JPS5933000A - Dehydration of digested night soil sludge - Google Patents
Dehydration of digested night soil sludgeInfo
- Publication number
- JPS5933000A JPS5933000A JP57141492A JP14149282A JPS5933000A JP S5933000 A JPS5933000 A JP S5933000A JP 57141492 A JP57141492 A JP 57141492A JP 14149282 A JP14149282 A JP 14149282A JP S5933000 A JPS5933000 A JP S5933000A
- Authority
- JP
- Japan
- Prior art keywords
- sludge
- water
- digested
- site
- washing
- 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
Links
Landscapes
- Treatment Of Sludge (AREA)
Abstract
Description
【発明の詳細な説明】
この発明は、し尿消化汚泥の脱水処理方法に関するもの
であり、さらに詳しくいうと、し尿の好気性または嫌気
性消化処理によって生じる消化汚泥の脱水処理方法に関
するものである。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for dehydrating digested human waste sludge, and more specifically, to a method for dehydrating digested sludge produced by aerobic or anaerobic digestion of human waste.
従来のこの種の処理方法について、第1図を参照して説
明する。し尿の好気性あるいは嫌気性消化汚泥は、凍結
融解処理における所要エネルギーを減らすために遠心濃
縮機などによって濃縮したのち、硫酸のような酸や塩化
第二鉄のような酸性凝集剤によってpH調整をpH調整
部1で行った後、凍結融解部2において凍結、融解し、
脱水性の改善がはかられる。かくして脱水性が改善され
た汚泥は、脱水部3で脱水処理され、脱水ケーキと脱離
液で分離されていた。A conventional processing method of this type will be explained with reference to FIG. Aerobic or anaerobic digested sludge from human waste is concentrated using a centrifugal concentrator to reduce the energy required in the freeze-thaw process, and then the pH is adjusted using an acid such as sulfuric acid or an acidic flocculant such as ferric chloride. After being carried out in the pH adjustment section 1, it is frozen and thawed in the freezing and thawing section 2,
Improves dehydration. The sludge with improved dewatering properties was dehydrated in the dewatering section 3, and separated into a dehydrated cake and a desorbed liquid.
しかし、以上の従来方法によると、消化汚泥中の、主と
して重炭酸塩や炭酸塩でなるアルカリ度成分が酸と反応
して炭酸ガスを生成し、この炭酸ガが汚泥中に分散する
現象が発生する。そのため、見かけの汚泥容量が増大し
、凍結融解処理における実質的な処理量が減少し、かつ
、凍結処理効果も低下する等の欠点があった。However, according to the above conventional method, the alkalinity component mainly consisting of bicarbonate and carbonate in the digested sludge reacts with acid to generate carbon dioxide gas, and this carbon dioxide gas is dispersed in the sludge. do. Therefore, there were disadvantages such as an increase in the apparent sludge volume, a decrease in the actual throughput in the freeze-thaw treatment, and a decrease in the effect of the freeze-thaw treatment.
この発明は、以上のような従来の方法にあった欠点を除
去しようとするもので、し尿消化汚泥をあらかじめ水で
洗浄してアルカリ度成分を減少させることにより炭酸ガ
スの発生を抑制し、かつ、凍結処理効果を向上したし尿
消化汚泥の脱水処理方法を提供することを目的とするも
のである。This invention aims to eliminate the drawbacks of the conventional methods as described above, and it suppresses the generation of carbon dioxide gas by washing the human waste digested sludge with water in advance to reduce the alkalinity component. The object of the present invention is to provide a method for dehydrating human waste digested sludge with improved freezing treatment effect.
以下、この発明の一実施例を、第一図を参照して説明す
る。図において、従来のpH調整部1に先行して、消化
汚泥の水洗部1、水洗汚泥を濃縮するための沈澱部12
、沈澱分離により濃縮された汚泥をさらに濃縮する遠心
濃縮部13による処理を行なう。これを、好気性消化汚
泥の場合について詳述する。An embodiment of the present invention will be described below with reference to FIG. In the figure, a conventional pH adjustment section 1 is preceded by a water washing section 1 for digested sludge, and a settling section 12 for concentrating the washed sludge.
The sludge concentrated by sedimentation is further concentrated by a centrifugal concentration section 13. This will be explained in detail in the case of aerobic digestion sludge.
好気性消化汚泥は、まず、水洗部11で、汚泥量の2倍
以上、望ましくは4倍以上の水により水洗する。下表に
、この場合の水洗希釈倍数と、硫酸でpH2.5に調整
した場合のガス発生量および凍結処理後のろ過比抵抗の
値を示した。The aerobically digested sludge is first washed in the washing section 11 with water at least twice the amount of sludge, preferably at least four times the amount of the sludge. The table below shows the water washing dilution factor in this case, the amount of gas generated when the pH was adjusted to 2.5 with sulfuric acid, and the value of the filtration specific resistance after freezing treatment.
この表からわかるように、希釈倍数が2倍以上の水洗に
よりガス発生量は75%低減し、4倍以上ではガス発生
量は零になり、ろ過比抵抗も85%低下したことがわか
る。As can be seen from this table, the amount of gas generated was reduced by 75% when the dilution factor was 2 times or more, and when the dilution factor was 4 times or more, the amount of gas generated was zero and the filtration specific resistance was also reduced by 85%.
かようにして水洗部11で水洗された汚泥は、ついで沈
澱部12で沈澱部分離により濃縮され、さらに遠心濃縮
部13で固形分濃度4〜8%まで濃縮される。濃縮され
た汚泥は、ついで、従来の手順に従って処理さ第1る。The sludge thus washed with water in the water washing section 11 is then concentrated in the sedimentation section 12 by separating the sediment, and further concentrated in the centrifugal concentration section 13 to a solid content concentration of 4 to 8%. The thickened sludge is then first treated according to conventional procedures.
