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JPS5948128B2 - filter plate - Google Patents
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JPS5948128B2 - filter plate - Google Patents

filter plate

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Publication number
JPS5948128B2
JPS5948128B2 JP56214732A JP21473281A JPS5948128B2 JP S5948128 B2 JPS5948128 B2 JP S5948128B2 JP 56214732 A JP56214732 A JP 56214732A JP 21473281 A JP21473281 A JP 21473281A JP S5948128 B2 JPS5948128 B2 JP S5948128B2
Authority
JP
Japan
Prior art keywords
filter
liquid
plate
filter plate
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
Application number
JP56214732A
Other languages
Japanese (ja)
Other versions
JPS58112009A (en
Inventor
忠 桐沢
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 JP56214732A priority Critical patent/JPS5948128B2/en
Publication of JPS58112009A publication Critical patent/JPS58112009A/en
Publication of JPS5948128B2 publication Critical patent/JPS5948128B2/en
Expired 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、この種の濾板にあっては第1図に示すように濾板
10A、 IOB、 IOCにおいて、板状体IAIB
には夫々中央部に通液孔2A、2Bが設けられ、板状体
IA、ICの内面、および板状体1Bの両面には導液溝
3A、 3B、 3 C等の導液手段が形成せられ、
更に板状体IA、IB、ICには周枠4A、4B、4C
が囲設せられ、周枠4A。
Conventionally, in this type of filter plate, as shown in FIG.
Liquid passage holes 2A, 2B are provided in the center of each, and liquid guide means such as liquid guide grooves 3A, 3B, 3C are formed on the inner surface of the plate-shaped body IA, the IC, and both sides of the plate-shaped body 1B. forced,
Furthermore, surrounding frames 4A, 4B, 4C are attached to plate-like bodies IA, IB, and IC.
is surrounded by surrounding frame 4A.

4B、4Cの下縁には濾液排出導孔5A、5B。The lower edges of 4B and 4C have filtrate discharge holes 5A and 5B.

5Cが設けられる。5C is provided.

かくして圧濾過を行うには濾板10A、 IOC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は゛して固定し、圧波過器を構成
するが、この際各濾板10A、IOB、 IOC間には
濾布6A、 6B、 6Cを挟持させる。
In order to perform pressure filtration in this way, the filter plates 10A and IOC are arranged at both ends, a plurality of filter plates 10B are arranged in the middle, they are superposed, fixed by applying an appropriate pressing force to both ends, and the pressure waver is installed. At this time, filter cloths 6A, 6B, and 6C are sandwiched between each of the filter plates 10A, IOB, and IOC.

かくして濾室10′が゛圧濾過器内に形成されポンプ7
によって被処理液を矢印に沿って圧入径路8から濾板1
0Aの通液孔2Aに圧入すれば被処理液は濾板10B、
IOCの通液孔2Bを介して矢印に沿って濾布6A、
6B、6C内部即ち濾室10′内部に充満し、濾布6A
、6B、6Cによって濾過される。
Thus, a filter chamber 10' is formed in the pressure filter and the pump 7
The liquid to be treated is passed from the press-in path 8 to the filter plate 1 along the arrow.
If the liquid is press-fitted into the liquid passage hole 2A of 0A, the liquid to be treated will flow through the filter plate 10B,
Filter cloth 6A along the arrow through the liquid passage hole 2B of the IOC,
6B, 6C, that is, the inside of the filter chamber 10' is filled with filter cloth 6A.
, 6B, 6C.

かくして濾液は矢印に示すように各濾板10A、 IO
B、 IOCの導液溝3A、 3B、 3Cを介し
て濾液排出導孔5A、5B、5Cがら排出せられる。
Thus, the filtrate flows through each filter plate 10A, IO as shown by the arrow.
B. The filtrate is discharged from the filtrate discharge holes 5A, 5B, and 5C via the liquid guide grooves 3A, 3B, and 3C of the IOC.

濾布6A、6B、6C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。
As the solid content contained in the liquid to be treated accumulates inside the filter cloths 6A, 6B, and 6C, the filtration pressure increases, and the filtration process ends when a predetermined pressure is reached.

