JPS624165B2 - - Google Patents

Info

Publication number
JPS624165B2
JPS624165B2 JP54030404A JP3040479A JPS624165B2 JP S624165 B2 JPS624165 B2 JP S624165B2 JP 54030404 A JP54030404 A JP 54030404A JP 3040479 A JP3040479 A JP 3040479A JP S624165 B2 JPS624165 B2 JP S624165B2
Authority
JP
Japan
Prior art keywords
filter element
water
filtration device
filter
metal tube
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
Application number
JP54030404A
Other languages
Japanese (ja)
Other versions
JPS55121811A (en
Inventor
Kazuhiko Terao
Kenji Shimada
Setsu Kubota
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.)
Totoku Electric Co Ltd
Original Assignee
Totoku Electric Co Ltd
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 Totoku Electric Co Ltd filed Critical Totoku Electric Co Ltd
Priority to JP3040479A priority Critical patent/JPS55121811A/en
Publication of JPS55121811A publication Critical patent/JPS55121811A/en
Publication of JPS624165B2 publication Critical patent/JPS624165B2/ja
Granted legal-status Critical Current

Links

Description

【発明の詳細な説明】 本発明は流体中に浮遊する粒子状物質を除去す
る濾過装置に係るものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a filtration device for removing particulate matter suspended in a fluid.

従来汚水処理に於ける濾過装置としては、砂濾
過装置或いは活性炭濾過装置などが一般に用いら
れて来ている。また有機排水の浄化方法としては
活性汚泥法が一般に行なわれて来ている。
Conventionally, as a filtration device in sewage treatment, a sand filtration device, an activated carbon filtration device, etc. have been generally used. Furthermore, activated sludge method has generally been used as a method for purifying organic wastewater.

しかしながら汚水処理に於ける砂濾過装置や活
性炭濾過装置は、逆洗浄がむずかしく目詰まりを
起しやすい更に長期間の運転が出来ないばかりで
なく保守管理に大きな費用を要する欠点があつ
た。また有機排水に於ける活性汚泥法は、有機物
粒子を活性汚泥フロツクに吸着させて酸化分解し
沈殿槽に導いてフロツクを沈降させて上澄液を浄
化水として放流しているが、汚水中の有機物の負
荷や流入量の経時的変化によつて酸化分解槽での
有機物粒子の消化が一定せず、フロツクの粒子径
や比重が変化して同じ粒子径でも沈降速度が異な
り、沈殿槽での滞留時間を一定に出来ない欠点が
あるそして特に40μ以下の粒子径の小さい物質の
沈降速度は非常に遅いため実質的には上澄液との
分離がむずかしく、分離されずに放流されてしま
う。これ等の微粒子を取り去るためには沈殿槽で
の長時間の滞留が必要となり広い用地と大きな沈
殿槽を必要とするため、膨大な設備費と管理費を
要し経済的見地から得策な方法といい難い。
However, sand filtration equipment and activated carbon filtration equipment used in sewage treatment have drawbacks such as difficult backwashing, easy clogging, inability to operate for long periods of time, and high maintenance costs. In addition, in the activated sludge method for organic wastewater, organic particles are adsorbed onto activated sludge flocs, oxidized and decomposed, led to a settling tank, where the flocs settle and the supernatant liquid is discharged as purified water. Digestion of organic particles in the oxidative decomposition tank is not constant due to changes in organic load and inflow rate over time, and the particle size and specific gravity of the flocs change, resulting in different sedimentation rates even with the same particle size, and It has the disadvantage that the residence time cannot be kept constant, and the sedimentation rate of substances with small particle sizes of 40μ or less is very slow, so it is practically difficult to separate them from the supernatant liquid, and they are discharged without being separated. In order to remove these fine particles, it is necessary to stay in the sedimentation tank for a long time, which requires a large area and a large sedimentation tank, which requires a huge amount of equipment and management costs, so it is not an economical method. Good and difficult.

したがつて、これ等の処理水を中水道用水とし
て使用することは水不足を解消する有効な手段で
はあるが、充分な浄化が安価な費用で行なえなか
つたため、河川へ放流して来ているのが実情であ
る。
Therefore, although using this treated water as gray water is an effective means of resolving water shortages, it has not been possible to purify it sufficiently at a low cost, so it has been discharged into rivers. is the reality.

