JPS6254521B2 - - Google Patents
Info
- Publication number
- JPS6254521B2 JPS6254521B2 JP58187357A JP18735783A JPS6254521B2 JP S6254521 B2 JPS6254521 B2 JP S6254521B2 JP 58187357 A JP58187357 A JP 58187357A JP 18735783 A JP18735783 A JP 18735783A JP S6254521 B2 JPS6254521 B2 JP S6254521B2
- Authority
- JP
- Japan
- Prior art keywords
- water
- tank
- pipe
- filtration
- 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
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 208
- 238000001914 filtration Methods 0.000 claims description 57
- 238000000746 purification Methods 0.000 claims description 26
- 238000011001 backwashing Methods 0.000 claims description 23
- 239000008213 purified water Substances 0.000 claims description 22
- 238000000926 separation method Methods 0.000 claims 1
- 239000007787 solid Substances 0.000 description 11
- 238000004140 cleaning Methods 0.000 description 8
- 230000000630 rising effect Effects 0.000 description 7
- 230000000694 effects Effects 0.000 description 6
- 230000007423 decrease Effects 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 239000002184 metal Substances 0.000 description 2
- 238000005406 washing Methods 0.000 description 2
- 238000010521 absorption reaction Methods 0.000 description 1
- 230000002411 adverse Effects 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- JEGUKCSWCFPDGT-UHFFFAOYSA-N h2o hydrate Chemical compound O.O JEGUKCSWCFPDGT-UHFFFAOYSA-N 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 238000005192 partition Methods 0.000 description 1
- 230000035515 penetration Effects 0.000 description 1
- 229910052573 porcelain Inorganic materials 0.000 description 1
- 239000011148 porous material Substances 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 238000011085 pressure filtration Methods 0.000 description 1
- 230000001105 regulatory effect Effects 0.000 description 1
- 239000011347 resin Substances 0.000 description 1
- 229920005989 resin Polymers 0.000 description 1
- 239000010865 sewage Substances 0.000 description 1
- 239000012209 synthetic fiber Substances 0.000 description 1
- 229920002994 synthetic fiber Polymers 0.000 description 1
- 239000002351 wastewater Substances 0.000 description 1
Landscapes
- Filtration Of Liquid (AREA)
Description
【発明の詳細な説明】
本発明は、濾材逆洗機能付き濾過装置、更に詳
述すれば、濾過槽内の濾材が洗浄の必要な目詰り
状態となつたとき、当該濾材を濾過槽内から取り
外すことなく自動的に逆洗(通常の濾過作用時に
於ける原水流通方向とは逆向きに洗浄水を流通さ
せて行う洗浄)させることが出来る濾材逆洗機能
付き濾過装置に関するものである。DETAILED DESCRIPTION OF THE INVENTION The present invention provides a filtration device with a filter media backwashing function, and more specifically, when the filter media in the filtration tank becomes clogged and requires cleaning, the filter media can be removed from the filtration tank. This invention relates to a filtration device with a filter media backwashing function that allows automatic backwashing (cleaning performed by flowing wash water in the opposite direction to the flow direction of raw water during normal filtration) without removing the filter.
濾過装置に使用される多孔質濾材としては、多
孔質磁器、発泡樹脂、天然又は合成繊維、金属
網、焼結金属等があり、これ等の濾材は気孔径1
〜100μの範囲に調整され、安定性も高く一般に
広く用いられている。このような多孔質濾材は、
原水中の懸浮物質(以下、SSと略称する)が濾
材中に付着する目詰りによつて濾過能力が低下す
れば、新しい物と交換したり洗浄して再使用する
必要がある。従来の濾過装置で、濾材を濾過槽内
から取り外すことなく逆洗し得るようにしたもの
も知られているが、従来のこの種の濾過装置で
は、原水流通路とは別に濾材逆洗用洗浄水の流通
路を設け、逆洗必要時期に原水供給を断つて洗浄
水供給に切り換える必要があつたため、濾過装置
全体の構造が非常に複難になるばかりでなく、原
水とは別に洗浄水を必要とする欠点があつた。 Porous filter media used in filtration devices include porous porcelain, foamed resin, natural or synthetic fibers, metal mesh, sintered metal, etc. These filter media have a pore size of 1
It is adjusted to a range of ~100μ, has high stability, and is widely used in general. Such porous filter media are
If suspended solids (hereinafter abbreviated as SS) in raw water adhere to the filter media and the filtration ability decreases due to clogging, the filter must be replaced with a new one or cleaned and reused. Some conventional filtration devices are known that allow backwashing of the filter media without removing it from the filtration tank. It was necessary to provide a water flow path and cut off the raw water supply and switch to the wash water supply when backwashing was required, which not only made the overall structure of the filtration device extremely complicated, but also required washing water to be supplied separately from the raw water. It had the necessary flaws.
更に、従来の濾過装置は一般に強制加圧濾過法
によるものであつて、原水を濾過槽へ加圧供給し
て濾材を通過させるものであるから、原水中の
SSは濾材中に強固に付着することになり、当該
濾材を逆洗するためには同等以上の高圧で洗浄水
を供給する必要があるばかりでなく、十分な洗浄
効果を得ることが困難であつた。又、濾材の洗浄
開始を自動的に行わせるためには、濾材目詰りに
伴う原水圧力の変化を高精度に検出する必要があ
り、自動制御を行う点でも問題があつた。 Furthermore, conventional filtration devices generally use forced pressure filtration, in which raw water is supplied under pressure to a filtration tank and passed through a filter medium.
