JPH05309361A - Porous medium for water treament - Google Patents

Porous medium for water treament

Info

Publication number
JPH05309361A
JPH05309361A JP4137661A JP13766192A JPH05309361A JP H05309361 A JPH05309361 A JP H05309361A JP 4137661 A JP4137661 A JP 4137661A JP 13766192 A JP13766192 A JP 13766192A JP H05309361 A JPH05309361 A JP H05309361A
Authority
JP
Japan
Prior art keywords
medium
wastewater
pollutants
substances
filthy
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
JP4137661A
Other languages
Japanese (ja)
Inventor
Hideyuki Kuwabara
秀行 桑原
Kazuhiko Maruyama
和彦 丸山
Kiyoe Ishikawa
清榮 石川
Toshio Yoshida
俊男 吉田
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.)
Tonen General Sekiyu KK
Original Assignee
Tonen 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 Tonen Corp filed Critical Tonen Corp
Priority to JP4137661A priority Critical patent/JPH05309361A/en
Publication of JPH05309361A publication Critical patent/JPH05309361A/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)
  • Separation Of Suspended Particles By Flocculating Agents (AREA)
  • Filtering Materials (AREA)
  • Physical Water Treatments (AREA)
  • Water Treatment By Sorption (AREA)

Abstract

PURPOSE:To provide a porous medium for water treatment wherein the medium can be used as a fluidizing medium in the case of floatation separation of filthy substances by fine bubbles and also as a solid medium in the case of filtration of the filthy substances and it is not flocculated by being charged with static electricity due to the friction between the media and it can remove the filthy substances well. CONSTITUTION:A porous medium is pelleted by kneading a polar group- containing modified polyolefin. pumiceous band balloon, and hydroxyapatite and extrusion-forming the kneaded mixture. Consequently, since hydrophilic property is provided to the medium by the polar group of the polyolefin, the medium is not changed with static electricity and is not flocculated each other and adsorption of the filthy substances to the fine pores in the surface of the medium and growth of the substances and adhesion of the filthy substances to the fine bubbles produced out of the fine pores are carried out well, thus the filthy substances are removed and separated by floatation. Moreover, microbes are stuck to the medium due to the addition of the apatite and biological decomposition is utilized.

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、洗濯廃水、食品廃水、
家庭用廃水等の種々の廃水から汚濁物質を除去して清浄
化するのに使用される水処理用多孔質媒体に関し、特に
有機性の汚濁物質を除去するのに好適な多孔質媒体に関
する。本発明の媒体は、廃水の汚濁物質の浮上分離の際
の流動媒体としても、汚濁物質の濾過の際の固定媒体と
しても使用できる。
BACKGROUND OF THE INVENTION The present invention relates to laundry wastewater, food wastewater,
The present invention relates to a porous medium for water treatment used for removing and cleaning pollutants from various wastewater such as domestic wastewater, and particularly to a porous medium suitable for removing organic pollutants. The medium of the present invention can be used both as a fluid medium for floating separation of pollutants of wastewater and as a fixed medium for filtration of pollutants.

【0002】[0002]

【従来の技術】例えばクリーニング工場にて発生する多
量の洗濯廃水は、使用された洗剤の残留分、並びに洗濯
物から出て来る油脂分、無機固形分等の種々の汚濁物質
を含んでおり、そのまま河川などに排水することはでき
ず、水処理により汚濁物質を除去することを要してい
る。
2. Description of the Related Art For example, a large amount of laundry wastewater generated in a cleaning plant contains various contaminants such as residual residues of detergent used, oils and fats coming out of laundry, and inorganic solids. It cannot be directly discharged to rivers, etc., and it is necessary to remove pollutants by water treatment.

【0003】従来、このような廃水の処理法として、簡
易的には、例えば工場内の大きな原水槽に廃水を滞留さ
せ、汚濁物質の沈殿を待って汚濁物質と上澄み水とを分
離し、上澄み水を河川などに排水する方法が採用されて
いるが、汚濁物質の分離に長時間を要すること、そのた
めに大きな原水槽が必要になるので用地が膨大になるこ
と、汚濁物質の種類によっては沈殿による分離ができな
いことなどの欠点があった。
Conventionally, as a method of treating such wastewater, for example, simply, the wastewater is retained in a large raw water tank in a factory, the pollutant is allowed to settle, and the pollutant is separated from the supernatant water. Although the method of draining water to rivers is adopted, it takes a long time to separate pollutants, and a large raw water tank is required for that purpose, and the site becomes huge. There was a defect that it could not be separated by.

