JPS6133293A - Filter - Google Patents

Filter

Info

Publication number
JPS6133293A
JPS6133293A JP59152637A JP15263784A JPS6133293A JP S6133293 A JPS6133293 A JP S6133293A JP 59152637 A JP59152637 A JP 59152637A JP 15263784 A JP15263784 A JP 15263784A JP S6133293 A JPS6133293 A JP S6133293A
Authority
JP
Japan
Prior art keywords
water
filter
inflow
layer
perforated plate
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
JP59152637A
Other languages
Japanese (ja)
Inventor
Yukio Kato
幸男 加藤
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Individual
Original Assignee
Individual
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Individual filed Critical Individual
Priority to JP59152637A priority Critical patent/JPS6133293A/en
Publication of JPS6133293A publication Critical patent/JPS6133293A/en
Pending legal-status Critical Current

Links

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W10/00Technologies for wastewater treatment
    • Y02W10/10Biological treatment of water, waste water, or sewage

Landscapes

  • Biological Treatment Of Waste Water (AREA)

Abstract

PURPOSE:To prevent the deterioration in function of a filter by providing a discharge port to a bottom surface of the part close to the bottom surface and forming a filter medium of filter medium layer in the discharge side with ballast, broken stone or wood wool-like material. CONSTITUTION:One end of the inside of vessel of a main body 1 is partitioned at right angles for the flow direction by providing a perforated plate 4 perpendicularly to provide an inflow chamber A between the perforated plate 4 and the wall surface. The part between the plate 4 and the wall surface of the other end is partitioned to form a discharge chamber C by providing perpendicularly a perforated plate 5 parallel to the perforated plate 4 and a filter medium 6 is incorporated between the perforated plates 4, 5 to form a filter medium layer B and an inflow pipe 2 communicating to a circulation pump is perpendicularly provided in the inflow chamber A and an inflow port 8 is opened in the position immersed into water. When the circulation pump is actuated, water is flowed into a water storage chamber A from the inflow port 8 of the inflow pipe 2 and passed through the filter medium layer B in the lateral direction from the water flow holes 7 of the perforated plate 4 and returned through a discharge port 3 to be circulated.

Description

【発明の詳細な説明】 本発明は濾過装置の改良に関するもので、槽内を流れ方
向はぼ直角に空間層を介して濾過材層全立設して仕切り
、横方向に通水させ接触酸化を計るろ過装置の菌の繁殖
増加の形態は、通水空間の大きい濾過材では濾過材内部
に菌が繁殖蓄積をつづける形態をとり、通水空間の小さ
い濾過材或いは漉す作用のある濾過材では時間の経過と
共に菌の走化性により、濾過活流入面KF膜としての菌
の繁殖が優先し、その厚みを増して行く形態を取る。炉
腹は剥離してその部分の通水量が回復し、この繰返しK
よって浄化力を持続する。一方漉す作用のある濾過材は
流れと共に流入する固形物或いは遊離した菌体等流入面
にひっかかり菌体に変るなどその表面に通水抵抗が集中
して水面が上昇する為、オーバーフロー状に濾過材層上
部を流れやすく、その為水と菌との接触が不足し菌の枯
死など生じやすい。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to an improvement in a filtration device, in which the inside of a tank is partitioned by vertically arranging all the filtration media layers with a space layer at right angles to the flow direction, and water is passed laterally to perform catalytic oxidation. The growth of bacteria in filtration devices is such that bacteria continue to grow and accumulate inside the filter medium with a large water passage space, while bacteria continues to grow and accumulate inside the filter medium with a small water passage space or with a filtering function. As time passes, due to the chemotaxis of the bacteria, the proliferation of the bacteria as a filtration active inflow surface KF membrane takes priority, and the thickness increases. The furnace belly peels off, the water flow rate in that area is restored, and this process is repeated.
Therefore, it maintains its purifying power. On the other hand, with filter media that has a filtration effect, solid matter or free bacterial cells that flow in with the flow get caught on the inflow surface and turn into bacterial cells, and water flow resistance is concentrated on the surface and the water level rises. It flows easily at the top of the layer, and as a result, there is insufficient contact between water and bacteria, which tends to cause the bacteria to wither.

