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JPS6250200B2 - - Google Patents
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JPS6250200B2 - - Google Patents

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Publication number
JPS6250200B2
JPS6250200B2 JP54100306A JP10030679A JPS6250200B2 JP S6250200 B2 JPS6250200 B2 JP S6250200B2 JP 54100306 A JP54100306 A JP 54100306A JP 10030679 A JP10030679 A JP 10030679A JP S6250200 B2 JPS6250200 B2 JP S6250200B2
Authority
JP
Japan
Prior art keywords
plastic
wastewater
filter
filter bed
magnetic
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
Application number
JP54100306A
Other languages
Japanese (ja)
Other versions
JPS5626589A (en
Inventor
Masafumi Morya
Tomio Imachi
Makoto Takai
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.)
Myoshi Oil and Fat Co Ltd
Original Assignee
Myoshi Oil and Fat 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 Myoshi Oil and Fat Co Ltd filed Critical Myoshi Oil and Fat Co Ltd
Priority to JP10030679A priority Critical patent/JPS5626589A/en
Publication of JPS5626589A publication Critical patent/JPS5626589A/en
Publication of JPS6250200B2 publication Critical patent/JPS6250200B2/ja
Granted 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

  • Apparatus Associated With Microorganisms And Enzymes (AREA)
  • Immobilizing And Processing Of Enzymes And Microorganisms (AREA)
  • Biological Treatment Of Waste Water (AREA)

Description

【発明の詳細な説明】[Detailed description of the invention]

