JPH069680B2 - How to deodorize sludge - Google Patents

How to deodorize sludge

Info

Publication number
JPH069680B2
JPH069680B2 JP61091241A JP9124186A JPH069680B2 JP H069680 B2 JPH069680 B2 JP H069680B2 JP 61091241 A JP61091241 A JP 61091241A JP 9124186 A JP9124186 A JP 9124186A JP H069680 B2 JPH069680 B2 JP H069680B2
Authority
JP
Japan
Prior art keywords
sludge
hydrogen peroxide
mol
iron
amount
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 - Fee Related
Application number
JP61091241A
Other languages
Japanese (ja)
Other versions
JPS62247899A (en
Inventor
八州家 三上
裕次 谷村
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.)
Nittetsu Mining Co Ltd
Original Assignee
Nittetsu Mining Co 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 Nittetsu Mining Co Ltd filed Critical Nittetsu Mining Co Ltd
Priority to JP61091241A priority Critical patent/JPH069680B2/en
Publication of JPS62247899A publication Critical patent/JPS62247899A/en
Publication of JPH069680B2 publication Critical patent/JPH069680B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は下水汚泥、し尿汚泥、製紙工場の汚泥などであ
って硫化水素、メチールメルカプタン、アンモニア、ア
ミン類によって悪臭を発生する汚泥の脱臭方法に関する
ものである。
DETAILED DESCRIPTION OF THE INVENTION [Industrial field of application] The present invention relates to deodorization of sewage sludge, human waste sludge, sludge of a paper mill, etc., which produces a foul odor due to hydrogen sulfide, methyl mercaptan, ammonia, and amines. It is about the method.

〔従来の技術〕[Conventional technology]

従来、これらの汚泥の脱水には塩化第2鉄と消石炭を用
いる方法が行なわれていたが、最近では省エネルギー型
としてベルトプレスによる脱水方法が実施されている。
この方法は、有機高分子を用いて中性領域で脱水が行な
われるので腐敗が早く悪臭気の発生量が多く、作業環境
上からも問題となっている。
Conventionally, the method of using ferric chloride and slaked coal has been used to dehydrate these sludges, but recently, a dehydration method using a belt press has been implemented as an energy-saving type.
In this method, since organic polymers are used for dehydration in a neutral region, the organic matter is quickly decomposed and a large amount of foul odor is generated, which is a problem from the working environment.

この対策の1つとして本発明者らは、3価の鉄を主成分
とするポリ硫酸鉄溶液を有機高分子と併用することによ
って、脱水ケーキの含水率を低下すると同時に脱臭効果
があることを見い出し、第22回下水道研究発表会(昭
和60年6月)で提案した。
As one of the countermeasures, the present inventors have found that by using a polyiron sulfate solution containing trivalent iron as a main component in combination with an organic polymer, it is possible to reduce the water content of the dehydrated cake and to have a deodorizing effect. Found and proposed at the 22nd Sewer Research Presentation (June 1985).

また、下水汚泥などの脱臭について過酸化水素が有効で
あることも東京都下水道局によって発表されている。
The Tokyo Sewerage Bureau has also announced that hydrogen peroxide is effective for deodorizing sewage sludge.

〔発明が解決しようとする問題点〕[Problems to be solved by the invention]

ところがこれらの方法は、ポリ硫酸鉄や過酸化水素を大
量に用いる必要があること、過剰の過酸化水素などによ
って装置が腐食されるなどの問題がある。本発明者らは
これらの問題を解決するため、種々検討を行なったとこ
ろ、(1)3価の鉄は嫌気性汚泥と接する一部が2価の鉄
に還元されること、(2)この還元された2価の鉄は反応
性に富んでおり硫化物とすぐ反応すること、(3)3価の
鉄が存在しないと脱臭効果が悪いこと、(4)過酸化水
素、次亜塩素酸ソーダなどの酸化剤と併用すると脱臭効
果が著しく向上すること、(5)ポリ硫酸鉄、塩化第2鉄
などの3価の鉄を主成分とする凝集剤のみで脱臭すると
使用量が多いため汚泥のpHが低下(pH5以下)し、
脱水機などに腐食を起こす。また過酸化水素、次亜塩素
酸ソーダなどの酸化剤のみで脱臭を行なうと悪臭物質1
モル当たり5〜10倍のモル数が必要であり著しく腐食
を起こすことなどを知見した。
However, these methods have problems that it is necessary to use a large amount of polyiron sulfate and hydrogen peroxide, and the apparatus is corroded by excess hydrogen peroxide. The present inventors have conducted various studies to solve these problems. (1) Trivalent iron is partially reduced to divalent iron in contact with anaerobic sludge, (2) The reduced divalent iron is highly reactive and reacts immediately with sulfides, (3) the deodorizing effect is poor in the absence of trivalent iron, (4) hydrogen peroxide, hypochlorous acid The deodorizing effect is remarkably improved when used in combination with an oxidizing agent such as soda. PH of (lower than pH5),
Causes corrosion to dehydrators. Also, if deodorizing is performed only with an oxidizing agent such as hydrogen peroxide or sodium hypochlorite, a foul-smelling substance 1
It was found that 5 to 10 times the number of moles is required per mole and significant corrosion occurs.

