JP3859402B2 - Filtration basin washing wastewater treatment method - Google Patents

Filtration basin washing wastewater treatment method Download PDF

Info

Publication number
JP3859402B2
JP3859402B2 JP26786299A JP26786299A JP3859402B2 JP 3859402 B2 JP3859402 B2 JP 3859402B2 JP 26786299 A JP26786299 A JP 26786299A JP 26786299 A JP26786299 A JP 26786299A JP 3859402 B2 JP3859402 B2 JP 3859402B2
Authority
JP
Japan
Prior art keywords
washing
water
filtration
basin
membrane
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 - Fee Related
Application number
JP26786299A
Other languages
Japanese (ja)
Other versions
JP2001087764A (en
Inventor
敏雄 川西
行彦 堤
光昭 布
丈 山本
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.)
Kubota Corp
Original Assignee
Kubota Corp
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 Kubota Corp filed Critical Kubota Corp
Priority to JP26786299A priority Critical patent/JP3859402B2/en
Publication of JP2001087764A publication Critical patent/JP2001087764A/en
Application granted granted Critical
Publication of JP3859402B2 publication Critical patent/JP3859402B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Images

Landscapes

  • Separation Using Semi-Permeable Membranes (AREA)

Description

【0001】
【発明の属する技術分野】
本発明は、浄水処理施設におけるろ過池洗浄排水の処理方法に関するものである。
【0002】
【従来の技術】
従来、浄水処理施設としては、例えば図4に示すものがある。図4において、原水1は着水井2に受水した後に凝集沈殿池3に導き、凝集剤を添加して原水中の懸濁成分を凝集沈殿させる。凝集沈殿池3の上澄水は砂ろ過池4へ導き、ろ過した処理水を消毒槽5に導き、塩素消毒した後に水道水として供給する。
【0003】
砂ろ過池4の逆洗時には、処理水を洗浄水として逆洗を行ない、洗浄排水は排水池6を着水井2に返送する。洗浄水は砂ろ過池4が複数ある場合は、他の砂ろ過池4の処理水を利用し、あるいは、砂ろ過池4の処理水を別途に設けた洗浄水槽に洗浄水として貯留したものを利用する。排水池6は汚泥の沈降堆積を防ぐために攪拌機による攪拌を常時に行なっている場合が多い。
【0004】
【発明が解決しようとする課題】
上記した構成において、排水池6に貯留した洗浄排水を着水井2に返送する場合に、返送水は高濁度でマンガン等の濃度も高いので、一時的に浄水処理系統に悪影響を及ぼす恐れがある。さらに、砂ろ過池4で除去したクリプトスポリジウム等の病原性微生物も返送水とともに着水井に返送されるので、これらの病原性微生物が浄水処理系統内で循環し、濃縮される恐れもある。
【0005】
一方、洗浄排水を膜ろ過した後に、膜ろ過水を水道水として利用する場合には、膜の破損などがあった時に、高濁度の洗浄排水が水道水中に混入する恐れがある。この膜ろ過水を着水井2に返送する場合には、一時的に原水濁度が低下し、凝集沈殿池3における凝集剤の最適注入率に影響を与える恐れがある。さらに、水道水として利用できる水質となった膜ろ過水を、着水井へ返送して原水と混合することは浄水処理系統として無駄が多くなる。
【0006】
本発明は上記した課題を解決するものであり、ろ過池の洗浄排水を膜ろ過し、この膜ろ過水をろ過池の洗浄水として再利用する浄水処理施設におけるろ過池洗浄排水の処理方法を提供することを目的とする。
【0007】
【課題を解決するための手段】
上記課題を解決するために、請求項1に係る本発明は、浄水処理施設におけるろ過池の洗浄排水を排水池に一旦貯留し、排水池の洗浄排水を膜ろ過装置でろ過し、膜ろ過水を洗浄水として洗浄水槽に貯留し、洗浄水槽の洗浄水をろ過池へ供給してろ過池の洗浄を行ない、洗浄排水を排水池に戻して循環再利用するものである。
【0008】
上記した構成により、洗浄水系統が浄水処理系統と分かれて存在するので、洗浄排水中の病原性微生物は、膜ろ過によって完全に浄水処理系統から分離され、浄水処理系統に戻ることがなく、ろ過池の洗浄は1〜2日に1回行なわれるため、膜が破損した場合でも一時的に洗浄を停止し、その間に処置をすることで水道水中への漏出を防ぐことができる。洗浄水が膜ろ過水であるために、通常の砂ろ過した処理水を使用する場合よりもさらに低濁度の洗浄水となり、洗浄の効果が高くろ過池に残留する濁質が少なくなるので、洗浄直後における浄水処理での濁度漏出を減らすことができる。
【0009】
ろ過池の洗浄は1〜2日に1回程度行ない、洗浄時には多量の洗浄排水が発生するので、洗浄排水を排水池に一旦貯留し、洗浄排水を膜ろ過装置において所定の定流量で処理することで、洗浄排水から再生する洗浄水を、次回の洗浄に必要な量だけ洗浄水槽に確保することができ、洗浄水の循環再利用を行なえる。
請求項2に係る本発明は、膜ろ過装置に駆動圧力を与える膜ろ過ポンプの吐出圧を利用して膜ろ過水を洗浄水として洗浄水槽へ揚水し、洗浄水槽の洗浄水を洗浄水槽の水頭圧でろ過池へ供給してろ過池の洗浄を行ない、洗浄排水を排水池に戻して循環再利用するものである。
【0010】
上記した構成により、ろ過池へ洗浄水を供給する駆動力として洗浄水槽の水頭圧を利用し、洗浄水槽へろ過水を供給する駆動力として膜ろ過ポンプの吐出圧を利用することができ、エネルギーを効果的に利用できる。
請求項3に係る本発明は、膜ろ過装置が、排水池に浸漬した外圧型膜モジュールと、外圧型膜モジュールに駆動圧力として負圧を作用させる膜ろ過ポンプと、外圧型膜モジュールの下方に配置した散気装置と、散気装置に接続したブロアとからなるものである。
【0011】
上記した構成により、既存の排水池に外圧型膜モジュールを浸漬することで、膜ろ過装置を構成することができ、膜ろ過処理を行なうための敷地を別途に必要としない。また、散気装置から散気する空気によって生起する気液混合の上向流が外圧型膜モジュールの膜面に掃流として作用し、この膜面洗浄のための掃流が気泡旋回流となって排水池を攪拌するので、排水池の攪拌機が不要となる。
【0012】
【発明の実施の形態】
