JPH0234645B2 - DENJIFUIRUTANOSENJOHOHOOYOBISENJOSOCHI - Google Patents
DENJIFUIRUTANOSENJOHOHOOYOBISENJOSOCHIInfo
- Publication number
- JPH0234645B2 JPH0234645B2 JP8371582A JP8371582A JPH0234645B2 JP H0234645 B2 JPH0234645 B2 JP H0234645B2 JP 8371582 A JP8371582 A JP 8371582A JP 8371582 A JP8371582 A JP 8371582A JP H0234645 B2 JPH0234645 B2 JP H0234645B2
- Authority
- JP
- Japan
- Prior art keywords
- electromagnetic filter
- cleaning
- surfactant
- filter
- electromagnetic
- 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 - Lifetime
Links
- 238000004140 cleaning Methods 0.000 claims description 33
- 239000004094 surface-active agent Substances 0.000 claims description 27
- 238000011001 backwashing Methods 0.000 claims description 25
- 239000007788 liquid Substances 0.000 claims description 16
- 238000000034 method Methods 0.000 claims description 11
- 238000001914 filtration Methods 0.000 claims description 7
- 239000000126 substance Substances 0.000 claims description 2
- 239000012535 impurity Substances 0.000 description 20
- 239000000243 solution Substances 0.000 description 19
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 18
- 238000010586 diagram Methods 0.000 description 7
- 230000000694 effects Effects 0.000 description 7
- 235000014593 oils and fats Nutrition 0.000 description 5
- 239000007864 aqueous solution Substances 0.000 description 4
- 239000002351 wastewater Substances 0.000 description 4
- 230000000052 comparative effect Effects 0.000 description 3
- 239000003925 fat Substances 0.000 description 3
- 239000000203 mixture Substances 0.000 description 3
- 239000003921 oil Substances 0.000 description 3
- 229910000831 Steel Inorganic materials 0.000 description 2
- 239000003945 anionic surfactant Substances 0.000 description 2
- 239000002736 nonionic surfactant Substances 0.000 description 2
- 238000005507 spraying Methods 0.000 description 2
- 239000010959 steel Substances 0.000 description 2
- 125000000129 anionic group Chemical group 0.000 description 1
- 239000000701 coagulant Substances 0.000 description 1
- 238000005345 coagulation Methods 0.000 description 1
- 238000009749 continuous casting Methods 0.000 description 1
- 238000005098 hot rolling Methods 0.000 description 1
- 239000010842 industrial wastewater Substances 0.000 description 1
- SZVJSHCCFOBDDC-UHFFFAOYSA-N iron(II,III) oxide Inorganic materials O=[Fe]O[Fe]O[Fe]=O SZVJSHCCFOBDDC-UHFFFAOYSA-N 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 230000001404 mediated effect Effects 0.000 description 1
