JP2003190999A - Method for accelerating solid-liquid separation of sludge - Google Patents

Method for accelerating solid-liquid separation of sludge

Info

Publication number
JP2003190999A
JP2003190999A JP2001390824A JP2001390824A JP2003190999A JP 2003190999 A JP2003190999 A JP 2003190999A JP 2001390824 A JP2001390824 A JP 2001390824A JP 2001390824 A JP2001390824 A JP 2001390824A JP 2003190999 A JP2003190999 A JP 2003190999A
Authority
JP
Japan
Prior art keywords
sludge
liquid separation
solid
sewage
concentration
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.)
Pending
Application number
JP2001390824A
Other languages
Japanese (ja)
Inventor
Hideaki Hamada
英明 浜田
Tomoya Okamura
知也 岡村
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.)
Hitachi Kiden Kogyo Ltd
Original Assignee
Hitachi Kiden Kogyo 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 Hitachi Kiden Kogyo Ltd filed Critical Hitachi Kiden Kogyo Ltd
Priority to JP2001390824A priority Critical patent/JP2003190999A/en
Publication of JP2003190999A publication Critical patent/JP2003190999A/en
Pending legal-status Critical Current

Links

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W10/00Technologies for wastewater treatment
    • Y02W10/10Biological treatment of water, waste water, or sewage

Landscapes

  • Activated Sludge Processes (AREA)
  • Treatment Of Sludge (AREA)

Abstract

<P>PROBLEM TO BE SOLVED: To provide a method for accelerating the solid-liquid separation of sludge capable of obtaining high concentrated sludge for a short time as compared with a conventional gravitational concentration method while reducing the cost required in equipment or chemicals. <P>SOLUTION: In the method for accelerating the solid-liquid separation of sludge for treating an organic substance in sewage using microorganisms and drawing out generated sludge to treat the same, the drawn-out sludge is heated to a degree degenerating the polymeric substance in sludge to reduce the viscosity thereof to accelerate the sedimentation properties of sludge. <P>COPYRIGHT: (C)2003,JPO

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、汚泥の固液分離促
進方法に関し、特に、活性汚泥法等により処理した汚泥
に対し、凝固剤等の使用薬品量を抑制し、かつ経済的
に、効率的に固液分離を促進するようにした汚泥の固液
分離促進方法に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for promoting solid-liquid separation of sludge, and particularly to sludge treated by an activated sludge method or the like, which suppresses the amount of chemicals such as coagulant used and is economically and efficiently. The present invention relates to a method for promoting solid-liquid separation of sludge, which is intended to promote solid-liquid separation.

【0002】[0002]

【従来の技術】従来、下水処理場などに流入する下水な
どの汚水(以下、「汚水」という。)を生物反応槽に導
き、該汚水と活性汚泥を混合させ、曝気・攪拌すること
により、汚水中の有機成分の生物処理を行い、これに伴
って発生する汚泥を、混合液中から沈殿、濃縮分離して
処理するようにしている。そして、生物反応槽内におい
て発生した汚泥を、沈殿、濃縮分離する方法として、重
力濃縮法、機械濃縮法等を挙げることができる。
2. Description of the Related Art Conventionally, sewage such as sewage that flows into a sewage treatment plant (hereinafter referred to as "sewage") is introduced into a biological reaction tank, and the sewage and activated sludge are mixed, aerated and stirred. Biological treatment of organic components in wastewater is performed, and sludge generated along with this is precipitated, concentrated and separated from the mixed solution for treatment. Then, as a method of precipitating and concentrating and separating the sludge generated in the biological reaction tank, a gravity concentration method, a mechanical concentration method, and the like can be mentioned.

【0003】[0003]

【発明が解決しようとする課題】ところで、生物反応槽
内における汚泥の含水率は、処理方法によって異なる
が、通常、99%程度であり、沈殿・濃縮分離操作の後
段に設けられる汚泥処理系での効率を向上させるために
は、この汚泥の含有率を低くし、最終的に汚泥処理系へ
送る汚泥量を少なくすることが重要となる。
The water content of sludge in the biological reaction tank varies depending on the treatment method, but is usually about 99%, and the sludge treatment system provided in the latter stage of the sedimentation / concentration separation operation In order to improve the efficiency of the sludge, it is important to reduce the content rate of this sludge and finally reduce the amount of sludge sent to the sludge treatment system.