本発明は、生物固定濾床体を製造する際、プラ
スチツク内に磁性体粉末を含有せしめ、これを濾
床体として用いることにより、従来の濾床体より
も微生物の付着性を高め、廃水を効率良く処理す
ることができる生物固定濾床体を用いた有機性廃
水の処理方法に関するものである。 有機性廃水を生物学的に処理する方法は、今日
多方面で用いられている。たとえば廃水中で微生
物を繁殖させ有機物を分解する活性汚泥法、微生
物を濾床体上で繁殖させ、これを廃水と接触し有
機物を分解する生物固定濾床体を用いる方法等が
ある。 生物固定濾床体を用いる方法は、活性汚泥法よ
り敷地面積が少なくてすみ、又管理が容易で優れ
ており、濾床体としてプラスチツクを用いる回転
円板法、あるいは砂利を用いる散水濾床法等が知
られている。 しかしながら、プラスチツク、活性炭、砂利等
を濾床として用いる従来の方法では、これらの濾
床に微生物が着床し難く、又着床した微生物が剥
離し易い等の欠点があり、そのため廃水を安定し
て処理することができない等の問題があつた。 そこで本発明者らは、塩化ビニル、ポリエチレ
ン、ポリプロピレンなどのプラスチツクに磁性体
粉末を含有せしめ磁化した濾床体を用いることに
より、微生物の剥離を防ぎ有機性廃水を容易に処
理できることに成功した。 即ち本発明は、プラスチツクに磁性体粉末を混
合し、成形して磁化して得られる磁性プラスチツ
クを生物固定濾床体として用いる有機性廃水の処
理方法であり、本発明によれば微生物の付着性が
非常に良い濾床体を用いるため、微生物による廃
水処理も効果的に行なわれ、従来の濾床体を使用
した生物処理方法と比較するとはるかに、
BOD、CODの除去率が高く、さらに処理水の
BOD、COD値を低くすることが可能である。 本発明の濾床体に用いる磁性プラスチツクは、
ポリエチレン、ポリプロピレン、塩化ビニル等の
プラスチツクに磁性体を練り込んで成形した後磁
化することによつても製造することができるが、
発泡剤を用いて、発泡して成形した後磁化し多孔
質プラスチツクとしたものがより好ましい。発泡
剤を用いて分解型発泡剤の分解温度が成形温度以
下の場合、あらかじめプラスチツク、磁性体粉末
および発泡剤を混合し、成形と発泡を同時に行な
つた後、磁化することにより強磁性多孔質プラス
チツクが得られるが、分解温度が成形温度以上の
場合には、前記混合物を成形加工した後、発泡加
工し、ついで磁化することによつても磁性プラス
チツクが得られる。さたさらに溶剤型発泡剤を使
用する場合にはプラスチツク、磁性体粉末をあら
かじめ混合し、成形時に発泡剤を圧入することに
より成形と発泡を行ない、さらに磁化して磁性プ
ラスチツクが得られ、この方法によれば発泡倍率
の高い製品が得られる。また、より発泡倍率の高
い製品を得るには、さらに放射線架橋もしくは架
橋剤をプラスチツクに添加することにより可能で
ある。さらにプラスチツクに磁性体粉末もしくは
発泡剤を均一に分散させるために、界面活性剤た
とえばステアリン酸、オレイン酸、ラウリン酸、
リノール酸、パルミチン酸などおよびこれらの塩
類(Na、Li、K、Ca、Mg)などを添加してやれ
ば良い。 成形方法としては押出し、カレンダ、コンベア
ベルトキヤスチングなどの方法が挙げられる。 発泡剤としては、分解形発泡剤として、重炭酸
ソーダ、炭酸アンモニウム、アゾビスイソブチロ
ニトリル、ジアゾアミノベンゼン、N・N′−ジ
メチル−N・N′−ジニトロソテレフタルアミド
等が、また溶剤型発泡剤として、プロパン、ブタ
ン、ヘプタン、ヘキサン、ベンゼン、塩化メチレ
ン、三塩化フツ化メタン等が挙げられる。 本発明で使用するプラスチツクとしては、ポリ
塩化ビニル、ポリエチレン、ポロプロピレン、エ
チレン−酢酸ビニル共重合樹脂、ポリスチレン、
ポリウレタン、ABS樹脂、ポリアミド、ポリビ
ニルホルマール、酢酸繊維素、アクリル樹脂、エ
ポキシ樹脂、フエノール樹脂、ユリア樹脂、シリ
コン樹脂などがあるが、これらに限定されるもの
ではない。 本発明で使用する磁性体粉末としては、マグネ
タイト、マグネシウムフエライト、ニツケルフエ
ライト、マンガンフエライト、コバルトフエライ
ト、亜鉛フエライト、バリウムフエライト、スト
ロンチウムフエライト、鉛フエライトなどがあ
る。 プラスチツク内に含有させる磁性体粉末の量
は、一般に1〜50%であるが、好ましくは、20〜
30%である。 しかしながら、プラスチツクの成形が可能であ
れば上記の範囲に限定されない。 以上の如く製造された磁性プラスチツクはシー
ト状もしくは粒状で得られ、廻転円板法における
濾床、散水濾床法における塊状濾材または平板状
濾材の濾床、接触酸化法における固定床、など
種々の生物処理法における濾床体として用い、そ
れに微生物を着床せしめて有機性廃水の処理を行
なうのである。 磁性プラスチツクに微生物を着床するには、以
下に述べる廃水処理操作と同条件にて廃水中の微
生物が磁性プラスチツク上に繁殖するまでの一定
期間、廃水と磁性プラスチツクとを接触させるこ
とにより着床し得る。 微生物を着床せしめた磁性プラスチツクを濾床
体とし有機性廃水の処理を行なうには廻転円板
法、散水濾床法、接触酸化法等の通常の操作法に
従つて行なう。例えば回転円板処理装置による方
法では、回転翼にシート状の磁性プラスチツクを
用い、回転速度、水の流入速度通常の条件下で水
と接触せしめ処理を行なう。 散水濾床法では、粒状(径:1〜10cm)の磁性
プラスチツクを層状にしきつめ、その上から廃水
を流化せしめると、磁性プラスチツクの表面に微
生物の膜が形成され、これにより廃水が浄化され
る。 以下に実施例によつて説明する。 実施例 1 プラスチツクとしてポリエチレンを用いマグネ
タイトを20%含有する円板(厚さ1.2cm×直径100
cm)を形成し、磁化して生物固定濾床体を得た。 この濾床体を回転円板法により、有機性実廃水
の処理実験を行なつた。なお、1週間運転を続け
ることにより円板上に生物膜が生育するのが認め
られた。 処理水の測定は、運転開始より1カ月経過した
後、3日間行なつた。試料のサンプリングは、午
後3時に行なつた。 実廃水の原水組成を表−1に、実験条件を表−
2に、処理結果を表−3に示す。
In the present invention, when manufacturing a bioimmobilized filter bed, magnetic powder is contained in plastic and used as a filter bed, thereby increasing the adhesion of microorganisms compared to conventional filter beds and reducing wastewater. The present invention relates to a method for treating organic wastewater using a biologically fixed filter bed that can be efficiently treated. Methods for biologically treating organic wastewater are widely used today. Examples include an activated sludge method in which microorganisms are propagated in wastewater to decompose organic matter, and a method using a bioimmobilized filter bed in which microorganisms are grown on a filter bed and brought into contact with wastewater to decompose organic matter. The method using a biologically fixed filter bed requires less site area than the activated sludge method, and is easier to manage. etc. are known. However, conventional methods that use plastic, activated carbon, gravel, etc. as filter beds have the disadvantage that microorganisms are difficult to settle on these filter beds, and the attached microorganisms are easy to detach. There were problems such as not being able to process the data. Therefore, the present inventors succeeded in preventing the detachment of microorganisms and making it possible to easily treat organic wastewater by using a magnetized filter bed made of plastic such as vinyl chloride, polyethylene, or polypropylene containing magnetic powder. That is, the present invention is a method for treating organic wastewater using a magnetic plastic obtained by mixing magnetic powder with plastic, molding it, and magnetizing it as a biological fixation filter. Because it uses a filter bed with very good filtration, wastewater treatment using microorganisms is also effective, and compared to the conventional biological treatment method using a filter bed, it is much more effective.
The removal rate of BOD and COD is high, and the treated water
It is possible to lower BOD and COD values. The magnetic plastic used for the filter bed of the present invention is
