JPH0767558B2 - Sewage treatment method - Google Patents
Sewage treatment methodInfo
- Publication number
- JPH0767558B2 JPH0767558B2 JP5075187A JP7518793A JPH0767558B2 JP H0767558 B2 JPH0767558 B2 JP H0767558B2 JP 5075187 A JP5075187 A JP 5075187A JP 7518793 A JP7518793 A JP 7518793A JP H0767558 B2 JPH0767558 B2 JP H0767558B2
- Authority
- JP
- Japan
- Prior art keywords
- iron
- filter medium
- treatment
- sewage treatment
- elution
- 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
Links
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W10/00—Technologies for wastewater treatment
- Y02W10/10—Biological treatment of water, waste water, or sewage
Landscapes
- Biological Treatment Of Waste Water (AREA)
- Purification Treatments By Anaerobic Or Anaerobic And Aerobic Bacteria Or Animals (AREA)
Description
【0001】[0001]
【産業上の利用分野】この発明は接触濾材として鉄濾材
を充填した汚水処理装置を用いた汚水処理方法に係り、
特に処理中に鉄濾材からの鉄イオンの溶出を長期に亘っ
て可能ならしめ、汚水中の有機成分とともにリン分をも
同時に除去するようにした汚水処理方法に関するもので
ある。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a sewage treatment method using a sewage treatment device filled with an iron filter medium as a contact filter medium ,
In particular, the present invention relates to a sewage treatment method that enables elution of iron ions from an iron filter medium during treatment for a long period of time and simultaneously removes phosphorus as well as organic components in sewage.
【0002】[0002]
【従来の技術】汚水中に鉄材を浸漬すると、鉄イオンが
溶出することは、古くから知られているが、この鉄材表
面に鉄イオンと結合してできた生成物および生物膜類や
塵埃などが付着するために、経年と共に鉄材表面からの
鉄イオンの溶出が自然に減少していくということも知ら
れている。It has been known for a long time that iron ions will be eluted when iron material is immersed in waste water. Products formed by binding iron ions to the surface of the iron material, biofilms, dust, etc. It is also known that the elution of iron ions from the surface of the iron material naturally decreases with the lapse of time due to the adhesion of iron.
【0003】産業排水や生活雑排水などの汚水処理にお
いて、鉄材を接触濾材とした汚水処理装置を用い、この
鉄濾材の表面から鉄イオンを溶出させて、この鉄イオン
と汚水中の有機リンの分解によるリン酸イオンを結合さ
せ、不溶性のリン酸鉄塩を生成させることによって、汚
水中のリン分を除去する方法が提案されている(特開昭
61−90792号公報、特開昭61−178092号
公報)。In the treatment of wastewater such as industrial wastewater and household wastewater, a sewage treatment apparatus using an iron material as a contact filter medium is used to elute iron ions from the surface of the iron filter medium to remove the iron ions and the organic phosphorus in the wastewater. There has been proposed a method for removing the phosphorus content in wastewater by binding phosphate ions by decomposition to produce an insoluble iron phosphate salt (Japanese Patent Laid-Open No. 61-90792, Japanese Patent Laid-Open No. 61-90792). 178092).
【0004】[0004]
【発明が解決しようとする課題】しかしながら、本発明
者らが行った鉄濾材を用いた接触曝気法による汚水処理
によると、処理の継続に伴い処理槽内の鉄濾材表面にリ
ン酸鉄などの皮膜が生成してリン除去率は低下すること
が判った。また、間欠曝気法による汚水処理でも処理槽
内に鉄濾材を浸漬後、日を経るに従ってリン除去率が低
下し、かつ不規則になる傾向が見られる。さらに、鉄製
回転円板法においても長期間の処理を続けると、鉄製円
板の表面にリン酸鉄塩の皮膜が形成されてリン除去率の
低下が認められる。However, according to the sewage treatment by the contact aeration method using the iron filter medium carried out by the present inventors, as the treatment is continued, the surface of the iron filter medium in the treatment tank is treated with iron phosphate or the like. It was found that a film was formed and the phosphorus removal rate was reduced. Further, even in the sewage treatment by the intermittent aeration method, the phosphorus removal rate tends to decrease and become irregular with the passage of time after the iron filter medium is immersed in the treatment tank. Further, even in the iron rotating disk method, if the treatment is continued for a long time, a film of iron phosphate is formed on the surface of the iron disk, and the phosphorus removal rate is reduced.
