JP2001205288A - Carrier for water treatment, its production method, and apparatus for water treatment - Google Patents
Carrier for water treatment, its production method, and apparatus for water treatmentInfo
- Publication number
- JP2001205288A JP2001205288A JP2000019796A JP2000019796A JP2001205288A JP 2001205288 A JP2001205288 A JP 2001205288A JP 2000019796 A JP2000019796 A JP 2000019796A JP 2000019796 A JP2000019796 A JP 2000019796A JP 2001205288 A JP2001205288 A JP 2001205288A
- Authority
- JP
- Japan
- Prior art keywords
- water treatment
- carrier
- weight
- thermoplastic resin
- resin
- 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.)
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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)
Abstract
Description
【0001】[0001]
【発明の属する技術分野】本発明は、微生物を用いる各
種の水処理に使用される水処理用担体、その水処理用担
体の製造方法、および、その水処理用担体が用いられる
水処理用装置に関する。The present invention relates to a water treatment carrier used for various water treatments using microorganisms, a method for producing the water treatment carrier, and a water treatment apparatus using the water treatment carrier. About.
【0002】[0002]
【従来の技術】従来より、微生物を用いる廃水処理など
の水処理においては、例えば、嫌気槽や好気槽などの水
処理槽に、流動床として、合成樹脂の成形物からなる水
処理用担体が投入されている。この水処理用担体は、槽
内において、微生物を付着して、その付着した微生物を
増殖させることによって、水処理を行なうものである。
このような水処理用担体としては、例えば、ポリエチレ
ン樹脂やポリプロピレン樹脂の成形物が用いられてい
る。2. Description of the Related Art Conventionally, in water treatment such as wastewater treatment using microorganisms, for example, a water treatment carrier comprising a synthetic resin molded product as a fluidized bed in a water treatment tank such as an anaerobic tank or an aerobic tank. Has been turned on. The carrier for water treatment performs water treatment by adhering microorganisms in the tank and growing the adhered microorganisms.
As such a carrier for water treatment, for example, a molded product of a polyethylene resin or a polypropylene resin is used.
【0003】[0003]
【発明が解決しようとする課題】しかるに、このような
ポリエチレン樹脂やポリプロピレン樹脂は、その比重が
1.0以下であるため、そのままの成形物を流動床に用
いると、水から浮き上がってしまうので、例えば、炭酸
カルシウムや硫酸バリウムなどの充填剤を配合して比重
を調整することにより、流動性の改善を図るようにして
いる。However, since the specific gravity of such a polyethylene resin or a polypropylene resin is 1.0 or less, if the molded product is used as it is in a fluidized bed, it will rise from water. For example, a filler such as calcium carbonate or barium sulfate is blended to adjust the specific gravity to improve the fluidity.
【0004】しかし、炭酸カルシウムや硫酸バリウムな
どの充填剤を配合すると、機械攪拌により、摩耗および
損傷しやすくなるという不具合を生じる。また、ポリエ
チレン樹脂やポリプロピレン樹脂は、そもそも疎水性で
あり、微生物との親和性が低く、水処理の効率の向上が
図りにくいという不具合をも有する。However, when fillers such as calcium carbonate and barium sulfate are blended, there is a problem that mechanical stirring causes wear and damage. In addition, polyethylene resins and polypropylene resins are inherently hydrophobic, have a low affinity for microorganisms, and have a disadvantage that it is difficult to improve the efficiency of water treatment.
【0005】一方、ポリウレタンフォームなどの発泡成
形物を、水処理用担体として用いることも知られている
が、発泡成形によると、任意の空孔率に成形しにくいた
め、最適の比重に調整することが困難で、流動性の改善
を図りにくいという不具合がある。また、発泡成形物で
は、任意の形状に成形しにくく、しかも、連続して大量
に生産しにくいという不具合をも有する。[0005] On the other hand, it is also known to use a foam molded article such as polyurethane foam as a carrier for water treatment. However, according to foam molding, it is difficult to mold to an arbitrary porosity. And it is difficult to improve the fluidity. In addition, the foam molded article has a disadvantage that it is difficult to mold into an arbitrary shape, and it is difficult to continuously mass-produce.
【0006】本発明は、このような不具合に鑑みなされ
たもので、その目的とするところは、流動性が良好で、
耐久性に優れ、しかも、生産性良く製造することのでき
る、水処理用担体、その水処理用担体の製造方法、およ
び、その水処理用担体が用いられる水処理用装置を提供
することにある。[0006] The present invention has been made in view of such disadvantages, and its object is to provide a liquid material having good fluidity.
An object of the present invention is to provide a water treatment carrier, a method for producing the water treatment carrier, and a water treatment apparatus using the water treatment carrier, which has excellent durability and can be produced with high productivity. .
【0007】[0007]
【課題を解決するための手段】上記目的を達成するため
に、本発明は、(1)親水性の熱可塑性樹脂、または、
親水性の熱可塑性樹脂および1種以上の他の熱可塑性樹
脂からなり、多孔質化されていることを特徴とする、水
処理用担体、(2)親水性の熱可塑性樹脂、または、親
水性の熱可塑性樹脂および1種以上の他の熱可塑性樹脂
を、発泡剤とともに溶融成形することによって得られる
ことを特徴とする、(1)に記載の水処理用担体、
(3)基質吸着物質、および/または、酵素活性を向上
させるあるいは生育促進する物質を含有していることを
特徴とする、(1)または(2)に記載の水処理用担
体、(4)親水性の熱可塑性樹脂、または、親水性の熱
可塑性樹脂および1種以上の他の熱可塑性樹脂を、発泡
剤とともに溶融成形することを特徴とする、水処理用担
体の製造方法、(5)親水性の熱可塑性樹脂、または、
親水性の熱可塑性樹脂および1種以上の他の熱可塑性樹
脂からなり、多孔質化されている水処理用担体が用いら
れていることを特徴とする、水処理用装置を含むもので
ある。To achieve the above object, the present invention provides (1) a hydrophilic thermoplastic resin or
A carrier for water treatment, comprising a hydrophilic thermoplastic resin and at least one other thermoplastic resin and being porous; (2) a hydrophilic thermoplastic resin, or a hydrophilic carrier; The water treatment carrier according to (1), which is obtained by melt-molding a thermoplastic resin and one or more other thermoplastic resins together with a foaming agent.
(3) The carrier for water treatment according to (1) or (2), wherein the carrier for water treatment according to (1) or (2) is characterized by containing a substrate-adsorbed substance and / or a substance that improves enzyme activity or promotes growth. (5) a method for producing a carrier for water treatment, which comprises melt-molding a hydrophilic thermoplastic resin or a hydrophilic thermoplastic resin and at least one other thermoplastic resin together with a foaming agent; Hydrophilic thermoplastic resin, or
A water treatment apparatus comprising a hydrophilic water-repellent resin and one or more other thermoplastic resins, wherein a porous water-treatment carrier is used.
【0008】[0008]
【発明の実施の形態】本発明の水処理用担体は、微生物
を用いる水処理などに用いられ、親水性の熱可塑性樹
脂、または、親水性の熱可塑性樹脂および1種以上の他
の熱可塑性樹脂からなり、多孔質化されている。BEST MODE FOR CARRYING OUT THE INVENTION The water treatment carrier of the present invention is used for water treatment using microorganisms and the like, and is made of a hydrophilic thermoplastic resin or a hydrophilic thermoplastic resin and at least one other thermoplastic resin. It is made of resin and made porous.
