JPH08318107A - Filter - Google Patents

Filter

Info

Publication number
JPH08318107A
JPH08318107A JP7146881A JP14688195A JPH08318107A JP H08318107 A JPH08318107 A JP H08318107A JP 7146881 A JP7146881 A JP 7146881A JP 14688195 A JP14688195 A JP 14688195A JP H08318107 A JPH08318107 A JP H08318107A
Authority
JP
Japan
Prior art keywords
trough
baffle
water
filter
tower
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
JP7146881A
Other languages
Japanese (ja)
Other versions
JP3518060B2 (en
Inventor
Hideyo Yamauchi
英世 山内
Satoru Nagai
悟 長井
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.)
Kurita Water Industries Ltd
Original Assignee
Kurita Water Industries 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 Kurita Water Industries Ltd filed Critical Kurita Water Industries Ltd
Priority to JP14688195A priority Critical patent/JP3518060B2/en
Publication of JPH08318107A publication Critical patent/JPH08318107A/en
Application granted granted Critical
Publication of JP3518060B2 publication Critical patent/JP3518060B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Abstract

PURPOSE: To surely discharge an oil component floating on a water surface while preventing a filter medium from being discharged during backward washing. CONSTITUTION: In a filter in which raw water is passed through a filter bed 12 in a downflow to be filtered and washing water is passed through the filter bed in an upflow to backwash the filter bed, in a space above the filter bed in a filter column 10, a trough 19 from which raw water overflow and also into which waste washing water overflows to regulate a water surface W in the column at an upper surface 19', a separation inclined body 22 placed below the trough 19 and having, on the upper surface, a downward inclined part 23 whose lower end forms a vertical flow passage 24, and the 1st and the 2nd baffles 26, 27 vertically installed above the downward inclined part 23 of the separation inclined body 22 with their lower ends being separated form the inclined part 23 are formed. The 1st baffle 26 is placed near the flow passage, and the 2nd baffle 27 is separated from the 1st baffle, vertically toward the trough. The upper ends of the 1st baffle 26 and the 2nd baffle 27 are positioned under the water surface regulated by the trough 19 in the column, and at the same level as the water surface W regulated by the upper surface of the trough in the column, respectively.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】この発明は濾過塔内に充填した濾
層に原水を下向流で通水して濾過処理すると共に、空気
及び洗浄水を濾層に上向流で通水し、濾層を展開して洗
浄する濾過装置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention allows raw water to flow through a filter bed packed in a filter tower in a downward flow to perform filtration treatment, and air and washing water to flow through the filter bed in an upward flow. The present invention relates to a filter device for developing and cleaning a filter layer.

【0002】[0002]

【従来の技術】このような下向流濾過、上向流洗浄(逆
洗)を行う濾過装置で、空気を併用した逆洗の際に濾層
を構成する濾材の一部が洗浄排水に混ざって塔外に排出
されるのを防止するため、濾過塔内の濾層の上方空間の
水中に傾斜案内板と、この傾斜案内板の上り坂の上方に
立設され、上端部が水面から上に突出した垂直バッフル
板とからなる固液分離装置を設け、逆洗によって傾斜案
内板上に巻き上げられた濾材の一部が傾斜案内板の上面
に発生する下降流で該上面を伝り、その下端から濾層上
に落下して戻るようにしたものは公知である。
2. Description of the Related Art In a filtering device for performing such a downflow filtration and an upflow washing (backwashing), a part of the filter material constituting the filter layer is mixed with the washing drainage during the backwashing using air together. In order to prevent the water from being discharged to the outside of the tower, the inclined guide plate is set up in the water in the space above the filter bed in the filtration tower, and it is erected above the slope of the inclined guide plate, and the upper end is above the water surface. A solid-liquid separation device consisting of a vertical baffle plate protruding from the inclined guide plate is provided, and a part of the filter medium rolled up on the inclined guide plate by backwash is transmitted to the upper surface of the inclined guide plate by a downward flow, It is known to drop the film from the lower end onto the filter layer and return it.

【0003】[0003]

【発明が解決しようとする課題】上述した固液分離装置
によって、逆洗の際に濾材の一部が洗浄排水に混ざって
排出されるのを防止できるが、空気が水面で横移動する
のを阻止し、塔頂の空気抜きから放出するために水面上
に突出した垂直バッフル板の上端部に遮られて水面に浮
上した油分が排出されず、この油分が次第に蓄積し、運
転を長期間行うと、油分が徐々に濾材を汚染し、処理水
の悪化が生じる。
The above-mentioned solid-liquid separation device can prevent a part of the filter medium from being mixed with the cleaning drainage and discharged during backwashing, but the air can move laterally on the water surface. The oil that floats above the water surface is not discharged because it is blocked by the upper end of the vertical baffle plate that projects above the water surface in order to release it from the air vent at the top of the tower. However, the oil gradually contaminates the filter medium, causing deterioration of the treated water.