【0004】そこで、無機凝集剤や高分子凝集剤を廃水
中に注入し、撹拌して汚濁物質を凝集し、汚濁物質を完
全にフロック化して廃水から分離除去する方法が採られ
ている。しかしながら、このような方法によって廃水中
の無機固形分の除去はできるものの、油脂分や洗剤分な
どの有機性の汚濁物質の除去は難しく、必ずしも十分に
処理できない。
Therefore, a method has been adopted in which an inorganic coagulant or a polymer coagulant is injected into waste water and stirred to coagulate the pollutants, and the pollutants are completely flocculated and separated from the waste water. However, although inorganic solids in wastewater can be removed by such a method, it is difficult to remove organic pollutants such as fats and oils and detergents, and it is not always possible to sufficiently treat them.

【0005】又廃水を加圧して空気を溶解させ、その溶
解した空気の浮上により汚濁物質を浮上させて分離除去
する加圧浮上型水処理法も知られているが、空気溶解量
が少ないため分離速度が遅く、30分以上もの長い分離
時間を要する欠点があった。
A pressure-floating type water treatment method is also known in which waste water is pressurized to dissolve air, and the dissolved air is levitated to separate and remove contaminants, but the amount of dissolved air is small. It has a drawback that the separation speed is slow and a long separation time of 30 minutes or more is required.

【0006】[0006]

【発明が解決しようとする課題】このようなことから、
本出願人は、廃水中の無機固形分、油脂分、洗剤分など
種々の汚濁物質を実質的に完全に除去することができ、
分離時間も5分に短縮することができ、然もコンパクト
な装置にて実施し得る廃水処理法を提案し、先頃、特願
平3−59312号として出願した。
From the above,
The Applicant is capable of substantially completely removing various contaminants such as inorganic solids, oils and fats, and detergents in wastewater,
We proposed a wastewater treatment method that can reduce the separation time to 5 minutes and can be implemented with a compact device, and recently applied for it as Japanese Patent Application No. 3-59312.

【0007】この提案の処理法は、汚濁物質を含む廃水
に無機凝集剤及び圧縮空気を注入して高速撹拌、混合す
ることにより、気泡を含むエマルジョン状の反応液を形
成させ、その反応液に高分子凝集剤を注入して廃水中の
汚濁物質をフロック化させ、フロック化された汚濁物質
を分離、除去し、得られた処理水を多孔質媒体の存在下
に撹拌し、処理水中の残留汚濁物質に媒体から発生する
微細気泡を付着させて浮上分離させるもので、無機凝集
剤及び高分子凝集剤による処理後の残存汚濁物質を、多
孔質媒体を流動媒体として使用して微細空気により浮上
分離させることが大きな特徴である。
In the proposed treatment method, an inorganic coagulant and compressed air are injected into wastewater containing pollutants, and the mixture is rapidly stirred and mixed to form an emulsion-like reaction liquid containing bubbles, and the reaction liquid is formed into the reaction liquid. Polymer coagulant is injected to flocculate pollutants in wastewater, the flocculated pollutants are separated and removed, and the resulting treated water is agitated in the presence of a porous medium to remain in the treated water. Fine air bubbles generated from the medium are attached to the pollutants to float and separate, and the residual pollutants after treatment with inorganic coagulants and polymer coagulants are floated by micro air using a porous medium as a flowing medium. The major feature is separation.

【0008】これによれば、多孔質媒体の表面の細孔に
汚濁物質の粒子を吸着させて成長させる一方、その媒体
表面の細孔から微細な気泡を発生させて、媒体に吸着、
成長した汚濁物質粒子の表面に付着させることができる
ので、有機性の残留汚濁物質を良好に浮上分離して処理
水から除去することができる。
According to this, while particles of the pollutant are adsorbed and grown in the pores on the surface of the porous medium, fine air bubbles are generated from the pores on the surface of the medium and adsorbed on the medium.
Since it can be attached to the surface of the grown pollutant particles, the organic residual pollutants can be favorably floated and separated and removed from the treated water.

【0009】しかしながら、上記の多孔質媒体は、ポリ
エチレン、ポリプロピレン等の樹脂に粘度や大谷石等の
無機物質粉末を混合して製造されているため、撹拌時の
媒体同士の摩擦により静電気を帯びて媒体同士が固まる
傾向があり、必ずしも期待された汚濁物質の除去性能を
発揮することができないことがあった。
However, since the above-mentioned porous medium is manufactured by mixing a resin such as polyethylene or polypropylene with an inorganic substance powder such as viscosity or Otani stone, it is charged with static electricity due to friction between the mediums at the time of stirring. There was a tendency for the media to solidify, and it was not always possible to exhibit the expected contaminant removal performance.