【0005】また、鉄濾材を使用する嫌気的汚水処理法
の場合、処理時間の経過に伴って硫酸塩還元バクテリア
の存在によって生成する硫化鉄類が鉄濾材表面に鉄腐食
防蝕皮膜としてリン酸鉄や塵埃とともに付着してくる。
ところが、この硫化鉄皮膜は緻密で強固であり、鉄イオ
ン溶出量を減じる鉄イオン溶出妨害生成物である。この
鉄イオン溶出妨害生成物については、本出願人が先に提
案した、汚水との接触表面積が非常に大きい鋳鉄製の中
空状の汚水処理用濾材(実公平2−2476号)を用い
た実験において、嫌気槽にこの濾材を浸漬して汚水処理
を行い、濾材浸漬5ケ月後および11ケ月後に濾材表面
の付着物を分析したところ、硫化物が5ケ月後の表面で
は4.61%であったものが、11ケ月後では13.4
7%と非常に高い数値を示し、濾材表面からの鉄イオン
の溶出に大きな影響を及ぼしていることが認められた。Further, in the case of the anaerobic sewage treatment method using an iron filter medium, iron sulfides produced by the presence of sulfate-reducing bacteria as the treatment time elapses, and iron phosphate as an iron anticorrosion coating on the iron filter medium surface. It adheres along with dust.
However, this iron sulfide coating is a dense and strong iron sulfide elution-preventing product that reduces the elution amount of iron ions. This iron ion elution-prevented product was tested by using the hollow sewage treatment filter made of cast iron (Jukei hei 2-2476) proposed by the present applicant and having a very large contact surface area with sewage. In the above, the filter medium was immersed in an anaerobic tank for sewage treatment, and the deposits on the surface of the filter medium were analyzed 5 months and 11 months after the filter medium had been dipped. Sulfide was 4.61% on the surface after 5 months. It was 13.4 after 11 months.
It showed a very high value of 7%, and it was recognized that it had a great influence on the elution of iron ions from the surface of the filter medium.
【0006】このように、鉄濾材を用いた汚水処理にお
いては、好気的条件下あるいは嫌気的条件下のいずれで
あっても、処理時間が経過するにつれて鉄濾材表面にリ
ン酸鉄塩類等および生物膜類や塵埃あるいは硫酸塩還元
バクテリアの存在に係る硫化鉄類皮膜などの鉄イオン溶
出妨害生成物が発生付着したりして汚水中の鉄イオン溶
出量が減少するために、鉄イオンが汚水中のリン酸イオ
ンと結合してリン分を除去する脱燐作用の低下が認めら
れ、これが鉄濾材を用いる汚水処理方法の大きな問題点
とされている。しかしながら、鉄イオンの溶出を有効か
つ経済的に長期に持続させる方法については、未だ解明
されていない。As described above, in the treatment of sewage using an iron filter medium, iron phosphates and the like are formed on the surface of the iron filter medium as the treatment time elapses under either aerobic or anaerobic conditions. Iron ion elution is reduced because the amount of iron ion elution disturbing products such as iron sulfide film related to the presence of biofilms, dust, or sulfate-reducing bacteria decreases. A reduction in the dephosphorization effect of removing the phosphorus content by binding with the phosphate ion in the inside is recognized, and this is a major problem of the wastewater treatment method using the iron filter medium. However, a method for effectively and economically sustaining the elution of iron ions for a long time has not yet been clarified.
【0007】本発明者らは、鉄濾材を接触濾材として用
いる汚水の処理における上記したような問題点を解消し
て、長期に亘って安定した鉄イオンの溶出を可能にし、
これによって汚水中の有機成分とともにリンを同時に、
しかも持続して除去することのできる汚水処理方法を見
出すに至ったものである。The present inventors have solved the above-mentioned problems in the treatment of sewage using an iron filter medium as a contact filter medium, and made it possible to stably elute iron ions over a long period of time.
As a result, phosphorus is simultaneously added to the organic components in the wastewater,
Moreover, they have come to find a sewage treatment method that can be continuously removed.
