GB1576390A - Creación de Inventos y Patentes con Inteligencia Artificial

GB1576390A – Filter press
– Google Patents

GB1576390A – Filter press
– Google Patents
Filter press

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Publication number
GB1576390A

GB1576390A
GB25491/77A
GB2549177A
GB1576390A
GB 1576390 A
GB1576390 A
GB 1576390A
GB 25491/77 A
GB25491/77 A
GB 25491/77A
GB 2549177 A
GB2549177 A
GB 2549177A
GB 1576390 A
GB1576390 A
GB 1576390A
Authority
GB
United Kingdom
Prior art keywords
filter
compression
pressurising
frames
filtration
Prior art date
1976-09-08
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
GB25491/77A
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.)

Individual

Original Assignee
Individual
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.)
1976-09-08
Filing date
1977-06-17
Publication date
1980-10-08

1977-06-17
Application filed by Individual
filed
Critical
Individual

1980-10-08
Publication of GB1576390A
publication
Critical
patent/GB1576390A/en

Status
Expired
legal-status
Critical
Current

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Classifications

B—PERFORMING OPERATIONS; TRANSPORTING

B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL

B01D—SEPARATION

B01D25/00—Filters formed by clamping together several filtering elements or parts of such elements

B01D25/12—Filter presses, i.e. of the plate or plate and frame type

Description

(54) FILTER PRESS
(71) I, TAKESHI HovA, a Citizen of
Japan of Bushidanchi 12-101, Oaza Bushi 997-8, Irumashi, Saitamaken, Japan, do hereby declare the invention for which I pray that a patent may be granted to me, and the method by which it is to be performed, to be particularly described in and by the following statement: – The present invention relates to a filter press.
According to the present invention, there is provided a filter press comprising: a plurality of annular filter frames; a plurality of annular filter elements of shapes substantially corresponding to that of said filter frames, disposed between respective adjacent pairs of the filter frames, the assembled filter frames and filter elements forming a tubular structure, the interior of which defines a compression chamber; closure means for closing the ends of the tubular structure; a substantially tubular flexible pressurising member disposed longitudinally within said tubular structure; liquid feeding means for feeding liquid to be filtered into said compression chamber externally of said pressurising member; and compression fluid supplying means for supplying compression fluid to the interior of said pressurising member.
The invention will be further described with reference to the accompanying drawings, in which: – Figure 1 is a schematic illustration of a part of a conventional filter press;
Figure 2 is a sectional view of the structure of a preferred embodiment of filter press in accordance with the present invention;
Figure 3 is a perspective view of the filter frame, filter cloth and guide bar of the filter press of Figure 2; and
Figure 4 is a schematic illustration of the filter press of Figure 2.
Conventionally, a variety of filter presses have been proposed and actually used. For instance, Figure 1 shows one popular type of single acting filter press consisting of a filter plate 1, a filter frame 2 and a filter cloth 3 disposed between the filter plate 1 and the filter frame 2 to be clamped between and compressed by them. A liquid to be treated is supplied to the filter frame 2, and then passed through the filter cloth 3. The liquid is finally collected through communication ports from a recess 4 of the filter plate 1. A cake 5 of separated materials left on the filter frame 2 can be removed at the time of separation of the filter plate 1 and the filter frame 2 from each other.
Although filter presses of this type provide an easy collection of the filtrated cake by separation of the filter plate 1 and the filter frame 2 from each other, the following problem is inevitably caused due to the single acting nature which relies solely on the pressure exerted on the liquid to be filtered. Namely, as the cake caught by the filter frame 2 is accumulated as a result of continuous operation of the filter press, a higher pressure on the liquid is required to make the liquid to pass through the filter mesh. This drastic increase of the required pressure of the liquid disadvantageously causes rapid wearing of the piston for pressurising the liquid and, consequently, necessitates a frequent renewing of parts of the piston such as the lip of the piston.
Another disadvantage is that repeated assembling and disassembling of the filter is necessary for performing complete separation of the liquid and the solid, since the capacity of the filter press for housing the liquid is very small, detracting from the performance of the filter press.
Referring to Figure 2 and the subsequent Figures showing an embodiment of the present invention, a filter press in accordance with the invention for use in filtration of a highly viscous liquid such as fowl-droppings or sea-bottom mud is generally denoted by a numeral 6.
