[go: up one dir, main page]

JPH0249766B2 - - Google Patents

Info

Publication number
JPH0249766B2
JPH0249766B2 JP58083924A JP8392483A JPH0249766B2 JP H0249766 B2 JPH0249766 B2 JP H0249766B2 JP 58083924 A JP58083924 A JP 58083924A JP 8392483 A JP8392483 A JP 8392483A JP H0249766 B2 JPH0249766 B2 JP H0249766B2
Authority
JP
Japan
Prior art keywords
header
valve
cleaning liquid
cleaning
pressure
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
Application number
JP58083924A
Other languages
Japanese (ja)
Other versions
JPS59209621A (en
Inventor
Yoshinari Iijima
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.)
Tsukishima Kikai Co Ltd
Original Assignee
Tsukishima Kikai Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Tsukishima Kikai Co Ltd filed Critical Tsukishima Kikai Co Ltd
Priority to JP58083924A priority Critical patent/JPS59209621A/en
Publication of JPS59209621A publication Critical patent/JPS59209621A/en
Publication of JPH0249766B2 publication Critical patent/JPH0249766B2/ja
Granted legal-status Critical Current

Links

Landscapes

  • Filtration Of Liquid (AREA)

Description

【発明の詳細な説明】 本発明はフイルタープレスの運転方法に関し、
詳しくは、室形成、加圧過脱水、原液供給部
内洗浄、室開枠脱水ケーキ排出の1連の操作を
一工程とし、その工程の繰返しからなるフイルタ
ープレスの運転方法において、原液供給部内洗浄
(以下ヘツダーブローと称す)に用いる有圧の液
体や乾燥用気体を含む洗浄用供給流体(以下洗浄
流体と称す)の処理方法に係わる。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method of operating a filter press,
Specifically, in a filter press operation method that consists of repeating a series of operations of forming a chamber, pressurizing excessive dehydration, cleaning the inside of the stock solution supply section, and discharging the dehydrated cake from the opening of the chamber as one process, cleaning the inside of the stock solution supply section ( The present invention relates to a method for processing a cleaning supply fluid (hereinafter referred to as cleaning fluid) containing a pressurized liquid and drying gas used for header blowing (hereinafter referred to as header blow).

従来、フイルタープレスの加圧過脱水操作に
よつて密閉した原液を圧搾し、その液は布外
へ搾出して排出し、室内には脱水ケーキを形成
させるがこのとき室の原液供給口附近には、そ
の圧搾力が及ばないことが多いので、原液の1部
が脱水ケーキにはなり切らないで、形成ケーキに
比べ極めて含水率の高い、所謂、末成ケーキとし
て枠ないし、布の1部に付着し、脱水ケーキ
排出操作後においても、それら局部に残存するこ
とがある。この残存物を放置したまゝ、工程が繰
返えされると脱水機の原液供給部内が狭搾となり
以後の原液供給時に原液押し込み効果を減じさせ
たり、1部の布に目詰りを生じてその局部の
過性を低下させるので、工程が繰返されるに従つ
て、末成ケーキをますます生じさせる悪循環を招
来する。従つて加圧過脱水の操作後に開枠する
ことなくヘツダーブロー操作を行なつて洗浄流体
を加圧下に供給することによつて、要部を洗浄し
更に減湿した後に次の操作に移行するようにして
いる。
Conventionally, the sealed raw solution is squeezed by the pressurized over-dehydration operation of a filter press, and the liquid is squeezed out of the cloth and discharged, forming a dehydrated cake in the chamber. Because the squeezing force is often insufficient, part of the raw solution does not become a dehydrated cake, and is not considered a so-called final cake, which has an extremely high moisture content compared to the formed cake. It may stick to the skin and remain in those areas even after the dehydrated cake discharge operation. If the process is repeated with this residue left unattended, the inside of the stock solution supply section of the dehydrator will become constricted, reducing the effectiveness of pushing the stock solution during subsequent supply of the stock solution, or clogging some of the fabrics, resulting in This reduces local hypersensitivity, leading to a vicious cycle in which as the process is repeated, more and more final cakes are produced. Therefore, by performing a header blow operation without opening the frame after pressurized over-dehydration and supplying cleaning fluid under pressure, it is possible to clean the main parts and further dehumidify before moving on to the next operation. I have to.

