JP2002233895A - Deodorization method for swage sludge - Google Patents

Deodorization method for swage sludge

Info

Publication number
JP2002233895A
JP2002233895A JP2001075028A JP2001075028A JP2002233895A JP 2002233895 A JP2002233895 A JP 2002233895A JP 2001075028 A JP2001075028 A JP 2001075028A JP 2001075028 A JP2001075028 A JP 2001075028A JP 2002233895 A JP2002233895 A JP 2002233895A
Authority
JP
Japan
Prior art keywords
sludge
air
cavitation
fine
bubbles
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
JP2001075028A
Other languages
Japanese (ja)
Inventor
Masahiro Matsunaga
全央 松永
Mikiya Kitami
幹冶 北見
Seiichiro Miyata
征一郎 宮田
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.)
PARATEKKU KK
Original Assignee
PARATEKKU KK
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 PARATEKKU KK filed Critical PARATEKKU KK
Priority to JP2001075028A priority Critical patent/JP2002233895A/en
Publication of JP2002233895A publication Critical patent/JP2002233895A/en
Pending legal-status Critical Current

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  • Treatment Of Sludge (AREA)

Abstract

PROBLEM TO BE SOLVED: To provide a method of deodorizing sewer sludge by suppressing the generation of hydrogen sulfide, mercaptan, ammonia, etc., in the sewer sludge. SOLUTION: The sewer sludge is forcibly fluidized and air is sucked by an ejector effect into the flowing sewer sludge. The sucked air is made into fine air bubbles by a cavitation effect.

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、下水汚泥の脱臭方
法に係るものである。
[0001] The present invention relates to a method for deodorizing sewage sludge.

【0002】[0002]

【従来の技術】下水汚泥には、有機物の腐敗や嫌気性菌
などが分泌するアンモニア、硫化水素、メルカプタン等
の臭気が発生し、下水処理場周辺では環境問題になって
いる。従来、汚泥の臭気対策には薬剤や微生物によって
分解する方法が採用されているが、薬剤による方法は、
薬剤そのものが汚泥に残る弊害がある。微生物によって
分解する方法は、処理速度が遅いために、大量処理には
不向きである。
2. Description of the Related Art Sewage sludge emits odors such as ammonia, hydrogen sulfide and mercaptan secreted by decay of organic matter and anaerobic bacteria, and this is an environmental problem around sewage treatment plants. Conventionally, the method of decomposing by sludge with chemicals or microorganisms has been adopted to control the odor of sludge.
There is an adverse effect that the drug itself remains in the sludge. The method of decomposing by microorganisms is not suitable for mass processing because the processing speed is slow.

【0003】[0003]

【発明が解決しようとする課題】本発明はかかる問題点
にかんがみてなされたもので、薬剤や微生物を使うこと
なく、大量処理ができ、かつ完全脱臭できる方法を提供
せんとするものである。
SUMMARY OF THE INVENTION The present invention has been made in view of the above problems, and an object of the present invention is to provide a method capable of performing a large amount of treatment without using drugs or microorganisms and completely deodorizing.

【0004】[0004]

【課題を解決するための手段】本発明者は、かかる問題
点に鑑みて鋭意研究を行い、下記請求項1〜3の手段で
問題を解決できることを見出した。 「請求項1」下水汚泥を強制流動させて該流動する汚泥
の中に空気の微細気泡を分散させることを特徴とする下
水汚泥の脱臭方法。 「請求項2」上記微細気泡は、流動する汚泥の中にエジ
ェクター作用で空気を吸引し、該吸引した空気をキャビ
テーション作用で微細気泡化したものである請求項1に
記載の脱臭方法。 「請求項3」上記微細気泡は、機械的なせん断力によっ
て微細気泡化したものである請求項1に記載の脱臭方
法。
Means for Solving the Problems The present inventor has made intensive studies in view of the above problems and found that the problems can be solved by the following claims 1 to 3. [Claim 1] A method for deodorizing sewage sludge, comprising forcibly flowing sewage sludge and dispersing fine air bubbles in the flowing sludge. [Claim 2] The deodorization method according to claim 1, wherein the fine air bubbles are obtained by sucking air into the flowing sludge by an ejector action and converting the sucked air into fine air bubbles by a cavitation action. [Claim 3] The deodorization method according to claim 1, wherein the fine bubbles are formed into fine bubbles by mechanical shearing force.