【0010】本発明の目的は、微細空気による汚濁物質
の浮上分離の際の流動媒体としても、汚濁物質の濾過の
際の固定媒体としても使用でき、然も媒体同士の摩擦に
より静電気を帯びて固まることがなく、汚濁物質の除去
性能を良好に発揮することができ、特に有機性の汚濁物
質の除去性能に優れた水処理用多孔質媒体を提供するこ
とである。
The object of the present invention is that it can be used both as a fluid medium for floating separation of pollutants by fine air, and as a fixed medium for filtration of pollutants, and it is still charged with static electricity due to friction between the media. It is an object of the present invention to provide a porous medium for water treatment, which does not solidify and can exhibit excellent performance of removing pollutants, and in particular has excellent performance of removing organic pollutants.

【0011】[0011]

【課題を解決するための手段】上記目的は、本発明に係
る水処理用多孔質媒体にて達成される。要約すれば本発
明は、極性基のある変性ポリオレフィンとシラスバルー
ンとヒドロキシアパタイトとを混練して、押出成形によ
りペレットに形成したことを特徴とする水処理用多孔質
媒体である。
The above object can be achieved by the porous medium for water treatment according to the present invention. In summary, the present invention is a porous medium for water treatment characterized in that a modified polyolefin having a polar group, shirasu balloon and hydroxyapatite are kneaded and formed into pellets by extrusion molding.

【0012】以下、本発明の水処理用多孔質媒体につい
て説明する。
The porous medium for water treatment of the present invention will be described below.

【0013】本発明の多孔質媒体に使用するシラスバル
ーンは、シラスを1000℃程度の高温で焼成したもの
で、シラス中に含有した水分により膨張した多孔質の軽
量粉末である。このシラスバルーンは、その表面の径が
数10〜数100μmの不規則な細孔に汚濁物質の粒子
を吸着するので、廃水処理の媒体として好適に使用する
ことができる。しかし、シラスバルーンは粉末なのでそ
のまま使用したのでは、媒体の目詰まりや流出を招く。
The shirasu balloon used in the porous medium of the present invention is obtained by firing shirasu at a high temperature of about 1000 ° C., and is a porous lightweight powder expanded by the water contained in the shirasu. Since this shirasu balloon adsorbs particles of pollutants in irregular pores having a surface diameter of several tens to several hundreds of μm, it can be suitably used as a medium for wastewater treatment. However, since Shirasu balloon is a powder, if it is used as it is, the medium will be clogged and flow out.

【0014】本発明では、シラスバルーンをプラスチッ
クをベースとしてペレットにした媒体として使用する。
このような媒体によれば、例えばこれを流動媒体として
用いた場合、その表面に位置したシラスバルーンの細孔
により汚濁物質の粒子を吸着して成長させる一方、細孔
に捕捉した空気から微細な気泡を発生させて、媒体表面
に吸着した汚濁物質の粒子に気泡を付着させ、汚濁物質
を浮上分離させることができる。
In the present invention, Shirasu balloon is used as a plastic-based pelletized medium.
According to such a medium, when it is used as a fluid medium, for example, particles of contaminants are adsorbed and grown by the pores of the Shirasu balloon located on the surface of the medium, while fine particles are removed from the air captured in the pores. It is possible to generate bubbles and attach the bubbles to the particles of the pollutant adsorbed on the surface of the medium to float and separate the pollutant.

【0015】このシラスバルーンの媒体に対する配合量
は10〜50wt%とする。シラスバルーンの配合量が
10wt%未満では汚濁物質の吸着が不十分で、汚濁物
質を良好に除去することができない。一方、配合量が5
0wt%を超えると媒体が脆くなって強度が不十分とな
り、実用に供すことができない。好ましくはシラスバル
ーンは15〜30wt%とするのがよい。シラスバルー
ンの粒度は50〜50μm、好ましくは80〜200μ
mである。
The amount of the shirasu balloon mixed with the medium is 10 to 50 wt%. If the amount of shirasu balloon is less than 10 wt%, the contaminants are not adsorbed sufficiently and the contaminants cannot be removed well. On the other hand, the compounding amount is 5
If it exceeds 0 wt%, the medium becomes brittle and the strength becomes insufficient, and it cannot be put to practical use. The shirasu balloon content is preferably 15 to 30 wt%. The particle size of the shirasu balloon is 50 to 50 μm, preferably 80 to 200 μm
m.

