[go: up one dir, main page]

JP2020028855A - Filter aid addition device, filtration facility and filter aid addition method - Google Patents

Filter aid addition device, filtration facility and filter aid addition method Download PDF

Info

Publication number
JP2020028855A
JP2020028855A JP2018155913A JP2018155913A JP2020028855A JP 2020028855 A JP2020028855 A JP 2020028855A JP 2018155913 A JP2018155913 A JP 2018155913A JP 2018155913 A JP2018155913 A JP 2018155913A JP 2020028855 A JP2020028855 A JP 2020028855A
Authority
JP
Japan
Prior art keywords
filter aid
stock solution
addition
amount
filter
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
JP2018155913A
Other languages
Japanese (ja)
Other versions
JP7031531B2 (en
Inventor
豊 重松
Yutaka Shigematsu
豊 重松
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.)
Sumitomo Metal Mining Co Ltd
Original Assignee
Sumitomo Metal Mining 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 Sumitomo Metal Mining Co Ltd filed Critical Sumitomo Metal Mining Co Ltd
Priority to JP2018155913A priority Critical patent/JP7031531B2/en
Publication of JP2020028855A publication Critical patent/JP2020028855A/en
Application granted granted Critical
Publication of JP7031531B2 publication Critical patent/JP7031531B2/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Images

Landscapes

  • Filtration Of Liquid (AREA)

Abstract

To provide a filter aid addition device capable of adequately controlling the addition amount of a filter aid even when the supply amount of a stock solution is small.SOLUTION: A filter aid addition device 1 comprises: a powder supplier 11 adding a powder filter aid to an addition tank 22 temporarily storing the stock solution before being supplied to a filter 25; a flow meter 12 measuring the flow rate of the stock solution supplied to the addition tank 22; and a control unit 13 controlling the operation of the powder supplier 11. The control unit 13 calculates the integrated flow rate of the stock solution to the addition tank 22 based on the measured value of the flow meter 12. The filter aid corresponding to the target amount of the stock solution is discharged by operating the powder supplier 11 in each target amount of the integrated flow rate and stopped. The average addition amount of the filter aid can be reduced by intermittently operating the powder supplier 11 and the addition amount of the filter aid can be adequately controlled even when the supply amount of the stock solution is small.SELECTED DRAWING: Figure 1

Description

本発明は、濾過助剤添加装置、濾過設備および濾過助剤添加方法に関する。さらに詳しくは、本発明は、濾過対象の原液に濾過助剤を添加する装置、その装置を備える濾過設備、および濾過対象の原液に濾過助剤を添加する方法に関する。   The present invention relates to a filter aid addition device, a filtration facility, and a filter aid addition method. More specifically, the present invention relates to an apparatus for adding a filter aid to a stock solution to be filtered, a filtration facility provided with the apparatus, and a method for adding a filter aid to a stock solution to be filtered.

原液を濾過機で濾過するにあたり、予め原液に濾過助剤を添加することがある(例えば、特許文献1)。原液に濾過助剤を添加することで、濾過機の濾過速度が向上するとともに、濾過の継続時間(濾材が目詰まりし、所定の濾過速度が得られなくなるまでの時間)が延びる。   When a stock solution is filtered by a filter, a filter aid may be added to the stock solution in advance (for example, Patent Document 1). By adding a filter aid to the stock solution, the filtration speed of the filter is improved, and the duration of filtration (the time until the filter medium is clogged and the predetermined filtration speed cannot be obtained) is extended.

特開昭56−121604号公報JP-A-56-121604

濾過助剤を粉体のまま原液に添加するには、粉体供給機が用いられる。粉体供給機の排出速度を調整することで、原液への濾過助剤の添加速度を調整できる。特定のプロセスからの排水を原液として濾過するような場合、原液の発生量はそのプロセスに依存する。したがって、場合によっては、原液の供給量が少なくなり、粉体供給機の排出速度を下限に設定しても、濾過助剤を過剰に添加してしまうことがある。   In order to add the filter aid to the stock solution as a powder, a powder feeder is used. By adjusting the discharge speed of the powder feeder, the addition speed of the filter aid to the stock solution can be adjusted. When the wastewater from a particular process is filtered as a stock solution, the amount of the stock solution generated depends on the process. Therefore, in some cases, the supply amount of the undiluted solution is reduced, and even when the discharge speed of the powder feeder is set to the lower limit, the filter aid may be excessively added.