【0008】[0008]
【課題を解決するための手段】即ち、この発明の第1の
発明は接触濾材として鉄濾材を用いた汚水処理装置で汚
水処理を行うに当たって、処理途中で上記鉄濾材を処理
装置から引き上げて大気曝露し、濾材表面に付着した鉄
イオン溶出妨害生成物を酸化分解して鉄濾材からの鉄イ
オンの溶出を持続させることを特徴とする汚水処理方法
であり、第2の発明は処理途中で上記鉄濾材を振動させ
て濾材表面に付着したリン酸鉄塩類等および生物膜類や
塵埃を離脱させるとともに、上記鉄濾材を処理装置から
引き上げて大気曝露を併せて行い、鉄濾材表面に付着し
た鉄イオン溶出妨害生成物を酸化分解して鉄濾材からの
鉄イオンの溶出を持続させることを特徴とする汚水処理
方法である。 That is, according to the first aspect of the present invention, when performing sewage treatment in a sewage treatment apparatus using an iron filter medium as a contact filter medium, the iron filter medium is treated during the treatment.
Iron picked up from the device and exposed to the atmosphere
The iron elution from the iron filter material is decomposed by oxidative decomposition of the ion elution disturbing product
Wastewater treatment method characterized by sustaining the elution of ON
According to the second invention, the iron filter medium is vibrated during the treatment.
Iron phosphates and biofilms attached to the surface of the filter media
Remove the dust and remove the iron filter material from the processor.
It was pulled up and exposed to the atmosphere at the same time, and it adhered to the iron filter medium surface.
From the iron filter media by oxidative decomposition of
Sewage treatment characterized by continuous elution of iron ions
Is the way.
【0009】[0009]
【作用】この発明は上記のように、汚水処理装置に接触
濾材として用いている鉄濾材が汚水処理の途中で硫化鉄
のような鉄イオン溶出妨害生成物が表面に付着して鉄イ
オンの溶出量が減少するので、この鉄濾材を処理装置か
ら引き上げ、大気に適宜の時間触れさせることによっ
て、酸化雰囲気での酸化分解で硫化鉄膜に多数の亀裂を
発生させ、鉄イオンの溶出量を回復させることができる
のであり、また鉄濾材表面に付着した鉄イオンと汚水中
のリン酸イオンの結合により生じたリン酸鉄塩を脱離さ
せるため、及びそれらの離脱により硫化鉄膜と大気との
接触性がよくなり、効率的な酸化作用を生ぜしめるため
に、鉄濾材に振動を与えることにより、減少しつつあっ
た鉄濾材からの鉄イオンの溶出量を増大させることがで
きる。 As described above, the present invention makes contact with the sewage treatment apparatus.
The iron filter medium used as a filter medium is iron sulfide during the treatment of sewage.
Products that interfere with the elution of iron ions, such as
Since the elution amount of ON is reduced, this iron filter medium is
By exposing it to the atmosphere for a suitable time.
A large number of cracks in the iron sulfide film due to oxidative decomposition in an oxidizing atmosphere.
Can be generated to recover the elution amount of iron ions
In addition, iron ions adhering to the surface of the iron filter medium and wastewater
The iron phosphate formed by the binding of phosphate ion
In order to make the iron sulfide film and its detachment,
For better contact and efficient oxidation
, It is decreasing by applying vibration to the iron filter media.
It is possible to increase the elution amount of iron ions from the iron filter media.
Wear.
【0010】この硫化鉄の生成は表面が黒褐色を呈する
ことで判定できるが、数滴の塩酸の滴下で硫化水素臭を
出すことからも判定できる。この硫化鉄膜は、生成から
3か月以上経ると、水洗やブラッシングなどでは除去で
きないほど強固であり、従ってこのような場合の酸化分
解はただ大気に触れさせるだけでなく、強制的な送風を
行うことが好ましい。この送風は処理装置から引き上げ
た硫化鉄膜などが付着している鉄濾材に常温風を吹きつ
けることで行われるが、付着物が特に強固と考えられる
ときは40〜60℃程度の温風とすればよく、これによ
って吹きつけ時間を1/10以下に短縮することが可能
であるので、状況に応じて選択すればよい。The formation of this iron sulfide can be judged by the fact that the surface exhibits a blackish brown color, but it can also be judged by the fact that hydrogen sulfide odor is produced by the addition of a few drops of hydrochloric acid. This iron sulfide film is so strong that it cannot be removed by washing with water or brushing after three months have passed since its formation. Therefore, the oxidative decomposition in such a case is not only exposed to the atmosphere but also forced blast. It is preferable to carry out. The air is blown by blowing normal temperature air onto the iron filter medium to which the iron sulfide film or the like pulled up from the processing device is attached. Since it is possible to shorten the spraying time to 1/10 or less by this, it is possible to select it according to the situation.