【0016】本発明では、媒体のベースプラスチックと
して極性基のある変性ポリオレフィンを使用する。これ
は、媒体が静電気を帯びるのを防止するためで、変性ポ
リオレフィンの極性基により媒体に親水性を持たせるこ
とができるので、媒体同士が摩擦されても静電気を帯び
ることがなく、媒体同士が固まることがない。従って廃
水中で媒体を良好に分散して媒体の表面に汚濁物質を接
触させることができ、汚濁物質の媒体表面の細孔への吸
着による成長及び細孔から発生した微細気泡の汚濁物質
への付着を良好に行なわせ、廃水から汚濁物質を除去し
て気泡により浮上分離させることができる。
In the present invention, a modified polyolefin having a polar group is used as the base plastic of the medium. This is to prevent the medium from being charged with static electricity, and since the medium can be made hydrophilic by the polar group of the modified polyolefin, even if the medium is rubbed with each other, the medium will not be charged with static electricity and the medium will not be charged. It never hardens. Therefore, it is possible to satisfactorily disperse the medium in the wastewater and bring the pollutant into contact with the surface of the medium, and the growth by adsorption of the pollutant to the pores on the medium surface and the formation of fine bubbles generated from the pores into the pollutant Adhesion can be performed well, contaminants can be removed from wastewater, and air bubbles can be used for floating separation.

【0017】このような極性基のある変性ポリオレフィ
ンとしては、ポリエチレンやプロピレン或いはエチレン
−プロピレン共重合体のマレイン酸変性物、ハイミク酸
変性物及びエポキシ基付加変性物等が挙げられる。
Examples of the modified polyolefin having a polar group include maleic acid modified products of polyethylene, propylene or ethylene-propylene copolymers, modified products of hymic acid and modified products of addition of epoxy groups.

【0018】極性基のある変性ポリオレフィンの配合量
は50〜90wt%の範囲が適当で、50wt%未満で
は媒体をペレット化することが困難であり、逆に90w
t%を超えるとシラスバルーンの量が少なくなって、媒
体に汚濁物質除去性能がなくなる。好ましくは極性基の
ある変性ポリオレフィンは65〜80wt%の範囲がよ
い。
The amount of the modified polyolefin having a polar group is appropriately in the range of 50 to 90 wt%, and if it is less than 50 wt%, it is difficult to pelletize the medium, and conversely 90 w.
If it exceeds t%, the amount of shirasu balloon becomes small and the medium has no ability to remove pollutants. The modified polyolefin having polar groups is preferably in the range of 65 to 80 wt%.

【0019】本発明によれば、有機性の汚濁物質を微生
物分解して除去できるようにするため、媒体に更にヒド
ロキシアパタイト(リン酸カルシウム系ヒドロキシアパ
タイト)を配合する。このヒドロキシアパタイトは人間
を初めとする生物の骨の構成物質であり、生物との親和
性が高い。このため媒体表面に微生物が容易に付着し
て、有機性の汚濁物質を栄養として繁殖し、汚濁物質が
微生物分解により廃水から除去される。又ヒドロキシア
パタイトを配合することにより、軽量なシラスバルーン
及びプラスチックによる媒体の比重を適当な重さに調整
する意味もある。
According to the present invention, hydroxyapatite (calcium phosphate-based hydroxyapatite) is further added to the medium so that the organic pollutants can be removed by microbial decomposition. This hydroxyapatite is a constituent material of human bones such as human beings and has a high affinity with living things. Therefore, the microorganisms easily attach to the surface of the medium, the organic pollutants propagate as nutrients, and the pollutants are removed from the wastewater by microbial decomposition. Also, by blending hydroxyapatite, it has the meaning of adjusting the specific gravity of the medium made of lightweight shirasu balloon and plastic to an appropriate weight.

【0020】ヒドロキシアパタイトの配合量はこれによ
る媒体の比重の調整を考慮して決める必要があるが、一
般的にヒドロキシアパタイトは0.5〜20wt%程度
がよく、0.5wt%未満では媒体への微生物の付着性
を良好にできず、逆に20wt%を超えるとヒドロキシ
アパタイトのコストが高いので媒体が高くなる。ヒドロ
キシアパタイトの粒度は2〜100μm、好ましくは5
〜30μmである。
The amount of hydroxyapatite to be blended must be determined in consideration of the adjustment of the specific gravity of the medium, but generally, the hydroxyapatite content is preferably in the range of 0.5 to 20% by weight. However, if the amount exceeds 20 wt%, the cost of hydroxyapatite is high and the medium becomes expensive. The particle size of hydroxyapatite is 2 to 100 μm, preferably 5
˜30 μm.

