GB2275000A - Method and means for screening solids from a liquid - Google Patents

Method and means for screening solids from a liquid Download PDF

Info

Publication number
GB2275000A
GB2275000A GB9325252A GB9325252A GB2275000A GB 2275000 A GB2275000 A GB 2275000A GB 9325252 A GB9325252 A GB 9325252A GB 9325252 A GB9325252 A GB 9325252A GB 2275000 A GB2275000 A GB 2275000A
Authority
GB
United Kingdom
Prior art keywords
chamber
liquid
solids
filter
piston
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
GB9325252A
Other versions
GB9325252D0 (en
GB2275000B (en
Inventor
Leo L Castagno
Christopher L Hudson
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.)
Vanmark Corp
Original Assignee
Vanmark Corp
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 Vanmark Corp filed Critical Vanmark Corp
Publication of GB9325252D0 publication Critical patent/GB9325252D0/en
Publication of GB2275000A publication Critical patent/GB2275000A/en
Application granted granted Critical
Publication of GB2275000B publication Critical patent/GB2275000B/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D33/00Filters with filtering elements which move during the filtering operation
    • B01D33/01Filters with filtering elements which move during the filtering operation with translationally moving filtering elements, e.g. pistons
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D29/00Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor
    • B01D29/01Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor with flat filtering elements
    • B01D29/05Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor with flat filtering elements supported
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D29/00Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor
    • B01D29/11Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor with bag, cage, hose, tube, sleeve or like filtering elements
    • B01D29/13Supported filter elements
    • B01D29/23Supported filter elements arranged for outward flow filtration
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D29/00Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor
    • B01D29/44Edge filtering elements, i.e. using contiguous impervious surfaces
    • B01D29/445Bar screens
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D29/00Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor
    • B01D29/60Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor integrally combined with devices for controlling the filtration
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D29/00Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor
    • B01D29/62Regenerating the filter material in the filter
    • B01D29/64Regenerating the filter material in the filter by scrapers, brushes, nozzles, or the like, acting on the cake side of the filtering element
    • B01D29/6469Regenerating the filter material in the filter by scrapers, brushes, nozzles, or the like, acting on the cake side of the filtering element scrapers
    • B01D29/6484Regenerating the filter material in the filter by scrapers, brushes, nozzles, or the like, acting on the cake side of the filtering element scrapers with a translatory movement with respect to the filtering element
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D29/00Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor
    • B01D29/62Regenerating the filter material in the filter
    • B01D29/66Regenerating the filter material in the filter by flushing, e.g. counter-current air-bumps
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D29/00Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor
    • B01D29/62Regenerating the filter material in the filter
    • B01D29/70Regenerating the filter material in the filter by forces created by movement of the filter element
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D29/00Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor
    • B01D29/76Handling the filter cake in the filter for purposes other than for regenerating
    • B01D29/80Handling the filter cake in the filter for purposes other than for regenerating for drying
    • B01D29/82Handling the filter cake in the filter for purposes other than for regenerating for drying by compression
    • B01D29/824Handling the filter cake in the filter for purposes other than for regenerating for drying by compression using pistons
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2201/00Details relating to filtering apparatus
    • B01D2201/28Position of the filtering element
    • B01D2201/287Filtering elements with a vertical or inclined rotation or symmetry axis

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Filtration Of Liquid (AREA)

Description

1 1 2275000 1 METHOD AND MEANS FOR SCREENING SOLIDS FROM A LIQUID MEDIUM
The invention relates to devices for removing suspended solids from a liquid and to a method of so removing suspended solids.
2 industrial and commercial frying operations, such as the manufacture of potato chips, use large quantities of oil. During any frying operation, portions of the fried material may flake off, such as skin from potatoes. These flakes are carbon particles. Some of these particles stick to the food being cooked and cause a blemish thereon. Other particles remain.suspended in the oil and must be removed before the oil can be recycled for further use.
