JP2002224693A - Sludge intensive treatment system - Google Patents

Sludge intensive treatment system

Info

Publication number
JP2002224693A
JP2002224693A JP2001027784A JP2001027784A JP2002224693A JP 2002224693 A JP2002224693 A JP 2002224693A JP 2001027784 A JP2001027784 A JP 2001027784A JP 2001027784 A JP2001027784 A JP 2001027784A JP 2002224693 A JP2002224693 A JP 2002224693A
Authority
JP
Japan
Prior art keywords
sludge
concentration
hydrogen sulfide
phosphorus
treatment plant
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
JP2001027784A
Other languages
Japanese (ja)
Other versions
JP3620450B2 (en
Inventor
Itaru Sakai
至 坂井
Jun Miyata
純 宮田
Kenichiro Mizuno
健一郎 水野
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.)
JFE Engineering Corp
Original Assignee
NKK Corp
Nippon Kokan 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 NKK Corp, Nippon Kokan Ltd filed Critical NKK Corp
Priority to JP2001027784A priority Critical patent/JP3620450B2/en
Publication of JP2002224693A publication Critical patent/JP2002224693A/en
Application granted granted Critical
Publication of JP3620450B2 publication Critical patent/JP3620450B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Abstract

PROBLEM TO BE SOLVED: To efficiently perform the prevention against the generation of malodor in a sludge receiving side intensive treatment plant and the reduction of phosphorous load in a sewage treatment plant receiving the return water at the time of treating intensively sludge. SOLUTION: The sludge intensive treatment system, in which the sludge discharged from the sewage treatment plants 1A, 1B and 1C is collected to the sludge intensive treatment plant 2 through sludge feed pipes 3A, 3B and 3C to be treated and the produced liquid separated from the sludge is returned to the sewage treatment plant through a water returning pipe 13, is provided with a monitoring means 4A, 4B and 4C for hydrogen sulfide concentration in the sludge in the sludge feed pipes and a hydrogen sulfide reduction directing means 5 for transmitting a direction of the reduction of hydrogen sulfide in the feed sludge to the sewage treatment plant, from which the sludge is fed through the sludge feed pipe, in the case that the hydrogen sulfide concentration monitored by the monitoring means for concentration of hydrogen sulfide exceeds a set value and a hydrogen sulfide concentration control means 8A, 8B and 8C for controlling the hydrogen sulfide concentration in the sewage treatment plant corresponding to the signal from the hydrogen sulfide reduction directing means 5.

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】この発明は、汚泥集約処理シ
ステム、特に、汚泥を集約処理する際に、受泥側集約処
理場での臭気の発生防止と、返流水を受け入れる下水処
理場におけるリン負荷軽減を効率良く行なうことができ
る汚泥集約処理システムに関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a sludge concentration treatment system, and more particularly, to preventing the generation of odor in a sludge receiving concentration treatment plant and a phosphorus load in a sewage treatment plant receiving return water when the sludge is concentrated. The present invention relates to a sludge intensive treatment system capable of efficiently reducing the amount of sludge.

【0002】[0002]

【従来の技術】都市部における汚泥処理は、個別の下水
処理場毎に汚泥処理設備を保有するのではなく、複数の
下水処理場より送泥管で汚泥を集めて集約処理場におい
て効率的に一括処理する方法が採用されている。
2. Description of the Related Art Sludge treatment in an urban area does not have a sludge treatment facility for each individual sewage treatment plant. A batch processing method is adopted.

【0003】[0003]

【発明が解決しようとする課題】上述した汚泥の集約処
理においては、以下のような問題を有していた。
However, the above-mentioned sludge concentration processing has the following problems.

【0004】通常、各水処理場と汚泥集約処理場とは
離れているので、送泥中に汚泥が腐敗し、受泥側の集約
処理場において硫化水素による臭気が発生する。
Normally, since each water treatment plant and the sludge concentration treatment plant are separated from each other, the sludge decays during the sludge feeding, and an odor due to hydrogen sulfide is generated at the concentration treatment plant on the mud receiving side.

【0005】集約処理場で処理された汚泥の脱離液
は、集約処理場に一番近い下水処理場に返流水として返
水され、再処理されるが、返水先の汚泥処理場でのリン
負荷が大きく、また、リン負荷量が予測できない。
[0005] The sludge desorbed liquid treated at the intensive treatment plant is returned to the sewage treatment plant closest to the intensive treatment plant as return water and reprocessed. The load is large and the phosphorus load cannot be predicted.

【0006】従って、この発明の目的は、汚泥を集約処
理する際に、受泥側集約処理場での臭気の発生防止と、
返流水を受け入れる下水処理場におけるリン負荷軽減を
効率良く行なうことができる汚泥集約処理システムを提
供することにある。
Accordingly, an object of the present invention is to prevent the generation of odor at the intensive treatment plant on the mud receiving side when performing the intensive treatment of sludge.
It is an object of the present invention to provide a sludge intensive treatment system capable of efficiently reducing a phosphorus load in a sewage treatment plant receiving return water.

【0007】[0007]

【課題を解決するための手段】請求項1記載の発明は、
単一または複数の下水処理場から排出された汚泥を、送
泥管により汚泥集約処理場に集めて処理した後、生成す
る汚泥脱離液を返水管により前記下水処理場に返水する
汚泥集約システムにおいて、前記送泥管内の汚泥の硫化
水素濃度監視手段と、前記硫化水素濃度監視手段により
監視された硫化水素濃度が設定値を超えた場合に、当該
汚泥管により汚泥を送出している下水処理場に対して、
送出汚泥中の硫化水素低減を警告する硫化水素警告手段
とを設けたことに特徴を有するものである。
According to the first aspect of the present invention,
After collecting and treating sludge discharged from one or a plurality of sewage treatment plants by a sludge pipe in a sludge concentration treatment plant, sludge concentration in which generated sludge desorbed liquid is returned to the sewage treatment plant by a return pipe In the system, means for monitoring the concentration of hydrogen sulfide in the sludge in the sludge pipe, and when the concentration of hydrogen sulfide monitored by the means for monitoring the concentration of hydrogen sulfide exceeds a set value, the sewage discharging sludge through the sludge pipe. For the treatment plant,
The present invention is characterized in that hydrogen sulfide warning means for warning reduction of hydrogen sulfide in the outflow sludge is provided.