この従来技術のヘツダーブロー操作には種々の
問題点を有し、これらの問題点につき第1図によ
り説明する。
This prior art header blowing operation has various problems, and these problems will be explained with reference to FIG.

固定端板1と移動端板2との間の複数の板4
は水平かつ可動に支持され、各板4の面には
布5が張設され、これらの板4は移動端板2
の端面にその先端が固定された流体圧シリンダ3
により両端板1,2間に締付けられて、室が構
成され、過操作が行われ、その後各板間を開
放して、形成されたケーキの除去が行われる。
過操作は各板の締付後弁14と弁16,17を
閉じ、弁12を開いて、原液を配管11と可撓管
10を通して流入させ両端板と各板に直管状に
開口された流路(以下ヘツダー記す)内を通り、
各室内に流入し、原液中固体粒子は面上にケ
ーキを形成し、液体は布を通つて、板の下方
の開口9より排出される。過の終了に伴い弁1
2を閉じて、弁14,17を開いて前記ヘツダー
内に供給し、該ヘツダー内に残留する原液を除去
する洗浄操作をした後、弁17を閉じ弁16を開
いて空気を導入して該ヘツダー内の清水を除去、
減湿した後、弁14を閉じる一連のヘツダーブロ
ー操作が行なわれる。このヘツダーブロー時の空
気は、配管3より空気分離槽19へ導入して空気
と水に分離し、空気は管20より、水は管21に
よつてそれぞれ大気中に放出し、水は一旦水槽へ
放出した後そこからポンプ23により汚水処理装
置へ回送して再処理をする。しかし、空気分離槽
の経済性を有する汎用型は一般に分離性能が低い
ため、放出空気内に汚水ミストが混入し、このヘ
ツダーブロー操作のたびに屡々周囲を汚染する。
また上記洗浄流体の量の制御は、弁の開閉時間の
長短により行われるため、ときに変動するこれら
の供給管内の圧力によつて消費量が変化するので
結果的に洗浄流体が浪費する傾向がある。
A plurality of plates 4 between the fixed end plate 1 and the movable end plate 2
are horizontally and movably supported, a cloth 5 is stretched on the surface of each plate 4, and these plates 4 are connected to the movable end plate 2.
A fluid pressure cylinder 3 whose tip is fixed to the end face of
is tightened between the end plates 1 and 2 to form a chamber, over-operation is performed, and then the space between each plate is opened to remove the formed cake.
For over-operation, after tightening each plate, close the valve 14 and valves 16 and 17, open the valve 12, and let the stock solution flow through the piping 11 and the flexible tube 10 to form a straight pipe opening in both end plates and each plate. Passing through the road (hereinafter referred to as header),
Flowing into each chamber, the solid particles in the concentrate form a cake on the surface, and the liquid exits through the cloth through the openings 9 at the bottom of the plate. Valve 1 at the end of the
2 is closed, valves 14 and 17 are opened to supply the liquid into the header, and after a cleaning operation is performed to remove the stock solution remaining in the header, valve 17 is closed and valve 16 is opened to introduce air to the header. Remove fresh water in the header,
After dehumidification, a series of header blow operations are performed to close valve 14. The air during this header blowing is introduced into the air separation tank 19 from the pipe 3 and separated into air and water.The air is released into the atmosphere through the pipe 20 and the water is released into the atmosphere through the pipe 21, and the water is temporarily sent to the water tank. After being discharged, the water is sent from there by a pump 23 to a sewage treatment facility for reprocessing. However, general-purpose air separation tanks that are economical generally have low separation performance, so that sewage mist is mixed into the discharged air, often contaminating the surrounding area every time this header blow operation is performed.
Furthermore, since the amount of cleaning fluid is controlled by changing the opening and closing time of the valve, the consumption amount changes depending on the pressure inside these supply pipes, which sometimes fluctuates, and as a result, cleaning fluid tends to be wasted. be.

本発明は前記した従来技術を鑑みて、案出され
たもので、ヘツダーブローとその除水操作のため
の前記した欠点を解消し、さらに使用済の洗浄流
体のもつエネルギーを再活用することを目的とす
るものである。
The present invention was devised in view of the above-mentioned prior art, and aims to eliminate the above-mentioned drawbacks of header blow and its water removal operation, and to reuse the energy of used cleaning fluid. That is.

