JPS5980311A - Magnetic filter apparatus - Google Patents
Magnetic filter apparatusInfo
- Publication number
- JPS5980311A JPS5980311A JP18974682A JP18974682A JPS5980311A JP S5980311 A JPS5980311 A JP S5980311A JP 18974682 A JP18974682 A JP 18974682A JP 18974682 A JP18974682 A JP 18974682A JP S5980311 A JPS5980311 A JP S5980311A
- Authority
- JP
- Japan
- Prior art keywords
- magnetic
- raw water
- water
- purified water
- 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.)
- Pending
Links
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03C—MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03C1/00—Magnetic separation
- B03C1/02—Magnetic separation acting directly on the substance being separated
- B03C1/025—High gradient magnetic separators
- B03C1/031—Component parts; Auxiliary operations
- B03C1/032—Matrix cleaning systems
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03C—MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03C1/00—Magnetic separation
- B03C1/02—Magnetic separation acting directly on the substance being separated
- B03C1/025—High gradient magnetic separators
Landscapes
- Water Treatment By Electricity Or Magnetism (AREA)
Abstract
Description
【発明の詳細な説明】
本発明は、磁気フィルター装置に関Mる。さらに詳しく
は本光明は磁性成分を含む被処理原水から、ぞの導入品
または磁場を形成さける励磁]1イルへの電流を調11
)りることにJ、す1社性成分を効率にり分11111
−!lる磁気フィルター装置に係わるものである。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a magnetic filter device. More specifically, this Komei adjusts the electric current from the raw water to be treated containing magnetic components to the introduced product or the excitation to avoid forming a magnetic field.
) Rinni J, S1 company's ingredients in efficiency ratio 11111
-! This relates to a magnetic filter device.
従来、例えば高Ujスクフバー廃水、転炉スクラバー廃
水等の産業廃水から鉄分のようなMll酸成分回収Jる
のに好適な装置どして磁気フィルターが知られでいる。Magnetic filters have been known as devices suitable for recovering Mll acid components such as iron from industrial wastewater such as high Uj scrubber wastewater and converter scrubber wastewater.
近イ1.11気ノイルターの応用11む囲が拡大され、
例えば、紙パルブ工場廃水、化学工場廃水、下水中の浮
遊固型物を含有りる下水、活性汚泥処即水のようなバク
テリア金石廃液、有用微生物を含む醗酵液等、右11性
の非1ti 11+成分を含む原水に、例えば硫酸ばん
土、高分子凝集剤等を加えC史にこれにマグネタイl−
(、r”e20aよりなる磁性粒子(以干磁竹成分と呼
ぶ)を添加して強固に結合さゼ、いわゆる磁性760ツ
クを形成させ゛(磁気フィルターで捕捉し、分離した磁
す11)11ツクを逆洗して濃縮状態にし再度、磁気フ
ィルターで処理しく非磁性成分ど磁性成分とに分離し、
磁性成分は回収再生し、非磁性成分のうち、不要なもの
は廃棄し、有用41シのは回収Jるなどの手段にも利用
され(いる。Near 1.11 Application 11 area of Noirter has been expanded,
For example, wastewater from a paper pulp factory, chemical factory wastewater, sewage containing suspended solids in sewage, bacterial goldstone wastewater such as activated sludge treatment ready water, fermentation liquid containing useful microorganisms, etc. For example, sulfuric acid salt, polymer flocculant, etc. are added to raw water containing 11+ components, and magnetite l-
(Magnetic particles consisting of r''e20a (hereinafter referred to as magnetic bamboo component) are added to form a so-called magnetic 760 block. (Magnetic particles captured and separated with a magnetic filter 11) The tsuku is backwashed, concentrated, and treated again with a magnetic filter to separate non-magnetic and magnetic components.
Magnetic components are recovered and recycled, unnecessary non-magnetic components are discarded, and useful 41 components are recovered.
磁気フィルターには各種の型式のものが提案されている
。第1図に承りものは、磁気フィルターの一例を承り概
要図で、原水の導入と、逆洗水の排出を兼ねる流入口2
と、磁性成分を除去した後の浄化処理水の流出と、逆洗
水導入を兼ねる流出1−13を備えたフィルターへセル
4内に、例えば磁性祠判のIll FAからなる多層メ
ッシコのノイルターメディア5、フィルターメディア5
に均一な磁場を発生さIるポールピース6が内装され、
フィルターベレル4の外側にはノイルターメディア5を
囲/υで励磁1イル7をJj <と几に、該励磁コイル
7を囲むよ゛)にし′C磁力線を導くリターンフレーム
8を設()(なるものeある。Various types of magnetic filters have been proposed. Figure 1 shows a schematic diagram of an example of a magnetic filter.
Then, a multilayer mesh noilter made of Ill FA of a magnetic scale, for example, is installed in the cell 4 to a filter equipped with an outflow 1-13 that serves as an outflow of purified water after removing magnetic components and an outflow 1-13 that also serves as an introduction of backwash water. Media 5, filter media 5
A pole piece 6 is installed inside to generate a uniform magnetic field,
On the outside of the filter bellel 4, a return frame 8 is installed to surround the excitation coil 7 with /υ and the excitation coil 7 with /υ so as to surround the excitation coil 7. There is something e.