二?h−FI/四F−Q/7’l+hl八ケミテ:A+
+lr→−〒リテtr)#(4+勿(*、へニー+−a
く長期に通水による浄化は持続するが、通水抵抗が不足
する為、部分通水による菌の枯死を生じやすく菌の支持
面が小さい為、菌の遊離、剥離を生じ外部に大量に流出
し、直接の弊害と菌量回復の困難性等不都合を生ずる欠
点があり、何れの場合も菌の増加によって機能の低下、
消失をさけられない。
two? h-FI/four F-Q/7'l+hl eight chemistry: A+
+lr→-〒ritetr) #(4+Mu(*,heny+-a
Purification by water flow continues for a long time, but due to lack of water flow resistance, bacteria tend to die due to partial water flow, and the support surface for bacteria is small, causing bacteria to become loose and peel off, resulting in a large amount of bacteria leaking out to the outside. However, there are disadvantages such as direct adverse effects and difficulty in recovering the amount of bacteria, and in both cases, the increase in bacteria causes a decline in functionality,
I can't avoid disappearing.

この考案は上記に鑑み提案されたもので、濾過槽内部を
通水方向にほぼ直角に空間層を介して、多孔板或いは波
型の多孔板のあいだに濾過材を収納した濾過材層を立設
して仕切り、横力向く通水させ接触酸化を計る流過装置
に於いて、吐出口に接する濾過材層のろ過材を物理的に
漉す作用のある濾過材にし、濾過材層流出面と壁面とで
構成する空間層の底面或いは底面近くに吐出口を設け、
その水圧差を利用し、濾過材層の通水がオーバーフロー
状に流れやすい縦型濾過槽の構成上の欠点を除去し、そ
の機能を大巾に高めた濾過装置に関する。
This idea was proposed in view of the above, and a filtration material layer containing a filtration material is erected between perforated plates or corrugated perforated plates, with a space layer interposed almost perpendicularly to the direction of water flow inside the filtration tank. In a flow device that measures catalytic oxidation by passing water in the direction of lateral force, the filtration material in the filtration material layer that is in contact with the discharge port is made into a filtration material that has the effect of physically straining, and the outflow surface of the filtration material layer and A discharge port is provided at or near the bottom of the space layer formed by the wall surface,
The present invention relates to a filtration device that utilizes the water pressure difference to eliminate the structural drawbacks of a vertical filtration tank in which water tends to overflow through the filtration material layer, and greatly enhances its functionality.

