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JP3548886B2 - Washing and regenerating method of filter media in filter - Google Patents

Washing and regenerating method of filter media in filter Download PDF

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Publication number
JP3548886B2
JP3548886B2 JP34244698A JP34244698A JP3548886B2 JP 3548886 B2 JP3548886 B2 JP 3548886B2 JP 34244698 A JP34244698 A JP 34244698A JP 34244698 A JP34244698 A JP 34244698A JP 3548886 B2 JP3548886 B2 JP 3548886B2
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Japan
Prior art keywords
filter
raw water
filter medium
concentration
amount
Prior art date
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Expired - Fee Related
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JP34244698A
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Japanese (ja)
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JP2000167320A (en
Inventor
修 山下
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Ishigaki Co Ltd
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Ishigaki Co Ltd
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Priority to JP34244698A priority Critical patent/JP3548886B2/en
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Description

【0001】
【発明の属する技術分野】
この発明は、砂粒や金属の微細粒等の比重の大きな微細粒子を含む原水のろ過機におけるろ材層の洗浄再生方法に関する。
【0002】
【従来の技術】
従来、繊維ろ材を用いたろ過機では、目詰まりしたろ材を洗浄再生するに当たって、継続運転中に定期的に逆洗洗浄するもの、またろ材のろ過抵抗(損失水頭)をキャッチして逆洗洗浄するものなどがよく知られている。
【0003】
【発明が解決しようとする課題】
然しながら、上述のような従来の方法では、比重の重い無機質の汚濁物、例えば微細な砂粒や金属粒を含んだ原水をろ過する場合、ろ過抵抗が上がりにくいため、ろ材層中に汚濁物が設計値以上に捕捉される。そして、この汚濁物があまりに多く捕捉されると設置されている洗浄装置でろ材層を崩すことができなくなり、洗浄不能や洗浄不足になる。
【0004】
【課題を解決するための手段】
この発明は、上述のような課題を解決し得るものであって、その要旨とするところは、砂粒等の比重の大きな微粒子を含む原水のろ過機において、このろ過機の原水の流入側に、原水の流入量を測定する流量計と、汚濁濃度を測定する濁度計を設け、その検知信号をろ過装置の制御盤に送信し、上記ろ過機のろ液の取出側に濁度計を設け、検知したろ過水中の汚濁物の濃度をろ過装置の制御盤に送信すると共に、制御盤で受信した原水流入量と原水汚濁濃度からろ過水中の汚濁物の濃度を差し引いた汚濁濃度とを積算して汚濁物量を算出し、随時所定時間の汚濁物総量と設定値を比較演算し、汚濁物総量が設定値に達したとき、ろ材捕捉限界値として制御盤の指令信号をろ材の撹拌洗浄装置に送信し、ろ過機のろ材層を洗浄させるようにしたものである。
【0005】
【発明の実施の形態】
上記積算流入量の測定には、通常の流量計を用い、その下流に濁度計を設け、その流量と濃度(濁度)とをろ材の洗浄装置の制御盤に伝達し、その流入積算量からろ材層に送り込まれた汚濁物量を求め、その汚濁物量が一定量に達したとき、その情報によってろ過運転を停止してろ材の洗浄運転をするものである。また、その積算汚濁物量は、該ろ過機に設けたろ材の洗浄装置の能力に見合った撹拌可能な量とするものである。
【0006】
このようにこの発明では、ろ材層に流入する汚濁物が洗浄可能な量に達したときに洗浄するので、洗浄不能になったり、洗浄不充分になることなく安定したろ過運転を継続することができる。すなわち、従来の定期的にろ材を洗浄するものに比較して洗浄不能になったり洗浄不充分になったりすることがないものである。そして、ろ材中に流入する汚濁物量でろ材の洗浄時期を制御するので、運転継続中の原水の汚濁物濃度が変化してもそれに対応してろ材の洗浄再生が可能である。以下、図面に随ってこの発明を具体的に説明する。