【0011】この発明において使用する鉄濾材ユニット
の構成の一例について説明すると、図1に示すように、
鉄濾材ユニットAは、例えば鋼板(SS41)1を10
枚所要間隔に上下の塩化ビニルパイプ2、2で締結し、
その上部に振動機3を設置した取り付け板4を鋼板1の
上端に接するようにして上側の塩化ビニルパイプ2に取
り付けたものであり、これを嫌気槽にセットして用いら
れる。なお、5はSUS304などを用いた振動伝達部
であり、6はこの鉄濾材ユニットの脚部である。An example of the structure of the iron filter medium unit used in the present invention will be described. As shown in FIG.
The iron filter medium unit A includes, for example, a steel plate (SS41) 1 of 10
Fasten with the upper and lower vinyl chloride pipes 2 and 2 at the required space,
A mounting plate 4 having a vibrator 3 installed thereon is attached to the upper vinyl chloride pipe 2 so as to be in contact with the upper end of the steel plate 1, and this is set in an anaerobic tank for use. In addition, 5 is a vibration transmission part using SUS304 etc., 6 is a leg part of this iron filter medium unit.
【0012】[0012]
【実施例】以下、この発明を参考例および実施例により
詳細に説明する。参考例 認定5人型小型合併槽を用い、これに生活雑排水(原
水)を1.0m3/日で供給し、嫌気室として使用する
分離室に振動機を具えた鉄濾材ユニットを浸漬し、処理
水中のリン含有量が1.0mg/l以下となるように目
標を定めて処理を行った。その結果は表1に示した。な
お、表1におけるテスト日は処理開始日からの月数であ
る。The present invention will be described in detail below with reference to examples and examples . Reference example Using a certified 5 person type small combined tank, domestic wastewater (raw water) is supplied to this at 1.0 m 3 / day, and an iron filter medium unit equipped with a vibrator is immersed in the separation chamber used as an anaerobic chamber. The treatment was performed by setting a target so that the phosphorus content in the treated water was 1.0 mg / l or less. The results are shown in Table 1. The test date in Table 1 is the number of months from the process start date.
【0013】[0013]
【表1】 [Table 1]
【0014】上記参考例では、汚水処理開始2ケ月後、
3ケ月後においては鉄濾材ユニットを設置した嫌気室の
鉄分含有量が多いので、処理水中のリン含有量も低く脱
リン率も80%を超えて良好であり、その後数値は割愛
したが、順調に処理が進行した。そして、13ケ月後の
測定において、嫌気室の鉄分含有量が1.40mg/l
と低下し、処理水中のリン含有量が0.81mg/lと
上昇したため脱リン率が76%と低下した。この低下は
鉄濾材表面へのリン酸鉄塩や塵埃の付着量が増加して鉄
濾材からの鉄イオンの溶出量が減少していることを示し
ている。そこで、鉄濾材上に設置されている振動機を作
動して1時間鉄濾材に振幅10ミクロン以上の振動を与
えて鉄濾材表面の付着物を除去した。そして、振動付与
の半月後(処理開始から13ケ月半後)の測定で嫌気室
の鉄分含有量は3.68mg/lと上昇し、処理水中の
リン含有量0.61mg/l、脱リン率82.1%と向
上し、その後4ケ月間順調に処理が行われたが、18ケ
月後の測定で表1のように脱リン率が72.4%と低下
が見られた。このため、再度上記と同様にして2時間振
動を与えて付着物を除去したところ、除去後半月(処理
開始から18ケ月半)の処理を行った後でも嫌気室の鉄
分含有量3.26mg/l、脱リン率80%と正常であ
った。In the above reference example , two months after the start of sewage treatment,
After 3 months, the iron content in the anaerobic chamber where the iron filter medium unit was installed was high, so the phosphorus content in the treated water was low and the dephosphorization rate was over 80%, which was good. Processing proceeded. And, in the measurement after 13 months, the iron content in the anaerobic chamber was 1.40 mg / l.