以」−のような構造からなる磁気フィルターに、例えば
高炉スクラバー廃水のにうな鉄分を含む原水を導入して
鉄分を捕捉したり、パルプ工場廃水に磁性成分を加え゛
C11:磁性成分と結合させた磁性)[1ツクを含む原
水を導入して磁性フロックを捕捉したり、磁性)Uツク
を含む原水スラリーをう9人して磁性成分と非磁性成分
とを分mt L、たりする場合においては次のようなこ
とがいえる。For example, raw water containing iron, such as blast furnace scrubber wastewater, may be introduced into a magnetic filter with a structure similar to the above to capture iron, or a magnetic component may be added to pulp mill wastewater and combined with the magnetic component. In the case of introducing raw water containing 1 (magnetic) to capture magnetic flocs, or adding raw water slurry containing 1 (magnetic) to 9 mt L to separate the magnetic and non-magnetic components, The following can be said.
づなわら、磁気フrルターの操作面からみると、磁場の
出力を上げた場合、および原水の導入量を下げた場合は
フィルターメディアでの磁性成分の捕捉率はよい。づな
わち、Jtl J)i:!きれない磁性成分の処理浄化
水(濾過IJj液)への移行は減少するから磁性成分の
捕捉率のみからガロした場合、磁気フィルターへの性能
は充分発揮されるといえるが反面、供給電力用の増加や
原水処即準の低下を1r?くので操業−1ストは」−昇
する。一方、Ill場の出力を下げ、原水39人8を上
げた場合は操業コストは低下するものの磁性成分のノイ
ルターメディアにd3 LJる捕捉率は低下り゛る。さ
らに、原水導入fnおよび磁場出力を一定にしてll1
1竹成分をフィルターメディアに捕捉さヒ゛る操作を行
う場合の処理浄化水の水質をみると、原水の導入直後は
処I!I+浄化水中へのIll lll成分の移行が人
e < r4& t/l成分のフィルターメゾイノ′に
よる捕捉率は劣る。しかし原水の導入が一定11、)間
軒過りるどこの現象はFlv潤して、141 lll成
分はi「常に捕捉されるが、更に、原水の導入を杖りる
ど、フィルターメディアが、Jolt IIされた磁性
成分に、J:すl″l詰りし、原水の導入は困難となり
、逆洗ににる(0性成分の除去を必要とするに至る。However, from the operational point of view of the magnetic filter, the capture rate of magnetic components in the filter media is good when the output of the magnetic field is increased and when the amount of raw water introduced is decreased. That is, Jtl J)i:! Since the transfer of unrefined magnetic components to treated purified water (filtered IJJ liquid) is reduced, it can be said that the performance of the magnetic filter is fully demonstrated when considering only the capture rate of magnetic components. Increase or decrease in raw water treatment standard by 1r? Therefore, the operation - 1st strike will be increased. On the other hand, if the output of the Ill field is lowered and the raw water is increased, the operating cost will decrease, but the capture rate of d3LJ in the magnetic component Noir Tarmedia will decrease. Furthermore, with the raw water introduction fn and the magnetic field output constant, ll1
Looking at the water quality of treated purified water when carrying out an operation in which bamboo components are captured in filter media, it is found that immediately after raw water is introduced, it is treated as I! The transfer of the Ill lll components into the I+ purified water is less than e < r4 & the capture rate of the t/l components by the filter mesoino' is poor. However, when the introduction of raw water is constant11), this phenomenon occurs when the Flv is moistened, and the 141 lll components are always captured. J: 1''l is clogged with the magnetic components, making it difficult to introduce raw water and requiring backwashing (removal of the zero component).
以上のような原水導入時のフィルターメディアにおりる
磁性成分の捕捉状態の変化を推定すると、恐らく拡大図
で示−り第2図Δ〜D I) 、にうになるしのど考え
られる。Jなわら、原水導入開始直後の状態は第2図Δ
の如くで、フィルターメディアを構成する磁性ml線5
8に原水の流れ方向く矢印で示J)と甲f−j L t
l&M成分粒子が連なって捕捉され、1ift fl柑
線5aの間隙を磁性成分(イ)の一部捕捉2\1しない
まま原水の流れにのり【フリーパスJる1、原水の導入
が一定時間経過後に第2図Bのように磁性細線5aの間
隙が磁性成分粒子で充填されl、:状態となり原水中の
磁性成分(イ)はりべて磁性細線j a間隙にUきとめ
られ、原水の流れにのっく捕1)?されないまま処理浄
化水側に移行りることかない。11λ水導入が継続され
1社1(1成分が一定醋以上磁11柵F、158間に捕
捉されると第3図Cの如く磁性細線5aから最も遠く百
1れた場所では一旦は捕捉された%lii性成分(イ)
が処理浄化水の流勢に抗しきれずひき離され処理浄化水
に移行し、磁性成分の捕捉率が低Fする。さらに、この
状態で原水の導入が継続されるとμ目子細線5aの間隙
は磁性成分(イ)によって密に目詰りし、もはや原水の
導入は不可能となり、ここで逆洗水による磁性成分の洗
浄除去が必要となる。以上のように、磁気フィルターに
よる原水中の磁性成分の捕捉操作では原水の導入開始か
ら導入の中11、逆洗開始に至るまでの間、原水の導入
の経過に従って磁f′1成分の捕捉率は変化し一定しな
い。If we estimate the change in the state of capture of magnetic components in the filter media when raw water is introduced as described above, it is likely that the change will occur as shown in the enlarged view in Figure 2 (Δ~DI). J, the state immediately after starting the introduction of raw water is shown in Figure 2 Δ
The magnetic ml wire 5 that constitutes the filter media is as follows.
