JPS6048211B2 - Electromagnetic filter cleaning method and device - Google Patents
Electromagnetic filter cleaning method and deviceInfo
- Publication number
- JPS6048211B2 JPS6048211B2 JP1288979A JP1288979A JPS6048211B2 JP S6048211 B2 JPS6048211 B2 JP S6048211B2 JP 1288979 A JP1288979 A JP 1288979A JP 1288979 A JP1288979 A JP 1288979A JP S6048211 B2 JPS6048211 B2 JP S6048211B2
- Authority
- JP
- Japan
- Prior art keywords
- cleaning
- matrix
- electromagnetic filter
- water
- cold water
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired
Links
- 238000004140 cleaning Methods 0.000 title claims description 54
- 238000000034 method Methods 0.000 title claims description 20
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 49
- 239000011159 matrix material Substances 0.000 claims description 39
- 239000002351 wastewater Substances 0.000 claims description 18
- 238000001914 filtration Methods 0.000 claims description 11
- 230000001105 regulatory effect Effects 0.000 claims description 9
- 238000001514 detection method Methods 0.000 claims description 7
- 230000001276 controlling effect Effects 0.000 claims description 2
- 230000000694 effects Effects 0.000 description 5
- 230000005291 magnetic effect Effects 0.000 description 5
- 229910000831 Steel Inorganic materials 0.000 description 4
- 239000010959 steel Substances 0.000 description 4
- 210000002268 wool Anatomy 0.000 description 4
- 238000005192 partition Methods 0.000 description 3
- 230000001680 brushing effect Effects 0.000 description 2
- 238000005253 cladding Methods 0.000 description 2
- 230000007423 decrease Effects 0.000 description 2
- 230000005294 ferromagnetic effect Effects 0.000 description 2
- 239000000706 filtrate Substances 0.000 description 2
- 238000010586 diagram Methods 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 238000011086 high cleaning Methods 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 239000000696 magnetic material Substances 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 230000000717 retained effect Effects 0.000 description 1
- 238000010008 shearing Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
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
Landscapes
- Water Treatment By Electricity Or Magnetism (AREA)
- Filtration Of Liquid (AREA)
Description
【発明の詳細な説明】
本発明は、火力・原子力発電所等における高温高圧水系
中のクラッドを除去する目的の電磁フィルタ、特に強磁
性体のスチールウール等をマトリックスとして充填し、
これにより高勾配磁場を発生させる形式の、いわゆる高
勾配電磁フィルタの洗浄処理に関するものである。DETAILED DESCRIPTION OF THE INVENTION The present invention is an electromagnetic filter for the purpose of removing crud in high-temperature, high-pressure water systems in thermal power plants, nuclear power plants, etc.
This invention relates to a cleaning process for a so-called high-gradient electromagnetic filter that generates a high-gradient magnetic field.
一般に電磁フィルタではマトリックスとこれをフ磁化さ
せる電磁コイルとを備え、流体中の強磁性体および弱磁
性体の懸濁粒子(クラッド)を磁力により前記マトリッ
クスで捕捉して分離除去する濾過工程を行なうものであ
るが、ろ過継続によりマトリックス内にクラッドが堆積
してその差圧が5増大するか、あるいは濾過機能減退に
よりろ過水水質が悪化するときは、濾過を中断してマト
リックスの洗浄を行なわなければならない。Generally, an electromagnetic filter is equipped with a matrix and an electromagnetic coil that magnetizes the matrix, and performs a filtration process in which suspended particles (cladding) of ferromagnetic and weakly magnetic substances in a fluid are captured by the matrix using magnetic force and separated and removed. However, if crud accumulates in the matrix and the differential pressure increases due to continued filtration, or if the quality of the filtrate deteriorates due to a decline in filtration function, filtration must be interrupted and the matrix must be cleaned. Must be.
