JPS58114705A - Filter plate - Google Patents

Filter plate

Info

Publication number
JPS58114705A
JPS58114705A JP56211654A JP21165481A JPS58114705A JP S58114705 A JPS58114705 A JP S58114705A JP 56211654 A JP56211654 A JP 56211654A JP 21165481 A JP21165481 A JP 21165481A JP S58114705 A JPS58114705 A JP S58114705A
Authority
JP
Japan
Prior art keywords
filter
liquid
hole
plate
center
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
JP56211654A
Other languages
Japanese (ja)
Other versions
JPS6231963B2 (en
Inventor
Tadashi Kirisawa
桐沢 忠
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.)
NIPPON ENBAIRO KOGYO KK
Original Assignee
NIPPON ENBAIRO 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 NIPPON ENBAIRO KOGYO KK filed Critical NIPPON ENBAIRO KOGYO KK
Priority to JP56211654A priority Critical patent/JPS58114705A/en
Publication of JPS58114705A publication Critical patent/JPS58114705A/en
Publication of JPS6231963B2 publication Critical patent/JPS6231963B2/ja
Granted legal-status Critical Current

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  • Filtration Of Liquid (AREA)

Abstract

PURPOSE:To obtain a nearly uniform dehydrating rate of solid matter over the whole parts of a pressure filter by varying the thickness of each pressure filter plate which has a liquid passing hole in the center and a liquid collecting hole at the circumferential edge from the center part to both sides. CONSTITUTION:Platelike bodies 11A and 11B of filter plates 20A-20C have liquid passing holes 12A and 12B at the center parts, flow guiding grooves 30A-30C are formed in internal surfaces of the platelike bodies 11A and 11C and both surfaces of the body 11B, and, for example, porous thick plates 13A-13C are provided at lower half parts respectively. Further, the platelike bodies 11A- 11C have circumferential frames 14A- 14C and holes 15A-15C for collecting and discharging filtered liquid at low circumferences, and communicate with the grooves 30A-30C through conduit holes 17A-17C. The hole 15C is a blind hole. Thus, the thickness of the lower side then the central part of each filter plate is made larger than the upper side thereof; they are arranged as shown in figure, and filter cloths 16A-16C are sandwiched between filter plates. Consequently, the upper part 20A' of a filter room 20' is wider than the lower part 20'B and liquid to be filtered is forced in as shown by an arrow through a pump 18B to make nearly uniform the dehydrating rate of solid matter deposited in each filter room.

Description

【発明の詳細な説明】 本発明は圧濾過に用いられる履板に関するものである。[Detailed description of the invention] The present invention relates to a track board used for pressure filtration.

従来、この種の履板にあ1て紘第1図に示すように履板
(至)ム、QΦB、曽Cにおいて、板状体(1)ム、(
1)Bには夫々中央部に通液孔は)ム、(2)農が設け
られ、板状体(1)ム、(1)O+IO内面、および板
状体(1)BO1iliKハ導液溝(3)ム、 (3)
11 、 (3)0が形成せられ、更に板状体0)ム、
 (1)B 、 (1)OKは周枠(4)ム、(4)B
 、(4)0が囲設せられ、周枠←)ム、 (4)Im
 、 (4)0の下縁には濾液排出導孔(5)ム。
Conventionally, in this type of shoe, as shown in Fig. 1, a plate-like body (1), (
1) B has a liquid passage hole in the center, (2) a plate-like body, (1) an inner surface of O+IO, and a liquid-conducting groove on the plate-like body (1) BO1iliK. (3) Mu, (3)
11, (3)0 is formed, and a plate-like body 0)mu,
(1) B, (1) OK is the surrounding frame (4) M, (4) B
, (4) 0 is surrounded and the surrounding frame ←) Mu, (4) Im
, (4) A filtrate discharge hole (5) is provided on the lower edge of the 0.