SS will adhere firmly to the filter media, and in order to backwash the filter media, it is not only necessary to supply cleaning water at an equivalent or higher pressure, but it is also difficult to obtain a sufficient cleaning effect. Ta. Furthermore, in order to automatically start cleaning the filter medium, it is necessary to detect with high precision changes in the pressure of raw water due to clogging of the filter medium, which also poses a problem in terms of automatic control.
本発明は上記のような問題点を悉く解消し得る
濾材逆洗機能付き濾過装置を提供するものであつ
て、以下にその実施例を添付の例示図に基づいて
説明する。 The present invention provides a filtration device with a filter media backwashing function that can solve all of the above-mentioned problems, and embodiments thereof will be described below with reference to the attached illustrative drawings.
第1図は多筒式の濾過装置を示し、第2図は単
筒式の濾過装置を示す。何れの濾過装置も基本的
には同一構造であつて、互いに対応する箇所には
同一符号を付している。図に於て、1は濾過槽、
2は濾過槽1の上部に連設された浄水槽、3は浄
水槽2よりも高所に配設された原水槽、4は減速
槽、5は上昇管部5aの下端が濾過槽1の原水供
給部1aに接続されたサイフオン用逆U字形管、
6は前記逆U字形管5の下降管部5bの下端に接
続された自動開閉手段、7は前記濾過槽1内に垂
直に内装された筒状濾材(以下、濾筒と略称す
る)である。前記逆U字形管5の上端Uターン部
5cは前記浄水槽2の上端より高所に位置し、こ
の上端Uターン部5c内の上部と前記浄水槽2内
の底部とが連通管8によつて連通せしめられてい
る。 FIG. 1 shows a multi-tube type filtration device, and FIG. 2 shows a single-tube type filtration device. Both filter devices basically have the same structure, and corresponding parts are given the same reference numerals. In the figure, 1 is a filter tank,
2 is a water purification tank connected to the upper part of the filtration tank 1, 3 is a raw water tank arranged at a higher place than the water purification tank 2, 4 is a deceleration tank, and 5 is the lower end of the rising pipe part 5a of the filtration tank 1 an inverted U-shaped pipe for a siphon connected to the raw water supply section 1a;
Reference numeral 6 designates an automatic opening/closing means connected to the lower end of the descending pipe portion 5b of the inverted U-shaped pipe 5, and 7 designates a cylindrical filter medium (hereinafter abbreviated as a filter cylinder) installed vertically within the filter tank 1. . The upper U-turn portion 5c of the inverted U-shaped pipe 5 is located higher than the upper end of the water purification tank 2, and the upper portion of the upper U-turn portion 5c and the bottom portion of the water purification tank 2 are connected to each other by the communication pipe 8. It is connected by a wire.
前記濾筒7は、第3図及び第4図に示すように
多孔管9に一定の環状空間を隔てて同心状に遊嵌
された状態で上端蓋板10aと下端蓋板10bと
によつて挾着保持されている。前記多孔管9は、
その上端部が濾過槽1と浄水槽2との間に隔壁1
1を貫通して浄水槽2内に開口し、下端開口部は
キヤツプ12によつて閉塞されている。13は濾
筒7に対して一定の環状空間14を隔てて同心状
に外嵌する外筒であつて、その上端が前記上端蓋
板10aに取付けられ、下端は開放されている。
尚、第2図に示す単筒式濾過装置では濾過槽1の
囲壁が前記外筒13を兼用している。 As shown in FIGS. 3 and 4, the filter tube 7 is loosely fitted into the porous tube 9 in a concentric manner with a certain annular space in between, and is fitted with an upper end cover plate 10a and a lower end cover plate 10b. It is held in place. The porous pipe 9 is
The upper end is a partition wall 1 between the filtration tank 1 and the water purification tank 2.
1 and opens into the water purification tank 2, and the lower end opening is closed by a cap 12. Reference numeral 13 denotes an outer cylinder which is fitted concentrically to the filter cylinder 7 with a certain annular space 14 in between.The upper end of the outer cylinder 13 is attached to the upper end cover plate 10a, and the lower end is open.
In the single-tube filtration device shown in FIG. 2, the surrounding wall of the filtration tank 1 also serves as the outer cylinder 13.
前記自動開閉手段6の詳細は第5図に示されて
いる。図示の通り自動開閉手段6は、上部主開閉
バルブ15と下部副開閉バルブ16、及びフロー
ト17を内装した水槽18から構成されている。
前記主開閉バルブ15は、円錐状弁座19を備え
且つ上端が前記逆U字形管5の下降管部5bに連
通する弁函20と、この弁函20内に於て上下動
可能で且つ上下方向の貫通路21を備えた円錐状
可動弁体22とから構成され、前記円錐状弁座1
9の側面には、下降限位置にある前記可動弁体2
2によつて閉塞される弁孔23が設けられてい
る。24は前記上下両バルブ15,16を内装す
る放水槽であつて、放水管25を備え、且つ前記
弁孔23と連通している。 Details of the automatic opening/closing means 6 are shown in FIG. As shown in the figure, the automatic opening/closing means 6 includes an upper main opening/closing valve 15, a lower auxiliary opening/closing valve 16, and a water tank 18 in which a float 17 is installed.