この洗浄には通常、高温高圧水のろ過にあつては外部の
洗浄源を用いず、自己のもつエネルギを利用して逆方向
にブラッシングを行なう洗浄方法がある。すなわち電磁
フィルタのマトリックスのろ過水流出側に、少なくとも
マトリックス容積以上、好ましくは2〜3倍の空間を保
有させ、一方マトリック 門スの流入側のフラッシュ排
水流路内に急開弁を設け、前記空間に高温高圧のろ過水
を密閉した状態て前記急開弁を開くことによりマトリッ
クスに逆流過させてその洗浄を行なうことが提唱されて
いる。しかし、この洗浄方法では外部の洗浄源を用いな
いがために洗浄効率に限界があつて大巾に高い洗浄効果
を期待する事はできないし洗浄排出水の処理にも問題が
あつた。For this cleaning, there is usually a cleaning method in which when high-temperature, high-pressure water is filtered, brushing is performed in the opposite direction using the body's own energy without using an external cleaning source. That is, on the filtrate outflow side of the matrix of the electromagnetic filter, there is provided a space at least equal to or larger than the matrix volume, preferably 2 to 3 times the volume, and on the other hand, a quick-opening valve is provided in the flush drainage channel on the inflow side of the matrix gate. It has been proposed that high-temperature, high-pressure filtered water is sealed in a space and the quick-opening valve is opened to cause the water to flow back into the matrix for cleaning. However, since this cleaning method does not use an external cleaning source, there is a limit to the cleaning efficiency, and a very high cleaning effect cannot be expected, and there are also problems in the treatment of cleaning waste water.
本発明は、これら問題点を適確に解決するためにかかる
フラッシュ洗浄において、その洗浄効果を最大ならしめ
るように洗浄工程を制御すると同時に、洗浄排出水を凝
縮させて一旦貯留し、その後の処理を便ならしめる方法
および装置を提供することを目的とするものである。In order to accurately solve these problems, the present invention controls the cleaning process to maximize the cleaning effect in flash cleaning, and at the same time condenses and temporarily stores cleaning waste water for subsequent treatment. The object of the present invention is to provide a method and a device for making it easier to use.
また本発明の他の目的は、高勾配電磁フィルタの運転維
持管理を簡素化し安全性か高く著しく経済的な洗浄作業
ができる有効な方法およびその装置とすることにある。Another object of the present invention is to provide an effective method and apparatus for simplifying the operation and maintenance of a high-gradient electromagnetic filter, making it possible to perform safe and extremely economical cleaning operations.
本発明の特徴の一つとしては高温高圧水をろ過.する高
勾配電磁フィルタの洗浄時におけるマトリックス差圧を
一定例えば1〜10k9fIc1tの範囲に保持するよ
う制御しながら、フラッシュ排水をフラッシュタンク内
の冷水中に混入させて処理する高勾配電磁フィルタの洗
浄方法としたことにあ二る。また本発明のもう一つの重
要な特徴として、前記洗浄方法を実施するための好適な
装置として、ろ過槽内にマトリックスを備え、このマト
リックスを磁化するための電磁コイルが配備された高勾
3配電磁フィルタにあるフラッシュ排水流路に圧力調節
弁を設け、この圧力調節弁を制御するために圧力調節弁
に連絡した洗浄時におけるマトリックスの差圧検出端を
電磁フィルタ本体内に配備するとともに、前記フラッシ
ュ排水流路が、冷水を貯4’留し且つフラッシュ排水を
冷水中に混合させる機構を備えたフラッシュタンクに連
結されたものからなる高勾配電磁フィルタの洗浄装置と
することにある。One of the features of this invention is that it filters high-temperature, high-pressure water. A method for cleaning a high-gradient electromagnetic filter in which flush wastewater is mixed into cold water in a flash tank and treated while controlling the matrix differential pressure to be kept constant, for example, in the range of 1 to 10k9fIc1t during cleaning of the high-gradient electromagnetic filter. There are two reasons why. Another important feature of the present invention is that a suitable device for carrying out the cleaning method is a high-gradient three-way filter, which is equipped with a matrix in a filtration tank and equipped with an electromagnetic coil for magnetizing the matrix. A pressure regulating valve is provided in the flush drainage passage in the electromagnetic filter, and in order to control the pressure regulating valve, a differential pressure detection end of the matrix during cleaning, which is connected to the pressure regulating valve, is disposed within the electromagnetic filter body, and the To provide a cleaning device for a high gradient electromagnetic filter, in which a flash drainage channel is connected to a flash tank having a mechanism for storing cold water and mixing flush drainage into the cold water.