- 230000008929 regeneration Effects 0.000 description 1
- 238000011069 regeneration method Methods 0.000 description 1
- 238000005096 rolling process Methods 0.000 description 1
- 239000010865 sewage Substances 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
Landscapes
- Cleaning By Liquid Or Steam (AREA)
Description
本発明は電磁フイルタの洗浄方法及び洗浄装
置、更に詳しくは界面活性剤含有溶液と加圧空気
とを適宜に組合せて使用することにより電磁フイ
ルタを極めて効果的に洗浄することができる方法
及び該方法に直接使用する装置に関する。
都市下水や産業排水更には鉄鋼業の圧延廃水や
連続鋳造廃水等の製造工程廃水等(以下これらを
単に原水と略称する)には浮遊乃至懸濁物質(以
下これらを単に不純物と略称する)が含まれてい
るが、これらをそのまま環境へ放出すると重大な
公害源となるため何らかの手段で処理する必要が
あり、かかる処理手段に近年、電磁フイルタが使
用されている。この電磁フイルタは、必要なら原
水に適切な前処理をした後、これを磁気的に濾過
分離するものである。
ところで、不純物の含まれる原水を電磁フイル
タで処理すると、そのフイルタメデイア部に該不
純物が分離付着してくるため、これを例えば一定
時間毎に洗浄して、分離付着した該不純物を電磁
フイルタの外へ排出する必要がある。
従来、かかる洗浄は水と加圧空気とで電磁フイ
ルタを逆洗することにより行われている。
しかし、実際上、従来の逆洗だけで電磁フイル
タを繰り返し使用すると、従来の逆洗では洗浄で
きない不純物がフイルタメデイア部に次第に蓄積
されてきて、電磁フイルタの処理効率に重大な悪
影響を及ぼすようになる。そしてこのような場
合、従来の逆洗に代えて又は従来の逆洗に加え
て、電磁フイルタを効果的に洗浄して再生するこ
とのできる方法や装置が要請されているのであ
る。
本発明は叙上の要請に応える電磁フイルタの改
良された洗浄方法及び洗浄装置を提供するもので
ある。
以下、図面に基づいて従来の場合と比較しつつ
本発明の構成を詳細に説明する。
第1図は従来の電磁フイルタ処理手順を例示す
る系統図、第2図は電磁フイルタ部分の詳細図で
あり、フイルタメデイア31aとして磁性細線が
充填されている。原水を、必要なら適切な前処
理、例えば凝集剤及びマグネタイトによる共凝集
処理をした後、ポンプ11によりバルブ21を介
し電磁フイルタ31に供し、この電磁フイルタ3
1で不純物を磁気的に濾過分離して、バルブ2
2、逆洗水加圧タンク41及びバルブ23を順次
経て処理水が得られている。電磁フイルタ31を
中核として以上の各単位からなる濾過系統によ
り、原水を所定時間連続処理した後、電磁フイル
タ31の電源を断ち、適宜のバルブ操作を行つ
て、次の逆洗系統により電磁フイルタ31に分離
付着した不純物を洗浄して排出する。すなわち、
図示しないコンプレツサからの加圧空気でバルブ
24を経て逆洗水加圧タンク41に蓄えられてい
る一部の処理水をバルブ22を介して押し出す一
方で、前記加圧空気をバルブ25を介して送入
し、加圧空気と処理水とを混合状態で電磁フイル
タ31に噴射する。そして、この際のある種の衝
撃流により電磁フイルタ31内のフイルタメデイ
ア31aに分離付着している不純物を洗浄し、か
くして逆洗水が排出されている。逆洗後は、再び
濾過系統により原水を処理し、以下同様に、濾過
系統と逆洗系統とを繰り返して行うのである。
しかし、前述したように、このような従来の逆
洗だけでは、電磁フイルタを繰り返し使用する
と、かかる逆洗によつて洗浄されない不純物が電
磁フイルタ内のフイルタメデイア31aに次第に
蓄積され、電磁フイルタの処理効率に重大な悪影
響を及ぼすようになる。
本発明者らは、従来の逆洗によつて洗浄され
ず、電磁フイルタ内のフイルタメデイア31aに
蓄積されてくる不純物について、その組成等を追
究し、これを充分に洗浄して排出するべく鋭意研
究した結果、不純物を電磁フイルタ内のフイルタ
メデイア31aから剥がれ難くしている原因は油
脂類にあり、油脂類がその他の不純物を包含する
如く媒介して強固にフイルタメデイア31aへ付
着しているのであり、したがつて該油脂類を親和
力の強いものにより取り込んでその媒介能を打ち
消すようにする一方で衝撃を加えて剥離すればよ
いことを見出し、本発明を完成するに至つたので
ある。
すなわち本発明は、使用により各種の不純物が
分離付着した電磁フイルタを、界面活性剤含有溶
液と加圧空気とを適宜組合せて送入することによ
り洗浄する電磁フイルタの洗浄方法に係り、そし
てまたこの洗浄方法に直接使用する洗浄装置に係
る。
本発明において、界面活性剤は通常、水溶液の
状態で使用するが、洗浄対象である不純物の性状
や量更には所望する洗浄程度等に応じて適宜、そ
の種類や濃度及び液温等を選択する。そして、そ
の濃度や液温が高くなると、他の条件にもよる
が、概して洗浄効果はよくなる。しかし、多くの
場合標準的には、アニオン系とノニオン系の各界
面活性剤を混合したものを0.5〜10%の濃度に溶
解した20〜80℃の液温の水溶液を用いればよい。
一方、かかる界面活性剤含有溶液と組合せて使用
する加圧空気は従来の逆洗に用いられていた程度
のものでよい。
本発明を完成するに際して、本発明者らは種々
の試験を行い、その中では界面活性剤含有溶液だ
けを使用する場合でも相応の洗浄効果が得られ
た。その具体的効果は後述する比較例として挙げ
るが、この程度の洗浄効果ではなお不充分で、電
磁フイルタを再生するというには至らなかつた。
