JPH06154796A - Method and equipment for sludge treatment - Google Patents
Method and equipment for sludge treatmentInfo
- Publication number
- JPH06154796A JPH06154796A JP31546692A JP31546692A JPH06154796A JP H06154796 A JPH06154796 A JP H06154796A JP 31546692 A JP31546692 A JP 31546692A JP 31546692 A JP31546692 A JP 31546692A JP H06154796 A JPH06154796 A JP H06154796A
- Authority
- JP
- Japan
- Prior art keywords
- sludge
- ozone
- contact
- treatment
- sewage
- 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
Links
- 239000010802 sludge Substances 0.000 title claims abstract description 111
- 238000000034 method Methods 0.000 title claims description 8
- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 claims abstract description 63
- 238000006243 chemical reaction Methods 0.000 abstract description 12
- 239000010801 sewage sludge Substances 0.000 abstract description 10
- 241001148471 unidentified anaerobic bacterium Species 0.000 abstract description 4
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 abstract description 3
- 238000000354 decomposition reaction Methods 0.000 abstract description 3
- 239000001301 oxygen Substances 0.000 abstract description 3
- 229910052760 oxygen Inorganic materials 0.000 abstract description 3
- 238000004062 sedimentation Methods 0.000 abstract description 2
- 238000013019 agitation Methods 0.000 abstract 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 8
- 230000018044 dehydration Effects 0.000 description 5
- 238000006297 dehydration reaction Methods 0.000 description 5
- 230000006866 deterioration Effects 0.000 description 5
- 235000019645 odor Nutrition 0.000 description 5
- 239000010865 sewage Substances 0.000 description 5
- 238000003756 stirring Methods 0.000 description 4
- 230000000694 effects Effects 0.000 description 3
- 238000001914 filtration Methods 0.000 description 3
- 239000007789 gas Substances 0.000 description 3
- 239000000126 substance Substances 0.000 description 3
- 230000009471 action Effects 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 230000008569 process Effects 0.000 description 2
- 239000002699 waste material Substances 0.000 description 2
- 230000002776 aggregation Effects 0.000 description 1
- 238000004220 aggregation Methods 0.000 description 1
- 230000004075 alteration Effects 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 239000000701 coagulant Substances 0.000 description 1
- 238000003795 desorption Methods 0.000 description 1
- 230000002542 deteriorative effect Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000029087 digestion Effects 0.000 description 1
- 238000005189 flocculation Methods 0.000 description 1
- 230000016615 flocculation Effects 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 238000002347 injection Methods 0.000 description 1
- 239000007924 injection Substances 0.000 description 1
- 239000007791 liquid phase Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 244000005700 microbiome Species 0.000 description 1
- 230000001546 nitrifying effect Effects 0.000 description 1
- 239000012071 phase Substances 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 239000007790 solid phase Substances 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
Landscapes
- Treatment Of Sludge (AREA)
Abstract
Description
【0001】[0001]
【産業上の利用分野】本発明は汚泥処理に関し、特に送
泥管内の汚泥中の嫌気性最近の活性を抑制して汚泥の腐
敗を抑制する汚泥処理に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to sludge treatment, and more particularly to sludge treatment that suppresses anaerobic recent activity in sludge in a sludge pipe to suppress sludge decay.
【0002】[0002]
【従来の技術】従来、汚泥の処理は種々の分野で必要と
されている。例えば下水処理場においては下水処理量の
1%程度が発生汚泥量となっており、この汚泥処理は各
下水処理場ごとに単独に行うことが多い。2. Description of the Related Art Conventionally, sludge treatment has been required in various fields. For example, in a sewage treatment plant, the generated sludge amount is about 1% of the sewage treatment amount, and this sludge treatment is often performed independently for each sewage treatment plant.
【0003】一般に、大都市圏においては人口の集中等
の要因により複数の下水処理場が近接している場合が多
く、これら各下水処理場の発生汚泥を一か所に集中して
汚泥の集約処理を行うことにより汚泥処理時間を短縮
し、また汚泥処理コストを低くすることができる。Generally, in a metropolitan area, a plurality of sewage treatment plants are often close to each other due to factors such as population concentration, and sludge generated from each of these sewage treatment plants is concentrated in one place. By performing the treatment, the sludge treatment time can be shortened and the sludge treatment cost can be reduced.