本発明は上記事情に鑑み、原液の供給量が少ない場合であっても、濾過助剤の添加量を適切に制御できる濾過助剤添加装置、およびその濾過助剤添加装置を備える濾過設備を提供することを目的とする。
また、本発明は、原液の供給量が少ない場合であっても、濾過助剤の添加量を適切に制御できる濾過助剤添加方法を提供することを目的とする。
In view of the above circumstances, the present invention provides a filter aid adding device capable of appropriately controlling the amount of a filter aid even when the supply amount of a stock solution is small, and a filtration facility provided with the filter aid adding device. The purpose is to do.
Another object of the present invention is to provide a method for adding a filter aid that can appropriately control the amount of the filter aid even when the supply amount of the stock solution is small.

第1発明の濾過助剤添加装置は、濾過機に供給される前の原液が一時的に貯留される添加槽に粉体の濾過助剤を添加する粉体供給機と、前記添加槽に供給される前記原液の流量を測定する流量計と、前記粉体供給機の動作を制御する制御装置と、を備え、前記制御装置は、前記流量計の測定値に基づいて、前記添加槽への前記原液の積算流量を求め、前記積算流量が目標量に達するたびに、前記粉体供給機を動作させて該目標量の前記原液に見合う量の前記濾過助剤を排出させ、停止させることを特徴とする。
第2発明の濾過設備は、第1発明の濾過助剤添加装置と、前記添加槽と、前記濾過機と、を備えることを特徴とする。
第3発明の濾過設備は、第2発明において、前記添加槽から排出された原液を一時的に貯留し、撹拌する撹拌槽を備えることを特徴とする。
第4発明の濾過助剤添加方法は、粉体供給機を用いて、濾過機に供給される前の原液が一時的に貯留される添加槽に粉体の濾過助剤を添加する方法であって、前記添加槽への前記原液の積算流量が目標量に達するたびに、前記粉体供給機を動作させて該目標量の前記原液に見合う量の前記濾過助剤を排出させ、停止させることを特徴とする。
A filter aid adding apparatus according to a first aspect of the present invention includes a powder feeder for adding a powdery filter aid to an addition tank in which a stock solution before being supplied to a filter is temporarily stored, A flow meter for measuring the flow rate of the undiluted solution, and a control device for controlling the operation of the powder feeder, wherein the control device, based on the measurement value of the flow meter, to the addition tank Obtaining the integrated flow rate of the stock solution, every time the integrated flow reaches the target amount, operating the powder feeder to discharge an amount of the filter aid corresponding to the target amount of the stock solution, and stopping. Features.
The filtration equipment of the second invention is characterized by comprising the filter aid addition device of the first invention, the addition tank, and the filter.
The filtration equipment of the third invention is characterized in that, in the second invention, a stirring tank for temporarily storing and stirring the stock solution discharged from the addition tank is provided.
The filter aid adding method of the fourth invention is a method of adding a powder filter aid to an addition tank in which a stock solution before being supplied to the filter is temporarily stored using a powder feeder. Every time the integrated flow rate of the stock solution to the addition tank reaches a target amount, operating the powder feeder to discharge an amount of the filter aid corresponding to the target amount of the stock solution and stop the process. It is characterized by.

なお、本明細書において、「流量」は、単位時間当たりに流れる流体の量を意味する。「積算流量」は、特定の期間に流れる流体の積算量を意味する。「供給量」は、特定箇所に供給される流体の流量を意味する。「添加速度」は、単位時間当たりに添加される物質の量を意味する。「添加量」は、特定の期間に添加される物質の積算量を意味する。「排出速度」は、単位時間当たりに特定箇所から排出される物質の量を意味する。   In the present specification, “flow rate” means the amount of fluid flowing per unit time. “Integrated flow rate” means the integrated amount of fluid flowing in a specific period. “Supply amount” means the flow rate of a fluid supplied to a specific location. "Addition rate" means the amount of substance added per unit time. “Addition amount” means an integrated amount of a substance added in a specific period. “Discharge rate” means the amount of a substance discharged from a specific location per unit time.

