JP3171554B2 - Microbial carrier - Google Patents
Microbial carrierInfo
- Publication number
- JP3171554B2 JP3171554B2 JP06770896A JP6770896A JP3171554B2 JP 3171554 B2 JP3171554 B2 JP 3171554B2 JP 06770896 A JP06770896 A JP 06770896A JP 6770896 A JP6770896 A JP 6770896A JP 3171554 B2 JP3171554 B2 JP 3171554B2
- Authority
- JP
- Japan
- Prior art keywords
- carrier
- microorganism carrier
- microorganism
- specific gravity
- thickness
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
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
- Immobilizing And Processing Of Enzymes And Microorganisms (AREA)
- Biological Treatment Of Waste Water (AREA)
Description
【0001】[0001]
【発明の属する技術分野】本発明は、下水、ゴミ浸出
水、産業廃水等の有機性廃水の生物処理に使用される微
生物担体に関するものである。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a microorganism carrier used for biological treatment of organic wastewater such as sewage, leachate leachate, and industrial wastewater.
【0002】[0002]
【従来の技術】有機性廃水の生物処理においては、従来
から高負荷対策、硝化/脱窒時間の短縮等の目的で種々
の微生物担体が曝気槽に投入され、MLSS(活性汚
泥)単独の場合と比較してより短時間で処理を完了させ
る工夫がなされている。これらの微生物担体は浮遊状態
で用いるために、比重が1程度で大きさが3〜7mmの略
立方体または球状体とされており、材質としてはポリビ
ニルアルコール、ポリエチレングリコール、ポリウレタ
ン、セルロース等が普通である。2. Description of the Related Art In the biological treatment of organic wastewater, various microorganism carriers have been put into an aeration tank for the purpose of high load countermeasures, shortening of nitrification / denitrification time, and the like. In order to complete the process in a shorter time than in the case of the above, a device is devised. Since these microorganism carriers are used in a suspended state, they have a specific gravity of about 1 and are generally cubic or spherical with a size of 3 to 7 mm, and are usually made of polyvinyl alcohol, polyethylene glycol, polyurethane, cellulose, or the like. is there.
【0003】微生物担体の大きさは大きければ大きいほ
どMLSS(活性汚泥)との分離が簡単となり、曝気槽
からの流失を防止し易くなる。しかし上記のように大き
さが10mm以下に制限されていたのは、大きさが10mmを越
えると沈降し易くなり、MLSSとの比重差を僅かにし
ても処理水との均一な混合が困難となるためである。[0003] The larger the size of the microorganism carrier, the easier it is to separate it from MLSS (activated sludge), and the more easily it is prevented from flowing out of the aeration tank. However, as described above, the size was limited to 10 mm or less, because if the size exceeds 10 mm, sedimentation is likely to occur, and even if the specific gravity difference with MLSS is small, uniform mixing with treated water is difficult. It is because it becomes.
【0004】また微生物担体の大きさを小さくするほど
比表面積が増加するため、微生物の付着量を増大させる
ことができるとともに、処理水との均一な混合が容易と
なる。しかし小さ過ぎるとMLSSとの分離が困難とな
る。このために従来通常に使用されている微生物担体は
比重が1.02〜1.05で大きさが3〜7mmの粒子である。Since the specific surface area increases as the size of the microorganism carrier decreases, the amount of adhered microorganisms can be increased and uniform mixing with treated water becomes easy. However, if it is too small, separation from the MLSS becomes difficult. For this reason, microorganism carriers conventionally used usually are particles having a specific gravity of 1.02 to 1.05 and a size of 3 to 7 mm.
