JPS62106894A - Filter material for anaerobic treatment of sanitary sewage - Google Patents
Filter material for anaerobic treatment of sanitary sewageInfo
- Publication number
- JPS62106894A JPS62106894A JP60246669A JP24666985A JPS62106894A JP S62106894 A JPS62106894 A JP S62106894A JP 60246669 A JP60246669 A JP 60246669A JP 24666985 A JP24666985 A JP 24666985A JP S62106894 A JPS62106894 A JP S62106894A
- Authority
- JP
- Japan
- Prior art keywords
- sheets
- anaerobic
- sludge
- treatment
- wastewater
- 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.)
- Granted
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
- Purification Treatments By Anaerobic Or Anaerobic And Aerobic Bacteria Or Animals (AREA)
- Biological Treatment Of Waste Water (AREA)
Abstract
Description
【発明の詳細な説明】 (イ)産業上の利用分野 本発明は汚水処理槽に使用する濾材に関する。[Detailed description of the invention] (b) Industrial application fields The present invention relates to a filter medium used in a sewage treatment tank.
更に詳しくは、本発明は汚水を生物学的処理により浄化
する嫌気性適法に用いる1材の構造に関する。More specifically, the present invention relates to the structure of a single material used in an anaerobic method for purifying wastewater by biological treatment.
(ロ)従来の技術及びこの発明が解決しようとする問題
点
廃水の生物学的処理は好気性菌による好気性処理と嫌気
性菌による嫌気性処理に大別される。好気性処理は反応
時間が短く、良好な処理水質が得られるために、一般的
に廃水は活性汚泥法及び生物模法で代表される好気性処
理で処理されてきた。(B) Prior art and problems to be solved by the present invention Biological treatment of wastewater is broadly divided into aerobic treatment using aerobic bacteria and anaerobic treatment using anaerobic bacteria. Since aerobic treatment requires a short reaction time and provides good treated water quality, wastewater has generally been treated by aerobic treatment, typified by the activated sludge method and the biological simulation method.
一方嫌気性処理はごく小規模の館処理として採用された
ものの、殆んどは、し尿や汚泥処理の一部に使われたに
すぎない。しかしながら、最近廃水処理に省エネルギー
化が推進される様になって、嫌気性処理が見直されてき
た。つまり好気性処理は絶えず曝気により酸素を供給し
なければならず、この装置に大きな動力費が必要となる
。これに対し嫌気性処理では酸素の供給を必要としない
ばかりではなく、反対に酸素の存在は反応を阻害するの
である。このように曝気操作が不要であることは動力費
が著しく節減されることになり省エネルギー化ができる
。また嫌気性処理の終産物はメタンと炭酸ガスであり、
前者のメタンはエネルギー源として回収できるし、廃水
中の病原微生物や寄生虫卵は速やかに死滅する。嫌気性
処理はこのような利点があるものの反応速度が遅い、処
理水質が悪い、微生物と汚濁物質との接触効率が悪いな
どの欠点がある。On the other hand, although anaerobic treatment was adopted as a very small-scale treatment, it was mostly used only for part of the treatment of human waste and sludge. However, recently, as energy conservation has been promoted in wastewater treatment, anaerobic treatment has been reconsidered. In other words, aerobic treatment requires constant supply of oxygen through aeration, which requires large power costs for this equipment. In contrast, anaerobic treatment not only does not require the supply of oxygen, but on the contrary, the presence of oxygen inhibits the reaction. Since no aeration operation is required in this way, power costs are significantly reduced, resulting in energy savings. The end products of anaerobic treatment are methane and carbon dioxide,
The former, methane, can be recovered as an energy source, and pathogenic microorganisms and parasite eggs in wastewater are quickly killed. Although anaerobic treatment has these advantages, it has disadvantages such as slow reaction rate, poor quality of treated water, and poor contact efficiency between microorganisms and pollutants.