【0008】請求項2記載の発明は、単一または複数の
下水処理場から排出された汚泥を、送泥管により汚泥集
約処理場に集めて処理した後、生成する汚泥脱離液を返
水管により前記下水処理場に返水する汚泥集約処理シス
テムにおいて、前記送泥管内の汚泥の硫化水素濃度監視
手段と、前記硫化水素濃度監視手段により監視された硫
化水素濃度が設定値を超えた場合に、当該汚泥管により
汚泥を送出している下水処理場に対して、送出汚泥中の
硫化水素低減指示を発信する硫化水素低減指示手段と、
前記硫化水素低減指示手段からの信号に従って当該下水
処理場における硫化水素濃度を制御する硫化水素濃度制
御手段とを設けたことに特徴を有するものである。
According to a second aspect of the present invention, the sludge discharged from one or a plurality of sewage treatment plants is collected and treated in a sludge concentration treatment plant by a sludge pipe, and the sludge desorbed liquid generated is returned to a return pipe. In the sludge intensive treatment system that returns to the sewage treatment plant, the hydrogen sulfide concentration monitoring means of the sludge in the sludge pipe, and when the hydrogen sulfide concentration monitored by the hydrogen sulfide concentration monitoring means exceeds a set value A hydrogen sulfide reduction instruction means for transmitting a hydrogen sulfide reduction instruction in the transmitted sludge to a sewage treatment plant that is transmitting sludge by the sludge pipe;
A hydrogen sulfide concentration control means for controlling the hydrogen sulfide concentration in the sewage treatment plant in accordance with a signal from the hydrogen sulfide reduction instruction means is provided.

【0009】請求項3記載の発明は、単一または複数の
下水処理場から排出された汚泥を、送泥管より汚泥集約
処理場に集めて処理した後、生成する汚泥脱離液を返水
管により前記下水処理場に返水する汚泥集約処理システ
ムにおいて、前記返水管内の汚泥のリン濃度監視手段
と、前記リン濃度監視手段により監視されたリン濃度が
設定値を超えた場合に、前記汚泥集約処理場に対して、
送出汚泥脱離液中のリン低減を警告するリン警告手段と
を設けたことに特徴を有するものである。
According to a third aspect of the present invention, the sludge discharged from a single or a plurality of sewage treatment plants is collected from a sludge pipe at a sludge concentration treatment plant and treated, and the sludge desorbed liquid produced is returned to a return pipe. In the sludge concentration treatment system for returning to the sewage treatment plant, the sludge phosphorus concentration monitoring means in the return pipe, and when the phosphorus concentration monitored by the phosphorus concentration monitoring means exceeds a set value, the sludge For the central processing plant,
It is characterized in that phosphorus warning means for warning the reduction of phosphorus in the discharged sludge desorbed liquid is provided.

【0010】請求項4記載の発明は、単一または複数の
下水処理場から排出された汚泥を、送泥管により汚泥集
約処理場に集めて処理した後、生成する汚泥脱離液を返
水管により前記下水処理場に返水する汚泥集約処理シス
テムにおいて、前記返水管内の汚泥のリン濃度監視手段
と、前記リン濃度監視手段により監視されたリン濃度が
設定値を超えた場合に、前記汚泥集約処理場に対して、
送出汚泥脱離液中のリン低減指示を発信するリン低減指
示手段と、前記リン低減指示手段からの信号に従って前
記汚泥集約処理場におけるリン濃度を制御するリン濃度
制御手段とを設けたことに特徴を有するものである。
According to a fourth aspect of the present invention, the sludge discharged from one or a plurality of sewage treatment plants is collected and treated by a sludge pipe at a sludge concentration treatment plant, and the sludge desorbed liquid produced is returned to a return pipe. In the sludge concentration treatment system for returning to the sewage treatment plant, the sludge phosphorus concentration monitoring means in the return pipe, and when the phosphorus concentration monitored by the phosphorus concentration monitoring means exceeds a set value, the sludge For the central processing plant,
It is characterized in that phosphorus reduction instruction means for transmitting a phosphorus reduction instruction in the discharged sludge desorbed liquid, and phosphorus concentration control means for controlling the phosphorus concentration in the sludge concentration treatment plant according to a signal from the phosphorus reduction instruction means are provided. It has.

【0011】請求項5記載の発明は、単一または複数の
下水処理場から排出された汚泥を、送泥管により汚泥集
約処理場に集めて処理した後、生成する汚泥脱離液を返
水管により前記下水処理場に返水する汚泥集約システム
において、前記送泥管内の汚泥の硫化水素濃度監視手段
と、前記硫化水素濃度監視手段により監視された硫化水
素濃度が設定値を超えた場合に、当該汚泥管により汚泥
を送出している下水処理場に対して、送出汚泥中の硫化
水素低減を警告する硫化水素警告手段と、前記返水管内
の汚泥のリン濃度監視手段と、前記リン濃度監視手段に
より監視されたリン濃度が設定値を超えた場合に、前記
汚泥集約処理場に対して、送出汚泥脱離液中のリン低減
を警告するリン警告手段とを設けたことに特徴を有する
ものである。
According to a fifth aspect of the present invention, the sludge discharged from one or a plurality of sewage treatment plants is collected and treated in a sludge concentration treatment plant by a sludge pipe, and the sludge desorbed liquid generated is returned to a return pipe. In the sludge aggregation system that returns to the sewage treatment plant, when the hydrogen sulfide concentration monitoring means of the sludge in the mud pipe and the hydrogen sulfide concentration monitored by the hydrogen sulfide concentration monitoring means exceeds a set value, A hydrogen sulfide warning unit for warning a sewage treatment plant that sends out sludge by the sludge pipe, a reduction in hydrogen sulfide in the sent out sludge; a phosphorus concentration monitoring unit for the sludge in the return pipe; When the phosphorus concentration monitored by the means exceeds a set value, the sludge concentration treatment plant is provided with phosphorus warning means for warning the reduction of phosphorus in the discharged sludge desorbed liquid. It is.

【0012】請求項6記載の発明は、単一または複数の
下水処理場から排出された汚泥を、送泥管により汚泥集
約処理場に集めて処理した後、生成する汚泥脱離液を返
水管により前記下水処理場に返水する汚泥集約処理シス
テムにおいて、前記送泥管内の汚泥の硫化水素濃度監視
手段と、前記硫化水素濃度監視手段により監視された硫
化水素濃度が設定値を超えた場合に、当該汚泥管により
汚泥を送出している下水処理場に対して、送出汚泥中の
硫化水素低減指示を発信する硫化水素低減指示手段と、
前記硫化水素低減指示手段からの信号に従って当該下水
処理場における硫化水素濃度を制御する硫化水素濃度制
御手段と、前記返水管内の汚泥のリン濃度監視手段と、
前記リン濃度監視手段により監視されたリン濃度が設定
値を超えた場合に、前記汚泥集約処理場に対して、送出
汚泥脱離液中のリン低減指示を発信するリン低減指示手
段と、前記リン低減指示手段からの信号に従って前記汚
泥集約処理場におけるリン濃度を制御するリン濃度制御
手段とを設けたことに特徴を有するものである。
According to a sixth aspect of the present invention, the sludge discharged from one or a plurality of sewage treatment plants is collected and treated by a sludge pipe at a sludge concentration treatment plant, and the sludge desorbed liquid generated is returned to a return pipe. In the sludge intensive treatment system returning water to the sewage treatment plant, in the sludge hydrogen sulfide concentration monitoring means of the sludge in the sludge pipe, when the hydrogen sulfide concentration monitored by the hydrogen sulfide concentration monitoring means exceeds a set value A hydrogen sulfide reduction instruction means for transmitting a hydrogen sulfide reduction instruction in the transmitted sludge to a sewage treatment plant that is transmitting sludge by the sludge pipe;
Hydrogen sulfide concentration control means for controlling the concentration of hydrogen sulfide in the sewage treatment plant according to a signal from the hydrogen sulfide reduction instruction means, phosphorus concentration monitoring means for sludge in the return pipe,
When the phosphorus concentration monitored by the phosphorus concentration monitoring means exceeds a set value, a phosphorus reduction instruction means for transmitting a phosphorus reduction instruction in the sludge desorption solution to the sludge concentration treatment plant; It is characterized in that phosphorus concentration control means for controlling the phosphorus concentration in the sludge concentration treatment plant in accordance with a signal from the reduction instruction means is provided.