【0005】上記したように、微生物担体の大きさ/形
状に関しては性能及び沈降しにくさと、MLSSとの分
離の容易さとは相反するものであり、特に深槽曝気槽の
ように散気設備が槽の中間深さの部分に設置されている
ために槽底部の流速が小さい場合には、通常の微生物担
体では槽底部に沈殿してしまうことがあった。なおこの
問題を解決するために、散気量を過大にし槽底部に流速
を大きくして沈降を防止する方法や、深槽を縦に2分割
して死水域を減少させる方法等があるが、いずれの方法
も旋回流速が大きくなることによる微生物担体の損耗が
激しくなったり、曝気動力のための運転費がかさんだ
り、設備改造に多大の費用がかかる等の実用上の問題が
あった。[0005] As described above, regarding the size / shape of the microorganism carrier, the performance and the difficulty of sedimentation are inconsistent with the ease of separation from the MLSS. When the flow rate at the bottom of the tank is low because the water is placed at the middle depth of the tank, the usual microorganism carrier may precipitate at the bottom of the tank. In order to solve this problem, there are a method of preventing the sedimentation by increasing the amount of diffused air and increasing the flow velocity at the bottom of the tank, and a method of vertically dividing the deep tank into two parts to reduce dead water area. All of these methods have practical problems such as increased wear of the microbial carrier due to an increase in the swirling flow rate, an increase in operating costs for aeration power, and a large cost for equipment remodeling.
【0006】[0006]
【発明が解決しようとする課題】本発明は上記した従来
の問題点を解決し、微生物の付着量を増大させることが
でき、少ない曝気動力で処理水との均一な混合が容易で
あり、しかもMLSSとの分離も容易な微生物担体を提
供するためになされたものである。SUMMARY OF THE INVENTION The present invention solves the above-mentioned conventional problems, can increase the amount of adhered microorganisms, facilitates uniform mixing with treated water with a small amount of aeration power, and The purpose of the present invention is to provide a microorganism carrier that can be easily separated from MLSS.
【0007】[0007]
【課題を解決するための手段】上記の課題を解決するた
めになされた本発明の微生物担体は、比重が1.0 〜1.1
の高分子材料からなり、厚みが0.5〜2 mmであり、かつ
一辺の長さが7〜20mmの板状体であることを特徴とする
ものである。なお、一辺の長さ/厚みとして定義される
アスペクト比を3.5 以上とすることが好ましい。使用さ
れる高分子材料は例えばポリビニルアルコールゲルとす
ることができる。また平板体の表面は平面とするほか、
湾曲面とすることも可能である。The microorganism carrier of the present invention made to solve the above problems has a specific gravity of 1.0 to 1.1.
Characterized by a plate-like body having a thickness of 0.5 to 2 mm and a side length of 7 to 20 mm . The aspect ratio defined as the length / thickness of one side is preferably 3.5 or more. The polymeric material used can be, for example, a polyvinyl alcohol gel. In addition to the flat surface of the flat body,
A curved surface is also possible.
【0008】[0008]
【発明の実施の形態】以下に図面を参照しつつ本発明の
好ましい実施の形態を示す。図1は平板状の微生物担体
の例を示すもので、ポリビニルアルコールゲル等の高分
子材料からなる一辺の長さが7〜20mmの正方形状であ
り、厚み一辺の長さ/厚みとして定義されるアスペクト
比を3.5 以上としたものである。なおこれらの値から機
械的に計算すると、厚みの最大値は5.7mm となるが、厚
みを増加させると内部が微生物の付着に寄与しないデッ
ドゾーンとなるので、実際には厚みは2mm以下とするこ
とが好ましい。最も好ましい厚みは0.5 〜1.5mm であ
り、アスペクト比は5〜100 程度の範囲とすることが好
ましい。なお図2は表面を湾曲させた微生物担体の例を
示すもので、材料、サイズ、厚み等は図1のものと同様
である。また湾曲状態は図示のような単純な形状の他に
W状等としてもよいが、水中でひらひらと舞うことがで
きることが必要であるため、板状の形態から大きく外れ
ることは好ましくない。Preferred embodiments of the present invention will be described below with reference to the accompanying drawings. FIG. 1 shows an example of a plate-shaped microbial carrier, which is made of a polymer material such as polyvinyl alcohol gel and has a square shape with a side length of 7 to 20 mm, and is defined as the length / side length / thickness. The aspect ratio is set to 3.5 or more. When mechanically calculated from these values, the maximum value of the thickness is 5.7 mm. However, when the thickness is increased, the inside becomes a dead zone that does not contribute to the attachment of microorganisms. Therefore, the thickness is actually 2 mm or less. Is preferred. The most preferable thickness is 0.5 to 1.5 mm, and the aspect ratio is preferably in the range of about 5 to 100. FIG. 2 shows an example of a microorganism carrier having a curved surface, and the material, size, thickness and the like are the same as those in FIG. In addition, the curved state may be a W shape or the like in addition to the simple shape as shown in the figure, but it is necessary to be able to flutter underwater, so it is not preferable that the shape deviates significantly from the plate shape.
