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JPH0751699A - Deodorizing method in sewage sludge treatment and device therefor - Google Patents

Deodorizing method in sewage sludge treatment and device therefor

Info

Publication number
JPH0751699A
JPH0751699A JP20385293A JP20385293A JPH0751699A JP H0751699 A JPH0751699 A JP H0751699A JP 20385293 A JP20385293 A JP 20385293A JP 20385293 A JP20385293 A JP 20385293A JP H0751699 A JPH0751699 A JP H0751699A
Authority
JP
Japan
Prior art keywords
sludge
tank
humus
concd
sewage 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.)
Granted
Application number
JP20385293A
Other languages
Japanese (ja)
Other versions
JP2584182B2 (en
Inventor
Yuji Fujiwara
勇次 藤原
Yoshinori Hamaya
芳則 浜谷
Kazuyoshi Nishida
和善 西田
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.)
Chugai Ro Co Ltd
Original Assignee
Chugai Ro 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 Chugai Ro Co Ltd filed Critical Chugai Ro Co Ltd
Priority to JP5203852A priority Critical patent/JP2584182B2/en
Publication of JPH0751699A publication Critical patent/JPH0751699A/en
Application granted granted Critical
Publication of JP2584182B2 publication Critical patent/JP2584182B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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  • Treatment Of Sludge (AREA)

Abstract

PURPOSE:To remove malodor of concd. sludge generated in the treatment of sewage sludge at a low cost without causing environmental pollution by aerating the concd. sludge generated in the treatment of sewage sludge in the presence of humus to decompose the org. acid in the concd. sludge with microorganisms. CONSTITUTION:The concd. sludge from a thickener generated in the treatment of sewage sludge is introduced from a receiver pipe 11 into a first tank 10 into which air is blown from an aerator 13, aerated respectively in the tanks 10a, 10b and 10c in the presence of humus and then sent to a dehydrating stage 7 from a waste water pipe 12. The sludge is aerated with the air supplied from the aerator 13 successively in the tanks 10a, 10b and 10c in the increasing direction of an ORP value. Consequently, the org. acid in the concd. sludge generated by an anaerobic reaction in the preceding stage is decomposed by the microorganisms in the humus, that is, the pH is increased, and the generation of malodor is suppressed.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は下水汚泥処理、特に、脱
水処理するまでの下水汚泥処理工程で発生する濃縮汚泥
の脱臭方法および脱臭装置に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a sewage sludge treatment, and more particularly to a deodorizing method and a deodorizing apparatus for concentrated sludge generated in a sewage sludge treating step until dehydration.

【0002】[0002]

【従来の技術】従来、下水処理場においては、一般に、
図3に示すように、スクリーン1でゴミ等を捕集したの
ち、最初沈澱槽2で固形物,汚泥を沈澱,分離させた
後、曝気槽3にて下水中に空気を吹き込み、下水汚泥中
の微生物を活性化させ、その後、最終沈澱槽4で汚泥を
沈澱分離させたのち系外に放水するようになっている。
一方、前記最初沈澱槽2と最終沈澱槽4とに沈澱した汚
泥は、濃縮槽5で濃縮され、この濃縮汚泥は貯留槽6を
経て脱水工程7でケーキ化されたのち、たとえば、焼却
処理されている。ところで、前記濃縮汚泥は悪臭が強
く、脱水作業場では作業環境が悪いため、金属系あるい
は酸化系の消臭剤を濃縮汚泥中に添加して悪臭対策を行
なっているのが現状である。
2. Description of the Related Art Conventionally, in a sewage treatment plant, generally,
As shown in FIG. 3, after collecting dusts and the like on the screen 1, solid matters and sludge are first settled and separated in the settling tank 2, and then air is blown into the sewage in the aeration tank 3 to remove the sludge. After activating the microorganisms, sludge is separated and separated in the final settling tank 4, and then discharged to the outside of the system.
On the other hand, the sludge settled in the first settling tank 2 and the final settling tank 4 is concentrated in a thickening tank 5, and the thickened sludge is caked in a dehydrating step 7 through a storage tank 6 and then incinerated, for example. ing. By the way, since the concentrated sludge has a bad odor and the working environment is bad in the dehydration work place, the present situation is to add a metallic or oxidizing deodorant to the concentrated sludge to prevent the bad odor.