【0013】請求項7記載の発明は、前記硫化水素濃度
監視手段、前記硫化水素低減指示手段および前記硫化水
素濃度制御手段の内の少なくとも1つは、前記送泥管に
敷設された光ファイバーを使用して通信を行なうもので
あることに特徴を有するものである。
According to a seventh aspect of the present invention, at least one of the hydrogen sulfide concentration monitoring means, the hydrogen sulfide reduction instruction means and the hydrogen sulfide concentration control means uses an optical fiber laid on the mud pipe. It is characterized in that the communication is performed by performing the communication.

【0014】請求項8記載の発明は、前記リン濃度監視
手段、前記リン低減指示手段および前記リン濃度制御手
段の内の少なくとも1つは、前記返水管に敷設された光
ファイバーを使用して通信を行なうものであることに特
徴を有するものである。
[0014] According to the present invention, at least one of the phosphorus concentration monitoring means, the phosphorus reduction instruction means and the phosphorus concentration control means communicates using an optical fiber laid on the return pipe. It is characterized by what it does.

【0015】[0015]

【発明の実施の形態】この発明の汚泥集約処理システム
の一実施態様を、図面を参照しながら説明する。
DESCRIPTION OF THE PREFERRED EMBODIMENTS One embodiment of the sludge concentration processing system of the present invention will be described with reference to the drawings.

【0016】図1は、この発明のシステム全体の構成
図、図2は、集約処理場における硫化水素発生の抑制処
理フローの一例を示すフロー図、図3は、硫化水素低減
指示手段および下水処理場における硫化水素濃度制御手
段の構成を示すブロック図、図4は、集約処理場におけ
るリン負荷抑制処理フローの一例を示すフロー図、図5
は、リン低減指示手段および集約処理場におけるリン濃
度制御手段の構成を示すブロック図である。
FIG. 1 is a block diagram of the entire system of the present invention, FIG. 2 is a flowchart showing an example of a process flow for suppressing the generation of hydrogen sulfide in an integrated treatment plant, and FIG. 3 is a hydrogen sulfide reduction instruction means and sewage treatment. FIG. 4 is a block diagram showing a configuration of the hydrogen sulfide concentration control means in the plant, FIG. 4 is a flowchart showing an example of a phosphorus load suppression process flow in the centralized treatment plant, and FIG.
FIG. 3 is a block diagram showing a configuration of a phosphorus reduction instruction unit and a phosphorus concentration control unit in an integrated treatment plant.

【0017】図1において、1A、1B、1Cは、下水
処理場である。下水処理場の数は、この例のように複数
に限定されず、1つでも良い。2は、汚泥の集約処理
場、3A、3B、3Cは、下水処理場1A、1B、1C
から集約処理場2に汚泥を送る送泥管、4A、4B、4
Cは、送泥管3A、3B、3Cに設置された送泥管内の
汚泥の硫化水素濃度を監視する硫化水素濃度監視手段で
あり、例えば、オンラインで測定可能な紫外線吸光光度
方式のセンサーが利用できる。
In FIG. 1, 1A, 1B and 1C are sewage treatment plants. The number of sewage treatment plants is not limited to a plurality as in this example, and may be one. 2 is an integrated sludge treatment plant, 3A, 3B and 3C are sewage treatment plants 1A, 1B and 1C
Pipes for sending sludge from the plant to the sewage treatment plant 2, 4A, 4B, 4
C is a hydrogen sulfide concentration monitoring means for monitoring the hydrogen sulfide concentration of the sludge in the mud pipes 3A, 3B and 3C, and uses, for example, a UV-absorbance type sensor that can be measured online. it can.

【0018】5は、硫化水素低減指示手段である。硫化
水素低減指示手段5は、図3に示すように、入力部6と
演算部7とを備えている。入力部6は、汚泥受入れ部で
の硫化水素濃度が設定値以下か否かを判断し、設定値以
下でない場合には、硫化水素濃度監視手段4A、4B、
4Cによるセンサー情報を演算部7に入力する。演算部
7は、これらセンサー情報を比較し、各硫化水素濃度監
視手段による硫化水素濃度の最大値を特定し、そして、
この最大値と硫化水素の低減に有効な曝気およびポリ鉄
添加のデータベースに基づいて、硫化水素濃度を設定値
以下に抑制することができる最適曝気条件および最適ポ
リ鉄添加条件を演算する。演算部7からの最適曝気条件
信号および最適ポリ鉄添加条件信号は、硫化水素濃度レ
ベルが最大値を示す汚泥管により汚泥を送出している特
定の下水処理場に対して発信される。なお、硫化水素低
減指示手段5の設置場所は、特に限定されない。
Reference numeral 5 denotes hydrogen sulfide reduction instruction means. The hydrogen sulfide reduction instruction means 5 includes an input unit 6 and a calculation unit 7 as shown in FIG. The input unit 6 determines whether or not the hydrogen sulfide concentration in the sludge receiving unit is equal to or less than a set value. If the hydrogen sulfide concentration is not equal to or less than the set value, the hydrogen sulfide concentration monitoring means 4A, 4B,
The sensor information by 4C is input to the calculation unit 7. The calculation unit 7 compares the sensor information, specifies the maximum value of the hydrogen sulfide concentration by each hydrogen sulfide concentration monitoring unit, and
Based on this maximum value and a database of aeration and polyiron addition effective for reducing hydrogen sulfide, the optimum aeration conditions and optimum polyiron addition conditions that can suppress the hydrogen sulfide concentration below the set value are calculated. The optimum aeration condition signal and the optimum polyiron addition condition signal from the calculation unit 7 are transmitted to a specific sewage treatment plant that sends out sludge through a sludge pipe whose hydrogen sulfide concentration level shows the maximum value. The location of the hydrogen sulfide reduction instruction means 5 is not particularly limited.