【0021】ヒドロキシアパタイトは湿式法等の化学合
成したものでも良いが、安価には燐灰石や例えば牛骨等
の動物の骨など天然物を利用することができる。
Hydroxyapatite may be chemically synthesized by a wet method or the like, but a natural product such as apatite or animal bone such as bovine bone can be inexpensively used.

【0022】媒体の比重は具体的な使用形態に応じて適
宜選択すればよいが、流動媒体、固定媒体のいずれの場
合も、1より多少重い程度が取扱いに便利である。
The specific gravity of the medium may be appropriately selected according to the specific usage, but in the case of both the fluid medium and the fixed medium, it is convenient to handle if it is slightly heavier than 1.

【0023】媒体の形状は任意の形をとることができる
が、押出成形により容易に製造できる点で、本発明の好
ましい一実施例を示す図1に示した媒体1のように、円
柱状にすることが好適である。又媒体の大きさも任意に
することができるが、大きい方が水流による抵抗が増し
て撹拌効果が大きくなること、又媒体を挿入する撹拌槽
等に設置した媒体流出防止用の金網等に媒体が目詰まり
するのを防止し易いことから、図1の媒体1の長さAが
1〜10mm、断面の直径Bが1〜10mmの程度の大
き目なものにすることがよい。媒体1の大きさは好まし
くは3〜8mm×3〜8mm、より好ましくは6〜7m
m×6〜7mmである。
The shape of the medium can be any shape, but in the point that it can be easily manufactured by extrusion molding, it has a cylindrical shape like the medium 1 shown in FIG. 1 showing a preferred embodiment of the present invention. Is preferred. The size of the medium can also be set arbitrarily, but the larger the size, the greater the resistance due to the water flow and the greater the stirring effect. Also, the medium is placed in the wire mesh for preventing medium outflow installed in the stirring tank or the like into which the medium is inserted. Since it is easy to prevent clogging, it is preferable that the medium 1 in FIG. 1 has a length A of 1 to 10 mm and a cross-sectional diameter B of 1 to 10 mm. The size of the medium 1 is preferably 3 to 8 mm x 3 to 8 mm, more preferably 6 to 7 m.
m × 6 to 7 mm.

【0024】又媒体は、図2(A)に示すように2個の
媒体1をその側方で連結したり、図2(B)に示すよう
に3個の媒体1を連結したり、図2(C)に示すように
4個の媒体1を同様に連結したりすることもでき、この
ように媒体1を側方で連結した連結媒体とした場合、媒
体1の大きさを単純に大きくするときよりも表面積を相
対的に大にできるので好ましい。媒体1が4個の連結媒
体の場合、図2(D)に示すように、4個の媒体1の内
側に適当な間隙を設けた態様にすることができる。
As for the medium, two mediums 1 are connected sideways as shown in FIG. 2 (A), or three mediums 1 are connected as shown in FIG. 2 (B). It is also possible to connect four media 1 in the same manner as shown in FIG. 2 (C). When the media 1 are laterally connected as described above, the size of the media 1 is simply increased. It is preferable because the surface area can be made relatively larger than that in the case of In the case where the medium 1 is four connected media, as shown in FIG. 2 (D), an appropriate gap may be provided inside the four media 1.

【0025】図1に示したような媒体1は、鉄板等に所
要の大きさの穴を多数開けたダイスを押出し機に取付け
て、極性基のある変性ポリオレフィンとシラスバルーン
とヒドロキシアパタイトとを混練した混練物を温度20
0℃前後でダイスから線状に押し出し、半硬化した線状
押出し物を押出しに続いて所要長さに連続的に切断する
ことにより容易に製造することができる。ダイスに設け
る穴と穴の間隙を所要の穴について小さくしておけば、
その穴から押し出された線状押出し物同士が接触して半
硬化する前に接着するので、図2(A)〜(D)に示し
た複数個の媒体1を連結した連結媒体が容易にできる。
In the medium 1 as shown in FIG. 1, a die having a large number of holes of a required size formed in an iron plate or the like is attached to an extruder, and a modified polyolefin having polar groups, shirasu balloon and hydroxyapatite are kneaded. The kneaded mixture was heated to 20
It can be easily produced by linearly extruding from a die at around 0 ° C., semi-cured linear extrudate, and then continuously cutting to a required length after extrusion. If the gap between the holes provided in the die is small for the required holes,
Since the linear extrudates extruded from the holes are brought into contact with each other and adhered to each other before being semi-cured, a connecting medium in which a plurality of mediums 1 shown in FIGS. 2A to 2D are connected can be easily formed. ..

