JP2016190190A - Sludge treatment system and sludge treatment method - Google Patents

Sludge treatment system and sludge treatment method Download PDF

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JP2016190190A
JP2016190190A JP2015070930A JP2015070930A JP2016190190A JP 2016190190 A JP2016190190 A JP 2016190190A JP 2015070930 A JP2015070930 A JP 2015070930A JP 2015070930 A JP2015070930 A JP 2015070930A JP 2016190190 A JP2016190190 A JP 2016190190A
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sludge
fibrous material
treatment
fibrous
sent
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JP6298792B2 (en
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山下 学
Manabu Yamashita
学 山下
康隆 末次
Yasutaka Suetsugu
康隆 末次
英司 杤岡
Eiji Tochioka
英司 杤岡
博英 山本
Hirohide Yamamoto
博英 山本
碓井 次郎
Jiro Usui
次郎 碓井
旬 岩崎
Jun Iwasaki
旬 岩崎
正夫 島田
Masao Shimada
正夫 島田
十四日 三宅
Toshika Miyake
十四日 三宅
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Japan Sewage Works Agency
Ishigaki Co Ltd
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Ishigaki Co Ltd
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Abstract

PROBLEM TO BE SOLVED: To provide a sludge treatment system capable of preventing decay of a fibrous material contained in sludge, thereby stably supplying, as a dehydration auxiliary agent, the fibrous material during dehydration at an intensive treatment plant.SOLUTION: Sludge and a fibrous material are separated from each other at each local treatment plant, and are transported via separate pipelines to an intensive treatment plant. The sludge and the fibrous material are separately stored at the intensive treatment plant, and a sludge treatment, such as dehydration, is carried out by supplying the fibrous material to the sludge.SELECTED DRAWING: Figure 1

Description

本発明は、汚泥処理システム及び汚泥処理方法に係り、詳しくは汚泥と繊維状物とを分けて移送する汚泥処理システム及び汚泥処理方法に関する。   The present invention relates to a sludge treatment system and a sludge treatment method, and more particularly, to a sludge treatment system and a sludge treatment method for transferring sludge and fibrous materials separately.

下水処理場の汚泥にはトイレットペーパーに由来する多量のセルロース系の繊維状物が含有されている。脱水機で安定的に低含水率の脱水ケーキを生成するためには、汚泥中に含まれる繊維分(セルロース成分)が大きく影響することが知られているが、日間変動や季節変動により汚泥に含まれる繊維状物の含有量が変動するため、安定的な脱水処理ができない。   The sludge in the sewage treatment plant contains a large amount of cellulosic fibrous material derived from toilet paper. In order to stably produce a dehydrated cake with a low water content by a dehydrator, it is known that the fiber content (cellulose component) contained in the sludge is greatly affected. Since the content of the fibrous material contained fluctuates, stable dehydration cannot be performed.

近年、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(ローカル)より送泥管で汚泥を集めて集約処理場において一括処理する方法が採用されている(たとえば、特許文献1、特許文献2を参照)。   In recent years, sludge treatment in urban areas does not have sludge treatment facilities for each individual sewage treatment plant, but collects sludge from a plurality of sewage treatment plants (local) through sludge pipes and performs batch treatment at an integrated treatment plant. A method is employed (see, for example, Patent Document 1 and Patent Document 2).

一般的にローカル処理場では、下水処理場に流入してくる原水について、水処理を施して放流し、汚泥は初沈汚泥と余剰汚泥を混合した状態で集約処理場に送っている。複数のローカル処理場から送られる汚泥量や汚泥性状が変動し、集約処理場では安定した汚泥処理(消化・脱水等)を行うことが困難となることがあった。   In general, in a local treatment plant, raw water flowing into a sewage treatment plant is subjected to water treatment and discharged, and sludge is sent to an intensive treatment plant in a state where primary sludge and excess sludge are mixed. The amount of sludge and sludge properties sent from a plurality of local treatment plants fluctuated, and it was sometimes difficult to perform stable sludge treatment (digestion, dehydration, etc.) at an integrated treatment plant.

特許文献1に記載の発明では、有機性汚水の処理槽で発生する汚泥を分離して脱水する汚泥の処理方法において、処理槽に流入する汚水からセルロース系の繊維分を回収するとともに、この繊維分を添加して汚泥を脱水している。   In the invention described in Patent Document 1, in a sludge treatment method for separating and dewatering sludge generated in a treatment tank of organic wastewater, cellulosic fibers are recovered from the wastewater flowing into the treatment tank, and this fiber Sludge is dehydrated by adding a minute.

特許文献2に記載の発明は、各下水処理場から汚泥集約処理場に汚泥を送泥する際に汚泥が腐敗し、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ことを防止するものである。   The invention described in Patent Document 2 prevents sludge from decaying when sludge is sent from each sewage treatment plant to the sludge intensive treatment plant, and generating an odor due to hydrogen sulfide in the intensive treatment plant on the receiving mud side. Is.

特開2003−80299号JP 2003-80299 A 特開2002−224693号JP 2002-224663 A

従来の方式では、移送中に汚泥性状が極端に変質することがあり、集約処理場で汚泥処理を行う際に、低含有率の脱水ケーキを安定的に生成することが困難となることがある。具体的には、気温の高い夏季や輸送距離が長いほど、集約処理場に移送されるまでに汚泥中の有機物の腐敗の影響により繊維状物も腐敗する。その結果、汚泥中の繊維分が減少して汚泥の脱水性が悪化し、たとえば、脱水機の前段にて高価な凝集剤や脱水助材を大量に投与する必要がある。   In the conventional method, the sludge properties may be extremely altered during transfer, and it may be difficult to stably produce a dehydrated cake with a low content when performing sludge treatment at an intensive treatment plant. . Specifically, as the temperature is high in summer and the transport distance is longer, the fibrous material also rots due to the effect of organic matter rot in the sludge before being transferred to the intensive treatment plant. As a result, the fiber content in the sludge is reduced and the dewaterability of the sludge is deteriorated. For example, it is necessary to administer a large amount of an expensive flocculant and dewatering aid at the front stage of the dehydrator.

