JPH0242473B2 - - Google Patents
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- JPH0242473B2 JPH0242473B2 JP57176358A JP17635882A JPH0242473B2 JP H0242473 B2 JPH0242473 B2 JP H0242473B2 JP 57176358 A JP57176358 A JP 57176358A JP 17635882 A JP17635882 A JP 17635882A JP H0242473 B2 JPH0242473 B2 JP H0242473B2
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- 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
- Immobilizing And Processing Of Enzymes And Microorganisms (AREA)
- Micro-Organisms Or Cultivation Processes Thereof (AREA)
- Biological Treatment Of Waste Water (AREA)
- Treatment Of Biological Wastes In General (AREA)
Description
本発明は微生物付着用粒子に関し、詳しくは水
処理や発酵生産に用いられる微生物を付着、担持
するための合成樹脂製の筒状粒子であつて、その
外表面を粗面化して微生物の付着剤を改善した筒
状粒子に関する。ここで筒状粒子とは貫通した中
空の粒子であつて切り口、すなわち横断剖が円
形、楕円形、多角形(たとえば三角形乃至十二角
形で星形のものなども含む)等のものを云う。
従来、家庭排水、工場排水等の排水処理の方法
に関して過、沈降分離、生物処理等の広い分野
にわたる技術が提案されている。これらの方法の
うち、特に水に浮遊する担体を使用して過、生
物処理等を効果的に行なう方法が開発されてい
る。また、特定の有用物質の生産を目的として行
なわれる発酵においても同様に培養液よりも比重
の軽い担体を用い、該担体に微生物を付着させて
発酵を行なう固定微生物膜法等が採り入れられて
きている。
これらの方法に使用される軽量粒子としてはパ
ーライト、シラスバルーン等で代表される天然の
軽量物や比重が1未満の合成樹脂粒子のほか、発
泡することにより、低比重にした合成樹脂、たと
えば発泡ポリエチレン、発泡ポリプロピレン、発
泡ポリスチレン等の既に充填材、吸着剤、保温材
等の目的で市販されている粒子が用いられてい
る。
しかしながら、天然の軽量物は水を吸収し易い
ため、半永久的に水に浮上する粒子として用いる
には難がある。また、低比重の合成樹脂粒子は均
一なものが大量に得られるという有利性がある反
面、微生物膜と粒子表面の固着強度が小さいた
め、粒子同士あるいは粒子と器壁との摩擦や粒子
と水または気泡による剪断(以下、単に粒子同士
の接触という。)によつて微生物膜の一部あるい
は全部が剥離するという欠点がある上に、経済性
の立場からみて合成樹脂原料が高いために粒子の
コストも高いものとなつてしまう。
このような状況下において本発明者らは合成樹
脂と無機質材料との混合物を主成分とし、これを
発泡せしめて得られる粒子が親水性にすぐれ、し
かも微生物膜の付着性が極めて大きく、さらに合
成樹脂と無機質材料の比率を変化させることによ
り粒子内の気泡のほとんどが独立気泡として維持
されるため、半永久的に水に浮上する粒子として
使用できることを見出し、水処理用の新規な微生
物担持用粒子として提供するに至つた(特開昭56
−89897号)。さらに、該低比重粒子に改良を加え
たものとして発泡合成樹脂の表面に特定粒子径の
無機および/または有機の物質を付着させた低比
重の微生物担持用粒子を開発した(特願昭56−
131241号)。これは合成樹脂の発泡倍率を高くし
て合成樹脂の使用量を可及的に減少せしめるばか
りでなく、粒子の比重調整を容易に行なうことが
できるという特色を有している。
しかしながら、これら微生物担持用粒子に共通
して言えることは、該粒子に微生物を付着、担持
させて液中で固定することなく使用する処理法、
たとえば流動層、混合層等による処理法では、固
定層による処理法において見られるような増殖微
生物による目詰まりもなく、しかも高濃度の微生
物を保持できるため高い反応速度が得られるとい
う長所を有しているが、粒子から剥離してくる余
剰微生物は微細であり沈降性が悪いため、後段の
余剰微生物に起因するSS分離のための従来型の
重力沈降槽を使用する場合、その装置を或程度大
きくせざるを得ないという短所があつた。このた
め、このような水処理法においては沈降性の良好
な余剰微生物を得ることが望まれていた。
本発明の目的は上記の欠点を解消して沈降性の
良好な余剰微生物を排出すると共に、該余剰微生
物の発生量が少なく、かつ微生物の付着性にすぐ
れた微生物付着用粒子を提供することである。
本発明は、比重が1未満の合成樹脂より成る筒
状粒子であつて、外径が1.5〜15mm、長さを外径
の比が0.2〜6.0であり、かつ肉厚が0.05〜1.0mmで
ある筒状粒子の外表面を物理的手段により粗面化
処理してなる微生物付着用粒子である。
本発明に用いる合成樹脂は見かけ比重が1未満
のものであり、特に熱可塑性樹脂が好ましく、具
体例としてはたとえばポリエチレン、ポリプロピ
レン、ポリスチレン、メチルペンテンポリマーな
どを挙げることができる。ここで、これら合成樹
脂は広義に解釈されるべきであり、たとえばポリ
エチレンを例示すると、エチレンのホモポリマー
のみならずエチレンと他のオレフインとのコポリ
マー等も包含するものである。また、合成樹脂の
比重についても発泡させて比重を1.0未満とした
ものも本発明に包含される。
合成樹脂に既知の成形手段を適用して筒状粒子
を得るが、該粒子の形状は前述したように貫通し
た中空の粒子であつて切り口、すなわち横断面が
円形、楕円形、多角形などのものである。多角形
としては三角形、四角形、六角形等が一般的で、
星形を含む十二角形程度のものまで任意である。
筒状粒子は、たとえば押出し成形によつて得られ
る成形体をカツター等によつて一定の長さに切断
