用いて硫化水素を発生させた
残渣は、塩化第一鉄であるので、この塩化第一鉄を終沈
でのリン酸の回収に再利用する。On the other hand, the separated dehydrated filtrate containing a large amount of heavy metals and zinc is neutralized with an alkali agent to precipitate and precipitate dissolved heavy metals and zinc as hydroxides.
After dehydration, a dehydrated cake containing a large amount of heavy metals and zinc is separated and collected. Since the separated water generated by this operation becomes clear, the separated water is returned to the concentration tank and treated together with the concentrated separated water. Further, since the residue from the generation of hydrogen sulfide using iron sulfide and hydrochloric acid is ferrous chloride, this ferrous chloride is reused for the recovery of phosphoric acid in the final precipitation.
【0021】[0021]
【発明の効果】本方法を行なうことによって、下水処理
場から排出されるリンを大幅に減少させることができ、
しかも、汚泥中の重金属類を削減させ、特に亜鉛の殆ど
を除去することが可能となり、残留した重金属類を不溶
性化し、更に有機質肥料として脱水ケーキを再利用する
場合、リン化合物の可溶性によって肥料効果を向上させ
ることができる。According to the present invention, phosphorus discharged from a sewage treatment plant can be significantly reduced,
Moreover, it is possible to reduce heavy metals in the sludge, in particular to remove most of the zinc, to make the remaining heavy metals insoluble, and to reuse the dehydrated cake as an organic fertilizer. Can be improved.
【図1】この発明に係る方法のフロー図である。FIG. 1 is a flow chart of a method according to the present invention.
Claims (2)
加し、含まれる溶解性リンを不溶性金属化合物として最
終沈殿池の汚泥と一緒に回収し、回収した汚泥に塩化第
二鉄及び次亜塩素酸ソーダを添加して汚泥中の重金属化
合物類を溶出させたのち固液分離し、不溶性のリン酸鉄
化合物、重金属塩化物および塩化亜鉛を含有した分離汚
泥に、硫化水素を反応させて不溶性リン酸化合物を溶解
性のリン酸とし、重金属類塩化物および塩化亜鉛を不溶
性の硫化物とする下水処理水から回収したリンの処理方
法。1. A metal salt is added to treated water of a sewage treatment plant or the like, and soluble phosphorus contained therein is recovered as an insoluble metal compound together with the sludge of the final sedimentation basin. Sodium chlorite is added to elute heavy metal compounds in the sludge, followed by solid-liquid separation, and hydrogen sulfide is reacted with the separated sludge containing the insoluble iron phosphate compound, heavy metal chloride and zinc chloride. A method for treating phosphorus recovered from sewage water in which an insoluble phosphate compound is soluble phosphoric acid and heavy metals chloride and zinc chloride are insoluble sulfides.
化物および塩化亜鉛を含有した分離汚泥に反応させる硫
化水素を硫化鉄と塩酸とを反応させて生ずる硫化水素と
し、このとき、同時に生ずる塩化第一鉄を溶解性リンを
不溶性金属化合物とするための金属塩類として使用する
ことを特徴とする請求項1記載の下水処理水から回収し
たリンの処理方法。2. The hydrogen sulfide to be reacted with the separated sludge containing the insoluble iron phosphate compound, heavy metal chloride and zinc chloride is hydrogen sulfide produced by reacting iron sulfide and hydrochloric acid. The method for treating phosphorus recovered from sewage treatment water according to claim 1, wherein ferrous iron is used as a metal salt for converting soluble phosphorus into an insoluble metal compound.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP32063696A JP3277832B2 (en) | 1996-12-02 | 1996-12-02 | Method for treating phosphorus recovered from sewage treatment water |
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JP32063696A JP3277832B2 (en) | 1996-12-02 | 1996-12-02 | Method for treating phosphorus recovered from sewage treatment water |
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JP3277832B2 JP3277832B2 (en) | 2002-04-22 |
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Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2004330039A (en) * | 2003-05-06 | 2004-11-25 | Ngk Insulators Ltd | Recovery method of phosphorus and coagulant |
WO2011146871A3 (en) * | 2010-05-20 | 2012-04-19 | Essential Water LLC | Method and system for providing effluent from at least one wastewater treatment plant |
CN107879501A (en) * | 2017-09-28 | 2018-04-06 | 内蒙古君正化工有限责任公司 | A kind of method of the recovery containing sodium hypochlorite waste water |
WO2020152896A1 (en) * | 2019-01-21 | 2020-07-30 | 株式会社島津製作所 | Water quality analyzer and water quality analysis method |
CN115180785A (en) * | 2022-07-25 | 2022-10-14 | 爱沃特智慧水务(安徽)有限公司 | Method for synchronously recycling phosphorus and iron from chemical phosphorus removal sludge of sewage plant |
-
1996
- 1996-12-02 JP JP32063696A patent/JP3277832B2/en not_active Expired - Fee Related
Cited By (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2004330039A (en) * | 2003-05-06 | 2004-11-25 | Ngk Insulators Ltd | Recovery method of phosphorus and coagulant |
WO2011146871A3 (en) * | 2010-05-20 | 2012-04-19 | Essential Water LLC | Method and system for providing effluent from at least one wastewater treatment plant |
CN103189582A (en) * | 2010-05-20 | 2013-07-03 | 艾森索水业有限责任公司 | Method and system for providing effluent from at least one wastewater treatment plant |
US8815093B2 (en) | 2010-05-20 | 2014-08-26 | Essential Water LLC | Method and system for providing effluent from at least one wastewater treatment plant |
CN107879501A (en) * | 2017-09-28 | 2018-04-06 | 内蒙古君正化工有限责任公司 | A kind of method of the recovery containing sodium hypochlorite waste water |
WO2020152896A1 (en) * | 2019-01-21 | 2020-07-30 | 株式会社島津製作所 | Water quality analyzer and water quality analysis method |
JPWO2020152896A1 (en) * | 2019-01-21 | 2021-11-11 | 株式会社島津製作所 | Water quality analyzer and water quality analysis method |
CN115180785A (en) * | 2022-07-25 | 2022-10-14 | 爱沃特智慧水务(安徽)有限公司 | Method for synchronously recycling phosphorus and iron from chemical phosphorus removal sludge of sewage plant |
CN115180785B (en) * | 2022-07-25 | 2023-12-22 | 爱沃特智能水务(安徽)有限公司 | Method for synchronously recycling phosphorus and iron from chemical phosphorus removal sludge of sewage plant |
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JP3277832B2 (en) | 2002-04-22 |
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