【0004】[0004]

【課題を解決するための手段】本発明は上述した問題点
を解消するために開発されたもので、濾過塔内に充填し
た濾層に原水を下向流で通水して濾過処理すると共に、
空気及び洗浄水を濾層に上向流で通水し、濾層を展開し
て洗浄する濾過装置において、塔内の濾層の上方の空間
内に、原水を溢出すると共に、洗浄排水が溢入して塔内
の水面を上面で規制するトラフと、上記トラフの下に位
置し、上面に下向き傾斜部を有し、該下向き傾斜部の下
端が上下方向の流路を形成する分離傾斜体と、この分離
傾斜体の下向き傾斜部の上方に下端を離して立設された
第1,第2の2つのバッフルとを設け、第1バッフルは
上記流路の近くに、第2バッフルは第1バッフルからト
ラフの方に離して立設し、且つ第1バッフルの上端はト
ラフが規制する塔内の水面下に、第2バッフルの上端は
トラフの上面が規制する塔内の水面と同じレベルに位置
させたことを特徴とする。
The present invention was developed in order to solve the above-mentioned problems, and the raw water is passed through the filter bed filled in the filtration tower in a downward flow to carry out the filtration treatment. ,
In a filter device in which air and wash water are passed through the filter layer in an upward flow, and the filter layer is developed and washed, raw water overflows into the space above the filter layer in the tower, and wash drainage overflows. A trough that enters and controls the water surface in the tower with an upper surface, and a separating slant that is located below the trough and that has a downward slope on the upper surface, and the lower end of the downward slope forms a vertical flow path. And two baffles, a first baffle and a second baffle, which are erected with their lower ends separated from each other, above the downwardly inclined portion of the separation inclined body. The first baffle is near the flow path, and the second baffle is the first baffle. Stand upright from the first baffle toward the trough, and the upper end of the first baffle is below the water level in the tower controlled by the trough, and the upper end of the second baffle is at the same level as the water level in the tower controlled by the upper surface of the trough. It is characterized by being located in.

【0005】[0005]

【実施例】図示の各実施例において、10は濾過塔で、
塔内下部にある通水支持板11上には砂利13を最下
層、その上に砂の濾材層14、更にその上にアンスラサ
イトの濾材層15を重ねて濾層12が設けてある。砂利
13の最下層中には処理水の流出管と逆洗用の洗浄水の
導入管を兼ねた給排管16を上、逆洗用の圧縮空気の送
気管17を下にして敷設してある。
EXAMPLES In each of the illustrated examples, 10 is a filtration tower,
On the water-passing support plate 11 in the lower part of the tower, a gravel 13 is provided as the lowermost layer, a sand filter medium layer 14 is formed thereon, and an anthracite filter medium layer 15 is further laminated thereon to form a filter layer 12. In the lowermost layer of the gravel 13, a supply / discharge pipe 16 that doubles as an outflow pipe for treated water and an inlet pipe for wash water for backwashing is laid up, and an air supply pipe 17 for compressed air for backwashing is laid down. is there.

【0006】濾過塔内の濾層12の上方の空間18内に
は、原水の供給と、洗浄排水の排出を兼ねた管20が接
続したトラフ19が設けてある。濾過工程時に管20か
らトラフ内に供給された原水はトラフの上面から溢出
し、逆洗工程時に濾層中を上向流した洗浄排水はトラフ
の上面から内部に溢入して管20から塔外に排出され
る。濾過工程時、逆洗工程時のいずれの場合も、濾過塔
内の水面Wはトラフ19に規制されてその上面19´と
同じレベルである。
In the space 18 above the filter layer 12 in the filter tower, there is provided a trough 19 to which a pipe 20 is connected, which serves to both supply raw water and discharge cleaning wastewater. The raw water supplied from the pipe 20 into the trough during the filtration process overflows from the upper surface of the trough, and the washing wastewater that has flowed upward in the filter layer during the backwash process overflows into the trough from the upper surface to the inside of the tower. It is discharged outside. In both the filtering step and the backwashing step, the water surface W in the filtration tower is regulated by the trough 19 and is at the same level as the upper surface 19 'thereof.

