JPH0356244Y2 - - Google Patents

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Publication number
JPH0356244Y2
JPH0356244Y2 JP1987127937U JP12793787U JPH0356244Y2 JP H0356244 Y2 JPH0356244 Y2 JP H0356244Y2 JP 1987127937 U JP1987127937 U JP 1987127937U JP 12793787 U JP12793787 U JP 12793787U JP H0356244 Y2 JPH0356244 Y2 JP H0356244Y2
Authority
JP
Japan
Prior art keywords
stock solution
slurry
filter press
transfer pipe
solution tank
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
Application number
JP1987127937U
Other languages
Japanese (ja)
Other versions
JPS6432705U (en
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 filed Critical
Priority to JP1987127937U priority Critical patent/JPH0356244Y2/ja
Publication of JPS6432705U publication Critical patent/JPS6432705U/ja
Application granted granted Critical
Publication of JPH0356244Y2 publication Critical patent/JPH0356244Y2/ja
Expired legal-status Critical Current

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Description

【考案の詳細な説明】 (産業上の利用分野) 本考案はフイルタープレスの原液供給路の内部
の詰まりを防止するためのフイルタープレスのエ
アブロー装置に関するものである。
[Detailed Description of the Invention] (Industrial Application Field) The present invention relates to an air blowing device for a filter press for preventing clogging inside the raw solution supply path of the filter press.

(従来の技術) センターフイード型のフイルタープレスは、多
数の濾板間に形成された濾室内に濾板の中央の原
液供給路を通じて原液槽から高圧で原液を供給
し、脱水濾過を行わせる装置であるが、脱水濾過
の終了後に開板してケーキを取出すときは、原液
供給路内の泥漿が外部に流出して外部を汚した
り、また原液供給路内に泥漿が付着して次第に流
れが悪くなる。このため、脱水作業終了後の原液
供給路内の泥漿を圧縮空気によつて一瞬のうちに
原液槽内へ逆流させるエアブローを行うことによ
つて詰まりの防止を図つている。
(Prior art) A center-feed type filter press supplies stock solution at high pressure from a stock solution tank through a stock solution supply path in the center of the filter plates into a filter chamber formed between a number of filter plates, and performs dehydration filtration. However, when the plate is opened to take out the cake after dewatering and filtration, the slurry in the stock solution supply channel may flow out and pollute the outside, or the slurry may adhere to the stock solution supply channel and gradually slow the flow. Deteriorate. For this reason, clogging is prevented by blowing air to instantly cause the slurry in the stock solution supply path to flow back into the stock solution tank using compressed air after the dewatering operation is completed.

従来、エアブローの際に泥漿が逆流する泥漿移
送用パイプの先端は原液槽の液面下に設けられた
液中サイレンサーに接続されており、泥漿はこの
液中サイレンサーを介して原液中に直接戻される
ようになつていた。ところが原液槽に耐薬品用の
ライニングなどが施されている場合にはエアブロ
ー時に液中サイレンサーに生じる衝撃的な振動に
よつてライニングが剥離される危険があつた。ま
たこのような危険性を避けるためにライニングに
接触しないようにパイプを上部から原液中に挿入
すると、激しい振動によつて泥漿用移送パイプの
破損が生じ易い欠点があつた。
Conventionally, the tip of the slurry transfer pipe, through which the slurry flows back during air blowing, is connected to a submerged silencer installed below the liquid level in the stock solution tank, and the slurry is directly returned to the stock solution via this submerged silencer. I was starting to be able to do it. However, if the stock solution tank is provided with a chemical-resistant lining, there is a risk that the lining will peel off due to the impact vibrations generated in the submerged silencer during air blowing. Furthermore, in order to avoid such a risk, if the pipe is inserted into the raw solution from above so as not to come into contact with the lining, there is a drawback that the slurry transfer pipe is likely to be damaged due to severe vibration.