【0009】熱可塑性樹脂を用いることで、溶融成形に
よって任意の形状に成形することができるとともに、連
続して大量に生産することができる。また、親水性の熱
可塑性樹脂を用いることで、初期の吸水性がよく、微生
物の親和性が高いので、微生物の付着および増殖を向上
させることができ、これによって、効率的な水処理を行
なうことができる。なお、本発明において、親水性の熱
可塑性樹脂とは、水により膨潤する樹脂をいう。また、
親水性の熱可塑性樹脂と他の熱可塑性樹脂とを配合すれ
ば、適宜比重を調整することができ、例えば、流動床と
して用いる場合には、その流動性を向上させることがで
きる。さらに、他の熱可塑性樹脂として、疎水性の熱可
塑性樹脂を用いれば、その疎水性の熱可塑性樹脂が疎水
部分となるので、水の浸入を防止でき、その結果、微生
物による分解を防止することができ、水処理用担体の強
度を保持することができる。By using a thermoplastic resin, it can be molded into an arbitrary shape by melt molding and can be continuously mass-produced. In addition, by using a hydrophilic thermoplastic resin, the initial water absorption is good, and the affinity of microorganisms is high, so that the adhesion and growth of microorganisms can be improved, thereby performing efficient water treatment. be able to. In the present invention, the hydrophilic thermoplastic resin refers to a resin that swells with water. Also,
By blending a hydrophilic thermoplastic resin with another thermoplastic resin, the specific gravity can be appropriately adjusted. For example, when used as a fluidized bed, its fluidity can be improved. Further, if a hydrophobic thermoplastic resin is used as the other thermoplastic resin, the hydrophobic thermoplastic resin becomes a hydrophobic portion, so that water can be prevented from entering, and as a result, decomposition by microorganisms can be prevented. And the strength of the water treatment carrier can be maintained.
【0010】このような親水性の熱可塑性樹脂として
は、例えば、ポリウレタン樹脂、ナイロン樹脂、ポリエ
ステル樹脂、エチレン−ビニルアルコール共重合体、ポ
リカプロラクトン樹脂、乳酸重合体、ポリ(メタ)アク
リル酸樹脂などが挙げられる。また、他の熱可塑性樹脂
としては、疎水性の熱可塑性樹脂、例えば、ポリエチレ
ン樹脂、ポリプロピレン樹脂、ポリ酢酸ビニル樹脂、ポ
リアセタール樹脂、アクリロニトリル−ブタジエン−ス
チレン(ABS)樹脂、アクリロニトリル−スチレン
(AS)樹脂、ポリ塩化ビニル樹脂、ポリカーボネート
樹脂、ポリエチレンポリプロピレン共重合体、ポリ塩化
ビニリデン樹脂などが挙げられる。Examples of such a hydrophilic thermoplastic resin include polyurethane resin, nylon resin, polyester resin, ethylene-vinyl alcohol copolymer, polycaprolactone resin, lactic acid polymer and poly (meth) acrylic resin. Is mentioned. Other thermoplastic resins include hydrophobic thermoplastic resins such as polyethylene resin, polypropylene resin, polyvinyl acetate resin, polyacetal resin, acrylonitrile-butadiene-styrene (ABS) resin, and acrylonitrile-styrene (AS) resin. , Polyvinyl chloride resin, polycarbonate resin, polyethylene polypropylene copolymer, polyvinylidene chloride resin and the like.
【0011】これらは、単独で使用してもよく、また、
2種類以上併用してもよい。親水性の熱可塑性樹脂と他
の熱可塑性樹脂とを配合する場合には、親水性の熱可塑
性樹脂の割合が、親水性の熱可塑性樹脂と他の熱可塑性
樹脂との合計に対して、5〜99重量%、好ましくは、
10〜95重量%である。好ましくは、親水性のポリウ
レタン樹脂、および、親水性のポリウレタン樹脂に他の
熱可塑性樹脂を配合したものが挙げられる。These may be used alone,
Two or more types may be used in combination. When blending a hydrophilic thermoplastic resin with another thermoplastic resin, the ratio of the hydrophilic thermoplastic resin is 5% of the total of the hydrophilic thermoplastic resin and the other thermoplastic resin. ~ 99% by weight, preferably
10 to 95% by weight. Preferably, a hydrophilic polyurethane resin or a mixture of a hydrophilic polyurethane resin and another thermoplastic resin is used.
【0012】なお、親水性のポリウレタン樹脂は、通
常、ポリオキシエチレンなどの親水性ユニットを含むも
のであるが、親水性のポリウレタン樹脂中には、ポリオ
キシエチレンなどの親水性ユニットと、ポリオキシプロ
ピレンおよび/またはポリオキシブチレンなどの疎水性
ユニットとを含んでいることが好ましい。親水性のポリ
ウレタン樹脂中に、親水性ユニットと疎水性ユニットと
を含むことで、親水性ユニットによって、初期の吸水性
を向上させて、微生物の親和性を高めて、微生物の付着
および増殖を向上させる一方で、疎水性ユニットによっ
て、長期の使用によっても、微生物により分解されにく
くし、強度を保持して、安定した使用を確保することが
できる。また、親水性ユニットと疎水性ユニットとを含
む場合には、その合計に対して、親水性ユニットの割合
が、10〜95重量%、さらには、20〜90重量%で
あることが好ましい。The hydrophilic polyurethane resin usually contains a hydrophilic unit such as polyoxyethylene. In the hydrophilic polyurethane resin, a hydrophilic unit such as polyoxyethylene, polyoxypropylene and And / or a hydrophobic unit such as polyoxybutylene. By including a hydrophilic unit and a hydrophobic unit in the hydrophilic polyurethane resin, the hydrophilic unit improves the initial water absorption, increases the affinity of microorganisms, and improves the adhesion and growth of microorganisms. On the other hand, the hydrophobic unit makes it difficult for microorganisms to decompose even after long-term use, maintains strength, and ensures stable use. When the hydrophilic unit and the hydrophobic unit are contained, the ratio of the hydrophilic unit to the total is preferably 10 to 95% by weight, more preferably 20 to 90% by weight.
【0013】また、本発明の水処理用担体には、基質吸
着物質、および/または、酵素活性を向上させるあるい
は生育促進する物質を含有させることが好ましい。これ
らを含有させることで、水処理用担体の表面に、より一
層、容易に微生物を付着および増殖させることができ、
さらに効率的な水処理を行なうことができる。The water treatment carrier of the present invention preferably contains a substrate adsorbing substance and / or a substance which improves enzyme activity or promotes growth. By containing these, the microorganisms can be more easily attached and grown on the surface of the water treatment carrier,
Further efficient water treatment can be performed.
