JPS5935279B2 - Method for concentrating organic sludge - Google Patents
Method for concentrating organic sludgeInfo
- Publication number
- JPS5935279B2 JPS5935279B2 JP55021979A JP2197980A JPS5935279B2 JP S5935279 B2 JPS5935279 B2 JP S5935279B2 JP 55021979 A JP55021979 A JP 55021979A JP 2197980 A JP2197980 A JP 2197980A JP S5935279 B2 JPS5935279 B2 JP S5935279B2
- Authority
- JP
- Japan
- Prior art keywords
- sludge
- concentration
- hydrogen peroxide
- flotation
- organic sludge
- 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.)
- Expired
Links
Landscapes
- Physical Water Treatments (AREA)
- Treatment Of Sludge (AREA)
Description
【発明の詳細な説明】
本発明は有機質を含む汚泥、たとえばし尿、下水または
産業用排水を浄化処理する際に発生する余剰汚泥、およ
びし尿浄化槽汚泥などを浮上濃縮する方法に関するもの
である。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for flotation and concentration of sludge containing organic matter, such as surplus sludge generated when purifying human waste, sewage or industrial wastewater, and human waste septic tank sludge.
浮上濃縮とは除去しようとする粒子に微細気泡を付着さ
せたり、からみつかせたりして、気泡の力を借りて強制
的に分離濃縮する方法である。Flotation concentration is a method in which fine bubbles are attached to or entangled with the particles to be removed, and the particles are forcibly separated and concentrated using the power of the bubbles.
従来、浮上濃縮する際の気泡発生方法としては加圧浮上
法、電解浮上法等があるが、これらの方法では、発生す
る気泡の大きさが浮上させようとする懸濁粒子の大きさ
にくらべて比較的大きく微細粒子まで浮上濃縮させるこ
とが困難であり、また懸濁粒子自身が粘着性のあるコロ
イド粒子で、浮上する際に粒子の周囲に付着した水分も
同伴してしまうなどの欠点がある。Conventionally, methods for generating bubbles during flotation concentration include pressure flotation and electrolytic flotation, but in these methods, the size of the bubbles generated is smaller than the size of the suspended particles to be floated. It is difficult to float and concentrate even relatively large and fine particles using a method of floating, and the suspended particles themselves are sticky colloidal particles, so when they float, they also take with them the moisture attached to their surroundings. be.
これらの結果、浮上濃縮汚泥濃度の低下、処理水SSの
増加による固形分回収率の低下をもたらし、実際上は浮
上濃縮する前に高分子凝集剤を添加して粒子を大きくし
た後に行なっているのが現状である。As a result, the concentration of flotation thickened sludge decreases, and the solid content recovery rate decreases due to an increase in treated water SS.In practice, this is done after adding a polymer flocculant to enlarge the particles before flotation concentration. is the current situation.
本発明はこれらの方法の欠点を除去し、さらに効果的に
汚泥を浮上濃縮するための方法について種々検討を重ね
た結果、汚泥をPH2〜3に調整後、過酸化水素を添加
、混合し静置することにより、浮上濃縮が効率よく行な
わせるようにした新規な有機質汚泥の濃縮方法を提供す
ることを目的とするものである。The present invention has been developed as a result of various studies to eliminate the drawbacks of these methods and to more effectively float and concentrate sludge. After adjusting the pH of sludge to 2 to 3, hydrogen peroxide is added and mixed, and then the sludge is stabilized. It is an object of the present invention to provide a novel method for concentrating organic sludge in which flotation concentration can be carried out efficiently by placing the sludge in the sludge.
以下、本発明の実施例に基づいて詳述する。Hereinafter, the present invention will be explained in detail based on examples.
本発明の原理は、過酸化水素が汚泥中で分解し、その時
発生する酸素の微細気泡に粒子を付着させて浮上濃縮す
るものである。The principle of the present invention is that hydrogen peroxide is decomposed in sludge, and particles are attached to microscopic oxygen bubbles generated at that time to float and concentrate.
本発明においてはまず第1の工程として汚泥のPHを硫
酸あるいは塩酸等の酸によりPHを4以下、好ましくは
PHを2〜3に調整する。In the present invention, as a first step, the pH of the sludge is adjusted to 4 or less, preferably 2 to 3, using an acid such as sulfuric acid or hydrochloric acid.