In typical commercial and industrial frying operations, the used oil containing the suspended solids is sent to a centrifuge separator, such as that manufactured by Lakos,, which concentrates the solids into a liquid sludge-type medium. Clean oil from the separator can be returned to the fryer for reuse. The sludge is sent to a filter vessel which has to be manually opened and cleaned, thereby exposing the operator to hot oil at a temperature of approximately 360 F. Thus. the manual replacement of the filter elemedt of the filter vessel presents risks of burn. as well as exposing the environment to the oily, dirty sludge. Also, the operator cannot tell when the filter element in the filter vessel is full. Therefore, cleaning of the filter element may occur too early or too late, rather than at the optimal time just as the filter element becomes full. Also, since the sludge is not compacted in the filter vessel, the volume of sludge requires the element to be changed more frequently than would be necessary with compacted sludge.
3 Furthermore, oil in the sludge is not recovered and therefore wasted.
Therefore, a primary objective of the present invention is the provision of a method and means for screening solids from a liquid medium so that cleaned liquid may be recycled for further use.
Another objective of the present invention is the provision of a device for removing suspended solids from oil and other sludge-type liquid mediums.
Another objective'of the present invention is the provision of a device wherein the waste solids are discharged from the device automatically and without manual handling.
Still a further objective of the present invention is the provision of a method.and means for filtering oil having suspended solids therein, so as to recover recyclable oil therefrom, and for compressing the removed solids before being discharged.
Another objective of the present invention is the provision of a safe and efficient method and means of removing suspended solids from a liquid.
These and other objectives will become apparent from the following description of the invention.
The device for removing suspended solids from a liquid comprises a chamber with a cylindrical wall and having an inlet 4 for introducing liquid into the chamber. The liquid contains suspended solids. The chamber also has an outlet for releasing liquid which has been cleansed so as to be substantially free from suspended solids. A discharge opening is provided for removing solids from the chamber. In one embodiment, a filter element is mounted ih a double acting piston which is mounted within the chamber for axial movement therein. The liquid is forced through the filter element in the piston so that solids are removed from the liquid. As the piston moves toward the bottom of the chamber, the solids are compressed. As the piston moves in the opposite direction toward the upper end of the chamber, liquid is back-flushed through the filter element to remove solids therefrom so as to clean the filter element. After a predetermined level of solids are accumulated within the is chamber, a discharge valve is opened so that the compressed solids can be removed through the discharge opening in the bottom of the chamber. A computer controls the introduction and release of liquid into the chamber, and controls movement of the piston for compression and discharge of the solids from the chamber.
In a second embodiment, the filter element is in the form of a cylinder extending substantially along the cylindrical wall of the chamber. The liquid is introduced into the interior of the chamber and is forced radially outwardly through the filter element into a drainage area adjacent the chamber wall. A piston mounted within the chamber is actuated to scrape solids from the cylindrical filter element and to compress the solids. As with the first embodiment, when the solids accumulate to a predetermined level in the chamber, a discharge valve is opened so that the solids can be automatically removed through a discharge opening for disposal.
In operation, liquid containing suspended solids is Introduced into the chamber and forced through the filter so as to remove the solids from the liquid. The cleaned liquid. which Is substantially free from suspended solids, is released from the chamber for recycling. The suspended solids removed by the filter element are compressed, and eventually discharged from the chamber without any manual handling thereof.
An embodiment of the invention will now be described, by way of example only, reference being made to the accompanying drawings, in which:
Figure 1 is a side elevation view of the device of the present invention.
Figure 2 is a side elevation sectional view of the device of the present invention.
Figure 3 is a view of the piston in the filter chamber of the device, as taken along lines 3-3 of Figure 2.
Figure 4 is a sectional view of the piston taken along lines 4-4 of Figure 3.
Figures 5-8 are partial side elevation sectional views showing the device during various stages of operation.
Figure 9 is a schematic view showing the interconnection of the device with a computer or microprocessor.
6 Figure 10 is a view similar to Figure 2 showing an alternative embodiment of the device.
Figure 11 is a sectional view taken along lines 11-11 of Figure 10.