本発明は上述の点に鑑みなされたもので、その
目的とするところは、外径及びスリツト間隔の異
なるフイルター素子を複数個同心状に配置した濾
過装置の外側から内側へ向つて汚水を通過させる
ことにより、汚水中に浮遊する粒子状物質を粒子
径の大きさの順に各フイルター素子により段階的
に除去し各フイルター素子への負荷を平均化する
と共に、逆洗浄によつて長期間の運転を可能とす
ることによつて水処理を能率良く行なう点にあ
る。別の目的は、沈殿槽のような膨大な面積と施
設を必要とすることなく小型で安価な濾過設備を
提供し水処理コストを低廉にすると共に、水の再
利用を可能とする点にある。
The present invention has been made in view of the above points, and its purpose is to pass wastewater from the outside to the inside of a filtration device in which a plurality of filter elements with different outer diameters and slit intervals are arranged concentrically. By doing this, particulate matter suspended in wastewater is removed step by step by each filter element in order of particle size, and the load on each filter element is averaged, and backwashing allows long-term operation. The point is that water treatment can be carried out efficiently by making it possible. Another purpose is to provide small and inexpensive filtration equipment that does not require huge areas and facilities such as sedimentation tanks, thereby reducing water treatment costs and making it possible to reuse water. .

以下に本発明を図面について説明する。 The invention will be explained below with reference to the drawings.

第1図イは本発明の濾過装置を構成するフイル
ター素子の有孔多角金属管芯体の一例を示す斜視
図で、六角金属管芯体1の各辺面に液体の通過孔
2を穿ち、望ましくは上記各辺面を内側に歪ませ
てわん曲面3を形成せしめる。芯体1は六角金属
管に限定されるものではなく、三角形状以上の多
角の金属管であればよい。第1図ロ及びハはフイ
ルター素子5の斜視図及び部分拡大断面図で、有
孔多角金属管芯体1の外周面にフイルター用線4
がスリツト間隔dが一定になるようにスペース巻
きされており、わん曲面3により芯体1とフイル
ター用線4との間に空間が形成され、液体の流通
を良くしている。
FIG. 1A is a perspective view showing an example of a perforated polygonal metal tube core of a filter element constituting the filtration device of the present invention, in which liquid passage holes 2 are bored on each side of the hexagonal metal tube core 1. Preferably, each side surface is distorted inward to form a curved surface 3. The core body 1 is not limited to a hexagonal metal tube, but may be any polygonal metal tube having a triangular shape or more. FIGS. 1B and 1C are a perspective view and a partially enlarged cross-sectional view of the filter element 5, in which filter wires 4 are attached to the outer peripheral surface of the perforated polygonal metal tube core 1.
is space-wound so that the slit interval d is constant, and a space is formed between the core body 1 and the filter wire 4 by the curved surface 3, which improves the flow of liquid.

第2図イ及びロは本発明濾過装置の斜視図及
び側面図で、第1図における有孔多角金属管芯体
1の外径が段階的に異なつたフイルター素子5,
5′,5″を複数個外側から内側へ同心状に配置
し、各フイルター素子間に空隙を保持するように
組立てたものである。この際各フイルター素子の
スリツト間隔dは有孔多角金属管芯体1の外径の
大きさに従つて順次狭くなるように設計されてい
ることが必要である。
FIGS. 2A and 2B are a perspective view and a side view of the filtration device 6 of the present invention, in which the filter elements 5 and 5 have a perforated polygonal metal tube core 1 in FIG.
A plurality of filter elements 5' and 5'' are arranged concentrically from the outside to the inside, and assembled so as to maintain a gap between each filter element. At this time, the slit interval d of each filter element is a perforated polygonal metal tube. It is necessary that the core body 1 is designed to be gradually narrower as the outer diameter of the core body 1 increases.

