JP2003251109A - Moving bed type sand filter, moving bed type biological membrane sand filtering method and system therefor - Google Patents

Moving bed type sand filter, moving bed type biological membrane sand filtering method and system therefor

Info

Publication number
JP2003251109A
JP2003251109A JP2002053079A JP2002053079A JP2003251109A JP 2003251109 A JP2003251109 A JP 2003251109A JP 2002053079 A JP2002053079 A JP 2002053079A JP 2002053079 A JP2002053079 A JP 2002053079A JP 2003251109 A JP2003251109 A JP 2003251109A
Authority
JP
Japan
Prior art keywords
filter
moving bed
bed type
sand
filtration
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
JP2002053079A
Other languages
Japanese (ja)
Inventor
Masayuki Enzaki
正之 煙▲崎▼
Masahito Fujita
雅人 藤田
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.)
Takuma Co Ltd
Original Assignee
Takuma Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Takuma Co Ltd filed Critical Takuma Co Ltd
Priority to JP2002053079A priority Critical patent/JP2003251109A/en
Publication of JP2003251109A publication Critical patent/JP2003251109A/en
Pending legal-status Critical Current

Links

Classifications

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

Abstract

<P>PROBLEM TO BE SOLVED: To provide a non-wasteful and stable moving bed type biological membrane sand filtering method. <P>SOLUTION: A moving bed type sand filter 1 is constituted so as to circulate filter media by utilizing an air lift 4 to wash them. The lost head of a filter bed 3, concretely, pressure P on a discharge side, a pressure difference between the upper and lower parts of the filter bed or the fluctuation of a water level is detected by using the moving bed type sand filter 1 to adjust the supply amount F of air to the air lift 4. An ascending flow moving bed type sand filter 1 is preferably used. The waste of energy required in operation can be omitted and the life of an apparatus, or the like, can be extended. This filter can be put to practical use in a moving bad type biological membrane sand filter. <P>COPYRIGHT: (C)2003,JPO

Description

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

【0001】[0001]

【発明の属する技術分野】本発明は、エアリフトを利用
した移動床式砂ろ過器(以下、本発明の説明においては
単に「移動床ろ過器」という。移動床式砂ろ過方法及び
システムについても同じように略称する)を用い、下水
道処理水やし尿処理水、河川水、産業排水、廃棄物埋立
地浸出水などの汚水を対象として、汚濁物質をろ過し除
去する移動床ろ過方法に関し、さらに、エアリフトを利
用した移動床式生物膜砂ろ過器(以下、本発明の説明に
おいては単に「移動床膜ろ過器」という。移動床式生物
膜砂ろ過方法及びシステムについても同じように略称す
る)を用い、前記と同様に汚水を対象として、汚濁物質
をろ過して除去し、同時にろ材の砂表面に微生物膜を生
成させ、汚濁物質を生物的に分解して除去する移動床膜
ろ過方法に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a moving bed type sand filter utilizing an air lift (hereinafter, simply referred to as "moving bed filter" in the description of the present invention. The same applies to a moving bed type sand filtering method and system. A sewage treated water, human waste treated water, river water, industrial wastewater, waste landfill leachate, etc., as a target, and a moving bed filtration method for filtering and removing pollutants. A moving bed type biofilm sand filter utilizing an air lift (hereinafter, simply referred to as “moving bed membrane filter” in the description of the present invention. The same applies to the moving bed type biofilm sand filtration method and system). Using the same as above, targeting sewage, to remove the contaminants by filtration, at the same time to generate a microbial membrane on the sand surface of the filter medium, to the moving bed membrane filtration method of biologically decomposing and removing the contaminants

【0002】[0002]

【従来の技術】本発明にいう移動床ろ過器は、前記の汚
水などを被処理水としてろ過操作を実施しつつ、エアリ
フトを利用してろ材である砂または粒体を連続的に循
環、逆洗し、汚濁物質を砂から分離してろ材を再生し、
ろ過床に循環することにより、ろ過とろ材の洗浄とを同
時に実施して連続ろ過操作を可能にする。代表的な機種
として上向流移動床式砂ろ過器があげられ、ほかにも水
平流移動床式砂ろ過器などがあげられる。
2. Description of the Related Art A moving bed filter according to the present invention performs a filtering operation using the above-mentioned sewage as treated water while using an air lift to continuously circulate or reverse the sand or granules as a filter medium. Wash, separate pollutants from sand and regenerate filter media,
By circulating in the filtration bed, filtration and washing of the filter medium are simultaneously carried out to enable continuous filtration operation. As a typical model, there is an upflow moving bed sand filter, and there is also a horizontal moving bed sand filter.