The filter press 6 is constituted by a compression part 7, a liquid-introducing part 8 and a pressurising medium feeding part 9. The compression part 7 includes four guide bars 12 extending between fixed ends 10, 11, as shown in Figure 3. A plurality of annular, ring-shaped filter frames 13 are slidably held by the guide bars. Each filter frame 13 has four guide grooves at its corners for slidingly engaging with the guide bars, and has at its uppermost portion a tab 15 for engagement at the time of disassembling with a known disassembler 16 incorporating a chain.
An annular liquid-collecting groove 17 is formed in the side surface of each filter frame 13 suitably spaced from the inner periphery of the latter. The groove 17 is in communication with a depending groove 18 formed at the bottom of each filter frame 13. A plurality of tabs 20 are formed on the side surface of the filter frame 13 for retaining an adjacent annular filter cloth 19. The filter cloth 19 has four notches 22 formed in its outer periphery for engagement with the guide bars 12 and is similarly shaped, as viewed end-on, to the filter frame 13. Bores 21 are formed axially passing through the filter cloth 19 for receiving the tabs 20 on the filter frame 13 for retaining the body of the filter cloth.
A plurality of such filter frames and a plurality of such filter cloths are arranged in alternation with one another on the guide bars abutting each other, and are adapted to be pressingly moved toward the left-hand side fixed end plate 10 by a movable end portion 25 engaged by a connecting rod 24 adapted to be actuated by a hydraulic cylinder 23 provided at the right-hand side fixed end part 11.
A fluid-inlet port 26 is formed through the left-hand side fixed end plate 10, and is connected to a fluid pressurising pump 28 via a stop valve 27. The fluid may be a compressed air. A flexible inflatable member 29 which may be a bag made of a rubber or like material is fixed at its periphery to the fixed end plate 10 by means of a clamp ring 30. The fluid-inlet port 26 is in communication with the interior of the inflatable member 29 which is supported at its free end by a supporting rod 31 to extend inwardly of a compression chamber 33 defined by the filter frames 13.
The compression chamber 33 is in communicaiton with a liquid-feeding pump 36, via a stop valve 35 and a radial port 34 formed in the clamp ring 30. The liquidfeeding pump 36 is adapted to pressingly feed a liquid to be treated from a tank 37 into the compression chamber 33.
Beneath the compression part 7, lying under the dropping grooves 18 formed at the bottoms of the frames 13 is a laterally displaceable conduit 38 for collecting the separated liquid.
A conveyor belt 39 is disposed below the dropping groove 18 for collecting the filtrated cake in a manner known per se.
In operation, as the hydraulic cylinder 23 is operated, the filter frames are pressed together. Then, the liquid-feeding pump 36 is started to feed the liquid to be treated into the compression chamber causing an external pressure on the inflatable member 29 to deflate the latter. After the inflatable member 29 is deflated to a certain reduced size, the resulting reaction force causes a filtering pressure for a primary filtration. The stop valve 27 of the pressurising part 9 is closed at this moment.
The primary filtration pressure is accordingly transmitted to the hydraulic cylinder 23.
The stop valve 35 is closed after the liquid pressure is increased up to a predetermined level.
Subsequently, the stop valve 27 of the pressurising means 9 is opened and the air pump 28 is started so that compressed air may be introduced into the inflatable member 29. The inflation of the member 29 then causes compression of the liquid in the compression chamber 33 to perform a secondary filtration.
Partly because this secondary filtration is made from the inside of the mass of the liquid and partly because the flexible inflatable member 29 follows the reduction of the volume of the material under filtration, a highly efficient filtration is effected in a shorter period of time.
Subsequently, the stop valve 35 at the liquid inlet port 34 is opened. The pump 36 is then started to further introduce the liquid into the compression chamber 33. The valve 27 of the pressurising means is kept opened during the introduction of the additional or new liquid, to allow the deflation of the inflatable member 29 by discharging the air into atmosphere. Alternatively, suction may be used for hastening the deflation of the inflatable member.
After the deflation of the inflatable member 29, the liquid pressure again causes the primary filtration pressure across the filter cloth 19. The stop valve 35 is again closed to enable the pressurising means 9 to perform the secondary filtration in the manner described.
The primary and secondary filtrations are thus repeated until the compression chamber 33 becomes full of the filtrated cake so as not to allow the further inflation of the inflatable member 29. The filtration is then completed for the time of operation.
