JPH0123595Y2 - - Google Patents
Info
- Publication number
- JPH0123595Y2 JPH0123595Y2 JP1984199821U JP19982184U JPH0123595Y2 JP H0123595 Y2 JPH0123595 Y2 JP H0123595Y2 JP 1984199821 U JP1984199821 U JP 1984199821U JP 19982184 U JP19982184 U JP 19982184U JP H0123595 Y2 JPH0123595 Y2 JP H0123595Y2
- Authority
- JP
- Japan
- Prior art keywords
- ring
- anaerobic
- filter medium
- shaped plate
- filter
- 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
Links
- 238000004065 wastewater treatment Methods 0.000 claims description 9
- 229920003002 synthetic resin Polymers 0.000 claims description 5
- 239000000057 synthetic resin Substances 0.000 claims description 5
- 239000010802 sludge Substances 0.000 description 8
- 230000005484 gravity Effects 0.000 description 6
- 238000000034 method Methods 0.000 description 4
- 244000005700 microbiome Species 0.000 description 4
- 239000002351 wastewater Substances 0.000 description 4
- 230000003014 reinforcing effect Effects 0.000 description 3
- 239000010865 sewage Substances 0.000 description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 3
- 238000011001 backwashing Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000005260 corrosion Methods 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 238000001746 injection moulding Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 230000000813 microbial effect Effects 0.000 description 1
- 238000012856 packing Methods 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W10/00—Technologies for wastewater treatment
- Y02W10/10—Biological treatment of water, waste water, or sewage
Landscapes
- Biological Treatment Of Waste Water (AREA)
Description
【考案の詳細な説明】
(産業上の利用分野)
この考案は、微生物の働きによつて廃水を浄化
する廃水処理槽内に充填し、該微生物を着生繁殖
させる媒体となる廃水処理用濾材に関するもので
ある。[Detailed description of the invention] (Field of industrial application) This invention is a filter material for wastewater treatment that is filled into a wastewater treatment tank that purifies wastewater by the action of microorganisms, and serves as a medium for epiphytic propagation of the microorganisms. It is related to.
(従来の技術)
有機性汚水等の廃水を生物化学的に浄化させる
方法は大きく分けて、好気性微生物の働きを利用
する好気性処理方法と、嫌気性微生物の働きを利
用する嫌気性方法とがあり、従来から、これらに
使用する濾材が種々開発されている。例えば、実
公昭56−21520号公報には、半円形状の第1の羽
根板群と第2の羽根板群とを各羽根が図示のよう
に互に直交し、かつ球形の輪郭を有すようにした
濾材が示されている。(Prior art) Methods for biochemically purifying wastewater such as organic sewage can be broadly divided into aerobic treatment methods that utilize the action of aerobic microorganisms, and anaerobic treatment methods that utilize the action of anaerobic microorganisms. Various types of filter media have been developed for use in these applications. For example, Japanese Utility Model Publication No. 56-21520 discloses that a first group of semicircular blades and a second group of blades are arranged such that each blade is orthogonal to each other as shown in the figure and has a spherical outline. A filter medium constructed as shown in FIG.
(考案が解決しようとする問題点)
ところで、この種の濾材に要求される性能とし
ては、好気性処理用の場合、微生物汚泥の付着
量を多くするため比表面積が大きいこと、汚水
の循環効率を良くするため空隙率が大きいこと、
濾材の充填作業が簡単なこと、および安価で
あることなどが要求され、一方、嫌気性処理用の
場合、上記,,およびの要件に加えて、
汚泥による目詰り、偏流が生じない形状である
こと逆洗時の汚泥剥離が容易なことおよび比
重は1.0より大であるが、余り重すぎないことな
どが要求される。(Problem that the invention aims to solve) By the way, the performance required of this type of filter medium is that for aerobic treatment, it must have a large specific surface area to increase the amount of microbial sludge attached, and it must have a high sewage circulation efficiency. The porosity is large to improve the
In addition to the above requirements, in the case of anaerobic treatment, the filter media must be easy to fill and inexpensive.