And the phosphorus content in the treated water increased to 0.81 mg / l, the dephosphorization rate decreased to 76%. This decrease indicates that the amount of iron phosphate and dust adhering to the surface of the iron filter medium is increasing and the amount of iron ions eluted from the iron filter medium is decreasing. Then, the vibrating machine installed on the iron filter medium was operated and the iron filter medium was vibrated with an amplitude of 10 microns or more for 1 hour to remove the deposits on the surface of the iron filter medium. The iron content in the anaerobic chamber increased to 3.68 mg / l in the measurement half a month after the vibration was given (13 and a half months after the treatment was started), and the phosphorus content in the treated water was 0.61 mg / l and the dephosphorization was performed. The rate was improved to 82.1 %, and the treatment was successfully performed for four months thereafter, but the dephosphorization rate was decreased to 72.4% as shown in Table 1 after 18 months. For this reason, when the adhered matter was removed again by applying vibration for 2 hours in the same manner as above, the iron content in the anaerobic chamber was 3.26 mg / even after the treatment in the second half of the removal (18 months and a half from the start of treatment). 1, the dephosphorization rate was 80%, which was normal.
【0015】上記のように、鉄濾材からの鉄イオンの溶
出量が減少して脱リン率の低下があった場合に、振動機
にて鉄濾材に振動を付与することにより、鉄イオンの溶
出量が回復し、汚水処理を順調に進められることが判っ
た。なお、振動機による振動付与時間は、少なくとも1
時間は要するが、直前の測定による鉄イオンの溶出量お
よび脱リン率によって適宜決定すればよい。As described above, when the amount of iron ions eluted from the iron filter medium is reduced and the dephosphorization rate is reduced, the iron filter medium is vibrated by a vibrator to elute the iron ions. It was found that the amount recovered and the sewage treatment proceeded smoothly. In addition, the vibration application time by the vibrator is at least 1
Although it takes time, it may be appropriately determined depending on the elution amount of iron ions and the dephosphorization rate measured immediately before.
【0016】実施例 嫌気槽が2室、接触曝気槽が3室、および沈殿槽からな
る1.5m3/日の処理水を処理できる生活雑排水処理
モデル装置を用いて、嫌気槽の2室ともに実施例1とは
異なり、振動機を設置していない鉄濾材を充填し、汚水
処理を行った。その結果は表2に示した。なお、表2に
おけるテスト日とは嫌気槽に鉄濾材を充填して汚水処理
を開始した日からの通算日数を示す。 Example : An anaerobic tank is used for two chambers, a contact aeration tank is for three chambers, and a settling tank is used for treating 1.5 m 3 / day of treated water. Different from Example 1, both were filled with an iron filter medium without a vibrator and treated for sewage. The results are shown in Table 2. The test date in Table 2 indicates the total number of days from the day when the iron filter medium was filled in the anaerobic tank and the sewage treatment was started.
【0017】[0017]
【表2】 [Table 2]
【0018】上記の実施例においては、処理を開始して
から初期には処理水中のリン含有量は1.0mg/l以
下で、脱リン率も80%以上と良好に処理が行われた。
しかし、16ケ月後の測定ではリン含有量は1.62m
g/lと上昇し、脱リン率が65.2%と低下した。こ
の時の鉄濾材からの鉄イオンの溶出量を測定したとこ
ろ、嫌気槽第1室では1.54mg/l、第2室では
2.04mg/lと低下していた。In the above-mentioned examples , the treatment was carried out satisfactorily with the phosphorus content in the treated water being 1.0 mg / l or less and the dephosphorization rate being 80% or more from the beginning of the treatment.
However, the phosphorus content was 1.62 m when measured after 16 months.
It increased to g / l and the dephosphorization rate decreased to 65.2%. When the elution amount of iron ions from the iron filter medium at this time was measured, it decreased to 1.54 mg / l in the first chamber of the anaerobic tank and 2.04 mg / l in the second chamber.