【0003】[0003]

【発明が解決しようとする課題】しかしながら、前記消
臭剤は大量に使用されるため、ランニングコストが高く
なるばかりか、金属系消臭剤の場合、濃縮汚泥を脱水,
焼却した後も、消臭剤に含まれる重金属が溶出し、自然
界に蓄積して新たな環境悪化を引き起こす恐れがあり、
そのため、最終処分地に投棄する前に脱水ケーキを焼却
し、その焼却灰を成形,焼却して重金属が溶出しないよ
う処理する必要がある。また、酸化系消臭剤の場合、脱
臭の結果、硫酸を生成するので、配管や機器に腐蝕対策
を施す必要がある。さらに、消臭剤による脱臭は、化学
反応によるものなので、濃縮汚泥と消臭剤とを均一に混
合しないと効果が無いため、撹拌装置により撹拌を行っ
ているが、均一に混合するのは困難である。さらにま
た、消臭剤による脱臭では、濃縮汚泥の流れに合わせ
て、随時消臭剤を投入する必要があるので、消臭剤の受
入設備,貯留設備,定量供給設備が必要になるという問
題を有する。前記問題を解決するため、種々検討した結
果、一般に濃縮汚泥はpH4.5〜6.5、ORP値
(酸化還元電位)−150〜280mVの値を有し、臭
気の主成分は硫化水素、メチルメルカプタン等の硫黄化
合物であり、これらは脱臭処理前の濃縮汚泥のpH値お
よびORP値より脱臭処理後の値を高くすれば臭気の発
生を抑制できることが明らかになった。
However, since the above-mentioned deodorant is used in a large amount, not only the running cost becomes high, but also in the case of the metal-based deodorant, the concentrated sludge is dehydrated,
Even after incineration, heavy metals contained in deodorants may elute and accumulate in the natural world, causing new environmental deterioration.
Therefore, it is necessary to incinerate the dehydrated cake before it is dumped at the final disposal site, and to form and incinerate the incinerated ash to treat the heavy metal so as not to elute. Further, in the case of an oxidative deodorant, sulfuric acid is generated as a result of deodorization, so it is necessary to take measures against corrosion in pipes and equipment. Furthermore, since deodorization with a deodorant is due to a chemical reaction, it will not be effective unless the concentrated sludge and deodorant are uniformly mixed, so stirring is performed with a stirring device, but it is difficult to mix them uniformly. Is. Furthermore, in deodorization with a deodorant, it is necessary to add the deodorant at any time according to the flow of the concentrated sludge, and therefore, there is a problem that a deodorant receiving facility, a storage facility, and a quantitative supply facility are required. Have. As a result of various studies in order to solve the above problems, generally, concentrated sludge has a pH of 4.5 to 6.5 and an ORP value (oxidation-reduction potential) of −150 to 280 mV, and the main components of odor are hydrogen sulfide and methyl sulfide. It was clarified that sulfur compounds such as mercaptans can suppress the generation of odors by increasing the post-deodorization value than the pH value and ORP value of the concentrated sludge before the deodorization processing.

