JPH0788491A - Microorganism treatment method for water contaminated with hardly decomposable aromatic compound - Google Patents

Microorganism treatment method for water contaminated with hardly decomposable aromatic compound

Info

Publication number
JPH0788491A
JPH0788491A JP5258882A JP25888293A JPH0788491A JP H0788491 A JPH0788491 A JP H0788491A JP 5258882 A JP5258882 A JP 5258882A JP 25888293 A JP25888293 A JP 25888293A JP H0788491 A JPH0788491 A JP H0788491A
Authority
JP
Japan
Prior art keywords
activated carbon
aromatic compound
water
hardly decomposable
water contaminated
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
JP5258882A
Other languages
Japanese (ja)
Inventor
Toshihito Kondo
敏仁 近藤
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.)
Fujita Corp
Original Assignee
Fujita Corp
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 Fujita Corp filed Critical Fujita Corp
Priority to JP5258882A priority Critical patent/JPH0788491A/en
Publication of JPH0788491A publication Critical patent/JPH0788491A/en
Pending legal-status Critical Current

Links

Classifications

    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W10/00Technologies for wastewater treatment
    • Y02W10/10Biological treatment of water, waste water, or sewage

Landscapes

  • Biological Treatment Of Waste Water (AREA)

Abstract

PURPOSE:To treat with microorganisms water contaminated with aromatic compounds such as phenol which are hardly decomposable by microorganism treatment without employing a simple active carbon adsorption method. CONSTITUTION:In the microorganism treatment of water contaminated with aromatic compounds which are hardly decomposable, the contaminates adsorbed on active carbon are decomposed stepwise by microorganisms using a rotary disk filter bed carrying the active carbon.

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、芳香族化合物系難分解
性物質で汚染された水を微生物処理して水中の芳香族化
合物系難分解性物質を分解する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 method for decomposing aromatic compound-based hardly decomposable substances by treating microorganisms with water contaminated with aromatic compound-based hardly decomposable substances.

【0002】[0002]

【従来の技術】都市ゴミ等の廃棄物埋立地からの浸出水
は、各種プラスチック製品その他の化学製品に由来する
芳香族化合物系の難分解性物質(以下、難分解性物質と
いう)を含有することが多い。そのような水を一般的な
好気性微生物処理法により処理しても、難分解性物質だ
けはほとんど分解されずに流出してしまう。このような
難分解性物質で汚染された水の処理法としては、従来、
活性炭を用いて難分解性物質を吸着させる方法しかなか
ったから、吸着能力いっぱいまで難分解性物質を吸着し
た活性炭を新しい活性炭と交換する手間や費用を要する
という問題点があった。
2. Description of the Related Art Leachate from landfills such as municipal waste contains aromatic compound-based persistent substances (hereinafter referred to as persistent substances) derived from various plastic products and other chemical products. Often. Even if such water is treated by a general aerobic microbial treatment method, only the hardly decomposable substance is hardly decomposed and flows out. As a method for treating water contaminated with such a persistent substance,
Since there is only a method of adsorbing the hardly decomposable substance using the activated carbon, there is a problem that it takes time and money to replace the activated carbon having adsorbed the hardly decomposable substance up to the adsorption capacity with a new activated carbon.

【0003】[0003]

【発明が解決しようとする課題】そこで本発明は、芳香
族化合物系難分解性物質で汚染された水を単なる活性炭
吸着法によらずに微生物処理する方法を提供しようとす
るものである。
Therefore, the present invention is intended to provide a method for treating water contaminated with an aromatic compound-based hardly decomposable substance by a microbial treatment, not by a simple activated carbon adsorption method.

【0004】[0004]

【課題を解決するための手段】本発明は、芳香族化合物
系難分解性物質で汚染された水を微生物処理法により処
理して水中の芳香族化合物系難分解性物質を分解するに
当たり、処理装置として回転円板に活性炭を担持させた
回転円板濾床を用いることを特徴とするものである。
DISCLOSURE OF THE INVENTION The present invention relates to the treatment of water contaminated with an aromatic compound-based persistent substance by a microbial treatment method to decompose the aromatic compound-based persistent substance in water. The apparatus is characterized by using a rotating disk filter bed in which activated carbon is supported on the rotating disk.