【0003】また、移動床膜ろ過器は、前記の移動床ろ
過器とほぼ同じ構成のろ過器を用い、ただし、ろ材であ
る砂や粒体を、ろ材、かつ窒素化合物の分解能を有する
微生物の支持体として利用し、被処理水に含まれる汚濁
物質の連続ろ過と窒素化合物の生物的分解、除去とを同
時に実施するものである。
As the moving bed membrane filter, a filter having substantially the same structure as that of the moving bed filter described above is used, except that sand or granules, which are filter media, are used as filter media and microorganisms capable of decomposing nitrogen compounds. It is used as a support, and continuous filtration of pollutants contained in water to be treated and biological decomposition and removal of nitrogen compounds are simultaneously carried out.

【0004】前記の上向流移動床式砂ろ過器について、
その一例を示した図1を参照して簡単に説明する。図1
に例示した移動床式砂ろ過器1は、底部がロート状の筒
型容器をろ過槽2とし、ろ材の砂を適量充填してろ過床
3を形成し、汚濁物質を含んだろ過供給水7をろ過槽2
の下部から供給してろ過床3を上方に向かって、すなわ
ちろ過床3中を上向流になって通過させ、固形汚濁物質
をろ過、分離し、ろ過水8を上部からオーバーフローさ
せて取り出す。一方、ろ過床3の下部にはエアリフト管
4を挿入して空気9を吹き込む。ろ材の砂はエアリフト
に吸引されてエアリフト管4中を空気とともに上昇しな
がら空気と水とで洗浄される。エアリフト管4の上端に
は分離器5が設けられて、上昇してきた砂と同伴する空
気と洗浄排水とが分離される。
Regarding the above-mentioned upflow moving bed sand filter,
A brief description will be given with reference to FIG. 1 showing an example thereof. Figure 1
The moving bed type sand filter 1 illustrated in FIG. 2 has a cylindrical container having a funnel-shaped bottom as a filtration tank 2, and a filter bed 3 is formed by filling an appropriate amount of sand as a filter medium to form a filtration feed water 7 containing pollutants. Filter tank 2
Is supplied from the lower part of the above, and is passed through the filter bed 3 in the upward direction, that is, in the upward direction through the filter bed 3, solid contaminants are filtered and separated, and filtered water 8 is taken out by overflowing from the upper part. On the other hand, the air lift pipe 4 is inserted in the lower part of the filtration bed 3 to blow air 9. The sand of the filter medium is sucked by the air lift and is washed with air and water while rising in the air lift pipe 4 together with the air. A separator 5 is provided at the upper end of the air lift pipe 4 to separate the rising sand, the accompanying air, and the cleaning drainage.

【0005】分離された砂は汚濁物質とともにサンドウ
オッシャー6へと沈降する。サンドウオッシャー6下部
からは、ろ過床3を通過したろ過水の一部が洗浄水とし
て導入され、上向流となって沈降する砂と向流接触し、
砂と汚濁物質とを分離し、砂をろ材として再生させる。
再生されたろ材は、サンドウオッシャー6からろ過床3
の表面に沈降し、ろ過床3に循環される。汚濁物質は上
向水に同伴してサンドウオッシャー6内を上方へと移動
し、前記の洗浄排水とともに排水10としてろ過器1外
に排出される。この様にして、ろ過と洗浄とを交互に切
り替えて操作することなく、常時、連続定量的にろ材が
洗浄されているので、ろ過床は一定の水準で清澄に維持
され、損失水頭も安定して低く保たれる特長がある。
The separated sand settles in the sand washer 6 together with pollutants. From the lower part of the sand washer 6, a part of the filtered water that has passed through the filter bed 3 is introduced as washing water and comes into countercurrent contact with the sand that forms an upward flow and sinks,
The sand and pollutants are separated and the sand is regenerated as a filter medium.
The reclaimed filter material is sent from the sand washer 6 to the filter bed 3
Settles on the surface of and is circulated to the filtration bed 3. The pollutants move upward in the sand washer 6 along with the upward water, and are discharged to the outside of the filter 1 as drainage 10 together with the washing drainage. In this way, the filter bed is constantly and quantitatively washed without switching between filtration and washing, so that the filtration bed is maintained at a certain level and the head loss is stable. The feature is that it is kept low.