以下、実施例に沿って説明する。第1図は混用濾過装置
であり、本体1の槽内の一端を多孔板4を立設し、流れ
方向直角に仕切り、壁面との間に流入室Aを設け、多孔
板4に平行して他端壁面との間を多孔板5を立設して仕
切り吐出室Cを形成し、多孔板4と5の間に濾過材6を
収納して濾過材層Bを形成し流入室Aに循環用ポンプと
連通ずる流入パイプ2を垂設し水没する位置に流入口8
を開口する。吐出室Cには底面或いは底面近くに吐出パ
イプ3を設ける。尚、ア過材層B内に槽内の緩衝作用が
確実に得られ、菌の繁殖の形態が涙膜状になる目のこ1
かい漉す作用のある、天然又は人工の繊維質を不規則に
絡1せた木毛状物、商品名ビニロック或いは通水空間の
小さい砂利又はいて、通水を制限し、通水抵抗により空
間層Aでの上下緩衝流を生ぜしめ、通水を平均化するよ
うにしている。このろ過装置を地上に設置し、循環ポン
プを作動すると池の水は流入パイプ2の流入口8よシ貯
水室Aにたえず流入し多孔板4の通水孔7よl”過材層
Bを横方向に通水し吐出口3より池に戻され循環する。
Hereinafter, it will be explained along with examples. FIG. 1 shows a mixed filtration device, in which a perforated plate 4 is installed upright at one end of the tank of the main body 1 to partition it at right angles to the flow direction, and an inflow chamber A is provided between the tank and the wall surface, and a perforated plate 4 is installed parallel to the perforated plate 4 to partition the tank at right angles to the flow direction. A perforated plate 5 is erected between the other end wall surface to form a partition discharge chamber C, and a filter medium 6 is stored between the perforated plates 4 and 5 to form a filter medium layer B, which is circulated to the inflow chamber A. An inlet pipe 2 that communicates with the water pump is installed vertically, and an inlet 8 is installed at a position where it will be submerged in water.
Open. A discharge pipe 3 is provided at or near the bottom of the discharge chamber C. In addition, the buffering effect in the tank can be reliably obtained in the filtration material layer B, and the form of bacterial growth is tear film-like.
A wooden wool-like substance with natural or artificial fibers randomly intertwined, which has a filtering effect, product name: Vinyrock, or gravel with small water-permeable spaces, restricts water flow and creates a spatial layer due to water-flow resistance. A vertical buffer flow is created at A to equalize the water flow. When this filtration device is installed on the ground and the circulation pump is operated, water in the pond constantly flows into the water storage chamber A through the inlet 8 of the inflow pipe 2, and through the water passage hole 7 of the perforated plate 4 through the overfill layer B. Water passes in the horizontal direction and is returned to the pond through the discharge port 3 for circulation.

作用効果については、流入パイプ2の流入口βは流入室
AK水没して設けられ、流入時に空気の混入等の変化を
さけ池水と同一じ環境条件にして急激な水温などの変化
を防止する様にしている、従って主たる変化は流入時の
流れになる。
Regarding the function and effect, the inlet port β of the inflow pipe 2 is submerged in the inflow chamber AK, so that changes such as air mixing during inflow are prevented, and the environmental conditions are the same as that of the pond water, thereby preventing sudden changes in water temperature, etc. Therefore, the main change is the flow at the time of inflow.

流入室Aの流入水は濾過材層Bの通水抵抗を受け、そこ
で攪拌状態になり、水面が上昇し流れは上下に緩衝する
。濾過材層Bは通水によって濾過材6に濾過菌(菌)が
繁殖増加し通過する水は浄化される。その間の経過九つ
いては漉す作用によって流入面に菌や目詰り物質がひっ
かかシ表面の通水抵抗が増加し、せき止められる状態で
流入側水面が上昇し、空間層Aで緩衝作用その他の詩作
用が支障なく得られる。循環水は上記濾過材の表面を通
水して濾過材層Bに流入する事になるが、濾過材6内部
は通水空間が大きい為、横方向に通水しないで、流入し
た水はfJi、維質をつたわって流表面の通水と落差に
よる内部の流れで第1図に示すように三角形になる。砂
利等通水空間の小さい濾過材では菌の増加によって短日
時で水圧差による横方向の通水が主体になり、水圧の上
昇によって長期に持続する。
The inflowing water in the inflow chamber A is subjected to the water flow resistance of the filter material layer B, and becomes agitated there, the water level rises, and the flow is buffered vertically. As water passes through the filter material layer B, filter bacteria (bacteria) increase in the filter material 6 and the water passing therethrough is purified. During this period, bacteria and clogging substances are caught on the inflow surface due to the straining action, and the water flow resistance on the surface increases, the water level on the inflow side rises in a dammed state, and the spatial layer A has a buffering effect and other poetic effects. You can get it without any trouble. The circulating water passes through the surface of the filtering material and flows into the filtering material layer B, but since the water passage space inside the filtering material 6 is large, the water does not pass in the lateral direction, and the inflowing water flows into the filtering material layer B. , the internal flow due to water flow on the flow surface through the fibers and the head difference creates a triangular shape as shown in Figure 1. In filter media with small water-flowing spaces, such as gravel, the increase in bacteria causes water to flow mainly in the lateral direction due to water pressure differences over short periods of time, which persists over a long period of time due to the increase in water pressure.