【0026】本発明の多孔質媒体は、これを洗濯廃水、
食品廃水、家庭用廃水等の廃水の処理に、流動媒体とし
て使用しても固定媒体として使用してもいずれでもよ
い。又前処理なしに廃水に直接用いて廃水の汚濁物質を
処理することも、或いは無機凝集剤及び/又は高分子凝
集剤による廃水の処理後に処理水に用いて、残存汚濁物
質を処理するようにしてもよい。いずれの場合も、媒体
同士の摩擦により静電気を帯びて固まることがないの
で、廃水中で媒体を良好に分散して媒体の表面に汚濁物
質を接触させることができ、媒体を介して汚濁物質を廃
水から除去して気泡により浮上分離させることができ
る。
The porous medium of the present invention is the same as the washing wastewater,
It may be used as a fluid medium or a fixed medium for treating wastewater such as food wastewater and household wastewater. It is also possible to treat the pollutants of the wastewater by directly using the wastewater without pretreatment, or to treat the residual pollutants by using the treated water after treating the wastewater with the inorganic coagulant and / or the polymer coagulant. May be. In any case, since the medium does not solidify due to static electricity due to friction between the medium, it is possible to disperse the medium well in the waste water and bring the pollutant into contact with the surface of the medium. It can be removed from wastewater and floated and separated by air bubbles.

【0027】又媒体にヒドロキシアパタイトを配合した
ので、媒体に微生物を付着させて汚濁物質の微生物分解
を活用することができ、有機性の汚濁物質が多い廃水で
あってもその汚濁物質を良好に除去することができる。
Since hydroxyapatite is mixed in the medium, microorganisms can be attached to the medium to utilize the microbial decomposition of pollutants, and the pollutants can be satisfactorily treated even in wastewater containing a large amount of organic pollutants. It can be removed.

【0028】更に又微生物の付着性が良いことから媒体
を微生物の増殖用ベッドとして用いることもでき、媒体
を微生物を利用した発酵タンク等に流動媒体或いは固定
媒体として使用することができる。
Further, since the adherence of microorganisms is good, the medium can be used as a bed for growing microorganisms, and the medium can be used as a fluid medium or a fixed medium in a fermentation tank or the like using microorganisms.

【0029】[0029]

【実施例】本発明の多孔質媒体の実施例について説明す
る。本発明の多孔質媒体を使用してクリーニング廃水の
処理を行なった。クリーニング廃水は、PHが9.0、
濁度が190ppm、SSが146ppm、CODが1
08ppm及びn−ヘキサン抽出物が76ppmの原水
を、未処理のまま本発明の媒体による処理に使用した。
媒体は、ベースプラスチックとしてマレイン酸変性ポリ
オレフィンを使用した。
EXAMPLES Examples of the porous medium of the present invention will be described. Cleaning wastewater was treated using the porous media of the present invention. The cleaning wastewater has a pH of 9.0,
Turbidity 190 ppm, SS 146 ppm, COD 1
Raw water at 08 ppm and 76 ppm n-hexane extract was used as-is for treatment with the media of the invention.
The medium used was a maleic acid-modified polyolefin as the base plastic.

【0030】容積が3m3 の撹拌槽に2m3 のクリーニ
ング廃水を導入し、これに図1で示した長さAが6m
m、直径Bが6mmの円柱状の媒体1を約100kg
(容積約0.3m3 装入した。そしてクリーニング廃水
中に空気圧縮機により圧縮空気を0.6m3 /分の流量
で吹き込んで、廃水及び媒体を撹拌して処理し、廃水を
清浄化した。媒体から発生した微細気泡により浮上した
汚濁物質のスカムは、処理時に撹拌槽上からの流出によ
り除去した。
2 m 3 of cleaning wastewater was introduced into a stirring tank having a volume of 3 m 3 , and the length A shown in FIG. 1 was 6 m.
m, a cylindrical medium 1 having a diameter B of 6 mm is about 100 kg.
(A volume of about 0.3 m 3 was charged. Then, compressed air was blown into the cleaning wastewater by an air compressor at a flow rate of 0.6 m 3 / min, and the wastewater and the medium were agitated and treated to purify the wastewater. The scum of pollutants floating by the fine bubbles generated from the medium was removed by flowing out from the stirring tank during the treatment.