8 shows the flow direction of raw water with an arrow J) and A f-j L t
The l&M component particles are captured in a row, and the magnetic component (a) passes through the gap between the 1ift fl line 5a and flows into the raw water without capturing part of the magnetic component (a). Later, as shown in Fig. 2B, the gap between the magnetic wires 5a is filled with magnetic component particles, and the magnetic component (a) in the raw water is transferred to the gap between the magnetic wires 5a and the flow of the raw water. Ninokkuri 1)? It will not be transferred to the treated purified water side without being treated. As the introduction of 11λ water continues and more than a certain amount of 1 component (1 component) is captured between the magnetic 11 fences F and 158, as shown in Fig. %lii component (a)
cannot resist the flow of treated purified water and is separated and transferred to treated purified water, resulting in a low F capture rate of magnetic components. Furthermore, if the raw water continues to be introduced in this state, the gaps between the μ-mesh fine wires 5a will be densely clogged with the magnetic components (a), and it will no longer be possible to introduce the raw water, and the magnetic components caused by the backwash water will be It is necessary to wash and remove. As described above, in the operation of capturing magnetic components in raw water using a magnetic filter, the capture rate of the magnetic f'1 component is determined according to the progress of raw water introduction from the start of introduction of raw water to the beginning of introduction and backwashing. changes and is not constant.
第3図は、捕捉状況の1例をこれをグラフに表わしたも
ので、第2図への原水の導入初期は磁性成分の捕捉率は
劣るが次第に捕捉率は上昇し、第2図Bの原水導入中期
には最高に達Jるが、これし第2図0のう9人後期に承
りように磁性成分の捕1犀mの増大に伴つI l+li
捉率は低下し、遂には捕捉性能は第2図1〕の導入量1
1Jように全く低下して逆洗処理μざるをえなくなる。Figure 3 is a graph showing an example of the capture situation.At the beginning of the introduction of raw water into Figure 2, the capture rate of magnetic components is poor, but the capture rate gradually increases, and as shown in Figure 2B. It reaches its highest level in the middle of the introduction of raw water, but as shown in the latter half of Fig. 2, I + li increases as the amount of magnetic components captured increases.
The capture rate decreases, and the capture performance finally reaches the introduction amount 1 in Figure 2 (1).
1J, and backwashing process μ becomes necessary.
しlこがって、磁竹成かの捕捉牢を常に一定にし、シロ
)も磁場形成のための消費電力を最小限に押えて効率よ
く磁気フィルターを運転り゛るためには例えば原水の導
入初期(賛1性成分の捕捉状態が第2図Aのようになっ
ているどき)には、原水の中位時間当りの導入用を下げ
るかまたは磁場形成の電力供給ffi!iを上げるかi
15るいはその両者を48行して1jう。原水y)入中
則(磁性成分の捕捉状態が第2図Bのj、うに11−営
な捕捉状態が#1(持されているとき)には原水の単位
時間当りの導入用を上げるか、または磁場形成電力の供
給量をダウンさせるかあるいは両者を01行しく行・う
。さらに、原水導入後期(磁性成分の捕捉状態が第2図
Cのにうになって正常な捕捉状態が維持困難となつ/j
場合)には原水の導入用を下げるか、または磁場形成電
力の供給量を大きくするかあるいは両名を併行して行う
といった操作が必要である。However, in order to operate the magnetic filter efficiently by minimizing the power consumption for forming the magnetic field, it is necessary to keep the trapping force of the porcelain bamboo constant at all times. At the initial stage of introduction (when the captured state of the positive component is as shown in Figure 2 A), the medium amount of raw water introduced per hour may be lowered or the power supply for magnetic field formation ffi! Do you want to raise i?
15 or both for 48 lines and 1j. Raw water y) Input rule (when the magnetic component capture state is j in Figure 2 B, and the uni-11-active capture state is #1), the amount of raw water introduced per unit time should be increased. , or reduce the supply amount of magnetic field forming power, or perform both in the same way.Furthermore, in the later stages of raw water introduction (the state of capture of magnetic components becomes as shown in Figure 2 C, it is difficult to maintain a normal capture state). Tonatsu/j
(case), it is necessary to reduce the amount of raw water introduced, increase the amount of magnetic field forming power supplied, or perform both in parallel.