第2図により本発明の方法の一実施例を説明す
る。
An embodiment of the method of the present invention will be explained with reference to FIG.

本発明は前記の過操作終了し、弁12を閉
じ、弁14を開いて、フイルタープレス等内の圧
力を抜いた後、更に弁17を開いてフイルタープ
レス内に洗浄液を導入し、ヘツダ内等に残留する
スラツジを洗い落し、これらの液体を密閉槽24
内に導入し、密閉槽24内の液量が液面計25に
より一定高さを計測した時、弁17を閉じ洗浄液
の供給を停止し、弁16を開いて洗浄用の圧縮気
体を送りフイルタープレスへ通して残留洗浄液を
密閉槽24内に導入し該槽24内の圧力計26が
一定圧を計測した後、弁14,16を閉じる。こ
の操作によつて発生した、前記末成ケーキの残存
物を含む液体と気体を、この操作終了後一時貯留
しておき、次の工程の過操作の始めに弁14を
開いて、密閉槽24内の貯留物を該槽24内の圧
力を利用して、フイルタープレスへ返送して過
処理する方法である。密閉槽24内の前記した残
存物を含む液体を全量排出し、該槽24内の圧力
計26が再び洗浄流体導入前の圧力以下に低下し
たとき、弁14を閉じ、弁12を開いて原液の
過を行う。なお、これらの一連の操作は各計測器
に接点付などの自動制御用の計器を用いて制御す
ることにより、全自動化が可能である。
In the present invention, after the above-mentioned overoperation is completed, the valve 12 is closed, the valve 14 is opened, and the pressure inside the filter press, etc. is released, and then the valve 17 is further opened to introduce the cleaning liquid into the filter press, and the inside of the header etc. The remaining sludge is washed away and this liquid is poured into a sealed tank 24.
When the liquid level in the sealed tank 24 reaches a certain level using the liquid level gauge 25, the valve 17 is closed to stop the supply of cleaning liquid, and the valve 16 is opened to send compressed gas for cleaning to the filter. The remaining cleaning liquid is introduced into the closed tank 24 through the press, and after the pressure gauge 26 in the tank 24 measures a constant pressure, the valves 14 and 16 are closed. The liquid and gas generated by this operation, including the residue of the final cake, are temporarily stored after this operation is completed, and the valve 14 is opened at the beginning of the over-operation of the next step, and the closed tank 24 is stored. This method utilizes the pressure within the tank 24 to return the stored material to the filter press for overtreatment. When the entire amount of the liquid containing the above-mentioned residue in the closed tank 24 is discharged and the pressure gauge 26 in the tank 24 drops below the pressure before introducing the cleaning fluid, the valve 14 is closed and the valve 12 is opened to drain the undiluted solution. Do the same thing. It should be noted that these series of operations can be fully automated by controlling each measuring instrument using an automatic control instrument such as a contact point.

上記したように、本発明の方法は、密閉槽24
を1槽設置することにより、従来その処理操作に
用いられていた空気分離槽、排水槽および排水ポ
ンプを不要とし、洗浄流体に与えた圧力エネルギ
ーにより新たにその他の装置並びにエネルギーを
用いることなく、洗浄流体の浪費も、汚水ミスト
の発生等の二次汚染も生ずることがないという長
所を有する。
As mentioned above, the method of the present invention includes the closed tank 24
By installing a single tank, the air separation tank, drainage tank, and drainage pump that were conventionally used for the treatment operation are no longer necessary, and the pressure energy applied to the cleaning fluid eliminates the need for additional equipment and energy. It has the advantage that there is no wastage of cleaning fluid and no secondary contamination such as generation of sewage mist.

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

第1図は従来法のヘツダ洗浄装置を示し、第2
図は本発明の一実施例のヘツダ洗浄装置の説明図
である。 1,2……端板、3……流体圧シリンダ、4…
…板、5……布、6,7,8……ヘツダー、
9……液排出口、10……可撓管、12,1
4,16,17……弁、24……密閉槽、25…
…液面計、26……圧力計。
Figure 1 shows a conventional header cleaning device;
The figure is an explanatory diagram of a header cleaning device according to an embodiment of the present invention. 1, 2... End plate, 3... Fluid pressure cylinder, 4...
...board, 5...cloth, 6,7,8...header,
9...Liquid outlet, 10...Flexible tube, 12,1
4, 16, 17... Valve, 24... Sealed tank, 25...
...Liquid level gauge, 26...Pressure gauge.