【0005】[0005]

【発明の実施の形態】汚泥に空気の微細気泡を混合する
と、汚泥の酸素濃度が高くなり、嫌気性の菌の活動を抑
止でき、硫化水素、メルカプタン等の発生を防止でき
る。また腐敗の抑制および腐敗によって発生したアンモ
ニア等を酸化分解することができる。汚泥に溶解する空
気の量は、気泡全体の表面積に比例するので、気泡の直
径はより小さいほど有利である。
BEST MODE FOR CARRYING OUT THE INVENTION When fine air bubbles are mixed with sludge, the oxygen concentration of the sludge increases, the activity of anaerobic bacteria can be suppressed, and the generation of hydrogen sulfide, mercaptan and the like can be prevented. Further, it is possible to suppress rot and oxidatively decompose ammonia and the like generated by the rot. Since the amount of air dissolved in the sludge is proportional to the surface area of the entire bubble, the smaller the bubble diameter, the better.

【0006】汚泥に微細気泡を混合分散させる手段とし
ては、いわゆるエアーレーションによる方法が有効であ
るが、従来から使用されている散気管、散気板、散気筒
等の微細孔から空気を噴出す方法は、気泡の噴出孔に汚
泥が目詰りし易いので、本発明の目的には、目詰まりの
おきにくい、あるいはまったく起きない構造が好まし
い。
As a means for mixing and dispersing fine air bubbles in sludge, a so-called aeration method is effective, but air is blown out from fine holes such as conventionally used diffusers, diffusers and diffusers. In the method, since the sludge is easily clogged in the bubble outlet, for the purpose of the present invention, a structure in which clogging hardly occurs or does not occur at all is preferable.

【0007】本発明の目的には、図1〜3に示す気泡発
生装置が好ましい。図1の装置は、上部に空気自吸口
1、側面に汚泥の圧入口2、気泡の噴出口3を備えた発
生装置で、汚泥を圧入口2から圧入し、中で旋回流を発
生させて3から汚泥を噴射させるものであるが、汚泥を
圧入して中で旋回流を発生させ、から汚泥を噴出させる
とき、自吸口1から空気が吸い込まれ、吸い込まれた空
気は汚泥の旋回流と混ざり、旋回流の界面で発生するせ
ん断作用により微細気泡に分断されて噴出口から汚泥と
一緒に噴出される機構である。
For the purposes of the present invention, the bubble generator shown in FIGS. The apparatus shown in FIG. 1 is a generator having an air self-priming port 1 at an upper portion, a sludge pressure inlet 2 on a side surface, and a bubble jet port 3. Sludge is injected from the pressure inlet 2 to generate a swirling flow therein. When the sludge is injected from the self-priming port 1, air is sucked in from the self-priming port 1, and the sucked air is mixed with the swirl flow of the sludge. It is a mechanism that is separated into fine bubbles by the shearing action generated at the interface of the mixing and swirling flow and is ejected together with the sludge from the ejection port.

【0008】図2の方法は下部から小型ブロワーで送り
込まれた空気は旋回上昇の過程で微細気泡に分断されて
汚泥と混合され、頂部の出口で大量の微細気泡を発生さ
せる機構である。図1,2の装置は従来装置のような微
細な気泡の噴出孔がないので目詰まりがおきにくい特徴
がある。
The method shown in FIG. 2 is a mechanism in which air sent from a lower portion by a small blower is divided into fine bubbles in the process of swirling and mixed with sludge, and a large amount of fine bubbles are generated at an outlet at the top. The apparatus shown in FIGS. 1 and 2 has a feature that the clogging hardly occurs because there is no ejection hole for fine bubbles unlike the conventional apparatus.

