JPS6231963B2 - - Google Patents

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Publication number
JPS6231963B2
JPS6231963B2 JP56211654A JP21165481A JPS6231963B2 JP S6231963 B2 JPS6231963 B2 JP S6231963B2 JP 56211654 A JP56211654 A JP 56211654A JP 21165481 A JP21165481 A JP 21165481A JP S6231963 B2 JPS6231963 B2 JP S6231963B2
Authority
JP
Japan
Prior art keywords
filter
liquid
plate
pressure
filtration
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
JP56211654A
Other languages
Japanese (ja)
Other versions
JPS58114705A (en
Inventor
Tadashi Kirisawa
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)

Description

【発明の詳細な説明】 本発明は圧濾過に用いられる濾板に関するもの
である。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a filter plate used for pressure filtration.

従来、この種の濾板にあつては第1図に示すよ
うに濾板10A,10B,10Cにおいて、板状
体1A,1Bには夫々中央部に通液孔2A,2B
が設けられ、板状体1A,1Cの内面、および板
状体1Bの両面には導液溝3A,3B,3C等の
導液手段が形成せられ、更に板状体1A,1B,
1Cには周枠4A,4B,4Cが囲設せられ、周
枠4A,4B,4Cの下縁には濾液排出導孔5
A,5B,5Cが設けられる。かくして圧濾過を
行うには濾板10A,10Cを両端に配し、複数
個の濾板10B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、この際各濾板10A,10B,10C間に
は濾布6A,6B,6Cを挾持させる。かくして
濾室10′が圧濾過器内に形成されポンプ7によ
つて被処理液を矢印に沿つて圧入径路8から濾板
10Aの通液孔2Aに圧入すれば被処理液は濾板
10B,10Cの通液孔2Bを介して矢印に沿つ
て濾布6A,6B,6C内部即ち濾室10′内部
に充満し、濾布6A,6B,6Cによつて濾過さ
れる。かくして濾液は矢印に示すように各濾板1
0A,10B,10Cの濾液排出導孔5A,5
B,5Cから排出せられる。濾布6A,6B,6
C内部に被処理液に含まれる固形分が堆積するに
つれて濾過圧は高まり、所定圧に達した所で濾過
工程を終了する。この後濾板10Aの通液孔2A
に空気、窒素ガス等の圧力気体を圧入して濾布6
A,6B,6C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10′は巾
が実質的に均一であり、濾布6A,6B,6C内
部に堆積している固形分の密度は略均一であるか
ら圧濾過器内に圧入された圧力気体は浮力によつ
て濾室10′内で選択的に上行流出する。かくし
て濾室10′内において濾布6A,6B,6C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
とになる。
Conventionally, in filter plates 10A, 10B, and 10C of this type of filter plate, as shown in FIG.
Liquid guiding means such as liquid guiding grooves 3A, 3B, 3C are formed on the inner surfaces of the plate-like bodies 1A, 1C and on both sides of the plate-like body 1B.
1C is surrounded by peripheral frames 4A, 4B, and 4C, and filtrate discharge holes 5 are provided at the lower edges of the peripheral frames 4A, 4B, and 4C.
A, 5B, and 5C are provided. In order to perform pressure filtration in this way, the filter plates 10A and 10C are arranged at both ends, and a plurality of filter plates 10B are arranged in the middle, polymerized, and fixed by applying an appropriate pressing force to both ends to form a pressure filter. However, at this time, filter cloths 6A, 6B, and 6C are sandwiched between each of the filter plates 10A, 10B, and 10C. In this way, a filter chamber 10' is formed in the pressure filter, and when the pump 7 presses the liquid to be treated from the press-in path 8 into the liquid passage hole 2A of the filter plate 10A along the arrow, the liquid to be treated flows into the filter plate 10B, It fills the inside of the filter cloths 6A, 6B, 6C, that is, the inside of the filter chamber 10' along the arrows through the liquid passage hole 2B of 10C, and is filtered by the filter cloths 6A, 6B, 6C. Thus, the filtrate flows through each filter plate 1 as shown by the arrows.
0A, 10B, 10C filtrate discharge holes 5A, 5
It is discharged from B and 5C. Filter cloth 6A, 6B, 6
As solid content contained in the liquid to be treated accumulates inside C, the filtration pressure increases, and the filtration process ends when a predetermined pressure is reached. After this, the liquid passage hole 2A of the filter plate 10A
Pressurized gas such as air or nitrogen gas is injected into the filter cloth 6.
The solid content deposited in A, 6B, and 6C is squeezed and dehydrated. However, in this case, the width of the filter chamber 10' is substantially uniform, and the density of the solids deposited inside the filter cloths 6A, 6B, and 6C is substantially uniform, so that the solids are press-fitted into the pressure filter. The pressurized gas flows selectively upwardly within the filter chamber 10' due to buoyant forces. In this way, only the upper half of the solid matter deposited inside the filter cloths 6A, 6B, and 6C in the filter chamber 10' is selectively compressed and dehydrated, while the lower half is hardly dehydrated.