特許文献1の発明では、汚水処理場で発生する汚泥から繊維分を脱水助材として添加しているが、汚水から繊維分を全量回収しているため、回収装置の負荷が大きい。また、通常、繊維分のみを回収することが困難であり、他の腐敗し易い有機物(食品残渣等)も一緒に回収することになり、保管時に有機物の腐敗の影響を受けて繊維分も腐敗する。   In invention of patent document 1, although the fiber part is added as a dehydration auxiliary material from the sludge generated in a sewage treatment plant, since the whole fiber part is collect | recovered from sewage, the load of a collection | recovery apparatus is large. In addition, it is usually difficult to recover only the fiber, and other perishable organic substances (food residues, etc.) will also be collected together. The fiber will also be spoiled due to the effects of organic spoilage during storage. To do.

特許文献2の発明では、汚泥腐敗による臭気対策は可能であるが、ローカル処理場から集約処理場に繊維分を分離して移送することはできない。   In the invention of Patent Document 2, it is possible to take measures against odor due to sludge decay, but it is not possible to separate and transfer fibers from the local treatment plant to the central treatment plant.

本発明は、上記問題点に鑑みてなされたものであり、繊維状物の腐敗を防止してローカル処理場から集約処理場へ汚泥と繊維状物を個別に移送し、集約処理場で汚泥の脱水時に繊維状物を脱水助材として安定して供給できる汚泥処理システム及びその方法を提供する。すなわち、汚泥の脱水性や消化ガス生成量に大きな影響を与える繊維状物を腐敗させずにローカル処理場から集約処理場移送し、集約処理場で安定した脱水処理や消化処理等の汚泥処理をすることができる汚泥処理システム及びその方法を提供することを目的とする。   The present invention has been made in view of the above problems, and prevents sludge of fibrous materials and individually transfers sludge and fibrous materials from a local treatment plant to an intensive treatment plant. Provided are a sludge treatment system and method capable of stably supplying a fibrous material as a dehydration aid during dehydration. In other words, fibrous materials that have a large impact on the sludge dewaterability and digestion gas production amount are transferred from the local treatment plant to the central treatment plant without being spoiled, and sludge treatment such as stable dehydration and digestion treatment is performed at the central treatment plant. It is an object of the present invention to provide a sludge treatment system and a method thereof.

請求項1に記載の発明は、ローカル処理場の内少なくとも1つで汚泥から繊維状物を分離回収する繊維状物分離回収装置と、前記汚泥を前記ローカル処理場から集約処理場まで圧送ポンプを用いて送る汚泥搬送部と、前記繊維状物分離回収装置で分離回収された繊維状物を、前記ローカル処理場から前記集約処理場まで送る繊維状物搬送部と、前記集約処理場で、前記汚泥搬送部で送られてきた汚泥に、前記繊維状物搬送部で送られてきた繊維状物を混合し、この混合されたものを汚泥処理する汚泥処理装置とを有することを特徴とする。   According to the first aspect of the present invention, there is provided a fibrous material separation and recovery device that separates and recovers fibrous material from sludge in at least one of the local treatment plants, and a pump for pumping the sludge from the local treatment plant to the centralized treatment plant. The sludge transport unit that is used to send the fibrous material separated and recovered by the fibrous material separation and recovery device, the fibrous material transport unit that sends the local processing plant to the central processing plant, and the central processing plant, It has a sludge treatment apparatus which mixes the fibrous material sent by the said fibrous material conveyance part with the sludge sent by the sludge conveyance part, and sludge-treats this mixed thing.

請求項2に記載の発明は、請求項1に記載の汚泥処理システムにおいて、前記集約処理場には、前記繊維状物搬送部で送られてきた繊維状物を蓄える繊維状物貯留部が設けられており、前記汚泥処理装置は、前記汚泥搬送部で送られてきた汚泥に、前記繊維状物貯留部に蓄えられている繊維状物を混合し、この混合されたものを汚泥処理するように構成されていることを特徴とする。   According to a second aspect of the present invention, in the sludge treatment system according to the first aspect, the aggregate treatment plant is provided with a fibrous material storage unit for storing the fibrous material sent by the fibrous material conveying unit. The sludge treatment device mixes the fibrous material stored in the fibrous material storage unit with the sludge sent by the sludge transport unit, and sludges the mixed material. It is comprised by these.

請求項3に記載の発明は、請求項2に記載の汚泥処理システムにおいて、前記集約処理場で、前記汚泥搬送部で送られてきた汚泥中の繊維状物の濃度を測定する繊維状物濃度測定部を有し、前記繊維状物濃度測定部で測定した結果、繊維状物の濃度が所定の値よりも低い場合に、前記繊維状物貯留部に蓄えられている繊維状物を混合し、この混合されたものを前記汚泥処理装置で汚泥処理するように構成されていることを特徴とする。   The invention according to claim 3 is the sludge treatment system according to claim 2, wherein the concentration of the fibrous material for measuring the concentration of the fibrous material in the sludge sent by the sludge transport unit at the aggregation treatment plant. When the concentration of the fibrous material is lower than a predetermined value as a result of measurement by the fibrous material concentration measuring unit, the fibrous material stored in the fibrous material storage unit is mixed. The mixed product is configured to be sludge treated with the sludge treatment apparatus.

請求項4に記載の発明は、請求項1〜請求項3のいずれか1項に記載の汚泥処理システムにおいて、前記汚泥処理装置は、前記混合されたものを脱水処理する脱水処理装置、前記混合されたものを消化処理する消化処理装置の少なくともいずれかで構成されていることを特徴とする。   The invention according to claim 4 is the sludge treatment system according to any one of claims 1 to 3, wherein the sludge treatment device is a dehydration treatment device for dehydrating the mixed material, and the mixing. It is characterized by comprising at least one of digestion processing apparatuses for digesting processed products.