以下、本発明の実施の形態を図面に基づいて説明する。図1において、原水11を浄水処理する浄水処理系統では、原水1を着水井12に受水した後に凝集沈殿池13に導き、凝集沈殿池13において凝集剤を添加して原水中の懸濁成分を凝集沈殿させる。
【0013】
その後、凝集沈殿池13において分離した上澄水を砂ろ過池14へ導いて砂ろ過し、この砂ろ過した処理水を消毒槽15に導き、塩素消毒した後に水道水として供給する。
砂ろ過池14の洗浄は1〜2日に1回程度行なう。洗浄水系統では、砂ろ過池14の逆洗時に多量に発生する洗浄排水を排水池16に一旦貯留し、膜ろ過装置17に膜ろ過ポンプ18で駆動圧力を与え、排水池16の洗浄排水を所定の定流量で吸引ろ過して処理する。膜ろ過装置17に駆動圧力を与える膜ろ過ポンプ18を膜ろ過装置17の前に設けて排水池16の洗浄排水を加圧ろ過して処理することもできる。
【0014】
この膜ろ過水を洗浄水として洗浄水槽19に貯留し、洗浄水槽19の洗浄水を洗浄ポンプ20で、あるいは洗浄ポンプ20を設けずに洗浄水槽の水頭差で砂ろ過池14へ供給して砂ろ過池14の洗浄を行なう。このとき、必要に応じて洗浄水に洗浄用の薬品を添加する。洗浄排水は排水池16に戻し、洗浄排水を洗浄水に再生して、次回の洗浄に必要な量だけ洗浄水槽19に確保して洗浄水の循環再利用を行なう。
【0015】
このように、洗浄水系統が浄水処理系統と分かれて存在することにより、砂ろ過池14の洗浄排水中に含まれ病原性微生物は、膜ろ過によって完全に浄水処理系統から分離されるので、浄水処理系統に戻ることがなくなり、膜が破損した場合でも洗浄を停止している間に処置することができ、水道水中への漏出はない。
また、砂ろ過池14へ供給する洗浄水が膜ろ過水であるために、砂ろ過した処理水を洗浄水として使用する場合よりも、さらに低濁度の洗浄水となり、洗浄の効果が高くなって砂ろ過池14に残留する濁質が少なくなるので、洗浄直後における浄水処理系統での濁度漏出を減らすことができる。
【0016】
図2は本発明の他の実施の形態を示すものである。図2において、洗浄水槽19は砂ろ過池14より高所、もしくはその下限水位が砂ろ過池14より高くなるように設けており、膜ろ過装置17の膜ろ過水は、膜ろ過ポンプ18の吐出圧を利用して洗浄水槽19へ揚水する。
この洗浄水槽19の膜ろ過水からなる洗浄水を、洗浄水槽19の水頭圧を利用して砂ろ過池14へ供給することで、砂ろ過池14の洗浄を行なう。洗浄排水は排水池16に戻して循環再利用する。
【0017】
この構成により、砂ろ過池14へ洗浄水を供給する駆動力として洗浄水槽19の水頭圧を利用し、洗浄水槽19へ膜ろ過水を供給する駆動力として膜ろ過ポンプ18の吐出圧を利用することができ、エネルギーを効果的に利用できる。
上記した何れの実施の形態においても、膜ろ過装置17としては種々の形式のものを利用することができるが、好ましい構成としては、図3に示すように、膜ろ過装置17は、排水池16に浸漬した外圧型膜モジュール21と、外圧型膜モジュール21に駆動圧力として負圧を作用させる膜ろ過ポンプ18と、外圧型膜モジュール21の下方に配置した散気装置22と、散気装置22に接続したブロア23を備えたものを使用する。外圧型膜モジュール21は0.1μm程度以下の孔径を有するセラミック膜または有機膜からなる。
【0018】
この構成では、既存の排水池16に外圧型膜モジュールを浸漬することで、膜ろ過装置17を構成することができ、膜ろ過処理を行なうための敷地を別途に必要としない。また、散気装置22から散気する空気によって生起する気液混合の上向流が外圧型膜モジュール21の膜面に掃流として作用し、この膜面洗浄のための掃流が気泡旋回流となって排水池16を攪拌するので、排水池16の攪拌機が不要となる。
【0019】
【発明の効果】
以上のように、本発明によれば、洗浄水系統を浄水処理系統と分けて形成し、洗浄排水を膜ろ過することにより、洗浄排水中の病原性微生物を完全に浄水処理系統から分離することができ、洗浄水に膜ろ過水を使用することで、洗浄の効果を高めて洗浄直後における浄水処理での濁度漏出を抑制できる。排水池に一旦貯留した多量の洗浄排水を、膜ろ過装置により所定の定流量で処理して洗浄水に再生し、次回の洗浄に必要な量だけ洗浄水槽に確保することで、洗浄水の循環再利用を行なうことができる。
【0020】
また、洗浄水槽の水頭圧を利用して洗浄水をろ過池へ供給し、膜ろ過ポンプの吐出圧を利用して洗浄水槽へろ過水を供給することで、エネルギーを効果的に利用できる。槽内に浸漬する外圧型膜モジュールを使用することで、既存の排水池において膜ろ過装置を構成することができ、膜ろ過処理を行なうための別途の敷地が不要となり、外圧型膜モジュールの膜面に作用する掃流が気泡旋回流となって排水池を攪拌するので、排水池の攪拌機が不要となる。
【図面の簡単な説明】
【図1】本発明の実施の形態におけるろ過池洗浄排水の処理方法を示すフローシートである。
【図2】本発明の他の実施の形態におけるろ過池洗浄排水の処理方法を示すフローシートである。
【図3】膜ろ過装置の構成を示す模式図である。
【図4】従来の浄水処理を示すフローシートである。
【符号の説明】
11 原水
12 着水井
13 凝集沈殿池
14 砂ろ過池
15 消毒槽
16 排水池
17 膜ろ過装置
18 膜ろ過ポンプ
19 洗浄水槽
20 洗浄ポンプ
[0001]
BACKGROUND OF THE INVENTION
The present invention relates to a method for treating filtration basin washing wastewater in a water purification treatment facility.
[0002]
[Prior art]
Conventionally, as a water purification treatment facility, for example, there is one shown in FIG. In FIG. 4, raw water 1 is received by a landing well 2 and then led to a coagulating sedimentation basin 3, and a coagulant is added to coagulate and precipitate suspended components in the raw water. The supernatant water of the coagulation sedimentation basin 3 is guided to the sand filtration basin 4, and the filtered treated water is guided to the sterilization tank 5 and supplied as tap water after chlorination.
[0003]
At the time of backwashing the sand filtration basin 4, the backwashing is performed using the treated water as washing water, and the washing drainage returns the drainage basin 6 to the landing well 2. When there are a plurality of sand filtration ponds 4, use wash water from other sand filter ponds 4 or store the wash water from the sand filter pond 4 in a wash water tank provided separately. Use. In many cases, the drainage basin 6 is constantly stirred by a stirrer in order to prevent sedimentation of sludge.