【0014】このような基質吸着物質としては、例え
ば、自然石を含む天然セラミックス、人工セラミック
ス、活性炭、カーボンブラック、ケイ酸塩化合物などが
挙げられる。これらは、単独で使用してもよく、また、
2種類以上併用してもよい。好ましくは、活性炭、カー
ボンブラックが挙げられる。また、基質吸着物質を配合
する割合は、例えば、熱可塑性樹脂100重量部に対し
て、0.1〜40重量部、好ましくは、0.5〜30重
量部である。Examples of such a substrate adsorbing substance include natural ceramics containing natural stone, artificial ceramics, activated carbon, carbon black, silicate compounds and the like. These may be used alone,
Two or more types may be used in combination. Preferably, activated carbon and carbon black are used. The proportion of the substrate adsorbing substance is, for example, 0.1 to 40 parts by weight, or preferably 0.5 to 30 parts by weight, per 100 parts by weight of the thermoplastic resin.
【0015】また、酵素活性を向上させるあるいは生育
促進する物質としては、例えば、銅や亜鉛などの金属
や、そのような金属の、水に不溶あるいは難溶の塩、酸
化物、硫化物、水酸化物など、さらには、そのような金
属または金属化合物に、無機物および/または有機物が
含有されているものなどが挙げられる。これらは、単独
で使用してもよく、また、2種類以上併用してもよい。
好ましくは、酸化銅、硫化銅、水酸化銅が挙げられる。
また、酵素活性を向上させるあるいは生育促進する物質
を配合する割合は、例えば、熱可塑性樹脂100重量部
に対して、0.005〜5重量部、好ましくは、0.0
1〜3重量部である。Examples of the substance which enhances the enzyme activity or promotes growth include metals such as copper and zinc, and salts, oxides, sulfides, and water-insoluble or poorly-soluble salts of such metals in water. Examples thereof include oxides and the like, and those in which an inorganic substance and / or an organic substance are contained in such a metal or a metal compound. These may be used alone or in combination of two or more.
Preferably, copper oxide, copper sulfide, and copper hydroxide are used.
The proportion of the substance that improves the enzyme activity or promotes the growth is, for example, 0.005 to 5 parts by weight, preferably 0.05 parts by weight, per 100 parts by weight of the thermoplastic resin.
1 to 3 parts by weight.
【0016】なお、基質吸着物質や、酵素活性を向上さ
せるあるいは生育促進する物質は、例えば、マスターバ
ッチとして調製されていてもよい。The substance adsorbed on the substrate or the substance which improves the enzyme activity or promotes the growth may be prepared, for example, as a master batch.
【0017】そして、本発明の水処理用担体は、例え
ば、親水性の熱可塑性樹脂、または、親水性の熱可塑性
樹脂および1種以上の他の熱可塑性樹脂、および、必要
により、基質吸着物質、および/または、酵素活性を向
上させるあるいは生育促進する物質を配合して、発泡剤
とともに、例えば、押出成形機などの公知の溶融成形機
によって、押出成形などの公知の溶融成形法によって成
形することにより得ることができる。なお、押出成形で
は、例えば、2種類以上の熱可塑性樹脂を、2種類以上
の仕切られたダイから同時に引き出し、形状が自由に成
形できる、いわゆる共押出成形を行なってもよい。な
お、このような成形条件としては、例えば、押出成形の
場合では、単軸押出のスクリュー径50mmφにおいて
は、吐出量が5〜35kg/hr、スクリューの回転数
が10〜80min-1、ダイの温度が130〜230℃
である。また、成形する形状は、例えば、流動床として
用いる場合には、粒状、球状、円柱状、円筒状、俵状、
米粒状、ラグビーボール状など、任意の形状に成形すれ
ばよい。また、そのサイズも適宜選択され、例えば、1
〜50mm程度のものが好ましい。The carrier for water treatment of the present invention comprises, for example, a hydrophilic thermoplastic resin, or a hydrophilic thermoplastic resin and at least one other thermoplastic resin, and if necessary, a substrate adsorbing substance. And / or a substance that improves the enzyme activity or promotes the growth of the enzyme is blended, and molded together with the foaming agent by a known melt molding method such as extrusion molding by a known melt molding machine such as an extruder. Can be obtained. In the extrusion molding, for example, so-called co-extrusion molding in which two or more kinds of thermoplastic resins can be simultaneously drawn out from two or more kinds of partitioned dies and freely shaped can be performed. In addition, as such molding conditions, for example, in the case of extrusion molding, when the screw diameter of single screw extrusion is 50 mmφ, the discharge rate is 5 to 35 kg / hr, the number of rotations of the screw is 10 to 80 min −1 , Temperature is 130-230 ° C
It is. Further, the shape to be molded, for example, when used as a fluidized bed, granular, spherical, cylindrical, cylindrical, bales,
What is necessary is just to shape into arbitrary shapes, such as a rice grain shape and a rugby ball shape. Also, the size is appropriately selected.
Those having a size of about 50 mm are preferable.
【0018】また、溶融成形後、成形物をダイから吐出
させた後に、水中カット、ホットカット、ミストカット
などのカット方法でカットしてもよい。例えば、水中カ
ットやホットカットにより、その内部を多孔質化しつ
つ、表面をスキン層とすることもできる。After the melt molding, the molded product may be discharged from a die and then cut by a cutting method such as underwater cutting, hot cutting, and mist cutting. For example, the surface can be made into a skin layer while the inside thereof is made porous by underwater cutting or hot cutting.
【0019】用いられる発泡剤としては、例えば、通常
使用される、化学的発泡剤や物理的発泡剤などが挙げら
れる。化学的発泡剤としては、例えば、アゾ化合物(例
えば、アゾジカルボンアミド(ADCA)、バリウムア
ゾジカルボキシレート(Ba/AC)など)、ニトロソ
化合物(例えば、N,N−ジニトロソペンタメチレンテ
トラミン(DPT)など)、ヒドラジン誘導体(例え
ば、4,4’−オキシビス(ベンゼンスルホニルヒドラ
ジド)(OBSH)など)、セミカルバジド化合物、ア
ジド化合物、トリアゾール化合物、イソシアネート化合
物、重炭酸塩(例えば、重炭酸ナトリウムなど)、炭酸
塩、亜硝酸塩、水素化物、重炭酸ナトリウムと酸の混合
物(例えば、重炭酸ナトリウムとクエン酸など)、過酸
化水素と酵母との混合物、亜鉛粉末と酸との混合物など
が挙げられる。Examples of the foaming agent to be used include, for example, commonly used chemical foaming agents and physical foaming agents. As the chemical foaming agent, for example, azo compounds (eg, azodicarbonamide (ADCA), barium azodicarboxylate (Ba / AC), etc.), nitroso compounds (eg, N, N-dinitrosopentamethylenetetramine (DPT)) ), Hydrazine derivatives (e.g., 4,4'-oxybis (benzenesulfonylhydrazide) (OBSH), etc.), semicarbazide compounds, azide compounds, triazole compounds, isocyanate compounds, bicarbonates (e.g., sodium bicarbonate, etc.), Examples include carbonate, nitrite, hydride, a mixture of sodium bicarbonate and an acid (for example, sodium bicarbonate and citric acid), a mixture of hydrogen peroxide and yeast, a mixture of zinc powder and an acid, and the like.