【0031】比較のために、ベースプラスチックとして
変性のないポリオレフィンを使用した媒体を使用して、
上記と同様にした。
For comparison, using a medium using unmodified polyolefin as the base plastic,
Same as above.

【0032】本発明で使用した媒体の組成及び得られた
処理水の汚濁成分を、比較例と共に表1に示す。
The composition of the medium used in the present invention and the polluted components of the obtained treated water are shown in Table 1 together with Comparative Examples.

【0033】[0033]

【表1】 [Table 1]

【0034】表1に示されるように、本発明の媒体を用
いてクリーニング廃水を処理した場合、濁度、SS、C
OD及びn−ヘキサン抽出物質の各項目共、比較例より
も大幅に減少しており、優れた汚濁物質の除去効果が奏
された。特にn−ヘキサン抽出物質の除去効果が顕著で
あった。
As shown in Table 1, when the cleaning wastewater was treated with the medium of the present invention, turbidity, SS, C
The respective items of OD and n-hexane extracted substance were significantly reduced as compared with the comparative example, and an excellent pollutant removal effect was exhibited. Particularly, the effect of removing the n-hexane extracted substance was remarkable.

【0035】以上では、本発明の媒体をクリーニング廃
水に直接使用して処理を行なったが、予め無機凝集剤及
び/又は高分子凝集剤による処理後に、本発明の媒体を
使用して更に処理をすれば、クリーニング廃水の汚濁物
質を高度に除去することができるのは明らかである。
In the above, the treatment of the medium of the present invention was carried out by directly using the cleaning wastewater. However, after the treatment with the inorganic flocculant and / or the polymer flocculant in advance, the treatment of the medium of the present invention was further performed. It is clear that the pollutants of the cleaning wastewater can be highly removed by doing so.

【0036】[0036]

【発明の効果】以上説明したように、本発明の多孔質媒
体は、極性基のある変性ポリオレフィンとシラスバルー
ンとヒドロキシアパタイトとを混練してペレットに成形
してなり、変性ポリオレフィンの極性基により媒体に親
水性を持たせているので、洗濯廃水、食品廃水、家庭用
廃水等の廃水の処理に用いて、媒体同士が摩擦により静
電気を帯びて固まることがなく、媒体の表面に汚濁物質
を良好に接触して、汚濁物質の媒体表面への吸着及び媒
体からの気泡による浮上分離により、高い除去性能で汚
濁物質を除去することができる。更に媒体にヒドロキシ
アパタイトを配合したので、媒体に微生物を付着させて
汚濁物質の微生物分解を活用することができ、有機性の
汚濁物質が多い廃水であってもその汚濁物質の除去を良
好に行なわせることができる。
As described above, the porous medium of the present invention is formed by kneading a modified polyolefin having polar groups, shirasu balloon and hydroxyapatite into pellets, and the medium is formed by the modified polar groups of the modified polyolefin. Since it has hydrophilicity, it can be used for the treatment of wastewater such as laundry wastewater, food wastewater, household wastewater, etc., and the media do not get electrostatically charged due to friction between the media and solidify the surface of the media. By adsorbing the pollutant on the surface of the medium and floating separation from the medium by air bubbles, the pollutant can be removed with high removal performance. Furthermore, since hydroxyapatite has been added to the medium, microorganisms can be attached to the medium to utilize the microbial decomposition of pollutants, and even in wastewater containing many organic pollutants, the pollutants can be removed well. Can be made.

【0037】又本発明の媒体は、廃水の処理に際し流動
媒体としても固定媒体としても使用でき、更に無機凝集
剤及び/又は高分子凝集剤等による前処理なしに廃水に
直接用いて廃水の汚濁物質を処理することも、或いは無
機凝集剤及び/又は高分子凝集剤による廃水の処理後に
処理水に用いて、残存汚濁物質を処理する態様の処理に
も使用できる。
The medium of the present invention can be used as a fluid medium or a fixed medium in treating wastewater, and is used directly in wastewater without pretreatment with an inorganic coagulant and / or a polymer coagulant, etc. It can be used for treating the substance, or for treating the residual pollutant by treating the wastewater with the inorganic flocculant and / or the polymer flocculant and then treating the wastewater.

