JPH08150306A - Method for washing filter press filter cloth for cement base waste water - Google Patents

Method for washing filter press filter cloth for cement base waste water

Info

Publication number
JPH08150306A
JPH08150306A JP6331312A JP33131294A JPH08150306A JP H08150306 A JPH08150306 A JP H08150306A JP 6331312 A JP6331312 A JP 6331312A JP 33131294 A JP33131294 A JP 33131294A JP H08150306 A JPH08150306 A JP H08150306A
Authority
JP
Japan
Prior art keywords
filter
filter cloth
washing
dehydration
valve
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
JP6331312A
Other languages
Japanese (ja)
Other versions
JP3551392B2 (en
Inventor
Kiyoshi Tanii
清 谷井
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.)
TANII KOGYO KK
Original Assignee
TANII KOGYO KK
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 TANII KOGYO KK filed Critical TANII KOGYO KK
Priority to JP33131294A priority Critical patent/JP3551392B2/en
Publication of JPH08150306A publication Critical patent/JPH08150306A/en
Application granted granted Critical
Publication of JP3551392B2 publication Critical patent/JP3551392B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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  • Filtration Of Liquid (AREA)

Abstract

PURPOSE: To shorten jet washing to reduce wear of filter cloth due to high pressure jetting by, after washing of a filter cloth after dehydration in a filter press is finished, closing a drain line of a filter plate and leaving the device as it is in a state in which a filter chamber is filled with fresh water until the next dehydration starts. CONSTITUTION: After a day's dehydration is finished and cake 18 is made to fall, filter plates 1, ... are closely adhered to each other to form one body. At this time, a discharge valve 5 remains open and a valve 6 is opened, and remaining sludge in a sludge tank 4 and remaining liquid in a pump 8 and a line are returned to a storing tank 7 to perform washing. Next, the filter plates 1, ... are opened to wash the surface of filter cloths 2, .... After that, the filter plates 1, ... are made one body again, and a drain valve 10 is closed, and also a fresh water valve 17 is opened to make all filter chambers 14, ...filled to capacity. Then, water supply is stopped to leave the device as it is until next dehydration. In this state, the ion content of sludge water permeated in filter cloth fiber is eluted into fresh water to prevent insoluble matter to be deposited.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明はセメント系廃水の濾布固
定式のフィルタープレスの濾布の、洗浄工法に関するも
のである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for cleaning a filter cloth of a cement-type wastewater filter cloth fixed type filter press.

【0002】[0002]

【従来の技術】濾布固定式フィルタープレスの従来の濾
布の洗浄方法は、噴射水洗浄として、高圧噴射ノズルに
よって、手動、あるいは自動洗浄機により濾過板の濾布
表面を洗浄するもの及び、素洗い洗浄として、清水を圧
送して洗浄濾過を行うもの、あるいは濾過板の濾過水路
側より通水するいわゆる逆洗浄する方法などがとられて
いる。いずれの方法においても、洗浄水は、流水状態で
の短時間の濾布の洗浄方法である。
2. Description of the Related Art A conventional method for cleaning a filter cloth of a fixed filter cloth filter press is to wash the surface of a filter cloth of a filter plate by a high pressure jet nozzle, manually or by an automatic washing machine, as washing with water. As the rinsing and washing, there are adopted a method in which fresh water is pressure-fed for washing and filtering, or a so-called back washing method in which water is passed from the side of the filtration channel of the filter plate. In either method, the washing water is a method for washing the filter cloth in a running water state for a short time.