【0009】このような本発明の微生物担体は、従来の
粒状の微生物担体に比較してMLSS中で沈降する際の
抵抗が大きくなり、沈降しにくくなる。図3は本発明の
微生物担体と従来の微生物担体との沈降速度を比較した
グラフである。本発明の微生物担体としては厚みを1.0m
m の一定値とし、一辺の長さを様々に変えた図1の形状
のものを準備し、また対照品として一辺の長さが5mmの
立方体の微生物担体を準備した。なお材質はともに比重
が1.03のポリビニルアルコールゲルとした。[0009] Such a microorganism carrier of the present invention has a greater resistance to settling in the MLSS than a conventional granular microorganism carrier, and is less likely to settle. FIG. 3 is a graph comparing the sedimentation rates of the microorganism carrier of the present invention and a conventional microorganism carrier. The thickness of the microorganism carrier of the present invention is 1.0 m
1 was prepared with a constant value of m, and the length of each side was variously changed. A cubic microorganism carrier having a side length of 5 mm was prepared as a control. The material was a polyvinyl alcohol gel having a specific gravity of 1.03.
【0010】次に本発明の微生物担体の流動性を確認す
るため、図4に示した深槽曝気槽のスケールモデルを用
いて、テストを行なった。この図4のモデルは槽体1の
中段に散気装置2を配置するとともに、槽体1の幅方向
の中央に垂直な隔壁3を設けたものである。本発明の微
生物担体としては一辺の長さ及び厚みを様々に変えた図
1の形状のものを準備し、また対照品として一辺の長さ
が5mmの立方体の微生物担体を準備した。なお材質はと
もに比重が1.03のポリビニルアルコールゲルとした。Next, in order to confirm the fluidity of the microorganism carrier of the present invention, a test was conducted using a scale model of a deep aeration tank shown in FIG. In the model of FIG. 4, the air diffuser 2 is arranged in the middle of the tank body 1, and a vertical partition wall 3 is provided at the center in the width direction of the tank body 1. As the microbial carrier of the present invention, those having the shapes shown in FIG. 1 with various lengths and thicknesses of one side were prepared, and a cubic microbial carrier having a side length of 5 mm was prepared as a control. The material was a polyvinyl alcohol gel having a specific gravity of 1.03.
【0011】図5はこれらの微生物担体を均一に流動さ
せるために要する最低通気量を示すグラフであり、流動
化可能通気率(水量1m3 当り1時間に要する散気空気
量)に換算して示してある。なお図5中の破線は、実規
模の深槽曝気槽で通常の散気量とした場合の槽底部の流
速を与えるスケールモデル槽での通気量であり、この通
気量以下で微生物担体が均一に流動化すれば、実規模の
深槽曝気槽でも良好な流動が可能なことを意味する。こ
の図5に示されるように、厚みが2mm以下で一辺の長さ
を7〜20mmの範囲内としたものは、良好な流動性を示
す。FIG. 5 is a graph showing the minimum aeration required to make these microorganism carriers flow uniformly, which is converted into a fluidizable aeration rate (amount of diffused air required for 1 hour per 1 m 3 of water). Is shown. The broken line in FIG. 5 indicates the air flow rate in the scale model tank which gives the flow velocity at the bottom of the tank when the normal aeration volume is set in the full-scale deep aeration tank. Means that good flow is possible even in a full-scale deep aeration tank. As shown in FIG. 5, a material having a thickness of 2 mm or less and a length of one side in the range of 7 to 20 mm shows good fluidity.