【図面の簡単な説明】[Brief description of drawings]

【図1】本発明の媒体の好ましい一実施例の形状を示す
斜視図である。
FIG. 1 is a perspective view showing the shape of a preferred embodiment of the medium of the present invention.

【図2】図1の媒体を連結した連結媒体の諸態様を示す
斜視図である。
FIG. 2 is a perspective view showing various aspects of a connection medium in which the media of FIG. 1 are connected.

【符号の説明】[Explanation of symbols]

1 媒体 A 長さ B 直径 1 Medium A Length B Diameter

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.5 識別記号 庁内整理番号 FI 技術表示箇所 // C02F 1/52 Z 7824−4D (72)発明者 吉田 俊男 東京都中央区築地4−1−1 東燃化学株 式会社内─────────────────────────────────────────────────── ─── Continuation of the front page (51) Int.Cl. 5 Identification number Internal reference number FI technical display location // C02F 1/52 Z 7824-4D (72) Inventor Toshio Yoshida 4-1 Tsukiji, Chuo-ku, Tokyo -1 Tonen Chemical Co., Ltd.

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 極性基のある変性ポリオレフィンとシラ
スバルーンとヒドロキシアパタイトとを混練して、押出
成形によりペレットに形成したことを特徴とする水処理
用多孔質媒体。
1. A porous medium for water treatment, characterized in that a modified polyolefin having a polar group, shirasu balloon and hydroxyapatite are kneaded and formed into pellets by extrusion molding.
JP4137661A 1992-04-30 1992-04-30 Porous medium for water treament Pending JPH05309361A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP4137661A JPH05309361A (en) 1992-04-30 1992-04-30 Porous medium for water treament

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP4137661A JPH05309361A (en) 1992-04-30 1992-04-30 Porous medium for water treament

Publications (1)

Publication Number Publication Date
JPH05309361A true JPH05309361A (en) 1993-11-22

Family

ID=15203867

Family Applications (1)

Application Number Title Priority Date Filing Date
JP4137661A Pending JPH05309361A (en) 1992-04-30 1992-04-30 Porous medium for water treament

Country Status (1)

Country Link
JP (1) JPH05309361A (en)

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2002346583A (en) * 2001-05-22 2002-12-03 Mitsubishi Rayon Co Ltd Microorganism immobilized carrier
JP2004167471A (en) * 2002-11-05 2004-06-17 Nippon Steel Chem Co Ltd Water treatment material, nitrate nitrogen treating material, and its production method
JP2005040767A (en) * 2003-07-25 2005-02-17 Aisin Takaoka Ltd Water purification material, its production method, its using method, and water purification material mixture
JP2012206084A (en) * 2011-03-30 2012-10-25 Cci Corp Treatment method for fat-containing wastewater and wastewater treatment material therefor
CN108516653A (en) * 2018-05-25 2018-09-11 哈尔滨工程大学 A kind of MBBR couples boat domestic sewage treatment device and method with electric flocculation
CN114378981A (en) * 2021-12-14 2022-04-22 宁波坚锋新材料有限公司 Water-carrying porous friction medium and method for cleaning waste plastic

Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2002346583A (en) * 2001-05-22 2002-12-03 Mitsubishi Rayon Co Ltd Microorganism immobilized carrier
JP4530320B2 (en) * 2001-05-22 2010-08-25 三菱レイヨン株式会社 Microorganism immobilization carrier
JP2004167471A (en) * 2002-11-05 2004-06-17 Nippon Steel Chem Co Ltd Water treatment material, nitrate nitrogen treating material, and its production method
JP4545408B2 (en) * 2002-11-05 2010-09-15 新日鐵化学株式会社 Water treatment material, nitrate nitrogen treatment material and production method thereof
JP2005040767A (en) * 2003-07-25 2005-02-17 Aisin Takaoka Ltd Water purification material, its production method, its using method, and water purification material mixture
JP2012206084A (en) * 2011-03-30 2012-10-25 Cci Corp Treatment method for fat-containing wastewater and wastewater treatment material therefor
CN108516653A (en) * 2018-05-25 2018-09-11 哈尔滨工程大学 A kind of MBBR couples boat domestic sewage treatment device and method with electric flocculation
CN114378981A (en) * 2021-12-14 2022-04-22 宁波坚锋新材料有限公司 Water-carrying porous friction medium and method for cleaning waste plastic
CN114378981B (en) * 2021-12-14 2023-08-22 宁波坚锋新材料有限公司 Water-carrying porous friction medium and method for cleaning waste plastics

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