請求項5に記載の発明は、ローカル処理場の内少なくとも1つで汚泥から繊維状物を分離回収する繊維状物分離回収工程と、前記汚泥を前記ローカル処理場から集約処理場まで圧送ポンプを用いて送る汚泥搬送工程と、前記繊維状物分離回収工程で分離回収された繊維状物を、前記ローカル処理場から前記集約処理場まで送る繊維状物搬送工程と、前記集約処理場で、前記汚泥搬送工程で送られてきた汚泥に、前記繊維状物搬送工程で送られてきた繊維状物を混合し、この混合されたものを汚泥処理する汚泥処理工程とを含むことを特徴とする。   According to a fifth aspect of the present invention, there is provided a fibrous material separation and recovery step for separating and recovering fibrous material from sludge at at least one of the local treatment plants, and a pump for pumping the sludge from the local treatment plant to the centralized treatment plant. The sludge transporting step to send using, the fibrous material separated and recovered in the fibrous material separation and recovery step, the fibrous material transporting step to send from the local treatment plant to the aggregation processing plant, and the aggregation processing plant, A sludge treatment step of mixing the fibrous material sent in the fibrous material conveyance step with the sludge sent in the sludge conveyance step, and sludge treating the mixed material.

請求項6に記載の発明は、請求項5に記載の汚泥処理方法において、前記集約処理場では、前記繊維状物搬送工程で送られてきた繊維状物を蓄える繊維状物貯留工程を実行し、前記汚泥処理工程は、前記汚泥搬送工程で送られてきた汚泥に、前記繊維状物貯留工程で蓄えられている繊維状物を混合し、この混合されたものを汚泥処理するように構成されていることを特徴とする。   The invention according to claim 6 is the sludge treatment method according to claim 5, wherein the aggregate treatment plant executes a fibrous material storage step for storing the fibrous material sent in the fibrous material conveyance step. The sludge treatment step is configured to mix the fibrous material stored in the fibrous material storage step with the sludge sent in the sludge transporting step, and sludge the mixed material. It is characterized by.

請求項7に記載の発明は、請求項6に記載の汚泥処理方法において、前記集約処理場では、前記汚泥搬送工程で送られてきた汚泥中の繊維状物の濃度を測定する繊維状物濃度測定工程を実行し、前記繊維状物濃度測定工程で測定した結果、繊維状物の濃度が所定の値よりも低い場合に、前記繊維状物貯留工程で蓄えられている繊維状物を混合し、この混合されたものを前記汚泥処理工程で汚泥処理するように構成されていることを特徴とする。   The invention according to claim 7 is the sludge treatment method according to claim 6, wherein the concentration of the fibrous material for measuring the concentration of the fibrous material in the sludge sent in the sludge conveying step in the aggregation treatment plant. As a result of executing the measurement step and measuring the fibrous material concentration measurement step, the fibrous material stored in the fibrous material storage step is mixed when the concentration of the fibrous material is lower than a predetermined value. The mixed material is configured to be sludge treated in the sludge treatment step.

請求項8に記載の発明は、請求項5〜請求項7のいずれか1項に記載の汚泥処理システムにおいて、前記汚泥処理工程は、前記混合されたものを脱水処理する脱水処理工程、前記混合されたものを消化処理する消化処理工程の少なくともいずれかで構成されていることを特徴とする。   The invention according to claim 8 is the sludge treatment system according to any one of claims 5 to 7, wherein the sludge treatment step is a dehydration treatment step of dehydrating the mixed one, and the mixing It is characterized by comprising at least one of digestion processing steps for digesting the processed product.

本発明によれば、脱水性に影響の大きい繊維状物を腐敗する前に汚泥から回収し、汚泥処理助材として集約処理場の汚泥に添加するので、別途汚泥処理助材を購入する必要がなく、輸送費や在庫管理、保管スペース等が不要になるという効果を奏する。   According to the present invention, the fibrous material having a great influence on the dewaterability is recovered from the sludge before being spoiled and added to the sludge of the intensive treatment plant as a sludge treatment aid. Therefore, it is necessary to purchase a sludge treatment aid separately. In addition, there is an effect that transportation costs, inventory management, storage space, and the like are unnecessary.

また、脱水機に供給する汚泥中の繊維分濃度を常時一定レベルに維持でき、安定的に低含水率の脱水ケーキを生成可能な汚泥に改質できる。そして、安定的に低含水率の脱水ケーキを生成するので、脱水ケーキの輸送、処分するためのランニングコストを低減できる。   In addition, the fiber concentration in the sludge supplied to the dehydrator can be constantly maintained at a constant level, and the sludge can be stably reformed to produce a dehydrated cake having a low water content. And since the dehydrated cake of low moisture content is produced | generated stably, the running cost for transport and disposal of a dehydrated cake can be reduced.

さらに、消化槽へ繊維状物を添加すると消化ガスの生成量を増加させることができる。下水処理場からの回収エネルギーが増加し、下水処理場の自家発電あるいは周辺施設へのエネルギー供給に寄与する。   Furthermore, when a fibrous material is added to the digestion tank, the amount of digestion gas produced can be increased. The energy recovered from the sewage treatment plant will increase, contributing to in-house power generation at the sewage treatment plant or energy supply to surrounding facilities.

汚泥処理システムの概略を示す概略図である。It is the schematic which shows the outline of a sludge processing system. 汚泥処理方法の動作を示すフローチャートである。It is a flowchart which shows operation | movement of the sludge processing method.

本実施の形態に係る汚泥処理システム1は、図1で示すように、たとえば複数のローカル処理場3,4,5と、繊維状物分離回収装置3A,4A,5Aと、汚泥搬送部12,14,16と、繊維状物搬送部13,15,17と、汚泥処理装置(たとえば、消化処理装置(消化槽)2Dあるいは脱水処理装置2A)が設けられている集約処理場2とを備えて構成されている。なお、消化処理装置2D、脱水処理装置2Aは、これらの少なくともいずれかが設けられている構成であってもよい。   As shown in FIG. 1, the sludge treatment system 1 according to the present embodiment includes, for example, a plurality of local treatment plants 3, 4, 5, fibrous material separation and recovery devices 3 </ b> A, 4 </ b> A, 5 </ b> A, a sludge transport unit 12, 14, 16, a fibrous material transfer unit 13, 15, 17, and an aggregation treatment plant 2 in which a sludge treatment device (for example, a digestion treatment device (digestion tank) 2D or a dehydration treatment device 2A) is provided. It is configured. Note that the digestion processing device 2D and the dehydration processing device 2A may have at least one of them.