油脂類の媒介によつて強固にフイルタメデイア部
へ付着した不純物を充分に洗浄して排出するに
は、該油脂類への親和力が強い界面活性剤で油脂
類を取り込むことによりその媒介能を打ち消すよ
うにする一方で、加圧空気の衝撃力により不純物
をフイルタメデイア部から剥離することが肝要な
のである。この場合、界面活性剤含有溶液と加圧
空気とは適宜組合せて使用すればよい。第1図の
系統図においては、例えば、原水の方向から界面
活性剤含有溶液を電磁フイルタ31内に満たし、
一定時間静置した後、バルブ25を介し加圧空気
を電磁フイルタ31内へ送入し、これらをバルブ
26から排出してもよく、また例えば、逆洗水加
圧タンク41内に界面活性剤含有溶液を注入し、
前述した従来の逆洗と同様の操作を行つてもよ
い。要するに、加圧空気はフイルタメデイア部が
界面活性剤で湿潤状態のときに送入すればよいの
であり、そのためには界面活性剤含有溶液と加圧
空気とは、同時に又は別々に、更には連続的に又
は間欠的に送入してもよいのであり、結果として
界面活性剤の機能に加えて加圧空気の機能が発揮
されるようにすればよいのである。
そして実際上本発明は、電磁フイルタを1回使
用しただけでも著るしく強固に不純物が付着する
こともあるので、かかる場合従来の逆洗に代えて
適用することも当然に可能であるが、通常は従来
の逆洗に加えて適用する。すなわち、日常的な洗
浄は従来の逆洗で行い、例えば3か月に1回とい
つた割合で、従来の逆洗後に本発明を適用するの
である。
第3図は前記第1図に対応して本発明に係る洗
浄装置を例示する略視図である。第1図の場合と
同様に濾過系統と逆洗系統とが接続されている電
磁フイルタ32に、加温器として電気ヒータ51
が付設されている洗浄液タンク61及びこの洗浄
液タンク61に連結されている送液ポンプ12並
びに制御バルブ27,28が配管して組込まれて
いる洗浄系統が、前記電磁フイルタ32を含んで
循環路を形成するように接続されている。加温器
は洗浄液タンク61に投入される界面活性剤含有
溶液を所望温度に加温するものであればよく、図
面の場合の他に例えば加熱水蒸気を利用するもの
であつてもよい。また、図面の場合は上部開放の
洗浄液タンク61であるが、これは例えば密閉系
タンクであつてもよい。
前述の如く、電磁フイルタを界面活性剤含有溶
液と加圧空気との組合せで洗浄する場合、具体的
には多くの実施態様がある。しかし、実際上は従
来の逆洗も行う場合が多いのであり、また既存の
濾過系統や逆洗系統をそのまま活用するには、全
く別系統の関係配置で電磁フイルタを洗浄できる
ことが好ましく、併せて使用する界面活性剤含有
溶液を洗浄効果との関係で加温することができ、
しかも該界面活性剤含有溶液を繰り返し使用でき
る洗浄装置が最も好ましい。図面に例示する実施
例は、これらの望まれる諸条件を充足する代表例
である。
第1図においても説明したように、従来の逆洗
だけで電磁フイルタを繰り返し使用すると、その
フイルタメデイア部に不純物が蓄積してくる。そ
こで、従来の逆洗を行つた段階で、適切なバルブ
操作をし、界面活性剤含有溶液と加圧空気との組
合せにより電磁フイルタを洗浄する。第3図にお
いて例えば、予め洗浄液タンク61にその種類や
濃度等を適宜選択して界面活性剤の水溶液を準備
し、これを電気ヒータ51で所望温度に加熱す
る。次いで、加熱された界面活性剤含有溶液をポ
ンプ12でバルブ27を介して電磁フイルタ32
に送入し、バルブ28を介して洗浄液タンク61
へ返送する。そして、かかる界面活性剤含有溶液
の電磁フイルタ32を含む循環状態において、間
欠的にバルブ29を介し加圧空気を電磁フイルタ
32内へ噴射する。かくして、電磁フイルタ32
内のフイルタメデイア部は、界面活性剤の油脂類
に対する親和力と該油脂類によつて媒介された不
純物に対する加圧空気の衝撃剥離力とにより、完
全に洗浄され、再生される。尚、説明は省略する
が、本発明に係る洗浄装置の具体的な使用態様
は、叙上の場合に限定されるわけではない。
以上説明した本発明の効果をより具体的にする
ため、代表的に第1表を挙げる。第1表は、前述
の第3図に例示した装置の各系統をバルブ操作に
より選択し、次の条件及び区分で試験を行つた結
果である。
(1) 条件
原水…鉄鋼熱間圧延排水、SS=170〜220ppm。
電磁フイルタ…磁場=3KOe、濾過速度=
300m/時、フイルタ径=180mmψ、日常的に
従来の逆洗だけで3か月間繰り返して使用
し、最後に従来の逆洗を行つた段階での電磁
フイルタを洗浄対象とした。このときのフイ
ルタメデイア残存SS量は270〜310gであつ
た。
界面活性剤…アニオン系界面活性剤とノニオン
系界面活性剤との等量混合物の水溶液、濃度
=1重量%、液温=60℃、PH=6.5、送液量
=85/分。
加圧空気…従来の逆洗に使用されていたものを
利用した、圧力=3〜5Kg/cm2、全使用量=
0.24Nm3。
逆洗水…全使用量=0.08m3。
(2) 区分
対象…新規電磁フイルタの場合。
従来例1…従来通りで、洗浄対象そのままの場
合。
従来例2…洗浄対象に再度従来の逆洗を行つた
場合。
比較例1…洗浄対象に界面活性剤含有溶液を満
たし、1時間静置後、自重排出した場合。
比較例2…洗浄対象に界面活性剤含有溶液を1
時間循環して、自重排出した場合。
実施例1…洗浄対象に界面活性剤含有溶液を満
たし、1時間静置後、加圧空気を噴射して排
出した場合。
実施例2…洗浄対象に界面活性剤含有溶液を循
環しながら10分おきに加圧空気を噴射すると
いう工程を1時間行つた場合。