〔問題点を解決するための手段及びその作用〕[Means for Solving Problems and Their Actions]

本発明は上記の知見に基づくもので、硫化水素、メチー
ルメルカプタン、アンモニア、アミン類のいずれか1種
以上の成分からなる悪臭物質を含んでいる汚泥に、極め
て少量のポリ硫酸鉄と過酸化水素を添加する汚泥の脱臭
方法である。本発明でポリ硫酸鉄としたのは、ポリ硫酸
鉄中の3価の鉄が一部悪臭物質と接して2価の鉄とな
り、これが悪臭物質と反応して硫化鉄となり、2価の鉄
がほとんど残らずに済む。このために、2価の鉄を多く
用いた時のようにpHを9以上として鉄のフロックを作
る必要がなく、アルカリと使用量は激減する。添加する
ポリ硫酸鉄の量は、悪臭物質のモル数より少なく、その
2/1000〜5/1000程度で必要十分であり、そ
れゆえpHがほとんど低下しない。特に過酸化水素と2
価の鉄との反応ではフェントン基が発生し、これが分解
しにくい悪臭物質を分解するのでより脱臭効果を向上し
ている。本発明で用いる過酸化水素の添加量は悪臭物質
より遥かに少なく、モル数でその3/1000〜1/1
00でよく、過酸化水素のみを添加する従来の脱臭方法
に比べて極めて微量で済む。反応は上記のように鉄が触
媒として働いているので脱水機や周辺機器を酸化腐食す
ることはほとんどない。
The present invention is based on the above-mentioned findings, and a sludge containing a malodorous substance composed of one or more components of hydrogen sulfide, methyl mercaptan, ammonia and amines is added to an extremely small amount of polyiron sulfate and peroxide. This is a method of deodorizing sludge by adding hydrogen. In the present invention, polyferric sulfate means that trivalent iron in polyiron sulfate partially contacts with a malodorous substance to form divalent iron, which reacts with the malodorous substance to form iron sulfide and divalent iron. Almost nothing is left. For this reason, it is not necessary to adjust the pH to 9 or higher to form iron flocs as in the case where a large amount of divalent iron is used, and the amount of alkali and the amount used is drastically reduced. The amount of polyferric sulfate added is less than the number of moles of the malodorous substance, and about 2/1000 to 5/1000 is necessary and sufficient, and therefore the pH hardly decreases. Especially hydrogen peroxide and 2
The Fenton group is generated in the reaction with valent iron, which decomposes a malodorous substance that is difficult to decompose, thereby further improving the deodorizing effect. The addition amount of hydrogen peroxide used in the present invention is much smaller than that of a malodorous substance, and is 3/1000 to 1/1 in terms of mole number.
00, which is extremely small compared with the conventional deodorizing method in which only hydrogen peroxide is added. Since iron acts as a catalyst in the reaction as described above, the dehydrator and peripheral equipment are hardly oxidized and corroded.

薬品の添加順序は、好ましくはポリ硫酸鉄を添加した後
に過酸化水素を添加するが、同時に添加する方法でもよ
い。
The order of adding the chemicals is preferably such that hydrogen peroxide is added after polyiron sulfate is added, but a method of simultaneously adding may be used.

〔実施例〕〔Example〕

製紙工場の凝集沈殿汚泥で硫化水素3000ppm、メ
チールメルカプタンを80ppm含んでいる原汚泥に、
ポリ硫酸鉄溶液(Fe3+160g/、SO4 2-375
g/の溶液)を添加し、つぎに過酸化水素(H
30%溶液)を添加して脱臭処理をした結果と従来法に
より脱臭処理した結果を第1表に示す。
A raw sludge containing 3000 ppm hydrogen sulfide and 80 ppm methyl mercaptan in the coagulation sedimentation sludge of a paper mill,
Poly iron sulfate solution (Fe 3+ 160g /, SO 4 2- 375
g / solution) and then hydrogen peroxide (H 2 O 2
Table 1 shows the results of deodorization treatment by adding 30% solution) and the results of deodorization treatment by the conventional method.