この場合前記フラッシュタンクの冷水貯留量が、フラッ
シュ排水全量受入れ混合後100’C未満になる量であ
つて、フラッシュタンクの全容量が前記冷水とフラッシ
ュ排水全量とを受入れるに足る量であり、かつフラッシ
ュ排水を冷水中に混合させる機構を備えたフラッシュタ
ンクとすることが効果的である。In this case, the amount of cold water stored in the flash tank is below 100'C after receiving and mixing the entire amount of flash wastewater, and the total capacity of the flash tank is sufficient to receive the cold water and the entire amount of flash wastewater, and It is effective to use a flash tank equipped with a mechanism for mixing flush wastewater into cold water.
本発明の実施例を図面について説明すれば、電磁フィル
タ本体1内にマトリックス2が、通水隔フ板3により保
持されていて、その流入側および流出側にそれぞれ空間
4および空間5を区画形成していて、該空間4は、少な
くともマトリックス2の容積以上、好ましくは2〜3倍
の容積を区画保有している。To explain an embodiment of the present invention with reference to the drawings, a matrix 2 is held in an electromagnetic filter body 1 by a water flow partition plate 3, and a space 4 and a space 5 are defined on the inflow side and the outflow side, respectively. The space 4 has a volume that is at least more than the volume of the matrix 2, preferably 2 to 3 times the volume.
また前記通水隔板3は多孔板等を用iい、スチールウー
ル等のマトリックス2を保持すると同時に通水を均一に
分布する役目をする。また前記マトリックス2の外部は
、電磁コイル6がとり囲んで配備されていて、この電磁
コイル6に直流が流れると前記マトリックス2が磁化さ
れ、”さらにスチールウールの尖鋭部分には磁力が収斂
して高勾配が発生するように構成されている。またマト
リックス流入側の空間5に連通する流入路7に流入弁8
を設け、該流入弁8により電磁フィルタ本体1内に流入
した高温高圧水中のクラッドは、通常強磁性体または弱
磁性体てあるため、マトリックス2内を通過する間に磁
力によりスチールウールに捕捉保持されるようになつて
いる。これらのクラッドが除去されたろ過水は、流出側
の空間4を経て、頂部より流出弁9にある流出路10か
ら系へ戻るようになつている。なおバイパス流路11は
、流入路7と流出路10とを直接連結し、この流路中に
バイパス弁12が設けられてある。前記流入路7から分
岐されたフラッシュ排水流路13は、急開弁14および
圧力調節弁14′を経てフラッシュタンク15に直接又
はフラッシュタンク15内に設けられた多孔管等て構成
されるデイストリビユータ16に接続されて連結される
。The water flow partition plate 3 is made of a perforated plate or the like, and serves to hold the matrix 2 such as steel wool and at the same time distribute water flow uniformly. Further, an electromagnetic coil 6 is arranged surrounding the outside of the matrix 2, and when a direct current flows through the electromagnetic coil 6, the matrix 2 is magnetized, and furthermore, the magnetic force is converged on the sharp part of the steel wool. The structure is such that a high gradient is generated.In addition, an inflow valve 8 is provided in an inflow passage 7 communicating with a space 5 on the matrix inflow side.
The cladding in the high-temperature, high-pressure water that flows into the electromagnetic filter body 1 through the inflow valve 8 is usually a ferromagnetic or weakly magnetic material, so it is captured and held by the steel wool by magnetic force while passing through the matrix 2. It is becoming more and more common. The filtered water from which these cruds have been removed passes through the space 4 on the outflow side and returns to the system from the top through an outflow path 10 located in the outflow valve 9. Note that the bypass flow path 11 directly connects the inflow path 7 and the outflow path 10, and a bypass valve 12 is provided in this flow path. A flash drainage channel 13 branched from the inflow channel 7 is connected directly to the flash tank 15 via a quick-open valve 14 and a pressure control valve 14', or to a distributing channel constructed by a perforated pipe or the like provided in the flash tank 15. It is connected and coupled to the user 16.