The present invention relates to a method and apparatus for cleaning an electromagnetic filter, and more particularly, a method and a method for extremely effectively cleaning an electromagnetic filter by using a suitable combination of a surfactant-containing solution and pressurized air. Relating to equipment used directly for. Urban sewage, industrial wastewater, and manufacturing process wastewater such as rolling wastewater and continuous casting wastewater from the steel industry (hereinafter simply referred to as raw water) contain suspended or suspended substances (hereinafter simply referred to as impurities). However, if these are released into the environment as they are, they become a source of serious pollution, so they must be treated by some means, and in recent years, electromagnetic filters have been used as such treatment means. This electromagnetic filter is used to magnetically filter and separate raw water after subjecting it to appropriate pretreatment if necessary. By the way, when raw water containing impurities is treated with an electromagnetic filter, the impurities separate and adhere to the filter media, so this is cleaned at regular intervals, for example, and the separated and adhering impurities are removed from the outside of the electromagnetic filter. need to be discharged to Conventionally, such cleaning is accomplished by backwashing the electromagnetic filter with water and pressurized air. However, in practice, if an electromagnetic filter is repeatedly used only by conventional backwashing, impurities that cannot be cleaned by conventional backwashing will gradually accumulate in the filter media, which will have a serious negative effect on the processing efficiency of the electromagnetic filter. Become. In such a case, there is a need for a method and apparatus that can effectively clean and regenerate the electromagnetic filter instead of or in addition to conventional backwashing. The present invention provides an improved cleaning method and cleaning apparatus for electromagnetic filters that meet the above requirements. Hereinafter, the configuration of the present invention will be explained in detail based on the drawings while comparing it with a conventional case. FIG. 1 is a system diagram illustrating a conventional electromagnetic filter processing procedure, and FIG. 2 is a detailed diagram of the electromagnetic filter portion, which is filled with magnetic thin wire as a filter medium 31a. After the raw water has been subjected to appropriate pretreatment if necessary, such as co-coagulation treatment with a coagulant and magnetite, it is supplied to an electromagnetic filter 31 by a pump 11 via a valve 21.