The main opening/closing valve 15 includes a valve case 20 which is provided with a conical valve seat 19 and whose upper end communicates with the descending pipe portion 5b of the inverted U-shaped pipe 5, and which is movable up and down within the valve case 20. a conical movable valve body 22 with a through passage 21 in the direction, and the conical valve seat 1
9, the movable valve body 2 is located at the lower limit position.
A valve hole 23 is provided which is closed by 2. Reference numeral 24 denotes a water discharge tank in which the upper and lower valves 15 and 16 are housed, and is provided with a water discharge pipe 25 and communicates with the valve hole 23.
前記副開閉バルブ16は、前記弁函20の底部
に可動弁体22と同心位置に於て形成された弁孔
26を上下動によつて開閉するニードル弁体27
を備え、このニードル弁体27は、その上方軸部
27aが前記可動弁体22を相対上下動可能に貫
通し、上動により前記可動弁体22を押し上げる
ことが出来る。このニードル弁体27によつて開
閉される弁孔26の下側空間28は、連通孔29
を介して前記放水槽24に連通すると共に、連通
孔30を介して前記水槽18に連通している。 The auxiliary opening/closing valve 16 includes a needle valve element 27 that opens and closes a valve hole 26 formed at the bottom of the valve case 20 at a position concentric with the movable valve element 22 by vertical movement.
The needle valve body 27 has an upper shaft portion 27a that passes through the movable valve body 22 so as to be relatively vertically movable, and can push up the movable valve body 22 by upward movement. A space 28 below the valve hole 26 that is opened and closed by the needle valve body 27 is connected to a communication hole 29.
It communicates with the water tank 24 through a hole 30, and with the water tank 18 through a communication hole 30.
前記水槽18内のフロート17は、上動によつ
て前記副開閉バルブ16のニードル弁体27を、
その上方突出軸部17aを介して押し上げること
が出来る。31は水槽18内の水を抜くための小
径のサイフオン管である。32は水槽18内と逆
U字形管5に於ける上端Uターン部5c内の上部
とを連通させる連通管である。 The float 17 in the water tank 18 moves the needle valve body 27 of the sub-opening/closing valve 16 by upward movement.
It can be pushed up via its upwardly protruding shaft portion 17a. 31 is a small-diameter siphon tube for draining water from the water tank 18. 32 is a communication pipe that communicates the inside of the water tank 18 with the upper part of the upper end U-turn portion 5c of the inverted U-shaped pipe 5.
次に使用方法及び作用を説明する。河川水、工
業汚水、一般廃水等、懸浮物質(SS)の少ない
水、或いは前処理した水(以下、原水と略称す
る)は、原水供給管33より原水槽3に供給さ
れ、オーバーフロー管34により一定水位に保た
れた状態で給水管35を経て減速槽4に流入す
る。ここで流速が落され、給水管36及び流量調
整バルブ37を経由して濾過槽1の底部開口、即
ち原水供給部1aから濾過槽1内に入る。そして
この濾過槽1内の濾筒7で濾過された後の浄水は
浄水槽2内に入り、浄水槽2内を一定レベルL1
まで満たした後に浄水槽上端の出水管38よりオ
ーバーフローし、給水として利用される。39は
浄水槽2内からの空気抜き管である。濾過槽1の
原水供給部1aに供給される原水の一部は逆U字
形管5の上昇管部5a内に入り、水圧により自然
に上昇する。前記給水管36中の流量調整バルブ
37は、出水管38からの出水量が規定の水量と
なるように調整し、固定しておく。このときの逆
U字形管5の上昇管部5aに於ける原水レベル
L2と浄水槽2内の浄水レベルL1との水位差が本
装置の濾過開始水頭H1となる。 Next, the method of use and effect will be explained. Water with low suspended solids (SS), such as river water, industrial sewage, and general wastewater, or pretreated water (hereinafter referred to as raw water) is supplied to the raw water tank 3 through the raw water supply pipe 33, and is supplied to the raw water tank 3 through the overflow pipe 34. The water flows into the deceleration tank 4 through the water supply pipe 35 while being maintained at a constant water level. Here, the flow rate is reduced, and the water enters the filtration tank 1 from the bottom opening of the filtration tank 1, that is, the raw water supply section 1a, via the water supply pipe 36 and the flow rate adjustment valve 37. The purified water after being filtered by the filter tube 7 in the filter tank 1 enters the water purification tank 2, and the inside of the water purification tank 2 is kept at a certain level L1.
After the water is filled to the maximum, it overflows from the water outlet pipe 38 at the upper end of the water purification tank and is used as water supply. 39 is an air vent pipe from inside the water purification tank 2. A portion of the raw water supplied to the raw water supply section 1a of the filtration tank 1 enters the rising pipe section 5a of the inverted U-shaped pipe 5 and naturally rises due to water pressure. The flow rate regulating valve 37 in the water supply pipe 36 is adjusted and fixed so that the amount of water coming out from the water outlet pipe 38 is a specified amount. The raw water level in the rising pipe section 5a of the inverted U-shaped pipe 5 at this time
The water level difference between L2 and the purified water level L1 in the water purifying tank 2 becomes the filtration start water head H1 of this device.