汚水は矢印7の方向から流入し、各フイルター
素子5,5′,5″で濾過されて浄水が矢印8の方
向へ流出する。この場合最外層のフイルター素子
5は、例えば沈殿槽に於いて100μ以上の沈降速
度の速い粒子状物質を短時間で沈降分離した上澄
液から比較的沈降速度の遅い50〜100μ径の粒子
状物質を除去して、その内側(中間)のフイルタ
ー素子5′に対する負荷を軽減する。中間のフイ
ルター素子5′は、最外層のフイルター素子5を
通過した濾液中に含まれる粒子径が20〜50μ程度
の粒子状物質を分離する、従つて河川への放流水
は有機物負荷が減少し水質が常に安定したものと
なる。中間のフイルター素子5′を通過した濾液
は、内層のフイルター素子5″において粒子径3
〜20μの粒子状物質が取り除かれ、これを通過し
た濾液が中水道用水として供給されるものであ
る。なおフイルター素子5,5′,5″の数は三層
に限定されるものではなく、必要に応じ増減し得
る。
Sewage flows in from the direction of arrow 7, is filtered by each filter element 5, 5', and 5'', and purified water flows out in the direction of arrow 8. In this case, the outermost filter element 5 is placed in a sedimentation tank, for example. Particulate matter with a diameter of 50 to 100μ, which has a relatively slow sedimentation rate, is removed from the supernatant liquid obtained by sedimentation and separation of particulate matter with a diameter of 100μ or more and a fast sedimentation rate in a short period of time. The middle filter element 5' separates particulate matter with a particle size of about 20 to 50 μm contained in the filtrate that has passed through the outermost filter element 5, and therefore reduces the load on water discharged into the river. The organic matter load is reduced and the water quality is always stable.The filtrate that has passed through the middle filter element 5' has a particle size of 3" in the inner layer filter element 5".
Particulate matter of ~20 microns is removed, and the filtrate that passes through this is supplied as gray water. Note that the number of filter elements 5, 5', 5'' is not limited to three layers, and can be increased or decreased as necessary.

第3図は本発明の濾過装置を装着した濾過設
備の系統図を示す。1〜8の符号は第2図と同一
部分を表わす。9は濾過設備の外囲壁であり、1
0は沈殿槽、11は汚水、12は汚水波上ポン
プ、13は汚水取入れ口弁、14は放流水取出し
口弁、15は中水道用水取出し口弁、16は逆洗
浄用圧縮空気取り入れ口弁、17は汚泥取出し口
弁をそれぞれ示す。まず活性汚泥槽によつて処理
された汚水を沈殿槽10に導き100μ以上の大き
なフロツクを沈降させ、その上澄液をポンプ12
で波上げ、濾過装置内へ送り込む。汚水は各フ
イルター素子5,5′,5″により濾過される。内
層のフイルター素子5″を通過した濾液は中水道
用水取出し口弁15を経て中水道用水として供給
され、またここで分離されたものは放流水取出し
口弁14を通つて放流水となる。各フイルター素
子が目詰まりしたときは、逆洗浄用圧縮空気取入
れ口弁16を通して圧縮空気を導入し、フイルタ
ー用線4,4′,4″に詰まつた粒子状物質を吹き
飛ばして逆洗浄を行なう。その際の汚泥は汚泥取
出し口弁17から取り出す。
FIG. 3 shows a system diagram of a filtration facility equipped with the filtration device 6 of the present invention. Reference numerals 1 to 8 represent the same parts as in FIG. 9 is the outer wall of the filtration equipment; 1
0 is a sedimentation tank, 11 is sewage, 12 is a sewage wave pump, 13 is a sewage intake valve, 14 is a discharge water outlet valve, 15 is a gray water water outlet valve, 16 is a compressed air intake valve for backwashing , 17 indicate sludge outlet valves, respectively. First, sewage treated in the activated sludge tank is led to the settling tank 10, where large flocs of 100μ or more are settled, and the supernatant liquid is pumped into the sedimentation tank 10.
The waves are raised and sent into the filtering device 6 . The waste water is filtered by each filter element 5, 5', 5''. The filtrate that has passed through the inner layer filter element 5'' is supplied as gray water water through a gray water outlet valve 15, and is also separated here. The water passes through the discharge water outlet valve 14 and becomes discharge water. When each filter element becomes clogged, compressed air is introduced through the backwashing compressed air intake valve 16 to blow away particulate matter stuck in the filter wires 4, 4', 4'' and perform backwashing. The sludge at that time is taken out from the sludge outlet valve 17.