この後濾板10Aに空気、窒素ガス等の圧力気体を圧入
して濾布6A、6B、6C内に堆積している固形分を圧
搾して脱水する。
Thereafter, a pressurized gas such as air or nitrogen gas is forced into the filter plate 10A to compress and dehydrate the solid content deposited in the filter cloths 6A, 6B, and 6C.

しがしこの場合には濾室10′は幅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−であるから圧濾過器内に圧入された圧力気
体は浮力によって濾室10′内で゛選択的に上行流出す
る。
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 approximately uniform, so that the solid content in the pressure filter is The pressurized gas selectively flows upward in the filter chamber 10' due to buoyancy.

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。
Thus, in the filter chamber 10', the filter cloths 6A, 6B,
Only the upper half of the solid content deposited inside 6C is selectively compressed and dehydrated, and 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することを目的°とし、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、
周縁部には濾液排出孔を設け、周縁部には濾液排出孔を
設け、かつ中央部から一方の側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 and uniformly dehydrate the solid content deposited inside the filter chamber. Provide a liquid hole,
The gist is that a filtrate discharge hole is provided in the peripheral edge, a filtrate discharge hole is provided in the peripheral edge, and the plate thickness on one side from the center is made larger than on the other side.

; 本発明を第2図以下に示す一実施例によって説明す
れば一組の濾板20A、 20B、 20Cにおいて、
板状体11A、 IIBには夫々中央部に通液孔12A
; The present invention will be described with reference to an embodiment shown in FIG. 2 and below. In a set of filter plates 20A, 20B, 20C,
The plate-like bodies 11A and IIB each have a liquid passage hole 12A in the center.
.

12Bが設けられ、液状体11A、 IICの内面およ
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は例え
ば多孔質にすることによって導液手段を設けた厚板13
A、 13B、 13Cが張設せられ、更に板状体11
A。
12B, and liquid guide grooves 30A, 30B are provided on the inner surface of the liquid material 11A, IIC and both surfaces of the plate-like material 11B.
A thick plate 13 on which a liquid guiding means such as 30C is formed, and the lower half of each plate is provided with a liquid guiding means by making it porous, for example.
A, 13B, and 13C are stretched, and the plate-shaped body 11
A.

11B、 IICには周枠14A、 14B、 14C
が囲設せられ、更に板状体11A、 IIB、 IIC
の下周縁部には濾液を集液排出する集液孔15A、 1
5B、 15Cが設けられ、集液孔15A、 15B、
15Cには導液溝30A。
11B, IIC has surrounding frames 14A, 14B, 14C
are surrounded, and further plate-like bodies 11A, IIB, IIC
A liquid collection hole 15A, 1 for collecting and discharging filtrate is provided at the lower peripheral edge of the 1
5B, 15C are provided, and liquid collection holes 15A, 15B,
15C has a liquid guiding groove 30A.

30B、 30Cに通じる導孔17A、 17B、 1
7Cが連絡する。
Guide holes 17A, 17B, 1 leading to 30B, 30C
7C will contact you.

なお集液孔15Cは盲孔である。上記濾板20A、 2
0B、 20Cにおいて板状体11A、 IIB、 I
ICの中央部から下側の板厚は板厚13A、 13B、
13Cによって上側の板厚よりも大となっている。
Note that the liquid collecting hole 15C is a blind hole. The above filter plate 20A, 2
In 0B, 20C, plate-like bodies 11A, IIB, I
The plate thickness from the center of the IC to the bottom is 13A, 13B,
13C, it is larger than the upper plate thickness.

上記濾板20A、 20Cを両端に配し、複数個の濾。The filter plates 20A and 20C are arranged at both ends to form a plurality of filters.

板20Bを中間に配して重合し、集液孔15A、 15
B。
The plate 20B is arranged in the middle for polymerization, and the liquid collection holes 15A, 15 are formed.
B.

15Cを夫々付合わせ、両端に適当な押圧力を及ぼして
固定して圧波過器を構成するが、この際各濾板20A、
20B、 20C間には濾布16A、 16B、 1
6Cを挟持させる。
15C are attached to each other and fixed by applying an appropriate pressing force to both ends to form a pressure wave device. At this time, each filter plate 20A,
Between 20B and 20C are filter cloths 16A, 16B, 1
6C is held between the two.