【0019】8A、8B、8Cは、下水処理場1A、1
B、1Cに設けられた硫化水素濃度制御手段である。各
硫化水素濃度制御手段は、図3に示すように、硫化水素
低減指示手段5からの最適曝気条件信号に基づいて、下
水処理場の曝気装置9を制御する曝気装置制御部10
と、硫化水素低減指示手段5からの最適ポリ鉄添加条件
信号に基づいて下水処理場のポリ鉄添加装置11を制御
するポリ鉄添加装置制御部12とを備えている。なお、
硫化水素低減指示手段5および硫化水素濃度制御手段8
A、8B、8Cの設置場所は、特に限定されない。
8A, 8B and 8C are sewage treatment plants 1A and 1C, respectively.
B, 1C are means for controlling the concentration of hydrogen sulfide. As shown in FIG. 3, each hydrogen sulfide concentration control means includes an aeration device control unit 10 for controlling the aeration device 9 in the sewage treatment plant based on the optimum aeration condition signal from the hydrogen sulfide reduction instruction means 5.
And a polyiron addition device control unit 12 that controls the polyiron addition device 11 in the sewage treatment plant based on the optimum polyiron addition condition signal from the hydrogen sulfide reduction instruction means 5. In addition,
Hydrogen sulfide reduction instruction means 5 and hydrogen sulfide concentration control means 8
The installation locations of A, 8B, and 8C are not particularly limited.

【0020】13は、集約処理場2と特定の下水処理
場、例えば、集約処理場2に一番近い下水処理場1Cと
の管に配された返水管であり、集約処理場2で処理され
た汚泥の脱離液を下水処理場1Cに戻して再処理する。
Reference numeral 13 denotes a return pipe disposed in a pipe between the sewage treatment plant 2 and a specific sewage treatment plant, for example, a sewage treatment plant 1C closest to the sewage treatment plant 2. The sludge desorbed liquid is returned to the sewage treatment plant 1C for reprocessing.

【0021】14A、14B、14Cは、送泥管3A、
3B、3Cに設けられた送泥管内の汚泥のリン濃度を監
視するリン濃度監視手段である。
14A, 14B and 14C are mud pipes 3A,
This is a phosphorus concentration monitoring means for monitoring the phosphorus concentration of the sludge in the sludge pipes provided in 3B and 3C.

【0022】15は、返水管13に設けられた返水管1
3内の汚泥のリン濃度を監視するリン濃度監視手段であ
る。上記リン濃度監視手段14A、14B、14Cおよ
び15としては、例えば、オンラインで測定可能な紫外
線吸光光度方式のセンサーが使用される。
Reference numeral 15 denotes a return pipe 1 provided on the return pipe 13.
This is a phosphorus concentration monitoring means for monitoring the phosphorus concentration of the sludge in 3. As the phosphorus concentration monitoring means 14A, 14B, 14C, and 15, for example, ultraviolet absorption type sensors that can be measured online can be used.

【0023】16は、リン低減指示手段である。リン低
減指示手段16は、図5に示すように、入力部17と演
算部18とを備えている。入力部17は、返水管13の
リン濃度監視手段15からのセンサー情報に基づいて、
下水処理場1Cでのリン負荷量が設定値を超えるか否か
を判断し、超える場合には、リン濃度監視手段14A、
14B、14Cからのセンサー情報を演算部18に入力
する。演算部18は、リン濃度監視手段14A、14
B、14Cからのセンサー情報と送泥管3A、3B、3
Cからの汚泥量とから集約処理場2でのリン負荷総量を
演算し、このリン負荷総量と脱リン剤添加データベース
とから集約処理場2における最適脱リン剤添加条件を演
算する。演算部18からの最適脱リン剤添加条件信号
は、集約処理場2に発信される。脱リン剤としては、鉄
系の凝集剤が利用できる。なお、リン低減指示手段16
の設置場所は、特に限定されない。
Reference numeral 16 denotes phosphorus reduction instruction means. The phosphorus reduction instructing means 16 includes an input unit 17 and a calculation unit 18 as shown in FIG. The input unit 17 is based on the sensor information from the phosphorus concentration monitoring means 15 of the return pipe 13,
It is determined whether the phosphorus load in the sewage treatment plant 1C exceeds a set value, and if it exceeds, the phosphorus concentration monitoring means 14A,
The sensor information from 14B and 14C is input to the operation unit 18. The calculation unit 18 includes the phosphorus concentration monitoring means 14A, 14
B, sensor information from 14C and mud pipes 3A, 3B, 3
The total phosphorus load in the intensive treatment plant 2 is calculated from the amount of sludge from C, and the optimum dephosphorizing agent addition condition in the intensive treatment plant 2 is calculated from the total phosphorus load and the dephosphorizing agent addition database. The optimum dephosphorizing agent addition condition signal from the arithmetic unit 18 is transmitted to the centralized treatment plant 2. As the dephosphorizing agent, an iron-based flocculant can be used. The phosphorus reduction instruction means 16
Is not particularly limited.

【0024】19は、リン濃度制御手段である。リン濃
度制御手段19は、リン低減指示手段16からの最適脱
リン剤添加条件信号に基づいて、集約処理場2の脱リン
剤添加装置20を制御する脱リン剤添加装置制御部21
を備えている。
Reference numeral 19 denotes a phosphorus concentration control means. The phosphorus concentration control unit 19 controls the dephosphorizing agent adding device 20 of the centralized treatment plant 2 based on the optimal dephosphorizing agent adding condition signal from the phosphorus reducing instruction unit 16.
It has.

【0025】このように構成されている、この発明の汚
泥集約処理システムによる汚泥集約処理方法について説
明する。
The sludge concentration processing method by the sludge concentration processing system of the present invention having the above-described configuration will be described.

【0026】初めに、硫化水素濃度を制御する場合につ
いて、図2を参照しながら説明する。
First, the case of controlling the concentration of hydrogen sulfide will be described with reference to FIG.

【0027】先ず、集約処理場2における汚泥受入れ部
での硫化水素濃度設定値を設定する。この設定値は、硫
化水素臭を感じさせない濃度である。次に、硫化水素低
減指示手段5の入力部6が測定した汚泥受入れ部での硫
化水素濃度が設定値以下か否かを判断し、設定値以下で
ない場合には、硫化水素濃度監視手段4A、4B、4C
によるセンサー情報を、硫化水素低減指示手段5の演算
部7に入力する。一方、設定値以下である場合には、再
度、硫化水素濃度を測定する。
First, the set value of the concentration of hydrogen sulfide at the sludge receiving section in the integrated treatment plant 2 is set. This set value is a concentration at which the smell of hydrogen sulfide is not felt. Next, it is determined whether or not the hydrogen sulfide concentration at the sludge receiving unit measured by the input unit 6 of the hydrogen sulfide reduction instructing unit 5 is equal to or less than a set value. 4B, 4C
Is input to the calculation unit 7 of the hydrogen sulfide reduction instruction means 5. On the other hand, if it is not more than the set value, the hydrogen sulfide concentration is measured again.