することによつて容易に得ることが出来るが、製
造しやすく、かつ微生物膜が均一な厚さで付着し
やすく、しかも比表面も大きいという理由から横
断面が円形のものが好ましい。
本発明の筒状粒子は外径が1.5〜15mmのもので
あり、外径が小さい程、比表面積が大きくなり好
ましいが外径が1.5mm未満であると、水処理等に
用いた場合、粒子表面に付着している微生物によ
り粒子同士が凝着するため、効率的な水処理等が
行なえず、かつ該粒子内表面に微生物が増殖し充
満するため該粒子内部は反応に有効に作用しない
こととなる。一方、外径が15mmを超えると、比表
面積低下に伴ない微生物保持量が低下し、単位容
積当りの反応速度が低下して回転円板、散水
床、浸漬式床等の従来法における反応速度に近
づいてしまい本発明の特色が失なわれることとな
る。反応速度の面からみると、粒子の最も好まし
い外径は1.5〜10mmの範囲である。しかしながら、
糖類、デンプン類などを含有する排水を処理する
場合、付着微生物の膜厚が異常に大きくなり、小
さい粒子を使用すると互に凝着することがあるの
で、このような基質を含有する場合には外径が10
〜15mm程度の粒子を用いることが適している。な
お、筒状粒子の外径については横断面が円形以外
のものは円相当径を外径として取扱えばよい。
次に、筒状粒子の長さ(L)と外径(D)の比(L/
D)については0.2〜6.0とすべきであり、この比
が0.2未満であると、中空内部に微生物が保持さ
れ難いので余剰微生物の生成量の減少と良好な沈
降性という本発明の特色が失なわれてしまう。一
方、この値が6.0を超えると粒子の長さが長すぎ
て使用の際に粒子の移動性が悪くなり、たとえば
流動層で使用すると流動性を著しく阻害する上
に、微生物反応によつて生成したガスが曝気用ガ
スが筒状粒子内部に内包して該粒子の見かけ比重
が軽くなつたり、該粒内部に微生物を十分に保持
できなくなるという欠点が生じる。また、この値
が大きいと粒子の充填効率も低下する。したがつ
て、一般的には比(L/D)を0.5〜3.0の範囲と
することが好ましい。
また、筒状粒子の肉厚は0.05〜1.0mmであるこ
とが必要で、肉厚が0.05mm未満では粒子の輸送、
貯蔵時に破損しやすく、また1.0mmを超えると筒
状粒子の内表面の比表面積が減少するばかりでな
く、合成樹脂の使用量が増大し、コスト高を招
く。中空部の径は粒子の外径および肉厚によつて
異なるが通常1mmφ以上であることが好ましい。
さらに、本発明の微生物付着用粒子は外表面を
物理的手段により粗面化することによつて微生物
の付着性を改良したものである。この処理を行な
うことによつて粒子単位体積当りの微生物保持量
を増大することができる。粒子の表面を粗面化処
理しないで流動層、混合層、輸送層等を形成して
行なう水処理等に使用すると、粒子同士の接触に
より通常は筒状粒子の外表面には微生物はほとん
ど付着しなくなる。このような現象は粒子に効率
よく微生物を付着させて利用するという立場から
は好ましくない。したがつて、外表面の粗面化は
筒状の微生物付着用粒子には重要なことである。
粒子外表面の粗面化方法には、たとえば押出し
成形等により得られる成形体を一定の長さに切断
する前に、その表面を加熱処理する方法、濃硫酸
などの酸を用いてエツチングする方法。研磨材な
どによる機械的(すなわち物理的)手段により処
理する方法などがあるが、物理的手段による粗面
化処理が最も好ましい。物理的表面処理により粒
子の表面に凹凸、ひだ、傷などをつけることによ
つて微生物の付着性を良くし、かつ粒子同士の接
触によつても付着微生物のほとんどが容易には剥
離しないようにすることができる。
粒子表面の粗面化状態と微生物の付着性をさら
に詳細に検討すると、粗面化処理方法の違いによ
る粗面化状態の相違が微生物の付着性に大きな影
響を与えることが判る。すなわち、熱的あるいは
化学的に表面処理を行なつた粒子の表面には凹凸
が形成されるが、この凹凸は一般に滑らかなもの
であり、微生物の付着性は無処理の場合よりも大
巾に改善されるが、粒子同士の接触によつて微生
物は比較的剥離されやすい。
一方、物理的(機械的)な手段により粗面化し
たものは粒子表面に「引掻き傷」、「ささくれ」な
どの表面傷が生じている。これらの表面傷は微生
物の付着を容易にすると共に、粒子同士の接触に
よつても微生物は剥離し難い。合成樹脂に発泡剤
を添加して比重を低下せしめた筒状粒子に同様な
物理的手段を施すと、さらに鋭利な表面傷の発生
が見られるが、これは筒状粒子の表面近傍に存在
する独立気泡が物理的処理によつて破壊されるこ
とに起因するものと考えられる。前述の如く、こ
れらの鋭利な「引掻き傷」や「ささくれ」などの
存在する粒子表面には微生物が付着されやすく、
付着に要する日数も短期間ですむ上、付着した微
生物は粒子同士の接触があつても剥離しにくいと
という特性を有していることが判明した。したが
つて、本発明では物理的な粗面化処理を行なつた
筒状粒子が好ましい。
物理的な粗面化処理手段としては、たとえば押
出し成形により得られる筒状成形体の表面に研磨
材あるいは研磨ブラツシをかける方法や鋭利な刃
物を1個もしくは複数個設置して該表面に傷をつ
ける方法等がある。このような処理方法は表面処
理用機械等を固定しておき筒状成形品を連続的に
移動させたり、該機械等を回転あるいは往復運動
させて筒状成形品を連続的に処理するなどの連続
的操作が通常行なわれる。次いで、表面処理され
た筒状成形体を一定の長さに切断することによつ
て本発明の微生物付着用粒子が得られる。
物理的な粗面化処理を施した粒子は微生物の付
着性が良好であるため、該粒子の素材としては微
生物が付着した状態でも該粒子が沈降しないよう
に比重が約0.6〜0.9のものを使用すべきである。
本発明の筒状粒子は、前述したように押出し成
形等によつて一定の成形体を作るため、均一な肉
厚のものが得られ、次いでカツター等で所定の長
さに切断するので長さもほぼ均一である。したが
つて、均一な形状で、かつ比重も一定となるた
め、使用中に一部の粒子が沈降するようなことも
なく、良好な流動性が得られる。さらに特筆すべ
きことは、本発明の筒状粒子を使用した微生物処
理装置等から排出される余剰微生物は従来のもの
よりも沈降性が著しく良好であるため、後段の
SS分離のための沈降槽、過槽を小型化するこ
とができ、しかもSS分離後は極めて透視度のす
ぐれた処理水を得ることができる。また、排出さ