【0006】[0006]

【発明が解決しようとする課題】さて、移動床ろ過器の
運転条件は、ろ過床の状態を一定に保つて少なくとも所
要の水準以上のろ過水を安定して得るため、一般にろ過
器の運転条件は、余裕をもたせるため想定される最大負
荷の洗浄が可能なように設定してある。したがって、通
常状態における被処理水のろ過負荷は当初の設定条件を
下回り、エアリフトに吹き込む空気量が必要以上に大き
くなって、操業時間の大部分では、ろ材に過剰な循環と
洗浄とが実施されている。その結果、無駄なエネルギー
を消費し、かつエアリフトなどの内部装置やろ材の損耗
を助長していることが判った。逆に被処理水の流入過剰
などろ過床に設定以上の負荷があるとブレークスルーに
よるろ過不良の問題が発生する。膜ろ過プロセスに移動
床膜ろ過器を採用する場合においても、前記と同様の問
題が発生するものと考えられる。本発明は、これらの課
題を解決するために完成されたのである。
The operating conditions of the moving bed filter are generally those of the operating condition of the filter because at least the required level of filtered water can be stably obtained while keeping the condition of the filtering bed constant. Is set so that it is possible to clean the maximum load that is expected in order to provide a margin. Therefore, the filtration load of the treated water in the normal state is lower than the initially set condition, the amount of air blown into the air lift becomes unnecessarily large, and excessive circulation and cleaning are performed on the filter medium during most of the operating time. ing. As a result, it was found that wasteful energy was consumed and the wear of internal devices such as an air lift and the filter medium was promoted. On the other hand, if there is a load on the filtration bed that exceeds the set level due to excessive inflow of water to be treated, the problem of filtration failure due to breakthrough occurs. Even when a moving bed membrane filter is used in the membrane filtration process, it is considered that the same problems as described above will occur. The present invention has been completed to solve these problems.

【0007】[0007]

【課題を解決するための手段】本発明について図面を参
照して説明する。まず、本発明は、エアリフトを利用し
てろ材を循環し洗浄する移動床式砂ろ過器を用い、ろ過
床の損失水頭の変動を検出してエアリフトへの供給空気
量を調整することを特徴とする移動床式砂ろ過方法を提
供する。前記の移動床式砂ろ過器には、上向流移動床式
砂ろ過器を好ましく用いることができる。そして、エア
リフトを利用してろ材を循環し洗浄する移動床式砂ろ過
器と、ろ過床の損失水頭の変動を検出する検知器と、損
失水頭の変動にもとづいてエアリフトへの供給空気量を
調整する調整手段とを含んで構成されていることを特徴
とする移動床式砂ろ過システムを提供する。
The present invention will be described with reference to the drawings. First, the present invention is characterized by using a moving bed type sand filter that circulates and cleans a filter medium using an air lift, and detects the fluctuation of the head loss of the filter bed to adjust the amount of air supplied to the air lift. A moving bed type sand filtration method is provided. An upflow moving bed sand filter can be preferably used as the moving bed sand filter. Then, a moving bed type sand filter that uses an air lift to circulate and wash the filter media, a detector that detects fluctuations in the head loss of the filtration bed, and the amount of air supplied to the air lift is adjusted based on the fluctuations in the head loss. The present invention provides a moving bed type sand filtration system, which is characterized in that it comprises an adjusting means for

