JP2001205298A - Method for treating sewage sludge - Google Patents

Method for treating sewage sludge

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Publication number
JP2001205298A
JP2001205298A JP2000014644A JP2000014644A JP2001205298A JP 2001205298 A JP2001205298 A JP 2001205298A JP 2000014644 A JP2000014644 A JP 2000014644A JP 2000014644 A JP2000014644 A JP 2000014644A JP 2001205298 A JP2001205298 A JP 2001205298A
Authority
JP
Japan
Prior art keywords
sludge
concentration
phosphorus
microorganisms
sewage
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
Application number
JP2000014644A
Other languages
Japanese (ja)
Other versions
JP3705064B2 (en
Inventor
Yuji Furuya
勇治 古屋
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.)
Fuji Electric Co Ltd
Original Assignee
Fuji Electric Co 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 Fuji Electric Co Ltd filed Critical Fuji Electric Co Ltd
Priority to JP2000014644A priority Critical patent/JP3705064B2/en
Publication of JP2001205298A publication Critical patent/JP2001205298A/en
Application granted granted Critical
Publication of JP3705064B2 publication Critical patent/JP3705064B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Abstract

PROBLEM TO BE SOLVED: To provide a method for treating sewage sludge which solved the problem that when nitrate nitrogen and dissolved oxygen in the sludge are eliminated in the process of concentration and dewatering, phosphorus which was accumulated and fixed as polyphosphoric acid in the cells of microorganisms is released into water as orthophosphoric acid to increase the phosphorus concentration of wastewater. SOLUTION: In the method for treating sewage sludge generated in sewage works, in which phosphorus is removed biologically, comprising a concentration treatment process, a dewatering treatment process, and a drying or incineration treatment process, the sludge is concentrated and, without being allowed to stand at ordinary temperature for a long time, refrigerated while nitrate nitrogen is left in the sludge. In this way, the cell membranes of microorganisms in the sludge are broken so that phosphorus contained in the microorganisms is fixed as polyphosphoric acid, and the refrigerated sludge is melted, dewatered, and dried or incinerated.

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、下水・産業排水処
理など生物学的にリンを除去している活性汚泥処理過程
で発生するリンを高濃度に含有している下水汚泥の処理
方法に関する。
The present invention relates to a method for treating sewage sludge containing a high concentration of phosphorus generated in an activated sludge treatment process for biologically removing phosphorus such as sewage and industrial wastewater treatment.

【0002】[0002]

【従来の技術】一般に、下水処理場の最終沈殿池から排
出される汚泥は、まず重力濃縮、遠心濃縮、浮上濃縮な
どによって濃縮処理され、次にベルトプレス脱水、遠心
脱水、加圧脱水などにより脱水処理され、その後コンポ
スト、汚泥乾燥、汚泥焼却などの処理がされている。特
に、リン除去を生物学的に行っている高度下水処理場で
は、高濃度のリンが含有している汚泥を濃縮処理、脱水
処理するために、この過程で排出される排水にリンが高
濃度に含有することが問題となっている。
2. Description of the Related Art Generally, sludge discharged from a final sedimentation basin of a sewage treatment plant is first concentrated by gravity concentration, centrifugal concentration, flotation concentration, etc., and then by belt press dehydration, centrifugal dehydration, pressure dehydration, etc. It is dehydrated and then treated such as compost, sludge drying and sludge incineration. In particular, in advanced sewage treatment plants that biologically remove phosphorus, the sludge containing high concentration of phosphorus is concentrated and dewatered. Is a problem.

【0003】従来の下水汚泥の処理では、汚泥をコンポ
スト、埋立て、焼却などに利用し易い形で含水率を制御
することに主な目的がおかれ、濃縮処理や脱水処理過程
で発生する排水は、下水処理場の流入端へ返送して下水
処理場への流入水として処理されていた。高度下水処理
が普及し始め、下水汚泥にリンが高濃度に含有している
場合、濃縮処理や脱水処理で発生する排水は、下水処理
場の新たなリン負荷となり、リン除去に対する安定した
運転を妨げている。
[0003] In the conventional treatment of sewage sludge, the main purpose is to control the water content in such a manner that the sludge can be easily used for composting, landfilling and incineration, etc. Was returned to the inflow end of the sewage treatment plant and treated as inflow water to the sewage treatment plant. When advanced sewage treatment has begun to spread and sewage sludge contains a high concentration of phosphorus, the wastewater generated by the concentration and dehydration treatments will add a new phosphorus load to the sewage treatment plant, and ensure stable operation for phosphorus removal. Hindering.