It can also be manufactured by kneading a magnetic material into plastic such as polyethylene, polypropylene, vinyl chloride, etc., molding it, and then magnetizing it.
More preferably, the material is foamed using a foaming agent, molded, and then magnetized to form a porous plastic. When the decomposition temperature of the decomposable foaming agent is lower than the molding temperature, the plastic, magnetic powder, and foaming agent are mixed in advance, molding and foaming are performed simultaneously, and then magnetized to create a ferromagnetic porous material. A plastic can be obtained, but if the decomposition temperature is higher than the molding temperature, a magnetic plastic can also be obtained by molding the mixture, followed by foaming and then magnetization. Furthermore, when using a solvent-based blowing agent, the plastic and magnetic powder are mixed in advance, and the blowing agent is press-fitted during molding to perform molding and foaming, which is then magnetized to obtain magnetic plastic. According to the method, a product with a high foaming ratio can be obtained. In addition, a product with a higher expansion ratio can be obtained by further radiation crosslinking or by adding a crosslinking agent to the plastic. Additionally, surfactants such as stearic acid, oleic acid, lauric acid,
Linoleic acid, palmitic acid, and their salts (Na, Li, K, Ca, Mg) may be added. Examples of the molding method include extrusion, calendering, conveyor belt casting, and the like. Examples of blowing agents include decomposition blowing agents such as sodium bicarbonate, ammonium carbonate, azobisisobutyronitrile, diazoaminobenzene, N・N′-dimethyl-N・N′-dinitrosoterephthalamide, and solvent-based foaming agents. Examples of the agent include propane, butane, heptane, hexane, benzene, methylene chloride, trichlorofluorinated methane, and the like. Plastics used in the present invention include polyvinyl chloride, polyethylene, polypropylene, ethylene-vinyl acetate copolymer resin, polystyrene,
Examples include, but are not limited to, polyurethane, ABS resin, polyamide, polyvinyl formal, cellulose acetate, acrylic resin, epoxy resin, phenolic resin, urea resin, and silicone resin. Examples of the magnetic powder used in the present invention include magnetite, magnesium ferrite, nickel ferrite, manganese ferrite, cobalt ferrite, zinc ferrite, barium ferrite, strontium ferrite, and lead ferrite. The amount of magnetic powder contained in the plastic is generally 1 to 50%, but preferably 20 to 50%.
It is 30%. However, it is not limited to the above range as long as plastic molding is possible. The magnetic plastic produced as described above is obtained in the form of a sheet or granules, and can be used in various ways, such as a filter bed in the rotating disk method, a block or flat filter bed in the trickling bed method, and a fixed bed in the catalytic oxidation method. It is used as a filter bed in biological treatment methods, and microorganisms are implanted on it to treat organic wastewater. In order to implant microorganisms onto magnetic plastic, the wastewater is allowed to come into contact with the magnetic plastic for a certain period of time until the microorganisms in the wastewater propagate on the magnetic plastic under the same conditions as the wastewater treatment described below. It is possible. The treatment of organic wastewater using magnetic plastic on which microorganisms have been implanted as a filter bed is carried out according to conventional operating methods such as the rotating disk method, the trickling filter method, and the catalytic oxidation method. For example, in a method using a rotating disk processing apparatus, a sheet-like magnetic plastic is used for the rotor blade, and the processing is carried out by bringing it into contact with water under normal conditions of rotational speed and water inflow rate. In the trickling filter method, granular magnetic plastic (diameter: 1 to 10 cm) is tightly packed into a layer and wastewater is allowed to flow over the layer. A microbial film is formed on the surface of the magnetic plastic, which purifies the wastewater. Ru. Examples will be explained below. Example 1 A disk containing 20% magnetite using polyethylene as plastic (thickness 1.2 cm x diameter 100 mm)
cm) and magnetized to obtain a biofixed filter bed. A treatment experiment for organic wastewater was conducted using this filter bed using the rotating disk method. In addition, after one week of continuous operation, it was observed that a biofilm grew on the disk. Measurements of the treated water were carried out for three days after one month had passed since the start of operation. Sample sampling was performed at 3:00 p.m. The raw water composition of actual wastewater is shown in Table 1, and the experimental conditions are shown in Table 1.
2, the processing results are shown in Table 3.