During the filtration, the filtered liquid passes radially from the compression chamber 33 to the grooves 17 and 18 to be collected by the conduit 38 for subsequent treatment.
After the filtration is completed, the conduit 38 is laterally moved away from the filter press by suitable means, so that the lowermost conveyor belt 39 may confront the filter press.
A subsequent energisation of the hydraulic cylinder 23 in a known manner causes a returning movement of the movable end 25 from the compression part 7 to the right-hand side fixed end 11. The disassembler 16 is then started to separate the filter frames 13.
Since the cakes in the compression chamber 33 are in the form of separate compact bodies, most of them naturally drop onto the conveyor belt 39 as the frames 13 are moved. Parts of cakes sticking to the filter frames 13 or to the inflatable member 29 can conveniently be removed by a hammering effected on the filter frame or evacuation of the inflatable member 29 to deflate the latter.
The conveyor belt 39 thus collects the filtrated cakes and conveys them for the subsequent treatment or disposal.
Although in the foregoing description air has been described as used for inflating the inflatable member 29, incompressible fluid such as oil may alternatively be used.
The use of an incompressible fluid decreases the loss of compression of the filtered material attributable to the compression of the pressurising medium itself.
It is remarkable that the filtration of highly viscous materials or sludges such as fowl/droppings or sea-bottom muds are efficiently performed on a large scale by the present filter press, thanks to the provision of a flexible and inflatable pressurising member in the compression chamber defined by annular filter frames. The inflation of the inflatable member conveniently provides a secondary filtration which affords, in combination with the primary filtration provided by the pressure of the treated liquid itself, an enhanced filtration efficiency. In addition, since the secondary filtration is made by the inflatable member from the inner side of the mass of the filtered material, the application of the pressure to the filtering cloth is rendered highly uniform thereby to avoid undesirable local compression.
Since the filtration mainly relies on the compression performed by the pressurising member, the load on the liquid feeding pump can be greatly decreased as compared with conventional filter presses which rely solely upon the pressure of the liquid to be treated. In addition, the inflation of the pressurising member conveniently compensates for the reduction of the volume of the material under compression to provide a large rate of compression which ensures a much enhanced filtration efficiency.
The repeated inflation and deflation of the pressurising member advantageously provides a highly efficient filtration on a large scale.
The flexible nature of the pressurising member provides a uniform separation of the liquid from the solid material, irrespective of omni-presence of the material, since it allows the pressurising member to flex and thus to follow the shape of the material.
Since the filtered cakes are compact, in the form of separate unitary bodies, they can naturally drop downwardly as the filter frames are separated from each other
Although a small amount of filtered material may stick to the filter frames, it can easily be dropped by hammering the filter frames. Parts of cakes sticking to the pressurising member can be removed simply by evacuating and deflating the inflatable pressurising member. Thus the collection of the filtered cakes is also facilitated.
WHAT I CLAIM IS: – 1. A filter press comprising: a plurality of annular filter frames; a plurality of annular filter elements of shapes substantially corresponding to that of said filter frames, disposed between respective adjacent pairs of the filter frames, the assembled filter frames and filter elements forming a tubular structure, the interior of which defines a compression chamber; closure means for closing the ends of the tubular structure; a substantially tubular flexible pressurising member disposed longitudinally within said tubular structure; liquid feeding means for feeding liquid to be filtered into said compression chamber externally of said pressurising member: and compression fluid supplying means for supplying compression fluid to the interior of said pressurising member.
2. A filter press according to Claim 1 wherein the filter elements are filter cloths.
3. A filter press in accordance with Claim 1 or 2, wherein each of said filter frames has a groove formed in an end surface thereof collecting filtrate passing through the adjacent filter elements and a dropping groove in communication with said groove and communicating with the exterior of the tubular structure.
4. A filter press according to Claim 1, 2 or 3 wherein said pressurising member has an open end fixed to said closure
**WARNING** end of DESC field may overlap start of CLMS **.