各繊維状物分離回収装置3A、4A、5Aは、お互いが離れた各ローカル処理場3,4,5内に設置されており、繊維状物分離回収装置3Aでは、家庭から下水道管等を介して集められた汚泥から繊維状物を分離回収するようになっている。   Each of the fibrous material separation / recovery devices 3A, 4A, 5A is installed in each of the local treatment plants 3, 4, 5 separated from each other. In the fibrous material separation / recovery device 3A, a sewer pipe or the like is used from the home. The fibrous material is separated and collected from the collected sludge.

なお、繊維状物分離回収装置3Aでは、汚泥の一部から繊維状物を分離回収するようになっているが、汚泥の総てから繊維状物を分離回収するようになっていてもよい。   In the fibrous material separation and recovery apparatus 3A, the fibrous material is separated and recovered from a part of the sludge. However, the fibrous material may be separated and recovered from the entire sludge.

汚泥搬送部12は、ローカル処理場3から集約処理場2へ汚泥を搬送するようになっている。さらに説明すると、汚泥搬送部12は、繊維状物分離回収装置3Aで繊維状物が回収された汚泥(一部の汚泥から繊維状物を回収する場合にあっては、繊維状物が回収されなかった汚泥を含む)をローカル処理場3から集約処理場2まで圧送ポンプP1と汚泥搬送用配管6とを用いて送るようになっている。なお、汚泥搬送用配管6や圧送ポンプP1として、従前使用されていたものをほぼそのまま使用する。   The sludge transport unit 12 transports sludge from the local processing plant 3 to the central processing plant 2. More specifically, the sludge transport unit 12 is configured to collect the sludge from which the fibrous material is collected by the fibrous material separation and recovery device 3A (if the fibrous material is collected from some sludge, the fibrous material is collected. (Including the sludge that was not present) is sent from the local treatment plant 3 to the centralized treatment plant 2 using the pressure feed pump P1 and the sludge carrying pipe 6. In addition, what was used conventionally is used as it is as the sludge conveyance piping 6 and the pressure feed pump P1.

各汚泥搬送部14,16も、汚泥搬送部12と同様に、ローカル処理場4,5から集約処理場2へ汚泥を搬送するようになっており、各繊維状物分離回収装置4A,5Aで繊維状物が回収された汚泥を各ローカル処理場4,5から集約処理場2まで各圧送ポンプP3,P5と各汚泥搬送用配管8,10とを用いて送るようになっている。   Similarly to the sludge transport unit 12, each sludge transport unit 14 and 16 transports sludge from the local treatment plants 4 and 5 to the intensive treatment plant 2, and each of the fibrous material separation and recovery devices 4A and 5A The sludge from which the fibrous material has been collected is sent from the local treatment plants 4 and 5 to the central treatment plant 2 by using the pressure pumps P3 and P5 and the sludge transfer pipes 8 and 10, respectively.

繊維状物搬送部13は、繊維状物分離回収装置3Aで分離回収された繊維状物を、ローカル処理場3から集約処理場2まで、たとえば、圧送ポンプP2と汚泥搬送用配管6、8、10とは別の繊維状物搬送用配管7とを用いて送るようになっている。   The fibrous material transfer unit 13 is configured to transfer the fibrous material separated and recovered by the fibrous material separation and recovery device 3A from the local processing site 3 to the aggregation processing site 2, for example, a pumping pump P2 and sludge transfer pipes 6, 8, 10 is sent using a fibrous material transfer pipe 7 different from 10.

また、各繊維状物搬送部15,17も、繊維状物搬送部13と同様に、各繊維状物分離回収装置4A,5Aで分離回収された繊維状物を、各ローカル処理場4,5から集約処理場2まで、たとえば、各圧送ポンプP4,P6と、各汚泥搬送用配管6,8,10,7とは別の各繊維状物搬送用配管9,11とを用いて送るようになっている。   Similarly to the fibrous material conveying unit 13, the fibrous material conveying units 15 and 17 also receive the fibrous material separated and collected by the fibrous material separating and collecting devices 4A and 5A, respectively, in the local processing plants 4 and 5. To the central processing station 2 using, for example, the pumps P4 and P6 and the fibrous material transport pipes 9 and 11 different from the sludge transport pipes 6, 8, 10, and 7, respectively. It has become.

集約処理場2では、上記汚泥処理装置を用いて、各汚泥搬送部12,14,16で送られてきた汚泥に、各繊維状物搬送部13,15,17で送られてきた繊維状物を混合し、この混合されたものを汚泥処理するようになっている。   In the intensive treatment plant 2, using the sludge treatment apparatus, the fibrous material sent by the fibrous material transport units 13, 15, and 17 to the sludge sent by the sludge transport units 12, 14, and 16. Is mixed, and the mixed product is treated with sludge.

たとえば、集約処理場2で脱水処理装置2Aを用いて、各汚泥搬送部12,14,16で送られてきた汚泥に、各繊維状物搬送部13,15,17で送られてきた繊維状物を混合し、この混合されたものを(ただちに;たとえば、繊維状物の腐敗が始まって繊維状物の脱水性を担保する機能が損なわれる前に)脱水処理するようになっている。   For example, using the dewatering apparatus 2A in the intensive treatment plant 2, the fibrous material sent by the fibrous material transport units 13, 15, 17 to the sludge sent by the sludge transport units 12, 14, 16 The mixture is mixed, and the mixture is dehydrated (immediately; for example, before the decay of the fibrous material begins to impair the function of ensuring the dehydrating property of the fibrous material).

以上により、各ローカル処理場3,4,5で汚泥から繊維状物を分離回収し、汚泥を各ローカル処理場3,4,5から集約処理場2まで各圧送ポンプP1,P3,P5を用いて送り、各ローカル処理場3,4,5で分離回収された繊維状物を、各ローカル処理場3,4,5から集約処理場2まで送り、集約処理場2で、送られてきた汚泥に、送られてきた繊維状物を混合し、この混合されたものを脱水処理するので、低含水率の脱水ケーキを安定して生成することができる。   As described above, the fibrous material is separated and recovered from the sludge at each of the local treatment plants 3, 4 and 5, and the sludge is sent from each of the local treatment plants 3, 4, 5 to the central treatment plant 2 using the pumps P1, P3, and P5. The sludge sent from the local treatment plants 3, 4 and 5 to the central treatment plant 2 and sent from the local treatment plants 3, 4 and 5 to the central treatment plant 2 In addition, since the fed fibrous material is mixed and the mixed material is dehydrated, a dehydrated cake having a low water content can be stably produced.