【0007】22は上記トラフ19の下の水面下に位置
して設けられた分離傾斜体で、その上面は下向き傾斜部
23になって居り、下向き傾斜部の下端は上下方向に開
放した流路24を形成し、トラフ19から溢出して下向
流する原水は下向き傾斜部を伝り流路24を流下して濾
層12の上面に達し、濾層中を下向流して濾過される。
又、濾層中を上向流した洗浄排水は上記流路24を上昇
して水面Wに達し、トラフに溢入する。空気を併用して
逆洗を行う場合に、空気が分離傾斜体の下面下に溜るの
を防ぐため、分離傾斜体の下面25は流路24に向かっ
て上向きの斜面にし、空気が下面25を伝って流路24
に移動し、浮上するようにしておくことが好ましい。
Reference numeral 22 denotes a separating slant body provided below the water surface below the trough 19, and the upper surface thereof is a downward slant portion 23, and the lower end of the downward slant portion is a flow path which is opened in the vertical direction. The raw water that forms 24 and overflows from the trough 19 and flows downward flows along the downwardly inclined portion, flows down the flow path 24, reaches the upper surface of the filter layer 12, and flows downward in the filter layer to be filtered.
In addition, the washing drainage flowing upward in the filter layer ascends in the flow path 24, reaches the water surface W, and overflows into the trough. When backwashing is performed by using air together, in order to prevent air from accumulating under the lower surface of the separation inclined body, the lower surface 25 of the separation inclined body is an upward slope toward the flow path 24, and the air lowers the lower surface 25. Flow path 24
It is preferable to move to and float.

【0008】分離傾斜体の下向き傾斜部23上の水中に
は流路24の近くに第1バッフル26、この第1バッフ
ル26からトラフの方に離して第2バッフル27が立設
してある。両バッフル26,27の下端は下向き傾斜部
23の上面から上に少し離れている。第1バッフル26
の上端は水面下にあり、第2バッフル27の上端は水面
Wと同レベルに位置する。
A first baffle 26 and a second baffle 27, which is separated from the first baffle 26 toward the trough, are erected in the water on the downwardly inclined portion 23 of the separation inclined body near the flow path 24. The lower ends of the baffles 26 and 27 are slightly apart from the upper surface of the downward slope 23. First baffle 26
Is above the water surface, and the upper end of the second baffle 27 is located at the same level as the water surface W.

【0009】図1,2の実施例ではトラフ19、分離傾
斜体22は濾過体の同じ直径方向に設けてあり、トラフ
の幅は狭いのに対し、分離傾斜体は広幅で、幅は濾過塔
の直径の約3/4であり、流路24は分離傾斜体22の
左右両側と濾過塔の内周との間に濾過塔の直径の約1/
8宛の幅で2つ形成してある。そして、第1バッフル2
6は分離傾斜体の左右両側部の近くの上方に、トラフと
平行に2つ立設してある。又、第2バッフル27は、第
1バッフルからトラフの方に離して第1バッフルと平行
に2つ立設してある。
In the embodiment shown in FIGS. 1 and 2, the trough 19 and the separating slant 22 are provided in the same diameter direction of the filter, and the width of the trough is narrow, whereas the separating slant is wide and the filtering tower is wide. Is about 3/4 of the diameter of the filtration tower, and the flow path 24 is between the left and right sides of the separation slant 22 and the inner circumference of the filtration tower, and is about 1/3 of the diameter of the filtration tower.
Two are formed with a width of eight. And the first baffle 2
Two 6 are erected in parallel with the trough above the left and right sides of the separation slant. Further, two second baffles 27 are provided upright in parallel with the first baffle, apart from the first baffle toward the trough.

【0010】管20はトラフ19、分離傾斜体22の支
持を兼ねて濾過塔の底を貫通し、塔の中心に沿って立
ち、上端部は塔の直径方向のトラフの中央底部を貫通し
て開口している。管20が開口するトラフの中央部1
9″は膨らみを持たせてある。これにより濾過工程の
際、管20を上昇した原水はトラフ19の内部に入り、
トラフ19の全長の両側から塔内に溢出し、流路24を
経て濾層12中を下向流して濾過され、処理水は給排管
16に接続した処理水の排水管28から流出する。又、
逆洗工程の際は洗浄排水はトラフ19内に溢入し、トラ
フに接続した排出管21から排出される。
The pipe 20 penetrates through the bottom of the filtration tower for supporting the trough 19 and the separating slant 22 and stands along the center of the tower, and the upper end thereof penetrates through the central bottom of the diametrical trough of the tower. It is open. Central part 1 of trough where pipe 20 opens
9 ″ has a bulge, which allows the raw water that has risen in the pipe 20 to enter the inside of the trough 19 during the filtration process.
The treated water overflows into the tower from both sides of the entire length of the trough 19, flows downward through the filter layer 12 through the flow path 24, is filtered, and the treated water flows out from the treated water drain pipe 28 connected to the supply / discharge pipe 16. or,
During the backwashing process, the cleaning wastewater overflows into the trough 19 and is discharged from the discharge pipe 21 connected to the trough.