【0007】
【実施例】
図1は、この発明に係るろ過装置の作動フローをブロック図として示すもので図中、符号1はろ過機で内部にろ材層や洗浄装置が設けてある。このろ過機1の原水の流入側には、原水の流入量を瞬時流量として測定する電磁流量計2と、瞬時汚濁濃度を測定する濁度計3が設けてあり、その検知信号をろ過装置の制御盤4に送信するようにしてある。制御盤4にはあらかじめ実験にて導き出した設定値Vが入力してあり、電磁流量計2と濁度計3で測定した原水流入量aと原水汚濁濃度bを積算して汚濁物量Qを算出し、随時所定時間の汚濁物総量ΣQと設定値Vを比較演算し、汚濁物総量ΣQが設定値Vに達したとき、ろ材捕捉限界値としてろ材の撹拌洗浄装置を作動させるようにしてある。上記ろ過機1のろ液の取出側には濁度計5が設けてあり、検知したろ過水中の汚濁物の濃度cをろ過装置の制御盤4に送信して、原水汚濁濃度bからろ過水中の汚濁物の濃度cを差し引いた汚濁濃度(b−c)とすれば、制御盤4で受信した原水流入量aと汚濁濃度(b−c)とを積算して汚濁物量Q’を算出すればより正確なろ材捕捉限界値が把握でき、随時所定時間の汚濁物総量ΣQ’と設定値V’を比較演算して、汚濁物総量ΣQ’が設定値V’に達したとき、ろ材捕捉限界値として制御盤4の指令信号をろ材の撹拌洗浄装置に送信し、ろ過機1のろ材層を洗浄させることができる。破線矢印線はその連結状態を示すものである。また、矢印イは原水の流入線、矢印ロは処理水の取出線、矢印ハは洗浄水の流入線、矢印ニは洗浄排水の取出線を示すものである。
【0008】
上記作動フロー図では、原水は電磁流量計2および濁度計3を経てろ過機1に送られてろ過されたのち、その処理水は濁度計5を経て系外に取出される。一方、電磁流量計2では原水の流入量が測定され、その測定値は情報として制御盤4に伝達される。また、濁度計3では流入原水の濁度が測定されてその測定値が情報として制御盤4に伝達される。制御盤4では原水の流入水量情報とその濁度濃度情報とからろ材層に流入した積算汚濁物量が算出される。
【0009】
そして、上述のようなろ過運転を継続して、ろ過機1への原水の流入量(汚濁物量)が一定値に達すると原水の供給が停止され、ろ材の洗浄装置が作動し、ろ材が撹拌洗浄される。すなわち、この発明では原水の積算流入量によってろ材層の目詰まり具合を判断して適切な時期にろ材を撹拌洗浄し、洗浄不能や洗浄不足を防止できるものである。
【0010】
このろ材層に送られる汚濁物量Qは、原水汚濁濃度bと原水流入量aとによって、算定されるものであり、目詰まりしたろ材層が撹拌洗浄が可能であるかどうかの汚濁物の流入限界量は原水の性状やろ材の性状に基づいた実験値に基づいて決定するものである。
【0011】
従来、この種の粒状ろ材を用いたろ過機でろ材を洗浄するのに、単に、一定時間間隔で行うものでは、原水内の汚濁物の多少によってろ材層の目詰まり具合が異なるが、これに配慮することなく洗浄が行われるので、洗浄不能であったり、洗浄不足がしばしば発生した。すなわち、汚濁物が無機質の比重の大きなものでは捕捉した汚濁物がろ材層中に溜まってろ材層が固化して洗浄不能となったり、洗浄不足を生じていた。また、ろ材による損失水頭を検知して洗浄するものでも汚濁物が溜まってろ材層が閉塞すると撹拌できず、洗浄不能となっていた。このような場合、この発明ではろ材層で捕捉した汚濁物量に基づいて洗浄をするので、上述のような難点を解消して安定したろ過運転をすることができるものである。
【0012】
【発明の効果】
このようにこの発明に係る方法によれば、以上の説明で明らかなように、この発明のろ材の洗浄再生方法によれば、ろ材捕捉限界値が予測でき目詰まりしたろ過機のろ材層を洗浄できるものである。即ち、従来の洗浄方法にあっては、原液に含まれる比重の大きい物質が、ろ材隙間に多量に捕捉されてもろ過抵抗が上昇せず、洗浄時期の決定が難しく、洗浄不足を生じたり洗浄が不可能となる恐れがあったものであるが、この発明にあっては、原水流入側に流量計と、濁度計を設け、その検知信号をろ過装置の制御盤に送信すると共に、ろ液の取出側に濁度計を設け、ろ過水中の汚濁物の濃度をろ過装置の制御盤に送信すれば、原水流入量と原水汚濁濃度とろ過水中の汚濁物濃度から、正確なろ材捕捉限界値が把握でき、撹拌洗浄装置により自動的なろ過機のろ材層の洗浄が可能となるものである。
【図面の簡単な説明】
【図1】この発明に係るろ過機によるろ過操作の作動フロー図である。
【符号の説明】
1 ろ過機
2 電磁流量計
3 濁度計
4 制御盤
5 濁度計
a 原水流入量
b 原水汚濁濃度
c ろ過水中の汚濁物の濃度
b−c 汚濁濃度
Q、Q’ 汚濁物量
ΣQ 汚濁物総量
ΣQ’ 汚濁物総量
V、V’ 設定値
[0001]
TECHNICAL FIELD OF THE INVENTION
The present invention relates to a method for cleaning and regenerating a filter medium layer in a raw water filter including fine particles having a large specific gravity such as sand particles and metal fine particles.