一方菌の繁殖は走化性によバ濾過材流人面で戸膜として
の繁殖増加が優先し、菌は上に上にとその厚みを増し続
け、循環水はp膜との接触によシ浄化される。F膜はそ
の厚みに二つて剥離し、通水は表面の通水抵抗が小さく
なるので再び前にもどる。通水は濾過材流人面で酸素と
栄養源が次々と消費さ几るので菌の繁殖蓄積は濾過材流
入面に集中し、流出面に近ずく程少なくなる。
On the other hand, the proliferation of bacteria is prioritized by chemotaxis, and the proliferation of bacteria on the surface of the filter material as a membrane takes priority, and the bacteria continue to increase in thickness, and the circulating water is absorbed by contact with the P membrane. It is purified. The F membrane peels off in two parts depending on its thickness, and the water flow returns to the previous state again because the water flow resistance on the surface becomes smaller. As water flows through the filter medium, oxygen and nutrient sources are consumed one after another on the flow surface of the filter medium, so the breeding and accumulation of bacteria concentrates on the inflow surface of the filter medium, and decreases as it gets closer to the flow surface of the filter medium.

従って濾過材層Bの流出面5が空気中に露出していても
F床としての機能に支障を生じない。
Therefore, even if the outflow surface 5 of the filter layer B is exposed to the air, the function as an F bed will not be affected.

以上のように本発明によれば、吐出口を底面近くにする
事で水圧によシ漉す作用のある濾過材層の通水を強化し
、その効果が底面根強く働くのでオーバーフローをしや
すい構成上の欠点を除去すで上述の通水による浄化機能
を極めて長期に持続させる事ができる。特にビニロック
の場合は濾過材内部の流れは、水圧による横方向の流れ
と落差による流れで水と菌との接触が行われ、更に裏面
及び通水の達しない部分は空気中に露出する事になるの
で好気状態を失う事がない上、濾過材内部は大量の菌体
を蓄積出来る等の好都合が得られる。
As described above, according to the present invention, by placing the discharge port near the bottom surface, the water flow through the filtering material layer, which has a filtering effect using water pressure, is strengthened, and this effect is deeply rooted at the bottom surface, making it easy to overflow. By eliminating these drawbacks, the above-mentioned water purification function can be maintained for an extremely long period of time. In particular, in the case of Vinylock, the flow inside the filter medium is a lateral flow due to water pressure and a flow due to the head, which causes contact between water and bacteria, and furthermore, the back side and the areas where water does not reach are exposed to the air. Therefore, there is no loss of aerobic conditions, and the inside of the filter material can accumulate a large amount of bacterial cells, which is advantageous.

第2図は借内金流れ方向に複数のろ過材層を立設し、空
間層A、A’i7おいて仕切り、多孔板或は波型多孔板
4と5の間に濾過材として通水空間の大きい人工、又は
天然の繊維質を不規則に絡1せた木毛状物(商品名へチ
マロン)を収納し最終の′F−過材層には商品名ビニロ
ックを収納し、一層目のろ過材層、流入面に沿って多孔
板4を立設して流入家人を区分し空間層Aを設けた実施
例であり、第3図は多孔板4を設けないで上記のろ過材
を3分の2の厚みにした利用方法を示し、循環水を流入
口8よシ空間層Aに注入すると吐出口3の高さでで水面
が上昇し、多孔板4の通水孔7よυ濾過材層B、B内を
流nヘチマロン6及びビニロック几、濾過材6及び6流
入面9,9と多孔板−六軛間が形成される。この空間層
り及びDは初め17c濾過材をセットする時に支持凸起
或いは支持枠網体を利用して造っておいてもよい。
Figure 2 shows a plurality of filter media layers erected in the direction of debt flow, and water is passed between partitions, perforated plates, or corrugated perforated plates 4 and 5 at space layers A and A'i7 as filter media. A wooden wool-like material (trade name: Hechimaron) made of artificial or natural fibers intertwined irregularly is stored in a large space, and the final 'F-layer material is stored with the trade name of Vinylock. This is an embodiment in which a perforated plate 4 is erected along the inflow surface to separate the inflowing people and a spatial layer A is provided. In this example, when circulating water is injected into the space layer A through the inlet 8, the water level rises at the level of the outlet 3, and the water level rises to the level of the water passage hole 7 of the perforated plate 4. In the filter material layers B and B, the hechimaron 6 and the vinyl lock box, the filter media 6 and 6 inflow surfaces 9, 9, and the porous plate-six yoke are formed. This space layer and D may be created by using a support ridge or a support frame net when initially setting the filter medium 17c.