【0011】図3,4の実施例ではトラフ19、分離傾
斜体22は濾過塔の内周に沿って円周方向に設けてあ
る。分離傾斜体の上面の下向き傾斜部23は塔の中心に
向かって下り傾斜し、この下向き傾斜部の下端の内周は
塔の中心部に上下方向に開放した円形の流路24を形成
する。従って、トラフ19に供給されて溢出する原水は
上記流路24を流下し、濾層12中を下向流して濾過さ
れ、処理水は給排水管16に接続した処理水の排水管2
8から流出する。
In the embodiment shown in FIGS. 3 and 4, the trough 19 and the separating slant 22 are provided circumferentially along the inner circumference of the filtration tower. The downward sloping portion 23 of the upper surface of the separating sloping body is sloping downward toward the center of the tower, and the inner circumference of the lower end of the downward sloping portion forms a circular channel 24 that is open in the vertical direction in the central portion of the tower. Therefore, the raw water which is supplied to the trough 19 and overflows flows down through the flow path 24 and flows downward in the filter layer 12 to be filtered, and the treated water is drained from the treated water drain pipe 2 connected to the water supply / drain pipe 16.
Outflow from 8.

【0012】第1バッフル26は環状で、分離傾斜体の
下向きに傾斜部の下端の内周ないし流路の近くの上方に
立設してある。又、第2バッフル27は、第1バッフル
よりも直径が大きい環状で、第1バッフルからトラフ1
9の方に離して同心状に立設してある。
The first baffle 26 has an annular shape and is erected downwardly of the separating slanting body above the inner circumference of the lower end of the slanting portion or near the flow path. The second baffle 27 has an annular shape having a diameter larger than that of the first baffle, and the trough 1 extends from the first baffle.
They are erected concentrically and separated from each other.

【0013】図1,2、図3,4のいずれの実施例で
も、逆洗工程は任意に設定できるが、通常は空気のみ
で濾層をほぐす工程、空気と洗浄水を併用して濾層を
展開させ、濾材に付着したSSを剥離する工程、流速
を上げて洗浄水のみで濾材に付着したSSを剥離すると
共に、剥離したSSを排出し、且つ濾層を比重が大小に
異なる複数の濾材層で構成した場合は濾材層の境界面で
濾材を分級する工程とからなる。
In any of the embodiments shown in FIGS. 1, 2, 3 and 4, the backwashing step can be arbitrarily set, but normally, the step of loosening the filter layer with only air, or the combination of air and washing water is used. To remove the SS adhering to the filter medium, the flow rate is increased to exfoliate the SS adhering to the filter medium only with washing water, and the exfoliated SS is discharged, and the filter layers have a plurality of different specific gravities. When the filter material layer is used, it comprises a step of classifying the filter material at the boundary surface of the filter material layer.

【0014】の工程を行うには送気管17にコンプレ
ッサからの圧縮空気を20〜50m/時で、3〜10分
間供給し、濾層中を上向流する気泡で濾層をほぐし、濾
材に付着したSSを濾材から剥離すると共に、剥離した
SSを濾層の上部に押し上げる。濾層中を上向流した気
泡は、分離傾斜体の下面25を伝わり流路24に向かっ
て移動し、流路24かつ真上の水面に浮上し、塔頂の開
にした空気抜き10´から外に放出される。
In order to carry out the step (1), compressed air from the compressor is supplied to the air supply pipe 17 at a rate of 20 to 50 m / hour for 3 to 10 minutes, and the filter layer is loosened by the bubbles flowing upward in the filter layer to form a filter medium. The attached SS is peeled off from the filter medium, and the peeled SS is pushed up to the upper part of the filter layer. The bubbles that have flowed upward in the filter bed travel along the lower surface 25 of the separation gradient body and move toward the flow path 24, and rise to the water surface directly above the flow path 24, and from the air vent 10 'opened at the top of the tower. Released to the outside.

【0015】の工程が終ったら、空気の供給を続けた
まゝで、洗浄水の供給管29に接続した逆洗ポンプPを
運転し、洗浄水を20〜50m/時の流速で、3〜10
分間供給し、空気と洗浄水を濾層中に上向流させ、濾材
に付着したSSを剥離すると共に剥離したSSを洗浄排
水と一緒に流路24を上昇させてトラフ19に溢入さ
せ、管20から排出する。
After the step (3) is completed, the backwash pump P connected to the washing water supply pipe 29 is operated while the air is continuously supplied, and the washing water is supplied at a flow rate of 20 to 50 m / hour for 3 to 10 minutes.
Supplied for a minute, air and wash water are allowed to flow upward into the filter layer, the SS attached to the filter medium is peeled off, and the peeled SS together with the wash drainage is caused to rise in the channel 24 to overflow into the trough 19, Discharge from tube 20.