すなわち、各ローカル処理場3,4,5から集約処理場2まで送られた汚泥が腐敗しても、各ローカル処理場3,4,5から集約処理場2まで送られた繊維状物が腐敗することはない。そして、集約処理場2まで送られた汚泥に集約処理場2まで送られてきた繊維状物(脱水機能を担保する繊維状物)を加えて混同した後ただちに、脱水処理をするので、低含水率の脱水ケーキを安定して生成することができる。   That is, even if the sludge sent from each local treatment plant 3, 4, 5 to the central treatment plant 2 rots, the fibrous material sent from each local treatment plant 3, 4, 5 to the central treatment plant 2 rots. Never do. And after adding the fibrous material (fibrous material that guarantees the dehydration function) sent to the intensive treatment plant 2 to the sludge sent to the intensive treatment plant 2, the dehydration process is performed immediately, so the water content is low. Rate dehydrated cake can be produced stably.

なお、上述したように、少なくとも一部の集約処理場2に脱水処理装置2Aを設けることに代えてもしくは加えて消化処理装置2Dを設けてもよい。そして、集約処理場2において、脱水処理装置2Aを用いて上記混合されたものを脱水処理することに代えてもしくは加えて、上記混合されたものを消化処理装置2Dで消化処理するように構成してもよい。消化処理とは、汚泥を嫌気性微生物の作用で安定化し減量化するために行われる処理である。   As described above, a digestion processing apparatus 2D may be provided in place of or in addition to providing the dehydration processing apparatus 2A in at least a part of the aggregation processing sites 2. Then, instead of or in addition to dehydrating the mixed material using the dehydrating device 2A, the mixed material is digested by the digesting device 2D in the intensive treatment facility 2. May be. The digestion process is a process performed to stabilize and reduce sludge by the action of anaerobic microorganisms.

集約処理場2に脱水処理装置2Aと消化処理装置2Dとを設けた場合、先に消化処理装置2Dで消化処理をし、この消化処理がされたものに水処理装置2Aで脱水処理することとする。   In the case where the dehydration treatment apparatus 2A and the digestion treatment apparatus 2D are provided in the central processing place 2, the digestion treatment apparatus 2D is first digested, and the digestion process is performed on the water treatment apparatus 2A. To do.

また、汚泥処理システム1では、集約処理場2に、各繊維状物搬送部13,15,17で送られてきた繊維状物を(一時的に)蓄える繊維状物貯留部2Bが設けられており、脱水処理装置2Aが、各汚泥搬送部12,14,16で送られてきた汚泥に、繊維状物貯留部2Bに蓄えられている繊維状物を混合し、この混合されたものを上記汚泥処理(脱水処理、消化処理)するようになっている。これにより、安定した態様で繊維状物を汚泥処理装置(脱水処理装置2A、消化処理装置2D)に供給することができる。   Further, in the sludge treatment system 1, the aggregate treatment plant 2 is provided with a fibrous material storage unit 2B that (temporarily) stores the fibrous materials sent by the fibrous material conveying units 13, 15, and 17. In addition, the dewatering treatment apparatus 2A mixes the fibrous material stored in the fibrous material storage unit 2B with the sludge sent by the respective sludge transport units 12, 14, and 16, and the mixed material is mixed with the above. Sludge treatment (dehydration treatment, digestion treatment) is designed. Thereby, the fibrous material can be supplied to the sludge treatment apparatus (dehydration treatment apparatus 2A, digestion treatment apparatus 2D) in a stable manner.

さらに汚泥処理システム1では、集約処理場2に、各汚泥搬送部12,14,16で送られてきた汚泥中の繊維状物の濃度を測定する繊維状物濃度測定部2Cが設けられている。そして、繊維状物濃度測定部2Cで測定した結果、繊維状物の濃度が所定の値よりも低い場合に、繊維状物貯留部2Bに蓄えられている繊維状物を混合し、この混合されたものを上記汚泥処理(脱水処理、消化処理)するようになっている。これにより、汚泥処理装置(脱水処理装置2A、消化処理装置2D)において安定した態様で脱水処理、消化処理をすることができる。   Further, in the sludge treatment system 1, the aggregate treatment site 2 is provided with a fibrous substance concentration measuring unit 2 </ b> C that measures the concentration of the fibrous substance in the sludge sent by each sludge transport unit 12, 14, 16. . And when the density | concentration of a fibrous material is lower than a predetermined value as a result of measuring with 2C of fibrous substance density | concentration measurement parts, the fibrous substance stored in the fibrous substance storage part 2B is mixed, and this mixing is carried out. The above-mentioned sludge treatment (dehydration treatment, digestion treatment) is performed. Thereby, a dehydration process and a digestion process can be performed in the stable aspect in the sludge process apparatus (Dehydration process apparatus 2A, digestion process apparatus 2D).

また、上述したように、少なくとも1つの集約処理場2では、各汚泥搬送部12,14,16で送られてきた汚泥に、各繊維状物搬送部13,15,17で送られてきた繊維状物を混合し、この混合されたものを(ただちに;たとえば、繊維状物の腐敗が始まって繊維状物の有機性を担保する機能が損なわれる前に)消化処理装置2Dで消化処理するようになっている。   Further, as described above, in at least one of the intensive treatment plants 2, the fibers sent by the fibrous material transfer units 13, 15, and 17 to the sludge sent by the sludge transfer units 12, 14, and 16, respectively. The mixture is mixed and the mixture is digested immediately (for example, before the function of securing the organic property of the fibrous material is impaired by the start of the decay of the fibrous material). It has become.