作用効果については、菌は濾過材層B及びBの通水によ
って濾過材6,6内に繁殖増加するのであるが、最終P
:ii4材層Bの漉す作用にょp1槽内の水面が上昇し
、空間層A、Aの緩衝作用その他の詩作用が支障なく作
動し、多孔板4及びを間層わる事によって、流膜形成上
不適切とさ几ている、通水空間の大きい濾過材であるヘ
チマロン6に流nと共に流入する汚物など濾過材内部に
深く流入しないで、その流入面9にひつか\り、そこで
菌体にかわるなど長期には繁殖の型態は菌の走化性によ
シ炉腹或いは濾過材流入面側に最も多く濾過材6内部に
繁殖増加する、従って第2図空間層A及び第3図り、D
では日時がたつと剥離する沖膜など濾過材6及び6をは
なれた菌体が流入面に沿って形成している該空間層に蓄
積して行く事になる。通水は空間層の緩衝作用及び流入
方向可変作用で絶えず通水の平均化が得らnるので蓄積
する菌体を平均して横方向に通水する事によυ汚泥(菌
体)は活性を失わないばかシでなく、効率のよい浄化機
能を得る事が出来る。
Regarding the action and effect, bacteria multiply and increase in the filter media 6 and 6 by passing water through the filter media layers B and B, but the final P
:ii Due to the straining action of the 4 material layer B, the water level in the p1 tank rises, the buffering action and other poetic actions of the spatial layers A and A operate without any trouble, and the perforated plate 4 and the interlayers change to form a flow film. The filth that flows into Hechimaron 6, which is a filter medium with a large water passage space, which is considered inappropriate, does not flow deeply into the filter medium, but gets caught on the inflow surface 9, where bacterial cells are formed. In the long term, the mode of reproduction is due to the chemotaxis of the bacteria, and most of the reproduction increases inside the filter medium 6 on the furnace belly or on the inflow side of the filter medium. ,D
Then, as time passes, the filter media 6, such as the filtration membrane, which peels off, and the bacterial cells that are separated from the filtration media 6 will accumulate in the spatial layer formed along the inflow surface. The water flow is constantly averaged due to the buffering effect of the space layer and the variable inflow direction, so by averaging the accumulated bacteria and passing water laterally, υ sludge (bacteria) can be reduced. You can obtain efficient purification function without losing activity.

以上流入面に沿って空間層を設ける使用方法によって、
活性汚泥層を形成する事で通水空間の大きい濾過材へチ
マロンはその欠点である部分通水が防止出来、その長所
を充分活用出来る0更に通水空間の大きい濾過材は、吐
出口を底面近くに設ける事によるオーバーフロー防止効
果や最終層に於ける漉す作用等の効果が槽内全体に波及
する点で、波及効果上、最も適していて、易分解成分の
大量に処理さnる流入側涙過材層についても最も適する
濾過材となる。
By using the above method of providing a space layer along the inflow surface,
By forming an activated sludge layer, Cimarron can prevent partial water passage, which is its drawback, and make full use of its advantages.Furthermore, filter media with a large water passage space can be used with the discharge port at the bottom. The inlet side is the most suitable in terms of ripple effects, as the effect of overflow prevention by placing it nearby and the straining effect in the final layer spread throughout the tank, and the inflow side where a large amount of easily decomposed components are processed. It is also the most suitable filtration material for the tear filtration material layer.