れるSSの量が従来の粒子を用いた場合と比較し
て少ないことも本発明の特色の1つである。な
お、本発明の筒状粒子は水処理や発酵生産に利用
されるが、固定床方式以外の方法、すなわち固定
床装置を用いて水処理を行なう方法以外のものに
好適に用いられ、たとえば流動層装置、完全混合
装置等を用いて流動層、混合層、輸送層などを形
成して処理する方法に有利に適用することができ
る。その場合、処理法としては下向流、十字流、
上向流のいずれのタイプのものであつても差支え
なく、上向流とする場合にはガスを吹込むことに
より流動層、混合層を形成することができる。
従来の粒子を用いて水処理を行なつた場合、一
般に該粒子に微生物を付着させ流動層や混合槽な
どを形成せしめた生物反応槽では粒子同士の接触
が常に行なわれており、粒子表面に増殖、付着し
ている余剰の微生物はその一部が絶えず剥離さ
れ、系外に流出する。ところが、この余剰微生物
は極めて活性度が高く、微細であるため沈降性が
悪い。そのため、清澄な処理水を得るためには、
大型の重力沈降槽を用意したり、凝集剤を添加す
る等の対策が必要とされる。しかし、本発明の筒
状粒子を用いた場合、該粒子外表面に増殖、付着
する微生物は粒子同士の接触によつても容易には
剥離せず、粒子への付着時間が長い。また、筒状
粒子の内部表面に増殖、付着する微生物は粒子同
士の接触による剥離は行なわれず、該筒状粒子内
部を通過する水や気体の流れによつて剥離する。
このとき余剰微生物に与えられる力は外表面に存
在する余剰微生物に加えられる力よりも小さいた
め、剥離する微生物量は外表面に比し少なく、粒
子に対する微生物の付着時間は長くなる。そのた
め、筒状粒子の内部表面に付着している微生物の
粘性が増し、微生物同士の結合力も大きく、また
懸濁している微細で沈降性の悪い微生物等を捕獲
するため、水や気体の流れなどによつて剥離した
余剰微生物は凝集性が大きく、良好な沈降性を示
す。さらに、前記の如く懸濁している微生物の捕
獲のほか筒状粒子内部表面に付着している微生物
は外表面の微生物に比し一層剥離し難い。そのた
め、微生物の付着滞留時間が長くなり、好気性消
化が行なわれるので汚泥量が減少する。
次に、本発明の筒状粒子の使用例を示す。
使用例
異なる粗面化処理を施した中空筒状粒子(素
材:ポリプロピレン)を使用して水処理実験を行
ない、微生物の付着速度、付着微生物濃度、処理
水BODおよび処理水SS沈降速度を下記の下向流
流動層装置を使用して求めた。
第1図に示すようなエアーリフトチユーブ4を
内蔵し、エアーリフトチユーブ4下部と反応部3
下部に散気管を備えた微生物反応槽Aに第1表に
示すような各種の粒子を充填し、反応槽上部より
ポンプ2にて排水供給した。一方、エアーリフト
チユーブ内をエアーリフトにより上昇してくる処
理水の一部を原水と混合せしめて微生物を付着し
た粒子を充填した反応部に下向流で通水し、かつ
散気管からの曝気により該反応部の粒子層に空気
を供給し、排水中の有機物を好気的に微生物処理
した。なお処理条件は次の通りである。
反応槽:ポリ塩化ビニル樹脂製、直径4B、高さ
約80cm(容量約6)のものを4台使用
粒子充填量:約2
原水:魚肉エキスを水道水に溶解したもの
原水供給量:約2/hr
流動床エキスパンシヨン:静止層高の約1.5〜2
倍になるようにエアーリフトチユーブ4下部よ
り空気を供給。なお、散気管5a,5bより空
気を供給し、処理水の溶存酸素が1ppm以上保
てるように空気量を調整した。
実験期間:25ケ月
平均水温:20.7℃
原水BOD:約200ppm
The present invention relates to particles for adhesion of microorganisms, and more specifically to cylindrical particles made of synthetic resin for adhering to and supporting microorganisms used in water treatment and fermentation production, the outer surface of which is roughened to act as an adhesion agent for microorganisms. This invention relates to cylindrical particles with improved properties. Here, the term cylindrical particles refers to particles that are hollow through the particles and have a cut end, that is, a cross section, that is circular, elliptical, or polygonal (for example, triangular to dodecagonal, including star-shaped particles). BACKGROUND ART Conventionally, techniques covering a wide range of fields such as filtration, sedimentation separation, and biological treatment have been proposed for methods of treating wastewater such as domestic wastewater and industrial wastewater. Among these methods, methods have been developed that use carriers floating in water to effectively carry out filtration, biological treatment, etc. Furthermore, in fermentation for the purpose of producing specific useful substances, fixed microbial membrane methods have also been adopted, in which a carrier with a specific gravity