ところで具体的に産業排水、下水道、し尿等の排水処理
或いは生活雑排水との合併処理には主に好気性菌による
生物学的処理が酋及し主流となついるが好気性菌による
接触曝気槽の前に沈澱分離槽又は嫌気性濾床を配置して
、接触曝気槽の負荷を軽減し浄化能力を向上する方法が
最近行なわれつある。沈澱電離槽は処理装置の構造が簡
単であり、維持管理は容易であるが嫌気性微生物の反応
速度が遅いことから滞留時間を長くとる必要があり、そ
のため2槽以上4槽以下位の槽を接続したり、槽容最を
大きくするほか、流潰変動が大きいと嫌気性菌が洗い出
されてしまい、浄化能力が著しく低下する等の問題点が
ある。従って現在の構造では汚水中の固形物を分離する
働きしか行なわれていない。これに対して濾床を充填し
た嫌気性−床法は多量の嫌気性菌の棲息を可能とし、か
なりの汚水中の有機物の分解が期待できることから最近
とくに合併式浄化槽の前処理法として実用化が進められ
つつある。この方法の利点としては、■ 生物処理槽内
に接触濾材が充填されているので汚泥を返送する必要が
なく維持管理が容易である。By the way, specifically, biological treatment using aerobic bacteria is mainly used to treat wastewater such as industrial wastewater, sewage, human waste, or combined treatment with domestic wastewater, but contact aeration tanks using aerobic bacteria are used. Recently, a method has been used to reduce the load on the contact aeration tank and improve the purification capacity by placing a sedimentation separation tank or an anaerobic filter bed in front of the contact aeration tank. Precipitation ionization tanks have a simple processing equipment structure and are easy to maintain, but the reaction rate of anaerobic microorganisms is slow, so it is necessary to have a long residence time. In addition to making connections and increasing the tank capacity, there are problems such as large fluctuations in flow and collapse will wash out anaerobic bacteria and significantly reduce purification ability. Therefore, the current structure only serves to separate solids from wastewater. On the other hand, the anaerobic bed method, which is filled with a filter bed, allows a large number of anaerobic bacteria to inhabit and can be expected to decompose a considerable amount of organic matter in wastewater, so it has recently been put into practical use as a pretreatment method for combined septic tanks. is being advanced. Advantages of this method include (1) Since the biological treatment tank is filled with contact filter media, there is no need to return the sludge, and maintenance is easy.
■ 汚泥生成量が少なく、かつ汚泥の沈降性も良好であ
る。■ The amount of sludge produced is small and the sludge settles well.
■ 多聞の電力を要する曝気を全く必要としない。■ Aeration, which requires a large amount of electricity, is not required at all.
等がある。しかし反面、嫌気性菌の膜体に対する付着力
が一般的に弱く、捕捉がしにくい欠点がある。etc. However, on the other hand, the adhesion of anaerobic bacteria to the membrane is generally weak, making it difficult to capture them.
かくして、嫌気性濾床に使用されている濾材の多くは立
体網状体やひも状接触材で好気性菌に用いられる平板状
接触材が使用される場合もある。Thus, most of the filter media used in anaerobic filter beds are three-dimensional mesh bodies or string-like contact materials, and in some cases, plate-like contact materials used for aerobic bacteria are also used.
網状体・ひも状体は好気性1床の濾材としては好適であ
るが嫌気性濾床はエヤーレーションによる曝気撹拌がな
いために嫌気性濾材としては次の問題があった。Although mesh and string bodies are suitable as aerobic one-bed filter media, anaerobic filter beds have the following problems because they do not require aeration and agitation by aeration.
■ 菌(微生物)の捕捉性が良くない。■ Poor ability to trap bacteria (microorganisms).
■ 槽内の汚水の流れを阻害する様な構造であり撹拌効
果が悪い。■ The structure obstructs the flow of wastewater in the tank, resulting in poor agitation effect.
■ 目づまりして汚泥の閉塞が生じ易い。■ It is easy to get clogged with sludge.
■ 網状体は充填する容器や枠体を、ひも状体は上下に
張る枠体を必要とするため設備や充填作業に手間がかか
り建設コスト高になる。■ Net-like materials require containers and frames to be filled, and string-like materials require frames to be stretched above and below, which requires time and effort in equipment and filling work, resulting in high construction costs.