【0008】また、本発明は、エアリフトを利用してろ
材を循環し洗浄する移動床式生物膜砂ろ過器を用い、膜
ろ過床の損失水頭の変動を検出してエアリフトへの供給
空気量を調整することを特徴とする移動床式生物膜ろ過
方法を提供する。そして、エアリフトを利用してろ材を
循環し洗浄する移動床式生物膜砂ろ過器と、ろ過床の損
失水頭の変動を検出する検知器と、損失水頭の変動にも
とづいてエアリフトへの供給空気量を調整する調整手段
とを含んで構成されていることを特徴とする移動床式生
物膜砂ろ過システムを提供する。
Further, the present invention uses a moving bed type biological membrane sand filter which circulates and cleans a filter medium using an air lift, and detects the fluctuation of the head loss of the membrane filtration bed to determine the amount of air supplied to the air lift. A moving bed type biofilm filtration method characterized by adjusting. Then, a moving bed type biofilm sand filter that circulates and cleans the filter medium using an air lift, a detector that detects fluctuations in the head loss of the filter bed, and the amount of air supplied to the air lift based on fluctuations in the head loss A moving bed type biofilm sand filtration system is provided, which comprises:

【0009】[0009]

【発明の実施の形態】図1を参照して本発明の実施形態
をを具体的に説明する。図1は、上向流移動床式ろ過器
を用いて本発明移動床ろ過方法及びそのシステムを実施
する場合を例に、そのシステムの概要を示すフローシー
トである。なお、本発明にかかる移動床膜ろ過システム
についても図1に示すフローシートにほぼ同様である
が、脱窒操作を円滑に実施するため必要に応じて、洗浄
排水10をろ過供給水7に循環するラインなどの脱窒操
作固有の付加装置を設けることができる。
BEST MODE FOR CARRYING OUT THE INVENTION An embodiment of the present invention will be specifically described with reference to FIG. FIG. 1 is a flow sheet showing an outline of a system, by way of example, in which the moving bed filtration method of the present invention and the system thereof are carried out using an upward flow moving bed filter. The moving bed membrane filtration system according to the present invention is almost the same as the flow sheet shown in FIG. 1, but the cleaning waste water 10 is circulated to the filtered supply water 7 as necessary to smoothly carry out the denitrification operation. It is possible to provide additional equipment specific to denitrification operation, such as a line for denitrification.

【0010】移動床ろ過器1では、ろ過・洗浄交互切替
方式のろ過器と異なり、使用するろ過器の最大ろ過量の
範囲内であれば、供給される汚濁物質量とろ材の洗浄に
よって分離、除去される汚濁物質の量とがほぼ平衡に達
し、ろ過床3の状態が一定に保たれ操業されているの
で、ろ過床3に供給される被処理水7中に含まれる汚濁
物質の増加など、負荷に特段の変動要因がない限り、ろ
過床3の損失水頭は運転時間の経過に無関係に一定に保
たれて推移している。この特徴を利用して、ろ過床3の
損失水頭の変動、具体的に被処理水をポンプ送水してい
る場合であれば原水又は被処理水送入ポンプの吐出側圧
力Pを、自然流下方式の場合ではその水位レベルを、あ
るいは直接ろ過床の差圧などを監視して、その変動から
ろ過床3における負荷変動の発生を検知することができ
る。
In the moving bed filter 1, unlike the filter of the alternating filtration / washing switching system, if it is within the maximum filtration amount of the filter to be used, it is separated by the amount of pollutants supplied and the washing of the filter medium, Since the amount of pollutants to be removed has almost reached the equilibrium and the filter bed 3 is kept in a constant state of operation, the increase of pollutants contained in the treated water 7 supplied to the filter bed 3 etc. As long as there is no particular variable factor in the load, the head loss of the filter bed 3 is kept constant regardless of the elapsed operating time. Utilizing this feature, the fluctuation of the head loss of the filtration bed 3, specifically, in the case of pumping the treated water, the discharge side pressure P of the raw water or the treated water feeding pump is set to the natural flow system. In this case, the water level or the pressure difference in the filtration bed can be directly monitored to detect the occurrence of load fluctuation in the filtration bed 3 from the fluctuation.