【0003】[0003]

【発明が解決しようとする課題】脱水ケーキを強度のあ
る硬質ケーキとすることができれば再資源として有効利
用が可能となる。そのためには洗浄排水及び戻りコンク
リートは発生の都度放置することなく即脱水する必要が
ある。生コンクリートには、混和剤が配合されているの
で生コン配合後の経過時間が短いものほど脱水性が悪
く、且つ、活性セメントが濾布の繊維中に浸透してお
り、毎日、高圧水噴射洗浄していても日数が重なると目
詰まり現象を生じ、日毎に脱水効率が低下し、濾布の交
換日数も短縮してくる。
If the dehydrated cake can be made into a strong hard cake, it can be effectively used as a resource. For that purpose, it is necessary to immediately dehydrate the wash drainage and return concrete without leaving them as they are generated. Since the admixture is mixed in the fresh concrete, the shorter the elapsed time after the fresh concrete is mixed, the poorer the dehydration property is, and the activated cement permeates into the fibers of the filter cloth, and the high-pressure water jet cleaning is performed every day. Even if it is carried out, if the number of days overlaps, a clogging phenomenon will occur, the dehydration efficiency will decrease each day, and the number of days to replace the filter cloth will also decrease.

【0004】前述のような点に鑑み、本発明は、設備費
のかからない方法によって、従来の濾布洗浄では果たし
得ない効果を提供し、労働時間の大幅短縮を図ることを
目的として発明したものである。
In view of the above points, the present invention was invented for the purpose of significantly reducing working hours by providing an effect that cannot be achieved by conventional filter cloth washing by a method that requires no equipment cost. Is.

【0005】[0005]

【課題を解決するための手段】フィルタープレスにおい
て脱水終了後、従来の方法による濾布の洗浄を終えた後
に付加する洗浄行程であって、各濾過板の排水口より可
撓管でもって一本の集合管にまとめ、該集合管の下部に
排水弁を設ける。可動板により、濾過板を押圧して一体
となし、前記排水弁を閉として、濾過室内に清水を満水
した状態のまま次回の脱水開始時点迄放置しておくもの
である。
[Means for Solving the Problems] This is a washing step to be added after the dewatering in a filter press is finished and the washing of a filter cloth by a conventional method is completed. And the drain valve is provided below the collecting pipe. The movable plate presses the filter plate to form an integral unit, the drain valve is closed, and the filter chamber is left as it is until the next dehydration start time while being filled with fresh water.

【0006】[0006]

【作用】本発明は、活性セメントが濾布の目詰まりを起
こす原因と、その過程に着目して発明したもので、即
ち、従来のように、例え高圧水によって、濾布を表裏両
面から、直接洗浄したとしても、濾布繊維の内部に浸透
するセメント分は一部残留してしまう。即時脱水におけ
るセメント分は水和反応が終了していない活性セメント
であり、濾布の繊維の内部に浸透したセメント分は、濾
布が乾燥することによって、繊維内部で固結し、濾布繊
維にCao−Sio−Ho系の化合物が付着する。
残留分が微少であっても、日を重ねて蓄積し、Cao−
Sio−Ho分は繊維中に沈着し、極めて落としに
くくなり、やがて濾布の目詰まりとなり、脱水効率の低
下をおこすこととなる。
The present invention has been made by paying attention to the cause of the activated cement causing the clogging of the filter cloth and the process thereof, that is, as in the conventional case, the filter cloth can be removed from both the front and back sides by high pressure water. Even if it is directly washed, a part of the cement that permeates the inside of the filter cloth fiber remains. The cement component in the immediate dehydration is an activated cement that has not completed the hydration reaction, and the cement component that has penetrated into the fiber of the filter cloth is solidified inside the fiber by the drying of the filter cloth, and the filter cloth fiber Cao-Sio 2 -H 2 o based compound is adhered to.
Even if the residual amount is very small, it accumulates over days, and Cao-
The Sio 2 -H 2 o component is deposited in the fiber and becomes extremely difficult to drop, and eventually the filter cloth becomes clogged, resulting in a reduction in dewatering efficiency.