【0004】[0004]

【発明が解決しようとする課題】最終沈殿池から排出さ
れる汚泥は、一日数回排出され、一定期間一定量蓄積さ
れた後に重力濃縮、遠心濃縮、浮上濃縮などによって濃
縮処理され、ベルトプレス脱水、遠心脱水、加圧脱水な
どにより脱水処理が行われる。この濃縮処理から脱水処
理過程の間も、汚泥中の微生物は活動しており、硝酸性
窒素、溶存酸素が汚泥中に存在しなくなると、微生物は
ポリリン酸として微生物細胞内に蓄積・固定化していた
リンを、オルトリン酸として水中に放出してしまい、濃
縮処理、脱水処理で発生する排水中に、オルトリン酸と
してリンが高濃度で含まれるという問題がある。
The sludge discharged from the final sedimentation basin is discharged several times a day, accumulated in a certain amount for a certain period, concentrated by gravity concentration, centrifugal concentration, flotation concentration, etc., and dewatered by belt press. The dehydration treatment is performed by centrifugal dehydration, pressure dehydration and the like. During the period from this concentration process to the dehydration process, the microorganisms in the sludge are active, and when nitrate nitrogen and dissolved oxygen are no longer present in the sludge, the microorganisms are accumulated and immobilized in the microbial cells as polyphosphoric acid. The resulting phosphorus is released into the water as orthophosphoric acid, and there is a problem that high concentrations of phosphorus as orthophosphoric acid are contained in wastewater generated by the concentration treatment and the dehydration treatment.

【0005】本発明は、下水汚泥を最終沈殿池から排出
して、濃縮処理、脱水処理を行う過程で、汚泥中のポリ
リン酸がオルトリン酸として水中に放出されることを抑
える下水汚泥の処理方法を提供することにある。
[0005] The present invention provides a method for treating sewage sludge which suppresses release of polyphosphoric acid in the sludge as orthophosphoric acid into water in the process of discharging sewage sludge from a final sedimentation tank and performing concentration treatment and dehydration treatment. Is to provide.

【0006】[0006]

【課題を解決するための手段】上記の課題は、生物学的
にリンを除去している下水処理場から発生する下水汚泥
を、濃縮処理過程、脱水処理過程、乾燥または焼却処理
過程とを有する下水汚泥の処理方法において、下水汚泥
を濃縮後、長時間にわたり常温のまま放置せず、汚泥中
の硝酸性窒素残留中に、微生物が活動を停止する温度範
囲に保持する処理、または凍結処理を行うことによって
達成される。ここで、微生物が活動を停止する温度は、
一般には下水を凍結する温度よりは高い。
The object of the present invention is to concentrate, dehydrate, dry or incinerate sewage sludge generated from a sewage treatment plant that biologically removes phosphorus. In the method of treating sewage sludge, after concentrating the sewage sludge, do not leave it at room temperature for a long time, and keep the temperature within the temperature range where microorganisms stop, or freeze, while nitrate nitrogen remains in the sludge. Achieved by doing. Here, the temperature at which the microorganism stops its activity is
Generally higher than the temperature at which sewage freezes.

【0007】微生物の活動を停止する温度範囲に保持す
ることにより、汚泥中のポリリン酸がオルトリン酸とし
て水中に放出されることを抑えることができ、また、下
水を凍結して氷の結晶を大きく成長させることにより、
下水汚泥中の微生物細胞膜を破壊して、微生物に含有さ
れているリンをポリリン酸として固定化することができ
る。その後、凍結した場合には汚泥は融解処理を経て液
化され、脱水、乾燥または焼却する下水汚泥の処理方法
によりこの課題は解決できる。
By maintaining the temperature range in which the activity of microorganisms is stopped, the release of polyphosphoric acid in sludge as orthophosphoric acid into water can be suppressed, and the sewage is frozen to increase the size of ice crystals. By growing
The microbial cell membrane in the sewage sludge is destroyed, and the phosphorus contained in the microorganism can be immobilized as polyphosphoric acid. Thereafter, when frozen, the sludge is liquefied through a thawing treatment, and this problem can be solved by a method of treating sewage sludge that is dehydrated, dried or incinerated.