このPH調整の目的としては、有機質を含む汚泥中には
微生物によって量産されたカタラーゼが多量に存在し、
これらは第2の工程で加える過酸化水素(H2O2)を
、酸素と水とに分解する酸化還元反応に対して触媒作用
を持っている。The purpose of this pH adjustment is that large amounts of catalase produced by microorganisms exist in sludge containing organic matter.
These have a catalytic effect on the redox reaction that decomposes hydrogen peroxide (H2O2) added in the second step into oxygen and water.
従って触媒作用が発揮されるPHの領域においては、加
えた過酸化水素は非常に早く分解され、分解によって生
ずる酸素ガスの気泡生成速度が、微少気泡の汚泥粒子へ
の吸着速度より大きくなって動作がダイナミックになり
、生成気泡は無駄に系外に放出される。Therefore, in the pH range where the catalytic effect is exerted, the added hydrogen peroxide is decomposed very quickly, and the rate of bubble formation of oxygen gas generated by decomposition becomes greater than the rate of adsorption of microbubbles to sludge particles. becomes dynamic, and the generated bubbles are wastefully discharged out of the system.
従って過酸化水素による浮上濃縮を行なう際には、PH
を4以下好ましくはPHを2〜3にして触媒作用をなく
す必要がある。Therefore, when performing flotation concentration using hydrogen peroxide, the PH
It is necessary to eliminate the catalytic action by setting the pH to 4 or less, preferably 2 to 3.
またこのPH領領域は浮上濃縮の障害となる有機質中の
高粘性多糖類の粘性低下が生じ、浮上濃縮を行なう際に
触媒作用低下とともに相乗的な効果をもたらす。Further, in this PH region, the viscosity of high-viscosity polysaccharides in the organic matter, which is an obstacle to flotation and concentration, is reduced, and when flotation and concentration is carried out, a synergistic effect is brought about along with a reduction in catalytic activity.
PHを4以下好ましくはPHを2〜3に調整した汚泥に
、第2の工程として過酸化水素を添加、混合する。In the second step, hydrogen peroxide is added and mixed to the sludge whose pH has been adjusted to 4 or less, preferably 2 to 3.
過酸化水素の添加量は固形物当り1.0%以上、好まし
くは1.0〜5%の範囲であり、1.0%より少ないと
浮上濃縮度の効果は少なく、5%以上であればそれ以上
の効果の向上は認められない。The amount of hydrogen peroxide added is 1.0% or more per solid matter, preferably in the range of 1.0 to 5%.If it is less than 1.0%, the effect of flotation concentration will be small, and if it is 5% or more, No further improvement in effectiveness was observed.
また静置時間は4時間以上、好ましくは8〜12時間程
時間節囲であり、8時間以下では浮上濃縮が完全に行な
われず、また24時間以上であればそれ以上の濃縮度の
向上は認められない。In addition, the standing time should be 4 hours or more, preferably 8 to 12 hours; if it is less than 8 hours, flotation concentration will not be completed, and if it is more than 24 hours, no further improvement in concentration will be observed. I can't.
なお、実施例として、し尿浄化槽汚泥について示したが
、その他、下水あるいは余剰汚泥等有機質を含む汚泥に
実施しても上記実施例と同等の効果を奏することは論を
またない。In addition, although human waste septic tank sludge was shown as an example, it goes without saying that the same effect as the above-mentioned example can be obtained even if the method is applied to sludge containing organic matter such as sewage or surplus sludge.
上記の第1および第2の工程における処理により、過酸
化水素の分解が効果的に行なわれ、分解によって生じた
気泡は電解によって生ずる気泡と同程度又はそれ以下の
極めて微細なものであり、微小な粒子まで付着、捕捉、
分離ができ、また過酸化水素が汚泥中に均一に混合され
ているため、汚泥中の各部分で均一な気泡の発生が可能
であり、分離液の清澄度が高いなどの効果が得られる。Through the treatments in the first and second steps above, hydrogen peroxide is effectively decomposed, and the bubbles produced by the decomposition are extremely fine, comparable to or smaller than bubbles produced by electrolysis. It attaches to, captures, and captures even particles.
Since hydrogen peroxide is uniformly mixed in the sludge, it is possible to generate bubbles uniformly in each part of the sludge, resulting in effects such as high clarity of the separated liquid.
また浮上動作そのものが静的なため、浮上濃縮部と清澄
液部との分離を工学的に適正に設計することにより分離
固形物濃度をより高くすることが出来る。Furthermore, since the flotation operation itself is static, the concentration of separated solids can be made higher by appropriately designing the separation between the flotation concentration section and the clarified liquid section from an engineering perspective.