第1発明によれば、粉体供給機を間欠的に運転することで、濾過助剤の平均的な添加量を低減でき、原液の供給量が少ない場合であっても、濾過助剤の添加量を適切に制御できる。
第2発明によれば、濾過助剤の添加量が過剰にならないので、原液を効率よく濾過できる。
第3発明によれば、濾過助剤が添加された原液を撹拌槽で再度撹拌するので、濾過助剤を間欠的に添加しても、濾過機に供給される原液の濾過助剤濃度を均一にできる。
第4発明によれば、粉体供給機を間欠的に運転することで、濾過助剤の平均的な添加量を低減でき、原液の供給量が少ない場合であっても、濾過助剤の添加量を適切に制御できる。
According to the first invention, by operating the powder feeder intermittently, the average addition amount of the filter aid can be reduced, and even when the supply amount of the stock solution is small, the addition of the filter aid is performed. The amount can be controlled appropriately.
According to the second invention, since the amount of the filter aid added does not become excessive, the stock solution can be efficiently filtered.
According to the third invention, since the stock solution to which the filter aid has been added is again stirred in the stirring tank, even if the filter aid is intermittently added, the concentration of the filter aid in the stock solution supplied to the filter is made uniform. Can be.
According to the fourth aspect of the present invention, by operating the powder feeder intermittently, the average amount of the filter aid can be reduced. The amount can be controlled appropriately.

本発明の一実施形態に係る濾過設備の説明図である。It is explanatory drawing of the filtration equipment which concerns on one Embodiment of this invention. 原液の積算流量の時間変化と、濾過助剤の添加タイミングとを示したグラフである。It is the graph which showed the time change of the integrated flow rate of stock solution, and the addition timing of a filter aid.

つぎに、本発明の実施形態を図面に基づき説明する。
(濾過設備)
図1に示すように、本発明の一実施形態に係る濾過設備AAは、原液を濾過して、濾液と残渣とを得る設備である。原液は濾過対象の液体であり、濾過により除去される懸濁物質が含まれている。原液は、例えば、特定のプロセスで発生する排液である。この場合、濾過設備AAへの原液の供給量は、そのプロセスにおける排液の発生量に依存する。
Next, an embodiment of the present invention will be described with reference to the drawings.
(Filtration equipment)
As shown in FIG. 1, a filtration facility AA according to one embodiment of the present invention is a facility that filters a stock solution to obtain a filtrate and a residue. The undiluted liquid is a liquid to be filtered, and contains suspended substances removed by filtration. The undiluted solution is, for example, a drainage generated in a specific process. In this case, the supply amount of the undiluted solution to the filtration facility AA depends on the amount of drainage generated in the process.

原液は、まず、貯留槽21に一時的に貯留される。貯留槽21は配管31を介して添加槽22に接続されている。配管31に設けられたポンプ32の駆動により、貯留槽21から添加槽22に原液が移送される。   The stock solution is first temporarily stored in the storage tank 21. The storage tank 21 is connected to the addition tank 22 via a pipe 31. The undiluted solution is transferred from the storage tank 21 to the addition tank 22 by driving a pump 32 provided in the pipe 31.

原液は添加槽22に一時的に貯留される。濾過助剤添加装置1により添加槽22に濾過助剤が添加される。添加槽22には撹拌機が設けられている。撹拌機により原液が撹拌され、濾過助剤が分散する。濾過助剤として、特に限定されないが、珪藻土、パーライトなどが用いられる。   The stock solution is temporarily stored in the addition tank 22. The filter aid is added to the addition tank 22 by the filter aid adding device 1. The addition tank 22 is provided with a stirrer. The stock solution is stirred by the stirrer, and the filter aid is dispersed. The filter aid is not particularly limited, but diatomaceous earth, perlite and the like are used.

添加槽22の下流には、撹拌槽23、24が設けられている。添加槽22と撹拌槽23、24とは直列に接続されている。添加槽22から排出された原液は第1の撹拌槽23に供給され、第1の撹拌槽23から排出された原液は第2の撹拌槽24に供給される。原液の移送は、例えば、オーバーフローにより行なわれる。撹拌槽23、24には撹拌機が設けられている。撹拌槽23、24は濾過助剤を含む原液を一時的に貯留するとともに、撹拌して濾過助剤を分散する。   Downstream of the addition tank 22, stirring tanks 23 and 24 are provided. The addition tank 22 and the stirring tanks 23 and 24 are connected in series. The stock solution discharged from the addition tank 22 is supplied to a first stirring tank 23, and the stock solution discharged from the first stirring tank 23 is supplied to a second stirring tank 24. The transfer of the stock solution is performed, for example, by overflow. The stirring tanks 23 and 24 are provided with a stirrer. The stirring tanks 23 and 24 temporarily store the stock solution containing the filter aid and stir to disperse the filter aid.