【0016】この場合、流路24を上昇した洗浄排水は
上端が水面下にある第1バッフル26の上を通りトラフ
19に向かって流れるが、上端が水面と同レベルにある
第2バッフル27で遮られて流れは緩和され、第1バッ
フルの上端を越えてトラフ19に向かう流れaは僅かに
なり、流れの大部分bは第1,第2バッフルの間を下降
し、分離傾斜体の下向き傾斜部23に沿い、第1バッフ
ルの下を潜って流路24に向かう流れcと、下向き傾斜
部を上り、第2バッフルの下を潜ってトラフ19に向か
う流れdに別れる。SSは流れdに乗ってトラフに溢入
し、排出管21から排出される。又、流路24から分離
傾斜体の上に巻き上げられた濾材は、第1,第2バッフ
ルの間で下降する間に重力で下向き傾斜部上に落ち、流
れdと分離して流れcに乗り、下向き傾斜部の上を転が
って流路24に達し、そこから濾層の上面に落下して回
収される。尚、洗浄水と併用された空気は流路24中を
上昇して水面Wに浮上し、空気抜き10´から外に放出
される。
In this case, the washing drainage that has risen in the flow path 24 flows toward the trough 19 while passing over the first baffle 26 whose upper end is below the water surface, but the second baffle 27 whose upper end is at the same level as the water surface. The flow is blocked and the flow is moderated, the flow a toward the trough 19 over the upper end of the first baffle becomes small, and most of the flow b descends between the first and second baffles, and the separation slant is directed downward. Along the sloping portion 23, there is a flow c that dives under the first baffle toward the flow path 24 and a flow d that goes up the downward sloping portion and dives under the second baffle toward the trough 19. The SS flows on the flow d, overflows into the trough, and is discharged from the discharge pipe 21. Further, the filter medium rolled up from the flow path 24 onto the separation slant falls on the downward slanted portion by gravity while descending between the first and second baffles, and is separated from the flow d and rides on the flow c. , Rolls over the downward slope, reaches the flow path 24, and then falls onto the upper surface of the filter layer to be collected. The air used together with the wash water rises in the flow path 24, floats on the water surface W, and is discharged to the outside from the air vent 10 '.

【0017】の工程は洗浄水を60〜100m/時の
流速で、3〜10分間供給して濾層中を上向流させ、濾
材に付着したSSを剥離すると共に、剥離したSSを管
20に排出し、同時に多層濾過装置の比重が異なる複数
の濾材層の境界面で混合した濾材を分級する。洗浄水の
流速はの工程よりも早いので、分離傾斜体上に巻き上
げられる濾材の量は多くなるが、この場合も第1バッフ
ルの上端を越えてトラフ19に向かう流れaは僅かで、
流れの大部分bは第1,第2バッフルの間を下降し、第
1バッフルの下を潜って流路24に向かう流れcと、第
2バッフルの下を潜って上昇し、トラフに向かう流れd
が生じるので、分離傾斜体上に巻き上げられた濾材は第
1,第2バッフルを下降する際に重力で下向き傾斜部上
に落ちて流れdとは分離し、流れcに乗って下向き傾斜
上を転がって流路24に達し、流路から濾層の上面に落
下して回収される。
In the step (1), washing water is supplied at a flow rate of 60 to 100 m / hour for 3 to 10 minutes to flow upward in the filter layer to remove the SS attached to the filter medium, and the removed SS to the pipe 20. At the same time, the mixed filter medium is classified at the boundary surface of a plurality of filter medium layers having different specific gravities of the multilayer filtration device. Since the flow rate of the washing water is faster than that of the step, the amount of the filter medium wound up on the separation slant increases, but in this case also, the flow a toward the trough 19 beyond the upper end of the first baffle is small,
Most of the flow b descends between the first and second baffles and flows under the first baffle toward the flow path 24, and flows under the second baffle up to the trough. d
Therefore, the filter medium wound up on the separating slant falls down on the downward slant part by gravity when descending the first and second baffles and is separated from the flow d, and rides on the flow c and descends on the downward slant. It rolls down to reach the channel 24, falls from the channel onto the upper surface of the filter layer, and is collected.

【0018】そして、,の工程中、第1,第2バッ
フルの間で水面Wに浮上した油分は、第2バッフル27
の上端を越えてトラフ19に向かう僅かな流れに乗って
トラフに溢入し、管20に排出される。従って、油分の
蓄積は生ぜず、濾材の汚染は起こる余地がない。
During the steps (1) and (2), the oil content floating on the water surface W between the first and second baffles is removed by the second baffle 27.
A slight flow of water is passed over the upper end of the trough 19 toward the trough 19, overflows into the trough, and is discharged to the pipe 20. Therefore, oil does not accumulate, and there is no room for contamination of the filter medium.

