GB2076682A - Centrifugal filters - Google Patents
Centrifugal filters Download PDFInfo
- Publication number
- GB2076682A GB2076682A GB8106603A GB8106603A GB2076682A GB 2076682 A GB2076682 A GB 2076682A GB 8106603 A GB8106603 A GB 8106603A GB 8106603 A GB8106603 A GB 8106603A GB 2076682 A GB2076682 A GB 2076682A
- Authority
- GB
- United Kingdom
- Prior art keywords
- filter
- centrifugal filter
- discharge
- scrapers
- cake
- 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
Links
- 239000012065 filter cake Substances 0.000 claims abstract description 5
- 238000007790 scraping Methods 0.000 claims description 25
- 238000005119 centrifugation Methods 0.000 claims description 3
- 238000007599 discharging Methods 0.000 claims 1
- 238000001914 filtration Methods 0.000 description 3
- 239000000463 material Substances 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- 238000009825 accumulation Methods 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 239000011248 coating agent Substances 0.000 description 1
- 238000000576 coating method Methods 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 230000033001 locomotion Effects 0.000 description 1
- 235000011837 pasties Nutrition 0.000 description 1
- 230000002035 prolonged effect Effects 0.000 description 1
- 239000000725 suspension Substances 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D35/00—Filtering devices having features not specifically covered by groups B01D24/00 - B01D33/00, or for applications not specifically covered by groups B01D24/00 - B01D33/00; Auxiliary devices for filtration; Filter housing constructions
- B01D35/16—Cleaning-out devices, e.g. for removing the cake from the filter casing or for evacuating the last remnants of liquid
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Centrifugal Separators (AREA)
Abstract
A filter comprising a stack of filter discs which are periodically rotated to remove cake centrifugally has a cake discharge device comprising two or more scrapers (6 and 7) which are so inclined relative to radial lines as to direct the filter cake in the filter casing (1) to an annular zone which includes the discharge opening (9) in the casing floor. The scrapers may be arranged on a wheel-like device (5) having a rim (10), spokes (12) and a hub (11) which is positioned on a central shaft (2) in the filter casing (1) beneath the filter discs and rotates with them. Intermediate radially oriented scrapers may be included. The position and inclination of scrapers may be adjustable. <IMAGE>
Description
SPECIFICATION
Centrifugal filters
The present invention relates to centrifugal filters.
Centrifugal filters, also known as disk-type pressure filters, having a plurality of filter disks arranged on a hollow shaft become coated during filtration with the material suspended in the liquid which coating is periodically removed by centrifugation, the filter residue falling to the bottom of the filter casing in which there is a discharge opening. The residue on the filter disks usually has a pasty or even a solid consistency.
With such filter devices, the residue collects at the base of the device inside the casing and it is important to remove that residue from the casing of the filter within a short time, to reduce the length of the shut-down periods. If prolonged cleaning periods to remove the filter residue are required, it would be necessary to have another, back-up filter in operation to provide continuous filtration.
It has previously been proposed, in German
Gebrauchsmuster No. 6 809 712 to provide rotating discharge paddles at the bottom of such centrifugal filters, said paddles rotating much more slowly than the shaft of the filter. With the aid of an additional gear, which is usually of the planetary type, the speed of the filter shaft may be selected such that the centrifugal force transmitted to the residue is just sufficient to enable it to drop to the bottom of the filter casing easily and thus reach the discharge opening.
However, the presence in the filter casing of filter elements moving at different speeds results in relative motions, which means that additional seals are imperative in the filter casing.
German Gebrauchsmuster No. 6 925 523 describes a centrifugal filter which is equipped with discharge scrapers which are physically attached to the filter shaft. A filter of this type has at least one outer scraper and one inner scraper.
This discharge device is connected by simple means to the drive of the hollow shaft of the filter and rotates during the centrifugal phase at the same, high speed as the filter disks. The outer scraper, which passes over the discharge opening, is inclined forward in the direction of rotation to press the residue into the discharge opening as it passes over said opening. To prevent excessive forces acting on the discharge scrapers in the event of a high accumulation of residue within a relatively short time, circular openings are provided in the discharge scrapers, which means that part of the residue passes through these openings into the space behind the scrapers and is not pushed in the direction of the discharge opening.This arrangement of the discharge scrapers results in the residue being continually centrifuged in an inward and outward direction with only a proportion of the residue being discharged from the filter casing when the outer scraper passes over the discharge opening.
There is a need for a centrifugal filter which gives a continuous, uniform discharge of the centrifuged residue without part of the residue rotating several times on the bottom of the filter casing around the axis of rotation of the filter.