【0011】さて、本発明の実施に先立っては、あらか
じめ対象となる被処理水をろ過して汚濁物質を除去し所
要の水質にする条件を、たとえば、被処理水量や水質を
パラメーターあるいは変数として、水質の安定性、経済
性等を含め、必要にして最適の吹込空気量と関係づけ、
プロセス制御系(PC)に組み込んでおくとよい。最適
状態の空気吹込量で運転中の移動床式ろ過器1におい
て、前記ポンプ吐出側圧力、圧力差又は水位レベルの増
加傾向は、通常、ろ過床3の負荷の増加傾向を示す。負
荷が増大する原因は、殆どの場合、ろ過する汚濁物質量
に対しろ材の洗浄が追いつかず、清浄なろ過状態に保た
れている状態に較べてろ過床3に汚濁物質がたまり、閉
塞傾向になることによる。放置すればろ過床3は閉塞
し、運転不能に陥る可能性がある。負荷変動を検知した
場合には、前記の関係にもとづいて、エアリフトに吹き
込む空気量Fが最適量になるように調整する。通常、負
荷が増大した場合には、吹込空気量Fを増加させてろ材
の洗浄能力を引き上げる。
Prior to the practice of the present invention, the conditions under which the target water to be treated is filtered in advance to remove pollutants to obtain the required water quality, for example, the amount of water to be treated or the water quality is used as a parameter or variable. , Including the stability of the water quality, economic efficiency, etc.
It is recommended to incorporate it in the process control system (PC). In the moving bed type filter 1 which is operating with the air blowing amount in the optimum state, the increasing tendency of the pump discharge side pressure, the pressure difference or the water level usually shows the increasing tendency of the load of the filtering bed 3. In most cases, the reason why the load increases is that the cleaning of the filter medium cannot catch up with the amount of pollutant to be filtered, and pollutant accumulates on the filter bed 3 as compared with the case where the filter is kept in a clean filtration state, which tends to cause clogging. It depends. If left unattended, the filtration bed 3 may be blocked and may be inoperable. When the load fluctuation is detected, the air amount F blown into the air lift is adjusted to be the optimum amount based on the above relationship. Normally, when the load increases, the blown air amount F is increased to raise the cleaning ability of the filter medium.

【0012】逆に前記の吐出側圧力、圧力差又は水位レ
ベルの減少は、通常、ろ過床の負荷の減少を示すもので
あって、ろ材の循環、洗浄処理量が過大傾向にあること
を示す。したがって、無駄なエネルギーの消費とろ材お
よびろ過器の寿命を縮めることになるので空気量を減少
しろ材の洗浄処理レベルを適正な状態に戻す。吹込空気
量の調整手段にとくに制限はなく、ろ過装置の構成によ
ってブロワーの回転数制御や管路に風量調節弁を設けて
制御するなど適宜に選択すればよい。
On the contrary, the decrease in the discharge side pressure, the pressure difference or the water level usually indicates a decrease in the load of the filter bed, and indicates that the circulation amount of the filter medium and the amount of cleaning treatment tend to be excessive. . Therefore, wasteful energy consumption and the life of the filter medium and the filter are shortened, so that the amount of air is reduced and the cleaning treatment level of the filter medium is returned to an appropriate state. The means for adjusting the blown air amount is not particularly limited, and may be appropriately selected by controlling the rotational speed of the blower or by providing an air flow rate adjusting valve in the pipeline depending on the configuration of the filtering device.