【0004】また、汚泥中に存在する微生物は沈澱槽で
沈澱すると空気が不足して嫌気反応により有機酸を生成
し、一方、空気を吹き込むと前記有機酸を分解する作用
を有する。そして、このような生物作用を行なう微生物
は、安価な腐植土中に多く存在する。したがって、本発
明は、この腐植土中の微生物を利用して、濃縮汚泥中の
有機酸を分解して汚泥のpHを上げて臭気の発生を抑制
する下水汚泥処理における脱臭方法およびその装置を提
供することを目的とする。
When the microorganisms existing in the sludge settle in the settling tank, the air is insufficient to generate an organic acid by an anaerobic reaction. On the other hand, when air is blown in, the microorganism has a function of decomposing the organic acid. And, many microorganisms that perform such biological action are present in inexpensive humus soil. Therefore, the present invention provides a deodorizing method and apparatus for treating sewage sludge, which utilizes the microorganisms in the humus to decompose the organic acid in the concentrated sludge to raise the pH of the sludge and suppress the generation of odor. The purpose is to do.

【0005】[0005]

【課題を解決するための手段】本発明は前記目的を達成
するために、下水汚泥処理における脱臭方法は、下水汚
泥処理工程で発生する濃縮汚泥を、腐植土の存在下で曝
気処理して前記濃縮汚泥中の有機酸を微生物により分解
するものであり、その脱臭装置は下水汚泥処理工程にお
ける濃縮槽からの濃縮汚泥の受入管と脱水機への濃縮汚
泥の排出管および曝気装置を備えた第1槽を設け、この
第1槽と並列に、曝気装置を備え、かつ、腐植土を投入
する第2槽を、該第2槽中の濃縮汚泥が前記第1槽との
間で循環可能に配管により連絡したものである。
In order to achieve the above object, the present invention is directed to a deodorizing method in the treatment of sewage sludge, wherein the concentrated sludge generated in the sewage sludge treatment step is aerated in the presence of humus soil. This is a device that decomposes organic acids in concentrated sludge by microorganisms, and its deodorizing device is equipped with a pipe for receiving concentrated sludge from the concentration tank in the sewage sludge treatment process, a pipe for discharging concentrated sludge to the dehydrator, and an aeration device. One tank is provided, the aeration device is provided in parallel with this first tank, and the second tank for feeding humus soil can circulate the concentrated sludge in the second tank with the first tank. It was communicated by piping.

【0006】[0006]

【実施例】つぎに、本発明の一実施例を図1にしたがっ
て説明する。図1は本発明にかかる下水汚泥処理におけ
る脱臭装置を示し、10は一端に前記従来の濃縮槽5か
らの濃縮汚泥を受け入れる受入管11と、脱水工程に放
出する排出管12とを有する第1槽で、図においては、
この第1槽10は10a,10b,10cの3槽からな
り、各槽10a,10b,10cには公知の曝気装置1
3が設置されている。また、14は腐植土を投入する第
2槽で、前記槽10b,10cに並列に設けられ、槽1
0cからの汚泥の一部を抜き取り、下記するように所定
時間、曝気したのち、槽10bに返送されるようになっ
ている。この第2槽14にも公知の曝気装置15が設置
されている。
EXAMPLE An example of the present invention will be described below with reference to FIG. FIG. 1 shows a deodorizing device in the treatment of sewage sludge according to the present invention, and 10 has a receiving pipe 11 for receiving the concentrated sludge from the conventional concentration tank 5 and a discharge pipe 12 for discharging the dehydration process at one end. In the tank, in the figure,
The first tank 10 is composed of three tanks 10a, 10b and 10c, and each of the tanks 10a, 10b and 10c has a known aeration device 1
3 are installed. Further, 14 is a second tank for introducing humus, which is provided in parallel with the tanks 10b and 10c,
A part of the sludge from 0c is extracted, aerated for a predetermined time as described below, and then returned to the tank 10b. A publicly known aeration device 15 is also installed in the second tank 14.