It is required to have a shape that does not cause clogging or drift due to sludge, to be easy to remove sludge during backwashing, and to have a specific gravity of more than 1.0, but not too heavy.
しかしながら、従来の濾材は、いずれも好気性
処理用もしくは嫌気性処理用のいずれか一方にの
み適した性能を有し、両者に要求される性能を全
て備えたものはなく汎用性に乏しいと言う問題が
あつた。例えば実公昭56−21520号公報に開示さ
れる濾材は、前者としての性能は有するものの、
構造上流れの方向性が生じるために偏流を生じ、
後者としての性能は完全ではない。 However, all conventional filter media have performance that is suitable only for either aerobic treatment or anaerobic treatment, and none have all the performance required for both, making them lacking in versatility. There was a problem. For example, although the filter medium disclosed in Utility Model Publication No. 56-21520 has the performance of the former,
Due to the structure, the directionality of the flow causes drift,
The latter performance is not perfect.
(問題点を解決するための手段)
本考案の廃水処理用濾材は、合成樹脂製の板体
が複数個組合わされてなるものであつて、上記板
体の外縁がほぼ球形の輪郭を有するとともに、内
部にほぼ球形の空洞部が形成され、該空洞部は各
板体間の通路を介して外部に連通されている。(Means for Solving the Problems) The wastewater treatment filter medium of the present invention is formed by combining a plurality of synthetic resin plates, and the outer edges of the plates have a substantially spherical outline. A substantially spherical cavity is formed inside, and the cavity is communicated with the outside through passages between the plates.
(作用)
内部にほぼ球形の空洞部を有していて偏流を起
こさない等、前述した好気性処理用および嫌気性
処理用として要求される性能を全て備えており、
特に比重を1.0〜1.05としたものにおいては汚水
処理層中で沈下し、空気逆洗したときほぼ球形で
あることとあいまつて回転しながら浮上するため
汚泥の剥離が容易である。(Function) It has all the performances required for aerobic treatment and anaerobic treatment as described above, such as having an almost spherical cavity inside and not causing drifting.
In particular, when the specific gravity is 1.0 to 1.05, the sludge sinks in the sewage treatment layer, and when backwashed with air, it floats while rotating due to its almost spherical shape, making it easy to remove the sludge.
(実施例) 以下本考案の実施例を図面に基いて説明する。(Example) Embodiments of the present invention will be described below with reference to the drawings.
本考案に係る廃水処理用濾材を第1図ないし第
3図に示し、濾材1は全体が球形の輪郭を有する
合成樹脂製のものであつて、第1のリング状の板
体2…および第2のリング状の板体3が組合わさ
れてなり、第4図に示すように、廃水処理装置4
の各槽(嫌気濾床槽)5,6,7内に多数充填さ
れる。 A filter medium for wastewater treatment according to the present invention is shown in FIGS. 1 to 3, and the filter medium 1 is made of synthetic resin and has a spherical outline as a whole. Two ring-shaped plates 3 are combined to form a wastewater treatment device 4, as shown in FIG.
Each tank (anaerobic filter bed tank) 5, 6, 7 is filled with a large number of anaerobic filters.
第1の板体2は単一の軸線A上で複数個交差
し、かつ同一中心Bを有するようにされている。
これら第1のリング状の板体2…は、第3図に示
すように等角度θをもつて交差されており、図示
例の場合、3枚のリング状の板体2…が互いに60
度の角度をもつて交差されている。 A plurality of first plates 2 intersect on a single axis A and have the same center B.
These first ring-shaped plates 2... are crossed at equal angles θ as shown in FIG. 3, and in the illustrated example, the three ring-shaped plates 2...
intersect at an angle of degree.