【0019】このように上端が水面Wと同レベルの第2
バッフルは流路24を上昇してトラフに向かう比較的に
勢いの強い流れを緩和し、且つ濾材がトラフに流入する
のを阻止する役目と、上端を越える僅かな流れを生じさ
せ、水面に浮上した油分をトラフに行かせる役目と、S
Sなどを下端の下を潜らせ、分離傾斜体の下向き傾斜部
に沿い上昇させてトラフに行かせる役目を有する。又、
上端と下端が水面下にある第1バッフルは、第2バッフ
ルによって緩和された流れを、第2バッフルと協同して
下向きにし、流れの中に含まれている濾材を分離傾斜体
の下向きに傾斜部上に落下させると共に、油分を浮上さ
せる役目と、その下端の下を潜り、下向き傾斜部に沿っ
て下降し、流路24に向かう流れを生じさせ、濾材を回
収する役目とを有する。これによりSS、及び油分の排
出と、濾材の回収が効果的に行われる。
In this way, the second end whose upper end is at the same level as the water surface W
The baffle lifts the flow path 24 to mitigate the relatively strong flow towards the trough and prevents the filter media from flowing into the trough, and causes a slight flow above the upper end to float above the water surface. The role of sending the oil that has been made to the trough, and S
It has the role of making S or the like go under the lower end and ascending along the downwardly inclined portion of the separation inclined body to go to the trough. or,
The first baffle, whose upper and lower ends are below the surface of water, makes the flow moderated by the second baffle downward in cooperation with the second baffle and tilts the filter medium contained in the flow downward of the separating slant. It has the role of causing the oil content to float while falling on the section, and the role of diving under the lower end of the section, descending along the downward slope, causing a flow toward the flow path 24, and collecting the filter medium. This effectively discharges SS and oil, and collects the filter medium.

【0020】図示の実施例では、濾層12に比重が大小
に異なる複数の濾材層を、比重の小さいもの程、上にし
て積層した多層濾層を使用したが、これに限らず濾層は
一種の濾材で構成したものでもよい。又、トラフ19に
原水を供給する管20は濾過塔の底を貫通し、塔内の中
心に沿って立ち、上端部をトラフの底を貫通したものを
使用したが、濾過塔の側壁、第1バッフル、第2バッフ
ルを貫通してトラフの中心部の側面に開口するものでも
よい。又、管20は原水供給と、洗浄排水の排出を兼ね
るものとしたが、トラフ19に連通した排出管21を設
け、原水供給用の管20と、洗浄排水排出用の排出管2
1とを独立して設けてもよい。
In the illustrated embodiment, a plurality of filter medium layers having different specific gravities are used as the filter layer 12, and a multilayer filter layer having a smaller specific gravity is laminated on top, but the filter layer is not limited to this. It may be composed of a kind of filter medium. A pipe 20 for supplying raw water to the trough 19 penetrates the bottom of the filtration tower, stands along the center of the tower, and has an upper end penetrating the bottom of the trough. It may be one that passes through the first baffle and the second baffle and opens on the side surface of the central portion of the trough. Further, although the pipe 20 is used to both supply the raw water and discharge the cleaning waste water, the discharge pipe 21 communicating with the trough 19 is provided, and the pipe 20 for supplying the raw water and the discharge pipe 2 for discharging the cleaning waste water are provided.
1 may be provided independently.

【0021】[0021]

【発明の効果】以上で明らかなように、本発明によれ
ば、濾過塔内の濾層の上方の空間内に、原水の供給管
と、洗浄排水の排出管とが接続し、原水を溢出すると共
に、洗浄排水が溢入して塔内の水面を上面で規制するト
ラフと、上記トラフの下に位置し、上面に下向き傾斜部
を有し、該下向き傾斜部の下端が上下方向の流路を形成
する分離傾斜体と、この分離傾斜体の下向き傾斜部の上
方に下端を離して立設された第1,第2の2つのバッフ
ルとを設け、第1バッフルは上記流路の近くに、第2バ
ッフルは第1バッフルからトラフの方に離して立設し、
且つ第1バッフルの上端はトラフが規制する塔内の水面
下に、第2バッフルの上端はトラフの上面が規制する塔
内の水面と同じレベルに位置させたことにより、1日、
2回程度の頻度で、逆洗を行って濾層を構成する濾材を
効果的に洗浄することができ、マッドボールが形成され
ないと共に、逆洗時に洗浄排水と一緒に濾材が排出され
るのを防止でき、それでいて油分は排出でき、油分の蓄
積による濾材の汚染は生じる余地がない。実験の結果で
は濾材の排出量は年間300日稼働したとして充填量の
5%以下に抑えられることが判明している。
As is apparent from the above, according to the present invention, the raw water supply pipe and the cleaning wastewater discharge pipe are connected to the space above the filter bed in the filtration tower to overflow the raw water. In addition, the washing drainage overflows and the trough that controls the water surface in the tower by the upper surface and the trough located below the trough and on the upper surface have a downward slope, and the lower end of the downward slope is the vertical flow. A separation slant forming a passage and two baffles, a first and a second baffle which are erected with their lower ends separated, are provided above the downward slant portion of this separation slant, and the first baffle is near the flow path. In addition, the second baffle is erected separately from the first baffle toward the trough,
Moreover, the upper end of the first baffle is located below the water surface in the tower regulated by the trough, and the upper end of the second baffle is located at the same level as the water surface in the tower regulated by the upper surface of the trough.
The filter material constituting the filter layer can be effectively washed by performing backwashing at a frequency of about twice, so that the mud balls are not formed and the filter material is discharged together with the cleaning drainage during the backwashing. It can be prevented, yet the oil can be discharged, and there is no room for contamination of the filter medium due to the accumulation of oil. From the results of the experiment, it has been found that the discharge amount of the filter medium can be suppressed to 5% or less of the filling amount, assuming that the filter medium has been operated for 300 days a year.