lighter than the culture solution is used, and microorganisms are attached to the carrier to carry out fermentation. There is. The lightweight particles used in these methods include natural lightweight particles such as pearlite and shirasu balloons, synthetic resin particles with a specific gravity of less than 1, and synthetic resins made to have a low specific gravity by foaming, such as foamed Particles such as polyethylene, foamed polypropylene, and foamed polystyrene, which are already commercially available for purposes such as fillers, adsorbents, and heat insulating materials, are used. However, since lightweight natural materials easily absorb water, it is difficult to use them as particles that float on water semi-permanently. In addition, although synthetic resin particles with a low specific gravity have the advantage of being able to obtain uniform particles in large quantities, the adhesion strength between the microbial membrane and the particle surface is low, so there is a risk of friction between particles or between particles and the vessel wall, and between particles and water. In addition, there is a disadvantage that part or all of the microbial membrane may be peeled off due to shearing caused by air bubbles (hereinafter simply referred to as contact between particles), and from an economic point of view, the synthetic resin raw material is expensive, so particles The cost also becomes high. Under these circumstances, the present inventors found that the particles obtained by foaming a mixture of synthetic resin and inorganic material as the main component have excellent hydrophilicity, and have extremely high adhesion of microbial membranes. By changing the ratio of resin and inorganic material, most of the air bubbles in the particles are maintained as closed cells, so we discovered that they can be used as particles that float semi-permanently on water, and we have created a new particle for supporting microorganisms for water treatment. (Unexamined Japanese Patent Publication No. 1983)
−89897). Furthermore, as an improved version of the low-density particles, we developed low-density particles for supporting microorganisms, which are made by attaching inorganic and/or organic substances of a specific particle size to the surface of a foamed synthetic resin (patent application 1983-
No. 131241). This method not only increases the expansion ratio of the synthetic resin and reduces the amount of synthetic resin used as much as possible, but also has the feature that the specific gravity of the particles can be easily adjusted. However, what these particles for supporting microorganisms have in common is a treatment method in which microorganisms are attached to and supported on the particles and used without being fixed in a liquid.