(考案が解決しようとする問題点) 本考案は以上のような従来の問題点を解決し
て、エアブロー時にも原液槽のライニングが剥離
したり、パイプが破損するおそれがなく、しかも
泥漿を原液槽中に確実に返送することができるフ
イルタープレスのエアブロー装置を目的として完
成されたものである。
(Problems to be solved by the invention) The present invention solves the above-mentioned conventional problems, and eliminates the risk of peeling off the lining of the stock solution tank or damaging the pipes even during air blowing. It was completed for the purpose of an air blowing device for a filter press that can reliably return the air to the tank.

(問題点を解決するための手段) 上記の課題を解決するためになされた本考案
は、フイルタープレスへ濾過されるべき原液を供
給する原液槽の上方に多数の気液分離板を備えた
エリミネータを設置するとともに、原液槽とフイ
ルタープレスとを結ぶ原液供給管を途中で分岐さ
せてエアブローの際に泥漿が逆流する泥漿移送用
パイプをこの分岐部に接続し、更に泥漿移送用パ
イプの先端を前記エリミネータに接続したことを
特徴とするものである。
(Means for Solving the Problems) The present invention, which was made to solve the above problems, is an eliminator equipped with a large number of gas-liquid separation plates above the stock solution tank that supplies the stock solution to be filtered to the filter press. At the same time, the stock solution supply pipe connecting the stock solution tank and the filter press is branched in the middle, and a slurry transfer pipe through which the slurry flows back during air blowing is connected to this branch, and the tip of the slurry transfer pipe is connected to the branch. It is characterized in that it is connected to the eliminator.

(実施例) 次に本考案を図示の実施例によつて更に詳細に
説明する。
(Example) Next, the present invention will be explained in more detail with reference to the illustrated example.

1は多数の濾板2を備えたセンターフイード型
のフイルタープレス、3は原液槽であり、濾過さ
れるべき原液はポンプ4によつて原液供給管10
を介してフイルタープレス1へ送られ、その各濾
板2の中央の原液供給路から濾室内に供給され
る。5はエアブロー用の圧縮空気源であつて、脱
水濾過あるいは圧搾工程終了後にエアブローパイ
プ6を通じてフイルタープレス1の各濾板2の中
央の流路へ高圧の圧縮空気を吸込み、原液供給路
内に残留している泥漿を泥漿移送用パイプ7に向
つて逆流させる。なお泥漿移送用パイプ7は、原
液槽3とフイルタープレス1とを結ぶ原液供給管
10の途中に形成された分岐部に接続したある。
1 is a center feed type filter press equipped with a large number of filter plates 2; 3 is a stock solution tank; the stock solution to be filtered is supplied to the stock solution supply pipe 10 by a pump 4;
It is sent to the filter press 1 via the filter plate 2, and is supplied into the filter chamber from the stock solution supply path in the center of each filter plate 2. Reference numeral 5 is a compressed air source for air blowing, which sucks high-pressure compressed air into the flow path in the center of each filter plate 2 of the filter press 1 through an air blow pipe 6 after the dehydration filtration or compression process is completed, and causes the air to remain in the stock solution supply path. The slurry flowing therein is caused to flow back toward the slurry transfer pipe 7. The slurry transfer pipe 7 is connected to a branch part formed in the middle of a stock solution supply pipe 10 that connects the stock solution tank 3 and the filter press 1.

従来はこのような泥漿移送用パイプ7は原液槽
3の液中に開口していたのであるが、本考案にお
いては原液槽3の上方にエリミネータ8が設置さ
れており、泥漿移送用パイプ7の先端はこのエリ
ミネータ8に接続されている。エリミネータ8は
図示のようにケース内に多数の気液分離板9を設
けたものであつて、エアブローされた泥漿がこの
気液分離板9に衝突すると気液分離が行われ、泥
漿のみが下方の原液槽3に落下するとともに、空
気は大気中に逃げる構造となつている。
Conventionally, such a slurry transfer pipe 7 opened into the liquid in the concentrate tank 3, but in the present invention, an eliminator 8 is installed above the concentrate tank 3, and the slurry transfer pipe 7 is opened into the liquid in the concentrate tank 3. The tip is connected to this eliminator 8. As shown in the figure, the eliminator 8 has a large number of gas-liquid separation plates 9 installed in the case, and when the air-blown slurry collides with the gas-liquid separation plates 9, gas-liquid separation occurs, and only the slurry flows downward. The structure is such that the air falls into the stock solution tank 3 and escapes into the atmosphere.