【0009】図3はキャビテーション作用を使って微細
気泡にする方法である。本発明の目的のためにはもっと
も好ましい方法である。キャビテーションを利用する場
合、空気はエジェクター作用によって自吸させる。すな
わちポンプを使ってパイプの中に汚泥を圧送すると、パ
イプにあけた穴から空気が吸引される原理を使って空気
を吸引し、吸引した空気にキャビテーションを発生させ
て微細な気泡に変換する方法である。キャビテーション
は汚泥の圧送パイプと気泡発生装置をつなぎ、図3に示
すような気泡発生装置の汚泥放出口の直径を扇型に拡径
させると、拡径部に負圧が発生してキャビテーションが
発生する。また拡径部に図4のような衝突板を設ける
と、ポケット部分にキャビテーションが効果的に発生す
る。キャビテーションが発生するとき、空気は数ミクロ
ンの微細な泡になって汚泥に分散する。また汚泥流には
数千気圧のせん断力が発生し、汚泥の中の有機質廃棄物
等の固形粒子は解きほぐされて懸濁分散され、発生した
空気の微細気泡と混合される。これによって有機物の腐
敗、嫌気性菌の活動も抑制され、またアンモニア等も酸
化分解される。キャビテーション発生装置の拡径部の角
度は40〜90度、ポンプの圧送圧は30〜200気圧
程度がよい。
FIG. 3 shows a method of forming fine bubbles using cavitation. This is the most preferred method for the purposes of the present invention. When cavitation is used, air is self-primed by an ejector action. That is, when sludge is pumped into a pipe using a pump, air is sucked using the principle that air is sucked from a hole drilled in the pipe, and cavitation is generated in the sucked air to convert it into fine bubbles It is. In cavitation, the sludge pumping pipe is connected to the bubble generator, and the diameter of the sludge discharge port of the bubble generator as shown in Fig. 3 is fan-shaped. Negative pressure is generated in the expanded part and cavitation occurs. I do. When the collision plate as shown in FIG. 4 is provided in the enlarged diameter portion, cavitation is effectively generated in the pocket portion. When cavitation occurs, the air disperses into the sludge in fine bubbles of several microns. Further, a shear force of several thousand atmospheres is generated in the sludge flow, and solid particles such as organic wastes in the sludge are disintegrated, suspended and dispersed, and mixed with fine bubbles of the generated air. As a result, decay of organic matter and the activity of anaerobic bacteria are suppressed, and ammonia and the like are oxidatively decomposed. The angle of the enlarged diameter portion of the cavitation generator is preferably 40 to 90 degrees, and the pumping pressure of the pump is preferably about 30 to 200 atmospheres.

【0010】上記した気泡発生装置はいずれも汚泥の貯
留槽に沈めて汚泥の中で微細な泡を発生させる。気泡発
生装置に汚泥を圧送するポンプは貯留槽の外に配置す
る。あるいは必要に応じて液中に沈めて使用する水中ポ
ンプを使用してもよい。気泡発生装置は貯留槽の中心部
に配置するほうがよい。従って大きな貯留槽の場合、貯
留槽の外にポンプを置くと、汚泥に沈めた気泡発生装置
とつなぐのに長いパイプが必要になる。このような場
合、水中ポンプを利用するとよい。水中ポンプを汚泥の
中に沈めて気泡発生装置とつなぐとパイプを短くできる
利点がある。あるいはポンプの排出口の先端に気泡発生
装置を取り付けるとパイプが不要になる。
[0010] Each of the above-mentioned bubble generators is submerged in a sludge storage tank to generate fine bubbles in the sludge. A pump for pumping sludge to the bubble generator is arranged outside the storage tank. Alternatively, a submersible pump that is used by submerging in a liquid as needed may be used. It is better to arrange the bubble generator in the center of the storage tank. Therefore, in the case of a large storage tank, if the pump is placed outside the storage tank, a long pipe is required to connect to the bubble generator submerged in the sludge. In such a case, a submersible pump may be used. If the submersible pump is submerged in the sludge and connected to the bubble generator, there is an advantage that the pipe can be shortened. Alternatively, if a bubble generator is attached to the tip of the outlet of the pump, the pipe becomes unnecessary.