【表】【table】

【表】【table】

【表】 比較例 1 磁性体粉末を含有せずに製造したポリエチレン
製の生物固定濾床体を用い、回転円板法により実
施例1と同様の処理実験を行なつた。 実験条件は、実施例1の表−2と同様である。
実廃水の原水組成を表−4に示す。実施例1と
は、多少日時的な差が生じているが、大きな原水
組成の変動はなかつた。処理結果を表−5に示
す。
[Table] Comparative Example 1 A treatment experiment similar to that in Example 1 was conducted using a rotating disk method using a polyethylene bioimmobilized filter bed manufactured without containing magnetic powder. The experimental conditions are the same as in Table 2 of Example 1.
Table 4 shows the raw water composition of actual wastewater. Although there was a slight difference in date and time from Example 1, there was no major change in the raw water composition. The treatment results are shown in Table 5.

【表】【table】

【表】【table】

【表】 実施例 2 プラスチツクとして塩化ビニール樹脂を用い、
亜鉛フエライトを20%含有させた磁性を持つた生
物固定濾床体(円板:厚さ1.2cm×直径100cm)を
製造した。 この濾床体を回転円板法により、実施例1と同
様な実験を行なつた。 実廃水の原水組成を表−6、処理結果を表−7
に示す。 なお、実験条件は、表−2と同一である。
[Table] Example 2 Using vinyl chloride resin as plastic,
A magnetic bioimmobilized filter bed (disc: 1.2 cm thick x 100 cm diameter) containing 20% zinc ferrite was manufactured. Experiments similar to those in Example 1 were conducted using this filter bed using the rotating disk method. Table 6 shows the raw water composition of actual wastewater, and Table 7 shows the treatment results.
Shown below. Note that the experimental conditions are the same as in Table-2.

【表】【table】

【表】 実施例 3 プラスチツクとしてポリプロピレンを用い、バ
リウムフエライトを30%含有させ、径5cmの充填
剤を製造した。 この充填剤を磁化したものを散水濾床体に使用
し、1週間運転を続け、濾床体に生物膜の発育が
認められてから生物処理実験を行なつた。処理水
の測定は、運転開始より1ケ月径過した後、3日
間行なつた。 実廃水の原水組成を表−8に、実験条件を表−
9に、処理結果を表−10に示す。
[Table] Example 3 A filler having a diameter of 5 cm was produced using polypropylene as plastic and containing 30% barium ferrite. This magnetized filler was used in a trickling filter, and operation was continued for one week. After the growth of biofilm was observed on the filter, a biological treatment experiment was conducted. Measurements of the treated water were carried out for 3 days, one month after the start of operation. The raw water composition of actual wastewater is shown in Table-8, and the experimental conditions are shown in Table-8.
9, and the processing results are shown in Table 10.