Claims (9)

**WARNING** start of CLMS field may overlap end of DESC **. of the inflatable member 29. The filtration is then completed for the time of operation. During the filtration, the filtered liquid passes radially from the compression chamber 33 to the grooves 17 and 18 to be collected by the conduit 38 for subsequent treatment. After the filtration is completed, the conduit 38 is laterally moved away from the filter press by suitable means, so that the lowermost conveyor belt 39 may confront the filter press. A subsequent energisation of the hydraulic cylinder 23 in a known manner causes a returning movement of the movable end 25 from the compression part 7 to the right-hand side fixed end 11. The disassembler 16 is then started to separate the filter frames 13. Since the cakes in the compression chamber 33 are in the form of separate compact bodies, most of them naturally drop onto the conveyor belt 39 as the frames 13 are moved. Parts of cakes sticking to the filter frames 13 or to the inflatable member 29 can conveniently be removed by a hammering effected on the filter frame or evacuation of the inflatable member 29 to deflate the latter. The conveyor belt 39 thus collects the filtrated cakes and conveys them for the subsequent treatment or disposal. Although in the foregoing description air has been described as used for inflating the inflatable member 29, incompressible fluid such as oil may alternatively be used. The use of an incompressible fluid decreases the loss of compression of the filtered material attributable to the compression of the pressurising medium itself. It is remarkable that the filtration of highly viscous materials or sludges such as fowl/droppings or sea-bottom muds are efficiently performed on a large scale by the present filter press, thanks to the provision of a flexible and inflatable pressurising member in the compression chamber defined by annular filter frames. The inflation of the inflatable member conveniently provides a secondary filtration which affords, in combination with the primary filtration provided by the pressure of the treated liquid itself, an enhanced filtration efficiency. In addition, since the secondary filtration is made by the inflatable member from the inner side of the mass of the filtered material, the application of the pressure to the filtering cloth is rendered highly uniform thereby to avoid undesirable local compression. Since the filtration mainly relies on the compression performed by the pressurising member, the load on the liquid feeding pump can be greatly decreased as compared with conventional filter presses which rely solely upon the pressure of the liquid to be treated. In addition, the inflation of the pressurising member conveniently compensates for the reduction of the volume of the material under compression to provide a large rate of compression which ensures a much enhanced filtration efficiency. The repeated inflation and deflation of the pressurising member advantageously provides a highly efficient filtration on a large scale. The flexible nature of the pressurising member provides a uniform separation of the liquid from the solid material, irrespective of omni-presence of the material, since it allows the pressurising member to flex and thus to follow the shape of the material. Since the filtered cakes are compact, in the form of separate unitary bodies, they can naturally drop downwardly as the filter frames are separated from each other Although a small amount of filtered material may stick to the filter frames, it can easily be dropped by hammering the filter frames. Parts of cakes sticking to the pressurising member can be removed simply by evacuating and deflating the inflatable pressurising member. Thus the collection of the filtered cakes is also facilitated. WHAT I CLAIM IS: –

1. A filter press comprising: a plurality of annular filter frames; a plurality of annular filter elements of shapes substantially corresponding to that of said filter frames, disposed between respective adjacent pairs of the filter frames, the assembled filter frames and filter elements forming a tubular structure, the interior of which defines a compression chamber; closure means for closing the ends of the tubular structure; a substantially tubular flexible pressurising member disposed longitudinally within said tubular structure; liquid feeding means for feeding liquid to be filtered into said compression chamber externally of said pressurising member: and compression fluid supplying means for supplying compression fluid to the interior of said pressurising member.

2. A filter press according to Claim 1 wherein the filter elements are filter cloths.

3. A filter press in accordance with Claim 1 or 2, wherein each of said filter frames has a groove formed in an end surface thereof collecting filtrate passing through the adjacent filter elements and a dropping groove in communication with said groove and communicating with the exterior of the tubular structure.

4. A filter press according to Claim 1, 2 or 3 wherein said pressurising member has an open end fixed to said closure
means at one end of the tubular structure, and a closed end, the filter press further including a support rod in the interior of said pressurising member, connected at one end to the closure means to which the open end of said pressurising member is fixed, the other end of said support rod supporting the closed end of the flexible member.

5. A filter press in accordance with any one of Claims 1 to 4 and including compression means for releasably pressing together said filter frames and said filter elements.

6. A filter press in accordance with any one of Claims 1 to 5 wherein said compression fluid supplying means includes an air pump for supplying compressed air to the interior of said pressurising member.

7. A filter press in accordance with any one of Claims 1 to 5 wherein said compression fluid supplying means includes a liquid feeding pump fluidically connected to the interior of said pressurising member.

8. A filter press according to any one of the preceding claims and including a chain-type disassembler engageable with said filter frames for separating them.

9. A filter press constructed and arranged to operate substantially as hereinbefore described with reference to and as illustrated in Figures 2 to 4 of the accompanying drawings.