Claims (1)

【特許請求の範囲】 1 洗浄流体を原液供給部へ供給した後に経過的
に密閉槽へ導入して有圧状態下で貯留物とし、こ
の貯留物を次の加圧過脱水工程の初期操作時
に、その保有圧力によつて室へ返送して処理す
ることを特徴とするフイルタープレスの洗浄液処
理方法。 2 特許請求の範囲第1項記載の洗浄液処理方法
において、貯留物および室への返送の操作を、
該貯留物の量および圧力を制御することによつて
行なうことを特徴とするフイルタープレスの洗浄
液処理方法。
[Scope of Claims] 1. After the cleaning fluid is supplied to the stock solution supply section, it is gradually introduced into a closed tank to become a reservoir under pressure, and this reservoir is used during the initial operation of the next pressurized over-dehydration process. A method for processing a cleaning liquid for a filter press, characterized in that the cleaning liquid is returned to a chamber for treatment according to its retained pressure. 2. In the method for treating a cleaning liquid according to claim 1, the operation of returning the stored material to the chamber is performed by:
A method for treating a cleaning liquid for a filter press, which is carried out by controlling the amount and pressure of the stored material.
JP58083924A 1983-05-13 1983-05-13 Method for treating washing liquid of filter press Granted JPS59209621A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP58083924A JPS59209621A (en) 1983-05-13 1983-05-13 Method for treating washing liquid of filter press

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP58083924A JPS59209621A (en) 1983-05-13 1983-05-13 Method for treating washing liquid of filter press

Publications (2)

Publication Number Publication Date
JPS59209621A JPS59209621A (en) 1984-11-28
JPH0249766B2 true JPH0249766B2 (en) 1990-10-31

Family

ID=13816143

Family Applications (1)

Application Number Title Priority Date Filing Date
JP58083924A Granted JPS59209621A (en) 1983-05-13 1983-05-13 Method for treating washing liquid of filter press

Country Status (1)

Country Link
JP (1) JPS59209621A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0465641U (en) * 1990-10-11 1992-06-08
JPH0549515U (en) * 1991-12-13 1993-06-29 株式会社ヨンマルゴ Optical display

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0465641U (en) * 1990-10-11 1992-06-08
JPH0549515U (en) * 1991-12-13 1993-06-29 株式会社ヨンマルゴ Optical display

Also Published As

Publication number Publication date
JPS59209621A (en) 1984-11-28

Similar Documents

Publication Publication Date Title
US4100066A (en) Treating paint waste solids
US7815808B2 (en) Hot-gas pressure-filter apparatus
JP2001123286A (en) Post treatment methods of metal strip, particularly, cleaning method, and apparatus for implementing the methods
JPH0249766B2 (en)
EP0759318A1 (en) Process for demoisturizing and drying solids/liquid mixtures and apparatus for carrying out the process
US4251924A (en) Removing residual dampness from an adsorption cell
US3499533A (en) Automatically cleaned,pivotable,filter assembly
JPH0852307A (en) Filter press
CA1118745A (en) Removing residual dampness from an adsorption cell
DE68908487T2 (en) Process for dewatering wet, fine-grained material using compressed gas.
JPS5879511A (en) Washing method for filter cloth of dehydrator
DE2856626A1 (en) Endless belt filter - with tubular heating coil in filtrate chamber for filter cake drying under vacuum
RU2823553C1 (en) Ion exchange unit
KR900004321Y1 (en) Air drying apparatus
US1719548A (en) Water-softening filter and process of regenerating and purifying the same
JPH11170092A (en) Tube press
JPH11253997A (en) High efficiency dehydration method and high efficiency dehydration device
JPS577210A (en) Method and apparatus for continuously and repeatedly washing filter material of filter machine
DE2601261A1 (en) DEVICE FOR CLEANING A LIQUID
SU1715384A1 (en) Dehydration technique for coagulated sediment in aeration stations
JPH0254127B2 (en)
RU2014289C1 (en) Slag dehydration device
JPS6236491Y2 (en)
US1840930A (en) Settling and filtering means for sludge
KR0142390B1 (en) Residual water removal device and method for water purification washing machine