【0005】回転円板濾床は、バイオディスクフィルタ
ーとも呼ばれる微生物処理装置である。一般的なもの
は、直径1〜3m、厚さ0.7〜20mm程度の円板を数
十枚、約2cm間隔で回転軸に固定し、それを、回転軸を
水平にして処理槽に取り付けて、円板面のおよそ半分が
廃水中に浸漬された状態でゆっくり回転するようにして
ある。
The rotating disk filter bed is a microbial treatment device also called a biodisc filter. In general, dozens of discs with a diameter of 1 to 3 m and a thickness of 0.7 to 20 mm are fixed to a rotating shaft at intervals of about 2 cm, and the disc is attached to the processing tank with the rotating shaft horizontal. Thus, about half of the disk surface is slowly rotated while being immersed in the waste water.

【0006】本発明においては、上記回転円板濾床の回
転円板に活性炭を担持させる。具体的な活性炭担持方法
は、円板が回転するにともない円板上の活性炭も被処理
水に接触するようにできればよく、特に限定されるもの
ではないが、簡単には、円板を中空構造のものにすると
共に多数の貫通孔(透水孔)を有するものとし、その中
空部に、活性炭を充填すればよい。装置運転中、水は透
水孔から円板内部に浸透し、中の活性炭と接触する。透
水孔から活性炭が漏れ出さないようにするには、透水孔
を金網等で覆うか、活性炭を網もしくは編織物からなる
袋に詰めてから円板中空部に入れる。活性炭としては、
粒径が0.5〜5mm程度の粒状のものが適当である。
In the present invention, activated carbon is supported on the rotary disc of the rotary disc filter bed. The specific activated carbon supporting method is not particularly limited as long as the activated carbon on the disk can be brought into contact with the water to be treated as the disk rotates, but it is not particularly limited. In addition to the above, it has a large number of through holes (water-permeable holes), and the hollow portion thereof may be filled with activated carbon. During the operation of the device, water permeates the inside of the disc through the water-permeable holes and comes into contact with the activated carbon inside. In order to prevent the activated carbon from leaking out from the water permeable hole, the water permeable hole is covered with a metal net or the like, or the activated carbon is packed in a bag made of net or knitted fabric and then put in the hollow portion of the disc. As activated carbon,
A granular material having a particle size of about 0.5 to 5 mm is suitable.

【0007】回転円板の材料としては、一般的な回転円
板濾床に使われている発泡プラスチック、プラスチッ
ク、耐水性合板、金属板等を使用することができる。活
性炭を担持させた円板を用いた回転円板濾床により難分
解性物質汚染水の処理を行うと、一般的な回転円板濾床
による有機性排水処理の場合と同様に、まず馴養により
円板表面および活性炭表面には微生物膜が形成される。
このとき、活性炭の表面積が大きいため、円板当たりの
微生物付着量は活性炭を担持させない場合よりも著しく
多くなる(活性炭表面には、一般的な有機物分解菌のほ
か、難分解性物質分解菌も付着する)。そして、有機物
を吸着した活性炭表面では水中よりも有機物の濃度が高
まるため、活性炭表面の微生物は旺盛に増殖し、それに
ともない難分解性物質をも活発に取り込んで分解する。
以上により、難分解性物質は確実に分解され、清浄化さ
れた水が放流される。
As the material of the rotary disc, there can be used foamed plastic, plastic, water-resistant plywood, metal plate and the like which are commonly used for a rotary disc filter bed. When water that is difficult to decompose is treated with a rotating disk filter bed that uses a disk that supports activated carbon, first, by acclimatization, as in the case of general organic wastewater treatment with a rotating disk filter bed, A microbial film is formed on the disk surface and the activated carbon surface.
At this time, since the surface area of activated carbon is large, the amount of adhered microorganisms per disc is significantly larger than that when no activated carbon is supported (on the surface of activated carbon, in addition to general organic substance-decomposing bacteria, hardly decomposable substance decomposing bacteria Adhere to). Since the concentration of organic matter on the surface of activated carbon on which organic matter is adsorbed is higher than that in water, microorganisms on the surface of activated carbon proliferate vigorously, and accordingly, persistent substances are also actively taken in and decomposed.
As described above, the hardly decomposable substance is surely decomposed and the purified water is discharged.