【0028】硫化水素低減指示手段5の演算部7は、硫
化水素濃度監視手段4A、4B、4Cからのセンサー情
報に基づいて各センサーの硫化水素濃度レベルを比較
し、最大値を特定する。そして、硫化水素の低減に有効
な曝気およびポリ鉄添加のデータベースに基づいて、最
適曝気条件および最適ポリ鉄添加条件を演算し、この最
適曝気条件信号および最適ポリ鉄添加条件信号を、硫化
水素濃度レベルが最大値を示す汚泥管により汚泥を送出
している特定の下水処理場に対して発信する。
The arithmetic unit 7 of the hydrogen sulfide reduction instructing means 5 compares the hydrogen sulfide concentration levels of the respective sensors based on the sensor information from the hydrogen sulfide concentration monitoring means 4A, 4B, 4C and specifies the maximum value. Then, based on a database of aeration and polyiron addition effective for reducing hydrogen sulfide, the optimum aeration condition and the optimum polyiron addition condition are calculated, and the optimum aeration condition signal and the optimum polyiron addition condition signal are converted to hydrogen sulfide concentration. It is transmitted to a specific sewage treatment plant that sends out sludge by a sludge pipe whose level shows the maximum value.

【0029】この最適曝気条件信号および最適ポリ鉄添
加条件信号を受けた下水処理場では、硫化水素濃度制御
手段8により最適な曝気およびポリ鉄添加を行なう。そ
して、集約処理場2における汚泥受入れ部での硫化水素
濃度を測定し、設定値以下か否かを判断し、設定値以下
でない場合には、再度、硫化水素濃度監視手段4A、4
B、4Cからのセンサー情報を硫化水素低減指示手段5
に入力する。
In the sewage treatment plant receiving the optimum aeration condition signal and the optimum polyiron addition condition signal, the hydrogen sulfide concentration control means 8 performs the optimum aeration and polyiron addition. Then, the concentration of hydrogen sulfide in the sludge receiving section of the intensive treatment plant 2 is measured, and it is determined whether or not the concentration is below the set value.
The sensor information from B and 4C is used to indicate hydrogen sulfide reduction.
To enter.

【0030】以上のようにして、送汚泥の硫化水素濃度
が設定値以下に低減される。
As described above, the concentration of hydrogen sulfide in the sludge sent is reduced to a set value or less.

【0031】次に、リン濃度を制御する場合について、
図4を参照しながら説明する。
Next, when controlling the phosphorus concentration,
This will be described with reference to FIG.

【0032】返流水を受け入れる下水処理場1Cでのリ
ン負荷量が設定値以下となるリン濃度監視手段15の濃
度レベルを設定する。次に、リン低減指示手段16の入
力部17が測定した返水管13内の汚泥のリン濃度が設
定値以下か否かを判断し、設定値以下でない場合には、
リン濃度監視手段14A、14B、14Cによって送泥
管3A、3B、3C内の汚泥のリン濃度を測定し、この
センサー情報をリン低減指示手段16の演算部18に入
力する。一方、設定値以下である場合には、再度、リン
濃度を測定する。
The concentration level of the phosphorus concentration monitoring means 15 at which the phosphorus load at the sewage treatment plant 1C for receiving the return water is equal to or less than the set value is set. Next, it is determined whether or not the phosphorus concentration of the sludge in the return pipe 13 measured by the input unit 17 of the phosphorus reduction instruction means 16 is equal to or less than a set value.
The phosphorus concentration of the sludge in the sludge feed pipes 3A, 3B, 3C is measured by the phosphorus concentration monitoring means 14A, 14B, 14C, and the sensor information is input to the arithmetic unit 18 of the phosphorus reduction instruction means 16. On the other hand, if it is not more than the set value, the phosphorus concentration is measured again.

【0033】リン低減指示手段16の演算部18は、リ
ン濃度監視手段14A、14B、14Cからのセンサー
情報と送泥管3A、3B、3Cからの汚泥量とから集約
処理場2でのリン負荷総量を演算し、このリン負荷総量
と脱リン剤添加データベースとから集約処理場2におけ
る最適脱リン剤添加条件を演算し、この結果を集約処理
場2に対して発信する。
The calculating section 18 of the phosphorus reduction instructing means 16 calculates the phosphorus load in the integrated treatment plant 2 based on the sensor information from the phosphorus concentration monitoring means 14A, 14B, 14C and the amount of sludge from the mud pipes 3A, 3B, 3C. The total amount is calculated, the optimum phosphorus removing agent addition condition in the centralized treatment plant 2 is calculated from the total phosphorus load and the database of the phosphorus-removing agent addition, and the result is transmitted to the centralized treatment plant 2.

【0034】この最適脱リン剤添加条件信号を受けた集
約処理場2では、リン濃度制御手段19により最適な脱
リン剤添加を行なう。そして、返水管13内の汚泥のリ
ン濃度をリン濃度監視手段15により測定し、設定値以
下か否かを判断し、設定値以下でない場合には、再度、
送泥管3A、3B、3C内の汚泥のリン濃度を測定す
る。
In the centralized treatment plant 2 which receives the optimum dephosphorizing agent addition condition signal, the phosphorus concentration controlling means 19 performs optimum dephosphorizing agent addition. Then, the phosphorus concentration of the sludge in the return pipe 13 is measured by the phosphorus concentration monitoring means 15 to determine whether or not the concentration is equal to or less than a set value.
The phosphorus concentration of the sludge in the sludge pipes 3A, 3B and 3C is measured.

【0035】以上のようにして、下水処理場1Cでのリ
ン負荷量が設定値以下に低減される。
As described above, the phosphorus load in the sewage treatment plant 1C is reduced to the set value or less.

【0036】この発明によれば、集約処理場の受入れ部
での汚泥の硫化水素濃度を、硫化水素臭を感じさせない
濃度以下に低減でき、しかも、返流水を受け入れる下水
処理場におけるリン負荷量の軽減を効率良く行なえる。
According to the present invention, the concentration of hydrogen sulfide in the sludge at the receiving section of the intensive treatment plant can be reduced to a concentration not causing the smell of hydrogen sulfide to be felt, and the phosphorus load in the sewage treatment plant receiving the return water can be reduced. Reduction can be performed efficiently.