[0002]
[Prior art]
Conventionally, a filter using a fiber filter medium is one that performs backwashing periodically during continuous operation when cleaning and regenerating clogged filter media, and also performs backwash cleaning by catching the filtration resistance (loss head) of the filter media. What you do is well known.
[0003]
[Problems to be solved by the invention]
However, in the conventional method as described above, when filtering inorganic contaminants having a high specific gravity, for example, raw water containing fine sand particles or metal particles, the filtration resistance is unlikely to increase. Captured above the value. If too much of this contaminant is captured, the filter device layer cannot be destroyed by the installed cleaning device, and cleaning becomes impossible or insufficient.
[0004]
[Means for Solving the Problems]
The present invention can solve the above-described problems, and the gist of the present invention is that in a raw water filter including fine particles having a large specific gravity such as sand particles, on the inflow side of the raw water of the filter, A flow meter that measures the inflow of raw water and a turbidity meter that measures the concentration of pollutants are provided.The detection signal is sent to the control panel of the filtration device, and a turbidity meter is provided on the filtrate extraction side of the filter. In addition to transmitting the detected concentration of contaminants in the filtered water to the control panel of the filtration device, integrating the raw water inflow amount received by the control panel and the pollutant concentration obtained by subtracting the concentration of the contaminants in the filtered water from the raw water pollutant concentration. Calculate the amount of contaminants and compare and calculate the total amount of contaminants for a predetermined period of time and the set value, and when the total amount of contaminants reaches the set value, send the command signal of the control panel as the filter medium capture limit value to the filter medium stirring and washing device. Send and wash the filter media layer of the filter Than it is.
[0005]
BEST MODE FOR CARRYING OUT THE INVENTION
For the measurement of the integrated inflow amount, a normal flow meter is used, and a turbidity meter is provided downstream thereof, and its flow rate and concentration (turbidity) are transmitted to a control panel of a filter medium washing device, and the integrated inflow amount is measured. The amount of contaminants sent to the filter medium layer is determined, and when the amount of contaminants reaches a certain amount, the filtering operation is stopped based on the information and the filter medium is washed. Further, the accumulated pollutant amount is an amount that can be stirred in accordance with the capacity of the filter device washing device provided in the filter.
[0006]
As described above, according to the present invention, the contaminants flowing into the filter medium layer are washed when they reach a washable amount, so that it is possible to continue a stable filtration operation without making washing impossible or insufficient washing. it can. That is, compared to a conventional filter medium that periodically cleans the filter medium, the filter medium does not become uncleanable or insufficiently cleaned. And since the washing time of the filter medium is controlled by the amount of the contaminants flowing into the filter medium, even if the concentration of the contaminants in the raw water changes during the continuous operation, the filter medium can be washed and regenerated correspondingly. Hereinafter, the present invention will be specifically described with reference to the drawings.