【0007】このようなメカニズムをもつことが把握さ
れたことによって、濾布繊維内部に浸透するセメント分
並びに濾布の裏面に、一部残存するセメント分を固結し
ないようにするには、濾布を乾燥させないこと、更には
常時清水に浸漬することによって、イオン分が清水中に
完全に溶出し、前記、Cao−Sio−Ho系化合
物が繊維中に沈着することを防ぎ次回の脱水行程が始ま
ると、脱水圧力により、該前記化合物は、濾布外へ放出
されるものである。
[0007] Since it has been understood that such a mechanism is provided, it is necessary to prevent the cement component that permeates the inside of the filter cloth fiber and the cement component that partially remains on the back surface of the filter cloth from solidifying. the cloth without drying, by further immersion in constantly Shimizu, ion content was completely eluted in Shimizu, wherein, the next time prevents Cao-Sio 2 -H 2 o compound is deposited on the fiber When the dehydration process starts, the compound is released to the outside of the filter cloth by the dehydration pressure.

【0008】[0008]

【実施例】本発明の実施例を図面に従って説明する。図
1は、本発明構造図、図2は、濾過板側断面図である。
本発明の一実施例としての構造は、各濾過板の下方に集
合管9を横臥し排水弁10を設け、該集合管の上部に
は、濾過板の排水口11より可撓管12でもって連結す
る連結口13を設ける。スラッジ槽4上方に清水管16
を配置し清水供給の制御をなす清水弁17を設ける。
Embodiments of the present invention will be described with reference to the drawings. FIG. 1 is a structural view of the present invention, and FIG. 2 is a side sectional view of a filter plate.
In the structure as one embodiment of the present invention, a collecting pipe 9 is laid down and a drain valve 10 is provided below each filter plate, and a flexible pipe 12 is provided above the collecting pipe from a drain port 11 of the filter plate. A connection port 13 for connection is provided. A fresh water pipe 16 above the sludge tank 4
Is provided to control the supply of fresh water.

【0009】本実施例による濾布洗浄方法は、従来技術
で示した素洗い洗浄と、噴射水洗浄を含んで説明する。
一日の脱水が終了して、最後のケーキ18を落下させた
後、再び可動板3により各濾過板1を押圧し隣接する濾
過板同士を密着して一対となす。スラッジ槽4の排出弁
5は開のままで弁6を開とする。スラッジ槽内の残留ス
ラッジ及びポンプ8及びその管路の残液は貯溜槽7へ戻
す。弁6を閉となしてから清水弁17を開となし、スラ
ッジ槽4へ所定量給水する。排水弁10は開のままポン
プ8を稼働しポンプケーシング内と管路を含めて濾過室
面を洗浄して排出する。所定時間経過後ポンプ8を停止
する。ここまでは素洗い洗浄である。
The method of cleaning the filter cloth according to the present embodiment will be described including the plain cleaning and the water spray cleaning described in the prior art.
After one day of dehydration is completed and the last cake 18 is dropped, the movable plates 3 again press the filter plates 1 to bring the adjacent filter plates into close contact with each other to form a pair. The valve 6 is opened while the discharge valve 5 of the sludge tank 4 remains open. The residual sludge in the sludge tank and the residual liquid in the pump 8 and its pipeline are returned to the storage tank 7. After closing the valve 6, the fresh water valve 17 is opened to supply a predetermined amount of water to the sludge tank 4. While the drain valve 10 is open, the pump 8 is operated to wash and discharge the filtration chamber surface including the inside of the pump casing and the pipeline. The pump 8 is stopped after a predetermined time has elapsed. Up to this point, it is a plain wash.

【0010】次に濾過板を開き、一枚毎、濾布の表面を
自動又は手動により高圧噴射水で洗浄する噴射水洗浄を
行う。以上の行程までは従来技術の洗浄方法であり、該
行程がすんだら本発明の実施となる。
Next, the filter plate is opened, and the surface of the filter cloth is washed automatically or manually with high-pressure jet water. Up to the above process, the conventional cleaning method is used, and when the process is completed, the present invention is carried out.