なお、本実施形態では、2つの撹拌槽23、24が設けられている。したがって、添加槽22と撹拌槽23、24とを合わせて3つの槽が直列に接続されている。その分、原液の滞留時間が長くなり、濾過助剤を均一に分散できる。撹拌槽23、24の数は特に限定されない、1つでもよいし、3つ以上でもよい。また、撹拌槽23、24を設けなくてもよい。   In this embodiment, two stirring tanks 23 and 24 are provided. Therefore, three tanks including the addition tank 22 and the stirring tanks 23 and 24 are connected in series. As a result, the residence time of the stock solution becomes longer, and the filter aid can be dispersed uniformly. The number of the stirring tanks 23 and 24 is not particularly limited, and may be one or three or more. Further, the stirring tanks 23 and 24 need not be provided.

最終段の撹拌槽24は配管33を介して濾過機25に接続されている。配管33に設けられたポンプ34の駆動により、撹拌槽24から濾過機25に原液が移送される。原液は濾過機25により濾過される。濾過機25からは濾液と残渣とが排出される。濾過機25の種類は特に限定されない。濾過機25として、例えば、フィルタープレスが用いられる。   The stirring tank 24 at the last stage is connected to a filter 25 via a pipe 33. The undiluted solution is transferred from the stirring tank 24 to the filter 25 by the drive of the pump 34 provided in the pipe 33. The stock solution is filtered by the filter 25. The filtrate and the residue are discharged from the filter 25. The type of the filter 25 is not particularly limited. As the filter 25, for example, a filter press is used.

濾過機25には濾過助剤を含む原液が供給される。濾過助剤の作用により、濾過機25の濾過速度が向上するとともに、濾過の継続時間が延びる。なお、予め濾過助剤を分散させた原液を濾過機25に通して濾過する操作を「ボディフィード」と称する。本実施形態の濾過設備AAはボディフィードを行なう。   A stock solution containing a filter aid is supplied to the filter 25. The action of the filter aid improves the filtration speed of the filter 25 and extends the duration of filtration. The operation of filtering a stock solution in which a filter aid is dispersed in advance through a filter 25 is referred to as “body feed”. The filtration equipment AA of the present embodiment performs a body feed.

原液の濾過に先立ち、濾過助剤を分散させた清澄液を濾過機25に通して、濾材表面に濾過助剤の層を形成する操作を「プリコート」と称する。ボディフィードと共に、プリコートを行なってもよい。   Prior to the filtration of the undiluted solution, an operation of passing the clarified liquid in which the filter aid is dispersed through a filter 25 to form a layer of the filter aid on the surface of the filter medium is referred to as “precoating”. Pre-coating may be performed together with the body feed.

(濾過助剤添加装置)
つぎに、濾過助剤添加装置1の構成を説明する。
濾過助剤添加装置1は粉体供給機11を有する。粉体供給機11は内部に保持した粉体を切り出して排出する装置である。粉体供給機11の構成は特に限定されないが、粉体を保持するホッパーと、ホッパーの下部に設けられた排出部とを有することが一般的である。排出部として、ロータリーバルブ、スクリューコンベア、フライトコンベア、テーブルフィーダなどがある。排出部を駆動する電動機の回転速度を調整することで、粉体の排出速度を調整できる。粉体供給機11には粉体の濾過助剤が保持されている。粉体供給機11は濾過助剤を粉体のまま添加槽22に添加する。
(Filter aid addition device)
Next, the configuration of the filter aid adding device 1 will be described.
The filter aid adding device 1 has a powder feeder 11. The powder feeder 11 is a device for cutting out and discharging the powder held inside. Although the configuration of the powder feeder 11 is not particularly limited, it generally includes a hopper for holding powder and a discharge unit provided below the hopper. The discharge unit includes a rotary valve, a screw conveyor, a flight conveyor, a table feeder, and the like. The discharge speed of the powder can be adjusted by adjusting the rotation speed of the electric motor that drives the discharge unit. The powder feeder 11 holds a powder filter aid. The powder feeder 11 adds the filter aid to the addition tank 22 as powder.

濾過助剤添加装置1は流量計12を有する。流量計12は配管31を流れる原液の流量、すなわち、添加槽22に供給される原液の流量を測定する。また、濾過助剤添加装置1は粉体供給機11の動作を制御する制御装置13を有する。流量計12の測定値は制御装置13に入力されている。制御装置13は流量計12の測定値に基づき、粉体供給機11の動作を制御する。より詳細には、制御装置13は粉体供給機11の排出部を駆動する電動機の回転速度を調整して、濾過助剤の排出速度を調整する。   The filter aid adding device 1 has a flow meter 12. The flow meter 12 measures the flow rate of the stock solution flowing through the pipe 31, that is, the flow rate of the stock solution supplied to the addition tank 22. The filter aid adding device 1 has a control device 13 for controlling the operation of the powder feeder 11. The measurement value of the flow meter 12 is input to the control device 13. The control device 13 controls the operation of the powder feeder 11 based on the measurement value of the flow meter 12. More specifically, the control device 13 adjusts the rotation speed of the electric motor that drives the discharge unit of the powder feeder 11 to adjust the discharge speed of the filter aid.