[0004]
[Problems to be solved by the invention]
In the above-described configuration, when the washing wastewater stored in the drainage basin 6 is returned to the landing well 2, the return water has high turbidity and a high concentration of manganese, etc., which may temporarily adversely affect the water purification system. is there. Furthermore, since pathogenic microorganisms such as Cryptosporidium removed in the sand filtration pond 4 are also returned to the receiving well together with the return water, these pathogenic microorganisms may circulate and concentrate in the water purification system.
[0005]
On the other hand, when membrane filtration water is used as tap water after membrane filtration of washing wastewater, there is a possibility that washing water with high turbidity may be mixed into tap water when there is a membrane breakage or the like. When this membrane filtrate is returned to the landing well 2, the raw water turbidity is temporarily lowered, which may affect the optimum injection rate of the coagulant in the coagulation sedimentation basin 3. Furthermore, it is wasteful as a water purification treatment system to return the membrane filtered water having a quality which can be used as tap water to the landing well and mix it with raw water.
[0006]
The present invention solves the above-mentioned problems, and provides a method for treating the filtration basin washing wastewater in a water purification treatment facility that filters the washing effluent of the filtration basin and reuses this membrane filtrate as the washing water of the filtration pond. The purpose is to do.
[0007]
[Means for Solving the Problems]
In order to solve the above-mentioned problem, the present invention according to claim 1 is to temporarily store the washing drainage of the filtration pond in the water treatment facility in the drainage basin, and filter the washing drainage of the drainage pond with a membrane filtration device. Is stored in a wash water tank as wash water, the wash water of the wash water tank is supplied to the filter basin to wash the filter basin, and the wash wastewater is returned to the drain basin for circulation reuse.
[0008]
With the configuration described above, since the washing water system is separated from the water purification system, pathogenic microorganisms in the washing wastewater are completely separated from the water purification system by membrane filtration, and are not returned to the water purification system. Since the pond is washed once every 1 to 2 days, even if the membrane is damaged, the washing is temporarily stopped, and leakage into the tap water can be prevented by taking measures during that time. Since the washing water is membrane filtration water, it becomes washing water with lower turbidity than when using normal sand-filtered treated water, and since the washing effect is high and the turbidity remaining in the filtration pond is less, Turbidity leakage in the water purification process immediately after washing can be reduced.
[0009]