【0008】また、排出される生汚泥の濃度が高い場合
には、濃縮処理過程を省略して、直接、微生物が活動を
停止する温度範囲に保持する処理過程、または凍結と融
解処理過程に入れる処理方法により解決される。。活性
汚泥に含有しているリンは、脱リン細菌によってポリリ
ン酸の形態で微生物体内に貯蔵されており、脱リン細菌
は、嫌気状態(分子状酸素すなわち亜硝酸性窒素と硝酸
性窒素さらに溶存酸素も存在しない状態)においてポリ
リン酸をオルトリン酸として水中に放出することが知ら
れている。
If the concentration of the discharged sludge is high, the concentration process is omitted and the process is directly carried out in a process of maintaining the temperature range in which the microorganism stops its activity, or in a process of freezing and thawing. It is solved by the processing method. . Phosphorus contained in activated sludge is stored in microorganisms in the form of polyphosphoric acid by dephosphorylated bacteria, and dephosphorylated bacteria are in an anaerobic state (molecular oxygen, that is, nitrite nitrogen and nitrate nitrogen, and dissolved oxygen). It is known that polyphosphoric acid is released into water as orthophosphoric acid in the absence of water.

【0009】本発明者等は、凍結融解後の汚泥と常温放
置の汚泥とを脱水処理した排水について、リン濃度に注
目して詳細に検討したところ、下記の点が判明した。ま
ず、汚泥を常温状態で放置した場合には、汚泥中の脱リ
ン細菌は活動しており、汚泥中の硝酸性窒素は放置時間
と共に減少して嫌気状態となり、脱リン細菌中のポリリ
ン酸は、オルトリン酸として水中に放出される。
The present inventors have studied the wastewater obtained by dewatering sludge after freezing and thawing and sludge left at room temperature by paying attention to the phosphorus concentration, and have found the following points. First, when the sludge is left at room temperature, the phosphorus-removing bacteria in the sludge are active, the nitrate nitrogen in the sludge decreases with the standing time and becomes anaerobic, and the polyphosphoric acid in the phosphorus-removing bacteria becomes Is released into the water as orthophosphoric acid.

【0010】一方、汚泥中の硝酸性窒素存在下で凍結処
理を行う場合、硝酸性窒素が存在するために、リンは脱
リン細菌の細胞内にポリリン酸として存在している。凍
結処理過程で適切な温度制御を行うことで、下水汚泥は
水の分子から氷の結晶となり、その後、汚泥自体が凍結
する。水の分子は固体の状態では液体の状態よりも体積
が増加することは自明の事実であるが、このとき、微生
物の細胞が氷の体積増加のため圧縮・破壊されて、微生
物が死滅することが見出された。この状態で融解処理し
た場合、常温放置してもリンは死滅した微生物細胞内に
ポリリン酸として存在しており、水中にオルトリン酸と
して検出されないことを確認した。
On the other hand, when freezing is performed in the presence of nitrate nitrogen in sludge, phosphorus is present as polyphosphoric acid in the cells of dephosphorylated bacteria due to the presence of nitrate nitrogen. By performing appropriate temperature control during the freezing process, the sewage sludge turns into ice crystals from water molecules, and then the sludge itself freezes. It is self-evident that water molecules increase in volume in the solid state compared to the liquid state, but at this time, the cells of the microorganisms are compressed and destroyed due to the increase in the volume of ice, and the microorganisms die. Was found. When the melting treatment was performed in this state, it was confirmed that phosphorus was present as polyphosphoric acid in the dead microbial cells even when left at room temperature, and was not detected as orthophosphoric acid in water.

【0011】また、凍結融解処理において汚泥中の一部
の脱リン細菌が生育し活動を再開しても、硝酸性窒素が
残留している間は、オルトリンとしてリンを水中に放出
することはないため、この間に脱水処理を行うことによ
って脱水排水中のリン濃度を低くすることができる。こ
の検討結果から、下水汚泥の濃縮処理過程と、脱水処理
過程との間に、凍結融解過程を入れることで、リンが高
濃度に含まれてしまうという問題を解決できる。
In addition, even if a part of the dephosphorylated bacteria in the sludge grows and resumes the activity in the freeze-thaw treatment, phosphorus is not released into the water as orthorin while nitrate nitrogen remains. Therefore, the phosphorus concentration in the dewatered wastewater can be reduced by performing the dehydration treatment during this time. From this examination result, it is possible to solve the problem that phosphorus is contained in a high concentration by inserting a freeze-thaw process between the sewage sludge concentration process and the dehydration process.