[0007]
【Example】
FIG. 1 is a block diagram showing an operation flow of a filtration device according to the present invention. In the drawing, reference numeral 1 denotes a filtration machine in which a filter medium layer and a washing device are provided. On the raw water inflow side of the filter 1, an electromagnetic flow meter 2 for measuring the flow rate of the raw water as an instantaneous flow rate, and a turbidity meter 3 for measuring the instantaneous pollutant concentration are provided. The information is transmitted to the control panel 4. The control panel 4 receives a set value V derived in advance through experiments, and calculates a pollutant amount Q by integrating the raw water inflow amount a and the raw water contamination concentration b measured by the electromagnetic flow meter 2 and the turbidity meter 3. Then, the total amount of contaminants の Q for a predetermined time is compared with the set value V, and when the total amount of contaminants ΣQ reaches the set value V, the filter medium stirring and washing device is operated as a filter medium capture limit value. A turbidity meter 5 is provided on the filtrate extraction side of the filter 1 and transmits the detected concentration c of the contaminants in the filtered water to the control panel 4 of the filtration device to convert the raw water contamination concentration b into the filtered water. If the pollutant concentration (bc) is obtained by subtracting the pollutant concentration c, the pollutant concentration Q ′ is calculated by integrating the raw water inflow a received by the control panel 4 and the pollutant concentration (bc). If the total amount of contaminants ΣQ 'reaches the set value V' when the total amount of contaminants ΣQ 'reaches the set value V' at any time, the total amount of contaminants ΣQ 'can be grasped more accurately. By transmitting a command signal of the control panel 4 as a value to the filter medium stirring and washing apparatus, the filter medium layer of the filter 1 can be washed. The broken arrow lines indicate the connection state. An arrow A indicates an inflow line of raw water, an arrow B indicates an extraction line of treated water, an arrow C indicates an inflow line of cleaning water, and an arrow D indicates an extraction line of cleaning wastewater.
[0008]
In the above operation flow diagram, raw water is sent to the filter 1 via the electromagnetic flow meter 2 and the turbidity meter 3 and filtered, and then the treated water is taken out of the system via the turbidity meter 5. On the other hand, the electromagnetic flow meter 2 measures the inflow of raw water, and the measured value is transmitted to the control panel 4 as information. The turbidity meter 3 measures the turbidity of the inflowing raw water and transmits the measured value to the control panel 4 as information. The control panel 4 calculates the integrated pollutant amount flowing into the filter medium layer from the inflow amount information of the raw water and the turbidity concentration information thereof.
[0009]
Then, when the filtration operation as described above is continued and the inflow of raw water (the amount of pollutants) into the filter 1 reaches a certain value, the supply of the raw water is stopped, the filter cleaning device is activated, and the filter is stirred. Washed. That is, in the present invention, the degree of clogging of the filter medium layer is determined based on the accumulated inflow amount of raw water, and the filter medium is agitated and washed at an appropriate time, thereby preventing washing from being impossible or insufficient washing.
[0010]
The amount Q of contaminants sent to the filter medium layer is calculated based on the raw water contamination concentration b and the raw water inflow amount a. The pollutant inflow limit as to whether or not the clogged filter medium layer can be stirred and washed. The amount is determined based on experimental values based on the properties of raw water and the properties of the filter medium.
[0011]
Conventionally, if the filter media is washed with a filter using this type of granular filter media simply at regular time intervals, the degree of clogging of the filter media layer differs depending on the amount of contaminants in the raw water. Since cleaning is performed without consideration, cleaning is often impossible or insufficient. That is, when the pollutant has a large inorganic specific gravity, the trapped pollutant accumulates in the filter medium layer, solidifying the filter medium layer, making it impossible to wash or insufficient washing. In addition, even when the filter head is washed by detecting the head loss due to the filter medium, if the contaminants accumulate and the filter medium layer is closed, the stirring cannot be performed, and the washing cannot be performed. In such a case, in the present invention, the washing is performed based on the amount of contaminants trapped in the filter medium layer, so that the above-described difficulties can be solved and a stable filtration operation can be performed.