【0004】しかしながら、従来の重力濃縮法は、水よ
りも比重の重い汚泥が自然沈降する現象を利用して汚泥
の濃縮を行うものであるが、汚泥濃度が増加すると沈降
性が著しく悪化し、結果的に含水率として98%程度の
汚泥しか得られず、十分な高濃度の濃縮汚泥を得ること
ができず、後段での固液分離率が期待するほど得られな
いという問題があった。また、自然沈降によって沈殿・
濃縮分離を行うため、時間がかかり、これに伴って必要
とされる沈殿槽が大きくなるという問題があった。
However, the conventional gravity concentrating method concentrates sludge by utilizing the phenomenon that sludge, which has a higher specific gravity than water, spontaneously sediments, but when the sludge concentration increases, the sedimentation property remarkably deteriorates, As a result, there was a problem that only a sludge having a water content of about 98% was obtained, a concentrated sludge having a sufficiently high concentration could not be obtained, and a solid-liquid separation rate in the latter stage could not be obtained as expected. In addition, sedimentation by natural sedimentation
Since the concentration and separation are performed, there is a problem that it takes time and the settling tank required becomes large accordingly.

【0005】一方、機械濃縮法には、遠心分離法や浮上
濃縮法などがあるが、これらの方法では、通常の含水率
は96%程度と、重力濃縮法に比べ高濃度の汚泥を得る
ことができる反面、設備にかかるコストが高くなるとと
もに、効率良く沈殿・分離を行うためには薬品の添加が
不可欠であり、経済性に劣るという問題があった。
On the other hand, the mechanical concentration method includes a centrifugal separation method, a floating concentration method, and the like. In these methods, a normal water content is about 96%, and a sludge having a higher concentration than that of the gravity concentration method can be obtained. On the other hand, there is a problem that the cost of equipment becomes high, and addition of chemicals is indispensable for efficient precipitation / separation, which is inferior in economic efficiency.

【0006】本発明は、上記従来の汚泥の固液分離方法
の有する問題点に鑑み、設備や添加する薬品にかかるコ
ストを低廉にしながら、従来の重力濃縮法よりも短時間
で高濃度の濃縮汚泥が得られるようにした汚泥の固液分
離促進方法を提供することを目的とする。
In view of the problems of the above-mentioned conventional solid-liquid separation method for sludge, the present invention makes it possible to reduce the cost of equipment and chemicals to be added, while concentrating to a high concentration in a shorter time than the conventional gravity concentration method. An object of the present invention is to provide a method for promoting solid-liquid separation of sludge so that sludge can be obtained.

【0007】[0007]

【課題を解決するための手段】上記目的を達成するた
め、本発明の汚泥の固液分離促進方法は、微生物を利用
して下水など汚水中の有機物質を処理し、これにより発
生した汚泥を引き抜き処理する汚泥の固液分離促進方法
において、引き抜いた汚泥を、汚泥中の高分子物質が変
成し、粘性が減少する程度に加熱することにより汚泥の
沈降性を促進するようにしたことを特徴とする。
In order to achieve the above object, the method for promoting solid-liquid separation of sludge of the present invention uses a microorganism to treat organic substances in wastewater such as sewage, and to remove sludge generated by this treatment. In the method for promoting solid-liquid separation of sludge to be withdrawn, the extracted sludge is heated to such an extent that the polymer substance in the sludge is denatured and the viscosity is decreased, so that the sedimentation property of the sludge is promoted. And

【0008】この汚泥の固液分離促進方法は、水と比較
すると汚泥の比重は重いため、経時的に自然沈降によっ
て固液分離が可能となり、高濃度の汚泥を得ることがで
きるが、特に、高濃度になるとそれ自身の持つ粘性によ
って沈降性が悪くなり固液分離が不能となる汚泥を、汚
泥中の高分子物質が変成し、粘性が減少する程度に加熱
することにより汚泥の沈降性を促進させることができ
る。
In this method for promoting solid-liquid separation of sludge, since the specific gravity of sludge is heavier than that of water, it becomes possible to separate solid-liquid by natural sedimentation over time, and a high-concentration sludge can be obtained. When the concentration becomes high, the settling property of the sludge becomes poor due to its own viscosity and solid-liquid separation becomes impossible. Can be promoted.

【0009】この場合において、引き抜いた汚泥に、酸
若しくは酸性凝集剤をpHが5以下となるように添加、
調整し、これを加熱するようにすることができる。
In this case, an acid or acidic coagulant is added to the extracted sludge so that the pH is 5 or less,
It can be adjusted and heated.