【0004】汚泥の集約処理を行うには、各処理場にて
発生する汚泥を集中汚泥処理場に輸送する必要があり、
その輸送方法としてはトラック輸送、船舶輸送、パイプ
輸送問うが考えられる。[0004] In order to carry out the integrated treatment of sludge, it is necessary to transport the sludge generated in each treatment plant to the central sludge treatment plant,
The transportation methods include truck transportation, ship transportation, and pipe transportation.
【0005】上記輸送対象となる下水汚泥は、水処理系
の剰余汚泥、消化脱離液等が混合したものであり、特に
この下水汚泥のパイプ輸送を行う場合には、輸送中に下
水汚泥が腐敗及び変質するおそれがある。The above-mentioned sewage sludge to be transported is a mixture of surplus sludge of water treatment system, digestion and desorption liquid, etc. Especially, when the sewage sludge is transported by a pipe, the sewage sludge is transported during the transportation. There is a risk of decay and deterioration.
【0006】尚、上記輸送対象である下水汚泥は、水処
理系の余剰汚泥、硝化脱離液等の混合したものである。The sewage sludge to be transported is a mixture of excess sludge in the water treatment system, nitrifying and desorbing liquid, and the like.
【0007】また、下水汚泥が輸送されて処理にかけら
れるまでの時間は5〜24時間程度を要する場合が多
い。この汚泥の含水率は99%(汚泥1%、水99%)
程度である。[0007] Further, it often takes about 5 to 24 hours until the sewage sludge is transported and processed. The water content of this sludge is 99% (sludge 1%, water 99%)
It is a degree.
【0008】[0008]
【発明が解決しようとする課題】しかし、パイプ輸送等
により汚泥の集約処理を行う場合、輸送管(送泥管)内
は絶対嫌気状態となり、嫌気性微生物の繁殖等により下
水汚泥の腐敗の進行が早くなる。また、輸送管内の沈積
物等も下水汚泥の腐敗や変質を進める要因となる。However, when sludge is intensively processed by pipe transportation or the like, the inside of the transportation pipe (mud feeding pipe) is in an absolutely anaerobic state, and the deterioration of sewage sludge progresses due to the propagation of anaerobic microorganisms. Will be faster. In addition, deposits in the transportation pipes also contribute to the deterioration and alteration of sewage sludge.
【0009】このように下水汚泥の腐敗や変質が進む
と、集中汚泥処理場にて汚泥を処理する際に汚泥の沈降
性や脱水性が悪化し、汚泥集約後の汚泥処理を安定に行
うことが困難となる。このため、例えば脱水濾過速度が
30%程度低下し、また脱水用薬品消費量や脱水機台数
を増やすことが必要となる。When the sewage sludge is deteriorated or deteriorated in this way, the sludge settling property and dewatering property are deteriorated when the sludge is treated in the central sludge treatment plant, and the sludge treatment after the sludge aggregation is stably performed. Will be difficult. Therefore, for example, the dehydration filtration rate is reduced by about 30%, and it is necessary to increase the consumption amount of dehydration chemicals and the number of dehydrators.
【0010】更に、上記のように汚泥の腐敗が進むと、
濃縮、脱水等の汚泥処理工程において悪臭の発生量が増
加して作業環境が悪くなり、また脱臭装置の設置台数を
増やすことも必要となる。Further, as the sludge decays as described above,
In sludge treatment processes such as concentration and dehydration, the amount of offensive odors increases and the working environment deteriorates, and it is also necessary to increase the number of deodorizers installed.
【0011】本発明は上記背景のもとになされたもので
あり、汚泥の輸送中における腐敗や変質を防ぎ、汚泥処
理における処理効率の向上及びコストの低減化に寄与す
ることを目的とする。The present invention has been made based on the above background, and an object thereof is to prevent spoilage and deterioration during transportation of sludge, and to contribute to improvement of treatment efficiency in sludge treatment and reduction of cost.
【0012】[0012]
【課題を解決するための手段及び作用】上記課題を解決
するため、本発明は汚泥処理槽内にオゾンを供給し、汚
泥とオゾンとを接触反応させて汚泥の処理を行った後に
この汚泥を送泥管に輸送する汚泥処理方法を提供する。Means and Actions for Solving the Problems In order to solve the above problems, the present invention supplies ozone into a sludge treatment tank, treats sludge with ozone to cause a sludge treatment, and then treats the sludge. Provided is a sludge treatment method for transportation to a mud pipe.