一方、好気性菌に使用される平板状接触材(例えば特公
昭47−7301号公報参照)、又は水平断面で屈曲し
ているが各屈曲面が垂直な接触材を用いると嫌気性菌は
付着力が弱いため、捕捉効率が著しく低下するという問
題点があった。On the other hand, if a flat contact material used for aerobic bacteria (for example, see Japanese Patent Publication No. 47-7301) or a contact material that is bent in horizontal section but each curved surface is vertical is used, anaerobic bacteria will not be attracted to it. Since the adhesion force was weak, there was a problem in that the capture efficiency was significantly reduced.
(ハ)問題点を解決するための手段及びその作用この発
明は、同一形状で略垂直の多数のシートを、平面上で交
互に半回転させて重ね合せ、接触部分を接着してブロッ
ク状に構成してなり、その各シートは、水平断面では連
続して屈曲し、その各屈曲面が全体的に垂直に対し一方
に傾斜して、それらの傾斜する各屈曲面に垂直断面略し
字状の汚泥一時捕捉用凹部を傾斜方向に間隔を有して形
成し、
且つその凹部の底面部が、幅方向に傾斜し、更に奥行方
向に汚泥流下抵抗用凸条を備えてなる嫌気性汚水処理用
濾材である。(c) Means for solving the problem and its effect This invention consists of stacking a large number of substantially vertical sheets of the same shape alternately by half a turn on a plane, and bonding the contacting parts to form a block. Each of the sheets is continuously bent in a horizontal section, each bent surface is inclined to one side with respect to the vertical as a whole, and each inclined bent surface has an abbreviated shape in the vertical section. For anaerobic sewage treatment, the recesses for temporarily trapping sludge are formed at intervals in the inclination direction, and the bottom surface of the recesses is inclined in the width direction, and is further provided with protrusions for resisting sludge flow in the depth direction. It is a filter medium.
すなわち、この発明は、各シートを特定のftj斜屈曲
屈曲面続して有し、且つ交互に反転して小ね合せられて
いるので、上方から傾斜して降下する汚水を交差するよ
うに混合できると共に、その交差によって全体として旋
回流を生じさせ、更にその混合旋回流が隣接するシート
の接触部にて逆に分割を繰り返し受けることになる。That is, in this invention, each sheet has a specific ftj oblique bending surface connected to each other, and is alternately inverted and plied together, so that the sewage that descends from above at an angle is mixed in a crosswise manner. At the same time, the intersection causes a swirling flow as a whole, and furthermore, the mixed swirling flow is repeatedly divided at the contact portions of adjacent sheets.
またこの発明は、特定の汚泥一時捕捉用凹部を有し、且
つその凹部に汚泥流下抵抗用凸条を形成しているので、
汚泥(嫌気性微生物を含む)の一方向な降下を阻止して
廃水と嫌気性微生物との接触時間を確保できるようにし
ている。In addition, this invention has a specific recess for temporarily trapping sludge, and a protrusion for resisting sludge flow is formed in the recess.
This prevents the sludge (including anaerobic microorganisms) from falling in one direction, ensuring enough contact time between wastewater and anaerobic microorganisms.
この発明において使用できる各シートとしては、プラス
チック、例えば塩化ビニル樹脂の押出成形シートを真空
成形にて賦形したもの、又は塩化ごニル樹脂の射出成型
したもの、その他金属板に凹凸成形したものが使用でき
る。待に押出成形シー1−を真空成形したものは、汚泥
一時捕捉用凹部の成形において、その凹部の肉厚を小さ
くすることになるので、一般の構造材、発生するメタン
、炭酸ガスによって生じる浮力に耐える構造材等として
、汚泥流下抵抗用凸条の形成が強度アップになり好適で
ある。Examples of the sheets that can be used in this invention include plastics, such as extrusion-molded sheets of vinyl chloride resin that are formed by vacuum forming, injection-molded sheets of vinyl chloride resin, and other metal plates that are formed into irregularities. Can be used. First, when extrusion-molded seams 1- are vacuum formed, the wall thickness of the recesses for temporarily trapping sludge is reduced, so the buoyancy caused by general structural materials, methane, and carbon dioxide gas is reduced. Formation of protrusions for resistance to sludge flow is suitable for use as a structural material that can withstand high temperatures, as it increases strength.