【0020】また、物理発泡剤としては、例えば、脂肪
族炭化水素類(例えば、ブタン、ペンタン、ヘキサンな
ど)、塩化炭化水素類(例えば、ジクロロエタン、ジク
ロロメタンなど)、フッ化塩化炭化水素類(例えば、ト
リクロロモノフロロメタン、ジクロロジフロロメタン、
ジクロロモノフロロメタン、ジクロロテトラフロロエタ
ンなど)、代替フロン類、空気、炭酸ガス、窒素ガス、
水などが挙げられる。これらは、単独で使用してもよ
く、また、2種類以上併用してもよい。好ましくは、A
DCA、OBSH、重炭酸ナトリウムと酸の混合物が挙
げられる。Examples of the physical foaming agent include aliphatic hydrocarbons (eg, butane, pentane, hexane, etc.), chlorinated hydrocarbons (eg, dichloroethane, dichloromethane, etc.), fluorinated hydrocarbons (eg, , Trichloromonofluoromethane, dichlorodifluoromethane,
Dichloromonofluoromethane, dichlorotetrafluoroethane, etc.), alternative fluorocarbons, air, carbon dioxide, nitrogen gas,
Water. These may be used alone or in combination of two or more. Preferably, A
DCA, OBSH, a mixture of sodium bicarbonate and an acid.
【0021】また、発泡剤を配合する割合は、例えば、
熱可塑性樹脂100重量部に対して、0.01〜20重
量部、好ましくは、0.05〜15重量部である。な
お、これら発泡剤は、例えば、マスターバッチとして調
製されていてもよい。The mixing ratio of the foaming agent is, for example, as follows:
It is 0.01 to 20 parts by weight, preferably 0.05 to 15 parts by weight, based on 100 parts by weight of the thermoplastic resin. In addition, these foaming agents may be prepared as a master batch, for example.
【0022】このようにして得られる本発明の水処理用
担体は、発泡剤によって成形時に多孔質化されるので、
その用いる発泡剤の配合量を加減してその水処理用担体
の空孔率(ポロシティまたは気孔率ともいう)を適宜選
択することにより、水処理用担体の比重を調整すること
ができ、その結果、例えば、流動床として用いた場合に
おける、流動性の向上を図ることができる。また、多孔
質化することにより、その表面には、通常、凹凸状の細
孔が形成されるので、これによって、その表面に、微生
物を付着させやすくすることができ、さらに効率的な水
処理を行なうことができる。しかも、熱可塑性樹脂に炭
酸カルシウムや硫酸バリウムなどの充填剤を配合する場
合などに比べて、摩耗および損傷が少なく、耐久性の向
上を図ることができる。The water treatment carrier of the present invention thus obtained is made porous at the time of molding by a foaming agent.
The specific gravity of the water treatment carrier can be adjusted by adjusting the amount of the foaming agent to be used and appropriately selecting the porosity (also referred to as porosity or porosity) of the water treatment carrier. For example, when used as a fluidized bed, fluidity can be improved. In addition, by making the surface porous, irregular pores are usually formed on the surface, so that microorganisms can be easily attached to the surface, and more efficient water treatment can be achieved. Can be performed. Moreover, as compared with the case where a filler such as calcium carbonate or barium sulfate is blended with the thermoplastic resin, wear and damage are reduced and durability can be improved.
【0023】なお、このような発泡剤を用いる場合に
は、その比重が、水の比重(1.0)に近い、0.93
〜1.15の範囲、好ましくは、0.97〜1.05の
範囲、さらに好ましくは、0.98〜1.03の範囲と
なるように、その空孔率を20〜90%、さらには、2
0〜80%とすることが好ましい。また、多孔質化は、
連続気泡であっても独立気泡であってもよく、例えば、
独立気泡である場合には、その気泡のサイズが、1〜3
000μm、さらには、10〜2000μmであること
が好ましい。When such a foaming agent is used, its specific gravity is 0.93, which is close to the specific gravity of water (1.0).
To 1.15, preferably 0.97 to 1.05, more preferably 0.98 to 1.03, so that the porosity is 20 to 90%, , 2
It is preferably set to 0 to 80%. In addition, making porous
It may be an open cell or a closed cell, for example,
When the cells are closed cells, the size of the cells is 1 to 3
000 μm, more preferably 10 to 2000 μm.
【0024】このようにして得られる本発明の水処理用
担体は、各種の水処理、例えば、産業廃水や生活廃水な
どの廃水処理などに用いることができ、より具体的に
は、微生物を用いた水処理、例えば、硝化菌(例えば、
アンモニア酸化菌、亜硝酸酸化菌など)などの好気性微
生物により処理するための好気槽、脱窒菌などの嫌気性
微生物により処理するための嫌気槽の、流動床や固定
床、とりわけ、流動床として用いることができる。図1
には、そのような水処理装置の一実施形態が示されてい
る。すなわち、図1において、この水処理装置は、好気
槽や嫌気槽として用いられる水処理槽1と、この水処理
槽1に接続される給水管2および排水管3とを備えてい
る。水処理槽1には、本発明の水処理用担体4が流動床
として投入されており、水処理槽1内に回転可能に設け
られる攪拌機5によって、攪拌されている。このような
水処理装置には、多孔質化されることにより比重が調整
される水処理用担体4が、流動床として用いられている
ので、水処理槽1内において、この水処理用担体4が、
良好に浮上および沈降することにより、効率的な水処理
を行なうことができる。The carrier for water treatment of the present invention thus obtained can be used for various kinds of water treatment, for example, wastewater treatment such as industrial wastewater and domestic wastewater, and more specifically, microorganisms. Water treatment, for example, nitrifying bacteria (eg,
Aerobic tank for treatment with aerobic microorganisms such as ammonia oxidizing bacteria and nitrite oxidizing bacteria) and anaerobic tank for treating with anaerobic microorganisms such as denitrifying bacteria. Can be used. FIG.
Shows an embodiment of such a water treatment device. That is, in FIG. 1, the water treatment apparatus includes a water treatment tank 1 used as an aerobic tank or an anaerobic tank, and a water supply pipe 2 and a drain pipe 3 connected to the water treatment tank 1. The water treatment carrier 4 of the present invention is charged into the water treatment tank 1 as a fluidized bed, and is stirred by a stirrer 5 rotatably provided in the water treatment tank 1. In such a water treatment apparatus, the water treatment carrier 4 whose specific gravity is adjusted by being made porous is used as a fluidized bed. But,
By effectively floating and settling, efficient water treatment can be performed.
【0025】なお、本発明の水処理用担体は、上記した
ように、本来、水処理に用いられるものであるが、気相
での処理、例えば、アンモニア、硫化水素などの脱臭に
用いることもできる。The carrier for water treatment of the present invention is originally used for water treatment as described above, but it can also be used for treatment in the gas phase, for example, for deodorization of ammonia, hydrogen sulfide and the like. it can.
【0026】[0026]
【実施例】以下に実施例および比較例を示し本発明をさ
らに具体的に説明するが、本発明は、何ら実施例および
比較例に限定されることはない。The present invention will be described in more detail with reference to Examples and Comparative Examples, but the present invention is not limited to Examples and Comparative Examples.