すなわち、pH調整部1で硫酸などによりpH調整され
、凍結融解部2に送られて凍結処理され、脱水性を改善
したのち、脱水部3で脱水処理される。That is, the pH is adjusted with sulfuric acid or the like in a pH adjustment section 1, and the material is sent to a freeze-thaw section 2 where it is frozen to improve its dehydration properties, and then dehydrated in a dehydration section 3.
なお、上記実施例ではpH調整部1における酸として硫
酸を用いたが、塩酸や塩化第二鉄、その他pHを所定値
に調整しうるものであればよい。In the above embodiment, sulfuric acid was used as the acid in the pH adjusting section 1, but any acid such as hydrochloric acid, ferric chloride, or any other acid that can adjust the pH to a predetermined value may be used.
さらに沈澱部12を除いて直接遠心濃縮部13で濃縮し
てもよい。Furthermore, the precipitation section 12 may be removed and the product may be directly concentrated in the centrifugal concentration section 13.
以上のように、この発明によれば、消化汚泥をpH調整
の前段で水洗することにより、アルカリ度を低減させて
ガス発生を大幅に抑制し、凍結融解処理効果を向上する
ことができる。As described above, according to the present invention, by washing the digested sludge with water before pH adjustment, the alkalinity can be reduced, gas generation can be significantly suppressed, and the freeze-thaw treatment effect can be improved.
第1図は、従来方法のフロー図、第2図はこの発明の一
実施例のフロー図である。
1・・pH調整部、2・・凍結融解部,3・・脱水部、
11・・水洗部、12・・沈澱部、13・・遠心濃縮部
。
なお、各図中、同一符号は同−又は相当部分を示す。FIG. 1 is a flowchart of a conventional method, and FIG. 2 is a flowchart of an embodiment of the present invention. 1. pH adjustment section, 2. Freeze-thaw section, 3. Dehydration section,
11..Water washing section, 12..Sedimentation section, 13..Centrifugal concentration section. In each figure, the same reference numerals indicate the same or corresponding parts.
Claims (3)
汚泥の脱水処理において、前記消化汚泥を水で洗浄した
後、硫酸のごとき酸、塩化第二鉄のごとぎ凝集剤により
pHを調整し、ついで凍結融解処理を施して脱水性を改
善した後脱水処理することを特徴とするし尿消化汚泥の
脱水処理方法。(1) In the dehydration treatment of digested sludge produced by aerobic and anaerobic digestion of human waste, the digested sludge is washed with water, and then the pH is adjusted with an acid such as sulfuric acid or a flocculant such as ferric chloride. A method for dewatering digested human waste sludge, which is characterized in that the dehydration treatment is performed after the dewatering property is improved by freeze-thawing treatment.
水を使用する特許請求の範囲第1項記載のし尿消化汚泥
の脱水処理方法。(2) The method for dehydrating human waste digested sludge according to claim 1, wherein water in an amount twice or more of the amount of digested sludge is used in washing with water.
を行なう特許請求の範囲第1項記載のし尿消化汚泥の脱
水処理方法。(3) The method for dewatering human waste digested sludge according to claim 1, wherein the pH is adjusted after the water-washed digested sludge is concentrated in a concentration section.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP57141492A JPS5933000A (en) | 1982-08-12 | 1982-08-12 | Dehydration of digested night soil sludge |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP57141492A JPS5933000A (en) | 1982-08-12 | 1982-08-12 | Dehydration of digested night soil sludge |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS5933000A true JPS5933000A (en) | 1984-02-22 |
JPH0138000B2 JPH0138000B2 (en) | 1989-08-10 |
Family
ID=15293176
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP57141492A Granted JPS5933000A (en) | 1982-08-12 | 1982-08-12 | Dehydration of digested night soil sludge |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS5933000A (en) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS6391107A (en) * | 1986-10-03 | 1988-04-21 | Nittetsu Mining Co Ltd | Treatment of waste water |
JPH0321392A (en) * | 1989-06-19 | 1991-01-30 | Niigata Eng Co Ltd | Coagulant adding method and apparatus |
JP2006116528A (en) * | 2004-09-21 | 2006-05-11 | Takuma Co Ltd | Biomass resource treatment method and its treatment equipment |
CN106145579A (en) * | 2016-08-05 | 2016-11-23 | 华东理工大学 | Alkaline residue and excess sludge coupled rotational flow release carbon method and device |
-
1982
- 1982-08-12 JP JP57141492A patent/JPS5933000A/en active Granted
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS6391107A (en) * | 1986-10-03 | 1988-04-21 | Nittetsu Mining Co Ltd | Treatment of waste water |
JPH0321392A (en) * | 1989-06-19 | 1991-01-30 | Niigata Eng Co Ltd | Coagulant adding method and apparatus |
JP2006116528A (en) * | 2004-09-21 | 2006-05-11 | Takuma Co Ltd | Biomass resource treatment method and its treatment equipment |
CN106145579A (en) * | 2016-08-05 | 2016-11-23 | 华东理工大学 | Alkaline residue and excess sludge coupled rotational flow release carbon method and device |
CN106145579B (en) * | 2016-08-05 | 2020-07-28 | 华东理工大学 | Alkali residue and excess sludge coupling rotational flow carbon release method and device |
Also Published As
Publication number | Publication date |
---|---|
JPH0138000B2 (en) | 1989-08-10 |
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