Impurities are magnetically filtered and separated using valve 2.
2. Treated water is obtained by sequentially passing through the backwash water pressurized tank 41 and valve 23. After the raw water is continuously treated for a predetermined period of time by the filtration system consisting of the above-mentioned units with the electromagnetic filter 31 as the core, the power to the electromagnetic filter 31 is cut off, appropriate valve operations are performed, and the electromagnetic filter 31 is filtered by the next backwashing system. Wash and discharge impurities that have separated and adhered to the surface. That is,
Pressurized air from a compressor (not shown) passes through the valve 24 and pushes out some of the treated water stored in the backwash water pressurizing tank 41 via the valve 22, while the pressurized air is pushed out via the valve 25. The pressurized air and treated water are injected into the electromagnetic filter 31 in a mixed state. Then, impurities separated and attached to the filter media 31a in the electromagnetic filter 31 are washed away by a certain kind of impact flow at this time, and the backwash water is thus discharged. After backwashing, the raw water is treated by the filtration system again, and the filtration system and backwashing system are repeated in the same manner. However, as described above, when an electromagnetic filter is repeatedly used by only conventional backwashing, impurities that are not cleaned by such backwashing gradually accumulate in the filter media 31a in the electromagnetic filter, and the processing of the electromagnetic filter becomes difficult. This will have a significant negative impact on efficiency. The present inventors investigated the composition of impurities that are not cleaned by conventional backwashing and accumulates in the filter media 31a in the electromagnetic filter, and are working diligently to thoroughly clean and discharge the impurities. As a result of research, the reason why impurities are difficult to peel off from the filter media 31a in the electromagnetic filter is due to oils and fats, which strongly adhere to the filter media 31a as if they contain other impurities. Therefore, they discovered that it is sufficient to take in the fats and oils with something that has a strong affinity to negate their mediating ability, and at the same time apply impact to peel them off, leading to the completion of the present invention. That is, the present invention relates to a method for cleaning an electromagnetic filter, in which an electromagnetic filter, on which various impurities have separated and adhered due to use, is cleaned by introducing a suitable combination of a surfactant-containing solution and pressurized air. This relates to a cleaning device that is used directly in the cleaning method. In the present invention, the surfactant is usually used in the form of an aqueous solution, but its type, concentration, liquid temperature, etc. are selected as appropriate depending on the nature and amount of the impurity to be cleaned, as well as the desired degree of cleaning. . As the concentration and liquid temperature increase, the cleaning effect generally improves, although it depends on other conditions. However, in most cases, it is standard to use an aqueous solution of a mixture of anionic and nonionic surfactants dissolved at a concentration of 0.5 to 10% at a temperature of 20 to 80°C.
On the other hand, the pressurized air used in combination with such a surfactant-containing solution may be the same as that used for conventional backwashing. In completing the present invention, the present inventors conducted various tests and found that even when only a surfactant-containing solution was used, a reasonable cleaning effect was obtained. The specific effect will be mentioned in a comparative example described later, but this level of cleaning effect was still insufficient and did not lead to the regeneration of the electromagnetic filter.