GB25491/77A
1976-09-08
1977-06-17
Filter press

Expired

GB1576390A
(en)

Applications Claiming Priority (1)

Application Number
Priority Date
Filing Date
Title

JP10671976A

JPS5332474A
(en)

1976-09-08
1976-09-08
Multiplex type filter press

Publications (1)

Publication Number
Publication Date

GB1576390A
true

GB1576390A
(en)

1980-10-08

Family
ID=14440750
Family Applications (1)

Application Number
Title
Priority Date
Filing Date

GB25491/77A
Expired

GB1576390A
(en)

1976-09-08
1977-06-17
Filter press

Country Status (6)

Country
Link

US
(1)

US4080293A
(en)

JP
(1)

JPS5332474A
(en)

DE
(1)

DE2731043C3
(en)

FR
(1)

FR2364052A1
(en)

GB
(1)

GB1576390A
(en)

IT
(1)

IT1089872B
(en)

Cited By (1)

* Cited by examiner, † Cited by third party

Publication number
Priority date
Publication date
Assignee
Title

GB2129328A
(en)

1982-10-29
1984-05-16
Contra Shear Holdings
Method of dewatering a material and a press therefor

Families Citing this family (8)

* Cited by examiner, † Cited by third party

Publication number
Priority date
Publication date
Assignee
Title

JPS5496538A
(en)

1978-01-17
1979-07-31
Kuraray Co Ltd
Adhesive mass composition

DE3609564A1
(en)

1985-12-11
1987-06-19
Netzsch Maschinenfabrik
Filter press having membrane plates

DE3807275A1
(en)

1988-03-05
1989-09-14
Mueller Umwelttechnik
Apparatus for pressure dewatering of aqueous sludges

US5164081A
(en)

1989-03-24
1992-11-17
The Standard Oil Company
Apparatus for separation and for treatment of fluid feedstreams, wafers for use therein and related methods

US5174900A
(en)

1989-03-24
1992-12-29
The Standard Oil Company
Apparatus for separation and for treatment of fluid feedstreams, wafers for use therein and related methods

SE532481C2
(en)

2008-07-04
2010-02-02
Stigebrandt Ake

Improved dewatering device having a bellows

CN111097219B
(en)

2019-12-02
2021-07-20
南华大学
Ore pulp separating device of submarine mining equipment

CN113524457B
(en)

2021-07-07
2022-07-12
山东兖州建设总公司
Construction is with portable dust-protection type wall fluting equipment

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Publication number
Priority date
Publication date
Assignee
Title

US270807A
(en)

1883-01-16

High-pressure filter-press

US596995A
(en)

1898-01-11

Filter-press

DE1436296A1
(en)

1962-09-24
1968-11-28
English Clays Lovering Pochin

Filter press

AT256886B
(en)

1964-06-19
1967-09-11
Chemokomplex Vegyipari Gep Es

Automatic high-performance filter press

US3360130A
(en)

1964-09-09
1967-12-26
Noritake Iron Works
Filter press

US3737041A
(en)

1971-12-20
1973-06-05
Kurita Machinery Manuf
Filter press

1976

1976-09-08
JP
JP10671976A
patent/JPS5332474A/en
active
Granted

1977

1977-02-08
US
US05/766,792
patent/US4080293A/en
not_active
Expired – Lifetime

1977-06-17
GB
GB25491/77A
patent/GB1576390A/en
not_active
Expired

1977-06-17
FR
FR7718587A
patent/FR2364052A1/en
active
Pending

1977-07-08
DE
DE2731043A
patent/DE2731043C3/en
not_active
Expired

1977-09-06
IT
IT50900/77A
patent/IT1089872B/en
active

Cited By (1)

* Cited by examiner, † Cited by third party

Publication number
Priority date
Publication date
Assignee
Title

GB2129328A
(en)

1982-10-29
1984-05-16
Contra Shear Holdings
Method of dewatering a material and a press therefor

Also Published As

Publication number
Publication date

IT1089872B
(en)

1985-06-18

DE2731043C3
(en)

1981-01-15

FR2364052A1
(en)

1978-04-07

DE2731043A1
(en)

1978-03-16

US4080293A
(en)

1978-03-21

DE2731043B2
(en)

1980-03-20

JPS5332474A
(en)

1978-03-27

JPS5535964B2
(en)

1980-09-18

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