このd明のシー]へに形成される屈曲面の傾斜は、汚泥
の捕捉と脱落を適度にするため水平に対し50〜70°
が々Yましく、約60°がより々Iましい。The slope of the curved surface formed on this d-light sea is 50 to 70 degrees to the horizontal in order to moderate the capture and shedding of sludge.
About 60 degrees is even more desirable.
(ニ)実施例
以下図に示す実施例に基づきこの発明を詳述する。なお
、これによってはこの発明が限定されるものではない。(d) Examples This invention will be described in detail below based on examples shown in the figures. Note that this invention is not limited to this.
まず、第3図にJ′3いて、嫌気性汚水処理用濾材(1
)は、廃水処理装置(H)の前処理槽である嫌気性濾床
(2)内に浸漬使用され、(3)は廃水流入路、(4)
はガス抜き管、(5)は汚泥排出路である。First, in Figure 3, J'3 is a filter medium for anaerobic wastewater treatment (1
) is used immersed in the anaerobic filter bed (2) which is the pre-treatment tank of the wastewater treatment device (H), (3) is the wastewater inflow channel, and (4)
(5) is a gas vent pipe, and (5) is a sludge discharge path.
なお、(6)は接触曝気槽で、(刀はこの槽と嫌気性濾
床(2)との接触槽、(8)はその好気性接触材、(9
)は散気管である。00)は最終処理用付属槽で、[1
1)はその余剰汚泥排出路、(’+21は処理水取出路
である。In addition, (6) is the contact aeration tank, (the sword is the contact tank between this tank and the anaerobic filter bed (2), (8) is its aerobic contact material, (9)
) is a diffuser pipe. 00) is the attached tank for final treatment, [1
1) is the excess sludge discharge path, and ('+21) is the treated water extraction path.
而して、嫌気性汚水処理用濾材(1)は、特に第1〜2
図において、同一形状で垂直の多数のシートO5) 0
6) a7)・・・・・・を平面上で交互に半回転(1
80°)させて重ね合せ、接触部分を接着しブロック状
に構成してなる。Therefore, the filter medium for anaerobic wastewater treatment (1) is particularly suitable for the first to second
In the figure, a number of identically shaped and vertical sheets O5) 0
6) Alternately rotate a7)....... on a plane by half a turn (1
80°), and the contact portions are glued to form a block shape.
シート(151は、押出成形により得られた塩化ビニル
樹脂板を真空成形したもので、水平断面では連続して屈
曲し、その各屈曲面(181(191・・・・・・が全
体的に垂直に対し一方に傾斜している
またそれらの各屈曲面(2)e・・・・・・には、垂直
断面略し字状の汚泥一時捕捉用凹部■(21)・・・・
・・を傾斜方向に間隔を有して形成し、且つその凹部の
底面部のを幅方向に傾斜させ(例えば水平に対し約30
゛)、更にその奥行方向、つまり傾斜方向く下向き)に
対して略直角に、垂直面部内に延びる汚泥流下抵抗用凸
条94)(ハ)を形成している。なお、シート■昭はシ
ー1− (151と全く同一の形状であるので説明を省
略する。The sheet (151 is a vacuum-formed vinyl chloride resin plate obtained by extrusion molding, and is continuously bent in the horizontal section, and each bent surface (181 (191...) is vertical as a whole. In addition, each of those curved surfaces (2)e, which are inclined to one side with respect to
... are formed at intervals in the inclination direction, and the bottom of the recess is inclined in the width direction (for example, about 30
Furthermore, a protruding strip 94) (c) for resisting sludge flow is formed that extends within the vertical surface portion approximately at right angles to the depth direction (that is, the downward inclination direction). Note that the sheet 1-(151) has exactly the same shape as the sheet 1-(151), so a description thereof will be omitted.