【0013】また、汚泥処理槽と、前記汚泥処理槽内の
汚泥にオゾンを供給するオゾン供給手段と、オゾン処理
された汚泥を汚泥輸送管に輸送する汚泥輸送手段とを有
する汚泥処理装置も提供される。Also provided is a sludge treatment device having a sludge treatment tank, an ozone supply means for supplying ozone to the sludge in the sludge treatment tank, and a sludge transportation means for transporting the ozone-treated sludge to a sludge transportation pipe. To be done.
【0014】更に、上記汚泥処理装置において、上記処
理槽内にて発生する排オゾンを回収して再供給する排オ
ゾン循環供給手段を有する汚泥処理装置も提供される。Further, in the sludge treatment device, there is also provided a sludge treatment device having an exhaust ozone circulation supply means for collecting and re-supplying the exhaust ozone generated in the treatment tank.
【0015】通常、オゾンの供給は、オゾンガスを散気
したり、オゾンの溶解液を流入する等の方法によりなさ
れるが、本発明においてはその供給方法及び手段は特に
限定されず、気相、固相、液相、またはこれらの組み合
わせ等のいずれの状態にて供給を行うことができる。Usually, ozone is supplied by a method of diffusing ozone gas, flowing in a solution of ozone, or the like. In the present invention, the supplying method and means are not particularly limited, and the gas phase, The supply can be performed in any state such as a solid phase, a liquid phase, or a combination thereof.
【0016】また、汚泥輸送手段としては例えばポンプ
等が挙げられるが、特に輸送手段を限定する必要はな
い。排オゾン循環供給手段としてはブロアー等を用いる
ことができるが、特に排オゾン循環供給手段は限定され
ない。The sludge transportation means may be a pump or the like, but the transportation means is not particularly limited. A blower or the like can be used as the exhaust ozone circulation supply means, but the exhaust ozone circulation supply means is not particularly limited.
【0017】排オゾン循環供給手段により排オゾンを回
収して再供給を行う事により、オゾン処理を効率的に行
うことができる。従って、使用オゾン量、排オゾン量と
もに減少するので経済的にも有利である。By collecting the exhaust ozone by the exhaust ozone circulation supply means and supplying it again, the ozone treatment can be efficiently performed. Therefore, both the amount of ozone used and the amount of exhausted ozone are reduced, which is economically advantageous.
【0018】上記のようにオゾンと汚泥とを接触反応さ
せることにより、嫌気性細菌等が殺菌され、悪臭の除去
作用も得られる。また、溶存酸素も増えるので汚泥腐敗
の進行を抑制することができる。従って、汚泥の輸送中
における汚泥の腐敗が抑制される。By contacting ozone with sludge as described above, anaerobic bacteria and the like are sterilized, and a bad odor removing action is also obtained. Further, since the dissolved oxygen also increases, the progress of sludge decay can be suppressed. Therefore, decay of sludge during transportation of sludge is suppressed.
【0019】更に、汚泥の凝縮性も向上するので輸送後
に汚泥の沈澱処理を迅速に行うことができる。Further, since the sludge condensability is also improved, the sludge settling treatment can be carried out quickly after transportation.
【0020】[0020]
【実施例】本実施例においては図1に示す汚泥処理装置
を用いて汚泥にオゾン及びオゾン水を供給し、汚泥とオ
ゾンとを接触させることにより汚泥の腐敗や変質を抑制
した。EXAMPLE In this example, ozone and ozone water were supplied to the sludge by using the sludge treatment device shown in FIG. 1, and the sludge was brought into contact with ozone to suppress spoilage and deterioration.
【0021】図1において1は送泥管2を通じて接触反
応槽3に汚泥を供給する送泥ポンプ、4はオゾン処理さ
れた汚泥を送泥管8に送り込む送泥ポンプである。In FIG. 1, reference numeral 1 denotes a sludge pump for supplying sludge to the contact reaction tank 3 through the sludge pipe 2, and reference numeral 4 denotes a sludge pump for feeding the ozone-treated sludge to the sludge pipe 8.
【0022】5は排オゾンを循環させて散気管6を通じ
て接触反応槽3に再供給する排オゾン循環ブロアー、7
は接触反応槽3内の汚泥を撹拌してオゾンと汚泥との接
触反応を促進させる撹拌モーター、9は排オゾンの処理
を行う排オゾン処理塔である。Reference numeral 5 is an exhaust ozone circulating blower for circulating exhaust ozone and re-supplying it to the contact reaction tank 3 through the air diffuser 6, 7
Is a stirring motor that stirs the sludge in the contact reaction tank 3 to promote the contact reaction between ozone and sludge, and 9 is an exhaust ozone treatment tower that processes the exhaust ozone.