以上の諸条件によって大量の菌体を立体的に蓄積し、通
水させ接触酸化を計る事により、縦型濾過槽の浄化機能
を顕著に高める事が出来る。
By accumulating a large amount of bacterial cells three-dimensionally under the above-mentioned conditions, and then passing water through the tank to measure catalytic oxidation, the purification function of the vertical filtration tank can be significantly enhanced.

尚、活性汚泥層は極めて長期にわだシ形成するので、こ
の間緩衝空間として基本的な条件である菌の環境条件を
安定させる作用効果を得る事が出来、水と菌との接触の
阻害原因となる流路或いは緩衝空間の汚泥をこ\に集積
する事でそれぞれの機能を長期に持続し、菌の増加によ
っても浄化機能の低下を生じない好都合が得られる。
In addition, since the activated sludge layer forms ruts for an extremely long period of time, it can act as a buffer space to stabilize the environmental conditions for bacteria, which is a basic condition, and prevents the contact between water and bacteria. By accumulating the sludge in the flow path or buffer space, each function can be maintained for a long time, and the purification function is advantageously prevented from deteriorating even when bacteria increase.

以上実施例について説明して米だが、本案は最終のろ過
材層の浄化機能が汚水や菌体の外部流出1その他すべて
をそこで阻止する事で浄化装置としての機能を決定する
ので上述のように水圧差を利用し、最終のろ過材層の通
水を強制的に強化し、最も適するテ過材を利用する事で
浄化機能を顕著に高める事が出来、更に濾過材を天然又
は人工の繊維質を不規則に絡1せた木毛状物、或いは不
織布状のヂ材等にする事で必要時には、掃除再生が容易
であり、第2図及び第3図のような利用方法によシ増加
する菌体を集積し、大量の菌体の活性を保ち、且つ、浄
化力?得る事が出来、菌の増加によっても機能の低下を
生じないと云う従来にない特徴を具備させる事が出来る
。その構造が簡単であるので養魚用、生活雑排水、深床
排水の浄化等その目的に応じて巾広く利用する事が出来
る。
The above example has been explained, but in this case, the purification function of the final filter layer determines the function as a purification device by blocking the external outflow 1 of sewage and bacterial cells, and so on. By using the water pressure difference to forcibly strengthen the water passage through the final filtration material layer, and by using the most suitable filtration material, the purification function can be significantly enhanced. It is easy to clean and recycle when necessary by using irregularly tangled wood wool or non-woven fabric, and it can be easily recycled using the methods shown in Figures 2 and 3. Accumulates an increasing number of bacterial cells, maintains the activity of a large amount of bacterial cells, and has purifying power? It can be provided with the unprecedented feature that the function does not deteriorate even when bacteria increase. Since its structure is simple, it can be used for a wide variety of purposes, such as fish farming, domestic gray water, and deep bed drainage purification.

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

第1図乃至第3図は本発明の実施例を示す断面図である
。図に於いて、1は本体、2は流入パイプ、3は吐出パ
イプ、4及び5は多孔板、6は濾過材、7は通水孔、8
は流入口、9は濾過材層流人面である。
1 to 3 are cross-sectional views showing embodiments of the present invention. In the figure, 1 is the main body, 2 is an inflow pipe, 3 is a discharge pipe, 4 and 5 are perforated plates, 6 is a filter material, 7 is a water hole, 8
9 is the inflow port, and 9 is the laminar flow surface of the filter material.

Claims (3)