本発明は以上のJ、うな磁性成分を含む原水の処理にa
3いて、フィルターメディアによる磁性成分の捕捉を良
好な状態に維持Cきるにう原水の導入量ならびに磁場形
成の電力供給量を自動的に調節覆ることにより、低運転
コス]〜でかつ一定の効率で磁性成分を捕捉−4るよう
にした磁気フィルターを提供づ−るものである。りなわ
ら、本発明は磁性成分を含む被処理原水の流入管と処F
J!浄化水の流出管とを備えたクースに、磁性成分を捕
捉りる機能をなり磁性材料からなるフィルターメディア
を内装し、通電により磁場を形成させる励磁コイルを前
記フィルターメディアを囲んで設番ノだ磁気ノイルター
装置においで、磁性成分を含む被処理原水の流入管に該
原水の導入用を調節する開閉弁を設番ノる一方、処理浄
化水の流出管には処理浄化水の水質感知装置を設り、さ
らに、該水質感知装置からの信号により前記励磁コイル
への電流供給用を調節する電流変換器に供給電流のvA
節を指令づると共に、前記開閉弁に対して原水の導入用
の調節を指令りる制御装置を(Sj設してなる磁気フィ
ルター装置を要旨と覆るものである。The present invention is directed to the treatment of raw water containing magnetic components.
3. By automatically adjusting the amount of raw water introduced and the amount of power supplied to form the magnetic field, the capture of magnetic components by the filter media is maintained in a good condition, resulting in low operating costs and constant efficiency. The present invention provides a magnetic filter that captures magnetic components. However, the present invention provides an inflow pipe for raw water to be treated containing magnetic components and a treatment F.
J! A filter media made of a magnetic material that has the function of capturing magnetic components is installed in a coos equipped with an outflow pipe for purified water, and an excitation coil that forms a magnetic field when energized is placed around the filter media. In a magnetic noirter device, an on-off valve is installed in the inflow pipe of the raw water to be treated containing magnetic components to adjust the introduction of the raw water, while a water texture sensing device for the treated purified water is installed in the outflow pipe of the treated purified water. and a current converter that adjusts the current supply to the excitation coil according to the signal from the water sensing device.
The gist is a magnetic filter device including a control device (Sj) that commands the flow rate and also commands the on-off valve to adjust the introduction of raw water.
以下本発明を一実施例を示1図面に基づいて説明する。The present invention will be explained below based on one embodiment and one drawing.
第4図は本発明の磁気)、fルター!li!1lfiT
の1llt!要図である。図におい−(,1は磁気フィ
ルターで構造的には第1図に示Jらのと変らない。なお
この図Cは第゛1図におG′Jるポールピース6と、リ
ターンフレーム8は省略しである。9は磁性成分を含む
原水流入管でこれには制御装H10から電気的な口il
Ill指令にj−り1m痕のl)3節される開閉弁1
1が設置Jられ、原水の導入用が調節される。12は原
水中の磁1!l戊分がフィルターメディア5に捕捉され
たあとの処理浄化水の流出管で、これには排出される処
理浄化水中の残留磁性成分量、濁Iff等の水質を測定
しその結果を電気的信号にかえC制御装置FI 10に
送る水質感知装置13が設問されている。Figure 4 shows the magnetism of the present invention), f Luther! li! 1lfiT
1llt! This is the essential diagram. In the figure, 1 is a magnetic filter, which is structurally the same as the one shown in FIG. This is omitted. 9 is a raw water inflow pipe containing a magnetic component, and an electric port is connected to this from the control device H10.
On-off valve 1 with 1m mark on Ill command with 3 sections
1 is installed and the introduction of raw water is adjusted. 12 is magnetic 1 in raw water! This is an outflow pipe for the treated purified water after the 100% fraction is captured by the filter media 5, and the water quality such as the amount of residual magnetic components and turbidity Iff in the treated purified water that is discharged is measured and the results are sent as electrical signals. Instead, the water texture sensing device 13, which is sent to the C control device FI 10, is asked.
’I /I LL電流変換器で、制御装置10からの指
令ににり励磁コイル7への供給電力を変化させCフィル
ターメディア5におけるvAsの出力を増減させる;層
面をなJものである。制御装置10には、水質感知装置
13からの電気的信号により処理浄化水中にII竹酸成
分一定値以上混入してきた場合あるいは一定116以下
となった場合にはこれに対応して前記間開弁11の開度
を増減さμ、原水の導入量を増減させ、あるいは前記電
流変換器14からの励磁コイル7への電力供給量を増減
させる指令パターンが記憶させである。The I/I LL current converter changes the power supplied to the excitation coil 7 in accordance with commands from the control device 10 to increase or decrease the output of vAs in the C filter media 5; The control device 10 is controlled by an electric signal from the water quality sensing device 13 to open the valve during the above period in response to the presence of a II bamboo acid component in the purified water of a certain value or more or when the concentration of the II bamboo acid component is below a certain value of 116. Command patterns for increasing/decreasing the opening of the coil 11, increasing/decreasing the amount of raw water introduced, or increasing/decreasing the amount of power supplied from the current converter 14 to the excitation coil 7 are stored.