ところでこれらのシート(151■肋・・・・・・は、
重ね合せる際に、隣接するシートの接触部に適宜接着剤
(例えば、70容間%のテトラハイドロフランと30容
最%のメチルエチルケトン(MEK)とからなる溶剤に
シート材料を溶かしたもの)を用いて強固に接着されて
いる。By the way, these sheets (151 ■ ribs...) are
When overlapping, use an appropriate adhesive (for example, sheet material dissolved in a solvent consisting of 70% by volume of tetrahydrofuran and 30% by volume of methyl ethyl ketone (MEK)) on the contact areas of adjacent sheets. It is firmly attached.
かくして、嫌気性濾床(2)内に流入する廃水(例えば
産業排水又は下水道)は、相隣接するシート(15)
[31の屈曲面部)じ・・・・・・幻弼・・・・・・に
より、交差混合し、且つ接88れる部分により分流して
これらを繰り返し降下する。また相隣接するシート(1
5) 06)の各屈曲面(I8)[F]・・・・・・(
至)弼・・・・・・は対向しているので、廃水は旋回流
となって降下する。Thus, wastewater (e.g. industrial wastewater or sewerage) flowing into the anaerobic filter bed (2) flows through the adjacent sheets (15).
[Bending surface portion of 31] Due to the illusion..., the water is cross-mixed, and the water is divided by the contacting portion 88 and repeatedly descends. Also, adjacent sheets (1
5) Each curved surface (I8) [F] of 06) (
Since the two sides are facing each other, the wastewater becomes a swirling flow and descends.
このような旋回流と交差a合分流とにより、嫌気性微生
物と廃水との接触が十分行なわれると共にシートへの汚
泥の必要以上の付着が防止でき、且つメタン、炭酸ガス
等のガスの滞留が防止できる。なお、ガスのill留は
ブロック状の嫌気性汚水処理用濾材(1)全体に大きな
浮力を与えるので、危険である。Such swirling flow and cross-merging/diverging flow allow sufficient contact between anaerobic microorganisms and wastewater, prevent excessive adhesion of sludge to the sheet, and prevent retention of gases such as methane and carbon dioxide. It can be prevented. Incidentally, the ill distillation of gas is dangerous because it imparts a large buoyancy to the entire block-shaped filter medium for anaerobic wastewater treatment (1).
更にこのように嫌気性汚水処理用濾材(1)内を降下す
る廃水は、嫌気性微生物との接触により、汚泥(嫌気性
微生物を含む)を形成し、その汚泥が徐々に降下して余
剰汚泥排出路(5)から適宜排出される。しかし通常嫌
気性微生物及びそれを含む汚泥はその性質上好気性微生
物に比しシート表面への付着性がきわめて悪く、しかも
処理時間が長い。Furthermore, the wastewater falling through the filter medium (1) for anaerobic sewage treatment forms sludge (including anaerobic microorganisms) due to contact with anaerobic microorganisms, and the sludge gradually descends to form excess sludge. It is appropriately discharged from the discharge path (5). However, due to their nature, anaerobic microorganisms and sludge containing them generally have extremely poor adhesion to the sheet surface compared to aerobic microorganisms, and furthermore, the treatment time is long.
従って、上述のような大きな流動性を付与された廃水は
、その汚泥を短時間に降下し、嫌気性微生物による処理
が不十分になるおそれがあった。Therefore, the wastewater imparted with the above-mentioned high fluidity descends into sludge in a short period of time, and there is a risk that the treatment by anaerobic microorganisms will be insufficient.