第2のリング状の板体3は上記第1のリング状
の板体2と同形同大のものであつて、その中心が
上記中心Bに一致し、かつ第1のリング状の板体
2…のすべてに対して垂直状に交差するようにさ
れている。この第2のリング状の板体3と平行に
輪郭がほぼ球形となるような径小のリング状板体
が設けられていてもよい。 The second ring-shaped plate 3 is of the same shape and size as the first ring-shaped plate 2, and its center coincides with the center B, and the second ring-shaped plate 3 is similar to the first ring-shaped plate 2. 2. It is arranged to intersect perpendicularly to all of... A small-diameter ring-shaped plate whose outline is approximately spherical may be provided parallel to the second ring-shaped plate 3.
また、第1のリング状の板体2と第2のリング
状の板体3との交差部分には、台形状の補強板1
0がそれぞれ起立状に設けられ、この部位の強度
が補強されるとともに、比表面積の増大化が図ら
れている。 Further, a trapezoidal reinforcing plate 1 is provided at the intersection of the first ring-shaped plate 2 and the second ring-shaped plate 3.
0 is provided in an upright manner, thereby reinforcing the strength of this portion and increasing the specific surface area.
また、該補強板10…は第2のリング状の板体
3とともに、廃水処理装置4内に充填された各濾
材1…のくい込み合いを防止する作用をする。な
お、濾材1を構成する板体はリング状に限らず、
複数個のアーチ形の板体を組合わせて形成しても
よい。 Further, the reinforcing plates 10 work together with the second ring-shaped plate body 3 to prevent the filter media 1 filled in the wastewater treatment device 4 from jamming together. Note that the plate forming the filter medium 1 is not limited to a ring shape.
It may also be formed by combining a plurality of arch-shaped plates.
しかして、以上のように構成された濾材1にお
いては、第1のリング状の板体2…の外縁2a
…、および第2のリング状の板体3の外縁3a…
がほぼ球形の輪郭を有するとともに、内部には空
洞部11が第1のリング状の板体2…の内縁2
b、および第2のリング状の板体3の内縁3bに
より形成されている。該空洞部11は、第1のリ
ング状の板体2…の外縁2a…、および第2のリ
ング状の板体3の外縁3aがなす上記ほぼ球形と
同一中心Bを有するほぼ球形とされるとともに、
各第1のリング状の板体2…および第2のリング
状の板体3間の間隙により形成される通路20を
介して外部に連通され、該通路20が上記中心B
に対して放射状とされているのが好ましい。 Therefore, in the filter medium 1 configured as described above, the outer edge 2a of the first ring-shaped plate 2...
..., and the outer edge 3a of the second ring-shaped plate body 3...
has a substantially spherical outline, and a cavity 11 is formed inside the inner edge 2 of the first ring-shaped plate 2.
b, and the inner edge 3b of the second ring-shaped plate 3. The hollow portion 11 has a substantially spherical shape having the same center B as the substantially spherical shape formed by the outer edge 2a of the first ring-shaped plate 2 and the outer edge 3a of the second ring-shaped plate 3. With,
It is communicated with the outside through a passage 20 formed by a gap between each of the first ring-shaped plates 2 and the second ring-shaped plate 3, and the passage 20 is connected to the center B.
It is preferable that it be radial with respect to.
なお、第1のリング状の板体2…および第2の
リング状の板体3の枚数は各板体間の空隙率や比
表面積等を考慮して設定されるとともに、比重は
1.0〜1.05とされるのが好ましく、例えば嫌気性
処理用の場合は比重が1.03程度とされるのがよ
い。 The number of the first ring-shaped plates 2 and the second ring-shaped plates 3 is set in consideration of the porosity and specific surface area between each plate, and the specific gravity is
The specific gravity is preferably 1.0 to 1.05, and for example, for anaerobic treatment, the specific gravity is preferably about 1.03.