(作用) このように構成されたものは、原液槽3から供
給された原液を原液供給管10を通じてフイルタ
ープレス1へ送り、その濾板2の中央に形成され
た原液供給路から各濾室内に供給して圧搾濾過を
行わせたのち、圧縮空気源5から高圧の圧縮空気
をこの原液供給路内へ導入してその内部に残留し
ている泥漿を逆流させることは従来のこの種エア
ブロー装置と変わるところはない。
(Function) In the device configured as described above, the stock solution supplied from the stock solution tank 3 is sent to the filter press 1 through the stock solution supply pipe 10, and the stock solution is fed into each filter chamber from the stock solution supply path formed in the center of the filter plate 2. After the compressed air is supplied and compressed and filtered, high-pressure compressed air is introduced from the compressed air source 5 into the raw solution supply channel to cause the slurry remaining inside to flow back, which is different from conventional air blowing devices of this type. There is nothing that will change.

しかし本考案においては、エアブローの際に泥
漿が逆流する泥漿移送用パイプ7を原液槽3とフ
イルタープレス1とを結ぶ原液供給管10の途中
の分岐部に接続されているうえ、泥漿移送用パイ
プ7の先端が原液槽3の上方に設置されたエリミ
ネータ8に接続されているため、エアブローの圧
力によりフイルタープレス1内の泥漿とともに、
原液供給管10内の泥漿のうち分岐部より先端側
のものも泥漿移送用パイプ7を通じてエリミネー
タ8へ吹き飛ばされる。そしてエアブローの圧力
は多数の気液分離板9の間から大気中に開放され
るとともに泥漿のみがその下方に設置された原液
槽3に流下することとなる。
However, in the present invention, the slurry transfer pipe 7 through which the slurry flows back during air blowing is connected to a branch in the middle of the concentrate supply pipe 10 connecting the concentrate tank 3 and the filter press 1, and the slurry transfer pipe 7 is Since the tip of the filter press 7 is connected to the eliminator 8 installed above the stock solution tank 3, the air blow pressure causes the slurry inside the filter press 1 to
Of the slurry in the stock solution supply pipe 10, that on the tip side from the branching part is also blown to the eliminator 8 through the slurry transfer pipe 7. Then, the pressure of the air blow is released to the atmosphere from between the many gas-liquid separation plates 9, and only the slurry flows down to the raw liquid tank 3 installed below.

従つて本考案によれば、従来のように原液槽3
内に衝撃が加わるおそれがないので、原液槽3内
のライニングが剥離したり振動によつて泥漿移送
用パイプ7が破損することがない。また泥漿移送
用パイプ7どなを原液槽3とフイルタープレス1
とを結ぶ原液供給管10の途中の分岐部に接続し
たので、フイルタープレス1に近い原液供給管1
0内の泥漿もエアブローにより除去される。しか
も逆流した泥漿は原液槽3内に確実に回収される
のでロスを生ずることもなく、経済性にも優れた
ものである。
Therefore, according to the present invention, the stock solution tank 3
Since there is no risk of impact being applied to the inside, the lining inside the stock solution tank 3 will not peel off or the slurry transfer pipe 7 will not be damaged due to vibration. In addition, the slurry transfer pipe 7 etc. are connected to the stock solution tank 3 and the filter press 1.
Since it is connected to a branch part in the middle of the stock solution supply pipe 10 that connects the stock solution supply pipe 1 to the filter press 1,
The slurry inside 0 is also removed by air blowing. Moreover, since the backflowing slurry is reliably collected in the stock solution tank 3, there is no loss, and it is also economically efficient.