【0012】[0012]

【発明の実施の形態】以下、本発明を3つの実施例につ
いて説明する。第1の実施例の装置構成を図1に示す。
この図に於いて、1は汚泥濃縮装置、2は凍結融解装
置、3は脱水装置、4は温度計、5は凍結温度制御装置
を表す。下水処理場から排出される生汚泥は、汚泥濃縮
装置1で処理し、濃縮汚泥を凍結融解装置2に入れる。
この時の汚泥溶液中のオルトリン酸濃度は1.2mg/
Lであった。凍結融解装置2での凍結処理過程では、温
度計4から汚泥の温度を計測し、凍結温度制御装置5に
より凍結融解装置2の温度を氷の結晶が大きく成長する
温度0℃〜―5℃程度の範囲で制御した。凍結を確認
後、汚泥を融解、脱水処理した脱水排水のオルトリン酸
濃度は、2.2mg/Lであった。
DESCRIPTION OF THE PREFERRED EMBODIMENTS Hereinafter, the present invention will be described with reference to three embodiments. FIG. 1 shows an apparatus configuration of the first embodiment.
In this figure, 1 is a sludge concentrator, 2 is a freeze-thaw device, 3 is a dehydrator, 4 is a thermometer, and 5 is a freezing temperature controller. Raw sludge discharged from the sewage treatment plant is treated by the sludge concentrator 1 and the concentrated sludge is put into the freeze-thaw device 2.
The concentration of orthophosphoric acid in the sludge solution at this time was 1.2 mg /
L. During the freezing process in the freeze-thaw device 2, the temperature of the sludge is measured by the thermometer 4, and the temperature of the freeze-thaw device 2 is adjusted by the freezing temperature control device 5 to a temperature of about 0 ° C. to −5 ° C. at which ice crystals grow large. Was controlled within the range. After confirming freezing, the concentration of orthophosphoric acid in the dewatered wastewater obtained by melting and dewatering the sludge was 2.2 mg / L.

【0013】凍結融解処理を行わずに、同じ汚泥を従来
法で脱水処理した脱水排水のオルトリン酸濃度は、3
0.2mg/Lであった。したがって、本発明により、
脱水排水のオルトリン酸濃度を従来法に比べここでは約
10分の1にできたことになる。次に、本発明の第2の
実施例の装置構成を図2に示す。この実施例では、生汚
泥のオルトリン酸濃度が高いため、第1の実施例から汚
泥濃縮装置1を省略した装置で構成している。
The concentration of orthophosphoric acid in the dewatered wastewater obtained by subjecting the same sludge to dewatering by the conventional method without performing freeze-thaw treatment is 3
It was 0.2 mg / L. Thus, according to the present invention,
This means that the concentration of orthophosphoric acid in the dewatered wastewater can be reduced to about one tenth in comparison with the conventional method. Next, FIG. 2 shows an apparatus configuration of a second embodiment of the present invention. In this embodiment, since the concentration of orthophosphoric acid in raw sludge is high, the sludge concentration apparatus 1 is omitted from the first embodiment.

【0014】下水処理場から排出される生汚泥を直接凍
結融解装置2に入れる。この時の汚泥溶液中のオルトリ
ン酸濃度は1.4mg/Lであった。凍結融解装置2で
の凍結処理過程では、温度計4から汚泥の温度を計測し
凍結温度制御装置5により凍結融解装置2の温度を氷の
結晶が大きく成長する温度0℃〜−5℃程度の範囲で制
御した。凍結を確認後、汚泥を融解し脱水処理した脱水
排水のオルトリン酸濃度は、1.7mg/Lであった。
Raw sludge discharged from the sewage treatment plant is directly put into the freeze-thaw apparatus 2. At this time, the concentration of orthophosphoric acid in the sludge solution was 1.4 mg / L. In the freezing process in the freeze-thaw device 2, the temperature of the sludge is measured from the thermometer 4, and the temperature of the freeze-thaw device 2 is adjusted by the freezing temperature control device 5 to a temperature of about 0 ° C. to −5 ° C. at which ice crystals grow large. Controlled by range. After confirming freezing, the concentration of orthophosphoric acid in the dewatered wastewater obtained by melting and dewatering the sludge was 1.7 mg / L.