The filtration basin is washed once or twice a day, and since a large amount of washing wastewater is generated during washing, the washing wastewater is temporarily stored in the drainage basin and the washing wastewater is processed at a predetermined constant flow rate in the membrane filtration device. Thus, the cleaning water regenerated from the cleaning wastewater can be secured in the cleaning water tank in an amount necessary for the next cleaning, and the cleaning water can be recycled and reused.
The present invention according to claim 2 uses the discharge pressure of a membrane filtration pump that applies a driving pressure to the membrane filtration device to pump the membrane filtrate into the washing tank as washing water, and uses the washing water in the washing tank as the head of the washing tank. The pressure is supplied to the filtration basin by pressure, and the filtration basin is washed. The washing wastewater is returned to the drainage basin and recycled.
[0010]
With the configuration described above, the head pressure of the washing water tank can be used as the driving force for supplying cleaning water to the filtration pond, and the discharge pressure of the membrane filtration pump can be used as the driving force for supplying filtered water to the washing water tank. Can be used effectively.
According to a third aspect of the present invention, the membrane filtration apparatus includes an external pressure membrane module immersed in a drainage basin, a membrane filtration pump that applies a negative pressure as a driving pressure to the external pressure membrane module, and a lower portion of the external pressure membrane module. The air diffuser is arranged and a blower connected to the air diffuser.
[0011]
With the above configuration, a membrane filtration device can be configured by immersing an external pressure membrane module in an existing drainage pond, and a separate site for performing membrane filtration is not required. Also, the upward flow of gas-liquid mixing caused by the air diffused from the diffuser acts as a sweep on the membrane surface of the external pressure membrane module, and the sweep for this membrane surface cleaning becomes a bubble swirl flow. Since the drainage pond is agitated, there is no need for a drainage agitator.
[0012]
DETAILED DESCRIPTION OF THE INVENTION
Hereinafter, embodiments of the present invention will be described with reference to the drawings. In FIG. 1, in a water purification system that purifies raw water 11, raw water 1 is received by a landing well 12 and then guided to a coagulation sedimentation basin 13. A coagulant is added to the coagulation sedimentation basin 13 and suspended components in the raw water. Flocculate and precipitate.
[0013]
Thereafter, the supernatant water separated in the coagulation sedimentation basin 13 is guided to the sand filtration basin 14 and subjected to sand filtration, and the treated water subjected to the sand filtration is guided to the disinfection tank 15 and supplied as tap water after chlorination.