(5) B 、 (5) Oが設けられる。かくして圧
濾過を行うには罐板叫ム、QOOを両端に配し、複数個
の履板04Bを中間に配して重合し、両端に適当な押圧
力を及ぼして固定し、圧濾過器を構成するが、この際各
鑵板(至)ムeQIB−α4c間には濾布(6)ム、(
8)B、(8)Oを挾持させる。かくして−室員宛圧濾
過器内に形成されポンプ(7)Kよ−て被処理液を矢印
に沿って圧入径路(8)から濾板曽ムの通液孔(2)ム
に圧入すれば被処理液は濾板QIB。
(5) B and (5) O are provided. In order to perform pressure filtration in this way, the pressure filter is placed at both ends, and a plurality of shoe plates 04B are placed in the middle, overlapped, and fixed by applying an appropriate pressing force to both ends, and the pressure filter is installed. At this time, a filter cloth (6), (
8) Hold B and (8) O. In this way, if the liquid to be treated is forced into the liquid passage hole (2) of the filter plate from the injection path (8) along the arrow by the pump (7) K formed in the pressure filter for the chamber member. The liquid to be treated is filter plate QIB.

o40の通液孔(2)Bを介して矢印に沿って濾布(6
)h 、 (6)11 、 <ts)O内[p・チtl
l*Otl内部ニ充満し、濾布(6)ム、(6)B、(
6)OKよって濾過される。かくして濾液社矢印に示す
ように各濾板(ト)AlOB、@0の濾液排出導孔(5
)ム、(5)B、(5)0から排出せられる。濾布(6
)ム、 (8)B 、 (6)(3内部に被処理液に含
まれる固形分が堆積するにつれて一過圧は高まシ、所定
圧に達した所で濾過工程を終了する。この後−板(至)
ムの通液孔Q)五に空気。
Insert the filter cloth (6) along the arrow through the liquid passage hole (2)B of o40.
) h , (6)11 , <ts) in O [p・chi tl
l*Otl is filled with filter cloth (6), (6) B, (
6) Filtered by OK. Thus, as shown by the filtrate arrow, each filter plate (g) AlOB, @0 filtrate discharge hole (5
)um, (5)B, (5)0. Filter cloth (6
) M, (8) B, (6) (3) As the solid content contained in the liquid to be treated accumulates inside, the temporary pressure increases, and the filtration process ends when the predetermined pressure is reached. After this - board (to)
Air in the liquid passage hole Q).

鷹素ガス等の圧力気体を圧入して濾布(6)ム、(6)
11、(@)0内に堆積している固形分を圧搾して脱水
する。しかしこの場合には濾室−′は巾が実質的に均一
であシ、濾布(6)ム、(8)B、(6)0内部に堆積
している固形分の密度は略均−であるから圧−過器内に
圧入された圧力気体は浮力によって一室叫ζで選択的に
上行流出する。かくして−室町内において濾布(6)ム
、 (6)B 、 (6)O内部に堆積している固形分
は上半部のみが選択的に圧搾脱水せられ下半部は殆んど
脱水せられないことに&る。
Pressure gas such as falcon gas is injected into the filter cloth (6), (6)
11. Squeeze and dehydrate the solid content deposited in (@)0. However, in this case, the width of the filter chamber is substantially uniform, and the density of the solids deposited inside the filter cloth (6), (8)B, and (6)0 is approximately uniform. Therefore, the pressurized gas pressurized into the pressurizer selectively flows upward in one chamber at a rate of ζ due to buoyancy. Thus, in Muromachi, only the upper half of the solids deposited inside the filter cloths (6) M, (6) B, and (6) O are selectively compressed and dehydrated, while the lower half is mostly dehydrated. I can't help it.

本発明は上記従来の欠点を改良して鑵室内部に堆積して
いる固形分を均一に脱水しかつ簡単に濾液を集める仁と
を目的とするもので板状体の中央部には送通孔を設け、
周縁部には集液孔を設置、かつ中央部から一方の伺の板
厚を他方の側よりも大としたことを骨子とする。
The purpose of the present invention is to improve the above-mentioned conventional drawbacks, to uniformly dehydrate the solid content accumulated inside the iron chamber, and to easily collect the filtrate. Make a hole,
The key points are that liquid collection holes are installed on the periphery, and the plate thickness on one side from the center is thicker than on the other side.