【0015】同じ汚泥を凍結融解処理を行わずに従来法
で直接脱水処理した脱水排水のオルトリン酸濃度は3
3.6mg/Lであった。したがって、本発明により、
脱水排水のオルトリン酸濃度を低くすることが可能にな
ったことになる。さらに、本発明の第3の実施例を図3
により説明する。この実施例では、第1の実施例の装置
構成の中の汚泥濃縮装置1に、硝酸性窒素計6を追加し
た装置で構成している。
The orthophosphoric acid concentration of the dewatered wastewater obtained by directly dewatering the same sludge by the conventional method without performing freeze-thaw treatment is 3
It was 3.6 mg / L. Thus, according to the present invention,
This means that the concentration of orthophosphoric acid in the dewatered wastewater can be reduced. FIG. 3 shows a third embodiment of the present invention.
This will be described below. In this embodiment, the apparatus is configured by adding a nitrate nitrogen meter 6 to the sludge concentration apparatus 1 in the apparatus configuration of the first embodiment.

【0016】下水処理場から排出される生汚泥は汚泥濃
縮装置1で処理し、濃縮汚泥を凍結融解装置2に入れ
る。この時の汚泥溶液中のオルトリン酸濃度は1.5m
g/Lであり、また硝酸性窒素計6の値は7.3mg/
Lであった。凍結融解装置2での凍結処理過程では、温
度計4から汚泥の温度を計測し、凍結温度制御装置5に
より凍結融解装置2の温度を氷の結晶が大きく成長する
温度0℃〜−5℃程度の範囲で制御した。凍結を確認
後、汚泥を融解して脱水処理した脱水排水のオルトリン
酸濃度は、2.4mg/Lであった。
Raw sludge discharged from the sewage treatment plant is treated by the sludge concentrator 1 and the concentrated sludge is put into the freeze-thaw apparatus 2. The concentration of orthophosphoric acid in the sludge solution at this time was 1.5 m
g / L, and the value of the nitrate nitrogen analyzer 6 is 7.3 mg / L.
L. During the freezing process in the freeze-thaw device 2, the temperature of the sludge is measured from the thermometer 4, and the temperature of the freeze-thaw device 2 is adjusted by the freezing temperature control device 5 to a temperature of about 0 ° C. to −5 ° C. at which ice crystals grow large. Was controlled within the range. After confirming the freezing, the concentration of orthophosphoric acid in the dewatered wastewater obtained by melting and dewatering the sludge was 2.4 mg / L.

【0017】同じ汚泥を硝酸性窒素計6の値が1.4m
g/Lになった時点で、凍結融解処理を行い、脱水処理
した脱水排水のオルトリン酸濃度は28.2mg/Lで
あった。したがって、濃縮汚泥の硝酸性窒素濃度を計測
して、その計測値から濃縮汚泥を凍結融解処理する間隔
を制御することによって脱水排水のリン濃度を低くする
ことができたことになる。
The same sludge has a nitrate-nitrogen meter 6 value of 1.4 m.
At the time when the concentration became g / L, a freeze-thaw treatment was performed, and the concentration of orthophosphoric acid in the dewatered dewatered wastewater was 28.2 mg / L. Therefore, by measuring the nitrate nitrogen concentration of the concentrated sludge and controlling the interval of freeze-thaw treatment of the concentrated sludge based on the measured value, the phosphorus concentration of the dewatered wastewater could be reduced.

【0018】[0018]

【発明の効果】本発明は、上記に説明したように、従来
の処理過程に、微生物が活動を停止する温度範囲に保持
する処理過程、または凍結融解処理過程を入れたので、
脱水処理過程で排出される排水のリン濃度が低い下水汚
泥の処理方法を提供できる。実際、本発明によれば、汚
泥中のポリリン酸を脱水汚泥に固定化することができ、
汚泥のコンポスト化にも利用しやすい汚泥を提供でき
る。
According to the present invention, as described above, the conventional process includes a process of maintaining the temperature range in which the microorganism stops its activity, or a process of freeze-thawing.
A method for treating sewage sludge having a low phosphorus concentration in wastewater discharged in the dehydration process can be provided. In fact, according to the present invention, polyphosphoric acid in sludge can be immobilized on dehydrated sludge,
Sludge that can be easily used for composting sludge can be provided.