Figure 12 is a partial sectional view taken along lines 12 12 of Figure 11.
The device of the present invention is generally designated In the drawings by the reference numeral 10. The device 10 Includes a central filter cylinder 12, an upper pneumatic cylinder 14,, and a lower discharge portion 16. more particularly. the filter cylinder 12 includes a cylindrical wall 18 defining a collection chamber 20 therein. The wall 18 is connected to an upper flange 22 and a lower flange 24. The upper flange 22 of the cylinder 12 is secured to a lower flange 26 of the pneumatic cylinder 14 with a plurality of nut and bolt assemblies 28, as best seen in Figure 1. Similarly, the lower flange 24 of the cylinder 12 is secured to an upper flange 30 of the discharge portion 16 using a plurality of nut and bolt assemblies 32. A lower flange 34 on the discharge portion 16 is heplurality of nut and bolt 20 bolted to a discharge chute 36 with assemblies 38.
The filter cylinder 12 includes a liquid inlet line 40 and a liquid outlet line 42. The inlet line 40 and the outlet line 42 each has a valve 50, 52, respectively which is movable between 7 open and closed positions. A conventional pneumatic actuator 54 is operatively connected to valve 50 to control the position thereof. Similarly, a conventional pneumatic actuator 56 is operatively connected to the valve 52 to move the valve between 5 the open and closed positions.
The pneumatic cylinder 14 includes an upper air line 58 and a lower air line 60 at the opposite ends of the cylinder, as best seen in Figure 2. Lines 58 and 60 are interconnected by line 59. An air supply line selectively provides air to the inlets 58, 600 jo as regulated by a solenoid 61. A double acting piston 62 is mounted within the pneumatic cylinder 14 for axial movement between- the ends of the cylinder. The piston 62 is mounted upon a shaft 64 which extends through the lower end of the pneumatic cylinder and into the filter cylinder 12.. as seen in Figure 2. A piston 66 is mounted on the lower end of the. shaft 64-within the filter chamber 20. A seal 68 is provided around the shaft 64 at the lower of the pneumatic cylinder 14, and a seal 70 is provided around the shaft 64 at the upper end of the filter cylinder 12, as seen in Figure 2, though other means of sealing may be employed. The shaft 64 is shown in.Figure 4 to be threadably attached to the piston 66. though other means for connecting the piston to the shaft may be employed.
As seen in Figure 4, the piston 66 includes a perimeter edge 72 with a sealing piston ring 74 mounted therein. The piston 66 includes a lower annular surface 76 and an interior recessed surfaced 78, with an axially extending wall 80 extending 8 therebetween. A filter element 82 engages the recessed surface 78 and is held in position by a retaining ring 84 received within a slot 86 extending around the wall 80. Preferably. filter element 82 is a Vee-Wire screen manufactured by Johnson Filtration Systems. A plurality of grooves 88 are machined into the recessed surface 78 to direct lquid passing through the -L c filter element 82 to passagewayes 90extending through the piston 66. The grooves 88 serve as collection troughs and can be formed in any desired pattern.
The pneumatic cylinder 14 includes an upper proximity switch 92, a lower proximity switch 94, and an intermediate proximity switch 96. The proximity-switches 92. 94 and 96 sense the position of piston 62 within the pneumatic cylinder 14, as described in further detail below.
The discharge portion 16 includes a valve 98 movable between open and closed positions. A conventional pneumatic actuator 100 controls the movement of the valve 98 between the open and closed positions. As seen in Figure 9, the solenoid 61 for the air supply line, the proximity switches 92. 94, and 96, and the pneumatic actuators 54. 56 and 100 are operatively connected to a computer or processing unit 102 which controls the operation of the device 10.