本発明を第2図以下に示す一実施例によつて説明すれば
一組Oll板曽ム、(2)1.−〇にお−て、板状体(
ロ)ム、鵠Bには夫々中央11に通液孔(ロ)ム、(至
)Bが設けられ、板状体(2)ム、鴎C内面および板状
体(1)Bの両画には導流溝−ム、−B。
The present invention will be explained with reference to an embodiment shown in FIG. 2 and below: (2) 1. −〇, the plate-shaped body (
B) M and B are provided with liquid passage holes (R) M and B in the center 11, respectively, and both sides of the plate-shaped body (2) M, the inner surface of the C and the plate-shaped body (1) B are provided. There is a flow guide groove, -B.

が形成せられ夫々の下半部に例えば多孔質な厚板(至)
ム、Q1n、(4cが張設せられ、更に板状体@ム、(
ロ)B、(ロ)OK”は屑枠鱒ム、@B、(ロ)Cが囲
設せられ、廻に板状体(ロ)A、(ロ)B、(ロ)CO
下周縁部には濾液を集液排出する集液孔(ト)A、QQ
B、(至)Cが設けられ、集液孔四ム、(ハ)B、(ト
)Cには導流溝に)ム、曽B、OIO[通じる。導孔a
ηム、(ロ)B、Q30が連絡する。なお集液孔(至)
Cは盲孔である。上妃濾板曽B、(ホ)Cにおいて板状
体aIB、(ロ)Cの中央部から下側の板厚は厚板(至
)ム、(至)B、(至)Cによって上側の板厚よυも大
とせられる。
is formed and the lower half of each is made of e.g. a porous plank.
Mu, Q1n, (4c is stretched, and the plate-like body @mu, (
B) B, (b) OK" are waste frame trout, @B, (b) C are surrounded, and the plate-like bodies (b) A, (b) B, (b) CO
There are liquid collection holes (G) A and QQ on the lower periphery to collect and discharge the filtrate.
B, (to) C are provided, and the liquid collecting holes (4), (c) B, (g) C are connected to the flow guide grooves), (3) B, and (3) OIO. Guide hole a
η M, (b) B, Q30 will contact you. In addition, the liquid collection hole (to)
C is a blind hole. The thickness of the lower plate from the center of the plate-like bodies aIB and (b) C in the upper filter plates B and (e) C is the thickness of the upper plate by the thick plate (to) m, (to) B, and (to) C. The board thickness υ can also be increased.

上記濾板(1)ム、@Jaを両端に配し、複数個の濾板
gOBt−中闇に配゛して重合し、集液孔αiIA。
The above filter plate (1) is arranged with @Ja on both ends, and is polymerized with a plurality of filter plates gOBt arranged in the middle to form a liquid collecting hole αiIA.

(至)B、(至)0を夫々付合わせ、両端に適当な押圧
力を及ぼして固定して圧濾過器を構成するが、との際各
濾板瞬ム、&JB、曽C間には1布04ム。
(To) B and (To) 0 are attached to each other, and an appropriate pressing force is applied to both ends to fix them to form a pressure filter, but between each filter plate, &JB, and C, 1 cloth 04mm.

(至)B、(40を挾持させる。かくして濾室げが圧線
過器内に形成されるが、濾室イの上Sばムは     
   1巾広であシ、下部cdBは中挟になっている。
(To) B, (40 is clamped. In this way, a filter chamber is formed in the pressure line filter, but the upper S chamber of the filter chamber is
It is 1 width wide, and the lower cdB is sandwiched in between.