濾過運転が進むにつれて濾筒7に付着するSS
量が増加し、この濾筒7に於ける水流抵抗が増し
て濾過水量が減少する。一方、原水供給量は一定
であるため上昇管部5aに於ける原水レベルが上
昇することになり、遂には原水の一部が逆U字形
管5の上端Uターン部5cを越えて下降管部5b
に流入し始める。このとき、第5図に示すように
自動開閉手段6に於ける主開閉バルブ15の可動
弁体22及び副開閉バルブ16のニードル弁体2
7は下降限位置にあつて、これ等弁体22,27
によつて開閉される弁孔23,26が閉塞されて
いるので、下降管部5b内に原水が貯留されてゆ
くことになる。逆U字形管5内の空気は、連通管
32、水槽18、連通孔30,29、放水槽2
4、及び放水管25を経由して排出される。 SS that adheres to the filter tube 7 as the filtration operation progresses
As the amount of filtered water increases, the water flow resistance in this filter tube 7 increases, and the amount of filtered water decreases. On the other hand, since the amount of raw water supplied is constant, the level of raw water in the rising pipe section 5a will rise, and a portion of the raw water will eventually exceed the U-turn section 5c at the upper end of the inverted U-shaped pipe 5 and reach the descending pipe section. 5b
begins to flow into At this time, as shown in FIG.
7 is at the lower limit position, and these valve bodies 22, 27
Since the valve holes 23 and 26, which are opened and closed by the downcomer pipe 5b, are closed, raw water is stored in the downcomer pipe portion 5b. The air inside the inverted U-shaped pipe 5 is transferred to a communication pipe 32, a water tank 18, communication holes 30, 29, and a water discharge tank 2.
4 and is discharged via the water discharge pipe 25.
下降管部5b内に流入して漸次上昇する原水
は、遂には上端Uターン部5cを含めて逆U字形
管5の全体に充満するレベルL3に到達し、この
結果、上端Uターン部5c内の上部から連通管3
2を経由して原水が水槽18内に流入することに
なる。この水槽18内に流入した原水がフロート
17を上昇させる結果、その上端突出軸部17a
が副開閉バルブ16のニードル弁体27を押し上
げ、弁孔26を開放する。続いて、上昇するニー
ドル弁体27が主開閉バルブ15の可動弁体22
を押し上げるので、弁孔23が開放される。従つ
て下降管部5b内の原水が弁函20、弁孔23、
及び放水槽24を経由して放水管25より急速に
放出され、この結果サイフオン作用が開始され、
原水が連続的に放出される。このサイフオン作用
による単位時間当り放水量を給水管36から供給
される原水の単位時間当り給水量よりも十分大な
らしめておくことにより、当該サイフオン作用に
よる高水頭の吸水力は、原水供給部1a及び濾過
槽1内を経由して浄水槽2内の浄水に作用し、こ
の浄水槽2内の浄水が濾過槽1及び逆U字形管5
を経由して、給水管36より供給されている原水
と共に放出管25より連続的に放出される。これ
が濾筒7に対する高水頭の逆洗水となる。 The raw water that flows into the downcomer pipe section 5b and gradually rises finally reaches a level L3 where the entire inverted U-shaped pipe 5, including the upper end U-turn section 5c, is filled, and as a result, the inside of the upper end U-turn section 5c. Connecting pipe 3 from the top of
The raw water flows into the water tank 18 via 2. As a result of the raw water flowing into this water tank 18 lifting the float 17, its upper end protruding shaft portion 17a
pushes up the needle valve body 27 of the sub-opening/closing valve 16 and opens the valve hole 26. Subsequently, the rising needle valve body 27 touches the movable valve body 22 of the main opening/closing valve 15.
, the valve hole 23 is opened. Therefore, the raw water in the downcomer pipe section 5b flows through the valve box 20, the valve hole 23,
and is rapidly discharged from the water discharge pipe 25 via the water discharge tank 24, and as a result, the siphon action is started,
Raw water is continuously released. By making the amount of water discharged per unit time due to this siphon action sufficiently larger than the amount of water supplied per unit time of raw water supplied from the water supply pipe 36, the water absorption power of the high water head due to the siphon action is It acts on the purified water in the water purification tank 2 via the filtration tank 1, and the purified water in the water purification tank 2 passes through the filtration tank 1 and the inverted U-shaped pipe 5.
The raw water is continuously discharged from the discharge pipe 25 along with the raw water supplied from the water supply pipe 36. This becomes high water head backwash water for the filter cylinder 7.