【0007】つぎに、前記構成からなる脱臭装置におけ
る脱臭工程について説明する。濃縮槽5からの濃縮汚泥
は受入管11から第1槽10に流入し、曝気装置13か
ら空気が吹き込まれ、槽10a,10b,10cでそれ
ぞれ曝気された汚泥は排水管12から脱水工程7に送ら
れる。そして、前記各槽10a,10b,10cで曝気
装置13から供給される空気により、流入する前記濃縮
汚泥よりも好気すなわちORP値が増加する方向に誘導
され、その結果、前工程における嫌気反応によって生成
された有機酸により酸性傾向にある濃縮汚泥は、その内
部に存在する微生物が有機酸を分解し、つまり、pHが
上昇し、臭気の発生を抑制することになる。
Next, the deodorizing step in the deodorizing device having the above-mentioned structure will be described. The thickened sludge from the thickening tank 5 flows into the first tank 10 from the receiving pipe 11, air is blown from the aeration device 13, and the sludge aerated in the tanks 10a, 10b, 10c is discharged from the drain pipe 12 to the dehydration step 7. Sent. Then, the air supplied from the aeration device 13 in each of the tanks 10a, 10b, 10c is induced in a direction in which the aerobic, that is, the ORP value, increases more than the inflowing concentrated sludge, and as a result, by the anaerobic reaction in the previous step. The concentrated sludge, which tends to be acidic due to the generated organic acid, is decomposed by the microorganisms present inside the sludge, that is, the pH is increased and the generation of odor is suppressed.

【0008】ところで、本発明においては、槽10cの
汚泥の一部を第2槽14に返送し、投入された腐植土と
混合するとともに、曝気装置15からの空気によりOR
P値を増加させ、汚泥を所定時間撹拌させる。前述のよ
うに、前記腐植土には多数の微生物が含まれているた
め、この微生物は空気により活性化し、濃縮汚泥中の有
機酸をさらに分解し、pHは第1槽10よりも上昇す
る。
By the way, according to the present invention, a part of the sludge in the tank 10c is returned to the second tank 14 and mixed with the humus that has been put in, and at the same time the air from the aeration device 15 is used for OR.
The P value is increased and the sludge is stirred for a predetermined time. As described above, since the humus contains a large number of microorganisms, the microorganisms are activated by the air, further decompose the organic acid in the concentrated sludge, and the pH becomes higher than that in the first tank 10.

【0009】このように、第2槽14で所定時間撹拌さ
れて十分に有機酸が分解し濃縮汚泥のpHが上昇する
と、この汚泥を再び第1槽10,実施例では槽10bに
返送し、第1槽のpHを上げるとともに、さらにここで
の微生物を活性化させて有機酸を分解し、pH値を上昇
させて臭気の発生を抑制して、前述のように、排出管1
2から脱水工程7に送るものである。
As described above, when the organic acid is sufficiently decomposed in the second tank 14 for a predetermined time to decompose and the pH of the concentrated sludge increases, the sludge is returned to the first tank 10, in the embodiment, the tank 10b, While raising the pH of the first tank, it further activates the microorganisms therein to decompose organic acids and raises the pH value to suppress the generation of odors.
2 to the dehydration step 7.

【0010】因みに、第1槽10,第2槽14での貯留
量が1.2m3,0.4m3で、濃縮槽からの流入量が
4.8m3/日、各曝気槽での供給空気量が200リッ
トル/分、第2槽への汚泥供給,返送量を各35リット
ル/回×4回/日、腐植土投入量を40kgとして実験
したところ、下表の通りの結果を得た。さらに、経時変
化の結果を図2に示す。
[0010] Incidentally, the first tank 10, the storage amount is 1.2 m 3 in the second tank 14, with 0.4 m 3, the inflow amount from the concentration tank is 4.8 m 3 / day, fed in each aeration tank When the amount of air was 200 liters / minute, the amount of sludge supplied to and returned from the second tank was 35 liters / time x 4 times / day, and the amount of humus input was 40 kg, the results were as shown in the table below. . Further, the results of changes over time are shown in FIG.