以上により、各ローカル処理場3,4,5で汚泥から繊維状物を分離回収し、汚泥を各ローカル処理場3,4,5から集約処理場2まで各圧送ポンプP1,P3,P5を用いて送り、各ローカル処理場3,4,5で分離回収された繊維状物を、各ローカル処理場3,4,5から集約処理場2まで送り、集約処理場2で、送られてきた汚泥に、送られてきた繊維状物を混合し、この混合されたものを消化処理するので、有機物の嫌気性醗酵により大量の消化ガスを安定して生成することができる。   As described above, the fibrous material is separated and recovered from the sludge at each of the local treatment plants 3, 4 and 5, and the sludge is sent from each of the local treatment plants 3, 4, 5 to the central treatment plant 2 using the pumps P1, P3, and P5. The sludge sent from the local treatment plants 3, 4 and 5 to the central treatment plant 2 and sent from the local treatment plants 3, 4 and 5 to the central treatment plant 2 In addition, since the fed fibrous material is mixed and the mixed material is digested, a large amount of digestion gas can be stably generated by anaerobic fermentation of organic matter.

すなわち、各ローカル処理場3,4,5から集約処理場2まで送られた汚泥が腐敗しても、各ローカル処理場3,4,5から集約処理場2まで送られた繊維状物が腐敗することはない。そして、集約処理場2まで送られた汚泥に集約処理場2まで送られてきた繊維状物(有機性を担保する繊維状物)を加えて混同した後ただちに、消化処理をするので、大量の消化ガスを安定して生成することができる。   That is, even if the sludge sent from each local treatment plant 3, 4, 5 to the central treatment plant 2 rots, the fibrous material sent from each local treatment plant 3, 4, 5 to the central treatment plant 2 rots. Never do. And after adding the fibrous material (fibrous material that guarantees organicity) sent to the intensive treatment plant 2 to the sludge sent to the intensive treatment plant 2, the digestion treatment is carried out immediately after mixing. Digestion gas can be generated stably.

また、汚泥処理システム1では、集約処理場2に、各繊維状物搬送部13,15,17で送られてきた繊維状物を(一時的に)蓄える繊維状物貯留部2Bが設けられており、消化処理装置2Dが、各汚泥搬送部12,14,16で送られてきた汚泥に、繊維状物貯留部2Bに蓄えられている繊維状物を混合し、この混合されたものを消化処理するようになっている。これにより、安定した態様で繊維状物を消化処理装置2Dに供給することができる。   Further, in the sludge treatment system 1, the aggregate treatment plant 2 is provided with a fibrous material storage unit 2B that (temporarily) stores the fibrous materials sent by the fibrous material conveying units 13, 15, and 17. The digester 2D mixes the fibrous material stored in the fibrous material storage unit 2B with the sludge sent by the sludge transport units 12, 14, 16 and digests the mixed material. It comes to handle. Thereby, a fibrous material can be supplied to the digestion processing apparatus 2D in a stable manner.

さらに汚泥処理システム1では、集約処理場2に、各汚泥搬送部12,14,16で送られてきた汚泥中の繊維状物の濃度を測定する繊維状物濃度測定部2Cが設けられている。そして、繊維状物濃度測定部2Cで測定した結果、繊維状物の濃度が所定の値よりも低い場合に、繊維状物貯留部2Bに蓄えられている繊維状物を混合し、この混合されたものを消化処理装置2Dで消化処理するように構成されている。これにより、消化処理装置2Dにおいて安定した態様で所定量の消化ガスを生成することができる。   Further, in the sludge treatment system 1, the aggregate treatment site 2 is provided with a fibrous substance concentration measuring unit 2 </ b> C that measures the concentration of the fibrous substance in the sludge sent by each sludge transport unit 12, 14, 16. . And when the density | concentration of a fibrous material is lower than a predetermined value as a result of measuring with 2C of fibrous substance density | concentration measurement parts, the fibrous substance stored in the fibrous substance storage part 2B is mixed, and this mixing is carried out. The food is digested by the digestion processing apparatus 2D. Thereby, a predetermined amount of digestion gas can be generated in a stable manner in the digestion apparatus 2D.

ここで、図2を参照し、汚泥処理システム1の動作を説明する。   Here, the operation of the sludge treatment system 1 will be described with reference to FIG.

上記動作は、各ローカル処理場3、4、5で汚泥から繊維状物を分離回収する繊維状物分離回収工程(ステップSA01)と、(繊維状物分離回収工程で繊維状物が回収された)汚泥を各ローカル処理場3,4,5から集約処理場2まで各圧送ポンプP1,P3,P5と各汚泥搬送用配管6,8,10とを用いて送る汚泥搬送工程(ステップSA02)と、繊維状物分離回収工程で分離回収された繊維状物を、各ローカル処理場3,4,5から集約処理場2まで、たとえば、各圧送ポンプP2,P4,P6と、各汚泥搬送用配管6,8,10とは別の各繊維状物搬送用配管7,9,11とを用いて送る繊維状物搬送工程(ステップSA03)と、集約処理場2で、汚泥搬送工程で送られてきた汚泥に、繊維状物搬送工程で送られてきた繊維状物を混合し、この混合されたものを(ただちに;たとえば、繊維状物の腐敗が始まって繊維状物の脱水性を担保する機能が損なわれる前に)汚泥処理する汚泥処理工程を含む。   In the above operation, the fibrous material separation and recovery step (step SA01) for separating and recovering the fibrous material from the sludge at each of the local treatment plants 3, 4, and 5 (the fibrous material was recovered in the fibrous material separation and recovery step) ) Sludge transporting process (step SA02) for sending sludge from each local treatment plant 3, 4, 5 to the centralized treatment plant 2 using each pumping pump P1, P3, P5 and each sludge transporting pipe 6, 8, 10. The fibrous materials separated and recovered in the fibrous material separation and recovery step are transferred from the local treatment plants 3, 4, 5 to the central treatment plant 2, for example, the pressure pumps P2, P4, P6, and the sludge conveyance pipes. It is sent in the sludge transporting process at the fibrous material transporting process (step SA03) to be sent using each of the fibrous material transporting pipes 7, 9, 11 other than 6, 8, 10 and the aggregation processing site 2. The fibrous form sent to the sludge in the fibrous material transport process It was mixed, those which are the mixture (immediately; for example, before the function of the start of the decay of fibrous materials to ensure the dewatering of the fibrous material is damaged) a sludge treatment process of sludge treatment.