【0008】[0008]

【実施例】下記の組成の人工廃水を実験用回転円板濾床
で処理した。 グルコース水溶液(50g/l)10ml K2HPO4 (21.7g/l),KH2PO4(8.5g/l),Na
2HPO4・12H2O(44.6g/l),NH4Cl(1.7g/l)の水
溶液0.27ml MgSO4・7H2O(22.5g/l),FeCl3・6H2O(0.
25g/l),NH4Cl(46.4g/l)の水溶液1ml CaCl2水溶液(27.5g/l)1ml ポリペプトン 0.15g 難分解性物質(フェノール) 0.05g
Example An artificial wastewater having the following composition was treated with a laboratory rotary disc filter bed. Glucose aqueous solution (50g / l) 10ml K 2 HPO 4 (21.7g / l), KH 2 PO 4 (8.5g / l), Na
An aqueous solution of 2 HPO 4 · 12H 2 O (44.6 g / l) and NH 4 Cl (1.7 g / l) 0.27 ml MgSO 4 · 7H 2 O (22.5 g / l), FeCl 3 · 6H 2 O (0.
25 g / l), NH 4 Cl (46.4 g / l) aqueous solution 1 ml CaCl 2 aqueous solution (27.5 g / l) 1 ml Polypeptone 0.15 g Persistent substance (phenol) 0.05 g

【0009】上記〜を混合し、水を加えて全量を1
000mlとし、pHを7.0に調整する(BOD:220
0ppm,COD:500ppm,全窒素:32ppm,リン:
3.5ppm)。
[0009] The above items (1) to (4) were mixed, water was added to make the total amount 1
000 ml and adjust pH to 7.0 (BOD: 220
0ppm, COD: 500ppm, total nitrogen: 32ppm, phosphorus:
3.5 ppm).

【0010】用いた回転円板濾床は次のようなものであ
る。 処理槽容積:2100ml 回転円板 比較例 直径17cm,厚さ1cmのものを6枚、1cm間隔で回転軸
に固定 総表面積:2750cm2;材質:塩化ビニル樹脂;回転
数:8rpm 実施例 上記比較例のものを中空構造にし、且つ直径15mmの透
水孔を25mm間隔で全面に穿設したもの。中空部には、
ナイロン織物製の袋に入れた粒状活性炭を充填(活性炭
充填量:54g/円板)。
The rotating disc filter bed used is as follows. Treatment tank volume: 2100 ml Rotating disk Comparative example 6 pieces with a diameter of 17 cm and a thickness of 1 cm are fixed to the rotating shaft at 1 cm intervals Total surface area: 2750 cm 2 ; Material: Vinyl chloride resin; Rotation speed: 8 rpm Example Above comparative example A hollow structure, and water-permeable holes with a diameter of 15 mm are formed on the entire surface at intervals of 25 mm. In the hollow part,
Fill with granular activated carbon in a nylon fabric bag (activated carbon filling amount: 54 g / disc).

【0011】上記の装置に、BOD面積負荷が5g/m2
日になるように上記人工廃水を連続的に供給し、連続処
理を行なった。実験中、処理槽から流出する処理水につ
いて、COD、BOD、およびフェノール濃度の測定を
行なった。実験結果を表1〜4に示す。
In the above equipment, the BOD area load is 5 g / m 2 ·
The artificial wastewater was continuously supplied and treated continuously on a daily basis. During the experiment, COD, BOD, and phenol concentration were measured for the treated water flowing out from the treatment tank. The experimental results are shown in Tables 1 to 4.

【0012】[0012]

【表1】 実験開始0〜15日の平均値(単位:ppm) [Table 1] Average value from 0 to 15 days from the start of the experiment (unit: ppm)

【0013】[0013]

【表2】 実験開始30〜45日の平均値(単位:pp
m)
[Table 2] Average value of 30 to 45 days from the start of the experiment (unit: pp
m)

【0014】[0014]

【表3】 実験開始60〜75日の平均値(単位:pp
m)
[Table 3] Average value 60 to 75 days after the start of the experiment (unit: pp
m)

【0015】[0015]

【表4】 実験開始300〜315日の平均値(単位:
ppm)
[Table 4] Average value of 300 to 315 days from the start of the experiment (unit:
ppm)

【0016】上記実験において、フェノールは活性炭1
g当たり0.10mg/dayが供給されたことになるが、用
いた活性炭のフェノール吸着能から計算される飽和吸着
量を超える量のフェノールを処理した後(表4に示した
時期)も処理水のフェノール濃度は0であり、活性炭を
担持した回転円板が単なるフェノール吸着装置として機
能しているのではなく、フェノールの微生物分解を促進
していることが確認された。
In the above experiment, phenol is activated carbon 1
Although 0.10 mg / day was supplied per g, the treated water was treated even after treating the phenol in an amount exceeding the saturated adsorption amount calculated from the phenol adsorption capacity of the activated carbon used (time shown in Table 4). The concentration of phenol was 0, and it was confirmed that the rotating disk supporting the activated carbon did not function as a simple phenol adsorption device but promoted the microbial decomposition of phenol.