即ち、逆U字形管5の上端に到達した原水レベ
ルL3と浄水槽2に於ける浄水レベルL1との水位
差が、濾筒7に対する逆洗開始水頭H2となり、
前記のように逆洗作用が開始される結果、濾過開
始水頭H1から逆洗開始水頭H2までの範囲の低〜
中レベルの水頭に対応する圧力で濾筒7の表側に
付着しているSSが、高水頭の逆洗水となつて濾
過槽1内の濾筒7を裏側から表側へ逆向きに流動
する浄水槽2内の浄水によつて洗浄除去される。 That is, the water level difference between the raw water level L3 that has reached the upper end of the inverted U-shaped pipe 5 and the purified water level L1 in the water purification tank 2 becomes the backwashing start water head H2 for the filter cylinder 7,
As a result of the start of the backwashing action as described above, the range from the filtration start water head H1 to the backwash start water head H2 is low to
SS attached to the front side of the filter tube 7 under pressure corresponding to a medium level water head becomes high water head backwash water and flows backward through the filter tube 7 in the filtration tank 1 from the back side to the front side.Purified water It is washed and removed by purified water in tank 2.
浄水槽2内の浄水レベルが連通管8の開口レベ
ルと等しい下限レベルL4に達すると、空気がこ
の連通管8を経由して逆U字形管5に於ける上端
Uターン部5c内に流入するため、サイフオン作
用が停止し、供給管36より供給される原水は再
び濾過槽1内に流入し、所期の濾過作用が開始さ
れる。同時に、逆U字形管5の上昇管部5aに於
ける原水は濾過開始水頭H1に対応するレベルL2
まで戻る。 When the purified water level in the water purification tank 2 reaches the lower limit level L4, which is equal to the opening level of the communication pipe 8, air flows into the upper U-turn portion 5c of the inverted U-shaped pipe 5 via this communication pipe 8. Therefore, the siphon action is stopped, the raw water supplied from the supply pipe 36 flows into the filtration tank 1 again, and the desired filtration action is started. At the same time, the raw water in the rising pipe section 5a of the inverted U-shaped pipe 5 is at a level L2 corresponding to the filtration start water head H1.
Go back to.
尚、上記のサイフオン作用に基づく濾筒逆洗作
用時に於ては、自動開閉手段6に於ける水槽18
内の水はサイフオン管31より漸次排出される
が、この排出水量よりも多量の水が連通管32、
副開閉バルブ16の弁孔26、及び放水槽24よ
り水槽18内に連続的に流入しているので、フロ
ート17は所要レベルまで浮上した状態に保持さ
れる。又、逆U字形管5内への空気の流入により
逆洗作用が終了したときは、下降管部5b内の水
は主開閉バルブ15の弁孔23及び副開閉バルブ
16の弁孔26から完全に流出し、この後、水槽
18内の水がサイフオン管31によつて排出され
る結果、フロート17が下降し、これに伴つてニ
ードル弁体27及び可動弁体22が重力によつて
下降限位置まで下降し、弁孔23,26が夫々閉
塞される。こうして次の逆洗作用の準備が整う。 In addition, during the filter cylinder backwashing action based on the above-mentioned siphon action, the water tank 18 in the automatic opening/closing means 6
The water inside is gradually discharged from the siphon pipe 31, but a larger amount of water than this discharged water flows into the communication pipe 32,
Since the water continuously flows into the water tank 18 from the valve hole 26 of the sub-opening/closing valve 16 and the water discharge tank 24, the float 17 is maintained in a floating state to a required level. Furthermore, when the backwashing action is completed due to the inflow of air into the inverted U-shaped pipe 5, the water in the descending pipe section 5b is completely drained from the valve hole 23 of the main opening/closing valve 15 and the valve hole 26 of the sub opening/closing valve 16. After that, the water in the water tank 18 is discharged by the siphon pipe 31, and as a result, the float 17 descends, and as a result, the needle valve body 27 and the movable valve body 22 reach their lower limit due to gravity. The valve holes 23 and 26 are respectively closed. In this way, preparations for the next backwashing operation are completed.
本発明の濾材逆洗機能付き濾過装置は以上のよ
うに実施し且つ使用し得るものであつて、その特
徴とする点は、多孔質濾材を使用した濾過槽を通
過した浄水を前記濾過槽の上部に形成された浄水
槽を経由させて流出させるようにした濾過装置に
於て、前記濾過槽の原水供給部に、前記浄水槽内
の浄水レベル(実施例ではL1)より上端Uター
ン部が高いサイフオン用逆U字形管の一端を接続
し、この逆U字形管の他端に、この逆U字形管内
が満水状態となつたときに開路に切り換えられ且
つ前記浄水槽内の浄水レベルが一定レベル以下
(実施例ではL4)となつたときに閉路に切り換え
られる自動開閉手段を接続した点にある。 The filtration device with a filter medium backwashing function of the present invention can be implemented and used as described above, and its characteristic point is that purified water that has passed through a filtration tank using a porous filter medium is transferred to the filtration tank. In a filtration device that allows water to flow out through a water purification tank formed at the top, the raw water supply section of the filtration tank has an upper end U-turn section that is lower than the purified water level (L1 in the embodiment) in the water purification tank. One end of the inverted U-shaped pipe for the high siphon is connected to the other end of the inverted U-shaped pipe, and the circuit is switched to open when the inverted U-shaped pipe is full of water, and the purified water level in the water purification tank is kept constant. The point is that an automatic opening/closing means is connected which switches the circuit to closed when the voltage drops below the level (L4 in the embodiment).