【表】【table】

【表】【table】

【表】 比較例 2 実施例3の比較として、ポロプロピレンのみで
充填剤を製造し、同一条件で散水濾床にて生物処
理実験を行なつた。 原水組成を表−11に、処理水を表−12に示す。
[Table] Comparative Example 2 As a comparison with Example 3, a filler was produced using only polypropylene, and a biological treatment experiment was conducted using a trickling filter under the same conditions. The raw water composition is shown in Table 11, and the treated water is shown in Table 12.

【表】【table】

【表】 実施例 4 プラスチツクとして、ポリエチレンを用い、コ
バルトフエライト粉末を15%含有させ、発泡剤と
してアゾジカルボンアミド1%を使用し、径が40
〜50mmの発泡した充填剤を製造し、磁化した。 得られた充填剤を散水濾床体に使用し、1週間
運転を続け、濾床体の表面に生物膜の発育が認め
られてから、生物処理実験を行なつた。処理水の
測定は、運転開始より1ケ月経過した後、3日間
行なつた。実廃水の原水組成を表−13に、実験条
件を表−14に、処理結果を表−15に示す。
[Table] Example 4 Polyethylene was used as the plastic, containing 15% cobalt ferrite powder, and 1% azodicarbonamide was used as the blowing agent.
A ~50 mm expanded filler was prepared and magnetized. The obtained filler was used in a trickling filter, and operation was continued for one week. After the growth of biofilm was observed on the surface of the filter, a biological treatment experiment was conducted. Measurements of the treated water were carried out for 3 days, one month after the start of operation. The raw water composition of actual wastewater is shown in Table 13, the experimental conditions are shown in Table 14, and the treatment results are shown in Table 15.

【表】【table】

【表】【table】

【表】 比較例 3 実施例4の比較として、プラスチツクとしてポ
リエチレンを用い、これにコバルトフエライト粉
末を15%含有させ、発泡剤としてアゾジカルボン
アミド1%を使用し、径が40〜50mmの発泡した充
填剤を製造した。得られた充填剤を実施例4と同
様に生物処理実験を行なつた。実廃水の原水組成
を表−16に、実験条件を表−17に、処理結果を表
−18に示す。
[Table] Comparative Example 3 As a comparison with Example 4, polyethylene was used as the plastic, containing 15% cobalt ferrite powder, and 1% azodicarbonamide was used as the foaming agent, and foamed with a diameter of 40 to 50 mm. A filler was produced. The obtained filler was subjected to a biological treatment experiment in the same manner as in Example 4. The raw water composition of actual wastewater is shown in Table 16, the experimental conditions are shown in Table 17, and the treatment results are shown in Table 18.

【表】【table】

【表】【table】

【表】【table】

Claims (1)

【特許請求の範囲】[Claims] 1 プラスチツクに磁性体粉末を混合し、成形し
磁化して得られたる磁性プラスチツクを生物固定
濾床体として用い、微生物を着床せしめた該生物
固定濾床体を有機性廃水と接触させ、有機性廃水
中の有機物を除去することを特徴とする有機性廃
水の処理方法。
1. The magnetic plastic obtained by mixing magnetic powder with plastic, molding and magnetizing it is used as a bioimmobilized filter, and the bioimmobilized filter on which microorganisms have been implanted is brought into contact with organic wastewater. A method for treating organic wastewater characterized by removing organic matter from the organic wastewater.
JP10030679A 1979-08-08 1979-08-08 Filter bed body to which organism is fixed Granted JPS5626589A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP10030679A JPS5626589A (en) 1979-08-08 1979-08-08 Filter bed body to which organism is fixed

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP10030679A JPS5626589A (en) 1979-08-08 1979-08-08 Filter bed body to which organism is fixed

Publications (2)

Publication Number Publication Date
JPS5626589A JPS5626589A (en) 1981-03-14
JPS6250200B2 true JPS6250200B2 (en) 1987-10-23

Family

ID=14270476

Family Applications (1)

Application Number Title Priority Date Filing Date
JP10030679A Granted JPS5626589A (en) 1979-08-08 1979-08-08 Filter bed body to which organism is fixed

Country Status (1)

Country Link
JP (1) JPS5626589A (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110127860B (en) * 2019-06-11 2021-07-30 南京大学 A kind of preparation method and equipment of novel biological magnetic suspension filler for water treatment
CN113149182A (en) * 2021-04-27 2021-07-23 内蒙古科技大学 Preparation method of magnetic biological carrier

Also Published As

Publication number Publication date
JPS5626589A (en) 1981-03-14

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