For example, treatment methods using fluidized beds, mixed beds, etc. have the advantage of not being clogged by proliferating microorganisms that occur in treatment methods using fixed beds, and can maintain high concentrations of microorganisms, resulting in high reaction rates. However, the surplus microorganisms that separate from the particles are minute and have poor sedimentation properties, so when using a conventional gravity sedimentation tank for separating SS caused by surplus microorganisms in the latter stage, the equipment must be used to some extent. The disadvantage was that it had to be made larger. Therefore, in such water treatment methods, it has been desired to obtain surplus microorganisms with good sedimentation properties. The purpose of the present invention is to eliminate the above-mentioned drawbacks, discharge surplus microorganisms with good sedimentation properties, and provide microorganism adhesion particles that generate a small amount of surplus microorganisms and have excellent adhesion of microorganisms. be. The present invention provides cylindrical particles made of synthetic resin with a specific gravity of less than 1, which have an outer diameter of 1.5 to 15 mm, a length to outer diameter ratio of 0.2 to 6.0, and a wall thickness of 0.05 to 1.0 mm. These are particles for attaching microorganisms, which are made by roughening the outer surface of certain cylindrical particles by physical means. The synthetic resin used in the present invention has an apparent specific gravity of less than 1, and thermoplastic resins are particularly preferred, and specific examples thereof include polyethylene, polypropylene, polystyrene, and methylpentene polymers. Here, these synthetic resins should be interpreted in a broad sense; for example, taking polyethylene as an example, it includes not only homopolymers of ethylene but also copolymers of ethylene and other olefins. Furthermore, the present invention also includes synthetic resins that are foamed to have a specific gravity of less than 1.0. Cylindrical particles are obtained by applying known molding means to synthetic resin, and as mentioned above, the particles are hollow particles with a through hole, and the cut end, that is, the cross section is circular, elliptical, polygonal, etc. It is something. Common polygons include triangles, quadrilaterals, and hexagons.
Any shape up to the size of a dodecagon including a star shape is possible.
Cylindrical particles can be easily obtained, for example, by cutting a molded product obtained by extrusion molding into a certain length with a cutter, etc., but it is easy to manufacture and has a uniform microbial film. A material with a circular cross section is preferred because it is thick enough to be easily adhered to and has a large specific surface. The cylindrical particles of the present invention have an outer diameter of 1.5 to 15 mm, and the smaller the outer diameter, the larger the specific surface area, which is preferable, but if the outer diameter is less than 1.5 mm, the particles Because the particles adhere to each other due to the microorganisms attached to the surface, efficient water treatment cannot be performed, and because the inner surface of the particles is filled with microorganisms, the inside of the particles does not work effectively for reactions. becomes. On the other hand, if the outer diameter exceeds 15 mm, the amount of microorganisms retained decreases as the specific surface area decreases, and the reaction rate per unit volume decreases, resulting in a decrease in the reaction rate of conventional methods such as rotating disks, sprinkled beds, and submerged beds. , and the features of the present invention are lost. From the standpoint of reaction rate, the most preferred outer diameter of the particles is in the range of 1.5 to 10 mm. however,
When treating wastewater containing sugars, starches, etc., the film thickness of attached microorganisms becomes abnormally large, and if small particles are used, they may adhere to each other. Outer diameter is 10
It is suitable to use particles of about ~15 mm. Regarding the outer diameter of the cylindrical particles, if the cross section is other than circular, the equivalent circular diameter may be treated as the outer diameter. Next, the ratio (L/
D) should be between 0.2 and 6.0; if this ratio is less than 0.2, it will be difficult to retain microorganisms in the hollow interior, and the features of the present invention, such as a reduction in the amount of surplus microorganisms produced and good sedimentation properties, will be lost. I'm getting used to it. On the other hand, if this value exceeds 6.0, the length of the particles is too long and the mobility of the particles becomes poor during use.For example, when used in a fluidized bed, fluidity is significantly inhibited, and the particles are generated by microbial reactions. The disadvantages are that the aeration gas is encapsulated inside the cylindrical particles, which reduces the apparent specific gravity of the particles, and that microorganisms cannot be sufficiently retained inside the particles. Moreover, when this value is large, the packing efficiency of particles also decreases. Therefore, it is generally preferable that the ratio (L/D) is in the range of 0.5 to 3.0. In addition, the wall thickness of the cylindrical particles must be 0.05 to 1.0 mm, and if the wall thickness is less than 0.05 mm, the particle transport
They are easily damaged during storage, and if the diameter exceeds 1.0 mm, not only will the specific surface area of the inner surface of the cylindrical particles decrease, but the amount of synthetic resin used will increase, leading to higher costs. Although the diameter of the hollow portion varies depending on the outer diameter and wall thickness of the particle, it is usually preferably 1 mmφ or more. Furthermore, the microorganism-adhesive particles of the present invention have improved adhesion of microorganisms by roughening the outer surface by physical means. By performing this treatment, the amount of microorganisms retained per unit volume of particles can be increased. When particles are used for water treatment by forming a fluidized bed, mixed layer, transport layer, etc. without roughening the surface, most microorganisms usually adhere to the outer surface of the cylindrical particles due to contact between the particles. I won't. Such a phenomenon is undesirable from the