このような本発明の濾過装置によれば、濾過運
転開始時に於ける前記逆U字形管の上昇管部での
原水レベルが前記浄水槽内の浄水レベルより若干
(例えば10cm程度)高くなるように、濾過槽に対
する原水の供給量と供給圧力を調整しておけば、
上記原水レベルと浄水レベルとの水位差(実施例
ではL2−L1)に相当する低水頭(実施例では
H1)に対応した圧力差から、前記逆U字形管内
の原水レベルが当該逆U字形管の上端に達したと
きの浄水レベルとの水位差(実施例ではL3−
L1)に相当する中水頭(実施例ではH2)に対応
した圧力差までの範囲内で濾過作用を行わせ、濾
材の目詰りによつて前記中水頭に対応する圧力差
が生じれば、自動的にサイフオン作用を開始させ
て浄水槽内の浄水を高水頭に対応する逆向きの圧
力差で逆流させ、以て濾過槽内の濾材を逆洗する
ことが出来る。又、所定量の浄水が逆流して逆洗
が完了すれば、自動的に元の濾過運転状態に復帰
させることが出来るのである。 According to the filtration device of the present invention, the level of raw water at the riser section of the inverted U-shaped pipe at the start of filtration operation is slightly higher (for example, about 10 cm) than the level of purified water in the water purification tank. , if you adjust the amount and pressure of raw water supplied to the filtration tank,
A low water head (in the example, L2-L1 in the example) corresponds to the water level difference between the raw water level and the purified water level above (L2-L1 in the example).
Based on the pressure difference corresponding to H1), the water level difference (L3-
The filtration action is performed within the range up to the pressure difference corresponding to the medium water head (H2 in the example) corresponding to L1), and if a pressure difference corresponding to the medium water head occurs due to clogging of the filter medium, automatic The siphon action is started immediately to cause the purified water in the water purification tank to flow back with a pressure difference in the opposite direction corresponding to the high water head, thereby making it possible to backwash the filter medium in the filtration tank. Moreover, when a predetermined amount of purified water flows back and the backwashing is completed, the original filtration operation state can be automatically restored.
従つて従来装置のように、原水流通路とは別に
濾材逆洗用洗浄水の流通路を設け、逆洗必要時期
に原水供給を断つて洗浄水供給に切り換える必要
がないため、濾過装置全体の構造が非常にシンプ
ルになるばかりでなく、原水とは別に洗浄水を準
備しておく必要もなくなる。更に、上記のように
濾材に対する原水の通過圧力差は非常に低く抑え
ることになるため、原水中のSSは濾材表面に軽
く付着することになり、従つて濾過槽上部の浄水
槽内の浄水をサイフオン作用で逆流させるだけで
あるにも拘わらず十分な洗浄効果を得ることが出
来るに至つたのである。 Therefore, unlike conventional equipment, there is no need to provide a wash water flow path for filter medium backwashing separately from the raw water flow path, and to cut off the raw water supply and switch to the wash water supply when backwashing is required. Not only is the structure extremely simple, but it also eliminates the need to prepare washing water separately from raw water. Furthermore, as mentioned above, the pressure difference of the raw water passing through the filter media is kept very low, so SS in the raw water will lightly adhere to the surface of the filter media, and therefore the purified water in the water purification tank at the top of the filter tank will be reduced. Even though the siphon effect only causes the water to flow backwards, a sufficient cleaning effect can be obtained.
又、逆洗開始及び濾過運転再開を自動的に行わ
せるために、濾材目詰りに伴う微妙な原水圧力の
変化を検出する必要はなく、逆U字形管内の原水
や浄水槽内の浄水の水位の変化を捉えて自動開閉
手段を開閉させれば良いので、制御系も簡単とな
り、しかも高精度の自動制御が行える。 In addition, in order to automatically start backwashing and restart filtration operation, there is no need to detect subtle changes in raw water pressure due to filter media clogging, and the level of raw water in the inverted U-shaped pipe or purified water in the water purification tank can be adjusted automatically. Since the automatic opening/closing means can be opened and closed based on changes in the temperature, the control system is simple and highly accurate automatic control can be performed.