【0037】以上は、硫化水素濃度監視手段4A、4
B、4Cにより監視された硫化水素濃度が設定値を超え
た場合に、当該汚泥管により汚泥を送出している特定の
下水処理場に対して、送出汚泥中の硫化水素低減を自動
的に制御するものであるが、硫化水素濃度監視手段4
A、4B、4Cにより監視された硫化水素濃度が設定値
を超えた場合に、当該汚泥管により汚泥を送出している
下水処理場に対して、送出汚泥中の硫化水素低減を警告
する硫化水素警告手段を設け、警告に従って人手により
上述の曝気およびポリ鉄添加装置を操作しても良い。
The above description is based on the hydrogen sulfide concentration monitoring means 4A,
When the hydrogen sulfide concentration monitored by B and 4C exceeds the set value, the specific sewage treatment plant that sends out sludge by the sludge pipe automatically controls the reduction of hydrogen sulfide in the sent out sludge. The hydrogen sulfide concentration monitoring means 4
When the hydrogen sulfide concentration monitored by A, 4B, and 4C exceeds a set value, a hydrogen sulfide warning the reduction of hydrogen sulfide in the transmitted sludge to a sewage treatment plant that sends out sludge through the sludge pipe. Warning means may be provided to manually operate the above-described aeration and polyiron addition apparatus according to the warning.

【0038】また、リン濃度監視手段15により監視さ
れた返水管13内のリン濃度が設定値を超えた場合に、
汚泥集約処理場2に対して、送出汚泥脱離液中のリン低
減を自動的に制御するものであるが、リン濃度監視手段
15により監視された返水管13内のリン濃度が設定値
を超えた場合に、リン低減を警告するリン警告手段を設
け、警告に従って人手により上述脱リン剤添加装置を操
作しても良い。なお、硫化水素警告手段およびリン警告
手段は、計器等であり、その手段は特に限定されない。
When the phosphorus concentration in the return pipe 13 monitored by the phosphorus concentration monitoring means 15 exceeds a set value,
For the sludge concentration treatment plant 2, the phosphorus reduction in the discharged sludge desorbed liquid is automatically controlled. However, the phosphorus concentration in the return pipe 13 monitored by the phosphorus concentration monitoring means 15 exceeds the set value. In such a case, a phosphorus warning means for warning the phosphorus reduction may be provided, and the above-mentioned phosphorus removing agent adding device may be manually operated according to the warning. Note that the hydrogen sulfide warning means and the phosphorus warning means are instruments and the like, and the means are not particularly limited.

【0039】硫化水素濃度制御とリン濃度制御とは、個
別に行なっても良い。
The hydrogen sulfide concentration control and the phosphorus concentration control may be performed separately.

【0040】硫化水素濃度制御に際して行なう曝気およ
びポリ鉄添加の添加は、両方またはその内の1つでも良
い。
The aeration and / or the addition of polyiron for controlling the hydrogen sulfide concentration may be both or one of them.

【0041】硫化水素濃度監視手段4A、4B、4C、
硫化水素低減指示手段5および硫化水素濃度制御手段8
A、8B、8Cの内の少なくとも1つは、送泥管3A、
3B、3Cに敷設された光ファイバーを使用して通信を
行なうものであっても良く、これにより、より確実且つ
迅速に硫化水素濃度制御が行なえる。
The hydrogen sulfide concentration monitoring means 4A, 4B, 4C,
Hydrogen sulfide reduction instruction means 5 and hydrogen sulfide concentration control means 8
At least one of A, 8B and 8C is a mud pipe 3A,
Communication may be performed using optical fibers laid on 3B and 3C, whereby the concentration of hydrogen sulfide can be more reliably and quickly controlled.

【0042】更に、リン濃度監視手段14A、14B、
14C、15、リン低減指示手段16およびリン濃度制
御手段19の内の少なくとも1つは、返水管に敷設され
た光ファイバーを使用して通信を行なうものであっても
良く、これにより、より確実且つ迅速にリン濃度制御が
行なえる。
Further, the phosphorus concentration monitoring means 14A, 14B,
At least one of 14C, 15, the phosphorus reduction instruction means 16 and the phosphorus concentration control means 19 may perform communication using an optical fiber laid in a return pipe, thereby providing a more reliable and more reliable communication. Phosphorus concentration control can be performed quickly.

【0043】[0043]

【発明の効果】以上説明したように、この発明によれ
ば、以下のような有用な効果がもたらされる。
As described above, the present invention has the following useful effects.

【0044】汚泥の集約処理において、送泥管に硫化水
素濃度監視手段やリン濃度監視手段を設置し、これらの
手段からのセンサー情報に基づいて、硫化水素、リン低
減の警告が発せられるので、受泥側集約処理場での臭気
の発生防止および返流水を受け入れる下水処理場におけ
るリン負荷軽減を効率良く行なうことが可能となる。
In the intensive treatment of sludge, a hydrogen sulfide concentration monitoring means and a phosphorus concentration monitoring means are installed in a sludge pipe, and a warning of hydrogen sulfide and phosphorus reduction is issued based on sensor information from these means. It is possible to efficiently prevent the generation of odor in the intensive treatment plant on the mud receiving side and reduce the phosphorus load in the sewage treatment plant receiving the return water efficiently.

【0045】また、前記センサー情報に基づいて、送泥
側下水処理場での硫化水素濃度制御と受泥側集約処理場
でのリン濃度制御とを自動的に操作する情報を与えるこ
とができるので、受泥側集約処理場での臭気の発生防止
および返流水を受け入れる下水処理場におけるリン負荷
軽減を更に効率良く行なうことが可能となる。
Also, information for automatically operating the hydrogen sulfide concentration control at the muddy sewage treatment plant and the phosphorus concentration control at the mud receiving intensive treatment plant can be given based on the sensor information. Thus, it is possible to more efficiently prevent the generation of odor in the intensive treatment plant on the mud receiving side and reduce the phosphorus load in the sewage treatment plant that receives the return water.

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

【図1】この発明のシステム全体の構成図である。FIG. 1 is a configuration diagram of the entire system of the present invention.

【図2】集約処理場における硫化水素発生の抑制処理フ
ローの一例を示すフロー図である。
FIG. 2 is a flowchart showing an example of a process flow of suppressing hydrogen sulfide generation in an integrated treatment plant.

【図3】硫化水素低減指示手段および下水処理場におけ
る硫化水素濃度制御手段の構成を示すブロック図であ
る。
FIG. 3 is a block diagram showing a configuration of a hydrogen sulfide reduction instruction unit and a hydrogen sulfide concentration control unit in a sewage treatment plant.

【図4】集約処理場におけるリン負荷抑制処理フローの
一例を示すフロー図である。
FIG. 4 is a flowchart showing an example of a phosphorus load suppression processing flow in an integrated processing plant.

【図5】リン低減指示手段および集約処理場におけるリ
ン濃度制御手段の構成を示すブロック図である。
FIG. 5 is a block diagram showing a configuration of a phosphorus reduction instructing unit and a phosphorus concentration control unit in an integrated treatment plant.