[0012]
【The invention's effect】
As described above, according to the method according to the present invention, as is apparent from the above description, according to the method for cleaning and regenerating a filter medium of the present invention, a filter medium layer of a filter machine in which a filter medium capture limit value can be predicted and clogged is cleaned. You can do it. That is, in the conventional cleaning method, even if a large amount of a substance having a high specific gravity contained in the stock solution is captured in a large amount in the filter medium gap, the filtration resistance does not increase, making it difficult to determine the cleaning time, causing insufficient cleaning or cleaning. However, according to the present invention , a flow meter and a turbidity meter are provided on the raw water inflow side, and the detection signal is transmitted to the control panel of the filtration device. If a turbidity meter is installed on the liquid extraction side and the concentration of contaminants in the filtered water is sent to the control panel of the filtration device, the filter media capture limit can be accurately determined based on the amount of raw water inflow, the raw water contamination concentration, and the concentration of contaminants in the filtered water. The value can be grasped, and the filter medium layer of the filter can be automatically cleaned by the stirring and cleaning device.
[Brief description of the drawings]
FIG. 1 is an operation flowchart of a filtration operation by a filter according to the present invention.
[Explanation of symbols]
DESCRIPTION OF SYMBOLS 1 Filtration machine 2 Electromagnetic flow meter 3 Turbidity meter 4 Control panel 5 Turbidity meter a Raw water inflow b Raw water contamination concentration c Concentration of contaminants in filtered water bc Contamination concentration Q, Q 'Contamination amount ΣQ Contamination amount 物 Q 'Total amount of pollutants V, V' Set value

Claims (1)

繊維ろ材等で圧縮性のろ材層を形成して砂粒等の比重の大きな微粒子を含む原水をろ過するろ過機1において、このろ過機1の原水流入側に、原水の流入量を測定する流量計2と、汚濁濃度を測定する濁度計3を設け、その検知信号をろ過装置の制御盤4に送信し、上記ろ過機1のろ液の取出側に濁度計5を設け、検知したろ過水中の汚濁物の濃度cをろ過装置の制御盤4に送信すると共に、制御盤4で受信した原水流入量aと原水汚濁濃度bからろ過水中の汚濁物の濃度cを差し引いた汚濁濃度(b−c)とを積算して汚濁物量Q’を算出し、随時所定時間の汚濁物総量ΣQ’と設定値V’を比較演算し、汚濁物総量ΣQ’が設定値V’に達したとき、ろ材捕捉限界値として制御盤4の指令信号をろ材の撹拌洗浄装置に送信し、ろ過機1のろ材層を洗浄させるろ過機におけるろ材の洗浄再生方法。A filter 1 for forming a compressible filter medium layer with a fiber filter medium and filtering raw water containing fine particles having a large specific gravity, such as sand particles, on a raw water inflow side of the filter 1 for measuring a flow rate of raw water. 2 and a turbidity meter 3 for measuring the pollutant concentration are provided, and the detection signal is transmitted to the control panel 4 of the filtration device, and a turbidity meter 5 is provided on the side of the filtrater 1 from which the filtrate is taken out. The concentration c of the contaminants in the water is sent to the control panel 4 of the filtration device, and the concentration c of the contaminants in the filtered water is subtracted from the inflow amount a of the raw water and the raw water contamination concentration b received by the control panel 4. −c) is integrated to calculate a pollutant amount Q ′, and, at any time, a comparison operation of the total pollutant amount ΣQ ′ for a predetermined time and the set value V ′, and when the total pollutant amount ΣQ ′ reaches the set value V ′ , The command signal of the control panel 4 is transmitted to the filter medium stirring and washing device as the filter medium capture limit value, and the filter medium layer of the filter 1 is removed. Cleaning regeneration method of the filter material in the filter machine to Kiyoshi.
JP34244698A 1998-12-02 1998-12-02 Washing and regenerating method of filter media in filter Expired - Fee Related JP3548886B2 (en)

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JP2002102615A (en) * 2000-09-27 2002-04-09 Buhei Kono Filtering system
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JP2011000569A (en) * 2009-06-22 2011-01-06 Miura Co Ltd Control method of filtration system
JP6101505B2 (en) * 2013-02-14 2017-03-22 株式会社川本製作所 Filtration device
JP7495045B2 (en) 2020-08-25 2024-06-04 メタウォーター株式会社 Washing control device and washing control method

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JPS607770Y2 (en) * 1982-03-10 1985-03-16 株式会社島津製作所 Filter cleaning device
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