【0019】さらに、脱水汚泥の含水率を従来法よりも
低くすることが可能である。また、汚泥処理過程で発生
する悪臭や汚泥固化を防止する効果もある。
Furthermore, the water content of the dewatered sludge can be made lower than in the conventional method. It also has an effect of preventing bad smell and sludge solidification generated in the sludge treatment process.

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

【図1】本発明の第1の実施例を説明する装置構成図FIG. 1 is an apparatus configuration diagram illustrating a first embodiment of the present invention.

【図2】本発明の第2の実施例を説明する装置構成図FIG. 2 is an apparatus configuration diagram illustrating a second embodiment of the present invention.

【図3】本発明の第3の実施例を説明する装置構成図FIG. 3 is an apparatus configuration diagram illustrating a third embodiment of the present invention.

【符号の説明】[Explanation of symbols]

1: 汚泥濃縮装置 2: 凍結融解装置 3: 脱水装置 4: 温度計 5: 凍結温度制御装置 6: 硝酸性窒素計 1: Sludge concentrator 2: Freezing and thawing device 3: Dehydrating device 4: Thermometer 5: Freezing temperature controller 6: Nitrate nitrogen meter

Claims (4)

【特許請求の範囲】[Claims] 【請求項1】生物学的にリンを除去している下水処理場
から発生する下水汚泥の処理方法において、少なくと
も、微生物が活動を停止する温度範囲に保持する処理過
程、脱水処理過程、乾燥または焼却処理過程を備えたこ
とを特徴とする下水汚泥の処理方法。
1. A method for treating sewage sludge generated from a sewage treatment plant that biologically removes phosphorus, wherein at least a treatment step for maintaining a temperature range in which microorganisms stop their activity, a dehydration treatment step, a drying or A method for treating sewage sludge, comprising an incineration process.
【請求項2】請求項1記載の方法において、前記微生物
が活動を停止する温度範囲に保持する処理過程の微生物
が活動を停止する温度範囲を、下水が凍結する温度範囲
とした凍結処理過程であることを特徴とする下水汚泥の
処理方法。
2. A freezing process according to claim 1, wherein the temperature range in which the microorganism stops its activity in the process of maintaining the temperature range in which the microorganism stops its activity is the temperature range in which the sewage freezes. A method for treating sewage sludge, which is characterized in that:
【請求項3】請求項1または2記載の方法において、前
記微生物が活動を停止する温度範囲に保持する処理過
程、または前記凍結処理過程の前段に、濃縮汚泥処理過
程を備えたことを特徴とする下水汚泥の処理方法。
3. The method according to claim 1, further comprising a concentrated sludge treatment step preceding the treatment step of keeping the temperature range in which the microorganism stops its activity or the freezing treatment step. Sewage sludge treatment method.
【請求項4】請求項3記載の方法において、濃縮汚泥処
理過程を実行する装置内の硝酸性窒素を計測し、濃縮汚
泥中の硝酸性窒素が残存している間に、前記微生物が活
動を停止する温度範囲に保持する処理、または前記凍結
処理を行うことを特徴とする下水汚泥の処理方法。
4. The method according to claim 3, wherein the nitrate nitrogen in the apparatus for performing the concentrated sludge treatment step is measured, and the activity of the microorganisms is increased while the nitrate nitrogen in the concentrated sludge remains. A method for treating sewage sludge, comprising performing a process of maintaining a temperature range in which the process is stopped, or performing the freezing process.
JP2000014644A 2000-01-24 2000-01-24 Sewage sludge treatment method Expired - Fee Related JP3705064B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2000014644A JP3705064B2 (en) 2000-01-24 2000-01-24 Sewage sludge treatment method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2000014644A JP3705064B2 (en) 2000-01-24 2000-01-24 Sewage sludge treatment method

Publications (2)

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JP2001205298A true JP2001205298A (en) 2001-07-31
JP3705064B2 JP3705064B2 (en) 2005-10-12

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Family Applications (1)

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Country Link
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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108609817A (en) * 2018-04-19 2018-10-02 广州市永蓝环保科技有限公司 A kind of curing of river sludge

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108609817A (en) * 2018-04-19 2018-10-02 广州市永蓝环保科技有限公司 A kind of curing of river sludge

Also Published As

Publication number Publication date
JP3705064B2 (en) 2005-10-12

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