本発明の磁気フィルター装置は以上のような構成よりな
っCおり、これを運転する(、二は、制御装置関係に電
力を入力し1から、原水をItil I!Jl弁11弁
膜1°Cある流入管9から磁気フィルター1へ導入する
。原水中の磁性成分はフィルターメディアに捕捉され処
理浄化水は流出管12ににり磁気フィルター外へ排出さ
れ、水質感知器13にJ、リヂエツクされるが、原水の
導入初期は前記第2図△のような捕捉挙動を示づので、
磁(’I酸成分充分フィルターメディア5に捕捉されず
に処理浄化水中に一部移行し、それが水質感知装置13
に検知されてその値が電気的信号に変換され制9M+装
置10に伝達される。イのtii′Iが予め設定されI
C数111以」ニの場合は、制御装置10から開閉弁1
1に開度絞りの指令が伝達され原水の導入量は減少りる
。同時に、電流変換器14に電流変換器14からの電流
出力増加の指令が伝達されて励磁コイルの1!&場が増
大され、ノ(ルターメディア5による磁性成分の捕捉が
強化される。その後(磁性成分がフィルターメディア5
に1充分捕捉されるようになれば(前記第2図B参照)
、処理浄化水中への磁性成分の移1’7 sa減少しそ
の餡が一定値以トとなって水質感知器13でその検出結
果が電気的信号として制御装置10に伝達され、該制御
装置10から発Uられる前記開閉弁11への開111増
加の指令に阜づき原水脣入間が増大し、また、電流変換
器14への供給電力量が減衰されて励磁コイルににる磁
場出力は減衰され、これにより運転効率は増大される(
正常運転の場合)。さらに、原水の導入がm続された結
果、前記第2図Cに示ずJ:うに、フィルターメディア
5における磁性成分が蓄積し、−巨捕捉された磁性成分
が処理浄化水の流勢に押されて磁性細線から引き111
Ilされ処理浄化水中に移行づると、これを水質感知器
13が感知して電気的11月が制御装置10へ送られる
から、制御装置10からは前記1京水の73’1人初期
にお()るど同様に開閉弁11の絞りあるいは電流変換
器14に供給電力増加の指令が発けられ、原水導入量の
減衰、あるい(コ励q振コイル7のIG磁場出力増大が
行われるのである。The magnetic filter device of the present invention has the above-mentioned configuration, and it is operated (Secondly, power is input to the control device, and the raw water is heated to a temperature of 1°C. The raw water is introduced into the magnetic filter 1 from the inflow pipe 9.The magnetic components in the raw water are captured by the filter media, and the treated purified water is discharged from the magnetic filter through the outflow pipe 12, and is re-evacuated to the water sensor 13. , At the initial stage of introduction of raw water, the trapping behavior shown in Figure 2 above is shown by △.
The magnetic ('I) acid component was not sufficiently captured by the filter media 5 and partially migrated into the treated purified water, and it was detected by the water texture sensing device 13.
The detected value is converted into an electrical signal and transmitted to the control device 10. tii'I of A is set in advance.
If the C number is 111 or more, the on-off valve 1 is
A command to throttle the opening is transmitted to 1, and the amount of raw water introduced is reduced. At the same time, a command to increase the current output from the current converter 14 is transmitted to the current converter 14, and the excitation coil 1! & The field is increased, and the capture of the magnetic component by the Luther media 5 is strengthened.Then, the magnetic component is
(See Figure 2 B above)
, the transfer of magnetic components into the treated purified water 1'7 sa decreases and its content exceeds a certain value, and the detection result is transmitted to the control device 10 as an electrical signal by the water feel sensor 13, and the control device 10 In response to the command to increase the opening 111 of the on-off valve 11 issued from U, the input of raw water increases, and the amount of power supplied to the current converter 14 is attenuated, and the magnetic field output to the excitation coil is attenuated. , which increases operating efficiency (
(in case of normal operation). Furthermore, as a result of continuous introduction of raw water, magnetic components in the filter media 5 accumulate as shown in FIG. 111 drawn from magnetic thin wire
When it is transferred to the treated purified water, the water sensor 13 detects this and sends an electrical signal to the control device 10. () Similarly, a command to increase the power supply is issued to the throttle of the on-off valve 11 or the current converter 14, and the amount of raw water introduced is attenuated or (the IG magnetic field output of the co-excited q-oscillation coil 7 is increased). It is.
逆洗工程へ入る指令は次の三点のいす”れか又は、その
組みあわせ判断をブ[」グラムして決定Jる。The command to enter the backwash process is determined by programming the following three points or a combination thereof.