一般に、濾過助剤は、清澄液に分散させた後、その液を原液に添加する。これに対して本実施形態の濾過助剤添加装置1は、濾過助剤を粉体のまま原液に添加する。そのため、濾過助剤を清澄液に分散させる設備、すなわち、タンク、撹拌機などが必要ない。そのため、濾過設備AAの設備コストを低減できるとともに、省スペース化できる。   Generally, a filter aid is added to a stock solution after it is dispersed in a clear solution. On the other hand, the filter aid adding device 1 of the present embodiment adds the filter aid to the stock solution as a powder. Therefore, equipment for dispersing the filter aid in the clarified liquid, that is, a tank, a stirrer or the like is not required. Therefore, the equipment cost of the filtration equipment AA can be reduced, and the space can be saved.

(濾過助剤添加方法)
つぎに、濾過助剤添加装置1による濾過助剤の添加方法を説明する。
濾過助剤の添加速度fは、原液の濾過助剤濃度ρが目標濃度ρtになるよう調整される。ここで、濾過助剤の目標濃度ρtは、原液の濾過助剤濃度ρとして最適な値に設定される。濾過助剤の目標濃度ρtは予め試験などにより求められる。原液の流量をiとすると、濾過助剤の目標添加速度ftは式(1)で表わされる。式(1)から分かるように、原液の流量iの増減にあわせて、濾過助剤の添加速度fを増減させればよい。
t=ρt・i ・・・(1)
(How to add filter aid)
Next, a method of adding a filter aid by the filter aid adding apparatus 1 will be described.
The addition speed f of the filter aid is adjusted so that the concentration ρ of the stock filter aid becomes the target concentration ρ t . Here, the target concentration ρ t of the filter aid is set to an optimum value as the filter aid concentration ρ of the stock solution. The target concentration ρ t of the filter aid is determined in advance by a test or the like. When the flow rate of the stock solution and i, the target addition speed f t of the filter aid is represented by the formula (1). As can be seen from equation (1), the addition rate f of the filter aid may be increased or decreased in accordance with the increase or decrease in the flow rate i of the stock solution.
f t = ρ t · i (1)

ところが、原液の流量iが少なすぎると、粉体供給機11の排出速度を下限に設定しても、濾過助剤の添加速度fが目標添加速度ftよりも速くなることがある。この場合、濾過助剤を過剰に添加してしまうことになる。 However, when the flow rate i undiluted is too small, also the discharge rate of the powder feeder 11 is set to the lower limit, there is that the addition rate f of the filter aid is faster than the target addition speed f t. In this case, a filter aid will be added excessively.

なお、一般的に行なわれているように、濾過助剤を分散させた清澄液(以下、「濾過助剤分散液」と称する。)を原液に添加する場合には、上記の問題は生じない。この場合には、濾過助剤分散液の濾過助剤濃度を調整できることに加え、濾過助剤分散液の添加速度をポンプの排出量で調整できることから、原液への濾過助剤の添加速度の調整幅が大きいからである。   In addition, when a clear liquid in which a filter aid is dispersed (hereinafter, referred to as a “filter aid dispersion”) is added to a stock solution, the above problem does not occur, as is generally performed. . In this case, in addition to being able to adjust the filter aid concentration of the filter aid dispersion, the addition rate of the filter aid dispersion can be adjusted by the discharge amount of the pump, so that the rate of addition of the filter aid to the stock solution can be adjusted. This is because the width is large.

本実施形態の濾過助剤添加装置1は、連続的に供給される原液に対して、濾過助剤を間欠的に添加する。これにより、濾過助剤の時間平均的な添加量を低減して、原液の濾過助剤濃度ρを目標濃度ρtに調整する。具体的には、以下に説明する制御を行なう。 The filter aid adding apparatus 1 of the present embodiment intermittently adds a filter aid to a continuously supplied stock solution. Thus, the time-average addition amount of the filter aid is reduced, and the filter aid concentration ρ of the stock solution is adjusted to the target concentration ρ t . Specifically, the control described below is performed.