【0012】また、微生物担体の一辺の長さを従来品よ
りも大きくすることによって、MLSSと微生物担体と
をスクリーン等で分離する場合の目開きを大きくするこ
とができる。例えば、一辺が7mmの微生物担体ならば目
開きが5mm□のスクリーンが使用でき、一辺が20mmの微
生物担体ならば目開きが15mm□のスクリーンが使用でき
る。このため、目開きの細かいスクリーンを使用せざる
を得なかった従来品に比較して、スクリーンの目詰まり
の清掃等の維持管理作業を大幅に低減することができ
る。Further, by making the length of one side of the microorganism carrier larger than that of the conventional product, the aperture when separating the MLSS and the microorganism carrier by a screen or the like can be increased. For example, when the microorganism carrier has a side of 7 mm, a screen having an aperture of 5 mm can be used. When the microorganism carrier has a side of 20 mm, a screen having an aperture of 15 mm can be used. For this reason, maintenance management work such as cleaning of clogging of the screen can be significantly reduced as compared with a conventional product in which a screen having a fine opening has to be used.
【0013】上記したように、本発明の微生物担体は沈
降しにくく、流動性が良好であるので、従来品よりも比
重を大きくすることができる。即ち、従来品の比重は最
大でも1.05程度とする必要があったが、本発明の微生物
担体は比重を1.1程度としても流動性が損なわれない。
図6は本発明品の比重を変化させた場合の流動化可能通
気率を示すグラフであり、一辺の長さが20mmで、厚みが
0.5mm 、1.0mm 、2.0mm の3種類の微生物担体を使用し
た。この図6のグラフから分かるように、本発明の微生
物担体は比重を1.1 まで増加させても流動性が良好であ
る。また当然のことであるが、微生物担体の浮上を防止
するためには比重は1.0 以上とする必要がある。As described above, since the microorganism carrier of the present invention hardly sediments and has good flowability, the specific gravity can be made larger than that of the conventional product. That is, although the specific gravity of the conventional product had to be about 1.05 at the maximum, the fluidity of the microorganism carrier of the present invention is not impaired even when the specific gravity is about 1.1.
FIG. 6 is a graph showing the fluidizable air permeability when the specific gravity of the product of the present invention is changed. The length of one side is 20 mm and the thickness is 20 mm.
Three types of microbial carriers of 0.5 mm, 1.0 mm and 2.0 mm were used. As can be seen from the graph of FIG. 6, the microbial carrier of the present invention has good fluidity even when the specific gravity is increased to 1.1. Needless to say, the specific gravity needs to be 1.0 or more in order to prevent the floating of the microorganism carrier.
【0014】[0014]
【発明の効果】以上に説明したように、本発明の微生物
担体は沈降しにくく流動性が良好であるので、従来品よ
りも通気率を減少させることができ、曝気動力を10〜30
%程度削減することができる。また本発明の微生物担体
はMLSSとの比重差を大きくとることができるので、
担体分離槽における担体流出の危険性をなくすることが
できる。更に本発明の微生物担体は一辺の長さを大きく
したので、スクリーン等により担体分離を行なう場合で
も目詰まりのおそれのない目開きが5mm以上のスクリー
ンを使用することができる。しかも板状体としたので微
生物の付着に寄与する比表面積を大きくとることがで
き、多量の微生物を担持させることができる。As described above, since the microorganism carrier of the present invention hardly sediments and has good fluidity, the air permeability can be reduced as compared with the conventional product, and the aeration power can be reduced by 10 to 30.