この場合該デイストリビユータ16の代りに、フラッシ
ュ排水流路13をフラッシュタンク15の側板にそつて
切線方向に導入させる構造としてもよく、要はフラッシ
ュタンク内にあらかじめ貯留してある冷水と電磁フィル
タ本体1より排出される洗浄排水とが迅速にかつ均一に
混合される機構を備えていればよい。前記フラッシュタ
ン;.1゜ノ゛ノニol”;:ニo:ニ8’およびタン
ク頂部に排気弁19のある排気管19′を設けてある。In this case, instead of the distributor 16, a structure may be adopted in which the flash drainage channel 13 is introduced in the tangential direction along the side plate of the flash tank 15, in short, the cold water previously stored in the flash tank and the electromagnetic filter It is only necessary to provide a mechanism for quickly and uniformly mixing the cleaning wastewater discharged from the main body 1. Said flash tan;. An exhaust pipe 19' having an exhaust valve 19 is provided at the top of the tank.
さらに、前記マトリックス2の流入および流出側には、
圧力検出端20がそれぞれ設けられてあり、洗浄時にお
けるマトリックス2の前後の圧力を検出して、差圧指示
調節計21に伝送する。Furthermore, on the inflow and outflow sides of the matrix 2,
A pressure detection end 20 is provided, and the pressure before and after the matrix 2 during cleaning is detected and transmitted to a differential pressure indicating controller 21 .
この差圧指示調節計21は、これを受けてマトリツ」ク
ス2の差圧を検知し、信号を圧力調節弁14′に送つて
、設定差圧を保持するよう圧力調節弁14’を制御する
。この場合前記急開弁14を連動させてもよいし別個に
操作することもでき、さらには急開弁14を操作したの
ちに圧力調節弁14’を連動的に操作することもできる
。しかして、電磁フィルタでのろ過作用中は流入弁8お
よび流出弁9は開き、急開弁14およびバイパス弁12
は閉じて運転され、かつ電磁コイル6は通電されている
。In response to this, the differential pressure indicating controller 21 detects the differential pressure in the matrix 2, sends a signal to the pressure regulating valve 14', and controls the pressure regulating valve 14' to maintain the set differential pressure. . In this case, the quick-opening valve 14 may be operated in conjunction with each other or may be operated separately, and furthermore, after the quick-opening valve 14 is operated, the pressure regulating valve 14' may be operated in conjunction with the quick-opening valve 14. During filtration with the electromagnetic filter, the inflow valve 8 and outflow valve 9 open, and the quick-open valve 14 and bypass valve 12 open.
is closed and operated, and the electromagnetic coil 6 is energized.
即ち、処理すべき高温高圧水は流入弁8を経て電磁フィ
ルタ本体1の空間5に入り、ついでマトリックス2を通
過する間にクラッドが除去され、枦過水は空間4から流
出弁9を経て系に戻る。このろ過継続によりマトリック
ス2内にクラッドが堆積してその差圧が増大するか或い
は枦過機能減退により枦過水水質が悪化するのて、これ
らを検出して枦過を中断して洗浄工程に移る。この洗浄
工程に入るときは、まず前記バイパス弁12を開き、流
出弁9を閉じ、ついて流入弁8を閉じて、電磁コイル6
の通電を停止する。That is, the high-temperature, high-pressure water to be treated enters the space 5 of the electromagnetic filter body 1 through the inlet valve 8, and then the crud is removed while passing through the matrix 2, and the overflow water flows from the space 4 through the outflow valve 9 into the system. Return to As this filtration continues, crud accumulates in the matrix 2 and the differential pressure increases, or the water quality deteriorates due to a decline in the filtration function.If this is detected, the filtration is interrupted and the cleaning process is started. Move. When entering this cleaning process, first open the bypass valve 12, close the outflow valve 9, then close the inflow valve 8, and close the electromagnetic coil 6.
energization is stopped.