■ タイマーで決めた■)間
■ 処理水の水質又は原水・処理水の水質から演算して
得た目的処理水質以下の悪い水質になった時
■ フィルターメディア5の前後(上下)の圧・力にリ
フィルターメディアの圧力損失を演詐し、−室以上の圧
力損失が生じた時に、即ち、第2図のDの状況が進行し
始めた時
実施例
[方法1
被処理原水として下水二次処理水を選び、本発明装置を
用い−てSSの除去を次の条件下で行った。■ Time determined by the timer ■ When the water quality of the treated water or the target treated water quality calculated from the water quality of the raw water and treated water has become poor or below the water quality ■ Pressure and force before and after (up and down) the filter media 5 When the pressure loss of the refilter media is falsified and a pressure loss greater than - chamber occurs, that is, when the situation D in Figure 2 begins to develop, Example [Method 1: Secondary sewage is used as the raw water to be treated. The treated water was selected and SS was removed using the apparatus of the present invention under the following conditions.
磁場(磁稈強1良):3KO0一定
原水道水速匪(線速IJ[) : 25 On+ /b
r一定温加物
FeaOa粉(対原水) : I Eim(Izl(平
均粒1¥0.5μw+)
1ii!l 酸アルミニウム(対1爪水): 10mM
A高分子−凝集剤(対原水): 0.5m(]/立1重
水水質
1)II:6.8
SSニア11141/文
COl、):61+1(1/立
「結果」
>rp人++、’r (7) 原水SS@GO(7II
1g/立)とし、本発明装置通過後の処理浄化水の88
@Cとし、(Go−C)/Goを処理性能としてIIi
@にとり濾過経過時間を横軸にとって捕捉状態をグラフ
に表示したどころ第3図のようになった。同図において
処理性能が1.0の場合には100%(完全な)処理を
している場合である。Magnetic field (magnetic culm strength 1 good): 3KO0 constant raw tap water speed (linear speed IJ[): 25 On+ /b
r Constantly heated FeaOa powder (vs. raw water): I Eim (Izl (average particle 1 ¥0.5μw+) 1ii!l Aluminum acid (vs. raw water): 10mM
A polymer-flocculant (vs. raw water): 0.5 m (]/vertical 1 heavy water water quality 1) II: 6.8 SS Near 11141/Bun COl, ): 61+1 (1/vertical ``result''>rp person++, 'r (7) Raw water SS@GO (7II
88% of the treated purified water after passing through the device of the present invention.
@C and (Go-C)/Go as processing performance IIi
When I plotted the captured state on a graph with the elapsed filtration time on the horizontal axis, it turned out as shown in Figure 3. In the figure, when the processing performance is 1.0, it means that 100% (complete) processing is being performed.
実施例
し方法」
磁場:3KOe一定
原水通水速度:
△の導入初期・・・最初100m /brで以後除々に
250m/l+rま℃増大
Bの導入中期・・・最初250m /l+rで以後除々
に1001+1 /hrまで減少0の導入後期・・・最
初100m/hrで以後除々に50m/hrまで減少
りの導入量1#J ・・−最初50 m / brテ以
後除々に30m/l+rまで減少
その他の条件は実験例1に同じ
[結果1
第5図にような結果となり、濾過経過時間の経過と共に
処理性能は低下したが、実験例1はと低下しなかった。Magnetic field: 3 KOe Constant raw water flow rate: △ Initial stage of introduction: 100 m/br at first, then gradually increased to 250 m/l+r. Middle stage of introduction of B: Initially 250 m/l+r, then gradually increased to 250 m/l+r. Decreased to 1001+1/hr Late introduction of 0...At first 100m/hr, then gradually decreased to 50m/hrIntroduction amount 1#J...-Initially 50m/hr, then gradually decreased to 30m/l+rOthers The conditions were the same as in Experimental Example 1 [Result 1] The results were as shown in Fig. 5, and the processing performance decreased as the filtration time elapsed, but did not decrease as in Experimental Example 1.
実施例
1 プj ン人 」
磁場 :
Δの導入初期・・・最初5 K Oeで以後除々に3
K Oeまで減少
Bの導入中期・・・最初3 K Oeで以後除々に4K
OOまで増大
0のう9人後朋・・・最初4KOeで以後除々に5 K
Ocまで増大
りの導入末期・・・最初5KO(!で以後除々に7 K
Oeまで増大
原水通水速11T : 250m /l+r一定イの他
の条イ1は実験例1に同じ
E結果]
第6図のにうな結果どなり、Cの導入後期及び1)の導
入末期におい(実験例1ばど処理性能がイL(下しなか
った。Example 1 Magnetic field: Initial introduction of Δ...at first 5 K Oe and then gradually increasing to 3
Mid-term introduction of B...at first 3K Oe and then gradually 4K
Increased to OO 0 out of 9 people...at first 4 KOe and then gradually 5 K
In the final stage of introduction, increasing to Oc...first 5 KOs (! and then gradually 7 Ks)
Increased raw water flow rate up to Oe 11T: 250m/l+r Constant A and other rows A have the same E results as in Experimental Example 1] The results shown in Figure 6 are loud, and the late introduction of C and the final stage of introduction of 1). Experimental Example 1 Bad processing performance did not decrease.