制御装置13には流量計12の測定値(原液の流量i)が入力されている。制御装置13は、流量計12の測定値iに基づいて、添加槽22への原液の積算流量Iを求める。ここで、積算流量Iは原液の流量iを時間積分して求められる。   The measured value of the flow meter 12 (the flow rate i of the undiluted solution) is input to the control device 13. The controller 13 obtains the integrated flow rate I of the stock solution into the addition tank 22 based on the measurement value i of the flow meter 12. Here, the integrated flow rate I is obtained by integrating the flow rate i of the stock solution with time.

図2のグラフに示すように、積算流量Iは時間の経過とともに増加する。図2のグラフにおいてItは目標量である。目標量Itは予め制御装置13に設定されている。制御装置13は時刻t=0から流量iの積分を開始して積算流量Iを求める。制御装置13は積算流量Iが目標量Itに達したら、積算流量Iの値を0に戻し、再び流量iの積分を開始して積算流量Iを求める。 As shown in the graph of FIG. 2, the integrated flow rate I increases over time. I t In the graph of FIG. 2 is a target amount. Target amount I t is set in advance controller 13. The control device 13 starts integration of the flow rate i from time t = 0 to obtain the integrated flow rate I. When the control device 13 integrated flow I reaches the target amount I t, the value of the accumulated flow rate I returned to 0 to obtain the integrated flow I to start integrating again flow i.

制御装置13は積算流量Iが目標量Itに達するたびに、粉体供給機11を動作させて、濾過助剤を添加槽22に添加する。この際、粉体供給機11は目標量Itの原液に見合う量(以下、「目標添加量Ft」と称する。)の濾過助剤を添加する。ここで、濾過助剤の目標添加量Ftは、目標量Itの原液の濾過助剤濃度ρが目標濃度ρtとなる量である。濾過助剤の目標添加量Ftは式(2)で表わされる。
t=ρt・It ・・・(2)
The control device 13 each time the accumulated flow I reaches the target amount I t, the powder feeder 11 is operated, the addition of a filter aid addition tank 22. In this case, the powder feeder 11 is an amount commensurate with the stock solution of the target quantity I t (hereinafter, referred to as "the target addition amount F t".) Is added a filtration aid. Here, the target amount F t of the filter aid is that amount which filter aid concentration of the stock solution of the target quantity I t [rho is the target density [rho t. Target addition amount F t of the filter aid is represented by the formula (2).
F t = ρ t · I t (2)

制御装置13は、積算流量Iが目標量Itに達するたびに、粉体供給機11から目標添加量Ftの濾過助剤を排出させ、停止させる。ここで、粉体供給機11の排出速度は下限に設定してもよいし、下限でなくてもよい。粉体供給機11の動作時間は、排出速度と目標添加量Ftとから求められる。 Controller 13, the integrated each time the flow I reaches the target amount I t, from the powder feeder 11 is discharged filter aid target addition amount F t, is stopped. Here, the discharge speed of the powder feeder 11 may be set to the lower limit or may not be the lower limit. Operating time of the powder feeder 11 is determined from the discharge speed and the target amount F t.

以上のように、濾過助剤添加装置1は粉体供給機11を間欠的に運転する。これにより、濾過助剤の平均的な添加量を低減できる。そのため、原液の供給量が少ない場合であっても、濾過助剤の添加量を適切に制御できる。濾過助剤の添加量が過剰にならないので、原液を効率よく濾過できる。   As described above, the filter aid adding device 1 operates the powder feeder 11 intermittently. Thereby, the average addition amount of the filter aid can be reduced. Therefore, even when the supply amount of the stock solution is small, the addition amount of the filter aid can be appropriately controlled. Since the addition amount of the filter aid does not become excessive, the stock solution can be efficiently filtered.

ところで、原液に対して濾過助剤を間欠的に添加すると、原液の濾過助剤濃度が時間的に変動する恐れがある。濾過助剤を添加する時間間隔を、添加槽22における原液の滞留時間よりも十分に短くすれば、原液の濾過助剤濃度の変動を抑えることができる。濾過助剤を添加する時間間隔は、目標量Itにより調整できる。目標量Itを添加槽22の有効容積の1/2以下とすることが好ましい。そうすれば、濾過助剤を添加する時間間隔を、添加槽22における原液の平均滞留時間の1/2以下にでき、原液の濾過助剤濃度の変動を抑えることができる。 By the way, if the filter aid is intermittently added to the stock solution, the concentration of the filter aid in the stock solution may fluctuate with time. If the time interval for adding the filter aid is sufficiently shorter than the residence time of the stock solution in the addition tank 22, fluctuations in the concentration of the filter aid in the stock solution can be suppressed. Time interval for adding a filter aid can be adjusted by the target quantity I t. It is preferred that less than half of the effective volume of the addition tank 22 the target quantity I t. By doing so, the time interval for adding the filter aid can be made equal to or less than の of the average residence time of the stock solution in the addition tank 22, and fluctuations in the filter aid concentration of the stock solution can be suppressed.