【0017】[0017]

【発明の効果】上述のように、本発明の方法は回転円板
に活性炭を担持させておくだけで済み、担持させた活性
炭は長期間交換不要であり、また処理操作としては一般
的な回転円板濾床による都市下水処理と何ら変わるとこ
ろがないから、芳香族化合物系難分解性物質で汚染され
た水を容易に且つ効率よく清浄化することができ、処理
効果もきわめて確実である。
As described above, according to the method of the present invention, it is only necessary to support the activated carbon on the rotating disk, and the activated carbon supported does not need to be replaced for a long period of time. There is no difference from the treatment of municipal sewage using a disc filter bed, so that water contaminated with aromatic compound-based hardly decomposable substances can be easily and efficiently cleaned, and the treatment effect is extremely reliable.

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 芳香族化合物系難分解性物質で汚染され
た水を微生物処理法により処理して水中の芳香族化合物
系難分解性物質を分解するに当たり、処理装置として回
転円板に活性炭を担持させた回転円板濾床を用いること
を特徴とする、芳香族化合物系難分解性物質で汚染され
た水の微生物処理法。
1. When decomposing the aromatic compound-based hardly-decomposable substance in water by treating the water contaminated with the aromatic compound-type hardly-decomposable substance by a microbial treatment method, activated carbon is applied to a rotating disk as a treatment device. A method for treating microorganisms of water contaminated with an aromatic compound-based hardly decomposable substance, characterized by using a supported rotating disk filter bed.
JP5258882A 1993-09-24 1993-09-24 Microorganism treatment method for water contaminated with hardly decomposable aromatic compound Pending JPH0788491A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP5258882A JPH0788491A (en) 1993-09-24 1993-09-24 Microorganism treatment method for water contaminated with hardly decomposable aromatic compound

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP5258882A JPH0788491A (en) 1993-09-24 1993-09-24 Microorganism treatment method for water contaminated with hardly decomposable aromatic compound

Publications (1)

Publication Number Publication Date
JPH0788491A true JPH0788491A (en) 1995-04-04

Family

ID=17326344

Family Applications (1)

Application Number Title Priority Date Filing Date
JP5258882A Pending JPH0788491A (en) 1993-09-24 1993-09-24 Microorganism treatment method for water contaminated with hardly decomposable aromatic compound

Country Status (1)

Country Link
JP (1) JPH0788491A (en)

Similar Documents

Publication Publication Date Title
Al-Amshawee et al. Biocarriers for biofilm immobilization in wastewater treatments: a review
JP5591899B2 (en) Microbial activity control substance supply device, environmental purification method and bioreactor using the same
Annadurai et al. Adsorption and bio-degradation of phenol by chitosan-immobilized Pseudomonas putida (NICM 2174)
Kolb et al. Activated carbon sequencing batch biofilm reactor to treat industrial wastewater
PIRBAZARI et al. Evaluation of biofilm development on various natural and synthetic media
JPS60147287A (en) Drinking water modifier
Suidan et al. Anaerobic dechlorination using a fluidized-bed GAC reactor
CA1328633C (en) Microbiological purification of water and a microorganism for use in said process
Sevillano et al. Feasibility study of degradation of phenol in a fluidized bed bioreactor with a cyclodextrin polymer as biofilm carrier
JP4719094B2 (en) Method for treating liquid containing selenate compound using microorganisms
JP3488853B2 (en) Deodorant, deodorizing method, deodorizing member and deodorizing device
JPH0788491A (en) Microorganism treatment method for water contaminated with hardly decomposable aromatic compound
JPS62279888A (en) Treatment of sewage
CA2221476A1 (en) Method and system for bioremediation of hydrocarbon contaminated water
JPH0818037B2 (en) Wastewater microbial treatment equipment
Kim et al. Effect of biological treatments on COD adsorption
Klimenko et al. Biosorption processes for natural and wastewater treatment–part 1: Literature review
JPH11262790A (en) Purifying treatment method purifying treatment material and regeneration of purifying treatment material
Vuoriranta et al. Bioregeneration of activated carbon in a fluidized GAC bed treating bleached kraft mill secondary effluent
JP2554560B2 (en) Method and apparatus for biological regeneration of activated carbon
JP2563010B2 (en) Method of treating organic chlorine compounds
Dharmawan et al. Combination of activated allophane-effective microorganisms for bioremediation of iron and manganese on pharmaceutical industry wastewater
JPH0775795A (en) Microbiological treatment of waste water containing grease
JPH03123688A (en) Bag for purifying drinking water
Summers et al. Biodegradation of MIB and geosmin in biological sand and BAC filters: acclimation, steady-state and varying influent