【0010】これにより、汚泥の粘性の原因となってい
る高分子物質が、酸若しくは酸性凝集剤の持つ酸化力と
加熱温度によってより確実に変成し、粘性が減少し、沈
降性を一層促進することができる。
As a result, the polymer substance that causes the viscosity of the sludge is more surely transformed by the oxidizing power of the acid or the acidic flocculant and the heating temperature, the viscosity is reduced, and the sedimentation property is further promoted. be able to.

【0011】また、汚泥の加熱温度を、40〜100℃
にすることができる。
The heating temperature of sludge is 40 to 100 ° C.
Can be

【0012】これにより、汚泥の粘性の原因となる高分
子物質が最も変成し易くなって、粘性が減少するので、
効率的に沈降性を促進することができる。
As a result, the polymer substance that causes the viscosity of the sludge is most likely to be transformed and the viscosity is reduced,
The sedimentation property can be efficiently promoted.

【0013】[0013]

【発明の実施の形態】以下、本発明の汚泥の固液分離促
進方法の実施の形態を図面に基づいて説明する。
BEST MODE FOR CARRYING OUT THE INVENTION Embodiments of a method for promoting solid-liquid separation of sludge according to the present invention will be described below with reference to the drawings.

【0014】本発明の汚泥の固液分離促進方法は、微生
物を利用して下水など汚水中の有機物質を処理し、これ
により発生した汚泥を引き抜き処理する汚泥の固液分離
促進方法において、引き抜いた汚泥を、汚泥中の高分子
物質が変成し、粘性が減少する程度に加熱することによ
り汚泥の沈降性を促進するようにしたものである。
The method for promoting solid-liquid separation of sludge according to the present invention is a method for promoting solid-liquid separation of sludge in which an organic substance in sewage such as sewage is treated using microorganisms and the sludge generated thereby is extracted. The sludge is heated to such an extent that the polymer substance in the sludge is denatured and the viscosity is reduced, so that the sludge settling property is promoted.

【0015】ここで、図1に、本発明の汚泥の固液分離
促進方法の作用を実証するためのメスシリンダを用いた
沈降性試験の結果を示す。本実験では、生物処理を行っ
た含水率約99%の汚泥を、1リットルのメスシリンダ
に入れた後、静置することによって固液分離し、一定時
間ごとに分離した汚泥が占める容積の割合を観察した。
また、対照として、処理を行わない汚泥に関しても同様
の観察を行った。
Here, FIG. 1 shows the result of a sedimentation test using a graduated cylinder for demonstrating the action of the sludge solid-liquid separation promoting method of the present invention. In this experiment, sludge with a water content of about 99% was put into a 1-liter graduated cylinder and then left to stand to perform solid-liquid separation, and the ratio of the volume occupied by the sludge separated at regular intervals. Was observed.
Further, as a control, the same observation was made for the untreated sludge.

【0016】この実験の結果から、含水率約99%の汚
泥は、処理を全く施さなかった場合では、実際の濃縮槽
と比べて大きさが全く異なることもあって、24時間経
過しても全く固液分離が行えないのに対して、80℃の
温度条件下で1時間保持した汚泥では、最初の1時間で
は分離汚泥の占める割合は95%程度であったが、24
時間では75%となった。
From the results of this experiment, the sludge having a water content of about 99% may be completely different in size from the actual concentration tank without any treatment, and even after 24 hours have passed. While solid-liquid separation cannot be performed at all, in the sludge kept at a temperature of 80 ° C. for 1 hour, the proportion of the separated sludge was about 95% in the first hour, but 24
It was 75% in time.

【0017】さらに、酸を少量(容積で0.1%、pH
5)添加し、80℃の温度条件下で1時間保持した汚泥
では、分離汚泥の占める割合は最初の1時間で80%、
24時間では50%と、濃縮槽が小さいにもかかわらず
沈降性は大幅に改善された。
In addition, a small amount of acid (0.1% by volume, pH
5) In the sludge added and kept for 1 hour under the temperature condition of 80 ° C, the ratio of the separated sludge is 80% in the first hour,
After 24 hours, the sedimentation property was greatly improved to 50% even though the concentration tank was small.