また、本実施形態の濾過設備AAは、添加槽22の下流に撹拌槽23、24が接続されている。濾過助剤が添加された原液を撹拌槽23、24で再度撹拌するので、濾過助剤を間欠的に添加しても、濾過機25に供給される原液の濾過助剤の濃度を均一にできる。   Further, in the filtration equipment AA of the present embodiment, stirring tanks 23 and 24 are connected downstream of the addition tank 22. Since the stock solution to which the filter aid has been added is again stirred in the stirring tanks 23 and 24, even if the filter aid is intermittently added, the concentration of the stock solution supplied to the filter 25 can be made uniform. .

〔その他の実施形態〕
上記実施形態では、制御装置13が粉体供給機11の動作を自動的に制御したが、これに代えて、作業員が粉体供給機11の動作を制御してもよい。この場合、作業員は流量計12の測定値に基づき、適切なタイミングで粉体供給機11を間欠的に動作させる。
[Other embodiments]
In the above-described embodiment, the control device 13 automatically controls the operation of the powder feeder 11, but instead, the operator may control the operation of the powder feeder 11. In this case, the operator intermittently operates the powder feeder 11 at an appropriate timing based on the measurement value of the flow meter 12.

AA 濾過設備
1 濾過助剤添加装置
11 粉体供給機
12 流量計
13 制御装置
21 貯留槽
22 添加槽
23 撹拌槽
24 撹拌槽
25 濾過機
AA filtration equipment 1 filtration aid addition device 11 powder supply device 12 flow meter 13 control device 21 storage tank 22 addition tank 23 stirring tank 24 stirring tank 25 filtration machine

Claims (4)

濾過機に供給される前の原液が一時的に貯留される添加槽に粉体の濾過助剤を添加する粉体供給機と、
前記添加槽に供給される前記原液の流量を測定する流量計と、
前記粉体供給機の動作を制御する制御装置と、を備え、
前記制御装置は、
前記流量計の測定値に基づいて、前記添加槽への前記原液の積算流量を求め、
前記積算流量が目標量に達するたびに、前記粉体供給機を動作させて該目標量の前記原液に見合う量の前記濾過助剤を排出させ、停止させる
ことを特徴とする濾過助剤添加装置。
A powder feeder for adding a powder filter aid to an addition tank in which the stock solution before being supplied to the filter is temporarily stored,
A flow meter for measuring the flow rate of the stock solution supplied to the addition tank,
A control device for controlling the operation of the powder feeder,
The control device includes:
Based on the measurement value of the flow meter, determine the integrated flow rate of the stock solution to the addition tank,
Each time the integrated flow rate reaches a target amount, a filter aid adding device that operates the powder feeder to discharge an amount of the filter aid corresponding to the target amount of the stock solution, and stops the filter aid. .
請求項1記載の濾過助剤添加装置と、
前記添加槽と、
前記濾過機と、を備える
ことを特徴とする濾過設備。
A filter aid adding device according to claim 1,
Said addition tank,
And a filtration device.
前記添加槽から排出された原液を一時的に貯留し、撹拌する撹拌槽を備える
ことを特徴とする請求項2記載の濾過設備。
3. The filtration equipment according to claim 2, further comprising a stirring tank for temporarily storing and stirring the stock solution discharged from the addition tank.
粉体供給機を用いて、濾過機に供給される前の原液が一時的に貯留される添加槽に粉体の濾過助剤を添加する方法であって、
前記添加槽への前記原液の積算流量が目標量に達するたびに、前記粉体供給機を動作させて該目標量の前記原液に見合う量の前記濾過助剤を排出させ、停止させる
ことを特徴とする濾過助剤添加方法。
Using a powder feeder, a method of adding a powder filter aid to an addition tank in which the stock solution before being supplied to the filter is temporarily stored,
Each time the integrated flow rate of the stock solution to the addition tank reaches a target amount, the powder feeder is operated to discharge an amount of the filter aid corresponding to the target amount of the stock solution, and to stop. Method of adding a filter aid.
JP2018155913A 2018-08-23 2018-08-23 Filtration aid addition device, filtration equipment and filtration aid addition method Active JP7031531B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2018155913A JP7031531B2 (en) 2018-08-23 2018-08-23 Filtration aid addition device, filtration equipment and filtration aid addition method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2018155913A JP7031531B2 (en) 2018-08-23 2018-08-23 Filtration aid addition device, filtration equipment and filtration aid addition method