尚H20□添加量は汚泥液の粘性その他の物性によって
最適直が決められる。The optimum amount of H20□ to be added is determined by the viscosity and other physical properties of the sludge liquid.
実施例 l
し尿浄化槽汚泥(濃度1.6%)に硫酸添加してPH調
整した後、過酸化水素を添加、混合し、24時間静置し
て浮上濃縮し、濃縮汚泥濃度を測定した結果を第1表に
示す。Example 1 After adjusting the pH by adding sulfuric acid to human waste septic tank sludge (concentration 1.6%), hydrogen peroxide was added and mixed, left to stand for 24 hours to float and concentrate, and the results of measuring the concentrated sludge concentration were Shown in Table 1.
この結果より、PHが4以下かつ過酸化水素を固形物当
り1.0%以上添加すると好結果が得られることがわか
る。This result shows that good results can be obtained when the pH is 4 or less and hydrogen peroxide is added in an amount of 1.0% or more based on solid matter.
実施例 2
し尿浄化槽汚泥を硫酸でPH=2.5に調整後過酸化水
素を固形物当り5.0%添加し、静置した結果を第2表
に示す。Example 2 Human waste septic tank sludge was adjusted to pH=2.5 with sulfuric acid, hydrogen peroxide was added in an amount of 5.0% based on the solid matter, and the mixture was allowed to stand. The results are shown in Table 2.
これより静置時間を4時間以上にすると濃縮度がかなり
良くなることがわかる。It can be seen from this that when the standing time is 4 hours or more, the degree of concentration is considerably improved.
□ 実施例 3
本発明法による結果(第2表24時間静置の結果)と従
来法(3kg/iの加圧水により回分式浮上装置で15
5分間浮上濃縮した結果)との比較を第3表に示す。□ Example 3 The results obtained by the method of the present invention (results after 24 hours of standing in Table 2) and the conventional method (15
Table 3 shows a comparison with the result of flotation concentration for 5 minutes).
以上の結果より、本発明の方法は従来の方法にくらべ浮
上濃縮濃度および処理水SSともに優れた結果を得てい
る。From the above results, the method of the present invention has obtained superior results in both the floating concentrate concentration and the treated water SS compared to the conventional method.
Claims (1)
添加して、懸濁粒子を浮上濃縮することを特徴とする有
機質汚泥の濃縮方法。 2 硫酸あるいは塩酸等の酸によりPHを4以下に調整
する特許請求の範囲第1項に記載の有機質汚泥の濃縮方
法。 3 過酸化水素を固形物当り、1.0%〜5%添加して
行なう特許請求の範囲第1項または第2項に記載の有機
質汚泥の濃縮方法。[Scope of Claims] 1. A method for concentrating organic sludge, which comprises adjusting the pH of sludge containing organic matter, adding hydrogen peroxide, and flotation concentration of suspended particles. 2. The method for concentrating organic sludge according to claim 1, wherein the pH is adjusted to 4 or less with an acid such as sulfuric acid or hydrochloric acid. 3. The method for concentrating organic sludge according to claim 1 or 2, which is carried out by adding hydrogen peroxide in an amount of 1.0% to 5% based on the solid matter.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP55021979A JPS5935279B2 (en) | 1980-02-22 | 1980-02-22 | Method for concentrating organic sludge |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP55021979A JPS5935279B2 (en) | 1980-02-22 | 1980-02-22 | Method for concentrating organic sludge |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS56118799A JPS56118799A (en) | 1981-09-17 |
| JPS5935279B2 true JPS5935279B2 (en) | 1984-08-28 |
Family
ID=12070134
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP55021979A Expired JPS5935279B2 (en) | 1980-02-22 | 1980-02-22 | Method for concentrating organic sludge |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5935279B2 (en) |
Families Citing this family (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE19756962A1 (en) * | 1997-12-20 | 1999-07-01 | Forschungszentrum Juelich Gmbh | Flotation reactor and process for flotation |
| EP1363857A2 (en) * | 2001-02-23 | 2003-11-26 | V.A.I. Ltd. | Methods and apparatus for biological treatment of waste waters |
| JP4493371B2 (en) * | 2004-03-04 | 2010-06-30 | 株式会社クボタ | Concentration separation method of sludge |
-
1980
- 1980-02-22 JP JP55021979A patent/JPS5935279B2/en not_active Expired
Also Published As
| Publication number | Publication date |
|---|---|
| JPS56118799A (en) | 1981-09-17 |
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