【0013】上記の移動床ろ過方法及びそのシステム
は、ろ過と脱窒とを同時に実施する移動床膜ろ過方法及
びそのシステムとしても効率的に利用することができ
る。移動床膜ろ過操作の場合には、前記したろ過操作に
おける負荷と吹込吸気量との関係に加えて、当該移動床
膜ろ過器における脱窒の負荷と吹込空気量との関係をあ
らかじめ把握し、制御系に組み込んでろ過操作との両立
をはかっておくとよい。一般的に、ろ過操作における負
荷の増大は操業不能に至ることがあるので、その条件設
定の優先順位は高いが、脱窒操作の過剰負荷への対応
は、処理水中の残窒素成分の増加をもたらすものの操業
自体が不能になることは少なく、また、洗浄排水の循環
や有機化合物の補充などの二次的手段も残されているの
で、それらを勘案して対応を設定すればよい。
The above moving bed filtration method and system thereof can also be effectively utilized as a moving bed membrane filtration method and system for simultaneously performing filtration and denitrification. In the case of the moving bed membrane filtration operation, in addition to the relationship between the load and the blown intake air amount in the above-described filtration operation, the relationship between the denitrification load and the blown air amount in the moving bed membrane filter is grasped in advance, It is advisable to incorporate it into the control system to achieve compatibility with the filtration operation. Generally, increasing the load in filtration operation may lead to inoperability, so the priority of setting the conditions is high, but responding to the excessive load of denitrification operation is to increase the residual nitrogen component in the treated water. However, the operation itself is unlikely to be disabled, and secondary means such as circulation of washing wastewater and supplementation of organic compounds are left, so it is only necessary to set the countermeasures in consideration of them.

【0014】[0014]

【発明の効果】本発明を利用することによって、移動床
ろ過方法及びそのシステムは、ろ過床の負荷の増減に対
しエアリフトへの空気吹込量を増減して、ろ材の循環、
洗浄量を適正に増減することができるので、エネルギー
などに無駄のない運転を実施し、かつ装置寿命を延ばす
ことができる。なお、本発明を利用し下水処理水を対象
にしたろ過操作においては、70日間の操業で使用エネ
ルギーを約30%節減することができた。
By utilizing the present invention, the moving bed filtration method and system can increase or decrease the amount of air blown into the air lift with respect to the increase or decrease of the load on the filtration bed to circulate the filter medium,
Since the cleaning amount can be appropriately increased / decreased, the operation without waste of energy can be performed and the life of the apparatus can be extended. In addition, in the filtration operation targeting the sewage treated water using the present invention, the energy used could be reduced by about 30% by the operation for 70 days.

【0015】また、移動床膜ろ過方法及びそのシステム
においても前記と同様の効果を期待することができる。
The same effects as described above can be expected in the moving bed membrane filtration method and system.

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

【図1】 本発明の一実施形態例を示す概略フローシー
FIG. 1 is a schematic flow sheet showing an embodiment of the present invention.

【符号の説明】[Explanation of symbols]

1:上向流移床式連続砂ろ過器 2:ろ過槽 3:ろ過床 4:エアリフト管 5:分離器 6:サンドウオッ
シャー 7:ろ過供給水 8:ろ過水 9:空気 10:洗浄排水 F:流量計 P:圧力計
1: Upflow transfer bed type continuous sand filter 2: Filtration tank 3: Filtration bed 4: Air lift pipe 5: Separator 6: Sand washer 7: Filtration water supply 8: Filtration water 9: Air 10: Wash drainage F: Flow meter P: Pressure gauge

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.7 識別記号 FI テーマコート゛(参考) C02F 3/34 101 B01D 29/08 510A ZAB 530C 540A Fターム(参考) 4D003 AA08 AB11 DA23 EA01 EA14 EA22 FA01 4D040 AA04 AA34 AA61 BB42 BB82 BB91 BB93 ─────────────────────────────────────────────────── ─── Continuation of front page (51) Int.Cl. 7 Identification code FI theme code (reference) C02F 3/34 101 B01D 29/08 510A ZAB 530C 540A F term (reference) 4D003 AA08 AB11 DA23 EA01 EA14 EA22 FA01 4D040 AA04 AA34 AA61 BB42 BB82 BB91 BB93

Claims (5)