Publications (2)

Publication Number Publication Date
JP2020028855A true JP2020028855A (en) 2020-02-27
JP7031531B2 JP7031531B2 (en) 2022-03-08

Family

ID=69623416

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2018155913A Active JP7031531B2 (en) 2018-08-23 2018-08-23 Filtration aid addition device, filtration equipment and filtration aid addition method

Country Status (1)

Country Link
JP (1) JP7031531B2 (en)

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS56121604A (en) * 1980-01-28 1981-09-24 Schneider Co Inc J R Improved filter
US4514306A (en) * 1982-12-15 1985-04-30 Monarch Wine Co., Inc. Method of and apparatus for controlling the quantity of filter aid fed to a sediment filter so as to maintain virtually constant a preselected optimum specific cake resistance
JPS6253717A (en) * 1985-09-02 1987-03-09 Mitaka Kogyosho:Kk Device for feeding filter aid for filter
JPH0316611A (en) * 1989-06-12 1991-01-24 Nec Corp Filter
JP2003334407A (en) * 2002-05-17 2003-11-25 Sumitomo Metal Mining Co Ltd Rainwater draining treatment method

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS56121604A (en) * 1980-01-28 1981-09-24 Schneider Co Inc J R Improved filter
US4514306A (en) * 1982-12-15 1985-04-30 Monarch Wine Co., Inc. Method of and apparatus for controlling the quantity of filter aid fed to a sediment filter so as to maintain virtually constant a preselected optimum specific cake resistance
JPS6253717A (en) * 1985-09-02 1987-03-09 Mitaka Kogyosho:Kk Device for feeding filter aid for filter
JPH0316611A (en) * 1989-06-12 1991-01-24 Nec Corp Filter
JP2003334407A (en) * 2002-05-17 2003-11-25 Sumitomo Metal Mining Co Ltd Rainwater draining treatment method

Also Published As

Publication number Publication date
JP7031531B2 (en) 2022-03-08

Similar Documents

Publication Publication Date Title
EP1873123B1 (en) Sludge concentration device
JP6003300B2 (en) Vacuum filtration apparatus and operation method thereof
JP2020028855A (en) Filter aid addition device, filtration facility and filter aid addition method
CN116036997A (en) Accurate dosing equipment based on municipal wastewater treatment system and application method
RU2322283C2 (en) Device for automatic control of water cleaning process
CN100549837C (en) Developing apparatus, developing method and developer circulating method
CN217745975U (en) Diatomite filtering system
US4001115A (en) Filtration system with storage and dilution reservoirs
RU2484880C2 (en) Method and system of reducing quantity of particles
CN104271222A (en) Slurry production apparatus and slurry production method
JP2011230019A5 (en)
JP5327159B2 (en) Sludge concentration and dehydration system and control method thereof
KR101818438B1 (en) Filter performance evaluation device
CN103488199B (en) Defoaming mechanism input and output material controls Apparatus and method for
KR101627483B1 (en) Pressurized Treating Water System
JPH0744444Y2 (en) Polishing waste liquid treatment device
JP5084991B2 (en) Sludge blanket layer stabilization method and coagulation sedimentation equipment
CN217527196U (en) Corrosion and scale inhibitor dosing device
CN216264891U (en) Online filtration and recycling system for diamond wire cutting liquid
JP2022185389A (en) Water treatment device
CN106943798A (en) Filter method for filtered fluid and the filter for filtered fluid
CN120276503A (en) Liquid quality control method, device and liquid output device
JP2003290607A (en) Method for adjusting supply amount of liquid to be treated and flocculation and sedimentation equipment
JP6429745B2 (en) Solid-liquid separation system and flocking device
CN115991393A (en) A vibration control method for quantitative feeding of shrimp and crab granular bait

Legal Events

Date Code Title Description
A621 Written request for application examination

Free format text: JAPANESE INTERMEDIATE CODE: A621

Effective date: 20210322

A977 Report on retrieval

Free format text: JAPANESE INTERMEDIATE CODE: A971007

Effective date: 20220114

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: 20220125

A61 First payment of annual fees (during grant procedure)

Free format text: JAPANESE INTERMEDIATE CODE: A61

Effective date: 20220207

R150 Certificate of patent or registration of utility model

Ref document number: 7031531

Country of ref document: JP

Free format text: JAPANESE INTERMEDIATE CODE: R150