しかるに嫌気性汚水処理用濾材(1)は、汚泥一時捕捉
用凹部■21)・・・・・・を有し、且つその内面部に
汚泥流下抵抗用凸条の)(ハ)を形成しているので、そ
の凹部の底面部いと凸条(241により廃水中の汚泥降
下が適宜制限され、汚泥中の嫌気性微生物と廃水の接触
時間を十分確保でき、廃水の前処理効率の向−1二がは
かれる。要するに、嫌気性汚水処理用濾材(1)は、嫌
気性微生物を付着しやすく、しかも増殖した余剰汚泥が
容易に脱落して新しい嫌気性微生物が付着するという適
度の捕捉と脱落を交互に繰り返す口とによって新鮮な汚
泥が再生し、処理降下があがるわけである。However, the filter medium (1) for anaerobic sewage treatment has a concave part (21) for temporarily trapping sludge, and also has convex stripes () (c) for resisting sludge flow formed on its inner surface. Therefore, the bottom of the recess and the convex strip (241) appropriately limit the fall of sludge in the wastewater, ensuring sufficient contact time between the anaerobic microorganisms in the sludge and the wastewater, and improving the efficiency of wastewater pretreatment. In short, the filter medium for anaerobic sewage treatment (1) easily attracts anaerobic microorganisms, and it alternately captures and sheds moderate amounts of excess sludge that has grown and easily falls off, allowing new anaerobic microorganisms to adhere. Fresh sludge is regenerated by repeating the process, and the treatment rate increases.
またシート間の空間が区切られることなく連通している
ので(シート間の空間が屈曲峯で区切られることがなり
〉、濾床中に発生するメタンガス、炭酸ガスなどが抜け
やすく、特に上述のごとく嫌気性汚水処理用濾材に加わ
る浮力を小さくできる。In addition, since the spaces between the sheets are connected without being separated (the spaces between the sheets are separated by curved ridges), it is easy for methane gas, carbon dioxide gas, etc. generated in the filter bed to escape, especially as mentioned above. The buoyancy force applied to the filter medium for anaerobic wastewater treatment can be reduced.
以上の実施例とは異なり、嫌気性汚水処理用濾材を構成
づる各シートに多数の小孔(例えば10〜50mmφの
通孔)を分散配設し、廃水の流用分布をより均一にする
こともできる。更に各シートを重ね合せて接着する際の
接着面積を十分確保するために、各屈曲面の屈曲峯の対
応接触個所に例えば平坦な接着用円形部を形成してもよ
い(例えば各シートに円形平坦ボスとそのボスを受ける
円形平坦受けを形成する)。Unlike the above embodiments, a large number of small holes (for example, holes of 10 to 50 mmφ) may be distributed in each sheet constituting the filter medium for anaerobic wastewater treatment to make the distribution of wastewater more uniform. can. Furthermore, in order to secure a sufficient bonding area when stacking and bonding each sheet, for example, a flat circular part for bonding may be formed at the corresponding contact point of the curved ridge of each curved surface (for example, a flat circular part for bonding may be formed on each sheet). form a flat boss and a circular flat receiver that receives the boss).
ここで参考までに嫌気性汚水処理用濾材を構成するシー
トに形成される汚泥一時捕捉用凹部及びその凹部内の汚
泥流下抵抗用凸条の一般的寸法仕様例及び実験例を挙げ
る。Here, for reference, examples of general dimensional specifications and experimental examples of recesses for temporarily trapping sludge formed in a sheet constituting a filter medium for anaerobic sewage treatment and protrusions for resisting sludge flow within the recesses will be given.