又、濾過槽内の構造も、実施例に示したような
濾筒利用の構造に限定されないが、実施例に示す
ように濾筒を垂直に配設して、濾過槽内で原水が
下方から上方へと流通する間に当該濾筒を通過す
るような濾過槽を構成する場合に於ては、濾過運
転時の濾過槽内での原水流程が所謂短絡流又は偏
流となると、濾筒の全有効濾材表面を原水が均等
に流通しなくなり、濾筒の有効濾材表面の内、原
水流量が多い箇所(原水流速の大なる箇所であつ
て、濾材の目詰りによつて漸次移行する)での濾
材に対するSSの侵入深さが大となり、全体的に
は、濾筒の全有効濾材表面を原水が均等に流通す
る場合と比較して、濾材に対するSSの付着力が
増大する。このことは、サイフオン作用によつて
浄水を逆流させて行う濾材の逆洗作用に悪影響を
もたらすことになる。更に、逆洗作用時に於て
も、濾過槽内を逆流する洗浄水(浄水槽内の浄
水)が短絡流や偏流となると、その洗浄水が流通
する箇所の濾材表面だけが逆洗されることにな
り、部分的な洗浄によつて水流抵抗が部分的に低
下すると、その箇所にのみ洗浄水が集中的に流通
することになり、濾筒の全有効濾材表面を均等に
洗浄することが不可能となる。 Furthermore, the structure inside the filter tank is not limited to the structure that uses a filter tube as shown in the example, but as shown in the example, the filter tube is arranged vertically so that the raw water flows from below in the filter tank. When configuring a filtration tank that passes through the filter cylinder while flowing upward, if the flow of raw water in the filtration tank during filtration operation becomes a so-called short-circuit flow or a biased flow, the whole filter cylinder will be completely drained. The raw water no longer flows uniformly on the surface of the effective filter medium, and the flow rate of raw water is high at the points on the surface of the effective filter medium of the filter tube (areas where the flow rate of raw water is high, and it gradually migrates due to clogging of the filter medium). The penetration depth of the SS into the filter medium increases, and overall, the adhesion force of the SS to the filter medium increases compared to the case where the raw water flows evenly over the entire effective surface of the filter cylinder. This has an adverse effect on the backwashing action of the filter medium, which is performed by causing purified water to flow back through the siphon action. Furthermore, during backwashing, if the wash water flowing back in the filter tank (purified water in the water purification tank) becomes short-circuited or drifts, only the surface of the filter medium where the wash water flows will be backwashed. If the water flow resistance is partially lowered due to partial cleaning, the cleaning water will flow concentrated only to that area, making it impossible to evenly clean the entire effective filter media surface of the filter cylinder. It becomes possible.
上記の点に鑑み、第1図及び第2図に示すよう
に濾筒7を垂直に配設した濾過槽1に対する原水
の出入り口の配置と、濾筒7に対する原水の出入
り口の配置とを考慮することにより、原水の流程
を短絡流や偏流とならないように調整し、又、第
1図に示す多筒式の濾過槽に於ては、第4図に示
すように各濾筒7に対して導水作用をする外筒1
3を付設することにより、総ての濾筒7に於て、
その全有効濾材表面を原水又は逆洗時の浄水が均
等に流通するようにしている。 In view of the above points, consider the arrangement of the inlet and outlet of raw water to the filter tank 1 in which the filter tube 7 is arranged vertically as shown in FIGS. 1 and 2, and the arrangement of the inlet and outlet of raw water to the filter tube 7. By doing so, the flow path of the raw water is adjusted so as not to cause short-circuit flow or uneven flow.In addition, in the multi-tube filter tank shown in Fig. 1, for each filter cylinder 7 as shown in Fig. 4, Outer cylinder 1 that acts as a water guide
3, all filter cylinders 7,
Raw water or purified water during backwashing is made to distribute evenly over the entire surface of the effective filter medium.
第3図は実験的に外筒13を付設した濾筒7と
外筒13を付設しない濾筒7とを併用した濾過槽
1を示しており、図に於て、C位置〜E位置に配
設された濾筒7、即ち外筒13を付設した濾筒7
の周囲では、第4図にも示すように外筒13の外
周にのみ×××で示す緩慢流乃至流れの静止状態
が生じ、濾筒7と外筒13との間の原水流通空間
14では矢印で示すように濾筒7の全長、全周囲
に於て所期流速の原水の流れが生じているのに比
べ、外筒13を付設していないA位置及びB位置
の濾筒7の周囲では、濾過槽囲壁に接する箇所に
於て×××で示す緩慢流乃至流れの静止状態が生
じ、濾筒7間では△△△で示す緩慢流及び斜めの
矢印で示す偏流が生じているため、これ等A位置
及びB位置にある外筒13を付設されていない濾
筒7では、その有効濾材表面の全面に原水を均等
に流通させることが出来ていないことが理解出来
よう。 FIG. 3 shows a filter tank 1 that experimentally uses both a filter tube 7 with an outer tube 13 attached and a filter tube 7 without an outer tube 13 attached, and in the figure, the filter tubes 7 are placed at positions C to E. Filter tube 7 installed, that is, filter tube 7 with outer tube 13 attached
As shown in FIG. 4, a slow flow or a stationary state of flow occurs only on the outer periphery of the outer cylinder 13 as indicated by XXX, and in the raw water circulation space 14 between the filter cylinder 7 and the outer cylinder 13. As shown by the arrow, raw water flows at the desired flow rate over the entire length and around the filter tube 7, whereas the flow around the filter tube 7 at the A position and B position where the outer tube 13 is not attached. In this case, a slow flow or a stationary state of flow occurs at the point in contact with the surrounding wall of the filter tank, indicated by ×××, and a slow flow indicated by △△△ and a drifted flow indicated by diagonal arrows occur between the filter tubes 7. It can be understood that in the filter tubes 7 that are not provided with the outer tube 13 located at the A position and the B position, the raw water cannot be distributed evenly over the entire surface of the effective filter medium.
上記のように濾筒7に対して外筒13を付設す
ることにより、総ての濾筒7の全有効濾材表面に
原水を均等に流通させることが出来、濾過効率を
高め、濾材に対するSSの付着状態を逆洗により
容易に洗浄除去し得る状態となし得る。又、逆洗
作用時には、有効濾材表面の全面を確実に洗浄す
ることが出来、所期の逆洗効果を期待し得る。 By attaching the outer tube 13 to the filter tube 7 as described above, raw water can be distributed evenly over all the effective filter media surfaces of all the filter tubes 7, increasing filtration efficiency and reducing the SS for the filter media. The adhesion can be easily removed by backwashing. Furthermore, during backwashing, the entire surface of the effective filter medium can be reliably washed, and the desired backwashing effect can be expected.