The sand filtration basin 14 is washed once or twice a day. In the washing water system, a large amount of washing wastewater generated during backwashing of the sand filtration basin 14 is temporarily stored in the drainage basin 16, and a driving pressure is applied to the membrane filtration device 17 by the membrane filtration pump 18. Process by suction filtration at a predetermined constant flow rate. A membrane filtration pump 18 that applies a driving pressure to the membrane filtration device 17 may be provided in front of the membrane filtration device 17 so that the washing wastewater in the drainage basin 16 is pressure filtered and processed.
[0014]
This membrane filtered water is stored in the washing water tank 19 as washing water, and the washing water in the washing water tank 19 is supplied to the sand filtration pond 14 by the washing pump 20 or by the head difference of the washing water tank without providing the washing pump 20. The filtration basin 14 is washed. At this time, if necessary, a cleaning chemical is added to the cleaning water. The washing wastewater is returned to the drainage basin 16 and the washing wastewater is regenerated into washing water, and only the amount necessary for the next washing is secured in the washing water tank 19 to recycle and reuse the washing water.
[0015]
Thus, since the washing water system is separated from the water purification system, the pathogenic microorganisms contained in the washing drainage of the sand filtration pond 14 are completely separated from the water purification system by membrane filtration. Even if the membrane is broken, it can be treated while washing is stopped, and there is no leakage into tap water.
Further, since the washing water supplied to the sand filtration pond 14 is membrane filtration water, the washing water has a lower turbidity than when the sand-filtered treated water is used as washing water, and the washing effect is enhanced. Therefore, since the turbidity remaining in the sand filtration pond 14 is reduced, turbidity leakage in the water purification system immediately after washing can be reduced.
[0016]
FIG. 2 shows another embodiment of the present invention. In FIG. 2, the washing water tank 19 is provided higher than the sand filtration basin 14 or its lower limit water level is higher than the sand filtration basin 14, and the membrane filtration water of the membrane filtration device 17 is discharged from the membrane filtration pump 18. The water is pumped to the washing water tank 19 using the pressure.
The sand filtration basin 14 is washed by supplying the wash water composed of the membrane filtration water of the wash water tank 19 to the sand filtration basin 14 using the head pressure of the washing water tank 19. The washing wastewater is returned to the drainage basin 16 and recycled.
[0017]
With this configuration, the head pressure of the washing water tank 19 is used as the driving force for supplying the washing water to the sand filtration pond 14, and the discharge pressure of the membrane filtration pump 18 is used as the driving force for supplying the membrane filtration water to the washing water tank 19. And can use energy effectively.