【0011】[0011]

【表1】 [Table 1]

【0012】なお、図2に示す臭気経時テストの測定方
法は、処理汚泥及びデオランL添加汚泥を合成樹脂製バ
ケツに採取し、臭気の経時変化を調べた。臭気成分は硫
化水素とメチルメルカプタンの臭気分析と同じ要領で測
定をした。
In the method of measuring the odor aging test shown in FIG. 2, the treated sludge and the sludge containing deorane L were sampled in a bucket made of synthetic resin, and the change with time of the odor was examined. The odor components were measured in the same manner as the odor analysis of hydrogen sulfide and methyl mercaptan.

【0013】[0013]

【発明の効果】以上の説明で明らかなように、本発明に
よれば、下水汚泥処理における濃縮汚泥の脱臭に、消臭
剤を使用することなく、安価な腐植土中の微生物を利用
して汚泥中の有機酸を分解するとともに、曝気により酸
素溶存量を増加して脱臭するため、重金属の溶出による
自然界への汚染問題は生じないので、焼却灰の焼成処理
が不要になる。また、腐蝕性の物質も生じないので配管
や機器に腐蝕対策を施す必要がなくなりメンテナンスも
容易なものとなる。さらに、曝気により濃縮汚泥と微生
物を撹拌するので、容易に均一に混合することができ
る。さらにまた、腐植土は一度投入すれば微生物が自己
増殖するので、長期間腐植土補充する必要がなく、か
つ、人体に悪影響をおよぼすものではないので、人手に
よる投入が可能であり、よって、受入,貯留,投入等の
設備を設けなくて良い。また、経時変化についても、消
臭剤より本発明の方が脱臭効果が持続する。
As is apparent from the above description, according to the present invention, microorganisms in inexpensive humus are utilized for deodorizing concentrated sludge in sewage sludge treatment without using a deodorant. Since the organic acid in the sludge is decomposed and the amount of oxygen dissolved is increased by deaeration to deodorize, there is no problem of pollution to the natural world due to elution of heavy metals, and thus the burning treatment of incinerated ash becomes unnecessary. In addition, since no corrosive substance is generated, it is not necessary to take measures against corrosion on the pipes and equipment, and the maintenance is easy. Furthermore, since the concentrated sludge and the microorganisms are agitated by aeration, they can be easily and uniformly mixed. Furthermore, since once the humus is added, the microorganisms self-reproduce, it is not necessary to replenish the humus for a long period of time, and it does not adversely affect the human body. , It is not necessary to provide facilities such as storage and input. Also, with respect to changes with time, the deodorizing effect of the present invention is longer than that of the deodorant.

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

【図1】 本発明の下水処理における脱臭装置の説明
図。
FIG. 1 is an explanatory diagram of a deodorizing device in sewage treatment of the present invention.

【図2】 臭気の経時変化を示すグラフ。FIG. 2 is a graph showing changes in odor with time.

【図3】 従来の下水処理の工程図。FIG. 3 is a process diagram of conventional sewage treatment.

【符号の説明】[Explanation of symbols]

5…濃縮槽、10…第1槽、10a,10b,10c…
槽、13,15…曝気装置、14…第2槽。
5 ... concentration tank, 10 ... first tank, 10a, 10b, 10c ...
Tanks 13, 15 ... Aeration device, 14 ... Second tank.