かくすることにより高温高圧水はバイパス流路11から
バイパスされるとともに、電磁フィルタ本体1内部には
高温・高圧水がそのまま保留される。一方フラッシュタ
ンク15には、排気弁19を開き排水弁18を閉じた状
態でます冷水流入弁17を開いて冷水をデイストリビユ
ータ16が水没するまて導入し、冷水流入弁17を閉じ
る。この導フ冷水量は、電磁フィルタからの洗浄排水を
受入オた後にフラッシュタンク15内の水温が100゜
C苓超えない量であり、かつフラッシュタンク15σ全
容量は、導入冷水量とフラッシュタンクからσ洗浄排水
全量とを受入れるに十分な量であるこ(が必要である。
かかる状態でフラッシュ排水流路13中にある急開弁1
4を急激に開くと、電磁フィルタ本体1内の高温高圧水
は急激な減圧によりその一部が蒸発して体積が膨張する
ので、空間4内の水がマトリックス2内を急激に流下し
、その剪断力によりスチールウールに付着していたクラ
ッドは剥離除去される。As a result, the high-temperature, high-pressure water is bypassed from the bypass channel 11, and the high-temperature, high-pressure water is retained inside the electromagnetic filter body 1 as it is. On the other hand, into the flash tank 15, with the exhaust valve 19 open and the drain valve 18 closed, the cold water inflow valve 17 is opened to introduce cold water until the distributor 16 is submerged, and the cold water inflow valve 17 is closed. The amount of cold water introduced into the flash tank is such that the water temperature in the flash tank 15 does not exceed 100°C after receiving cleaning waste water from the electromagnetic filter, and the total capacity of the flash tank 15σ is calculated from the amount of cold water introduced and the flash tank. The amount must be sufficient to accept the entire amount of cleaning wastewater.
In such a state, the quick-open valve 1 in the flush drainage flow path 13
4, the high temperature and high pressure water in the electromagnetic filter main body 1 undergoes a rapid depressurization, causing a portion of it to evaporate and expand its volume, causing the water in the space 4 to rapidly flow down inside the matrix 2, causing its The shearing force causes the crud attached to the steel wool to be peeled off and removed.
この洗浄流速はマトリックス2の前後に差圧を生じ、圧
力検出端20により検知されて差圧指示調節計21に伝
達される。実験によれば、160℃,6k9f1cイ以
上の高温高圧水てあれば、マトリックス2内に十分な洗
浄流速が得られ、130℃,3k9fIdでも相当程度
の洗浄効果が得られた。そのときのマトリックス2前後
の差圧は1〜10k9fIcイの範囲てあり、最も効果
的なものは2〜5k9f1dの範囲であつた。したがつ
てあらかじめ差圧指示調節計21により、差圧をこの範
囲に設定しておけば、差圧指示調節計21により圧力調
節弁14′が自動的に制御されて最適の洗浄流速が保持
されるのて最大の洗浄効果をあフげることができる。フ
ラッシュ排水はデイストリビユータ16からフラッシュ
タンク15内に貯留されている冷水中に放散されて混合
し、フラッシュ排水中に混合する蒸気も冷水により凝縮
され、全量がフラッシュタンク15に受入れられ、これ
5ら混合水の温度は最終的に100℃以下に保たれる。
そのまま放置して冷却させ、その後にフラッシュタンク
15より排水弁18を開いて外部にとり出し目的に応じ
て処理するかあるいは廃棄する。o なお本方法および
装置は、高温高圧水の自己エネルギによらず、外部の高
温高圧水を用いて洗浄を行なう場合にも適用できる。This cleaning flow rate generates a pressure difference across the matrix 2, which is detected by the pressure detection end 20 and transmitted to the differential pressure indicating controller 21. According to experiments, a sufficient cleaning flow rate was obtained in the matrix 2 using high-temperature, high-pressure water at 160° C. and 6k9flc or more, and a considerable cleaning effect was obtained even at 130° C. and 3k9fld. At that time, the differential pressure before and after the matrix 2 was in the range of 1 to 10k9fIc, and the most effective range was 2 to 5k9f1d. Therefore, if the differential pressure is set in advance within this range using the differential pressure indicating controller 21, the pressure regulating valve 14' will be automatically controlled by the differential pressure indicating controller 21 to maintain the optimal cleaning flow rate. The maximum cleaning effect can be achieved by The flash waste water is dispersed from the distributor 16 into the cold water stored in the flash tank 15 and mixed with it, and the steam mixed in the flash waste water is also condensed by the cold water, and the entire amount is received in the flash tank 15. The temperature of the mixed water is ultimately kept below 100°C.