【特許請求の範囲】[Claims] 【請求項1】エアリフトを利用してろ材を循環し洗浄す
る移動床式砂ろ過器を用い、ろ過床の損失水頭の変動を
検出してエアリフトへの供給空気量を調整することを特
徴とする移動床式砂ろ過方法。
1. A moving bed type sand filter that circulates and cleans a filter medium using an air lift is used to detect fluctuations in the head loss of the filtration bed and adjust the amount of air supplied to the air lift. Moving bed type sand filtration method.
【請求項2】前記の移動床式砂ろ過器として上向流移動
床式砂ろ過器を用いたことを特徴とする請求項1記載の
移動床式砂ろ過方法。
2. The moving bed type sand filtration method according to claim 1, wherein an upflow moving bed type sand filter is used as the moving bed type sand filter.
【請求項3】エアリフトを利用してろ材を循環し洗浄す
る移動床式生物膜砂ろ過器を用い、膜ろ過床の損失水頭
の変動を検出してエアリフトへの供給空気量を調整する
ことを特徴とする移動床式生物膜膜ろ過方法。
3. A moving bed type biological membrane sand filter that circulates and cleans a filter medium using an air lift is used to detect the fluctuation of the head loss of the membrane filtration bed to adjust the amount of air supplied to the air lift. A moving bed type biofilm membrane filtration method characterized.
【請求項4】エアリフトを利用してろ材を循環し洗浄す
る移動床式砂ろ過器と、ろ過床の損失水頭の変動を検出
する検知器と、損失水頭の変動にもとづきエアリフトへ
の供給空気量を調整する調整手段とを含んで構成されて
いることを特徴とする移動床式砂ろ過システム。
4. A moving bed type sand filter that circulates and cleans a filter medium using an air lift, a detector that detects fluctuations in the head loss of the filter bed, and the amount of air supplied to the air lift based on fluctuations in the head loss. A moving bed type sand filtration system comprising:
【請求項5】エアリフトを利用してろ材を循環し洗浄す
る移動床式生物膜砂ろ過器と、ろ過床の損失水頭の変動
を検出する検知器と、損失水頭の変動にもとづきエアリ
フトへの供給空気量を調整する調整手段とを含んで構成
されていることを特徴とする移動床式生物膜砂ろ過シス
テム。
5. A moving bed type biofilm sand filter that circulates and cleans a filter medium using an air lift, a detector that detects fluctuations in the head loss of the filter bed, and a supply to the air lift based on fluctuations in the head loss. A moving bed type biofilm sand filtration system comprising: an adjusting means for adjusting the amount of air.
JP2002053079A 2002-02-28 2002-02-28 Moving bed type sand filter, moving bed type biological membrane sand filtering method and system therefor Pending JP2003251109A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2002053079A JP2003251109A (en) 2002-02-28 2002-02-28 Moving bed type sand filter, moving bed type biological membrane sand filtering method and system therefor

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2002053079A JP2003251109A (en) 2002-02-28 2002-02-28 Moving bed type sand filter, moving bed type biological membrane sand filtering method and system therefor

Publications (1)

Publication Number Publication Date
JP2003251109A true JP2003251109A (en) 2003-09-09

Family

ID=28664601

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2002053079A Pending JP2003251109A (en) 2002-02-28 2002-02-28 Moving bed type sand filter, moving bed type biological membrane sand filtering method and system therefor

Country Status (1)

Country Link
JP (1) JP2003251109A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2005095818A (en) * 2003-09-26 2005-04-14 Sanki Eng Co Ltd Water purification method and water purification system
JP2009526643A (en) * 2006-02-17 2009-07-23 ジェネシス フルーイド ソリューションズ エルエルシー Apparatus and method for slurry dewatering
CN102008841A (en) * 2010-10-15 2011-04-13 扬州澄露环境工程有限公司 Non-cutoff differential pressure backwashing filter
CN102649616A (en) * 2012-05-09 2012-08-29 天津凯铂能膜工程技术有限公司 Comprehensive treatment method for garbage leachate

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2005095818A (en) * 2003-09-26 2005-04-14 Sanki Eng Co Ltd Water purification method and water purification system
JP2009526643A (en) * 2006-02-17 2009-07-23 ジェネシス フルーイド ソリューションズ エルエルシー Apparatus and method for slurry dewatering
CN102008841A (en) * 2010-10-15 2011-04-13 扬州澄露环境工程有限公司 Non-cutoff differential pressure backwashing filter
CN102008841B (en) * 2010-10-15 2012-09-05 扬州澄露环境工程有限公司 Non-cutoff differential pressure backwashing filter
CN102649616A (en) * 2012-05-09 2012-08-29 天津凯铂能膜工程技术有限公司 Comprehensive treatment method for garbage leachate

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