第1図は本発明一実施例にかかる多筒式濾過装
置の構成説明図、第2図は同単筒式濾過装置の構
成説明図、第3図は第1図の濾過槽内部の詳細を
示す縦断側面図、第4図は第3図の要部を拡大し
た縦断側面図、第5図は自動開閉手段の一実施例
を示す縦断側面図である。
1……濾過槽、1a……原水供給部、2……浄
水槽、3……原水槽、5……サイフオン用逆U字
形管、5a……上昇管部、5b……下降管部、5
c……上端Uターン部、6……自動開閉手段、7
……濾筒、8,32……連通管、9……多孔質、
13……導水用外筒、15……上部主開閉バル
ブ、16……下部副開閉バルブ、17……フロー
ト、18……水槽、19……円錐状弁座、21…
…貫通路、22……円錐状可動弁体、23,26
……弁孔、24……放水槽、25……放水管、2
7……ニードル弁体、31……小径のサイフオン
管、33……原水供給管、34……オーバーフロ
ー管、35,36……給水管、37……流量調整
バルブ。
FIG. 1 is an explanatory diagram of the configuration of a multi-tube filtration device according to an embodiment of the present invention, FIG. 2 is an explanatory diagram of the configuration of the same single-tube filtration device, and FIG. 3 shows details of the inside of the filtration tank in FIG. 1. FIG. 4 is an enlarged vertical side view of the main part of FIG. 3, and FIG. 5 is a vertical side view showing an embodiment of the automatic opening/closing means. DESCRIPTION OF SYMBOLS 1...Filtering tank, 1a...Raw water supply part, 2...Water purification tank, 3...Raw water tank, 5...Inverted U-shaped pipe for siphon, 5a...Rising pipe part, 5b...Descent pipe part, 5
c... Upper end U-turn part, 6... Automatic opening/closing means, 7
...Filter cylinder, 8,32...Communication pipe, 9...Porous,
13...Outer cylinder for water guiding, 15...Upper main opening/closing valve, 16...Lower auxiliary opening/closing valve, 17...Float, 18...Water tank, 19...Conical valve seat, 21...
...Through passage, 22... Conical movable valve body, 23, 26
... Valve hole, 24 ... Water tank, 25 ... Water pipe, 2
7... Needle valve body, 31... Small diameter siphon pipe, 33... Raw water supply pipe, 34... Overflow pipe, 35, 36... Water supply pipe, 37... Flow rate adjustment valve.
Claims (1)
を前記濾過槽の上部に形成された浄水槽を経由さ
せて流出させるようにした濾過装置に於て、前記
濾過槽の原水供給部に、前記浄水槽内の浄水レベ
ルより上端Uターン部が高いサイフオン用逆U字
形管の一端を接続し、この逆U字形管の他端に放
水管付き放水槽を接続し、該放水槽の下に排水口
付き水槽を配置し、該水槽と上記上端Uターン部
内の上部とを連通管により連通させ、上記水槽内
にフロートを昇降自在に内装し、前記放水槽内
に、下降状態で逆U字形管と上記放水管とを分断
すると共にフロートの上昇により押上げられたと
きには、その分断を解除する可動弁体を昇降自在
に配置し、前記浄水槽内の底部と上記上端Uター
ン部内の上部とを連通させて成る濾材逆洗機能付
き濾過装置。1. In a filtration device that allows purified water that has passed through a filtration tank using a porous filter medium to flow out via a water purification tank formed at the top of the filtration tank, the raw water supply section of the filtration tank is provided with the Connect one end of the inverted U-shaped pipe for the siphon whose upper end U-turn is higher than the purified water level in the water purification tank, connect a water tank with a water discharge pipe to the other end of this inverted U-shaped pipe, and drain water below the water tank. A water tank with a mouth is arranged, the water tank and the upper part of the upper U-turn part are communicated with each other by a communication pipe, a float is installed inside the water tank so as to be able to rise and fall freely, and an inverted U-shaped pipe is installed in the water discharge tank in a downward state. A movable valve body is arranged to be able to move up and down freely to separate the water discharge pipe and the water discharge pipe and to release the separation when the float is pushed up by the rise of the float, and the bottom part in the water purification tank and the top part in the upper U-turn part are disposed. A filtration device with a backwashing function that connects the filter media.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP58187357A JPS6082109A (en) | 1983-10-05 | 1983-10-05 | Filter apparatus with filter backwashing function |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP58187357A JPS6082109A (en) | 1983-10-05 | 1983-10-05 | Filter apparatus with filter backwashing function |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS6082109A JPS6082109A (en) | 1985-05-10 |
| JPS6254521B2 true JPS6254521B2 (en) | 1987-11-16 |
Family
ID=16204577
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP58187357A Granted JPS6082109A (en) | 1983-10-05 | 1983-10-05 | Filter apparatus with filter backwashing function |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS6082109A (en) |
-
1983
- 1983-10-05 JP JP58187357A patent/JPS6082109A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS6082109A (en) | 1985-05-10 |
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