このように本発明濾過装置は、濾過と逆洗浄を
繰返すことにより長時間の連続運転を行なえる特
徴があり、経済的効果は非常に大きい。
As described above, the filtration device of the present invention has a feature that it can be operated continuously for a long time by repeating filtration and backwashing, and has a very large economic effect.

以下に本発明の実施例について記載する。 Examples of the present invention will be described below.

実施例 対角が24.0mm、肉厚が0.6mmの有孔六角ステン
レス管の外周に、ビツカース硬度160で線径が0.6
mmφのステンレス線をスリツト間隔が50μの一定
間隔をもつよう巻回し、最外層のフイルター素子
5を製作した。同様に対角が18.0mm、肉厚が0.6
mmの有孔六角ステンレス管の外周に、0.6mmステ
ンレス線を20μのスリツト間隔で巻回し中間のフ
イルター素子5′を、また対角が12.0mm、肉厚が
0.6mmの有孔六角ステンレス管の外周に、0.6mmス
テンレス線を5μのスリツト間隔で巻回し内層の
フイルター素子5″を製作した。各フイルター素
子を外径とスリツト間隔の大きさの順に、外側か
ら内側へ段階的に同心状に配置し、本発明濾過装
置を構成した。沈殿槽内の浮遊粒子状物質濃度が
250ppmの上澄液を上記濾過装置を装着せる濾過
設備に送り、濾過した所、放流水取出し口弁14
からは浮遊粒子状物質濃度3.2ppmの水質を持つ
た放流用処理水が得られた、また中水道用水取出
し口弁15からは浮遊粒子状物質濃度0.8ppmの
中水道用水として満足な処理水を能率よく得るこ
とが出来た。
Example A wire diameter of 0.6 with a Bitkers hardness of 160 was placed on the outer periphery of a perforated hexagonal stainless steel tube with a diagonal of 24.0 mm and a wall thickness of 0.6 mm.
The outermost filter element 5 was manufactured by winding stainless steel wire of mmφ so that the slits had a constant interval of 50 μm. Similarly, the diagonal is 18.0mm and the wall thickness is 0.6
A 0.6 mm stainless steel wire is wound around the outer periphery of a perforated hexagonal stainless steel tube with a slit interval of 20 μ to form an intermediate filter element 5', with a diagonal of 12.0 mm and a wall thickness.
A 0.6 mm stainless steel wire was wound around the outer periphery of a 0.6 mm perforated hexagonal stainless steel tube with a slit interval of 5 μ to produce an inner layer filter element 5''. The filtration device of the present invention was constructed by arranging concentrically inward in stages.The suspended particulate matter concentration in the sedimentation tank was
The supernatant liquid of 250 ppm is sent to the filtration equipment equipped with the above filtration device, and after filtering, the discharge water outlet valve 14
Treated water for discharge with a suspended particulate matter concentration of 3.2 ppm was obtained from the outlet valve 15, and treated water with a suspended particulate matter concentration of 0.8 ppm was obtained from the water outlet valve 15. I was able to get it efficiently.

以上説明したように本発明の濾過装置は、外径
及びスリツト間隔の異なるフイルター素子を複数
個同心状に配置し汚水を通過させるようにしたも
のであるから、小型で安価な設備費にもかかわら
ず高い浄化能力と大きな処理能力を持ち、処理費
用を安価にすると共に、水の再利用の促進をはか
ることができる。また有機物排水に於ける活性汚
泥処理方法による処理水を、さらに浄化して河川
の有機物負荷を効率よく減少させることができ
る。加えてフイルター素子の目詰まりも、逆洗浄
により簡単に吹き飛ばすことができ、長時間の連
続運転が可能となつた。
As explained above, the filtration device of the present invention has a plurality of filter elements having different outer diameters and slit intervals arranged concentrically to allow wastewater to pass through it, so it is small and has low equipment costs. It has a high purification ability and a large treatment capacity, making it possible to reduce treatment costs and promote water reuse. In addition, the treated water by the activated sludge treatment method for organic wastewater can be further purified to efficiently reduce the organic matter load in rivers. In addition, clogged filter elements can be easily blown away by backwashing, making continuous operation possible for long periods of time.