【0011】再び可動板により各濾過板を押圧し、一体
となし、集合管の排水弁10を閉止する。清水弁17を
開きスラッジ槽を経て全濾過室内に満水状態として送水
を停止する。次回の脱水までそのまま放置する。この放
置状態にある時、濾布繊維中に浸透しているスラッジ水
のイオン分は清水中へ溶出し不溶解分の濾布繊維中での
沈着が防止される。排水弁10を開き排水を行ってから
当日の脱水行程に入る。
The filter plates are pressed again by the movable plate to be integrated, and the drain valve 10 of the collecting pipe is closed. The fresh water valve 17 is opened to fill the entire filtration chamber through the sludge tank to stop the water supply. Leave it as it is until the next dehydration. When in this standing state, the ionic components of the sludge water permeating into the filter cloth fiber are eluted into the fresh water, and the insoluble matter is prevented from being deposited in the filter cloth fiber. After opening the drain valve 10 to drain water, the dehydration process of the day starts.

【0012】前述の実施例の構造以外であっても、清水
を濾過板内の濾過室及び、管路に充填、排水を自在に出
来る構造を呈したものであれば、本発明の濾布の洗浄工
法は適用される。
Other than the structure of the above-mentioned embodiment, as long as it has a structure in which fresh water can be freely filled in the filter chamber and the pipe line in the filter plate and drained, the filter cloth of the present invention can be used. Cleaning method is applied.

【0013】[0013]

【効果】以上詳述したことで明らかなように、活性セメ
ントスラッジの脱水には、従来のように濾布表面での高
圧噴射水並びに、裏面からの噴射水では目詰まりを防止
することが困難である。本発明の洗浄方法を併用するこ
とにより、従来の噴射洗浄は大幅に短縮されるので高圧
噴射による濾布の磨耗を軽減する。特出すべき効果とし
ては、目詰まりが軽減されていることにより脱水効率の
低下を防ぐことであり、濾布交換日数も大幅に延長され
る。特に手動による濾布洗浄の場合は洗浄時間の短縮は
労務費の軽減に大きく寄与する。以上のような効果を有
するものである。
[Effect] As is clear from the above detailed description, it is difficult to prevent clogging by dehydrating activated cement sludge with high-pressure jet water on the surface of the filter cloth and jet water from the back surface as in the conventional case. Is. By using the cleaning method of the present invention together, the conventional spray cleaning is greatly shortened, and therefore the wear of the filter cloth due to the high pressure spray is reduced. The remarkable effect is to prevent the deterioration of the dehydration efficiency by reducing the clogging, and the filter cloth replacement days can be greatly extended. Particularly in the case of manual filter cloth washing, shortening the washing time greatly contributes to the reduction of labor costs. It has the above effects.

【図面の簡単な説明】[Brief description of drawings]

【図1】本発明実施例構造図である。FIG. 1 is a structural diagram of an embodiment of the present invention.

【図2】濾過板側断面図である。FIG. 2 is a sectional side view of a filter plate.

【符号の説明】[Explanation of symbols]

1 濾過板 2 濾布 3 可動板 4 スラッジ槽 5 排出弁 6 弁 7 貯溜槽 8 ポンプ 9 集合管 10 排水弁 11 排水口 12 可撓管 13 連結口 14 濾過室 15 濾過水路 16 清水管 17 清水弁 18 ケーキ 1 Filter Plate 2 Filter Cloth 3 Movable Plate 4 Sludge Tank 5 Discharge Valve 6 Valve 7 Reservoir 8 Pump 9 Collecting Pipe 10 Drain Valve 11 Drainage Port 12 Flexible Pipe 13 Connection Port 14 Filtration Chamber 15 Filtration Channel 16 Clean Water Pipe 17 Fresh Water Valve 18 cakes