【0019】そこで、汚水処理を中断して、第1室、第
2室の鉄濾材を処理槽から引き上げ、第1室の鉄濾材は
12時間、第2室の鉄濾材は48時間の大気曝露を行っ
た。その後、鉄濾材を夫々の嫌気槽に戻し、汚水処理を
続行した。そして、1ケ月後、4ケ月後(通算17ケ月
後、20ケ月後)の測定では脱リン率は良好であった。
ところが、21ケ月後には再び脱リン率の低下が測定さ
れたので、鉄濾材を引き上げ、第1室の鉄濾材は12時
間、第2室の鉄濾材は24時間、常温風の送風を伴う大
気曝露を行った。そして、鉄濾材を夫々の嫌気槽に戻し
て汚水処理を続行し、1ケ月後(通算22ケ月後)に測
定したところ、嫌気槽中の鉄イオン溶出量は、第1室で
4.91mg/l、第2室では7.68mg/lで、処
理水中のリン含有量は0.60mg/lであり、脱リン
率は83.4%と良好であった。Therefore, the wastewater treatment is interrupted, and the iron filter media in the first and second chambers are pulled out of the treatment tank. The iron filter media in the first chamber is exposed to the atmosphere for 12 hours and the iron filter media in the second chamber is exposed to the atmosphere for 48 hours. I went. After that, the iron filter media were returned to the respective anaerobic tanks, and the sewage treatment was continued. Then, the dephosphorization rate was good in the measurement after one month and four months (17 months and 20 months in total).
However, after 21 months, the decrease in the dephosphorization rate was measured again, so the iron filter medium was pulled up, the iron filter medium in the first chamber was for 12 hours, the iron filter medium in the second chamber was for 24 hours, and the ambient air was blown. Exposed. Then, the iron filter media were returned to the respective anaerobic tanks, the sewage treatment was continued, and the measurements were made one month later (22 months after the total). As a result, the iron ion elution amount in the anaerobic tank was 4.91 mg / in the first chamber. 1, the second chamber had 7.68 mg / l, the phosphorus content in the treated water was 0.60 mg / l, and the dephosphorization rate was 83.4%, which was good.
【0020】このように、大気曝露を行うことにより、
鉄濾材からの鉄イオンの溶出を妨害している鉄濾材表面
に付着した硫化鉄膜を酸化反応によって結晶化させ、膜
の緻密性を破壊して割れを発生させて、鉄濾材表面の鉄
イオン溶出面積を復活させることができるのである。こ
の大気曝露は、参考例と同じように振動機を上部にセッ
トした鉄濾材を用いて、振動付与による鉄濾材表面のリ
ン酸鉄塩類等および生物膜類や塵埃の除去に引き続いて
実施することにより、あるいは大気曝露中に、または大
気曝露終了後嫌気槽に戻した後に振動機を運転すること
により、鉄濾材表面のリン酸鉄塩や塵埃とともに硫化鉄
の処理もでき、汚水処理を持続してより効果的に行うこ
とができる。By thus exposing to the atmosphere,
The iron sulfide film adhering to the surface of the iron filter media that interferes with the elution of iron ions from the iron filter media is crystallized by an oxidation reaction, destroying the denseness of the film and causing cracks, and the iron ions on the iron filter media surface. The elution area can be restored. This atmospheric exposure should be performed following the removal of iron phosphates, etc., biofilms and dust on the surface of the iron filter medium by applying vibration, using the iron filter medium with the vibrator set above as in the reference example. By operating the vibrator either during exposure to the atmosphere or after returning to the anaerobic tank after exposure to the atmosphere, iron sulfide can be treated along with iron phosphate and dust on the surface of the iron filter medium, and sewage treatment can be continued. Can be done more effectively.
【0021】[0021]
【発明の効果】以上説明したように、この発明は嫌気槽
に接触濾材として鉄濾材を用いる汚水処理において、処
理の経過につれて表面にリン酸鉄塩や塵埃、さらには硫
化鉄のような鉄イオン溶出妨害生成物が付着して鉄イオ
ンの溶出量が減少し、脱リン率の低下した鉄濾材を槽か
ら引き上げて大気曝露することによって、あるいはこの
大気曝露の前後または大気曝露と同時に、鉄濾材上部に
接するように設けた振動機にて鉄濾材に振動を付与する
ことによって、鉄イオンの溶出量を回復せしめて脱リン
率を向上させることができるものであり、実用的効果の
大きいことが認められた。As described in the foregoing, the present invention is in a sewage treatment with iron filter medium as a contact medium in the anaerobic tank, punished
As the process progresses, iron phosphate, dust, and
Iron-ion elution-preventing products such as iron oxide adhere to
If the iron filter media with reduced dephosphorization rate was
Or by exposing it to the atmosphere
Before and after or at the same time as exposure to the atmosphere
Vibration is applied to the iron filter media with the vibrator installed in contact with it.