The material is left to cool as it is, and then the drain valve 18 is opened from the flash tank 15 to take it out to the outside and treated or disposed of depending on the purpose. o The present method and apparatus can also be applied when cleaning is performed using external high-temperature, high-pressure water, without relying on the self-energy of the high-temperature, high-pressure water.
また、前記各弁の切換操作はマトリックス2の差圧検出
端による差圧指示に基づいて連けιルて35操作させて
もよいし、他の別系統による制御操作でもよい。Further, the switching operation of each of the valves may be performed 35 times in succession based on the differential pressure instruction from the differential pressure detection terminal of the matrix 2, or may be controlled by another separate system.
本発明によれば高温高圧水の処理において簡単な制御に
より電磁フィルタのマトリックスの洗浄効果を最大にす
ることがてき、かつ簡単な機構に4θより洗浄排水を全
量液状て回収して後随時任意の処理を可能にすることが
でき運転管理上有益かつ便利であり、フラッシュタンク
も小容量のものですみ、ブラッシングのための絞り量も
小さく能率的な洗浄作業が可能となり、高温高圧水の自
己工ネルギも効果的に利用した経済的て安全性の高い洗
浄操作ができるものである。According to the present invention, the cleaning effect of the matrix of the electromagnetic filter can be maximized through simple control in the treatment of high-temperature, high-pressure water, and the entire amount of cleaning waste water is collected in liquid form using a 4θ mechanism using a simple mechanism. It is useful and convenient for operation management, requires only a small capacity flush tank, and the amount of squeeze for brushing is small, allowing for efficient cleaning work, and the ability to self-generate high-temperature, high-pressure water. This enables economical and highly safe cleaning operations that effectively utilize energy.
図面は本発明の実施例の系統説明図である。
1 ・・・・・・電磁フィルタ本体、2 ・・・・・・
マトリックス、3・・・・・・通水隔板、4,5・・・
・・・空間、6 ・・・・・・電磁コイル、7 ・・・
・・・流入路、8 ・・・・・・流入弁、9 ・・・・
・・流出弁、10・・・・・・流出路、11・・・・・
・バイパス流路、12・・・・・・バイパス弁、13・
・・・・・フラッシュ排水流路、14・・・・・・急開
弁、14’・・・・・・圧力調節弁、15・・・・・・
フラッシュタンク、16・・・・・・デイストリビユー
タ、17・・・・・・冷水流入弁、17’・・・・・・
冷水流入路、18・・・・・・排水弁、18’・・・・
・・排水路、19・・・・・・排気弁、19′ ・・・
・・・排気管、20・・・・・・圧力検出端、21・・
・・・・差圧指示調節計。The drawing is a system explanatory diagram of an embodiment of the present invention. 1... Electromagnetic filter body, 2...
Matrix, 3... Water flow partition, 4, 5...
... Space, 6 ... Electromagnetic coil, 7 ...
...Inflow path, 8 ...Inflow valve, 9 ...
...Outflow valve, 10...Outflow path, 11...
・Bypass flow path, 12... Bypass valve, 13.
...Flash drainage channel, 14...Quick opening valve, 14'...Pressure control valve, 15...
Flash tank, 16...Distributor, 17...Cold water inflow valve, 17'...
Cold water inflow path, 18... Drain valve, 18'...
...Drainage channel, 19...Exhaust valve, 19'...
...Exhaust pipe, 20...Pressure detection end, 21...
...Differential pressure indicating controller.