【0018】よって、本発明の汚泥の固液分離促進方法
によって汚泥を処理すれば、従来重力沈殿法では濃縮で
きず、機械濃縮法が必要であるような濃度の汚泥であっ
ても、重力沈殿法だけで十分高濃度の汚泥を得ることが
できる。
Therefore, if sludge is treated by the method for promoting solid-liquid separation of sludge of the present invention, even if the sludge cannot be concentrated by the conventional gravity settling method and the mechanical concentration method is required, gravity settling can be performed. A sludge of sufficiently high concentration can be obtained only by the method.

【0019】図2は、本発明の汚泥の固液分離促進方法
を、活性汚泥法に適用した一実施例を示す水処理プロセ
スのフロー図である。
FIG. 2 is a flow chart of a water treatment process showing an embodiment in which the sludge solid-liquid separation promoting method of the present invention is applied to an activated sludge method.

【0020】下水処理場に送られた汚水Aは、生物反応
槽1に導入され、生物反応槽1内で活性汚泥と混合さ
れ、曝気・攪拌されることにより汚水Aに含まれる有機
物質は生物処理される。この生物反応槽1内で処理され
た汚水は、活性汚泥とともに混合液Bとして最終沈殿池
2に送られ、ここで重力沈殿により処理水Cと分離汚泥
Dに固液分離される。
The sewage A sent to the sewage treatment plant is introduced into the biological reaction tank 1, mixed with the activated sludge in the biological reaction tank 1, and aerated and agitated so that the organic substances contained in the sewage A are biological. It is processed. The sewage treated in the biological reaction tank 1 is sent to the final settling basin 2 as a mixed solution B together with the activated sludge, where it is solid-liquid separated into treated water C and separated sludge D by gravity settling.

【0021】このようにして得られた処理水Cは、適切
な消毒処理等を施して、河川等に放流され、また、分離
汚泥Dは汚泥ポンプ3によって最終沈殿池2より引き抜
かれ、その一部は返送汚泥Eとして再び生物反応槽1に
送られ、それ以外の余剰汚泥Fは汚泥処理槽4に送られ
る。
The treated water C thus obtained is appropriately disinfected and discharged to a river or the like, and the separated sludge D is drawn out from the final settling tank 2 by the sludge pump 3. The part is sent again to the biological reaction tank 1 as returning sludge E, and the excess surplus sludge F is sent to the sludge treatment tank 4.

【0022】この汚泥処理槽4には、加温用ヒータ5が
設置されており、また、薬品ポンプ6によって薬品タン
ク7よりごく少量の酸若しくは酸性凝集剤を添加するこ
とができるようになっているが、この場合、酸若しくは
酸性凝集剤の添加はpHが5以下となるように調節して
行われる。そして、汚泥処理槽4に送られた余剰汚泥F
は、薬品タンク7より添加された酸と混合され、40〜
100℃、望ましくは、80℃程度以下に加熱処理を受
けた後、静置されることにより沈殿分離する。
A heater 5 for heating is installed in the sludge treatment tank 4, and a very small amount of acid or acidic coagulant can be added from the chemical tank 7 by the chemical pump 6. However, in this case, the addition of the acid or acidic coagulant is carried out by adjusting the pH to 5 or less. Then, excess sludge F sent to the sludge treatment tank 4
Is mixed with the acid added from the chemical tank 7,
After being subjected to heat treatment at 100 ° C., preferably about 80 ° C. or lower, it is allowed to stand to cause precipitation separation.

【0023】このように汚泥に、pHが5以下となるよ
うに調節して酸若しくは酸性凝集剤を添加、混合、攪拌
した後、加熱することにより汚泥の沈降性が促進される
ように改善され、その後段に設けた重力沈殿槽において
処理汚泥の自然沈降を利用して固液分離を行う。
As described above, the acid or acidic coagulant is added to the sludge so that the pH is adjusted to 5 or less, mixed and stirred, and then heated to improve sludge sedimentation. The solid-liquid separation is performed by using the natural sedimentation of the treated sludge in the gravity sedimentation tank provided in the subsequent stage.

【0024】この処理によって得られた余剰汚泥Fは高
濃度に濃縮され、濃縮汚泥Gとして系外に排出された
り、汚泥の脱水処理に供される。なお、分離液Hは必要
に応じてpH調整された後、生物反応槽1に返流され
る。
The excess sludge F obtained by this treatment is concentrated to a high concentration and discharged as a concentrated sludge G out of the system, or is used for sludge dewatering treatment. The separated liquid H is returned to the biological reaction tank 1 after its pH is adjusted if necessary.