【0027】実施例1 親水性の熱可塑性ポリウレタン樹脂(ジフェニルメタン
ジイソシアネート/ポリオキシエチレンプロピレングリ
コール(エチレンオキサイド含量80重量%)80重量
部とポリテトラメチレングリコール20重量部との混合
物/1,4−ブタンジオール、商品名:エラストラン
OH3−37、武田バーディシェウレタン工業社製、以
下同じ)100重量部に、発泡剤(ポリエチレン樹脂6
0重量%、重炭酸ナトリウムとクエン酸との混合物40
重量%のマスターバッチ、商品名:ハイドロセロール−
CF40E、ベーリンガーインゲルハイム社製、以下同
じ)0.5重量部を添加し、押出成形機(50mmφ単
軸押出機、L/D=34、池貝社製) を使用して成形
し、外径3mmφ、長さ3mmの円柱状の担体を得た。Example 1 A mixture of 80 parts by weight of a hydrophilic thermoplastic polyurethane resin (diphenylmethane diisocyanate / polyoxyethylene propylene glycol (ethylene oxide content: 80% by weight) and 20 parts by weight of polytetramethylene glycol / 1,4-butane) Diol, trade name: Elastolane
OH3-37, 100 parts by weight of Takeda Birdish Urethane Industry Co., Ltd .;
0% by weight, a mixture of sodium bicarbonate and citric acid 40
Wt% masterbatch, trade name: Hydrocerol-
0.5 part by weight of CF40E, manufactured by Boehringer Ingelheim Co., Ltd .; the same applies hereinafter), and molded using an extruder (50 mmφ single screw extruder, L / D = 34, manufactured by Ikegai Co., Ltd.), and an outer diameter of 3 mmφ To obtain a columnar carrier having a length of 3 mm.
【0028】実施例2 親水性の熱可塑性ポリウレタン樹脂100重量部に、発
泡剤1.0重量部を添加し、押出成形機(50mmφ単
軸押出機、L/D=34、池貝社製) を使用して成形
し、外径3mmφ、長さ3mmの円柱状の担体を得た。Example 2 1.0 part by weight of a foaming agent was added to 100 parts by weight of a hydrophilic thermoplastic polyurethane resin, and an extruder (50 mmφ single screw extruder, L / D = 34, manufactured by Ikegai Co., Ltd.) was used. Then, a cylindrical carrier having an outer diameter of 3 mmφ and a length of 3 mm was obtained.
【0029】実施例3 親水性の熱可塑性ポリウレタン樹脂100重量部に、発
泡剤2.5重量部を添加し、押出成形機(50mmφ単
軸押出機、L/D=34、池貝社製) を使用して成形
し、外径3mmφ、長さ3mmの円柱状の担体を得た。Example 3 2.5 parts by weight of a foaming agent was added to 100 parts by weight of a hydrophilic thermoplastic polyurethane resin, and an extruder (50 mmφ single screw extruder, L / D = 34, manufactured by Ikegai Co., Ltd.) was used. Then, a cylindrical carrier having an outer diameter of 3 mmφ and a length of 3 mm was obtained.
【0030】実施例4 親水性の熱可塑性ポリウレタン樹脂と、ポリエチレン樹
脂(商品名:エボリュー SP0510、三井化学社
製、以下同じ)とが、重量比で8/2の割合で配合され
る混合物100重量部に、発泡剤1.5重量部を添加
し、押出成形機(50mmφ単軸押出機、L/D=3
4、池貝社製) を使用して成形し、外径3mmφ、長さ
3mmの円柱状の担体を得た。Example 4 100 parts by weight of a mixture in which a hydrophilic thermoplastic polyurethane resin and a polyethylene resin (trade name: Evolue SP0510, manufactured by Mitsui Chemicals, same hereafter) are mixed in a weight ratio of 8/2. Parts, a foaming agent (1.5 parts by weight) was added, and an extruder (50 mmφ single screw extruder, L / D = 3
4, Ikegai Co., Ltd.) to obtain a columnar carrier having an outer diameter of 3 mm and a length of 3 mm.
【0031】実施例5 親水性の熱可塑性ポリウレタン樹脂と、ポリエチレン樹
脂とが、重量比で8/2の割合で配合される混合物10
0重量部に、発泡剤3.0重量部を添加し、押出成形機
(50mmφ単軸押出機、L/D=34、池貝社製) を
使用して成形し、外径3mmφ、長さ3mmの円柱状の
担体を得た。Example 5 A mixture 10 in which a hydrophilic thermoplastic polyurethane resin and a polyethylene resin are blended at a weight ratio of 8/2.
0 parts by weight, 3.0 parts by weight of a foaming agent were added, and the mixture was molded using an extruder (50 mmφ single screw extruder, L / D = 34, manufactured by Ikegai Co., Ltd.) to have an outer diameter of 3 mmφ and a length of 3 mm. Was obtained.
【0032】実施例6 親水性の熱可塑性ポリウレタン樹脂と、ポリエチレン樹
脂とが、重量比で8/2の割合で配合される混合物10
0重量部に、発泡剤0.1重量部を添加し、押出成形機
(50mmφ単軸押出機、L/D=34、池貝社製) を
使用して成形し、外径4mmφ、内径2mmφ、長さ3
mmの円筒状の担体を得た。Example 6 A mixture 10 in which a hydrophilic thermoplastic polyurethane resin and a polyethylene resin were blended at a weight ratio of 8/2.
0.1 parts by weight of a foaming agent is added to 0 parts by weight, and the mixture is molded using an extruder (50 mmφ single screw extruder, L / D = 34, manufactured by Ikegai Co., Ltd.) to obtain an outer diameter of 4 mmφ, an inner diameter of 2 mmφ, Length 3
mm was obtained.
【0033】実施例7 親水性の熱可塑性ポリウレタン樹脂と、ポリエチレン樹
脂とが、重量比で8/2の割合で配合される混合物10
0重量部に、発泡剤0.3重量部を添加し、押出成形機
(50mmφ単軸押出機、L/D=34、池貝社製) を
使用して成形し、外径4mmφ、内径2mmφ、長さ3
mmの円筒状の担体を得た。Example 7 A mixture 10 in which a hydrophilic thermoplastic polyurethane resin and a polyethylene resin were blended at a weight ratio of 8/2.
0 parts by weight, 0.3 parts by weight of a foaming agent are added, and the mixture is molded using an extruder (50 mmφ single screw extruder, L / D = 34, manufactured by Ikegai Co., Ltd.) to obtain an outer diameter of 4 mmφ, an inner diameter of 2 mmφ, Length 3
mm was obtained.
【0034】実施例8 親水性の熱可塑性ポリウレタン樹脂と、ポリエチレン樹
脂とが、重量比で8/2の割合で配合される混合物10
0重量部に、発泡剤0.7重量部を添加し、押出成形機
(50mmφ単軸押出機、L/D=34、池貝社製) を
使用して成形し、外径4mmφ、内径2mmφ、長さ3
mmの円筒状の担体を得た。Example 8 A mixture 10 in which a hydrophilic thermoplastic polyurethane resin and a polyethylene resin were blended at a weight ratio of 8/2.
To 0 parts by weight, 0.7 parts by weight of a foaming agent was added, and the mixture was molded using an extruder (50 mmφ single screw extruder, L / D = 34, manufactured by Ikegai Co., Ltd.) to obtain an outer diameter of 4 mmφ, an inner diameter of 2 mmφ, Length 3
mm was obtained.
【0035】実施例9 親水性の熱可塑性ポリウレタン樹脂と、ポリエチレン樹
脂とが、重量比で8/2の割合で配合される混合物10
0重量部に、発泡剤0.5重量部を添加し、押出成形機
(90mmφ単軸押出機、L/D=34、池貝社製) を
使用して成形し、ダイからの吐出直後に水中カッター
(Gala社製、以下同じ)を使用して、水中カットす
ることにより、4mmφの球状の担体を得た。Example 9 A mixture 10 in which a hydrophilic thermoplastic polyurethane resin and a polyethylene resin were blended at a weight ratio of 8/2.