(A)汚泥一時捕捉用凹部
底面部 奥行: 5〜15mm、幅: 40〜b垂
直面部 高さ:15〜45mm、幅:40〜120 m
m(B)汚泥流下抵抗用凸条
高さ: 1〜3mm
幅:1〜3mm
条数: 2〜5条
〔実験例〕
(△)嫌気性汚水処理用濾材
く本発明品〉
縦・横・高さ: 500x 500x 500 (m
m )構成シート:塩化ビニル樹脂押出成形板(板厚さ
約0.5mm)を真空成形したもの、屈曲ビッヂ:
200mm
構成シート間のピッチ(波の1サイクル):0mm
屈曲高さく波の全高さ):80mm
汚泥一時捕捉用凹部
底面部 奥行:10mm、幅80mm垂直面部 高さ
:30mm、幅80 mm汚泥流下抵抗用凸条
高さ: 2胴
幅 : 2mm
条数= 2条
〈比較対照量〉
大日本プラスチック■製市販品:
タレオパッキン(登録商標)PW80
縦・横・高さ+ 500X 500x 480 (m
m )構成シート二本発明と同じ
構成シート間のピンチ:80mm
屈曲とッチ(波のサイクル) : 125mm屈曲高
さく波の全高さ):50mm
シート間のピッチを確保すると共に両シートを接着する
ための平面ボスとそのボスを受ける平面受けとを形成し
ている。(A) Bottom part of concave part for temporary sludge capture Depth: 5 to 15 mm, Width: 40 to b Vertical part Height: 15 to 45 mm, Width: 40 to 120 m
m (B) Convex strips for resisting sludge flow Height: 1 to 3 mm Width: 1 to 3 mm Number of strips: 2 to 5 [Experimental example] (△) Filter material for anaerobic sewage treatment - product of the present invention> Vertical, horizontal, Height: 500x 500x 500 (m
m) Constituent sheet: Vacuum-formed vinyl chloride resin extrusion molded plate (plate thickness approximately 0.5 mm), bent bidge:
200mm Pitch between constituent sheets (1 cycle of waves): 0mm Bending height, total height of waves): 80mm Bottom of recess for temporary sludge capture Depth: 10mm, width 80mm Vertical surface Height: 30mm, width 80mm Resistance to sludge flow Convex strip height: 2 Body width: 2 mm Number of strips = 2 (comparison quantity) Commercial product manufactured by Dainippon Plastic ■: Taleo Packing (registered trademark) PW80 Length, width, height + 500 x 500 x 480 (m
m) Pinch between two constituent sheets same as the present invention: 80mm Bending and touching (wave cycle): 125mm bending height, total height of waves): 50mm Ensure pitch between sheets and bond both sheets together It forms a flat boss and a flat receiver for receiving the boss.
(B)嫌気性菌
下水より入手したMLssm度約20,000−の嫌気
性菌(水温24℃)
(C)実験装置
水槽 縦・横・高さ 1x IX 2(m )高さ約5
00 mmの架台上に嫌気性汚水処理用濾材を載置
水位 1.3m
(D)実験方法
バキュームカーにより徐々に嫌気性菌を水槽中に入れた
く約1.3m’)。この模48時間放置し、次いで水槽
内の嫌気性菌を抜き取り1週間放置後辺材に付着した菌
体の重めをはかりm3当りの濾材の菌体保持保持mを換
りした。(B) Anaerobic bacteria Anaerobic bacteria with MLssm degree of approximately 20,000 - obtained from sewage (water temperature 24°C) (C) Experimental equipment water tank Length/width/height 1 x IX 2 (m) Height approx. 5
A filter medium for anaerobic sewage treatment was placed on a 00 mm stand with a water level of 1.3 m (D) Experimental method Anaerobic bacteria were gradually introduced into the water tank using a vacuum car (approx. 1.3 m'). This sample was left to stand for 48 hours, and then the anaerobic bacteria in the aquarium were extracted, and after being left for one week, the weight of the bacteria adhering to the sapwood was measured, and the amount of bacteria held on the filter medium per m3 was changed.
(E)試験結果
メタン発酵法に代表される嬉気性処理は嫌気性微生物の
増殖および代謝活性を利用した処理法であるが、処理効
果は菌体保持量の多い方がそれに対応して大きい。本結
果では発明品の濾材は比較対照品の約10倍の菌体保持
量が得られた。(E) Test results Aerobic treatment, typified by methane fermentation, is a treatment method that utilizes the growth and metabolic activity of anaerobic microorganisms, and the treatment effect is correspondingly greater as the amount of bacterial cells retained is greater. The results show that the filter medium of the invention had about 10 times the amount of bacterial cells retained as compared to the comparative product.
(ホ)発明の効果
この発明によれば、廃水と嫌気性微生物との接触を適度
に確保でき、高い処理効率が得られ、更に構造材として
の十分な強度が得られる。(E) Effects of the Invention According to the present invention, it is possible to ensure appropriate contact between wastewater and anaerobic microorganisms, to obtain high treatment efficiency, and to obtain sufficient strength as a structural material.