In any of the above-described embodiments, various types of membrane filtration devices 17 can be used. However, as a preferable configuration, as shown in FIG. An external pressure membrane module 21 immersed in the membrane, a membrane filtration pump 18 that applies a negative pressure to the external pressure membrane module 21 as a driving pressure, an air diffuser 22 disposed below the external pressure membrane module 21, and an air diffuser 22 The one provided with the blower 23 connected to is used. The external pressure membrane module 21 is made of a ceramic membrane or an organic membrane having a pore diameter of about 0.1 μm or less.
[0018]
In this structure, the membrane filtration apparatus 17 can be comprised by immersing an external pressure type membrane module in the existing drainage pond 16, and the site for performing a membrane filtration process is not required separately. Further, the upward flow of the gas-liquid mixture caused by the air diffused from the diffuser 22 acts as a sweep on the membrane surface of the external pressure membrane module 21, and the sweep for cleaning the membrane surface is a bubble swirl flow. Since the drainage basin 16 is stirred, the stirrer for the drainage basin 16 becomes unnecessary.
[0019]
【The invention's effect】
As described above, according to the present invention, the washing water system is formed separately from the water purification system, and the pathogenic microorganisms in the washing waste water are completely separated from the water purification system by membrane filtration of the washing water. By using membrane filtered water as washing water, the effect of washing can be enhanced and leakage of turbidity in water purification treatment immediately after washing can be suppressed. A large amount of washing wastewater once stored in the drainage basin is treated with a membrane filtration device at a predetermined constant flow rate and regenerated into washing water, and only the amount necessary for the next washing is secured in the washing water tank, thereby circulating the washing water. Can be reused.
[0020]
Moreover, energy can be used effectively by supplying wash water to the filtration basin using the head pressure of the wash water tank and supplying filtered water to the wash water tank using the discharge pressure of the membrane filtration pump. By using an external pressure membrane module immersed in the tank, it is possible to configure a membrane filtration device in an existing drainage pond, eliminating the need for a separate site for membrane filtration treatment, and the membrane of the external pressure membrane module Since the sweep acting on the surface becomes a bubble swirl flow and stirs the drainage basin, a stirrer for the drainage basin becomes unnecessary.
[Brief description of the drawings]
BRIEF DESCRIPTION OF DRAWINGS FIG. 1 is a flow sheet showing a method for treating filtration basin washing wastewater in an embodiment of the present invention.
FIG. 2 is a flow sheet showing a method for treating filtration basin washing wastewater according to another embodiment of the present invention.
FIG. 3 is a schematic diagram showing the configuration of a membrane filtration device.
FIG. 4 is a flow sheet showing a conventional water purification treatment.
[Explanation of symbols]
DESCRIPTION OF SYMBOLS 11 Raw water 12 Landing well 13 Coagulation sedimentation tank 14 Sand filtration tank 15 Disinfection tank 16 Drainage tank 17 Membrane filtration apparatus 18 Membrane filtration pump 19 Washing water tank 20 Washing pump