実施例
「方法」
磁場および原水通水速度:
△の導入初期・・・最初、磁場5KOe、原水通水速度
100m/hrr開始し、以後除々に5KOeより3K
Oeへ下げつつ200m/hrへ増大さぼる。Example "Method" Magnetic field and raw water flow rate: Initial introduction of △...At first, the magnetic field was 5KOe and the raw water flow rate was 100 m/hr, and then gradually increased from 5KOe to 3K.
The speed increases to 200m/hr while lowering the speed to Oe.
Bの導入中期・・・lυ初、Ij場3KO(!S原水通
水速度250m/hr、で開始し、以後除々に200m
、’br、150m /lo゛、100m/l+rと減
少させ、150I!l/hrの時、t41’aを4KO
C+に増大さぼる。Mid-term introduction of B...At the beginning of lυ, Ij field 3KO (!S) Started with raw water flow rate of 250 m/hr, and then gradually increased to 200 m/hr.
,'br, 150m/lo゛, decreased to 100m/l+r, 150I! When l/hr, 4KO t41'a
Increased to C+.
Cの導入接明・・・最初、磁場4KOe、原水通水速度
100m/hrで開始し、以後除々に50 m ’ /
l+rニ減少させ、ilmは5 K Oeに増大させ
る。 ひの導入末期・・・最初、磁場5KOe。Introduction of C...First, start with a magnetic field of 4 KOe and a raw water flow rate of 100 m/hr, and then gradually increase the flow rate to 50 m'/hr.
l+r is decreased and ilm is increased to 5 K Oe. At the end of the introduction phase...at first, the magnetic field was 5 KOe.
原水通水速度5’0 +n / l+rで開始し、以後
除々に30 m / ll’rに減少させ、(Go−C
)/Goが更に低下し始めた峙(例えば0.7以上にな
った時)直らに逆洗を行う。The raw water flow rate started at 5'0 +n/l+r, and then gradually decreased to 30 m/ll'r.
)/Go starts to decrease further (for example, when it becomes 0.7 or more), immediately perform backwashing.
その他の条件は実験例1に同じ
[結果]
第7図のような結果となり、処理性flluの低下は少
むかった。Other conditions were the same as in Experimental Example 1 [Results] The results shown in FIG. 7 were obtained, and the decrease in processability flu was small.
本発明の磁気フィルター装置は以」−述べたにうに、磁
気フィルターの処理浄化水の流出管に水質感知)(にを
設りてその感知結果に基づく電気的(Fi号を受けl、
二制tl′ll装置の指令により原水尋人量とフィルタ
ーメゾ−r j’ (7月社場出力を調節して、原水中
の磁性成分の捕捉効率を一定化すると共に、磁気ノイル
ターの運転コストを低減しようと覆るものであり、その
工業的利用価値は大である。The magnetic filter device of the present invention, as mentioned above, is equipped with a water-sensing sensor in the outflow pipe of treated purified water of the magnetic filter, and an electrical sensor based on the sensing result.
Based on the instructions from the two-control tl'll device, the amount of raw water and the output of the filter meso-r It is intended to reduce the amount of carbon dioxide, and its industrial value is great.
第1図は磁気フィルターを断面で表わし1.:概要図、
第2図は磁気フィルター内におりる磁性成分の捕捉状態
を111定した図、第;3図は実験例1にお(ノる磁気
フィルターにJ:る磁性成分の捕捉状態を示リグラフ、
第4図は本発明の一例を承り磁気フィルター装+N (
1)概要図、第5図は実験例2におりる1縣気ノCルタ
ーによる磁性成分の捕捉状態を示1Jクラノ、第6図は
実験例3にa3Lノる磁気フィルターにJ、る磁性成分
の捕捉状flffを示1グラフ、第7図は実験例4にお
【ノる磁気フィルターによる磁v1成分の捕捉状態を示
すグラフである。
1・・・磁気フィルター 4・・・ケース5・・
・フィルターメディア 6・・・ポールピース7・・
・励磁コイル 8・・・リターンフレーl\9・
・・流入恰 10・・・制御装置11・・・開
閉弁 12・・・流出管13・・・水質感知器
14・・・電流変換器15・・・タイマー
代理人 弁理士 定立 勉
第1図
第2図
扮ノ
第4図
1へ
(#、−jツ
バ 第6図
C。Figure 1 shows the magnetic filter in cross section.1. : Outline diagram,
Figure 2 is a graph showing the state of capture of magnetic components in the magnetic filter;
Figure 4 shows an example of the present invention with a magnetic filter device +N (
1) Outline diagram, Figure 5 shows the state of capture of magnetic components by the 1-field C router in Experimental Example 2. FIG. 7 is a graph showing the state of capture of the magnetic v1 component by the magnetic filter in Experimental Example 4. 1...Magnetic filter 4...Case 5...
・Filter media 6...Pole piece 7...
・Exciting coil 8...Return fly l\9・
... Inflow condition 10 ... Control device 11 ... Opening/closing valve 12 ... Outflow pipe 13 ... Water sense detector 14 ... Current converter 15 ... Timer agent Patent attorney Tsutomu Seiri Figure 1 Figure 2 costume No. 4 Go to Figure 1 (#, -j Tsuba Figure 6 C.