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 多数の濾過板を垂直状に並設し、各濾過
板間に、濾室が形成され各濾過板に濾布を添設し、前記
濾過板及び濾布を貫通して各濾室を連通する貫通孔が形
成され、濾室に原液を圧入して脱水するフィルタープレ
スにおける、脱水終了後の濾布の洗浄を終えた後におい
て、濾過板の排水管路を閉塞して、濾過室内に清水を満
水した状態のまま次回の脱水開始時点迄放置しておく、
漬け置き工法をなすことを特徴とするセメント系廃水の
フィルタープレス濾布洗浄工法。
1. A plurality of filter plates are vertically arranged side by side, a filter chamber is formed between each filter plate, a filter cloth is attached to each filter plate, and each filter plate and the filter cloth are penetrated to each other. A through-hole that connects the filter chamber is formed, and in a filter press for dewatering by pressing the stock solution into the filter chamber, after the washing of the filter cloth after the dehydration is finished, the drain pipe line of the filter plate is closed, Leave fresh water in the filtration chamber until the next dehydration starts,
Cement-based wastewater filter press filter cloth washing method characterized by performing a soaking and placing method.
JP33131294A 1994-11-28 1994-11-28 Filter press filter cloth for cement wastewater Cleaning method Expired - Fee Related JP3551392B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP33131294A JP3551392B2 (en) 1994-11-28 1994-11-28 Filter press filter cloth for cement wastewater Cleaning method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP33131294A JP3551392B2 (en) 1994-11-28 1994-11-28 Filter press filter cloth for cement wastewater Cleaning method

Publications (2)

Publication Number Publication Date
JPH08150306A true JPH08150306A (en) 1996-06-11
JP3551392B2 JP3551392B2 (en) 2004-08-04

Family

ID=18242281

Family Applications (1)

Application Number Title Priority Date Filing Date
JP33131294A Expired - Fee Related JP3551392B2 (en) 1994-11-28 1994-11-28 Filter press filter cloth for cement wastewater Cleaning method

Country Status (1)

Country Link
JP (1) JP3551392B2 (en)

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101890256A (en) * 2010-07-21 2010-11-24 景津压滤机集团有限公司 Suspension type filter cloth and cloth clamp
KR101352623B1 (en) * 2012-03-30 2014-01-17 윤종기 a Water Injector Device of Sludge Filter Plate
KR101352624B1 (en) * 2012-03-30 2014-01-17 윤종기 a Water Injector Fabrication method of Sludge Filter Plate
CN104190127A (en) * 2014-09-26 2014-12-10 吉首大学 Filling and washing type ore pulp press filter
CN104911348A (en) * 2015-07-08 2015-09-16 吉首大学 Combined and efficient filter pressing device in electrolytic zinc process
CN104984576B (en) * 2015-07-08 2016-08-24 吉首大学 Basic magnesium carbonate is carried out the device of efficient filter pressing by a kind of pump circulation anti-blockage type
CN108457833A (en) * 2018-06-22 2018-08-28 山西临龙泵业有限公司 Plunger centrifugal pump station for filter press

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101890256A (en) * 2010-07-21 2010-11-24 景津压滤机集团有限公司 Suspension type filter cloth and cloth clamp
KR101352623B1 (en) * 2012-03-30 2014-01-17 윤종기 a Water Injector Device of Sludge Filter Plate
KR101352624B1 (en) * 2012-03-30 2014-01-17 윤종기 a Water Injector Fabrication method of Sludge Filter Plate
CN104190127A (en) * 2014-09-26 2014-12-10 吉首大学 Filling and washing type ore pulp press filter
CN104190127B (en) * 2014-09-26 2015-11-04 吉首大学 Fill rinsing type ore pulp filter press
CN104911348A (en) * 2015-07-08 2015-09-16 吉首大学 Combined and efficient filter pressing device in electrolytic zinc process
CN104984576B (en) * 2015-07-08 2016-08-24 吉首大学 Basic magnesium carbonate is carried out the device of efficient filter pressing by a kind of pump circulation anti-blockage type
CN108457833A (en) * 2018-06-22 2018-08-28 山西临龙泵业有限公司 Plunger centrifugal pump station for filter press

Also Published As

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