上記汚泥処理工程は、脱水処理工程(ステップSA04)、消化処理工程(ステップSA05)の少なくともいずれかを含む。   The sludge treatment process includes at least one of a dehydration process (step SA04) and a digestion process (step SA05).

脱水処理工程(ステップSA04)は、上記混合されたものを脱水処理する工程であり、消化処理工程(ステップSA05)は、上記混合されたものを消化処理する工程である。   The dehydration process (step SA04) is a process of dehydrating the above-mentioned mixture, and the digestion process (step SA05) is a process of digesting the above-mentioned mixture.

汚泥処理工程を、脱水処理工程(ステップSA04)と消化処理工程(ステップSA05)とで構成した場合、先に消化処理工程(ステップSA05)での消化処理をし、この消化処理がされたものを脱水処理工程(ステップSA04)で脱水処理する。   When the sludge treatment process is composed of a dehydration process (step SA04) and a digestion process (step SA05), the digestion process is first performed in the digestion process (step SA05), and the digested process is performed. Dehydration is performed in the dehydration process (step SA04).

また、汚泥処理システム1の汚泥処理方法において、集約処理場2では、繊維状物搬送工程で送られてきた繊維状物を(一時的に)蓄える繊維状物貯留工程を実行し、脱水処理工程は、汚泥搬送工程で送られてきた汚泥に、繊維状物貯留工程に蓄えられている繊維状物を混合し、この混合されたものを脱水処理し、消化処理工程は、汚泥搬送工程で送られてきた汚泥に、繊維状物貯留工程に蓄えられている繊維状物を混合し、この混合されたものを消化処理する。これらの動作は、汚泥処理方法として把握することができる。   In the sludge treatment method of the sludge treatment system 1, the aggregate treatment plant 2 executes a fibrous material storage step (temporarily) for storing the fibrous material sent in the fibrous material conveyance step, and the dehydration treatment step. Mixes the sludge sent in the sludge transporting process with the fibrous material stored in the fibrous material storage process, dehydrates this mixture, and the digestion process sends it in the sludge transporting process. The sludge that has been mixed with the fibrous material stored in the fibrous material storage step is digested. These operations can be grasped as a sludge treatment method.

さらに、汚泥処理方法において、集約処理場2では、汚泥搬送工程で送られてきた汚泥中の繊維状物の濃度を測定する繊維状物濃度測定工程を実行し、繊維状物濃度測定工程で測定した結果、繊維状物の濃度が所定の値よりも低い場合に、繊維状物貯留工程で蓄えられている繊維状物を混合し、この混合されたものを、脱水処理工程で脱水処理、消化処理工程で消化処理の少なくともいずれかの処理をする。   Further, in the sludge treatment method, the intensive treatment plant 2 executes a fibrous substance concentration measuring step for measuring the concentration of fibrous substances in the sludge sent in the sludge conveying step, and the measurement is performed in the fibrous substance concentration measuring step. As a result, when the concentration of the fibrous material is lower than the predetermined value, the fibrous material stored in the fibrous material storage step is mixed, and this mixed product is dehydrated and digested in the dehydration processing step. At least one of digestion treatment is performed in the treatment step.

なお、上記説明では、繊維状物を各繊維状物搬送部13,15,17で移送したが、繊維状物搬送用配管7,9,11を用いることに代えて、繊維状物分離回収装置で分離回収された繊維状物を、車両等(例えば、トラック)で各ローカル処理場3,4,5から集約処理場2まで移送してもよい。これにより、新たな配管を設ける必要がなくなる。   In the above description, the fibrous material is transferred by the fibrous material conveying units 13, 15, and 17. However, instead of using the fibrous material conveying pipes 7, 9, and 11, the fibrous material separating and collecting device is used. The fibrous material separated and recovered in (1) may be transferred from each of the local treatment plants 3, 4 and 5 to the aggregation treatment plant 2 by a vehicle or the like (for example, a truck). This eliminates the need to provide new piping.

また、一部のローカル処理場(例えば3のみ)のみ分離搬送し、残りのローカル処理場(4,5)では混合した状態で搬送してもよい。   Alternatively, only some of the local processing plants (for example, only 3) may be transported separately, and the remaining local processing plants (4, 5) may be transported in a mixed state.

この発明は前述の発明の実施の形態に限定されることなく、適宜な変更を行うことにより、その他の態様で実施し得るものである。   The present invention is not limited to the embodiments of the invention described above, and can be implemented in other modes by making appropriate modifications.

1 汚泥処理システム
2 集約処理場
2A 脱水処理装置
2B 繊維状物貯留部
2C 繊維状物濃度測定部
3、4、5 ローカル処理場
3A、4A、5A 繊維状物分離回収装置
12、14、16 汚泥搬送部
13、15、17 繊維状物搬送部
P1、P3、P5 圧送ポンプ
DESCRIPTION OF SYMBOLS 1 Sludge processing system 2 Aggregate treatment plant 2A Dehydration processing device 2B Fibrous material storage unit 2C Fibrous material concentration measurement unit 3, 4, 5 Local treatment plant 3A, 4A, 5A Fibrous material separation and recovery device 12, 14, 16 Sludge Conveyance unit 13, 15, 17 Fibrous material conveyance unit P1, P3, P5 Pressure feed pump

Claims (8)