Claims (1)
備えた高勾配電磁フィルタの洗浄方法において、前記マ
トリックスの流入側と流出側との差圧を一定に保持する
ように制御しつつ、洗浄排水を冷水中に放散混入せしめ
ることを特徴とする電磁フィルタの洗浄方法。 2 前記マトリックスの流入側と流出側との差圧が、1
〜10kgf/cm^2の範囲に制御されて処理される
特許請求の範囲第1項記載の洗浄方法。 3 前記洗浄排水を放散混入された冷水が、温度100
℃未満となるように調整されて処理される特許請求の範
囲第1項又は第2項記載の洗浄方法。 4 前記洗浄排水が、前記マトリックスの流入側に設け
た開閉自在の急開弁を開放して冷水中に放散混入される
ものである特許請求の範囲第1項、第2項又は第3項記
載の洗浄方法。 5 電磁コイル、マトリックスを備え高温高圧水を濾過
するための高勾配電磁フィルタの洗浄装置において、前
記マトリックスの流入側と流出側との差圧を検知する差
圧検出部を設け、この差圧検出部によつて開閉操作され
る圧力調節弁と急開弁を付設したフラッシュ排水流路を
配備すると共に、該フラッシュ排水流路を冷水を貯留し
かつ洗浄排水を冷水中に放散混入せしめる機構を備えた
フラッシュタンクと接続した電磁フィルタの洗浄装置。 6 前記フラッシュタンクが、洗浄排水全量と、該洗浄
排水を100℃未満とする冷水貯留量とを受け入れる大
きさである特許請求の範囲第5項記載の電磁フィルタの
洗浄装置。7 前記圧力調節弁が、前記マトリックスの
流入側に設けたフラッシュ排水流路中にある急開弁の下
流側に備えられるものである特許請求の範囲第5項又は
第6項記載の電磁フィルタの洗浄装置。 8 前記フラッシュ排水流路が、デイストリビユータを
介して前記フラッシュタンクに接続配備されているもの
である特許請求の範囲第5項、第6項又は第7項記載の
電磁フィルタの洗浄装置。[Claims] 1. A method for cleaning a high-gradient electromagnetic filter equipped with an electromagnetic coil and a matrix for filtering high-temperature, high-pressure water, the method comprising controlling the differential pressure between the inflow side and the outflow side of the matrix to be kept constant. A method for cleaning an electromagnetic filter, which is characterized in that cleaning wastewater is dispersed and mixed into cold water. 2 The differential pressure between the inflow side and the outflow side of the matrix is 1
The cleaning method according to claim 1, wherein the cleaning method is controlled to a range of 10 kgf/cm^2. 3. The cold water into which the cleaning waste water was diffused and mixed has a temperature of 100%.
3. The cleaning method according to claim 1 or 2, wherein the cleaning method is adjusted so that the temperature is below .degree. 4. Claims 1, 2, or 3, wherein the cleaning waste water is dispersed and mixed into the cold water by opening a quick-open valve that can be opened and closed provided on the inflow side of the matrix. cleaning method. 5. A high gradient electromagnetic filter cleaning device for filtering high-temperature, high-pressure water, which is equipped with an electromagnetic coil and a matrix, is provided with a differential pressure detection section that detects a differential pressure between the inflow side and the outflow side of the matrix, and this differential pressure detection section is provided. A flush drain channel is equipped with a pressure regulating valve and a quick-opening valve that are opened and closed by the operator, and the flush drain channel is equipped with a mechanism for storing cold water and dispersing and mixing cleaning waste water into the cold water. An electromagnetic filter cleaning device connected to a flush tank. 6. The electromagnetic filter cleaning device according to claim 5, wherein the flush tank is sized to receive the entire amount of cleaning waste water and a stored amount of cold water that makes the cleaning waste water less than 100°C. 7. The electromagnetic filter according to claim 5 or 6, wherein the pressure regulating valve is provided on the downstream side of a quick-opening valve located in a flush drainage channel provided on the inflow side of the matrix. cleaning equipment. 8. The electromagnetic filter cleaning device according to claim 5, 6, or 7, wherein the flash drainage channel is connected to the flash tank via a distributor.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1288979A JPS6048211B2 (en) | 1979-02-07 | 1979-02-07 | Electromagnetic filter cleaning method and device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1288979A JPS6048211B2 (en) | 1979-02-07 | 1979-02-07 | Electromagnetic filter cleaning method and device |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS55104616A JPS55104616A (en) | 1980-08-11 |
| JPS6048211B2 true JPS6048211B2 (en) | 1985-10-25 |
Family
ID=11817957
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP1288979A Expired JPS6048211B2 (en) | 1979-02-07 | 1979-02-07 | Electromagnetic filter cleaning method and device |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS6048211B2 (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP3948802B2 (en) * | 1997-11-27 | 2007-07-25 | 本田技研工業株式会社 | Magnet filter cleaning device |
-
1979
- 1979-02-07 JP JP1288979A patent/JPS6048211B2/en not_active Expired
Also Published As
| Publication number | Publication date |
|---|---|
| JPS55104616A (en) | 1980-08-11 |
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