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 下水汚泥処理工程で発生する濃縮汚泥
を、腐植土の存在下で曝気処理して前記濃縮汚泥中の有
機酸を微生物により分解することを特徴とする下水汚泥
処理における脱臭方法。
1. A deodorizing method in sewage sludge treatment, which comprises aerating the concentrated sludge generated in the sewage sludge treatment step in the presence of humus to decompose organic acids in the concentrated sludge by microorganisms.
【請求項2】 下水汚泥処理工程における濃縮槽からの
濃縮汚泥の受入管と脱水機への濃縮汚泥の排出管および
曝気装置を備えた第1槽を設け、この第1槽と並列に、
曝気装置を備え、かつ、腐植土を投入する第2槽を、該
第2槽中の濃縮汚泥が前記第1槽との間で循環可能に配
管により連絡したことを特徴とする下水汚泥処理におけ
る脱臭装置。
2. A first tank provided with a receiving pipe for the concentrated sludge from the thickening tank in the sewage sludge treatment process, a discharging pipe for the concentrated sludge to the dehydrator, and an aeration device is provided in parallel with the first tank.
In a sewage sludge treatment, characterized in that a second tank equipped with an aeration device and into which humus is charged is connected to the first tank by a pipe so that the concentrated sludge in the second tank can circulate. Deodorizing device.
JP5203852A 1993-08-18 1993-08-18 Deodorizing equipment in sewage sludge treatment Expired - Fee Related JP2584182B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP5203852A JP2584182B2 (en) 1993-08-18 1993-08-18 Deodorizing equipment in sewage sludge treatment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP5203852A JP2584182B2 (en) 1993-08-18 1993-08-18 Deodorizing equipment in sewage sludge treatment

Publications (2)

Publication Number Publication Date
JPH0751699A true JPH0751699A (en) 1995-02-28
JP2584182B2 JP2584182B2 (en) 1997-02-19

Family

ID=16480768

Family Applications (1)

Application Number Title Priority Date Filing Date
JP5203852A Expired - Fee Related JP2584182B2 (en) 1993-08-18 1993-08-18 Deodorizing equipment in sewage sludge treatment

Country Status (1)

Country Link
JP (1) JP2584182B2 (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100445642B1 (en) * 2001-08-10 2004-08-30 서희동 Method for removing malodor by using activated humic substances
JP2008055324A (en) * 2006-08-31 2008-03-13 Hitachi Housetec Co Ltd Sewage cleaning tank
JP2008246326A (en) * 2007-03-29 2008-10-16 Kubota Corp Deodorizing method and deodorizer for organic sludge
KR20170130501A (en) 2015-03-26 2017-11-28 신에쓰 가가꾸 고교 가부시끼가이샤 A release agent composition for a silicone pressure-sensitive adhesive, a release film and a laminate

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5075851A (en) * 1973-11-01 1975-06-21
JPS5245144A (en) * 1975-10-07 1977-04-09 Tokuji Nakamichi Corrosion type tiolet trough
JPS5628000U (en) * 1979-08-13 1981-03-16
JPS6150678A (en) * 1984-08-18 1986-03-12 川崎重工業株式会社 Classifier and controller thereof
JPH0531490A (en) * 1991-08-02 1993-02-09 Ebara Jitsugyo Kk Biological treatment of organic sewage

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5075851A (en) * 1973-11-01 1975-06-21
JPS5245144A (en) * 1975-10-07 1977-04-09 Tokuji Nakamichi Corrosion type tiolet trough
JPS5628000U (en) * 1979-08-13 1981-03-16
JPS6150678A (en) * 1984-08-18 1986-03-12 川崎重工業株式会社 Classifier and controller thereof
JPH0531490A (en) * 1991-08-02 1993-02-09 Ebara Jitsugyo Kk Biological treatment of organic sewage

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100445642B1 (en) * 2001-08-10 2004-08-30 서희동 Method for removing malodor by using activated humic substances
JP2008055324A (en) * 2006-08-31 2008-03-13 Hitachi Housetec Co Ltd Sewage cleaning tank
JP2008246326A (en) * 2007-03-29 2008-10-16 Kubota Corp Deodorizing method and deodorizer for organic sludge
KR20170130501A (en) 2015-03-26 2017-11-28 신에쓰 가가꾸 고교 가부시끼가이샤 A release agent composition for a silicone pressure-sensitive adhesive, a release film and a laminate
US10563063B2 (en) 2015-03-26 2020-02-18 Shin-Etsu Chemical Co., Ltd. Release agent composition for silicone adhesive, release film, and laminate

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