Claims (3)

浄水処理施設におけるろ過池の洗浄排水を排水池に一旦貯留し、排水池の洗浄排水を膜ろ過装置でろ過し、膜ろ過水を洗浄水として洗浄水槽に貯留し、洗浄水槽の洗浄水をろ過池へ供給してろ過池の洗浄を行ない、洗浄排水を排水池に戻して循環再利用することを特徴とするろ過池洗浄排水の処理方法。The washing drainage of the filtration pond in the water treatment facility is temporarily stored in the drainage basin, the washing drainage of the drainage pond is filtered with a membrane filtration device, the membrane filtrate is stored in the washing tank as washing water, and the washing water in the washing tank is filtered. A method for treating filtration basin wastewater, which is supplied to a pond to wash the filtration basin, and the washing wastewater is returned to the drainage basin for recycling. 膜ろ過装置に駆動圧力を与える膜ろ過ポンプの吐出圧を利用して膜ろ過水を洗浄水として洗浄水槽へ揚水し、洗浄水槽の洗浄水を洗浄水槽の水頭圧でろ過池へ供給してろ過池の洗浄を行ない、洗浄排水を排水池に戻して循環再利用することを特徴とする請求項1に記載のろ過池洗浄排水の処理方法。Using the discharge pressure of the membrane filtration pump that gives the driving pressure to the membrane filtration device, the membrane filtration water is pumped up as washing water to the washing tank, and the washing water from the washing tank is supplied to the filtration basin at the head pressure of the washing tank and filtered. 2. The method for treating filtration basin washing wastewater according to claim 1, wherein the pond is washed, and the washing wastewater is returned to the drainage pond and recycled. 膜ろ過装置は、排水池に浸漬した外圧型膜モジュールと、外圧型膜モジュールに駆動圧力として負圧を作用させる膜ろ過ポンプと、外圧型膜モジュールの下方に配置した散気装置と、散気装置に接続したブロアとからなることを特徴とする請求項1又は2に記載のろ過池洗浄排水の処理方法。The membrane filtration apparatus includes an external pressure membrane module immersed in a drainage basin, a membrane filtration pump that applies a negative pressure to the external pressure membrane module as a driving pressure, an air diffuser disposed below the external pressure membrane module, The processing method of the filtration basin washing waste water of Claim 1 or 2 which consists of a blower connected to the apparatus.
JP26786299A 1999-09-22 1999-09-22 Filtration basin washing wastewater treatment method Expired - Fee Related JP3859402B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP26786299A JP3859402B2 (en) 1999-09-22 1999-09-22 Filtration basin washing wastewater treatment method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP26786299A JP3859402B2 (en) 1999-09-22 1999-09-22 Filtration basin washing wastewater treatment method