【符号の説明】[Explanation of symbols]

1A、1B、1C:下水処理場 2:集約処理場 3A、3B、3C:送泥管 4A、4B、4C:硫化水素濃度監視手段 5:硫化水素低減指示手段 6:入力部 7:演算部 8A、8B、8C:硫化水素濃度制御手段 9:曝気装置 10:曝気装置制御部 11:ポリ鉄添加装置 12:ポリ鉄添加装置制御部 13:返水管 14A、14B、14C、15:リン濃度監視手段 16:リン低減指示手段 17:入力部 18:演算部 19:リン濃度制御手段 20:脱リン剤添加装置 21:脱リン剤添加装置制御部 1A, 1B, 1C: Sewage treatment plant 2: Concentration treatment plant 3A, 3B, 3C: Sludge pipe 4A, 4B, 4C: Hydrogen sulfide concentration monitoring means 5: Hydrogen sulfide reduction instruction means 6: Input unit 7: Operation unit 8A , 8B, 8C: hydrogen sulfide concentration control means 9: aeration apparatus 10: aeration apparatus control section 11: polyiron addition apparatus 12: polyiron addition apparatus control section 13: return pipe 14A, 14B, 14C, 15: phosphorus concentration monitoring means 16: Phosphorus reduction instruction means 17: Input unit 18: Operation unit 19: Phosphorus concentration control means 20: Dephosphorizing agent adding device 21: Dephosphorizing agent adding device control unit

───────────────────────────────────────────────────── フロントページの続き (72)発明者 水野 健一郎 東京都千代田区丸の内一丁目1番2号 日 本鋼管株式会社内 Fターム(参考) 4D059 AA05 BF20 BK16 CB01 DA24 EA20 EB20  ────────────────────────────────────────────────── ─── Continuing on the front page (72) Inventor Kenichiro Mizuno 1-2-1 Marunouchi, Chiyoda-ku, Tokyo F-term in Nihon Kokan Co., Ltd. 4D059 AA05 BF20 BK16 CB01 DA24 EA20 EB20

Claims (8)