【0025】これにより、従来の重力濃縮法によれば、
1%の汚泥を3%に濃縮するのに12時間程度必要であ
るが、本発明の汚泥の固液分離促進方法によれば、同程
度の能力を示すには、加熱処理に1時間、固液分離に6
時間程度かければよく、従来の半分程度で汚泥を濃縮す
ることができる。また、本発明の汚泥の固液分離促進方
法を用いれば、特に複雑な設備を設けず、また、大きな
コストをかけることなく、従来の重力濃縮法よりも短時
間で高濃度の濃縮汚泥を得ることができる。
Thus, according to the conventional gravity concentration method,
It takes about 12 hours to concentrate 1% of sludge to 3%, but according to the method for promoting solid-liquid separation of sludge of the present invention, in order to show the same level of ability, it is necessary to perform heat treatment for 1 hour. 6 for liquid separation
It only takes a long time, and the sludge can be concentrated in about half the amount of conventional sludge. Further, if the method for promoting solid-liquid separation of sludge of the present invention is used, highly concentrated concentrated sludge can be obtained in a shorter time than the conventional gravity concentration method without providing particularly complicated equipment and without incurring a large cost. be able to.

【0026】なお、生物反応槽1より引き抜いた汚泥の
含水率が99%以上と十分高い場合には、予め重力沈殿
による固液分離を行って含水率を減少させた後、本発明
の汚泥の固液分離促進処理方法を実施することにより、
処理量を減少させ、さらに処理コストを軽減することが
できる。
When the water content of the sludge extracted from the biological reaction tank 1 is 99% or more, which is sufficiently high, solid-liquid separation by gravity precipitation is performed in advance to reduce the water content, and then the sludge of the present invention is treated. By carrying out the solid-liquid separation promoting treatment method,
It is possible to reduce the processing amount and further reduce the processing cost.

【0027】[0027]

【発明の効果】本発明の汚泥の固液分離促進方法によれ
ば、水と比較すると汚泥の比重は重いため、経時的に自
然沈降によって固液分離が可能となり、高濃度の汚泥を
得ることができるが、特に、高濃度になるとそれ自身の
持つ粘性によって沈降性が悪くなり固液分離が不能とな
る汚泥を、汚泥中の高分子物質が変成し、粘性が減少す
る程度に加熱することにより汚泥の沈降性を促進させる
ことができる。これにより、汚泥の沈降性を促進し、高
濃度の汚泥を短時間で得られ、また、機械濃縮を行う際
に必要となる設備投資費や運転費よりもはるかに安価に
汚泥を処理をすることができる。
According to the method for promoting solid-liquid separation of sludge of the present invention, since the specific gravity of sludge is heavier than that of water, solid-liquid separation is possible by natural sedimentation over time, and a high-concentration sludge can be obtained. However, especially when the concentration becomes high, the sludge, which has a poor viscosity due to its own viscosity and cannot be solid-liquid separated, must be heated to such an extent that the polymer substances in the sludge are denatured and the viscosity decreases. By this, the sedimentation property of sludge can be promoted. As a result, sludge settling ability is promoted, high-concentration sludge can be obtained in a short time, and sludge is treated at a cost much lower than the capital investment and operating costs required for mechanical concentration. be able to.

【0028】また、引き抜いた汚泥に、酸若しくは酸性
凝集剤をpHが5以下となるように添加、調整し、これ
を加熱するようにすることにより、汚泥の粘性の原因と
なっている高分子物質が、酸若しくは酸性凝集剤の持つ
酸化力と加熱温度によってより確実に変成し、粘性が減
少し、沈降性を一層促進することができる。
Further, by adding and adjusting an acid or an acidic coagulant to the extracted sludge so that the pH becomes 5 or less, and heating this, the polymer that causes the viscosity of the sludge is added. The substance can be more surely transformed by the oxidizing power of the acid or the acidic flocculant and the heating temperature, the viscosity is reduced, and the sedimentation property can be further promoted.

【0029】また、汚泥の加熱温度を、40〜100℃
にすることにより、汚泥の粘性の原因となる高分子物質
が最も変成し易くなって、粘性が減少するので、効率的
に沈降性を促進することができる。
The heating temperature of the sludge is 40 to 100 ° C.
By so doing, the polymer substance that causes the viscosity of the sludge is most likely to be denatured and the viscosity is reduced, so that the sedimentation property can be efficiently promoted.