【0023】上記装置によりオゾン処理された汚泥は送
泥管8を通じて汚泥処理センター等に輸送される。The sludge treated with ozone by the above apparatus is transported to a sludge treatment center or the like through the sludge pipe 8.
【0024】尚、接触反応槽3に代えて受泥槽を用いて
もよい。A mud receiving tank may be used instead of the contact reaction tank 3.
【0025】上記装置により汚泥とオゾンとを接触反応
させて輸送を行ったところ、汚泥中の嫌気性菌等が殺菌
されて輸送中における汚泥の腐敗や変質が抑制されると
ともに、悪臭の除去効果も得られた。When the sludge and ozone are brought into contact with each other by the above-mentioned apparatus to carry out the transportation, the anaerobic bacteria in the sludge are sterilized to prevent the sludge from spoiling and deteriorating during the transportation, and the odor is removed. Also got.
【0026】更に、オゾン及びオゾン水を撹拌モーター
7により均一に緩連撹拌するとともに排オゾン循環ブロ
アーにて循環バッ気を与えているのでオゾン処理効果が
増大している。Further, since ozone and ozone water are uniformly and slowly stirred by the stirring motor 7 and the circulation bag is provided by the exhaust ozone circulation blower, the ozone treatment effect is increased.
【0027】また、汚泥の凝集性も向上するので、脱水
用凝集沈降剤の薬品投入量を低くなり、脱水濾過速度も
短縮された。Further, since the sludge flocculation property is also improved, the amount of the flocculation-precipitating agent for dehydration introduced into the chemical is reduced, and the dehydration filtration rate is also shortened.
【0028】[0028]
【発明の効果】本発明においては、オゾン(オゾンガス
やオゾン水等)と汚泥の接触反応効果により悪臭が除去
される。また嫌気性細菌が殺菌されるとともに溶存酸素
も増加するので汚泥の腐敗を抑制することができる。従
って、輸送された汚泥の沈降性(濃縮性)も向上する。INDUSTRIAL APPLICABILITY In the present invention, the bad odor is removed by the contact reaction effect of ozone (ozone gas, ozone water, etc.) and sludge. In addition, anaerobic bacteria are sterilized and dissolved oxygen increases, so that spoilage can be suppressed. Therefore, the sedimentation property (concentration property) of the transported sludge is also improved.
【0029】また、汚泥の凝縮性が向上するので、脱水
用凝集剤等の薬品投入量を減らすことができ、脱水濾過
速度も短縮することができる。更にオゾン処理前から含
まれている悪臭もオゾン処理により除去することができ
る。Further, since the sludge condensability is improved, the amount of chemicals such as a coagulant for dewatering can be reduced, and the dewatering filtration rate can be shortened. Further, the odor contained before the ozone treatment can be removed by the ozone treatment.
【図1】本発明の一実施例に係る汚泥処理装置の説明図FIG. 1 is an explanatory diagram of a sludge treatment device according to an embodiment of the present invention.
1…1は送泥管2を通じて接触反応槽3に汚泥を供給す
る送泥ポンプ、4はオゾン処理された汚泥を送泥管8に
送り込む送泥ポンプである。5は排オゾンを循環させて
散気管6を通じて接触反応槽3に再供給する排オゾン循
環ブロアー、7は接触反応槽3内の汚泥を撹拌してオゾ
ンと汚泥との接触反応を促進させる撹拌モーター、9は
排オゾンの処理を行う排オゾン処理塔であるブロアー 2…オゾン発生装置 3…オゾン含有水製造装置 4…オゾン分解装置 5…注入ポンプ 7…汚泥圧送管Reference numeral 1 denotes a sludge pump for supplying sludge to the contact reaction tank 3 through the sludge pipe 2, and 4 denotes a sludge pump for feeding the ozone-treated sludge to the sludge pipe 8. Reference numeral 5 is an exhaust ozone circulation blower that circulates the exhaust ozone and re-supplies it to the contact reaction tank 3 through the air diffuser 6, and 7 is a stirring motor that agitates the sludge in the contact reaction tank 3 to accelerate the contact reaction between ozone and sludge. , 9 is a blower which is a waste ozone treatment tower for treating waste ozone 2 ... Ozone generator 3 ... Ozone-containing water production device 4 ... Ozone decomposition device 5 ... Injection pump 7 ... Sludge pressure feed pipe
Claims (3)
オゾンとを接触反応させて汚泥の処理を行った後にこの
汚泥を送泥管に輸送する汚泥処理方法。1. A sludge treatment method in which ozone is supplied into a sludge treatment tank, sludge and ozone are brought into contact with each other to treat sludge, and then the sludge is transported to a sludge pipe.