【特許請求の範囲】[Claims] 【請求項1】 単一または複数の下水処理場から排出さ
れた汚泥を、送泥管により汚泥集約処理場に集めて処理
した後、生成する汚泥脱離液を返水管により前記下水処
理場に返水する汚泥集約システムにおいて、 前記送泥管内の汚泥の硫化水素濃度監視手段と、前記硫
化水素濃度監視手段により監視された硫化水素濃度が設
定値を超えた場合に、当該汚泥管により汚泥を送出して
いる下水処理場に対して、送出汚泥中の硫化水素低減を
警告する硫化水素警告手段とを設けたことを特徴とする
汚泥集約処理システム。
After collecting and treating sludge discharged from a single or a plurality of sewage treatment plants by a sludge pipe, the sludge desorbed liquid generated is returned to the sewage treatment plant by a return pipe. In the sludge concentration system for returning water, the hydrogen sulfide concentration monitoring means of the sludge in the sludge pipe, and when the hydrogen sulfide concentration monitored by the hydrogen sulfide concentration monitoring means exceeds a set value, the sludge pipe is used to remove the sludge. A sludge intensive treatment system, comprising: a hydrogen sulfide warning unit for warning a reduction in hydrogen sulfide in the discharged sludge to a sewage treatment plant that is discharging.
【請求項2】 単一または複数の下水処理場から排出さ
れた汚泥を、送泥管により汚泥集約処理場に集めて処理
した後、生成する汚泥脱離液を返水管により前記下水処
理場に返水する汚泥集約処理システムにおいて、 前記送泥管内の汚泥の硫化水素濃度監視手段と、前記硫
化水素濃度監視手段により監視された硫化水素濃度が設
定値を超えた場合に、当該汚泥管により汚泥を送出して
いる下水処理場に対して、送出汚泥中の硫化水素低減指
示を発信する硫化水素低減指示手段と、前記硫化水素低
減指示手段からの信号に従って当該下水処理場における
硫化水素濃度を制御する硫化水素濃度制御手段とを設け
たことを特徴とする汚泥集約処理システム。
2. Sludge discharged from one or a plurality of sewage treatment plants is collected and treated by a sludge pipe in a sludge concentration treatment plant, and sludge desorbed liquid generated is returned to the sewage treatment plant by a return pipe. In the sludge concentration treatment system for returning water, the hydrogen sulfide concentration monitoring means of the sludge in the sludge pipe, and the hydrogen sulfide concentration monitored by the hydrogen sulfide concentration monitoring means, when the hydrogen sulfide concentration exceeds a set value, the sludge pipe by the sludge pipe. To the sewage treatment plant that is sending water, a hydrogen sulfide reduction instruction means for transmitting an instruction to reduce hydrogen sulfide in the sent sludge, and controlling the concentration of hydrogen sulfide in the sewage treatment plant in accordance with a signal from the hydrogen sulfide reduction instruction means And a hydrogen sulfide concentration control means.
【請求項3】 単一または複数の下水処理場から排出さ
れた汚泥を、送泥管により汚泥集約処理場に集めて処理
した後、生成する汚泥脱離液を返水管により前記下水処
理場に返水する汚泥集約処理システムにおいて、 前記返水管内の汚泥のリン濃度監視手段と、前記リン濃
度監視手段により監視されたリン濃度が設定値を超えた
場合に、前記汚泥集約処理場に対して、送出汚泥脱離液
中のリン低減を警告するリン警告手段とを設けたことを
特徴とする汚泥集約処理システム。
3. Sludge discharged from one or a plurality of sewage treatment plants is collected and treated in a sludge concentration treatment plant by a sludge pipe, and the generated sludge desorbed liquid is returned to the sewage treatment plant by a return pipe. In the sludge concentration processing system for returning water, the phosphorus concentration monitoring means of the sludge in the return pipe, and when the phosphorus concentration monitored by the phosphorus concentration monitoring means exceeds a set value, the sludge concentration treatment plant And a phosphorus warning means for warning that phosphorus in the discharged sludge desorbed liquid has been reduced.
【請求項4】 単一または複数の下水処理場から排出さ
れた汚泥を、送泥管により汚泥集約処理場に集めて処理
した後、生成する汚泥脱離液を返水管により前記下水処
理場に返水する汚泥集約処理システムにおいて、 前記返水管内の汚泥のリン濃度監視手段と、前記リン濃
度監視手段により監視されたリン濃度が設定値を超えた
場合に、前記汚泥集約処理場に対して、送出汚泥脱離液
中のリン低減指示を発信するリン低減指示手段と、前記
リン低減指示手段からの信号に従って前記汚泥集約処理
場におけるリン濃度を制御するリン濃度制御手段とを設
けたことを特徴とする汚泥集約処理システム。
4. After collecting and treating sludge discharged from one or a plurality of sewage treatment plants in a sludge concentration treatment plant by a sludge pipe, the sludge desorbed liquid generated is returned to the sewage treatment plant by a return pipe. In the sludge concentration processing system for returning water, the phosphorus concentration monitoring means of the sludge in the return pipe, and when the phosphorus concentration monitored by the phosphorus concentration monitoring means exceeds a set value, the sludge concentration treatment plant And a phosphorus reduction instruction means for transmitting a phosphorus reduction instruction in the discharged sludge desorbed liquid, and a phosphorus concentration control means for controlling the phosphorus concentration in the sludge concentration treatment plant according to a signal from the phosphorus reduction instruction means. Sludge intensive treatment system.
【請求項5】 単一または複数の下水処理場から排出さ
れた汚泥を、送泥管により汚泥集約処理場に集めて処理
した後、生成する汚泥脱離液を返水管により前記下水処
理場に返水する汚泥集約システムにおいて、 前記送泥管内の汚泥の硫化水素濃度監視手段と、前記硫
化水素濃度監視手段により監視された硫化水素濃度が設
定値を超えた場合に、当該汚泥管により汚泥を送出して
いる下水処理場に対して、送出汚泥中の硫化水素低減を
警告する硫化水素警告手段と、前記返水管内の汚泥のリ
ン濃度監視手段と、前記リン濃度監視手段により監視さ
れたリン濃度が設定値を超えた場合に、前記汚泥集約処
理場に対して、送出汚泥脱離液中のリン低減を警告する
リン警告手段とを設けたことを特徴とする汚泥集約処理
システム。
5. Sludge discharged from one or a plurality of sewage treatment plants is collected and treated in a sludge concentration treatment plant by a sludge pipe, and the generated sludge desorbed liquid is returned to the sewage treatment plant by a return pipe. In the sludge collecting system for returning water, the hydrogen sulfide concentration monitoring means of the sludge in the sludge pipe, and when the hydrogen sulfide concentration monitored by the hydrogen sulfide concentration monitoring means exceeds a set value, the sludge pipe removes the sludge. A hydrogen sulfide warning unit that warns the sending sewage treatment plant of a reduction in hydrogen sulfide in the discharged sludge, a phosphorus concentration monitoring unit for the sludge in the return pipe, and a phosphorus concentration monitored by the phosphorus concentration monitoring unit. A sludge concentration treatment system, comprising: a phosphorus warning means for warning the sludge concentration treatment plant of a decrease in phosphorus in the discharged sludge desorbed liquid when the concentration exceeds a set value.
【請求項6】 単一または複数の下水処理場から排出さ
れた汚泥を、送泥管により汚泥集約処理場に集めて処理
した後、生成する汚泥脱離液を返水管により前記下水処
理場に返水する汚泥集約処理システムにおいて、 前記送泥管内の汚泥の硫化水素濃度監視手段と、前記硫
化水素濃度監視手段により監視された硫化水素濃度が設
定値を超えた場合に、当該汚泥管により汚泥を送出して
いる下水処理場に対して、送出汚泥中の硫化水素低減指
示を発信する硫化水素低減指示手段と、前記硫化水素低
減指示手段からの信号に従って当該下水処理場における
硫化水素濃度を制御する硫化水素濃度制御手段と、前記
返水管内の汚泥のリン濃度監視手段と、前記リン濃度監
視手段により監視されたリン濃度が設定値を超えた場合
に、前記汚泥集約処理場に対して、送出汚泥脱離液中の
リン低減指示を発信するリン低減指示手段と、前記リン
低減指示手段からの信号に従って前記汚泥集約処理場に
おけるリン濃度を制御するリン濃度制御手段とを設けた
ことを特徴とする汚泥集約処理システム。
6. Sludge discharged from one or a plurality of sewage treatment plants is collected and treated by a sludge pipe at a sludge concentration treatment plant, and the generated sludge desorbed liquid is returned to the sewage treatment plant by a return pipe. In the sludge concentration treatment system for returning water, the hydrogen sulfide concentration monitoring means of the sludge in the sludge pipe, and the hydrogen sulfide concentration monitored by the hydrogen sulfide concentration monitoring means, when the hydrogen sulfide concentration exceeds a set value, the sludge pipe by the sludge pipe. To the sewage treatment plant that is sending water, a hydrogen sulfide reduction instruction means for transmitting an instruction to reduce hydrogen sulfide in the sent sludge, and controlling the concentration of hydrogen sulfide in the sewage treatment plant in accordance with a signal from the hydrogen sulfide reduction instruction means Means for controlling the concentration of hydrogen sulfide, means for monitoring the phosphorus concentration of sludge in the return pipe, and when the phosphorus concentration monitored by the means for monitoring phosphorus concentration exceeds a set value, the sludge concentration treatment plant On the other hand, there are provided phosphorus reduction instruction means for transmitting a phosphorus reduction instruction in the discharged sludge desorbed liquid, and phosphorus concentration control means for controlling the phosphorus concentration in the sludge concentration treatment plant according to a signal from the phosphorus reduction instruction means. A sludge intensive treatment system characterized by the following.
【請求項7】 前記硫化水素濃度監視手段、前記硫化水
素低減指示手段および前記硫化水素濃度制御手段の内の
少なくとも1つは、前記送泥管に敷設された光ファイバ
ーを使用して通信を行なうものであることを特徴とす
る、請求項1、2、5または6記載の汚泥集約処理シス
テム。
7. At least one of the hydrogen sulfide concentration monitoring means, the hydrogen sulfide reduction instruction means, and the hydrogen sulfide concentration control means performs communication using an optical fiber laid in the mud pipe. The sludge concentration processing system according to claim 1, 2, 5, or 6, wherein
【請求項8】 前記リン濃度監視手段、前記リン低減指
示手段および前記リン濃度制御手段の内の少なくとも1
つは、前記返水管に敷設された光ファイバーを使用して
通信を行なうものであることを特徴とする、請求項3、
4、5または6記載の汚泥集約処理システム。
8. At least one of said phosphorus concentration monitoring means, said phosphorus reduction instruction means and said phosphorus concentration control means.
The third is that communication is performed using an optical fiber laid on the return pipe, wherein:
7. The sludge intensive treatment system according to 4, 5, or 6.
JP2001027784A 2001-02-05 2001-02-05 Sludge intensive treatment system Expired - Fee Related JP3620450B2 (en)

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Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100734861B1 (en) 2005-12-08 2007-07-03 한국전자통신연구원 System for real-time monitoring odor and method thereof
JP2013169506A (en) * 2012-02-20 2013-09-02 Nippon Hume Corp Sewage sludge treatment support device and support method
JP2016190190A (en) * 2015-03-31 2016-11-10 株式会社石垣 Sludge treatment system and sludge treatment method
JP2017000980A (en) * 2015-06-12 2017-01-05 水ing株式会社 Wastewater treatment method and system

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100734861B1 (en) 2005-12-08 2007-07-03 한국전자통신연구원 System for real-time monitoring odor and method thereof
JP2013169506A (en) * 2012-02-20 2013-09-02 Nippon Hume Corp Sewage sludge treatment support device and support method
JP2016190190A (en) * 2015-03-31 2016-11-10 株式会社石垣 Sludge treatment system and sludge treatment method
JP2017000980A (en) * 2015-06-12 2017-01-05 水ing株式会社 Wastewater treatment method and system

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