standpoint of efficiently attaching microorganisms to particles and utilizing them. Therefore, roughening the outer surface is important for cylindrical particles for microbial attachment. Methods for roughening the outer surface of particles include, for example, a method in which the surface is heat-treated before cutting a molded object obtained by extrusion molding into a certain length, and a method in which the surface is etched using an acid such as concentrated sulfuric acid. . Although there are methods of processing by mechanical (that is, physical) means using an abrasive or the like, surface roughening treatment by physical means is most preferable. Physical surface treatment improves the adhesion of microorganisms by creating irregularities, folds, and scratches on the surface of particles, and also prevents most of the attached microorganisms from easily detaching even when particles come into contact with each other. can do. A more detailed study of the roughening state of the particle surface and the adhesion of microorganisms reveals that the difference in the roughening state due to the difference in the surface roughening treatment method has a great effect on the adhesion of microorganisms. In other words, unevenness is formed on the surface of particles that have been thermally or chemically treated, but these unevenness are generally smooth, and the adhesion of microorganisms is much greater than in the case of no treatment. However, microorganisms are relatively easily detached due to contact between particles. On the other hand, particles whose surfaces have been roughened by physical (mechanical) means have surface flaws such as "scratches" and "hangnails" on their surfaces. These surface flaws make it easy for microorganisms to adhere to the surface, and the microorganisms are also difficult to peel off due to contact between particles. When similar physical means are applied to cylindrical particles whose specific gravity has been lowered by adding a foaming agent to a synthetic resin, even sharper surface scratches are observed, but these occur near the surface of the cylindrical particles. This is thought to be due to the fact that closed cells are destroyed by physical treatment. As mentioned above, microorganisms are easily attached to particle surfaces that have sharp "scratches" and "hangnails".
It was found that the number of days required for adhesion is short, and that the attached microorganisms are difficult to separate even if the particles come into contact with each other. Therefore, in the present invention, cylindrical particles subjected to physical roughening treatment are preferred. Physical roughening treatment means include, for example, applying an abrasive or an abrasive brush to the surface of a cylindrical molded product obtained by extrusion molding, or using one or more sharp blades to scratch the surface. There are ways to attach it. Such treatment methods include fixing a surface treatment machine and continuously moving the cylindrical molded product, or rotating or reciprocating the machine to continuously treat the cylindrical molded product. Continuous operation is usually performed. Next, the surface-treated cylindrical molded body is cut into a predetermined length to obtain particles for attaching microorganisms of the present invention. Particles that have been subjected to physical roughening treatment have good adhesion to microorganisms, so the material for these particles should have a specific gravity of about 0.6 to 0.9 to prevent the particles from settling even when microorganisms are attached. Should be used. As mentioned above, the cylindrical particles of the present invention are made into a constant molded body by extrusion molding, etc., so that a uniform wall thickness is obtained, and then cut into a predetermined length with a cutter etc., so that the length can be adjusted. Almost uniform. Therefore, the shape is uniform and the specific gravity is constant, so that some particles do not settle during use and good fluidity can be obtained. What is also noteworthy is that the surplus microorganisms discharged from the microorganism treatment equipment using the cylindrical particles of the present invention have significantly better sedimentation properties than conventional ones, so they can be used in the subsequent stages.
The sedimentation tank and overtank for SS separation can be downsized, and treated water with extremely high transparency can be obtained after SS separation. Another feature of the present invention is that the amount of SS discharged is smaller than when conventional particles are used. Although the cylindrical particles of the present invention are used for water treatment and fermentation production, they are also suitably used for methods other than fixed bed methods, that is, methods other than water treatment using fixed bed equipment, such as fluidized It can be advantageously applied to a method of forming and processing a fluidized bed, mixed layer, transport layer, etc. using a bed device, complete mixing device, etc. In that case, the processing methods include downward flow, cross flow,
Any type of upward flow may be used; in the case of upward flow, a fluidized bed or a mixed bed can be formed by blowing gas. When water treatment is performed using conventional particles, the particles are constantly in contact with each other in a biological reaction tank in which microorganisms are attached to the particles to form a fluidized bed, mixing tank, etc. A portion of the excess microorganisms that have proliferated and adhered are constantly peeled off and flowed out of the system. However, these surplus microorganisms have extremely high activity and are microscopic, so they have poor sedimentation properties. Therefore, in order to obtain clear treated water,
Measures such as preparing a large gravity settling tank and adding a flocculant are required. However, when the cylindrical particles of the present invention are used, the microorganisms that proliferate and adhere to the outer surface of the particles are not easily peeled off even when the particles come into contact with each other, and the adhesion time to the particles is long. Further, microorganisms that grow and adhere to the inner surface of the cylindrical particles are not separated by contact between the particles, but are separated by the flow of water or gas passing through the interior of the cylindrical particles.