〔発明の効果〕 本発明は、ポリ硫酸鉄と過酸化水素を汚泥に併用添加す
る脱臭方法であるが、ポリ硫酸鉄や過酸化水素をそれぞ
れ単独で使用する方法に比べて著しくその添加量を減ら
して悪臭成分を除去することができる。
[Effects of the Invention] The present invention is a deodorizing method in which polyiron sulfate and hydrogen peroxide are added to sludge in combination, but the addition amount thereof is remarkably higher than that in the method using polyiron sulfate and hydrogen peroxide alone. The malodorous component can be removed by reducing the amount.

また添加量が少ないから、汚泥のpH低下や過剰な過酸
化水素による機器の腐食も大幅に軽減されるので、その
実用上の効果は大である。
Further, since the addition amount is small, the pH drop of sludge and the corrosion of the equipment due to excess hydrogen peroxide are significantly reduced, and the practical effect thereof is great.

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】硫化水素、メチールメルカプタン、アンモ
ニア、アミン類のいずれか1種以上の成分からなる悪臭
物質を含んでいる汚泥に、当該悪臭物質1モルに対して
2/1000モル〜5/1000モルのポリ硫酸鉄と3
/1000モル〜10/1000モルの過下酸化水素を
添加することを特徴とする汚泥と脱臭方法。
1. A sludge containing a malodorous substance composed of one or more components of hydrogen sulfide, methyl mercaptan, ammonia and amines, is contained in an amount of 2/1000 mol to 5/1000 mol / mol of the malodorous substance. 1000 moles of polyiron sulfate and 3
/ 1000 mol to 10/1000 mol of hydrogen peroxide under superoxide is added, and a sludge and a deodorizing method.
JP61091241A 1986-04-22 1986-04-22 How to deodorize sludge Expired - Fee Related JPH069680B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP61091241A JPH069680B2 (en) 1986-04-22 1986-04-22 How to deodorize sludge

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP61091241A JPH069680B2 (en) 1986-04-22 1986-04-22 How to deodorize sludge

Publications (2)

Publication Number Publication Date
JPS62247899A JPS62247899A (en) 1987-10-28
JPH069680B2 true JPH069680B2 (en) 1994-02-09

Family

ID=14020921

Family Applications (1)

Application Number Title Priority Date Filing Date
JP61091241A Expired - Fee Related JPH069680B2 (en) 1986-04-22 1986-04-22 How to deodorize sludge

Country Status (1)

Country Link
JP (1) JPH069680B2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP6172838B2 (en) * 2012-12-28 2017-08-02 無臭元工業株式会社 Wastewater treatment method

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5245582A (en) * 1975-10-09 1977-04-11 Tokai Denka Kogyo Kk Solid-liquid separation method of organic waste fluid sludge
JPS53110964A (en) * 1977-03-10 1978-09-28 Kurita Water Ind Ltd Dehydrating method for organic sludge
JPS5462655A (en) * 1977-10-26 1979-05-19 Mitsubishi Gas Chemical Co Method of treating sludge
JPS5594698A (en) * 1979-01-12 1980-07-18 Tsukishima Kikai Co Ltd Method of improving dehydrating property of organic sludge
JPS62168600A (en) * 1986-01-20 1987-07-24 Kurita Water Ind Ltd Concentrating process for organic sludge

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5245582A (en) * 1975-10-09 1977-04-11 Tokai Denka Kogyo Kk Solid-liquid separation method of organic waste fluid sludge
JPS53110964A (en) * 1977-03-10 1978-09-28 Kurita Water Ind Ltd Dehydrating method for organic sludge
JPS5462655A (en) * 1977-10-26 1979-05-19 Mitsubishi Gas Chemical Co Method of treating sludge
JPS5594698A (en) * 1979-01-12 1980-07-18 Tsukishima Kikai Co Ltd Method of improving dehydrating property of organic sludge
JPS62168600A (en) * 1986-01-20 1987-07-24 Kurita Water Ind Ltd Concentrating process for organic sludge

Also Published As

Publication number Publication date
JPS62247899A (en) 1987-10-28

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