【特許請求の範囲】[Claims] (1)槽内を流れ方向に空間層をおいて、少くとも1個
以上のろ過材層を立設して仕切り、一端の空間層に流入
管、他端空間層に吐出管を設け、横方向に通水して接触
酸化を計るろ過装置に於て、吐出口を底面或いは底面近
くに設け、吐出側のろ過材層のろ過材が漉す作用のある
砂利、又は砕石その他の粒材或いは人工又は天然の繊維
質を不規則に絡ませた木毛状物で構成されている事を特
徴とするろ過装置。
(1) A space layer is placed in the flow direction inside the tank, and at least one or more filter media layers are installed vertically to partition the tank, an inlet pipe is provided in the space layer at one end, a discharge pipe is provided in the space layer at the other end, and the space layer is placed horizontally. In a filtration device that measures catalytic oxidation by passing water in the same direction, the discharge port is provided at or near the bottom, and the filter layer on the discharge side is made of gravel, crushed stone, other granular materials, or artificial material that acts as a filter. Or a filtration device characterized by being composed of a wood-hair-like material in which natural fibers are irregularly entangled.
(2)流入側ろ過材層のろ過材が通水空間の大きい人工
或いは天然の繊維質を不規則に絡ませた木毛状物である
特許請求の範囲第1項記載のろ過装置。
(2) The filtration device according to claim 1, wherein the filter medium of the inflow side filter layer is a wood wool-like material in which artificial or natural fibers with a large water passage space are irregularly entangled.
(3)ろ過材層が多孔板或いは波形の多孔板のあいだに
人工或いは天然の繊維質を不規則に絡ませた木毛状物を
収納したものである特許請求の範囲第1項記載のろ過装
置。
(3) The filtration device according to claim 1, wherein the filtration material layer is a perforated plate or a corrugated perforated plate containing a wood wool-like material in which artificial or natural fibers are irregularly entangled. .
JP59152637A 1984-07-23 1984-07-23 Filter Pending JPS6133293A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP59152637A JPS6133293A (en) 1984-07-23 1984-07-23 Filter

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP59152637A JPS6133293A (en) 1984-07-23 1984-07-23 Filter

Publications (1)

Publication Number Publication Date
JPS6133293A true JPS6133293A (en) 1986-02-17

Family

ID=15544748

Family Applications (1)

Application Number Title Priority Date Filing Date
JP59152637A Pending JPS6133293A (en) 1984-07-23 1984-07-23 Filter

Country Status (1)

Country Link
JP (1) JPS6133293A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0459097A (en) * 1990-06-22 1992-02-25 Ohbayashi Corp Water quality purifying equipment
JP2008104999A (en) * 2006-10-27 2008-05-08 Samutekku:Kk Apparatus for treating water to be treated

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0459097A (en) * 1990-06-22 1992-02-25 Ohbayashi Corp Water quality purifying equipment
JP2008104999A (en) * 2006-10-27 2008-05-08 Samutekku:Kk Apparatus for treating water to be treated

Similar Documents

Publication Publication Date Title
US20060138048A1 (en) Method for treating a contaminated fluid, system for treating a contaminated fluid, and method for making a biomass carrier suitable for treating a contaminated fluid
US5976374A (en) Self-cleansing filter
JPS6133293A (en) Filter
JPS5919584A (en) Catalytic oxidation tank equipped with washing means
JP3221307B2 (en) Water purification device with floating body
CN206219386U (en) A kind of deep filter layer multimedium filter material filter pool for advanced treatment of wastewater
CA2565052A1 (en) System for improved dissolved air floatation with a biofilter
JP4032367B2 (en) Water purification equipment
JP3022194U (en) Ornamental water tank wet & dry water purification device
JPS6133294A (en) Filter
JPH0999890A (en) Toilet device for ship
JP2565427B2 (en) Organic sewage biological filtration equipment
JPH09155383A (en) Foul water purification device
JPH0596288A (en) Sewage purifying tank
CN218527322U (en) Be arranged in aquaculture in-process water circulation purifier
CN215249870U (en) Anti-blocking type constructed wetland
JPH04166292A (en) Filtering device
JPH04166293A (en) Filtering device
JP2601391B2 (en) Biological nitrification denitrification equipment
JPH0642793Y2 (en) Aerobic immersion ▲ Floor ▼ Floor equipment
JP2946016B2 (en) Water pollution prevention block and water pollution prevention method
JP2565453B2 (en) Upflow biological nitrification denitrification method and apparatus
JP2584384B2 (en) Method and apparatus for treating organic sewage
JPH0339726B2 (en)
JPH05138183A (en) Sewage purification tank