嫌気処理方式による廃水処理装置4は第4図に
示すように、第1嫌気濾床槽5、第2嫌気濾床槽
6および第3嫌気濾床槽7等の複数個の槽を備
え、これらの内部には網状の床12が設けられ、
この上に上記濾材1…が多数充填されて、充填層
が形成されている。この際、水を張つた後に濾材
1を充填すれば自動的に方向が揃つて、隙間がほ
ぼ均等になる。また、充填される濾材1…は第1
嫌気濾床槽5、第2嫌気濾床槽6、第3嫌気濾床
槽7と移るにつれて、その球径が小さく設定さ
れ、例えば、第1嫌気濾床槽5の場合は140mm、
第2嫌気濾床槽6の場合は100mmおよび第3嫌気
濾床槽7の場合は80mmとされている。なお、13
は汚泥の剥離のための空気逆洗装置、14は床1
2の下側に堆積した汚泥を排出する排出管、15
は排気管である。 As shown in FIG. 4, the wastewater treatment device 4 using the anaerobic treatment method includes a plurality of tanks such as a first anaerobic filter bed tank 5, a second anaerobic filter bed tank 6, and a third anaerobic filter bed tank 7. A net-like floor 12 is provided inside the
A large number of the filter media 1 are filled on top of this to form a packed layer. At this time, if the filter medium 1 is filled after filling with water, the directions will be automatically aligned and the gaps will be approximately equal. Moreover, the filter medium 1 to be filled is the first
As the anaerobic filter bed tank 5, the second anaerobic filter bed tank 6, and the third anaerobic filter bed tank 7 are moved, the spherical diameter is set smaller; for example, in the case of the first anaerobic filter bed tank 5, it is 140 mm;
In the case of the second anaerobic filter bed tank 6, the length is 100 mm, and in the case of the third anaerobic filter bed tank 7, it is 80 mm. In addition, 13
is an air backwashing device for sludge removal, 14 is floor 1
15 a discharge pipe for discharging sludge accumulated on the lower side of 2;
is the exhaust pipe.
しかして、第1嫌気濾床槽5内に上側から導入
される廃水は濾材1…の充填層を流下した後、順
次オバーフローして、第2嫌気濾床槽6さらには
第3嫌気濾床槽7へと導入され、第1嫌気濾床槽
5内と同様、濾材1…の充填層をそれぞれ流下し
て浄化される。この際、上記充填層を流下する処
理水は、各濾材1の各リング状の板体間を通つ
て、空洞部11内へ入り、さらに各リング状の板
体間を経て再び濾材1の外部へ流れるから、何ら
流れを妨げられず、したがつて各濾材間に偏流を
生じることなく、充填層全体に均等に行われる。
これにより、処理水の全体が各濾材1のリング状
の板体に効率良く接触することになる。 Therefore, the wastewater introduced from above into the first anaerobic filter bed tank 5 flows down the packed bed of filter media 1, and then sequentially overflows to the second anaerobic filter bed tank 6 and then to the third anaerobic filter bed tank. 7, and similarly to the inside of the first anaerobic filter bed tank 5, the filter media 1 are purified by flowing down the packed layers of the filter media 1. At this time, the treated water flowing down the packed bed passes between the ring-shaped plates of each filter medium 1, enters the cavity 11, and then passes between the ring-shaped plates and returns to the outside of the filter medium 1. Since the flow is not obstructed in any way, the flow is uniformly distributed throughout the packed bed without any uneven flow between the filter media.
Thereby, the entire treated water comes into contact with the ring-shaped plate of each filter medium 1 efficiently.
なお、上述の濾材1は合成樹脂を射出成形によ
り一体成形しても良く、また、構造も図示例に限
定されず、少なくとも内部に球形の空洞部を有す
る限り変更自由である。 The filter medium 1 described above may be integrally molded from synthetic resin by injection molding, and the structure is not limited to the illustrated example, but may be modified as long as it has at least a spherical cavity inside.