In order to sufficiently wash and discharge impurities that have strongly adhered to the filter media through the mediation of oils and fats, the mediating ability of the oils and fats can be counteracted by incorporating the oils and fats with a surfactant that has a strong affinity for the oils and fats. At the same time, it is important to peel impurities from the filter media using the impact force of pressurized air. In this case, the surfactant-containing solution and pressurized air may be used in appropriate combination. In the system diagram of FIG. 1, for example, a surfactant-containing solution is filled into the electromagnetic filter 31 from the direction of the raw water,
After being allowed to stand still for a certain period of time, pressurized air may be fed into the electromagnetic filter 31 via the valve 25 and discharged from the valve 26. Alternatively, for example, a surfactant may be added to the backwash water pressurized tank 41. Inject the containing solution,
The same operation as the conventional backwashing described above may be performed. In short, pressurized air should be introduced when the filter media is wet with the surfactant, and for this purpose, the surfactant-containing solution and the pressurized air should be fed simultaneously, separately, or even continuously. The air may be fed in at once or intermittently, and as a result, the function of pressurized air can be exerted in addition to the function of a surfactant. In fact, the present invention can be applied in place of conventional backwashing in such cases, since impurities may adhere to the electromagnetic filter even after one use. Usually applied in addition to conventional backwashing. That is, daily cleaning is performed by conventional backwashing, and the present invention is applied after conventional backwashing, for example, once every three months. FIG. 3 is a schematic diagram corresponding to FIG. 1, illustrating a cleaning device according to the present invention. As in the case of FIG. 1, an electric heater 51 is connected to the electromagnetic filter 32 to which the filtration system and the backwash system are connected.
A cleaning system including a cleaning liquid tank 61 attached thereto, a liquid feeding pump 12 connected to the cleaning liquid tank 61, and control valves 27 and 28 connected thereto includes the electromagnetic filter 32 and a circulation path. connected to form. The heater may be one that heats the surfactant-containing solution introduced into the cleaning liquid tank 61 to a desired temperature, and may be one that uses heated steam, for example, in addition to the one shown in the drawing. Further, in the drawing, the cleaning liquid tank 61 is open at the top, but it may be a closed tank, for example. As mentioned above, there are many specific embodiments for cleaning electromagnetic filters with a combination of a surfactant-containing solution and pressurized air. However, in practice, conventional backwashing is often performed, and in order to utilize the existing filtration system and backwashing system as is, it is preferable to be able to clean the electromagnetic filter in a completely separate system. The surfactant-containing solution used can be heated in relation to the cleaning effect.
Furthermore, a cleaning device that can repeatedly use the surfactant-containing solution is most preferable. The embodiment illustrated in the drawings is a representative example that satisfies these desired conditions. As explained in FIG. 1, when an electromagnetic filter is repeatedly used only by conventional backwashing, impurities accumulate in the filter media. Therefore, when conventional backwashing is performed, appropriate valve operations are performed to clean the electromagnetic filter using a combination of a surfactant-containing solution and pressurized air. In FIG. 3, for example, an aqueous solution of a surfactant is prepared in advance in a cleaning liquid tank 61 by appropriately selecting its type, concentration, etc., and heated to a desired temperature by an electric heater 51. Next, the heated surfactant-containing solution is passed through the electromagnetic filter 32 by the pump 12 through the valve 27.
and the cleaning liquid tank 61 via the valve 28.
Send it back to Then, while the surfactant-containing solution is being circulated through the electromagnetic filter 32, pressurized air is intermittently injected into the electromagnetic filter 32 via the valve 29. Thus, the electromagnetic filter 32
The inner filter media is completely cleaned and regenerated by the affinity of the surfactant for fats and oils and the impact stripping force of pressurized air against impurities mediated by the fats and oils. Incidentally, although the explanation is omitted, the specific usage mode of the cleaning device according to the present invention is not limited to the above-mentioned case. In order to make the effects of the present invention explained above more concrete, Table 1 is listed as a representative example. Table 1 shows the results of tests conducted under the following conditions and categories by selecting each system of the apparatus illustrated in FIG. 3 above by operating valves. (1) Conditions Raw water: Steel hot rolling wastewater, SS = 170 to 220 ppm. Electromagnetic filter...Magnetic field = 3KO e , filtration rate =
300m/hour, filter diameter = 180mmψ, and was used repeatedly for 3 months using only conventional backwashing on a daily basis, and the electromagnetic filter that had been subjected to conventional backwashing was the subject of cleaning. At this time, the amount of SS remaining on the filter media was 270 to 310 g. Surfactant: Aqueous solution of a mixture of equal amounts of anionic surfactant and nonionic surfactant, concentration = 1% by weight, liquid temperature = 60°C, PH = 6.5, liquid feeding rate = 85/min. Pressurized air...Using the air used for conventional backwashing, pressure = 3-5Kg/cm 2 , total amount used =
0.24Nm3 . Backwash water...Total amount used = 0.08m3 . (2) Category Target: New electromagnetic filter. Conventional example 1: As before, the object to be cleaned remains the same. Conventional Example 2: A case where conventional backwashing is performed again on the object to be cleaned. Comparative Example 1: The object to be cleaned was filled with a surfactant-containing solution, allowed to stand for 1 hour, and then drained under its own weight. Comparative example 2...1 surfactant-containing solution was applied to the cleaning target
When the self-weight is discharged after a time cycle. Example 1: The object to be cleaned was filled with a surfactant-containing solution, left to stand for 1 hour, and then discharged by spraying pressurized air. Example 2: The process of spraying pressurized air every 10 minutes while circulating a surfactant-containing solution to the object to be cleaned was carried out for one hour.