【0011】空気を吸い込む自吸パイプは、図1に示す
ように汚泥の液面から外に出して気泡発生装置と外気を
連通させる。
[0011] The self-priming pipe for sucking in air comes out of the liquid level of the sludge as shown in FIG. 1 and communicates the bubble generator with the outside air.

【0012】[0012]

【実施例】実施例1(硫化水素の消臭) 1000ppmの硫化水素を含む臭気の強い下水汚泥の
貯槽(10m)の底に図3のキャビテーション発生装
置を沈め、貯槽の外に置いたポンプとホースでつなぎ、
圧力100気圧で汚泥を循環圧送し、5時間キャビテー
ション処理した。 結果 硫化水素濃度は30ppmに減少し、匂いが消えた。
Example 1 (Deodorization of Hydrogen Sulfide) A cavitation generator of FIG. 3 was submerged at the bottom of a storage tank (10 m 3 ) of odorous sewage sludge containing 1000 ppm of hydrogen sulfide, and was placed outside the storage tank. And a hose.
The sludge was circulated at a pressure of 100 atm and cavitation-treated for 5 hours. Results The hydrogen sulfide concentration was reduced to 30 ppm and the odor was gone.

【0013】実施例2(アンモニアの消臭) 2000ppmのアンモニアを含む下水汚泥20m
汚泥の貯槽の底に、水中ポンプと図4のキャビテーショ
ン発生装置を沈め、両方をパイプでつないで汚泥を圧力
80気圧で循環圧送し、3時間キャビテーション処理し
た。アンモニア濃度は30ppmに減少し、匂いも消え
た。
[0013] the bottom of the reservoir of the sludge of Example 2 Sewage sludge 20 m 3 containing ammonia 2000 ppm (deodorizing ammonia), submerged cavitation generator of submersible pump and 4, the pressure sludge by connecting both pipe The solution was circulated at 80 atm and cavitation treated for 3 hours. The ammonia concentration decreased to 30 ppm and the odor disappeared.

【0014】実施例3(オゾンの効果) 2500ppmの硫化水素、1000ppmのメルカプ
タン、1500ppmのアンモニアを含む臭気のきわめ
て強い下水汚泥の貯槽(10m)の底に図3のキャビ
テーション発生装置を沈め、空気の自吸パイプはオゾン
発生装置と連結した。ポンプは水中ポンプを使用して直
接キャビテーション発生装置とホースで連結した。汚泥
は、圧力100気圧で循環圧送し、3時間キャビテーシ
ョン処理した。 結果 硫化水素濃度は10ppm、メルカプタンは10pp
m、アンモニアはほぼゼロに減少し、匂いは完全消臭で
きた。以上実施例1,2,3の結果より、本発明の方法
は、硫化水素、メルカプタン、アンモニア等の消臭に極
めて効果があることを確認できた。
Example 3 (Effect of ozone) The cavitation generator shown in FIG. 3 is submerged in the bottom of a storage tank (10 m 3 ) of odorous sewage sludge containing 2500 ppm of hydrogen sulfide, 1000 ppm of mercaptan and 1500 ppm of ammonia, and air Was connected to an ozone generator. The pump was hosed directly to the cavitation generator using a submersible pump. The sludge was circulated at a pressure of 100 atm and cavitation treated for 3 hours. Result The hydrogen sulfide concentration was 10 ppm, and mercaptan was 10 pp.
m, ammonia decreased to almost zero, and the odor was completely deodorized. From the results of Examples 1, 2, and 3, it was confirmed that the method of the present invention was extremely effective in deodorizing hydrogen sulfide, mercaptan, ammonia, and the like.

【0015】[0015]

【発明の効果】以上詳記した様に、本発明は薬剤や微生
物を使用することなく大量の汚泥を経済的に消臭できる
特徴を有するものである。
As described in detail above, the present invention has a feature that a large amount of sludge can be economically deodorized without using a drug or a microorganism.