Publications (2)

Publication Number Publication Date
JP2001087764A JP2001087764A (en) 2001-04-03
JP3859402B2 true JP3859402B2 (en) 2006-12-20

Family

ID=17450680

Family Applications (1)

Application Number Title Priority Date Filing Date
JP26786299A Expired - Fee Related JP3859402B2 (en) 1999-09-22 1999-09-22 Filtration basin washing wastewater treatment method

Country Status (1)

Country Link
JP (1) JP3859402B2 (en)

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP5143002B2 (en) 2006-08-01 2013-02-13 メタウォーター株式会社 Wastewater reuse method
KR101431886B1 (en) 2009-03-27 2014-09-22 메타워터 가부시키가이샤 Process for producing regenerated water and system for producing regenerated water
JP2015013222A (en) * 2013-07-03 2015-01-22 株式会社竹村製作所 Water treatment equipment using filter sand
JP6276525B2 (en) * 2013-07-03 2018-02-07 株式会社竹村製作所 Water treatment equipment using filtration sand

Also Published As

Publication number Publication date
JP2001087764A (en) 2001-04-03

Similar Documents

Publication Publication Date Title
US6426005B1 (en) Sequential descending bed filters with reject/washwater containing impurities being fed to a separate unit for elimination of impurities
JP4920990B2 (en) Separation membrane cleaning method
EP2072470B1 (en) Method of reutilizing wastewater
KR101858028B1 (en) Rapid complex water treatment system
JPH10109095A (en) Water purifying treatment device
JP2007289847A (en) Raw tap water purification method and its apparatus
JP2002177990A (en) Water cleaning method and water cleaning plant
JP3859402B2 (en) Filtration basin washing wastewater treatment method
JP2001276892A (en) Drain treatment device
JPH10109091A (en) Treatment of water
JP2002177956A (en) Water cleaning method and water cleaning plant
JPH09253456A (en) Treatment of organic drain
JP4373871B2 (en) Activated sludge treatment equipment
KR101689151B1 (en) Apparatus for treating wastewater and bidirectional filter thereof
KR100348417B1 (en) Apparatus and method of submerged membrane wastewater treatment with stabilized sludge
JP3281161B2 (en) Water purification equipment
JPH04305287A (en) Water treating equipment
JP4019277B2 (en) Method and apparatus for treating organic wastewater generated from fishing ports and fish markets
JP2003033764A (en) Method and apparatus for washing filtration body by using ozone
KR100313222B1 (en) Combined purification apparatus and method using submerged membrane process for use in advanced treatment
JP3874635B2 (en) Sewage treatment method and treatment apparatus
JP3807945B2 (en) Method and apparatus for treating organic wastewater
KR20150081920A (en) advanced treatment device of wastewater and advanced treatment method of wastewater
JP4104806B2 (en) Solid-liquid separation method and apparatus for organic wastewater treatment
KR100400358B1 (en) Intermittent operating phase submerged membrane bioreactor waste water treatment system

Legal Events

Date Code Title Description
A977 Report on retrieval

Free format text: JAPANESE INTERMEDIATE CODE: A971007

Effective date: 20041020

TRDD Decision of grant or rejection written
A01 Written decision to grant a patent or to grant a registration (utility model)

Free format text: JAPANESE INTERMEDIATE CODE: A01

Effective date: 20060822

A61 First payment of annual fees (during grant procedure)

Free format text: JAPANESE INTERMEDIATE CODE: A61

Effective date: 20060919

R150 Certificate of patent or registration of utility model

Free format text: JAPANESE INTERMEDIATE CODE: R150

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

Free format text: PAYMENT UNTIL: 20100929

Year of fee payment: 4

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

Free format text: PAYMENT UNTIL: 20100929

Year of fee payment: 4

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

Free format text: PAYMENT UNTIL: 20110929

Year of fee payment: 5

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

Free format text: PAYMENT UNTIL: 20120929

Year of fee payment: 6

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

Free format text: PAYMENT UNTIL: 20130929

Year of fee payment: 7

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

Free format text: PAYMENT UNTIL: 20140929

Year of fee payment: 8

LAPS Cancellation because of no payment of annual fees