0 parts by weight, 0.5 part by weight of a foaming agent is added, and molded using an extruder (90 mmφ single screw extruder, L / D = 34, manufactured by Ikegai Co., Ltd.). Using a cutter (manufactured by Gala, the same applies hereinafter), underwater cutting was performed to obtain a 4 mmφ spherical carrier.
【0036】実施例10 親水性の熱可塑性ポリウレタン樹脂と、ポリエチレン樹
脂とが、重量比で8/2の割合で配合される混合物10
0重量部に、発泡剤2.0重量部を添加し、押出成形機
(90mmφ単軸押出機、L/D=34、池貝社製) を
使用して成形し、ダイからの吐出直後に水中カッターを
使用して、水中カットすることにより、4mmφの球状
の担体を得た。Example 10 A mixture 10 in which a hydrophilic thermoplastic polyurethane resin and a polyethylene resin were blended at a weight ratio of 8/2.
0 parts by weight, 2.0 parts by weight of a foaming agent are added, and the mixture is molded using an extruder (90 mmφ single screw extruder, L / D = 34, manufactured by Ikegai Co., Ltd.). Using a cutter, underwater cutting was performed to obtain a 4 mmφ spherical carrier.
【0037】実施例11 親水性の熱可塑性ポリウレタン樹脂と、ポリエチレン樹
脂とが、重量比で8/2の割合で配合される混合物10
0重量部に、発泡剤4.0重量部を添加し、押出成形機
(90mmφ単軸押出機、L/D=34、池貝社製) を
使用して成形し、ダイからの吐出直後に水中カッターを
使用して、水中カットすることにより、4mmφの球状
の担体を得た。Example 11 A mixture 10 in which a hydrophilic thermoplastic polyurethane resin and a polyethylene resin were blended at a weight ratio of 8/2.
0 parts by weight, 4.0 parts by weight of a foaming agent were added, and the mixture was molded using an extruder (90 mmφ single screw extruder, L / D = 34, manufactured by Ikegai Co., Ltd.). Using a cutter, underwater cutting was performed to obtain a 4 mmφ spherical carrier.
【0038】実施例12 親水性の熱可塑性ポリウレタン樹脂と、ポリエチレン樹
脂とが、重量比で8/2の割合で配合される混合物10
0重量部に、発泡剤6.0重量部を添加し、押出成形機
(90mmφ単軸押出機、L/D=34、池貝社製) を
使用して成形し、ダイからの吐出直後に水中カッターを
使用して、水中カットすることにより、4mmφの球状
の担体を得た。Example 12 A mixture 10 in which a hydrophilic thermoplastic polyurethane resin and a polyethylene resin were blended at a weight ratio of 8/2.
0 parts by weight, 6.0 parts by weight of a foaming agent were added, and the mixture was molded using an extruder (90 mmφ single screw extruder, L / D = 34, manufactured by Ikegai Co., Ltd.). Using a cutter, underwater cutting was performed to obtain a 4 mmφ spherical carrier.
【0039】実施例13 親水性の熱可塑性ポリウレタン樹脂と、ポリエチレン樹
脂とが、重量比で8/2の割合で配合される混合物10
0重量部に、発泡剤3.0重量部、硫化銅(和光純薬社
製、以下同じ)0.1重量部、活性炭(商品名:DO−
5、武田薬品工業社製、以下同じ) 3.0重量部を添加
し、押出成形機(50mmφ単軸押出機、L/D=3
4、池貝社製) を使用して成形し、外径3mmφ、長さ
3mmの円柱状の担体を得た。Example 13 A mixture 10 in which a hydrophilic thermoplastic polyurethane resin and a polyethylene resin were blended at a weight ratio of 8/2.
0 parts by weight, 3.0 parts by weight of a foaming agent, 0.1 parts by weight of copper sulfide (manufactured by Wako Pure Chemical Industries, Ltd., the same applies hereinafter), activated carbon (trade name: DO-
5, Takeda Pharmaceutical Co., Ltd .; the same applies hereinafter) 3.0 parts by weight, and an extruder (50 mmφ single screw extruder, L / D = 3)
4, Ikegai Co., Ltd.) to obtain a columnar carrier having an outer diameter of 3 mm and a length of 3 mm.
【0040】実施例14 親水性の熱可塑性ポリウレタン樹脂と、ポリエチレン樹
脂とが、重量比で8/2の割合で配合される混合物10
0重量部に、発泡剤6.0重量部、硫化銅0.1重量
部、活性炭3.0重量部を添加し、押出成形機(90m
mφ単軸押出機、L/D=34、池貝社製) を使用して
成形し、ダイからの吐出直後に水中カッターを使用し
て、水中カットすることにより、4mmφの球状の担体
を得た。Example 14 A mixture 10 in which a hydrophilic thermoplastic polyurethane resin and a polyethylene resin were blended at a weight ratio of 8/2.
To 0 parts by weight, 6.0 parts by weight of a foaming agent, 0.1 parts by weight of copper sulfide, and 3.0 parts by weight of activated carbon were added, and an extruder (90 m
mφ single screw extruder, L / D = 34, manufactured by Ikegai Co., Ltd.), and cut underwater using a submerged cutter immediately after discharging from the die to obtain a 4 mmφ spherical carrier. .
【0041】比較例1 ポリエーテルポリオール(ソルビトール開始剤のエチレ
ンオキサイド付加物、商品名:MF−43、武田薬品工
業社製、)85重量部、ポリマーポリオール(グリセリ
ン開始剤のプロピレンオキサイド/エチレンオキサイド
付加物と、アクリロニトリル−スチレンポリマーとから
なるポリマーポリオール、商品名:POP−93、武田
薬品工業社製)15重量部、脱イオン水3重量部、ジメ
チルシロキサン(和光純薬社製)1重量部、トリレンジ
イソシアネート(2,4体/80重量%、2,6体/2
0重量%、武田薬品工業社製)15重量部を、常法に従
い反応させて、親水性のポリウレタンフォームを合成
し、これを、5mm角に裁断することにより、ポリウレ
タンフォームからなる5mm角の担体を得た。Comparative Example 1 85 parts by weight of polyether polyol (ethylene oxide adduct of sorbitol initiator, trade name: MF-43, manufactured by Takeda Pharmaceutical Co., Ltd.), polymer polyol (propylene oxide / ethylene oxide addition of glycerin initiator) And a polymer polyol comprising an acrylonitrile-styrene polymer, trade name: POP-93, manufactured by Takeda Pharmaceutical Co., Ltd.) 15 parts by weight, deionized water 3 parts by weight, dimethylsiloxane (manufactured by Wako Pure Chemical Industries, Ltd.) 1 part by weight, Tolylene diisocyanate (2,4 units / 80% by weight, 2,6 units / 2
(0% by weight, manufactured by Takeda Pharmaceutical Co., Ltd.) 15 parts by weight were reacted according to a conventional method to synthesize a hydrophilic polyurethane foam, which was cut into a 5 mm square to form a 5 mm square carrier made of a polyurethane foam. I got
【0042】比較例2 ポリエチレン樹脂と炭酸カルシウムとを、その比重が
1.02となるように配合した混合物100重量部を、
押出成形機(50mmφ単軸押出機、L/D=34、池
貝社製) を使用して成形し、外径4mmφ、内径2mm
φ、長さ3mmの円筒状の担体を得た。Comparative Example 2 100 parts by weight of a mixture of a polyethylene resin and calcium carbonate so that the specific gravity thereof was 1.02 was
Molded using an extruder (50 mmφ single screw extruder, L / D = 34, manufactured by Ikegai Co., Ltd.), outer diameter 4 mmφ, inner diameter 2 mm
A cylindrical carrier having a diameter of φ and a length of 3 mm was obtained.