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

【図1】本発明の濾過装置の第1実施例の縦断面図であ
る。
FIG. 1 is a vertical sectional view of a first embodiment of a filtration device of the present invention.

【図2】図2のII−II線での断面図である。FIG. 2 is a sectional view taken along line II-II in FIG.

【図3】本発明の濾過装置の他の一実施例の縦断面図で
ある。
FIG. 3 is a vertical cross-sectional view of another embodiment of the filtration device of the present invention.

【図4】図3のIV−IV線での断面図である。FIG. 4 is a sectional view taken along line IV-IV in FIG.

【符号の説明】[Explanation of symbols]

10 濾過塔 11 通水支持板 12 濾層 16 給排管 17 圧縮空気の送気管 18 濾過塔内の濾層の上方空間 19 トラフ 19´ トラフの上面 20 管 21 排出管 22 分離傾斜体 23 分離傾斜体の上面の下向き傾斜部 24 上下方向の流路 25 分離傾斜体の下面 26 第1バッフル 27 第2バッフル 28 処理水の排水管 29 洗浄水の供給管 W 濾過塔内の水面 10 Filter Tower 11 Water-passing Support Plate 12 Filter Layer 16 Supply / Discharge Pipe 17 Compressed Air Supply Pipe 18 Upper Space of Filter Layer in Filter Tower 19 Trough 19 'Top of Trough 20 Pipe 21 Discharge Pipe 22 Separation Gradient 23 Separation Gradient Lower sloped part of the upper surface of the body 24 Flow path in the vertical direction 25 Lower surface of the separation slanted body 26 First baffle 27 Second baffle 28 Drain pipe of treated water 29 Supply pipe of wash water W Water level in filtration tower

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 濾過塔内に充填した濾層に原水を下向流
で通水して濾過処理すると共に、空気及び洗浄水を濾層
に上向流で通水し、濾層を展開して洗浄する濾過装置に
おいて、塔内の濾層の上方の空間内に、原水を溢出する
と共に、洗浄排水が溢入して塔内の水面を上面で規制す
るトラフと、 上記トラフの下に位置し、上面に下向き傾斜部を有し、
該下向き傾斜部の下端が上下方向の流路を形成する分離
傾斜体と、 この分離傾斜体の下向き傾斜部の上方に下端を離して立
設された第1,第2の2つのバッフルとを設け、 第1バッフルは上記流路の近くに、第2バッフルは第1
バッフルからトラフの方に離して立設し、且つ第1バッ
フルの上端はトラフが規制する塔内の水面下に、第2バ
ッフルの上端はトラフの上面が規制する塔内の水面と同
じレベルに位置させたことを特徴とする濾過装置。
1. Raw water is passed in a downward flow into a filter layer packed in a filtration tower for filtration treatment, and air and washing water are passed in an upward flow to the filter layer to develop the filter layer. In the filtration device for cleaning by washing, the raw water overflows into the space above the filter layer in the tower, and the trough that controls the water surface inside the tower by the overflow of the washing drainage and the trough located below the trough. Has a downward slope on the upper surface,
A separating slant body whose lower end of the downward slanting portion forms a vertical flow path, and two baffles, a first baffle and a second baffle which are vertically installed above the downward slanting portion of the separating slanting body with their lower ends separated from each other. Provided, the first baffle is near the flow path, the second baffle is the first
Set up separately from the baffle toward the trough, and the upper end of the first baffle is below the water surface in the tower controlled by the trough, and the upper end of the second baffle is at the same level as the water surface in the tower controlled by the upper surface of the trough. A filtration device characterized by being positioned.
JP14688195A 1995-05-23 1995-05-23 Filtration device Expired - Fee Related JP3518060B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP14688195A JP3518060B2 (en) 1995-05-23 1995-05-23 Filtration device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP14688195A JP3518060B2 (en) 1995-05-23 1995-05-23 Filtration device