本発明は上記従来の欠点を改良して濾室内部に
堆積している固形分を均一に脱水しかつ簡単に濾
液を集めることを目的とするもので表面に導液手
段を設けた板状体の、中央部には送通孔を設け、
周縁部には集液孔を設け、かつ中央部から下方に
おいて該板状体の両面を上方よりも突出させたこ
とを骨子とする。
The present invention aims to improve the above-mentioned conventional drawbacks, uniformly dehydrate the solid content deposited inside the filter chamber, and easily collect the filtrate. A through hole is provided in the center of the
The gist is that a liquid collecting hole is provided in the peripheral portion, and that both surfaces of the plate-shaped body protrude downward from the center portion more than the upper portion.

本発明を第2図以下に示す一実施例によつて説
明すれば一組の濾板20A,20B,20Cにお
いて、板状体11A,11Bには夫々中央部に通
液孔12A,12Bが設けられ、板状体11A,
11C内面および板状体11Bの両面には導液溝
30A,30B,30C等の導液手段が形成せら
れ夫々の下半部に例えば多孔質な厚板13A,1
3B,13Cが張設せられ、更に板状体11A,
11B,11Cには周枠14A,14B,14C
が囲設せられ、更に板状体11A,11B,11
Cの下周縁部には濾液を集液排出する集液孔15
A,15B,15Cが設けられ、集液孔15A,
15B,15Cには導液溝30A,30B,30
Cに通じる導孔17A,17B,17Cが連絡す
る。なお集液孔15Cは盲孔である。上記濾板2
0A,20B,20Cにおいて板状体11A,1
1B,11Cの中央部から下方における両面は厚
板13A,13B,13Cによつて上方よりも突
出せられる。
The present invention will be described with reference to an embodiment shown in FIG. and plate-shaped body 11A,
Liquid guiding means such as liquid guiding grooves 30A, 30B, 30C are formed on the inner surface of 11C and both sides of the plate-like body 11B, and porous thick plates 13A, 1 are formed in the lower half of each.
3B, 13C are stretched, and further plate-shaped bodies 11A,
11B, 11C have peripheral frames 14A, 14B, 14C
are surrounded, and further plate-like bodies 11A, 11B, 11
A liquid collection hole 15 for collecting and discharging the filtrate is located at the lower peripheral edge of C.
A, 15B, 15C are provided, and liquid collecting holes 15A,
15B, 15C have liquid guide grooves 30A, 30B, 30
Guide holes 17A, 17B, and 17C leading to C communicate with each other. Note that the liquid collecting hole 15C is a blind hole. Above filter plate 2
Plate bodies 11A, 1 at 0A, 20B, 20C
Both sides of the parts 1B and 11C below the central part are made to protrude more than above by the thick plates 13A, 13B and 13C.

上記濾板20A,20Cを両端に配し、複数個
の濾板20Bを中間に配して重合し、集液孔15
A,15B,15C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、この際各濾板20A,20B,20C間には
濾布16A,16B,16Cを挾持させる。かく
して濾室20′が圧濾過器内に形成されるが、濾
室20′の上部20′Aは巾広に規制され、下部2
0′Bは両側から巾狭に規制されている。
The filter plates 20A and 20C are arranged at both ends, and a plurality of filter plates 20B are arranged in the middle, and the liquid collection holes 15
A, 15B, and 15C are attached to each other and fixed by applying an appropriate pressing force to both ends to form a pressure filter. At this time, filter cloths 16A, 16B, and 16C are placed between each filter plate 20A, 20B, and 20C. to hold. In this way, a filter chamber 20' is formed in the pressure filter, but the upper part 20'A of the filter chamber 20' is restricted to be wide, and the lower part 20'A is restricted to a wide width.
0'B is narrowly regulated from both sides.