(考案の効果)
以上詳述したように、本考案によれば、以下に
述べるような種々の優れた効果が得られる。(Effects of the invention) As detailed above, according to the present invention, various excellent effects as described below can be obtained.
(1) 全体としてほぼ球形の輪郭を有するから最密
充填が可能であり、充填層における比表面積を
極めて大きくすることができる。(1) Since it has an almost spherical outline as a whole, close packing is possible, and the specific surface area of the packed layer can be made extremely large.
(2) リング状の板体が組み合わされて構成されて
いるから、空隙率が大きく、汚水の循環効率が
高いとともに、目詰りも生じにくい。(2) Since it is constructed by combining ring-shaped plates, it has a large porosity, high wastewater circulation efficiency, and is less likely to become clogged.
ほぼ球形であるから、無造作に充填しても均
等な密度に配列でき、充填作業が簡単である。 Since they are almost spherical, they can be arranged at even density even if they are filled casually, making the filling operation easy.
内部にほぼ球形の空洞部があるから、偏流が
生じない。 Since there is an almost spherical cavity inside, drifting does not occur.
比重を1.0〜1.05とすると沈下し、空気逆流
のときに容易に浮上し、汚泥の剥離が容易であ
る。 When the specific gravity is 1.0 to 1.05, it will sink and easily float up when air flows backward, making it easy to peel off the sludge.
合成樹脂製であるから安価であり、しかも、
耐食性に優れて、耐用年数も半永久的と永い。 Since it is made of synthetic resin, it is inexpensive, and
It has excellent corrosion resistance and has a semi-permanent service life.
すなわち、本考案の濾材は好気性処理用として
持つべき性能と、嫌気性処理用として持つべき性
能との両者を兼ねており、汎用性に富んでいる。 That is, the filter medium of the present invention has both the performance required for aerobic treatment and the performance required for anaerobic treatment, and is highly versatile.
図面は本考案の一実施例を示し、第1図は廃水
処理用濾材を示す斜視図、第2図は第1図におけ
る矢符方向から見た同正面図、第3図は同平面
図、第4図は同濾材を適用した浄化装置の一部を
示す構成図である。
2……第1のリング状の板体、3……第2のリ
ング状の板体、2a,3a……外縁、11……空
洞部。
The drawings show one embodiment of the present invention, in which Fig. 1 is a perspective view showing a filter medium for wastewater treatment, Fig. 2 is a front view of the same as seen from the direction of the arrow in Fig. 1, and Fig. 3 is a plan view of the same. FIG. 4 is a block diagram showing a part of a purification device to which the same filter medium is applied. 2... First ring-shaped plate, 3... Second ring-shaped plate, 2a, 3a... Outer edge, 11... Cavity.
Claims (1)
ものであつて、前記板体の外縁がほぼ球形の輪郭
を有するとともに、内部にほぼ球形の空洞部が形
成され、該空洞部は各板体間の通路を介して外部
に連通されていることを特徴とする廃水処理用濾
材。 It is made by combining a plurality of plates made of synthetic resin, and the outer edge of the plate has an approximately spherical outline, and an approximately spherical cavity is formed inside, and the cavity is formed between each plate. A filter medium for wastewater treatment, characterized in that the filter medium is communicated with the outside through a passageway between the two.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP1984199821U JPH0123595Y2 (en) | 1984-12-28 | 1984-12-28 |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP1984199821U JPH0123595Y2 (en) | 1984-12-28 | 1984-12-28 |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS61115200U JPS61115200U (en) | 1986-07-21 |
JPH0123595Y2 true JPH0123595Y2 (en) | 1989-07-19 |
Family
ID=30760101
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP1984199821U Expired JPH0123595Y2 (en) | 1984-12-28 | 1984-12-28 |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH0123595Y2 (en) |
-
1984
- 1984-12-28 JP JP1984199821U patent/JPH0123595Y2/ja not_active Expired
Also Published As
Publication number | Publication date |
---|---|
JPS61115200U (en) | 1986-07-21 |
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