上記構成の圧−過11に#いて、ポンプ@によって被処
理液を矢印に沿って圧入径路(2)から濾板曽ムの通液
孔(至)ムに圧入すれば被電m*は濾板@Bの通液孔(
至)1を介して矢印に沿うて濾布ム、@B、@0から外
出し導流溝−ム、−1゜#OK沿って流下し導孔(2)
ム、@@B、四〇を介、して矢印に沿って集液孔■ム、
曽B、@OK流入し集液孔(至)ムの出口から矢印に示
すように排出される。かかる−過工穏においては一童−
i中挟の下部−1が先づ被処理液の固形分Cで充満され
る。仁の時点では濾*tdo巾広の上部ばムはいまだ1
iIjlI分OKよって完全に充満されず、隙間Iが生
じている。この状1は第411に示される。下部−1が
1iIy#分Cで充満されると濾過圧が急激に上昇する
とと4に濾過量が急激に低下するからこの時点で線通工
程を停止し、圧入径路(2)から分岐した残液排出径路
■ムを開けば上部−′ムの隙間、および通液孔#ム1、
(ロ)Bff、残存する。被処理液は該排出径路(6)
ムから排除される0次いで排出径路(2)ムを閉じ圧入
径路(至)の分岐管(至)Bを開いて空気、i1素等の
圧力気体を通液孔(至)ムを介して圧線過器内へ圧入す
る。圧線過器内に圧入された圧力気体は瀘室四に入り隙
間Eを介して上部dムに堆積している固形分および下部
mBK充満しているwA形分を圧搾して脱水する。この
ように上部−1に堆積してiる固形分Cは隙間Eを介し
て圧力気体によ1て均一に圧搾されるから脱水効率が向
上し、脱水率は下11AfdBK堆積している固形分C
と殆んど等しくなプ、かくして圧線過器全体にわたって
略掬−な固形分脱水率が得られるやである。脱水工程が
終了したら重合された一板曽ム、94B。
In the pressure filter 11 with the above configuration, if the liquid to be treated is forced into the liquid passage hole (to) of the filter plate from the injection path (2) along the arrow with the pump @, the energized m* is Liquid passage hole in plate @B (
To) 1, go out along the arrow through the filter cloth, @B, @0 and flow down through the guide groove, -1° #OK to the guide hole (2)
M, @@B, through 40, follow the arrow to the liquid collection hole ■ M,
So B, @OK flows in and is discharged from the outlet of the liquid collecting hole as shown by the arrow. Such - one child in overwork -
The lower part -1 of the i-middle is first filled with the solid content C of the liquid to be treated. At the time of Jin, the upper part of the filter width is still 1.
Due to the iIjlI minute OK, it is not completely filled and a gap I is created. This state 1 is shown in No. 411. When the lower part-1 is filled with 1iIy# of C, the filtration pressure increases rapidly and the filtration rate decreases rapidly. If you open the liquid discharge path #m, there will be a gap between the upper part and the liquid passage hole #1,
(b) Bff remains. The liquid to be treated is discharged through the discharge path (6)
Next, close the discharge path (2) and open the branch pipe (to) B of the injection path (to) to allow pressurized gas such as air or i1 to pass through the liquid hole (to) and pressurize it. Press fit into the radiation device. The pressurized gas injected into the strainer enters the filter chamber 4 through the gap E to compress and dehydrate the solid content deposited in the upper part d and the wA part filled in the lower part mBK. In this way, the solid content C deposited on the upper part 1 is compressed uniformly by the pressure gas through the gap E, so that the dewatering efficiency is improved, and the dewatering rate is lower than the solid content C deposited on the lower part 11AfdBK. C
Thus, a substantially low solids dewatering rate can be obtained over the entire pressure liner. After the dehydration process is completed, the polymerized Ippai Somu, 94B.

韓Cの両端に及ぼした押圧力を除去して濾板…ム、−B
、(イ)0を夫々開離させ、I11布(2)ム、QIB
、QiO内に堆積した固形分を取出す。
Remove the pressing force exerted on both ends of Korea C and remove the filter plate...Mom, -B
, (a) 0 respectively, I11 cloth (2) Mu, QIB
, the solid content deposited in QiO is taken out.

本発明は上記実施例によって限定せられるものではなく
、例えば第4図に示すように一板瞬toM*綽1に@ま
れだ部分、即ち線面を円形とし、多数の同心円状の導液
孔…Bおよび放射線状の一対の導液孔−1を設けてもよ
いし、第5図に示すように集液孔os農を周枠64B上
に設けて一対の導液孔−IKよって■液を集液孔(2)
IK導びいてもよい。
The present invention is not limited to the above embodiments, and for example, as shown in FIG. ...B and a pair of radial liquid guide holes -1 may be provided, or as shown in FIG. Liquid collection hole (2)
IK may also be used.