% Can be reduced. Also, since the microorganism carrier of the present invention can take a large difference in specific gravity from MLSS,
The risk of carrier outflow in the carrier separation tank can be eliminated. Further, since the length of one side of the microbial carrier of the present invention is increased, a screen having a mesh size of 5 mm or more without clogging can be used even when the carrier is separated by a screen or the like. Moreover, since the plate-like body is used, the specific surface area contributing to the attachment of microorganisms can be increased, and a large amount of microorganisms can be supported.
【図1】平板状の微生物担体の例を示す斜視図である。FIG. 1 is a perspective view showing an example of a plate-shaped microorganism carrier.
【図2】湾曲状の微生物担体の例を示す斜視図である。FIG. 2 is a perspective view showing an example of a curved microorganism carrier.
【図3】担体寸法と沈降速度との関係を示すグラフであ
る。FIG. 3 is a graph showing a relationship between a carrier size and a sedimentation velocity.
【図4】実験に使用したスケールモデルの断面図であ
る。FIG. 4 is a cross-sectional view of a scale model used in an experiment.
【図5】担体寸法と流動化可能通気率との関係を示すグ
ラフである。FIG. 5 is a graph showing the relationship between carrier size and fluidizable air permeability.
【図6】担体の比重と流動化可能通気率との関係を示す
グラフである。FIG. 6 is a graph showing the relationship between the specific gravity of the carrier and the fluidizable air permeability.
1 槽体、2 散気槽、3 隔壁 1 tank body, 2 diffuser tanks, 3 partition walls
───────────────────────────────────────────────────── フロントページの続き (58)調査した分野(Int.Cl.7,DB名) C02F 3/02 - 3/10 C12N 11/00 - 13/00 ──────────────────────────────────────────────────続 き Continued on the front page (58) Field surveyed (Int. Cl. 7 , DB name) C02F 3/02-3/10 C12N 11/00-13/00
Claims (4)
り、厚みが0.5〜2 mmであり、かつ一辺の長さが7〜20m
mの板状体であることを特徴とする微生物担体。1. A high-molecular material having a specific gravity of 1.0 to 1.1, a thickness of 0.5 to 2 mm, and a length of one side of 7 to 20 m.
A microbial carrier, which is a plate-like member having a m-like shape.
ペクト比が3.5 以上である請求項1記載の微生物担体。2. The microorganism carrier according to claim 1, wherein an aspect ratio defined as length / thickness of one side is 3.5 or more.
である請求項1または2記載の微生物担体。3. The microorganism carrier according to claim 1, wherein the polymer material is a polyvinyl alcohol gel.
かに記載の微生物担体。4. The microorganism carrier according to claim 1, wherein the surface is curved.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP06770896A JP3171554B2 (en) | 1996-03-25 | 1996-03-25 | Microbial carrier |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP06770896A JP3171554B2 (en) | 1996-03-25 | 1996-03-25 | Microbial carrier |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH09253681A JPH09253681A (en) | 1997-09-30 |
JP3171554B2 true JP3171554B2 (en) | 2001-05-28 |
Family
ID=13352737
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP06770896A Expired - Fee Related JP3171554B2 (en) | 1996-03-25 | 1996-03-25 | Microbial carrier |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP3171554B2 (en) |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP4994349B2 (en) * | 2008-12-01 | 2012-08-08 | メタウォーター株式会社 | Nitrification carrier circulation method in deep tank aeration tank |
-
1996
- 1996-03-25 JP JP06770896A patent/JP3171554B2/en not_active Expired - Fee Related
Also Published As
Publication number | Publication date |
---|---|
JPH09253681A (en) | 1997-09-30 |
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