(考案の効果) 本考案は以上の説明から明らかなように、エア
ブローの際に原液槽のライニングが剥離したり泥
漿移送用パイプが破損することがなく、しかもフ
イルタープレスの原液供給路内及び原液供給管内
の泥漿を原液槽内に確実に回収することができる
ものである。よつて本考案は従来の問題点を一掃
したフイルタープレスのエアブロー装置として、
その実用的価値は極めて大である。
(Effects of the invention) As is clear from the above explanation, the present invention prevents the lining of the stock solution tank from peeling off during air blowing and the slurry transfer pipe from being damaged. Sludge in the supply pipe can be reliably collected into the stock solution tank. Therefore, this invention is a filter press air blowing device that eliminates the problems of the conventional ones.
Its practical value is extremely great.

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

図面は本考案の実施例を示す配置図である。 1……フイルタープレス、3……原液槽、7…
…泥漿移送用パイプ、8……エリミネータ、9…
…気液分離板、10……原液供給管。
The drawing is a layout diagram showing an embodiment of the present invention. 1... Filter press, 3... Stock solution tank, 7...
...Sludge transfer pipe, 8...Eliminator, 9...
... Gas-liquid separation plate, 10... Stock solution supply pipe.

Claims (1)

【実用新案登録請求の範囲】[Scope of utility model registration request] フイルタープレス1へ濾過されるべき原液を供
給する原液槽3の上方に多数の気液分離板9を備
えたエリミネータ8を設置するとともに、原液槽
3とフイルタープレス1とを結ぶ原液供給管10
を途中で分岐させてエアブローの際に泥漿が逆流
する泥漿移送用パイプ7をこの分岐部に接続し、
更に泥漿移送用パイプ7の先端を前記エリミネー
タ8に接続したことを特徴とするフイルタープレ
スのエアブロー装置。
An eliminator 8 equipped with a large number of gas-liquid separation plates 9 is installed above the stock solution tank 3 that supplies the stock solution to be filtered to the filter press 1, and a stock solution supply pipe 10 connects the stock solution tank 3 and the filter press 1.
A slurry transfer pipe 7 is branched in the middle and the slurry flows back during air blowing, and the slurry transfer pipe 7 is connected to this branch.
The filter press air blowing device is further characterized in that the tip of the slurry transfer pipe 7 is connected to the eliminator 8.
JP1987127937U 1987-08-21 1987-08-21 Expired JPH0356244Y2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1987127937U JPH0356244Y2 (en) 1987-08-21 1987-08-21

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1987127937U JPH0356244Y2 (en) 1987-08-21 1987-08-21

Publications (2)

Publication Number Publication Date
JPS6432705U JPS6432705U (en) 1989-03-01
JPH0356244Y2 true JPH0356244Y2 (en) 1991-12-17

Family

ID=31380818

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1987127937U Expired JPH0356244Y2 (en) 1987-08-21 1987-08-21

Country Status (1)

Country Link
JP (1) JPH0356244Y2 (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP5753703B2 (en) * 2011-02-24 2015-07-22 株式会社共立 Filter press dewatering device and control method thereof
JP6924347B2 (en) * 2018-06-22 2021-08-25 株式会社石垣 Air blow device and air blow method for filter press

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS52115841A (en) * 1976-03-25 1977-09-28 Dainippon Toryo Co Ltd Equipment for recovering over-sprayed paint
JPS5549728B2 (en) * 1974-10-29 1980-12-13

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5821529Y2 (en) * 1978-09-28 1983-05-07 高砂熱学工業株式会社 eliminator

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5549728B2 (en) * 1974-10-29 1980-12-13
JPS52115841A (en) * 1976-03-25 1977-09-28 Dainippon Toryo Co Ltd Equipment for recovering over-sprayed paint

Also Published As

Publication number Publication date
JPS6432705U (en) 1989-03-01

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