本発明は上記構成を有するから板状体の通液孔から鑵布
内に圧入された被処理液は縮重によつて一過され、濾液
は集液孔に集められて一偶所から排出され、かくして集
液手段は極めて簡単化される。
Since the present invention has the above-mentioned configuration, the liquid to be treated that is press-injected into the iron cloth through the liquid passage hole of the plate-like body is passed through by degeneracy, and the filtrate is collected in the liquid collecting hole and discharged from one joint. The liquid collecting means is thus greatly simplified.

また板状体の中央部から一方の側の板厚を他方の側よ)
も大とするから、かかる■板を重合することKよって形
成せられた一室は中央部から一方の何が他方の側よりも
中杭にな)、シたかつて一過工程において一室の中挟に
なった部分に被処理液が充満した時点でも11w1の巾
広の部分においては堆積したm形分K[閤が生じてお)
、かかる時点で一過工程を停止して残存する被処理液を
排出後に圧力気体を及ぼぜば巾広の部分においては圧力
気体は該隙間を介して固形分を圧搾することにな夛、圧
濾過器全体にわたうて略均−な固形分の脱水率が得られ
ることになる。
Also, change the thickness of one side from the center of the plate to the other side)
Since the size of the board is also large, one chamber formed by polymerizing such a board is formed from the central part (one side is more central than the other), Even when the sandwiched part is filled with the liquid to be treated, the m-type part K that has accumulated in the wide part of 11w1 [occurs]
At this point, if the pressure gas is applied after the temporary process is stopped and the remaining liquid to be treated is discharged, the pressure gas will squeeze out the solid content through the gap in the wide area. A substantially uniform solid content dewatering rate can be obtained throughout the filter.

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

第1図は従来の濾板重合状態側断面図、第2図以下は本
考案の一実施例を示すものであり、第2図は正面図、第
3図は重合状騙側断面図、第4WJはg室部分の側断面
図、615図に他の実施例の正面図、第6図はI!に他
の実施例の正面図である。
Fig. 1 is a side sectional view of a conventional filter plate in a superposed state, and Fig. 2 and the following show an embodiment of the present invention. 4WJ is a side sectional view of the g chamber portion, Figure 615 is a front view of another embodiment, and Figure 6 is I! FIG. 3 is a front view of another embodiment.

Claims (1)

【特許請求の範囲】[Claims] 板状体の中央部には通液孔を設け、屑緻部には集液孔を
設け、かつ中央部から一方のllO板厚を他方の側よ)
も大とした仁とを待機とする濾板
A liquid passage hole is provided in the center of the plate, a liquid collection hole is provided in the waste part, and one llO plate thickness is extended from the center to the other side)
A filter plate with a large grain on standby.
JP56211654A 1981-12-28 1981-12-28 Filter plate Granted JPS58114705A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP56211654A JPS58114705A (en) 1981-12-28 1981-12-28 Filter plate

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP56211654A JPS58114705A (en) 1981-12-28 1981-12-28 Filter plate

Publications (2)

Publication Number Publication Date
JPS58114705A true JPS58114705A (en) 1983-07-08
JPS6231963B2 JPS6231963B2 (en) 1987-07-11

Family

ID=16609371

Family Applications (1)

Application Number Title Priority Date Filing Date
JP56211654A Granted JPS58114705A (en) 1981-12-28 1981-12-28 Filter plate

Country Status (1)

Country Link
JP (1) JPS58114705A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107081016A (en) * 2017-05-31 2017-08-22 四川建源节能科技有限公司 A kind of filter membrane

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5023398U (en) * 1973-06-26 1975-03-15
JPS522744A (en) * 1975-06-24 1977-01-10 Nippon Serufuotsuku Kk Method for producing fiber for light conduction
JPS5626513A (en) * 1979-08-09 1981-03-14 Kurita Mach Mfg Co Ltd Filter plate for filter press

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5023398U (en) * 1973-06-26 1975-03-15
JPS522744A (en) * 1975-06-24 1977-01-10 Nippon Serufuotsuku Kk Method for producing fiber for light conduction
JPS5626513A (en) * 1979-08-09 1981-03-14 Kurita Mach Mfg Co Ltd Filter plate for filter press

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107081016A (en) * 2017-05-31 2017-08-22 四川建源节能科技有限公司 A kind of filter membrane

Also Published As

Publication number Publication date
JPS6231963B2 (en) 1987-07-11

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