かくして濾板0′が圧濾過器内に形成されるが、濾室2
0′Aは幅広に規制され、下部20′Bは幅狭に規制さ
れている。
Thus, a filter plate 0' is formed in the pressure filter, but the filter chamber 2
0'A is regulated to be wide, and lower part 20'B is regulated to be narrow.

上記構成の圧波過器において、ポンプ18によって被処
理液を矢印に沿って圧入径路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。
In the pressure wave filter having the above configuration, if the liquid to be treated is forced into the liquid passage hole 12A of the filter plate 20A from the press-in path 19 along the arrow by the pump 18, the liquid to be treated will be transferred to the filter plate 20B.

の通液孔12Bを介して矢印に沿って濾布16A、 1
6B、 16C内部に充満し、濾布16A、 16B、
16Cが導液溝30A、 30B、 30Cを有する
濾板20A、 20B。
Filter cloth 16A, 1 along the arrow through the liquid passage hole 12B of
6B, 16C is filled with filter cloths 16A, 16B,
Filter plates 20A, 20B in which 16C has liquid guiding grooves 30A, 30B, 30C.

20Cの表面および多孔質な厚板13A、 13B、
13Cの表面によって規制されることにより濾過圧を生
20C surface and porous planks 13A, 13B,
Filtration pressure is generated by being regulated by the surface of 13C.

じ濾布16A、 16B、 16Cによって濾過される
It is filtered through filter cloths 16A, 16B, and 16C.

かくして濾液は濾液は濾布16A、 16B、 t6c
から外出し下半部は多孔質な厚板13B、 13Cを介
して導液溝30A、 30B、 30Cに沿って流下し
導孔17A。
Thus, the filtrate is filter cloth 16A, 16B, t6c.
The lower half of the liquid flows down through the porous thick plates 13B and 13C along the guide grooves 30A, 30B and 30C to the guide hole 17A.

17B、 17Cを介して矢印に沿って集液孔15A、
15B、 15C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。
Liquid collection hole 15A along the arrow via 17B, 17C,
The liquid flows into 15B and 15C and is discharged from the outlet of the liquid collection hole 15A as shown by the arrow.

かかる濾過工程においては濾室20′の幅狭に規制され
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。
In such a filtration process, the narrow lower portion 20'B of the filter chamber 20' is first filled with the solid content C of the liquid to be treated.

この時点では濾室20′の幅広に規制されている上部2
0′Aはいまだ固形分によって完全に充満されず、隙間
Eが生じている。
At this point, the upper part 2 of the filter chamber 20' is restricted to a wide width.
0'A is still not completely filled with solids, leaving a gap E.

この状態は第4図に示される。丁合l520’ 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20′Aの隙間、および通液孔12A、 12
Bに残存する被処理液は該排出径路19Aから排除され
る。
This state is shown in FIG. When the collation 1520'B is filled with the solid content C, the filtration pressure increases rapidly and the filtration rate decreases rapidly, so at this point the filtration process is stopped and the residual liquid discharge path 19A is branched from the press-in path 19. When opened, there is a gap in the upper part 20'A, and liquid passage holes 12A, 12.
The liquid to be treated remaining in B is removed from the discharge path 19A.

次いで排出径路19Aを閉じ圧入径路19の分岐管19
B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。
Next, the discharge path 19A is closed and the branch pipe 19 of the press-in path 19 is closed.
B is opened and pressurized gas such as air or nitrogen is forced into the pressure filter through the liquid passage hole 12A.

圧濾過器内に圧入された圧力気体は濾板0′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
The pressurized gas injected into the pressure filter enters the filter plate 0' through the gap E to squeeze out the solids deposited in the upper part 20'A and the solids filling the lower part 20'B. Dehydrate.

。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っ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、かくして圧波過器全体にわ
たって略均−な固形分脱水率が得られるのである。
. 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 and the dewatering rate is reduced by the solid content C deposited in the lower part 20'B. Thus, a substantially uniform solids dewatering rate can be obtained throughout the pressure waver.

脱水工程が終了したら重合された濾板2OA、 20B
、 20Cの両端に及ぼした押圧力を除去して濾板20
A、 20Bン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。
After the dehydration process is completed, the polymerized filter plates 2OA and 20B
, remove the pressing force exerted on both ends of the filter plate 20
A, 20B and 20C are separated, and the filter cloth 16A,
The solid content accumulated in 16B and 16C is taken out.