上記構成の圧濾過器において、ポンプ18Bに
よつて被処理液を矢印に沿つて圧入径路19から
濾板20Aの通液孔12Aに圧入すれば被処理液
は濾板20Bの通液孔12Bを介して矢印に沿つ
て濾布16A,16B,16C内部に充満し、濾
布16A,16B,16Cが導液溝30A,30
B,30Cを有する濾板20A,20B,20C
の表面および多孔質な厚板13A,13B,13
Cの表面によつて規制されることにより濾過圧を
生じ濾布16A,16B,16Cによつて濾過さ
れる。かくして濾液は濾布16A,16B,16
Cから外出し下半部は多孔質な厚板13A,13
B,13Cを介して導液溝30A,30B,30
Cに沿つて流下し導孔17A,17B,17Cを
介して矢印に沿つて集液孔15A,15B,15
Cに流入し集液孔15Aの出口から矢印に示すよ
うに排出される。かかる濾過工程においては濾室
20′の巾狭に規制されている下部20′Bが先づ
被処理液の固形分Cで充満される。この際下部2
0′Bは両側から巾狭に規制されているから下部
20′Bにおける濾過圧のかたよりはなく均一に
なり濾過効率の点で有利である。この時点では濾
室20′の巾広に規制されている上部20′Aはい
まだ固形分Cによつて完全に充満されず、隙間E
が生じている。この状態は第4図に示される。下
部20′Bが固形分Cで充満されると濾過圧が急
激に上昇するとともに濾過量が急激に低下するか
らこの時点で濾過工程を停止し、圧入径路19か
ら分岐した残液排出径路19Aを開けば上部2
0′Aの隙間、および通液孔12A,12Bに残
存する被処理液は該排出径路19Aから排除され
る。次いで排出径路19Aを閉じ圧入径路19の
分岐管19Bを開いて空気、窒素等の圧力気体を
通液孔12Aを介して圧濾過器内へ圧入する。圧
濾過器内に圧入された圧力気体は濾室20′に入
り隙間Eを介して上部20′Aに堆積している固
形分および下部20′Bに充満している固形分を
圧搾して脱水する。このように上部20′Aに堆
積している固形分Cは隙間Eを介して圧力気体に
よつて均一に圧搾されるから脱水効率が向上し、
脱水率は下部20′Bに堆積している固形分Cと
殆んど等しくなり、かくして圧濾過器全体にわた
つて略均一な固形分脱水率が得られるのである。
脱水工程が終了したら重合された濾板20A,2
0B,20Cの両端に及ぼした押圧力を除去して
濾板20A,20B,20Cを夫々開離させ、濾
布16A,16B,16C内に堆積した固形分を
取出す。
In the pressure filter having the above configuration, if the liquid to be treated is pressurized into the liquid passage hole 12A of the filter plate 20A from the press-in path 19 along the arrow by the pump 18B, the liquid to be treated passes through the liquid passage hole 12B of the filter plate 20B. The inside of the filter cloths 16A, 16B, 16C is filled along the arrows through the liquid guide grooves 30A, 30.
Filter plate 20A, 20B, 20C with B, 30C
surface and porous planks 13A, 13B, 13
By being regulated by the surface of C, a filtration pressure is generated and filtered by filter cloths 16A, 16B, and 16C. Thus, the filtrate passes through the filter cloths 16A, 16B, 16
The lower half of the board extending from C is a porous thick plate 13A, 13.
Liquid guide grooves 30A, 30B, 30 via B, 13C
The liquid flows down along C and passes through the guide holes 17A, 17B, 17C, and then flows along the arrows to the collection holes 15A, 15B, 15.
C and is discharged from the outlet of the liquid collecting hole 15A as shown by the arrow. In this filtration process, the narrowly restricted lower part 20'B of the filter chamber 20' is first filled with the solid content C of the liquid to be treated. At this time, lower part 2
Since 0'B is narrowly regulated from both sides, the filtration pressure in the lower part 20'B is not uneven but uniform, which is advantageous in terms of filtration efficiency. At this point, the width-limited upper part 20'A of the filter chamber 20' is not yet completely filled with the solid content C, and the gap E
is occurring. This state is shown in FIG. When the lower part 20'B is filled with the solid content C, the filtration pressure increases rapidly and the filtration rate decreases rapidly, so the filtration process is stopped at this point, and the residual liquid discharge path 19A branched from the injection path 19 is opened. When opened, the top 2
The liquid to be treated remaining in the gap 0'A and the liquid passage holes 12A and 12B is removed from the discharge path 19A. Next, the discharge path 19A is closed, and the branch pipe 19B of the press-in path 19 is opened to force a pressurized gas such as air or nitrogen into the pressure filter through the liquid passage hole 12A. The pressurized gas injected into the pressure filter enters the filter chamber 20' through the gap E, and dehydrates the solids deposited in the upper part 20'A and the solids filling the lower part 20'B. do. In this way, the solid content C deposited in the upper part 20'A is compressed uniformly by the pressure gas through the gap E, so that the dewatering efficiency is improved.
The dewatering rate is almost equal to the solid content C deposited in the lower part 20'B, and thus a substantially uniform solid content dewatering rate can be obtained throughout the pressure filter.
After the dehydration process is completed, the polymerized filter plates 20A, 2
The pressing force exerted on both ends of 0B and 20C is removed to separate the filter plates 20A, 20B and 20C, respectively, and the solid content accumulated in the filter cloths 16A, 16B and 16C is taken out.