The present invention provides a centrifugal filter in which filter cake is removed from a filter surface by centrifugation and is discharged through a discharge opening wherein the centrifugal filter is provided with two or more scraping members capable of rotation about a central axis, there being at least one outer and one inner scraping member, the outer scraping member having the outer edge as the leading edge and the inner scraping member having the inner edge as the leading edge. Suitably there is at least one additional scraping member present which is so positioned as to pass over the discharge opening when moved. Holes are not necessary in the scraping members.
Suitably the cake discharge device consists of a star-shaped scraper equipped with a number of radial arms, at least one discharge scraper being attached to each arm, the outer scrapers having the outer edge as the leading edge and the inner scrapers having the inner edge as the leading edge.
Suitably the scraping members are arranged on one or more arms extending radially from the centre of the base, preferably such that there is at least one scraping member on each arm and especially such that there is at least one outer scraping member and at least one inner scraping member on the same arm. It is another embodiment of the invention that scraping members are so arranged on the arms that they are staggered from the outer edge of the base to the centre of the base in the shape of a spiral of at least one flight.
According to a further embodiment of the invention, the position of the scraping members is adjustable in order to obtain the optimum discharge period for the various residues, the degree of inclination of the edges of each of the scraping members being the same or different.
The advantages obtained with the invention lie particularly in the fact that a residue flow is achieved in the bottom part of the filter casing, the maximum depth of the material being on the radius of the discharge opening. Contrary to the hitherto known types, the residue is not centrifuged alternately from the outside to the inside and vice versa to fall or be pressed into the discharge opening, which is suitably eccentric, when it happens to pass it, but is continually directed into the annular area above the discharge opening. It then drops automatically into the discharge opening.
One form of centrifugal filter of the invention will now be described, by way of example only, with reference to the accompanying drawings in which:
Figure 1 shows a sectional view of the centrifugal filter;
Figure 2 shows a horizontal cross-sectional view of the centrifugal filter taken above a filter scraper unit; and
Figure 3 shows a horizontal cross-sectional view of the centrifugal filter as in Figure 2 with a modified filter scraper unit.
Referring first to Figure 1, a cylindrical filter casing (1) is in the form of a vertical pressure vessel. A filter package contained therein comprises a central shaft (2) which is supported by bearings in the vessel lid and in the bottom (4) of the casing (1) and on which a plurality of filter disks (3) having intermediate seals are arranged.
A scraper unit (5), which is rigidly fixed to the central shaft (2), is located beneath the filter package. The lower edge of each of the discharge scrapers, outer discharge scrapers (6) and inner discharge scrapers (7), attached to the scraper base (5) is adapted to the shape of the bottom (4) of the casing (1 ) with a minimum tolerance.
Beneath the scraper base (5) and displaced to one side is a discharge opening (9).
Referring now to Figure 2, the scraper unit (5) comprises an annular rim (10) which is concentric with the casing (1) and which is supported from a hub (11) surrounding the shaft (2) by a plurality of spokes (12). The outer discharge scrapers (6) are positioned under the rim on alternate spokes and are angled in the direction of rotation of the shaft (2) (as shown by the arrow). The inner discharge scrapers (7) extend from the hub (11) at the base of the same spokes which carry the outer discharge scrapers (6) and are also angled in the direction of rotation though to a lesser degree than the outer discharge scrapers (6). The discharge opening (9) is displaced to one side of the casing (1).
Referring now to Figure 3, the scraper unit (5) made up of rim (10), hub (11) and spokes (12) has an additional set of intermediate scrapers (8) positioned parallel to and adjacent the spokes which do not carry the outer discharge scrapers (6). The casing (1), central shaft (2) and displaced discharge opening (9) are shown.
During filtration a suspension is introduced at the top of the centrifugal filter and runs down over the filter disks, the filter disks become coated with filter residue (also called the filter cake). The cake may be subjected to aftertreatment, for example washing, and then discharged. In order to remove the cake, the filter package is rotated by means of an external drive motor with the result that the cake on the filter disks (3) is centrifuged outwards
against the wall of the casing (1). From there, the
cake drops down and collects on the bottom (4) of the casing (1). The discharge scrapers (6 and 7)
convey the cake which accumulates on the
bottom (4) towards the cake discharge opening
(9) and the cake than leaves the casing through this opening. In detail, the filter cake is conveyed
by the outer discharge scrapers (6) in the direction
of rotation to the annular discharge area
incorporating the discharge opening (9) and is also conveyed by the inner discharge scrapers (7)
likewise in the direction of rotation to the annular discharge area. The solids flow reaches its maximum height at the radius of the discharge opening (9). The provision of the intermediate discharge scrapers (8) promotes the transport of the cake within the annular discharge area to the discharge opening (9) as those scrapers are positioned to travel over that opening. As can be seen from Figures 2 and 3, the trailing edges of the outer and inner discharge scrapers (6 and 7) extend slightly over the perimeter of the discharge opening.