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

【図1】メスシリンダを用いた沈降性試験の結果を示す
グラフである。
FIG. 1 is a graph showing the results of a sedimentation test using a graduated cylinder.

【図2】本発明の汚泥の固液分離促進方法を活性汚泥処
理に組み込んだ水処理プロセスのフロー図である。
FIG. 2 is a flow chart of a water treatment process in which the method for promoting solid-liquid separation of sludge of the present invention is incorporated into activated sludge treatment.

【符号の説明】[Explanation of symbols]

1 生物反応槽 2 最終沈殿池 3 汚泥ポンプ 4 汚泥処理槽 5 ヒータ 6 薬品ポンプ 7 薬品タンク A 汚水 B 混合液 C 処理水 D 分離汚泥 E 返送汚泥 F 余剰汚泥 G 濃縮汚泥 H 分離液 1 biological reaction tank 2 final settling tank 3 sludge pump 4 Sludge treatment tank 5 heater 6 chemical pump 7 Chemical tank A dirty water B mixture C treated water D separation sludge E Return sludge F surplus sludge G concentrated sludge H separation liquid

───────────────────────────────────────────────────── フロントページの続き Fターム(参考) 4D028 AA02 AC01 AC03 BE04 CB02 CD01 4D059 AA05 BE31 BE48 BE49 BE53 BE54 BF02 BF12 CA22 CA28 DA31 DA70 EA06 EB06    ─────────────────────────────────────────────────── ─── Continued front page    F-term (reference) 4D028 AA02 AC01 AC03 BE04 CB02                       CD01                 4D059 AA05 BE31 BE48 BE49 BE53                       BE54 BF02 BF12 CA22 CA28                       DA31 DA70 EA06 EB06

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】 微生物を利用して下水など汚水中の有機
物質を処理し、これにより発生した汚泥を引き抜き処理
する汚泥の固液分離促進方法において、引き抜いた汚泥
を、汚泥中の高分子物質が変成し、粘性が減少する程度
に加熱することにより汚泥の沈降性を促進するようにし
たことを特徴とする汚泥の固液分離促進方法。
1. A method for promoting solid-liquid separation of sludge, which comprises treating an organic substance in sewage such as sewage using microorganisms, and extracting the sludge generated thereby. A method for promoting solid-liquid separation of sludge, characterized in that the sludge settling property is promoted by heating to a degree such that the sludge is denatured and the viscosity is reduced.
【請求項2】 引き抜いた汚泥に、酸若しくは酸性凝集
剤をpHが5以下となるように添加、調整し、これを加
熱するようにしたことを特徴とする請求項1記載の汚泥
の固液分離促進方法。
2. The solid-liquid sludge according to claim 1, wherein an acid or acidic coagulant is added to the extracted sludge so as to have a pH of 5 or less, and the sludge is heated. Separation promotion method.
【請求項3】 汚泥の加熱温度を、40〜100℃にし
たことを特徴とする請求項1又は2記載の汚泥の固液分
離促進方法。
3. The method for promoting solid-liquid separation of sludge according to claim 1 or 2, wherein the heating temperature of the sludge is set to 40 to 100 ° C.
JP2001390824A 2001-12-25 2001-12-25 Method for accelerating solid-liquid separation of sludge Pending JP2003190999A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2001390824A JP2003190999A (en) 2001-12-25 2001-12-25 Method for accelerating solid-liquid separation of sludge

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2001390824A JP2003190999A (en) 2001-12-25 2001-12-25 Method for accelerating solid-liquid separation of sludge

Publications (1)

Publication Number Publication Date
JP2003190999A true JP2003190999A (en) 2003-07-08

Family

ID=27598591

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2001390824A Pending JP2003190999A (en) 2001-12-25 2001-12-25 Method for accelerating solid-liquid separation of sludge

Country Status (1)

Country Link
JP (1) JP2003190999A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2009154126A (en) * 2007-12-27 2009-07-16 Osaka Gas Co Ltd Method for improving settleability of sludge
JP2016055229A (en) * 2014-09-08 2016-04-21 栗田工業株式会社 Method for concentrating sludge

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2009154126A (en) * 2007-12-27 2009-07-16 Osaka Gas Co Ltd Method for improving settleability of sludge
JP2016055229A (en) * 2014-09-08 2016-04-21 栗田工業株式会社 Method for concentrating sludge

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