L本発明は上記実施例によって
限定されるものではない。
L The present invention is not limited to the above embodiments.

例えば第5図に示すように濾板20Bの板状体11Bの
下半部の板厚を上半部よりも大とするには板状体11B
の下半部片面のみを膨出加工させてもよいし、第6図に
示すように周枠14Bに囲まれた部分、即ち波面は円形
であってもよい。
For example, as shown in FIG. 5, in order to make the lower half of the plate 11B of the filter plate 20B thicker than the upper half, the plate 11B
Only one side of the lower half may be bulged, or the portion surrounded by the peripheral frame 14B, that is, the wave surface may be circular as shown in FIG.

本発明は上記したように中央部に通液孔を設けた板状体
の中央部から一方の側の板厚を他方の側よりも大とする
から、かかる濾板を重合することによって形成せられた
濾室は中央部から一方の側が他方の側よりも幅狭に規制
されることになり、したがって濾過工程において濾室の
幅狭に規制された部分に被処理液が充満した時点でも濾
室の幅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幅広に規
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、圧波過器全体にわたって略均
−な固形分の脱水率が得られることになる。
As described above, in the present invention, the thickness of one side from the center of the plate-shaped body provided with the liquid passage hole in the center is larger than that of the other side, so the filter plate can be formed by polymerizing. The width of the filtration chamber is narrower on one side than the other side from the center, so even when the narrowly regulated portion of the filtration chamber is filled with the liquid to be processed during the filtration process, the filtration chamber is narrower than the other side. In the wide regulated part of the chamber, gaps are created between the accumulated solids, and if the filtration process is stopped at this point and the remaining liquid to be treated is discharged, pressurized gas can be applied to the wide regulated part. In this case, the pressurized gas squeezes the solid content through the gap, and a substantially uniform dewatering rate of the solid content is obtained over the entire pressure waver.

【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側断面図、第6図は濾板
の更に他の実施例の平面図である。 図中、IIA、 IIB、 IIC・・・・・・板状体
、12A、 12B・・・・・・通液孔、15A、 1
5B、 15C・・・・・・集液孔、20A、 20B
、 20C・・・・・・濾板、20′・・・・・・濾室
、20′A・・・・・・幅広の部分、20′B・・・・
・・幅狭の部分。
Fig. 1 is a side sectional view of a conventional filter plate in a superposed state; Fig. 2 and the following show an embodiment of the present invention; Fig. 2 is a front view, Fig. 3 is a side sectional view of a superposed state; 5 is a side sectional view of a filter chamber portion, FIG. 5 is a side sectional view of another embodiment of the filter plate, and FIG. 6 is a plan view of still another embodiment of the filter plate. In the figure, IIA, IIB, IIC...Plate body, 12A, 12B...Liquid hole, 15A, 1
5B, 15C...Liquid collection hole, 20A, 20B
, 20C...Filter plate, 20'...Filter chamber, 20'A...Wide part, 20'B...
・Narrow part.

Claims (1)

【特許請求の範囲】[Claims] 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、周縁部には濾液排出孔を設け、かつ中央部から一
方の側の板厚を他方の側よりも大としたことを特徴とす
る濾板。
A plate-like body with a liquid guide means on its surface has a liquid passage hole in the center, a filtrate discharge hole in the peripheral part, and the plate thickness on one side from the center is larger than on the other side. A filter plate characterized by:
JP56214732A 1981-12-24 1981-12-24 filter plate Expired JPS5948128B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP56214732A JPS5948128B2 (en) 1981-12-24 1981-12-24 filter plate

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP56214732A JPS5948128B2 (en) 1981-12-24 1981-12-24 filter plate

Publications (2)

Publication Number Publication Date
JPS58112009A JPS58112009A (en) 1983-07-04
JPS5948128B2 true JPS5948128B2 (en) 1984-11-24

Family

ID=16660686

Family Applications (1)

Application Number Title Priority Date Filing Date
JP56214732A Expired JPS5948128B2 (en) 1981-12-24 1981-12-24 filter plate

Country Status (1)

Country Link
JP (1) JPS5948128B2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP7390579B2 (en) * 2020-12-16 2023-12-04 株式会社石垣 How to clean filter press cake

Also Published As

Publication number Publication date
JPS58112009A (en) 1983-07-04

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