Claims (10)
1. A centrifugal filter in which filter cake is removed from a filter surface by centrifugation and is discharged through a discharge opening wherein the centrifugal filter is provided with two or more scraping members capable of rotation about a central axis, there being at least one outer and one inner scraping member the outer scraping member having the outer edge as the leading edge and the inner scraping member having the inner edge as the leading edge.
2. A centrifugal filter as claimed in claim 1, wherein at least one additional scraping member is present which is so positioned as to pass over the discharge opening when moved.
3. A centrifugal filter as claimed in claim 1 or claim 2, wherein the scraping members are arranged on one or more arms extending radially from the centre of the base.
4. A centrifugal filter as claimed in claim 3, wherein there is at least one scraping member on each arm.
5. A centrifugal filter as claimed in claim 3 or claim 4, wherein there is at least one outer scraping member and at least one inner scraping member on the same arm.
6. A centrifugal filter as claimed in any one of claims 3 to 5, wherein the scraping members are so arranged on the arms that they are staggered from the outer edge of the base to the centre of the base in the shape of a spiral of at least one flight.
7. A centrifugal filter as claimed in any one of
claims 1 to 6, wherein the alignment of the
scraping members is adjustable.
8. A centrifugal filter as claimed in any one of
claims 1 to 7, wherein the positioning of the
scraping members is adjustable.
9. A centrifugal filter as claimed in claim 1, which is substantially as described herein with
reference to and as illustrated by the
accompanying drawings.
10. A disk-type pressure filter having a
centrifugal cake discharge device and a discharge
opening at the bottom of the casing, wherein the
cake-discharging device consists of a star-shaped scraper having a plurality of radial arms, to which at least one discharge scraper is attached, the outer scraper having the outer edge as the leading edge and the inner scraper having the inner edge as the leading edge.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE19803011622 DE3011622C2 (en) | 1980-03-26 | 1980-03-26 | Disc pressure filter |
Publications (2)
Publication Number | Publication Date |
---|---|
GB2076682A true GB2076682A (en) | 1981-12-09 |
GB2076682B GB2076682B (en) | 1984-08-15 |
Family
ID=6098352
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB8106603A Expired GB2076682B (en) | 1980-03-26 | 1981-03-03 | Centrifugal filters |
Country Status (4)
Country | Link |
---|---|
DE (1) | DE3011622C2 (en) |
FR (1) | FR2479012A1 (en) |
GB (1) | GB2076682B (en) |
NL (1) | NL8100831A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0993853A2 (en) * | 1998-10-16 | 2000-04-19 | Filtra di Pruni S. & C. S.n.c. | A device for filtering liquid substances |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE3339177A1 (en) * | 1982-11-25 | 1984-07-05 | Passavant-Werke AG & Co KG, 6209 Aarbergen | Process and device for purifying waste water or treating utility water |
Family Cites Families (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE1250785B (en) * | 1962-07-09 | 1967-09-28 | Erlenbach Zürich Dr.-Ing. Hans Müller (Schweiz) | Device for emptying solid filtration residues from rotary disc filters |
DE6809712U (en) * | 1968-12-03 | 1969-04-10 | Schenk Filterbau Gmbh | CENTRIFUGAL CLEANING FILTER |
DE6929523U (en) * | 1969-07-24 | 1969-11-13 | Schenk Filterbau G M B H Fa | CENTRIFUGAL CLEANING FILTER |
-
1980
- 1980-03-26 DE DE19803011622 patent/DE3011622C2/en not_active Expired
-
1981
- 1981-02-19 NL NL8100831A patent/NL8100831A/en not_active Application Discontinuation
- 1981-03-03 GB GB8106603A patent/GB2076682B/en not_active Expired
- 1981-03-25 FR FR8105966A patent/FR2479012A1/en active Granted
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0993853A2 (en) * | 1998-10-16 | 2000-04-19 | Filtra di Pruni S. & C. S.n.c. | A device for filtering liquid substances |
EP0993853A3 (en) * | 1998-10-16 | 2000-06-21 | Filtra di Pruni S. & C. S.n.c. | A device for filtering liquid substances |
Also Published As
Publication number | Publication date |
---|---|
GB2076682B (en) | 1984-08-15 |
DE3011622A1 (en) | 1981-10-01 |
FR2479012B3 (en) | 1982-12-03 |
DE3011622C2 (en) | 1985-03-28 |
FR2479012A1 (en) | 1981-10-02 |
NL8100831A (en) | 1981-10-16 |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
PG | Patent granted |