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

第1図イは本発明濾過装置を構成するフイルタ
ー素子の有孔多角金属管芯体の斜視図、同ロ及び
ハはフイルター素子の斜視図及び部分拡大断面図
である。第2図イ及びロは本発明濾過装置の斜視
図及び側面図である。第3図は本発明濾過装置を
装着した濾過設備の系統図である。 1,1′,1″…有孔多角金属管芯体、2…濾波
通過孔、3…わん曲面、4,4′,4″…フイルタ
ー用線、5,5′,5″…フイルター素子、…濾
過装置、9…外囲壁、10…沈殿槽、11…汚
水、12…ポンプ、13…汚水取入れ口弁、14
…放流水取出し口弁、15…中水道用水取出し口
弁、16…逆洗浄用圧縮空気取入れ口弁、17…
汚泥取出し口弁。
FIG. 1A is a perspective view of a perforated polygonal metal tube core of a filter element constituting the filtration device of the present invention, and FIGS. 1B and 1C are a perspective view and a partially enlarged sectional view of the filter element. FIGS. 2A and 2B are a perspective view and a side view of the filtration device of the present invention. FIG. 3 is a system diagram of filtration equipment equipped with the filtration device of the present invention. 1, 1', 1''...Perforated polygonal metal tube core, 2...Filtering passage hole, 3...Round curved surface, 4, 4', 4''...Filter wire, 5, 5', 5''...Filter element, 6 ...filtration device, 9...outer wall, 10...sedimentation tank, 11...sewage, 12...pump, 13...sewage intake valve, 14
...Discharge water outlet valve, 15...Water outlet valve for middle water supply, 16...Compressed air intake valve for backwashing, 17...
Sludge outlet valve.

Claims (1)

【特許請求の範囲】[Claims] 1 多角金属管の各辺面を内側に歪ませてわん曲
面を形成し、かつこれに液体の通過孔を穿つた有
孔多角金属管芯体上に、任意のスリツト間隔を保
持してフイルター用線を巻回してなる複数個のフ
イルター素子を、各フイルター素子の外径とスリ
ツト間隔の大きさの順に、該各フイルター素子間
に空隙を保持するように外側から内側へ段階的に
同心状に配置し組立てたことを特徴とする濾過装
置。
1 Each side surface of a polygonal metal tube is distorted inward to form a curved surface, and a perforated polygonal metal tube core with liquid passage holes is formed on the core body, and an arbitrary slit interval is maintained to form a filter. A plurality of filter elements formed by winding a wire are arranged concentrically from the outside to the inside in order of the outer diameter of each filter element and the size of the slit interval so as to maintain a gap between each filter element. A filtration device characterized by being arranged and assembled.
JP3040479A 1979-03-15 1979-03-15 Filtration device Granted JPS55121811A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP3040479A JPS55121811A (en) 1979-03-15 1979-03-15 Filtration device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP3040479A JPS55121811A (en) 1979-03-15 1979-03-15 Filtration device

Publications (2)

Publication Number Publication Date
JPS55121811A JPS55121811A (en) 1980-09-19
JPS624165B2 true JPS624165B2 (en) 1987-01-29

Family

ID=12302993

Family Applications (1)

Application Number Title Priority Date Filing Date
JP3040479A Granted JPS55121811A (en) 1979-03-15 1979-03-15 Filtration device

Country Status (1)

Country Link
JP (1) JPS55121811A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2013071054A (en) * 2011-09-28 2013-04-22 Jfe Engineering Corp Filter body and filter having the same
JP5399384B2 (en) * 2008-06-11 2014-01-29 株式会社クラレ Filter element, filter module and filtration device

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP5399384B2 (en) * 2008-06-11 2014-01-29 株式会社クラレ Filter element, filter module and filtration device
JP2013071054A (en) * 2011-09-28 2013-04-22 Jfe Engineering Corp Filter body and filter having the same

Also Published As

Publication number Publication date
JPS55121811A (en) 1980-09-19

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