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

【図1】図1は本発明実施例の説明図である。FIG. 1 is an explanatory diagram of an embodiment of the present invention.

【図2】図2は本発明実施例の説明図である。FIG. 2 is an explanatory view of an embodiment of the present invention.

【図3】図3は本発明実施例の説明図で、キャビテーシ
ョンを使用するときの説明図である。
FIG. 3 is an explanatory view of an embodiment of the present invention, which is an explanatory view when cavitation is used.

【図4】図4は本発明実施例の別のキャビテーション装
置の説明図である。
FIG. 4 is an explanatory diagram of another cavitation device according to the embodiment of the present invention.

【符号の説明】[Explanation of symbols]

1…空気自吸口 2…汚泥圧入口 3…気泡の噴出口 1. Air self-priming port 2. Sludge pressure inlet 3. Air bubble outlet

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】下水汚泥を強制流動させて該流動する汚泥
の中に空気の微細気泡を分散させることを特徴とする下
水汚泥の脱臭方法。
1. A method for deodorizing sewage sludge, comprising forcibly flowing sewage sludge and dispersing fine air bubbles in the flowing sludge.
【請求項2】上記微細気泡は、流動する汚泥の中にエジ
ェクター作用で空気を吸引し、該吸引した空気をキャビ
テーション作用で微細気泡化したものである請求項1に
記載の脱臭方法。
2. The deodorizing method according to claim 1, wherein the fine air bubbles are obtained by sucking air into the flowing sludge by an ejector action and converting the sucked air into fine air bubbles by a cavitation action.
【請求項3】上記微細気泡は、機械的なせん断力によっ
て微細気泡化したものである請求項1に記載の脱臭方
法。
3. The deodorizing method according to claim 1, wherein the fine bubbles are formed into fine bubbles by a mechanical shearing force.
JP2001075028A 2001-02-09 2001-02-09 Deodorization method for swage sludge Pending JP2002233895A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2001075028A JP2002233895A (en) 2001-02-09 2001-02-09 Deodorization method for swage sludge

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2001075028A JP2002233895A (en) 2001-02-09 2001-02-09 Deodorization method for swage sludge

Publications (1)

Publication Number Publication Date
JP2002233895A true JP2002233895A (en) 2002-08-20

Family

ID=18932178

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2001075028A Pending JP2002233895A (en) 2001-02-09 2001-02-09 Deodorization method for swage sludge

Country Status (1)

Country Link
JP (1) JP2002233895A (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2003019497A (en) * 2001-07-06 2003-01-21 Sumitomo Precision Prod Co Ltd Sludge treatment method and ejector
JP2010082541A (en) * 2008-09-30 2010-04-15 Nippon Paper Industries Co Ltd Method for inhibiting odor of wastewater
WO2012003815A2 (en) 2010-07-07 2012-01-12 Vysoké učeni technické v Brně Device for killing microorganisms in liquids
CN105668973A (en) * 2016-04-14 2016-06-15 湖南工业大学 Spiral-flow type jammed cavitation device for breaking excess sludge
CN109516659A (en) * 2018-12-18 2019-03-26 北京欧睿康环境技术有限公司 A kind of sludge treating system equipped with mud decrement device

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2003019497A (en) * 2001-07-06 2003-01-21 Sumitomo Precision Prod Co Ltd Sludge treatment method and ejector
JP2010082541A (en) * 2008-09-30 2010-04-15 Nippon Paper Industries Co Ltd Method for inhibiting odor of wastewater
WO2012003815A2 (en) 2010-07-07 2012-01-12 Vysoké učeni technické v Brně Device for killing microorganisms in liquids
CN105668973A (en) * 2016-04-14 2016-06-15 湖南工业大学 Spiral-flow type jammed cavitation device for breaking excess sludge
CN105668973B (en) * 2016-04-14 2019-01-11 湖南工业大学 A kind of spiral-flow type cracking excess sludge is jammed cavitation device
CN109516659A (en) * 2018-12-18 2019-03-26 北京欧睿康环境技术有限公司 A kind of sludge treating system equipped with mud decrement device

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