【0043】試験例1 実施例1〜12の担体を、80℃の熱風乾燥機で5時間
乾燥し、乾燥した担体100gをイオン交換水1Lに投
入し膨潤させることにより、重量比(膨潤重量/乾燥重
量)および比重(1Lの水に膨潤した担体を体積で10
0mL添加した時の流量を測定し計算した。)を測定し
た。なお、その内部に空気が残る場合には、減圧にして
気泡を取り除いた。その結果を表1に示す。Test Example 1 The carriers of Examples 1 to 12 were dried in a hot air drier at 80 ° C. for 5 hours, and 100 g of the dried carriers were poured into 1 L of ion-exchanged water and allowed to swell, whereby the weight ratio (swelling weight / (Dry weight) and specific gravity (10% by volume of the carrier swollen in 1 L of water)
The flow rate when 0 mL was added was measured and calculated. ) Was measured. If air remains in the interior, the pressure was reduced to remove air bubbles. Table 1 shows the results.
【0044】[0044]
【表1】 [Table 1]
【0045】表1から、発泡剤の量を変化させることに
よって、比重を調整できることがわかる。Table 1 shows that the specific gravity can be adjusted by changing the amount of the foaming agent.
【0046】試験例2 実施例5、12、13、14、および、比較例1、2で
得られた担体を活性汚泥に浸漬し、微生物を吸着させ
た。すなわち、嵩体積250mLの担体をドラフト流式
水槽5Lに投入し、以下に示す組成をもつ無機人工廃水
を使用し、水温20℃、pH7.0〜7.5、水理学的
滞留時間5時間の条件で、亜硝酸生成量から算出したア
ンモニア酸化速度を求めることで評価した。Test Example 2 The carriers obtained in Examples 5, 12, 13, 14 and Comparative Examples 1 and 2 were immersed in activated sludge to adsorb microorganisms. That is, a carrier having a bulk volume of 250 mL is put into 5 L of a draft flow water tank, and an inorganic artificial wastewater having the composition shown below is used. The water temperature is 20 ° C., the pH is 7.0 to 7.5, and the hydraulic retention time is 5 hours. The conditions were evaluated by obtaining the ammonia oxidation rate calculated from the amount of generated nitrous acid.
【0047】 無機人工廃水組成(1Lあたり) (NH4 )2 SO4 0.0943g KH2 PO4 0.6g NaHCO3 0.375g MgSO4 ・7H2 O 10mg CaCl2 ・2H2 O 1.8mg Fe−EDTA 1mg 実施例5、12、13、14、および、比較例1、2の
担体にアンモニア酸化細菌を付着させ評価した結果を図
2に示す。なお、比較例1の担体は、試験開始直後に気
泡が付着して浮上してしまい、評価ができなかった。そ
のため、図2では、比較例1の結果を省略して示す。図
2において、実施例5、12、13、14の担体は、そ
の比重が1.02〜1.03と水に近いことから流動性
が良く、また、親水性のポリウレタン樹脂が配合されて
いるので、菌が良好に付着し増殖して、アンモニア酸化
速度が良好に上昇していることがわかる。一方、比較例
2の担体は、その比重が1.02と水に近いが、疎水性
であるため菌の付着が不良であり、実施例5、12、1
3、14に比べてアンモニア酸化速度が上昇していない
ことがわかる。また、基質吸着物質、および、酵素活性
を向上させるあるいは生育促進する物質を含有している
実施例13、14は、アンモニア酸化速度の立ち上りが
速く、しかも最大活性が高くなっていることがわかる。[0047] Inorganic artificial wastewater composition (per 1L) (NH 4) 2 SO 4 0.0943g KH 2 PO 4 0.6g NaHCO 3 0.375g MgSO 4 · 7H 2 O 10mg CaCl 2 · 2H 2 O 1.8mg Fe -EDTA 1 mg FIG. 2 shows the results of attaching ammonia oxidizing bacteria to the carriers of Examples 5, 12, 13, 14 and Comparative Examples 1 and 2, and evaluating the results. In the carrier of Comparative Example 1, air bubbles adhered and floated immediately after the start of the test, and the carrier could not be evaluated. Therefore, in FIG. 2, the result of Comparative Example 1 is omitted. In FIG. 2, the carriers of Examples 5, 12, 13, and 14 have good fluidity due to their specific gravities of 1.02 to 1.03, which are close to water, and are blended with a hydrophilic polyurethane resin. Therefore, it can be seen that the bacteria adhere and grow well, and the ammonia oxidation rate is satisfactorily increased. On the other hand, the carrier of Comparative Example 2 has a specific gravity of 1.02, which is close to that of water, but has poor adhesion of bacteria due to its hydrophobicity.
It can be seen that the ammonia oxidation rate did not increase as compared with 3 and 14. In addition, it can be seen that in Examples 13 and 14 containing the substrate adsorbing substance and the substance that improves the enzyme activity or promotes the growth, the ammonia oxidation rate rises quickly and the maximum activity is high.
【0048】また、各担体表面でのアンモニア酸化細菌
の増殖(優占化) を、DNAプローブ法(FISH法)
を用いて評価した。 その結果、実施例5、12、13、
14の担体の表面でアンモニア酸化細菌が増殖し優先化
していることが確認された。観察では、90%がアンモ
ニア酸化細菌であった。The growth (dominance) of ammonia-oxidizing bacteria on the surface of each carrier was determined by the DNA probe method (FISH method).
Was evaluated using As a result, Examples 5, 12, 13,
It was confirmed that ammonia oxidizing bacteria proliferated and prioritized on the surface of the 14 carriers. Observations showed that 90% were ammonia oxidizing bacteria.
【0049】試験例3 実施例12および比較例2で得られた各担体を、嵩体積
で1.0m3 (膨潤時の外径8mmφ、長さ7mmの円
筒形の担体、重量125kg、充填量20%)を用い、
これを5m3 の水槽に投入し、機械攪拌式エアレータ
(出力0.75kw、回転数560〜570、新明和工
業社製)を使用して耐久試験を行なった。Test Example 3 Each of the carriers obtained in Example 12 and Comparative Example 2 was used in an amount of 1.0 m 3 in bulk volume (cylindrical carrier having an outer diameter of 8 mmφ and a length of 7 mm when swollen, a weight of 125 kg, and a filling amount of 20%)
This was put into a 5 m 3 water tank, and a durability test was performed using a mechanically agitated aerator (output: 0.75 kw, rotation speed: 560 to 570, manufactured by Shin-Meiwa Co., Ltd.).