At this time, the force applied to the excess microorganisms is smaller than the force applied to the excess microorganisms present on the outer surface, so the amount of microorganisms to be peeled off is smaller than that on the outer surface, and the time for the microorganisms to adhere to the particles becomes longer. Therefore, the viscosity of the microorganisms attached to the inner surface of the cylindrical particles increases, the bonding force between microorganisms becomes large, and in order to capture suspended microorganisms that are fine and have poor sedimentation properties, the flow of water and gas increases. The excess microorganisms detached by this process have a high flocculation property and exhibit good sedimentation properties. Furthermore, in addition to capturing suspended microorganisms as described above, microorganisms attached to the inner surface of the cylindrical particles are more difficult to peel off than microorganisms on the outer surface. As a result, the residence time of microorganisms increases, and aerobic digestion occurs, reducing the amount of sludge. Next, an example of use of the cylindrical particles of the present invention will be shown. Usage example A water treatment experiment was conducted using hollow cylindrical particles (material: polypropylene) with different surface roughening treatments, and the adhesion rate of microorganisms, adhering microorganism concentration, treated water BOD, and treated water SS sedimentation rate were determined as follows. It was determined using a downward flow fluidized bed apparatus. It has a built-in air lift tube 4 as shown in Fig. 1, and the lower part of the air lift tube 4 and the reaction part 3
A microbial reaction tank A equipped with an aeration pipe at the bottom was filled with various particles as shown in Table 1, and waste water was supplied from the top of the reaction tank using a pump 2. On the other hand, part of the treated water that rises in the air lift tube with the air lift is mixed with raw water and passed in a downward flow to the reaction section filled with particles with microorganisms attached, and aeration is carried out from the air diffuser tube. Air was supplied to the particle layer in the reaction section, and the organic matter in the wastewater was aerobically treated with microorganisms. The processing conditions are as follows. Reaction tank: 4 units made of polyvinyl chloride resin, diameter 4B, height approx. 80cm (capacity approx. 6) Particle filling amount: Approx. 2 Raw water: Fish meat extract dissolved in tap water Raw water supply amount: Approx. 2 /hr Fluidized bed expansion: approximately 1.5 to 2 of the static bed height
Air is supplied from the bottom of air lift tube 4 so that it doubles. Note that air was supplied from the diffuser pipes 5a and 5b, and the amount of air was adjusted so that dissolved oxygen in the treated water could be maintained at 1 ppm or more. Experiment period: 25 months Average water temperature: 20.7℃ Raw water BOD: Approx. 200ppm
【表】
微生物の付着速度および付着微生物濃度に関し
て各々の粒子を使用した連続実験結果を第6図に
示す。第6図中、Mixed Liqur Suspended
Solid(MLSS)は微生物濃度を表わす。MLSS測
定は4台の反応槽より100c.c.の粒子を抜き取り、
0.3規定の炭酸ソーダ溶液中にサンプルを入れて
撹拌を行ない剥離した微生物濃度を求めることに
より行なつた。第6図はMLSSの経月変化を示す
ものである。
第6図より明らかなように、物理的表面処理を
施した粒子は発泡、無発泡に関係なく、MLSS濃
度が高く微生物保持能力に極めてすぐれている。
また、微生物の付着速度に関しても、1ケ月以内
に急速な付着が行なわれ、それ以降は微生物濃度
は平衡に達する。平衡時におけるMLSS濃度は
18000〜20000ppmに達し、粒子No.3およびNo.4と
比較し、極めて高濃度に微生物を保持することが
判明した。
一方、化学的表面処理を施した粒子No.3は物理
的表面処理を施した粒子に比較して微生物付着速
度が緩やかであり、1.5〜2ケ月でほぼ平衡状態
に達するが、その時のMLSS濃度もやや少なく
5000ppm未満である。
さらに、粒子表面に対して粗面化処理を行わな
かつたNo.4の粒子は約1ケ月の間微生物の付着が
ほとんどなかつた。1.5ケ月よりMLSSは増加し
たが、外表面の状態は粒子と粒子の接触により光
沢があり、微生物はほとんど付着していない。
MLSSの増加は内筒部の内表面に付着増殖してき
た微生物に起因するものと考えられる。このた
め、4種の粒子のうち平衡時のMLSS濃度は一番
低い値を示した。1.5ケ月から2.5ケ月のほぼ平衡
状態となつたときの処理水SS沈降速度および処
理水質のBOD濃度(平均値)を示すと第2表の
ようになつた。[Table] Figure 6 shows the results of continuous experiments using each particle regarding the rate of attachment of microorganisms and the concentration of attached microorganisms. In Figure 6, Mixed Liqur Suspended
Solid (MLSS) represents the microbial concentration. For MLSS measurement, 100c.c. of particles were extracted from four reaction vessels.
The sample was placed in a 0.3N sodium carbonate solution, stirred, and the concentration of detached microorganisms was determined. Figure 6 shows the menstrual changes in MLSS. As is clear from FIG. 6, particles subjected to physical surface treatment have a high MLSS concentration and an extremely excellent ability to retain microorganisms, regardless of foaming or non-foaming.