ローカル処理場の内少なくとも1つで汚泥から繊維状物を分離回収する繊維状物分離回収装置と、
前記汚泥を前記ローカル処理場から集約処理場まで圧送ポンプを用いて送る汚泥搬送部と、
前記繊維状物分離回収装置で分離回収された繊維状物を、前記ローカル処理場から前記集約処理場まで送る繊維状物搬送部と、
前記集約処理場で、前記汚泥搬送部で送られてきた汚泥に、前記繊維状物搬送部で送られてきた繊維状物を混合し、この混合されたものを汚泥処理する汚泥処理装置と、
を有することを特徴とする汚泥処理システム。
A fibrous material separation and recovery device for separating and recovering fibrous material from sludge in at least one of the local treatment plants;
A sludge transport unit that sends the sludge from the local treatment plant to the central treatment plant using a pressure pump;
A fibrous material transport unit that sends the fibrous material separated and recovered by the fibrous material separation and recovery device from the local processing plant to the aggregation processing plant;
In the intensive treatment plant, the sludge sent in the sludge transport unit is mixed with the fibrous material sent in the fibrous material transport unit, and the sludge treatment device that performs sludge treatment on the mixed material,
A sludge treatment system characterized by comprising:
請求項1に記載の汚泥処理システムにおいて、
前記集約処理場には、前記繊維状物搬送部で送られてきた繊維状物を蓄える繊維状物貯留部が設けられており、
前記汚泥処理装置は、前記汚泥搬送部で送られてきた汚泥に、前記繊維状物貯留部に蓄えられている繊維状物を混合し、この混合されたものを汚泥処理するように構成されていることを特徴とする汚泥処理システム。
In the sludge treatment system according to claim 1,
The aggregate treatment plant is provided with a fibrous material storage unit for storing the fibrous material sent by the fibrous material conveyance unit,
The sludge treatment apparatus is configured to mix the sludge sent in the sludge transport unit with the fibrous material stored in the fibrous material storage unit, and sludge the mixed material. A sludge treatment system characterized by
請求項2に記載の汚泥処理システムにおいて、
前記集約処理場で、前記汚泥搬送部で送られてきた汚泥中の繊維状物の濃度を測定する繊維状物濃度測定部を有し、
前記繊維状物濃度測定部で測定した結果、繊維状物の濃度が所定の値よりも低い場合に、前記繊維状物貯留部に蓄えられている繊維状物を混合し、この混合されたものを前記汚泥処理装置で汚泥処理するように構成されていることを特徴とする汚泥処理システム。
In the sludge treatment system according to claim 2,
In the intensive treatment plant, it has a fibrous substance concentration measuring unit that measures the concentration of fibrous substances in the sludge sent by the sludge transport unit,
As a result of measurement by the fibrous substance concentration measurement unit, when the concentration of the fibrous substance is lower than a predetermined value, the fibrous substance stored in the fibrous substance storage unit is mixed and mixed. The sludge treatment system is configured to treat sludge with the sludge treatment apparatus.
請求項1〜請求項3のいずれか1項に記載の汚泥処理システムにおいて、
前記汚泥処理装置は、前記混合されたものを脱水処理する脱水処理装置、前記混合されたものを消化処理する消化処理装置の少なくともいずれかで構成されていることを特徴とする汚泥処理システム。
In the sludge treatment system according to any one of claims 1 to 3,
The sludge treatment system is constituted by at least one of a dehydration treatment device for dehydrating the mixed material and a digestion treatment device for digesting the mixed material.
ローカル処理場の内少なくとも1つで汚泥から繊維状物を分離回収する繊維状物分離回収工程と、
前記汚泥を前記ローカル処理場から集約処理場まで圧送ポンプを用いて送る汚泥搬送工程と、
前記繊維状物分離回収工程で分離回収された繊維状物を、前記ローカル処理場から前記集約処理場まで送る繊維状物搬送工程と、
前記集約処理場で、前記汚泥搬送工程で送られてきた汚泥に、前記繊維状物搬送工程で送られてきた繊維状物を混合し、この混合されたものを汚泥処理する汚泥処理工程と、
を含むことを特徴とする汚泥処理方法。
A fibrous material separation and recovery step of separating and recovering fibrous material from sludge in at least one of the local treatment plants;
A sludge conveying step for sending the sludge from the local treatment plant to the central treatment plant using a pressure pump;
A fibrous material conveying step of sending the fibrous material separated and recovered in the fibrous material separation and recovery step from the local processing plant to the aggregated processing plant;
In the intensive treatment plant, the sludge sent in the sludge transporting step is mixed with the fibrous material sent in the fibrous material transporting step, and the mixed sludge treatment step for sludge treatment,
The sludge processing method characterized by including.
請求項5に記載の汚泥処理方法において、
前記集約処理場では、前記繊維状物搬送工程で送られてきた繊維状物を蓄える繊維状物貯留工程を実行し、
前記汚泥処理工程は、前記汚泥搬送工程で送られてきた汚泥に、前記繊維状物貯留工程で蓄えられている繊維状物を混合し、この混合されたものを汚泥処理するように構成されていることを特徴とする汚泥処理方法。
The sludge treatment method according to claim 5,
In the aggregation processing plant, a fibrous material storing step for storing the fibrous material sent in the fibrous material conveying step is executed,
The sludge treatment step is configured to mix the fibrous material stored in the fibrous material storage step with the sludge sent in the sludge transporting step, and sludge the mixture. A sludge treatment method characterized by comprising:
請求項6に記載の汚泥処理方法において、
前記集約処理場では、前記汚泥搬送工程で送られてきた汚泥中の繊維状物の濃度を測定する繊維状物濃度測定工程を実行し、
前記繊維状物濃度測定工程で測定した結果、繊維状物の濃度が所定の値よりも低い場合に、前記繊維状物貯留工程で蓄えられている繊維状物を混合し、この混合されたものを前記汚泥処理工程で汚泥処理するように構成されていることを特徴とする汚泥処理方法。
The sludge treatment method according to claim 6,
In the intensive treatment plant, execute a fibrous substance concentration measuring step for measuring the concentration of fibrous substances in the sludge sent in the sludge conveying step,
As a result of measurement in the fibrous substance concentration measurement step, when the concentration of the fibrous substance is lower than a predetermined value, the fibrous substance stored in the fibrous substance storage step is mixed and mixed. The sludge treatment method is characterized in that sludge treatment is performed in the sludge treatment step.
請求項5〜請求項7のいずれか1項に記載の汚泥処理システムにおいて、
前記汚泥処理工程は、前記混合されたものを脱水処理する脱水処理工程、前記混合されたものを消化処理する消化処理工程の少なくともいずれかで構成されていることを特徴とする汚泥処理方法。
In the sludge treatment system according to any one of claims 5 to 7,
The sludge treatment step is constituted by at least one of a dehydration treatment step for dehydrating the mixed material and a digestion treatment step for digesting the mixed material.
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