【0050】実施例12の担体は、試験開始から1カ月
経過しても、目視では、変形または損傷しているように
見えなかった。それに対し、比較例2の担体は、試験開
始から1カ月経過した時点で、目視によって、表面が摩
耗しているものや、引き裂けた形状のものが観察され、
また、炭酸カルシウムが水に分散していることが確認さ
れた。また、走査型電子顕微鏡(SEM)により詳細に
観察した結果、実施例12の担体は、摩耗していないの
に対し、比較例2の担体は、全体的に摩耗していること
が確認された。The carrier of Example 12 did not appear to be visually deformed or damaged even after one month from the start of the test. On the other hand, the carrier of Comparative Example 2 was visually observed at one month after the start of the test to have a worn surface or a torn shape,
It was also confirmed that calcium carbonate was dispersed in water. Further, as a result of detailed observation with a scanning electron microscope (SEM), it was confirmed that the carrier of Example 12 was not worn, whereas the carrier of Comparative Example 2 was entirely worn. .
【0051】[0051]
【発明の効果】本発明の水処理用担体は、親水性の熱可
塑性樹脂、または、親水性の熱可塑性樹脂および1種以
上の他の熱可塑性樹脂からなり、多孔質化されているの
で、溶融成形によって任意の形状に成形することができ
るとともに、連続して大量に生産することができ、しか
も、発泡剤によって成形時に多孔質化されるので、その
用いる発泡剤の配合量を加減してその水処理用担体の空
孔率を適宜選択することにより、水処理用担体の比重を
調整することができる。その結果、例えば、流動床とし
て用いた場合における、流動性の向上を図ることができ
る。また、熱可塑性樹脂に炭酸カルシウムや硫酸バリウ
ムなどの充填剤を配合する場合などに比べて、摩耗およ
び損傷が少なく、耐久性の向上を図ることができる。し
かも、親水性の熱可塑性樹脂が用いられることにより、
初期の吸水性がよく、微生物の親和性が高いので、微生
物の付着および増殖を向上させることができ、これによ
って、より一層効率的な水処理を行なうことができる。The water treatment carrier of the present invention is made of a hydrophilic thermoplastic resin or a hydrophilic thermoplastic resin and at least one other thermoplastic resin, and is made porous. It can be molded into any shape by melt molding, can be continuously mass-produced, and is made porous at the time of molding with a foaming agent. The specific gravity of the water treatment carrier can be adjusted by appropriately selecting the porosity of the water treatment carrier. As a result, for example, when used as a fluidized bed, the fluidity can be improved. Further, as compared with the case where a filler such as calcium carbonate or barium sulfate is blended with the thermoplastic resin, wear and damage are reduced and durability can be improved. Moreover, by using a hydrophilic thermoplastic resin,
Since the initial water absorption is good and the affinity of the microorganisms is high, the adhesion and growth of the microorganisms can be improved, whereby more efficient water treatment can be performed.
【0052】また、本発明の水処理用担体に、基質吸着
物質、および/または、酵素活性を向上させるあるいは
生育促進する物質を含有させることで、水処理用担体の
表面に、容易に微生物を付着および増殖させることがで
き、さらに効率的な水処理を行なうことができる。In addition, by allowing the water treatment carrier of the present invention to contain a substrate-adsorbing substance and / or a substance that improves enzyme activity or promotes growth, microorganisms can be easily applied to the surface of the water treatment carrier. It can adhere and proliferate, and can perform more efficient water treatment.
【0053】そして、このような水処理用担体が用いら
れる水処理用装置は、槽内において水処理用担体が良好
に流動するため、効率的な水処理を行なうことができ
る。In the water treatment apparatus using such a water treatment carrier, the water treatment carrier flows well in the tank, so that efficient water treatment can be performed.
【図1】本発明の水処理装置の一実施形態を示す、概略
構成図である。FIG. 1 is a schematic configuration diagram showing one embodiment of a water treatment apparatus of the present invention.
【図2】試験例2の評価結果であって、経過日数に対し
てアンモニア酸化速度がプロットされている図である。FIG. 2 is a diagram showing evaluation results of Test Example 2, in which an ammonia oxidation rate is plotted with respect to elapsed days.
1 水処理槽 2 給水管 3 排水管 4 水処理用担体 5 攪拌機 DESCRIPTION OF SYMBOLS 1 Water treatment tank 2 Water supply pipe 3 Drain pipe 4 Carrier for water treatment 5 Stirrer
───────────────────────────────────────────────────── フロントページの続き Fターム(参考) 4D003 AA13 EA01 EA14 EA15 EA19 EA22 EA24 EA25 EA26 EA30 EA38 EA40 FA10 4D040 BB63 BB82 ──────────────────────────────────────────────────続 き Continued on the front page F term (reference) 4D003 AA13 EA01 EA14 EA15 EA19 EA22 EA24 EA25 EA26 EA30 EA38 EA40 FA10 4D040 BB63 BB82
Claims (5)
の熱可塑性樹脂および1種以上の他の熱可塑性樹脂から
なり、多孔質化されていることを特徴とする、水処理用
担体。1. A water treatment carrier comprising a hydrophilic thermoplastic resin, or a hydrophilic thermoplastic resin and at least one other thermoplastic resin, which is made porous.
の熱可塑性樹脂および1種以上の他の熱可塑性樹脂を、
発泡剤とともに溶融成形することによって得られること
を特徴とする、請求項1に記載の水処理用担体。2. Hydrophilic thermoplastic resin, or hydrophilic thermoplastic resin and one or more other thermoplastic resins,
The water treatment carrier according to claim 1, wherein the carrier is obtained by melt-molding with a blowing agent.
性を向上させるあるいは生育促進する物質を含有してい
ることを特徴とする、請求項1または2に記載の水処理
用担体。3. The water treatment carrier according to claim 1, wherein the carrier for water treatment contains a substance adsorbed on a substrate and / or a substance that improves enzyme activity or promotes growth.
の熱可塑性樹脂および1種以上の他の熱可塑性樹脂を、
発泡剤とともに溶融成形することを特徴とする、水処理
用担体の製造方法。4. The method of claim 1, wherein the hydrophilic thermoplastic resin, or the hydrophilic thermoplastic resin and one or more other thermoplastic resins,
A method for producing a water treatment carrier, comprising melt-forming together with a foaming agent.
の熱可塑性樹脂および1種以上の他の熱可塑性樹脂から
なり、多孔質化されている水処理用担体が用いられてい
ることを特徴とする、水処理用装置。5. A water treatment carrier made of a hydrophilic thermoplastic resin or a hydrophilic thermoplastic resin and at least one other thermoplastic resin, which is made porous. Characteristic device for water treatment.
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JP2007283222A (en) * | 2006-04-18 | 2007-11-01 | Unitika Ltd | Biological treatment carrier |
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JP2022087164A (en) * | 2017-12-13 | 2022-06-09 | 東洋炭素株式会社 | Microbial immobilization carrier |
US11518698B2 (en) | 2017-12-13 | 2022-12-06 | Toyo Tanso Co., Ltd. | Microorganism immobilized carrier |
CN108249564A (en) * | 2018-01-30 | 2018-07-06 | 山西大学 | A kind of preparation method and application method of denitrification solid-state carbon source |
CN108249564B (en) * | 2018-01-30 | 2020-12-25 | 山西大学 | Preparation method and use method of denitrification solid carbon source |
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