Claims (1)
!浄化水の流出管とを備えたウースに、磁性成分を捕捉
りるI幾能をなり(軸性1/l 1’31からなるノイ
ルターメデイj′を内装し、通電により1&場を形成さ
せる励磁コ、イルを前記フィルターメディアを囲lυで
設cJt:: t:磁気)rルター装置にJ3いて、H
目(1成分を含む被処理原水の流入管に該原水の導入M
4i:調節−する開閉弁をRGJる一方、処I’J!浄
化水の流出管には処理浄化水の水質感知装置を設(〕、
さらに、該水闇1感知装置からの電気的信号により前記
励磁コーfルl\の電流供給量を調節りる電流変換器に
供給電流の調節を111令するど其に、前記開閉弁に対
しては原水の勢へ吊の調節を指令゛りる制胛装首を付設
しくなることを特徴とJる磁気フールター装置。1 Inflow pipe and place for raw water containing magnetic components 111 1! I
! A woofer equipped with a purified water outflow pipe is equipped with an I geometry for capturing magnetic components (a noil termimeter j' consisting of an axial axis of 1/l 1'31 is installed, and a 1 & field is formed by energization. An excitation coil is set up around the filter media with lυ in the Luther apparatus, and H
(Introduction of the raw water to the inflow pipe of the raw water containing one component
4i: RGJ the on-off valve to be adjusted, while processing I'J! A water texture sensing device for treated purified water is installed in the purified water outflow pipe ().
Furthermore, the electrical signal from the water darkness 1 sensing device instructs the current converter that adjusts the amount of current supplied to the excitation coil fl\ to adjust the supplied current, and then The magnetic filter device is characterized in that it is equipped with a control neck that commands the adjustment of the suspension to the force of raw water.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP18974682A JPS5980311A (en) | 1982-10-28 | 1982-10-28 | Magnetic filter apparatus |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP18974682A JPS5980311A (en) | 1982-10-28 | 1982-10-28 | Magnetic filter apparatus |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS5980311A true JPS5980311A (en) | 1984-05-09 |
Family
ID=16246481
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP18974682A Pending JPS5980311A (en) | 1982-10-28 | 1982-10-28 | Magnetic filter apparatus |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS5980311A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB2331718A (en) * | 1997-11-27 | 1999-06-02 | Honda Motor Co Ltd | Cleaning apparatus for magnetic filter and cleaning method thereof |
JP2019155243A (en) * | 2018-03-09 | 2019-09-19 | 国立研究開発法人物質・材料研究機構 | Magnetic separator |
-
1982
- 1982-10-28 JP JP18974682A patent/JPS5980311A/en active Pending
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB2331718A (en) * | 1997-11-27 | 1999-06-02 | Honda Motor Co Ltd | Cleaning apparatus for magnetic filter and cleaning method thereof |
GB2331718B (en) * | 1997-11-27 | 2002-07-31 | Honda Motor Co Ltd | Cleaning apparatus for magnetic filter and cleaning method thereof |
JP2019155243A (en) * | 2018-03-09 | 2019-09-19 | 国立研究開発法人物質・材料研究機構 | Magnetic separator |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
KR101502675B1 (en) | system and method for recycling steelwastewater | |
CN106915809B (en) | Formula, preparation method and use method of heavy medium powder for water treatment | |
JP7128546B2 (en) | Method and system for preparing lithium carbonate from lithium ore | |
JPS5980311A (en) | Magnetic filter apparatus | |
CN101987263B (en) | Diatomite powder filter of city tap water and filtering method thereof | |
JP4519878B2 (en) | Filtration device | |
WO2016132557A1 (en) | Regeneration method for filtration device, filtration device, and water treatment device | |
Bicknell et al. | Concentration of seeded and naturally occurring enteroviruses from waters of varying quality by hollow fiber ultrafiltration | |
CN209554973U (en) | A kind of strong brine processing system with regeneration function | |
JPH06304559A (en) | Method for treating water and device therefor | |
JP2009195893A (en) | Operation method of water purification membrane filtration system | |
JPH11319844A (en) | Water purification system | |
JP2001347264A (en) | Water treatment equipment and water treatment method | |
Rahman et al. | Pursuing the effect of aeration, pH increment, and H2O2 coupled with UV irradiation on the removal efficiency of manganese by microfilter membrane | |
CN109574316A (en) | Waste water softens preprocess method | |
JPH08105995A (en) | Condensate filter | |
JPS5929015A (en) | Separation of magnetic component and nonmagnetic component | |
JPH06507206A (en) | Desiliconization method for inorganic aqueous solution | |
JPS5922617A (en) | Separation of magnetic component and non-magnetic component | |
CN109876665A (en) | A reverse osmosis system of a backwashable water purifier | |
CN209397040U (en) | A kind of water purification machine waste strength regulating device | |
CN206188536U (en) | Freeze -drying powder production line effluent disposal system | |
JP2010119982A (en) | System for treating muddy water and treating method therefor | |
JP2004000883A (en) | Method for treating solution containing selenium | |
JPH11290850A (en) | Water treatment method and apparatus |