本発明は上記実施例によつて限定せられるもの
ではなく、例えば第5図に示すように濾板20B
の周枠14Bに囲まれた部分、即ち濾面を円形と
し、多数の円心円状の導液孔30Bおよび放射線
状の一対の導液孔30′Bを設けてもよいし、第
6図に示すように集液孔15Bを周枠14B上に
設けて一対の導液孔30′Bによつて濾液を集液
孔15Bに導びいてもよい。
The present invention is not limited to the above embodiments, but for example, as shown in FIG.
The part surrounded by the peripheral frame 14B, that is, the filter surface, may be circular, and a large number of concentric liquid guide holes 30B and a pair of radial liquid guide holes 30'B may be provided. As shown in FIG. 1, a liquid collection hole 15B may be provided on the peripheral frame 14B, and the filtrate may be guided to the liquid collection hole 15B by a pair of liquid introduction holes 30'B.

本発明は上記構成を有するから板状体の通液孔
から濾布内に圧入された被処理液は濾布によつて
濾過され、濾液は集液孔に集められて一個所から
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 forced into the filter cloth from the liquid passage hole of the plate-like body is filtered by the filter cloth, and the filtrate is collected in the liquid collection hole and discharged from one place. The liquid collection means are thus greatly simplified.

また板状体の中央部から下方において該板状体
の両面を上方よりも突出させるから、かかる濾板
を重合することによつて形成せられた濾室は中央
部から下側が上側よりも巾狭に規制され、したが
つて濾過工程において濾室の巾狭になつた部分に
固形分が充満した時点でも濾室の巾広に規制され
た部分においては堆積した固形分に隙間が生じて
おり、かかる時点で濾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せば巾広に規
制された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り、圧濾過器全体に
わたつて略均一な固形分の脱水率が得られること
になる。
In addition, since both sides of the plate-like body protrude downward from the center of the plate-like body more than above, the filter chamber formed by superposing the filter plates has a width on the lower side from the center than on the upper side. Therefore, even when the narrow part of the filter chamber is filled with solids during the filtration process, there are gaps between the accumulated solids in the wide part of the filter chamber. At this point, if the filtration process is stopped and the remaining liquid to be treated is discharged and then pressure gas is applied, the pressure gas will squeeze the solid content through the gap in the wide regulated area, A substantially uniform solid content dewatering rate can be obtained throughout the pressure filter.

そして濾室下部は両側から巾狭に規制されてい
るので濾過圧が均等に及ぼされ易く濾過が均一に
行われ濾過効率に好影響が及ぼされる。
Since the lower part of the filtration chamber is narrowly regulated from both sides, filtration pressure is easily applied evenly, filtration is performed uniformly, and filtration efficiency is positively influenced.

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

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図は重合状態側断面図、第4図
は濾室部分の側断面図、第5図は濾板の他の実施
例の正面図、第6図は濾板の更に他の実施例の正
面図である。 図中、11A,11B,11C……板状体、1
2A,12B……通液孔、15A,15B,15
C……集液孔、20A,20B,20C……濾
板、20′……濾室、20′A……濾室の巾広の部
分、20′B……濾室の巾狭の部分。
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.
The figure is a front view, FIG. 3 is a side sectional view of the superposed state, FIG. 4 is a side sectional view of the filter chamber portion, FIG. 5 is a front view of another embodiment of the filter plate, and FIG. FIG. 7 is a front view of another embodiment. In the figure, 11A, 11B, 11C... plate-shaped body, 1
2A, 12B...Liquid hole, 15A, 15B, 15
C...Liquid collection hole, 20A, 20B, 20C...Filter plate, 20'...Filter chamber, 20'A...Wide part of the filter chamber, 20'B...Narrow part of the filter chamber.

Claims (1)

【特許請求の範囲】[Claims] 1 表面に導液手段を設けた板状体の中央部には
通液孔を設け、周縁部には集液孔を設け、かつ中
央部から下方において該板状体の両面を上方より
も突出させたことを特徴とする濾板。
1. A plate-shaped body provided with a liquid guiding means on its surface has a liquid passage hole in the center, a liquid collection hole in the peripheral edge, and both sides of the plate-shaped body protrude downward from the center from the upper side. A filter plate characterized by:
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 JPS58114705A (en) 1983-07-08
JPS6231963B2 true 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)

Families Citing this family (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

Family Cites Families (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS513191Y2 (en) * 1973-06-26 1976-01-29
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

Also Published As

Publication number Publication date
JPS58114705A (en) 1983-07-08

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