As a result, it was possible to recover the elution amount of iron ions and improve the dephosphorization rate, and it was confirmed that the practical effect is great.
【図1】この発明で用いる鉄濾材ユニットの構成の一例
を示す説明図である。FIG. 1 is an explanatory diagram showing an example of a configuration of an iron filter medium unit used in the present invention.
A 鉄濾材ユニット 1 鋼板 2 塩化ビニルパイプ 3 振動機 4 取り付け板 5 振動伝達部 6 脚部 A Iron filter medium unit 1 Steel plate 2 Vinyl chloride pipe 3 Vibrator 4 Mounting plate 5 Vibration transmission part 6 Legs
Claims (3)
装置にて汚水処理を行うに当たり、処理途中で上記鉄濾
材を処理装置から引き上げて大気曝露し、濾材表面に付
着した鉄イオン溶出妨害生成物を酸化分解して鉄濾材か
らの鉄イオンの溶出を持続させることを特徴とする汚水
処理方法。 1. A sewage treatment using an iron filter medium as a contact filter medium.
During the treatment of sewage with the equipment, the iron filter
The material is pulled up from the processing equipment, exposed to the atmosphere, and attached to the surface of the filter media.
The iron ion elution-deteriorated product that has adhered is oxidatively decomposed to obtain an iron filter medium.
Wastewater characterized by sustaining the elution of iron ions
Processing method.
装置にて汚水処理を行うに当たり、処理途中で上記鉄濾
材を振動させて濾材表面に付着したリン酸鉄塩類等およ
び生物膜類や塵埃の脱離と、鉄濾材を処理装置から引き
上げて、濾材表面に付着した鉄イオン溶出妨害生成物を
大気曝露にて酸化分解すること、を併用して鉄濾材から
の鉄イオンの溶出を持続させることを特徴とする汚水処
理方法。 2. Sewage treatment using an iron filter medium as a contact filter medium.
During the treatment of sewage with the equipment, the iron filter
By vibrating the material, iron phosphates, etc. adhering to the filter surface and
And desorption of biofilm and dust, and pulling iron filter media from the treatment equipment.
Raise the iron ion elution disturbing products adhering to the surface of the filter media.
From iron filter media that is oxidatively decomposed by exposure to the air
Sewage treatment characterized by maintaining the elution of iron ions in water
Reasoning method.
付着物の酸化分解を常温風または温風の送風により行う
ことを特徴とする請求項1または2に記載の汚水処理方
法。 3. The surface of a filter medium in an oxidizing atmosphere exposed to the atmosphere
Oxidative decomposition of deposits is performed by blowing air at room temperature or warm air
The sewage treatment method according to claim 1 or 2, characterized in that
Law.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP5075187A JPH0767558B2 (en) | 1993-03-08 | 1993-03-08 | Sewage treatment method |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP5075187A JPH0767558B2 (en) | 1993-03-08 | 1993-03-08 | Sewage treatment method |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH06254580A JPH06254580A (en) | 1994-09-13 |
| JPH0767558B2 true JPH0767558B2 (en) | 1995-07-26 |
Family
ID=13568952
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP5075187A Expired - Fee Related JPH0767558B2 (en) | 1993-03-08 | 1993-03-08 | Sewage treatment method |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0767558B2 (en) |
Family Cites Families (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH0611440B2 (en) * | 1985-02-01 | 1994-02-16 | ユニチカ株式会社 | Sewage treatment method |
| JPH01101690U (en) * | 1987-12-26 | 1989-07-07 |
-
1993
- 1993-03-08 JP JP5075187A patent/JPH0767558B2/en not_active Expired - Fee Related
Also Published As
| Publication number | Publication date |
|---|---|
| JPH06254580A (en) | 1994-09-13 |
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