Publications (2)

Publication Number Publication Date
JPH08318107A true JPH08318107A (en) 1996-12-03
JP3518060B2 JP3518060B2 (en) 2004-04-12

Family

ID=15417690

Family Applications (1)

Application Number Title Priority Date Filing Date
JP14688195A Expired - Fee Related JP3518060B2 (en) 1995-05-23 1995-05-23 Filtration device

Country Status (1)

Country Link
JP (1) JP3518060B2 (en)

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2002001017A (en) * 2000-06-19 2002-01-08 Nippon Shokubai Co Ltd Solid removing device
JP2008272733A (en) * 2007-03-30 2008-11-13 Kurita Water Ind Ltd Filtration apparatus
JP2009125657A (en) * 2007-11-22 2009-06-11 Kurita Water Ind Ltd Filtering apparatus
JP2011136323A (en) * 2009-12-03 2011-07-14 Kazunori Koishi Upward filtration apparatus having feature in lamination method of filter medium
KR20140109365A (en) 2011-12-05 2014-09-15 쿠리타 고교 가부시키가이샤 Packed column backwashing method
CN113769445A (en) * 2021-08-25 2021-12-10 河北中瀚水务有限公司 Intelligent common rapid filter tank system with air flushing and filtering method

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2002001017A (en) * 2000-06-19 2002-01-08 Nippon Shokubai Co Ltd Solid removing device
JP2008272733A (en) * 2007-03-30 2008-11-13 Kurita Water Ind Ltd Filtration apparatus
JP2009125657A (en) * 2007-11-22 2009-06-11 Kurita Water Ind Ltd Filtering apparatus
JP2011136323A (en) * 2009-12-03 2011-07-14 Kazunori Koishi Upward filtration apparatus having feature in lamination method of filter medium
KR20140109365A (en) 2011-12-05 2014-09-15 쿠리타 고교 가부시키가이샤 Packed column backwashing method
CN113769445A (en) * 2021-08-25 2021-12-10 河北中瀚水务有限公司 Intelligent common rapid filter tank system with air flushing and filtering method
CN113769445B (en) * 2021-08-25 2023-01-10 河北中瀚水务有限公司 Intelligent common rapid filter tank system with air flushing and filtering method

Also Published As

Publication number Publication date
JP3518060B2 (en) 2004-04-12

Similar Documents

Publication Publication Date Title
US4743382A (en) Method and apparatus for separating suspended solids from liquids
US4322299A (en) Method of simultaneous air-water wash of multiple-media filters
JP3524447B2 (en) Filtration device
CA1212905A (en) Granular media filter
JP3518060B2 (en) Filtration device
JPS58156313A (en) Filter apparatus
JP2599538B2 (en) Inclined plate type sedimentation tank and method for preventing clogging thereof
JPH0217908A (en) Method for washing solid-liquid separation apparatus
JPH1071305A (en) Moving filter bed type filter
CN111704202B (en) Environment-friendly chemical sewage treatment plant
JP3365183B2 (en) Filtration device and cleaning method thereof
JP4831052B2 (en) Filtration device
JP2003220305A (en) Mobile filter bed-type filter
JP2009125657A (en) Filtering apparatus
JPS5946649B2 (en) Horizontal flow deep filtration device
CN220443257U (en) Filter tank back flush anti-running filter material U-shaped weir plate mechanism
JPH078001Y2 (en) Settling equipment for sludge treatment
JPH0352607A (en) Water treatment device
KR100930827B1 (en) Solid-liquid separator for water treatment
JP2005305304A (en) Apparatus for washing/solid-liquid separation of granular material
JPH09276885A (en) Biological membrane filter apparatus using foldable filter material
JPS588518A (en) Apparatus for separating oil and water
JPH0312323Y2 (en)
JP3105799B2 (en) Solid-liquid separation method and portable solid-liquid separation device
JP3491389B2 (en) Multi-layer filtration device

Legal Events

Date Code Title Description
A61 First payment of annual fees (during grant procedure)

Free format text: JAPANESE INTERMEDIATE CODE: A61

Effective date: 20040119

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20080206

Year of fee payment: 4

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20090206

Year of fee payment: 5

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20090206

Year of fee payment: 5

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20100206

Year of fee payment: 6

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20110206

Year of fee payment: 7

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20110206

Year of fee payment: 7

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20120206

Year of fee payment: 8

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20120206

Year of fee payment: 8

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20130206

Year of fee payment: 9

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20130206

Year of fee payment: 9

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20140206

Year of fee payment: 10

LAPS Cancellation because of no payment of annual fees