第1図はこの発明の一実施例を示す部分説明斜視図、第
2図はその汚泥一時捕捉用凹部の縦断面図、第3図はそ
れを絹み込んだ廃水処理装置の一例を示す構成説明図で
ある。
(1)・・・・・・嫌気性汚水処理用線材、fly)
06) (171・・・・・・シート、(1810’3
・・・・・・屈曲面、N (2++・・・・・・汚泥一
時捕捉用凹部、241 固・・・・・・汚泥流下抵抗用
凸条。Fig. 1 is a partial explanatory perspective view showing one embodiment of the present invention, Fig. 2 is a vertical cross-sectional view of the recess for temporarily trapping sludge, and Fig. 3 is a configuration showing an example of a wastewater treatment device incorporating the same. It is an explanatory diagram. (1)・・・Wire rod for anaerobic sewage treatment, fly)
06) (171... Sheet, (1810'3
...Bending surface, N (2++...Concavity for temporary sludge trapping, 241 Solid...Convex strip for resisting sludge flow.
Claims (1)
に半回転させて重ね合せ、接触部分を接着してブロック
状に構成してなり、 その各シートは、水平断面では連続して屈曲し、その各
屈曲面が全体的に垂直に対し一方に傾斜して、それらの
傾斜する各屈曲面に垂直断面略L字状の汚泥一時捕捉用
凹部を傾斜方向に間隔を有して形成し、 且つその凹部の底面部が、幅方向に傾斜し、更に奥行方
向に汚泥流下抵抗用凸条を備えてなる嫌気性汚水処理用
濾材。[Scope of Claims] 1. A large number of substantially vertical sheets of the same shape are stacked on top of each other by alternately turning half a turn on a plane, and the contact portions are adhered to form a block shape, and each sheet has the following features: The horizontal cross section is continuously bent, and each of the curved surfaces is inclined to one side with respect to the vertical direction, and a recess for temporarily trapping sludge having an approximately L-shaped vertical section is formed in each of the inclined curved surfaces in the inclined direction. A filter medium for anaerobic sewage treatment, which is formed with intervals, the bottom surface of the recessed portion is inclined in the width direction, and further provided with protrusions for resisting sludge flow in the depth direction.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP60246669A JPS62106894A (en) | 1985-11-01 | 1985-11-01 | Filter material for anaerobic treatment of sanitary sewage |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP60246669A JPS62106894A (en) | 1985-11-01 | 1985-11-01 | Filter material for anaerobic treatment of sanitary sewage |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS62106894A true JPS62106894A (en) | 1987-05-18 |
JPH026592B2 JPH026592B2 (en) | 1990-02-09 |
Family
ID=17151850
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP60246669A Granted JPS62106894A (en) | 1985-11-01 | 1985-11-01 | Filter material for anaerobic treatment of sanitary sewage |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS62106894A (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH01139897U (en) * | 1988-03-18 | 1989-09-25 | ||
US7232196B2 (en) | 2003-10-04 | 2007-06-19 | Lg Electronics, Inc. | Refrigerator |
CN108483630A (en) * | 2018-03-12 | 2018-09-04 | 江西盖亚环保科技有限公司 | The processing method and processing unit of organic wastewater based on GY-1 type water treatment fillers |
-
1985
- 1985-11-01 JP JP60246669A patent/JPS62106894A/en active Granted
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH01139897U (en) * | 1988-03-18 | 1989-09-25 | ||
US7232196B2 (en) | 2003-10-04 | 2007-06-19 | Lg Electronics, Inc. | Refrigerator |
CN108483630A (en) * | 2018-03-12 | 2018-09-04 | 江西盖亚环保科技有限公司 | The processing method and processing unit of organic wastewater based on GY-1 type water treatment fillers |
Also Published As
Publication number | Publication date |
---|---|
JPH026592B2 (en) | 1990-02-09 |
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