Furthermore, regarding the rate of attachment of microorganisms, rapid attachment occurs within one month, after which the concentration of microorganisms reaches equilibrium. The MLSS concentration at equilibrium is
It reached 18,000 to 20,000 ppm, and was found to retain microorganisms at an extremely high concentration compared to particles No. 3 and No. 4. On the other hand, particle No. 3 with chemical surface treatment has a slower microbial adhesion rate than particles with physical surface treatment, reaching an almost equilibrium state in 1.5 to 2 months, but the MLSS concentration at that time Somewhat less hazy
Less than 5000ppm. Furthermore, particles No. 4 whose particle surfaces were not subjected to surface roughening treatment had almost no adhesion of microorganisms for about one month. Although the MLSS increased after 1.5 months, the outer surface was shiny due to particle-to-particle contact, and almost no microorganisms were attached.
The increase in MLSS is considered to be due to microorganisms that adhere to and proliferate on the inner surface of the inner cylinder. Therefore, the MLSS concentration at equilibrium showed the lowest value among the four types of particles. Table 2 shows the SS sedimentation rate of the treated water and the BOD concentration (average value) of the treated water after 1.5 to 2.5 months of almost equilibrium.
【表】
以上の4種の粒子についての同時比較実験によ
り、表面に物理的処理をして多数の表面傷をつけ
た粒子の表面には微生物が極めて付着し易く、微
生物の濃度も極めて高濃度に保持され、処理水質
も極めて良好で処理水SS沈降速度も著しく速い
ものが得られることが判明した。[Table] Simultaneous comparative experiments on the four types of particles mentioned above revealed that microorganisms easily adhere to the surfaces of particles whose surfaces have been physically treated and have many surface scratches, and the concentration of microorganisms is also extremely high. It was found that the SS of the treated water was maintained at a very high quality, the quality of the treated water was very good, and the SS sedimentation rate of the treated water was extremely fast.
第1図は好気性処理装置の説明図であり、第2
図〜5図は本発明の粒子の実施例の見取図であ
る。第6図はMLSSの経月変化を示すグラフであ
る。
1……原水供給管、2……ポンプ、3……反応
部、4……エアーリフトチユーブ、5a,5b…
…散気管、6……処理水抜出し管、A……反応
槽。
FIG. 1 is an explanatory diagram of the aerobic treatment device, and the second
Figures 5 to 5 are sketches of examples of particles of the present invention. FIG. 6 is a graph showing menstrual changes in MLSS. 1...Raw water supply pipe, 2...Pump, 3...Reaction section, 4...Air lift tube, 5a, 5b...
... Diffuser pipe, 6... Treated water extraction pipe, A... Reaction tank.
Claims (1)
あつて、外径が1.5〜15mm、長さと外径の比が0.2
〜6.0であり、かつ肉厚が0.05〜1.0mmである筒状
粒子の外表面を物理的手段により粗面化処理して
なる微生物付着用粒子。 2 合成樹脂が熱可塑性樹脂である特許請求の範
囲第1項記載の微生物付着用粒子。[Claims] 1. Cylindrical particles made of synthetic resin with a specific gravity of less than 1, with an outer diameter of 1.5 to 15 mm and a length to outer diameter ratio of 0.2.
6.0 and a wall thickness of 0.05 to 1.0 mm, the outer surface of the cylindrical particles is roughened by physical means. 2. Particles for attaching microorganisms according to claim 1, wherein the synthetic resin is a thermoplastic resin.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP57176358A JPS58198288A (en) | 1982-10-08 | 1982-10-08 | Particles for attaching microorganisms |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP57176358A JPS58198288A (en) | 1982-10-08 | 1982-10-08 | Particles for attaching microorganisms |
Related Parent Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP8026582A Division JPS5928391B2 (en) | 1982-05-14 | 1982-05-14 | Particles for attaching microorganisms |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS58198288A JPS58198288A (en) | 1983-11-18 |
| JPH0242473B2 true JPH0242473B2 (en) | 1990-09-21 |
Family
ID=16012208
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP57176358A Granted JPS58198288A (en) | 1982-10-08 | 1982-10-08 | Particles for attaching microorganisms |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS58198288A (en) |
Families Citing this family (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS61176000U (en) * | 1985-04-24 | 1986-11-01 | ||
| JP4530320B2 (en) * | 2001-05-22 | 2010-08-25 | 三菱レイヨン株式会社 | Microorganism immobilization carrier |
| JP2006015310A (en) * | 2004-07-05 | 2006-01-19 | Nippon Steel Chem Co Ltd | Nitrate nitrogen treatment material and method for producing the same |
| JP4979946B2 (en) * | 2005-12-27 | 2012-07-18 | 栗田工業株式会社 | Method for producing biofilm-forming carrier and biofilm-forming carrier |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5928391A (en) * | 1982-08-10 | 1984-02-15 | Nec Corp | Hetero-junction type photodetector |
-
1982
- 1982-10-08 JP JP57176358A patent/JPS58198288A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS58198288A (en) | 1983-11-18 |
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