にオゾンを供給するオゾン供給手段と、オゾン処理され
た汚泥を汚泥輸送管に輸送する汚泥輸送手段とを有する
汚泥処理装置。2. A sludge treatment device having a sludge treatment tank, an ozone supply means for supplying ozone to the sludge in the sludge treatment tank, and a sludge transportation means for transporting the ozone-treated sludge to a sludge transportation pipe.
る排オゾン循環供給手段を有することを特徴とする汚泥
処理装置。3. The sludge treatment device according to claim 2, further comprising an exhaust ozone circulation supply unit that recovers and resupposes exhaust ozone generated in the treatment tank.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP31546692A JPH06154796A (en) | 1992-11-26 | 1992-11-26 | Method and equipment for sludge treatment |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP31546692A JPH06154796A (en) | 1992-11-26 | 1992-11-26 | Method and equipment for sludge treatment |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH06154796A true JPH06154796A (en) | 1994-06-03 |
Family
ID=18065703
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP31546692A Pending JPH06154796A (en) | 1992-11-26 | 1992-11-26 | Method and equipment for sludge treatment |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH06154796A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR100413593B1 (en) * | 2001-06-11 | 2003-12-31 | 금호산업주식회사 | System and Process for Ozone-Enhanced Reduction and Recycling of Wastewater Sludge |
CN102583936A (en) * | 2012-02-02 | 2012-07-18 | 重庆大学 | Air lift type internal-external double circulation ozone sludge contact reaction device |
-
1992
- 1992-11-26 JP JP31546692A patent/JPH06154796A/en active Pending
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR100413593B1 (en) * | 2001-06-11 | 2003-12-31 | 금호산업주식회사 | System and Process for Ozone-Enhanced Reduction and Recycling of Wastewater Sludge |
CN102583936A (en) * | 2012-02-02 | 2012-07-18 | 重庆大学 | Air lift type internal-external double circulation ozone sludge contact reaction device |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
RU2148032C1 (en) | Method and apparatus for biological destruction of injurious impurities in water | |
JPH0255120B2 (en) | ||
JPH09314156A (en) | Ozone treatment apparatus in which biological filter device is incorporated | |
KR101208683B1 (en) | Water Re-Cycling System and method thereof | |
JP3788716B2 (en) | Organic wastewater treatment method and treatment apparatus | |
KR101053132B1 (en) | Hospital discharge infectious wastewater treatment and sterilization air conditioning system | |
JPH06154796A (en) | Method and equipment for sludge treatment | |
KR100435107B1 (en) | Advance Treatment Equipment and Process for Nitrogen and Phosphate Removal in Sewage and Wastewater | |
JP3380002B2 (en) | Sewage treatment method | |
JP3558204B2 (en) | Wastewater biological treatment equipment | |
JP2000117289A (en) | Treatment of dehydration-separated liquid from anaerobic-digested sludge and equipment therefor | |
JPH0686999A (en) | Method and device for transporting sludge | |
JPH02222798A (en) | Pretreatment of sludge | |
JP2002059200A (en) | Wastewater and sludge treatment methods | |
JPH10277584A (en) | Single tank sewage treatment method and apparatus therefor | |
JP3832888B2 (en) | Purification device operation method | |
JP2001149980A (en) | Wastewater and sludge treatment methods | |
JP2001149981A (en) | Wastewater and sludge treatment methods | |
JPH10192897A (en) | Sludge treating method | |
JP2003159595A (en) | Method for treating organic liquid utilizing ozone gas and apparatus therefor | |
JP3392295B2 (en) | Method and apparatus for treating organic sewage | |
JP2001047098A (en) | Wastewater and sludge treatment methods | |
JPH0796286A (en) | High-degree treatment of organic sewage | |
JPH03135418A (en) | Exhaust ozone treatment device | |
JP3340790B2 (en) | Wastewater treatment method |