【表】【table】
【表】
第1表の結果からも、本発明によれば、電磁フ
イルタのフイルタメデイア部が充分に洗浄再生さ
れていることが明らかである。[Table] From the results in Table 1, it is clear that according to the present invention, the filter media portion of the electromagnetic filter is sufficiently cleaned and regenerated.
第1図は従来の電磁フイルタ処理手順を例示す
る系統図、第2図は電磁フイルタ部分の詳細図、
第3図は第1図に対応して本発明に係る洗浄装置
を例示する略視図である。
11…ポンプ、12…送液ポンプ、21,2
2,……29…バルブ、31,32…電磁フイル
タ、31a…フイルタメデイア、41…逆洗水加
圧タンク、51…電気ヒータ、61…洗浄液タン
ク。
Figure 1 is a system diagram illustrating the conventional electromagnetic filter processing procedure, Figure 2 is a detailed diagram of the electromagnetic filter section,
FIG. 3 is a schematic diagram corresponding to FIG. 1, illustrating a cleaning device according to the present invention. 11...Pump, 12...Liquid feeding pump, 21,2
2,...29...Valve, 31,32...Electromagnetic filter, 31a...Filter media, 41...Backwash water pressure tank, 51...Electric heater, 61...Washing liquid tank.
Claims (1)
着した電磁フイルタを、界面活性剤含有溶液と加
圧空気とを適宜組合せて送入することにより洗浄
する電磁フイルタの洗浄方法。 2 濾過系統と逆洗系統とが接続された電磁フイ
ルタに、加温器付設の洗浄液タンク及び該洗浄液
タンクに連結された送液ポンプ並びに制御バルブ
を適宜配管して組込んだ洗浄系統を、前記電磁フ
イルタを含んで循環路を形成するように接続して
成る電磁フイルタの洗浄装置。[Claims] 1. A method for cleaning an electromagnetic filter, which cleans an electromagnetic filter on which various floating or suspended substances have separated and adhered due to use, by introducing a suitable combination of a surfactant-containing solution and pressurized air. . 2. A cleaning system in which a cleaning liquid tank equipped with a heater, a liquid sending pump connected to the cleaning liquid tank, and a control valve are installed by appropriately piping the electromagnetic filter to which the filtration system and the backwashing system are connected, as described above. An electromagnetic filter cleaning device that includes an electromagnetic filter and is connected to form a circulation path.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP8371582A JPH0234645B2 (en) | 1982-05-18 | 1982-05-18 | DENJIFUIRUTANOSENJOHOHOOYOBISENJOSOCHI |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP8371582A JPH0234645B2 (en) | 1982-05-18 | 1982-05-18 | DENJIFUIRUTANOSENJOHOHOOYOBISENJOSOCHI |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS58199016A JPS58199016A (en) | 1983-11-19 |
| JPH0234645B2 true JPH0234645B2 (en) | 1990-08-06 |
Family
ID=13810196
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP8371582A Expired - Lifetime JPH0234645B2 (en) | 1982-05-18 | 1982-05-18 | DENJIFUIRUTANOSENJOHOHOOYOBISENJOSOCHI |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0234645B2 (en) |
-
1982
- 1982-05-18 JP JP8371582A patent/JPH0234645B2/en not_active Expired - Lifetime
Also Published As
| Publication number | Publication date |
|---|---|
| JPS58199016A (en) | 1983-11-19 |
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