Normal operation of the device 10 is shown in Figure 5. In the normal operation mode, valves 50 and 52 are open so that fluid containing suspended solids enters the filter chamber 20 9 through the inlet line 40. Valve 98 is normally closed. The fluid pressure forces the liquid 104 upwardly through the filter element 82 and through the passages 90 in the piston 66, such that clean liquid, substantially free from suspended solids is expelled by the chamber 20 through the outlet line 42. Suspended solids 106 removed by the filter element are collected in the chamber below the piston 66.
At a preselected time.. the computer 102 actuates the pneumatic actuators 54, 56 to close the valves 50 and 52 in the inlet and outlet lines 40, 42. The computer 102 also actuates the solenoid 61 so as to introduce air into air inlet line 58. thereby forcing the pistons 62 and'66 downwardly in their respective cylinders. The piston 66 thereby compresses the solids in the bottom of the filter chamber 20. as seen in Figure 6. If, during the compression cycle, the piston 62 moves past the intermediate proximity switch 96, solenoid 61 will direct air into the lower air line 60 so as to raise the pistons 62. 66 upwardly to the initial position shown in Figure 5, until sensed by switch 92. The valves 50. 52 will then open such that additional liquid will be introduced into the filter chamber and normal operation will proceed.
The compression cycle will be repeated at preselected spaced intervals, as described above. When there is a sufficient accumulation of suspended solids in the chamber 20 such that the piston 62 does not pass the intermediate proximity switch 96 during the compression cycle, the computer 102 will actuate the pneumatic actuator 100 so as to open the valve 98 in the discharge portion 16. The pistons 62 and 66 will continue to descend in their respective cylinders so that the compressed solids 108 will be discharged from the chamber. 20 and into the discharge portion 16. When the piston 62 reaches the level of the lower proximity switch 94. the computer 102 will close the valve 98 in the discharge portion 16 of the device 10. Air will then be directed into air inlet llne 60 at the lower end of the pneumatic cylinder 14 so as to raise the pistons 62 and 66. AS seen in Figure 8, when the piston 66 is being raised, the liquid 104 Is forced downwardly through the passages 90 in the piston and through the filter element 82,, so as to back-flush and clean the filter element. Once the piston 62 reaches the upper proximity switch 92, the computer opens the valves 50 and 52 in the liquid inlet and outlet lines 40, 42,, respectively, such that the normal operation of the device can start over.
During the normal operation cycle shown in Figure 5, the valves 50, 52 in the inlet and outlet lines 40, 42, respectively, are open and liquid is forced upwardly through the filter element 82 by the pressure in the line 40. During the compression cycle shown in Figure 6, the purge cycle shown in Figure 7, and the filter cleaning cycle shown in Figure 8, the liquid control valves 50 and 52 in the liquid inlet and outlet lines 40. 421 respectively, remain closed such that no liquid is lost from the chamber 20. During the compression cycle, liquid is forced upwardly through the filter element 82 by the advancement of the 11 piston 66. During the purging cycle,When the valve 98 is open. the compressed solids 108 act as a plug to prevent liquid from passing through the discharge valve 98. When the valve 98 closes, it shears off a portion of the compacted solids below the valve, while a portion of the compressed solids remains above the valve to serve as the plug. During the filter cleaning cycle, the liquid 104 is forced downwardly through the filter element by the retraction of the piston 66 Thus,, the device 10 is automatically operated by the computer 102 through a normal filtering cycle, a periodic compression cycle, a purge cycle when sufficient solids are accumulated, and a cleaning cycle. There is no exposure of an operator r;m'Vthe environment to hot oil or liquid.
An alt-eTnative embodiment of the present invention is shown in Figures 10-12. In-the alternative embodiment. the filter cylinder 112 is modified from that shown in Figures 1 and 2. but -the pneumatic cylinder 14 and discharge portion 16 are unchanged. In the alternative embodiment, the filter element 114 is constructed of a Vee- Wire screen formed into a cylinder so as to mate with the wall of the filter cylinder 112. The bearing bars 116 on the element 114 engage the inner wall surface, as seen in Figure 12, so as to define a drainage area 118 between the filter element 114 and the cylinder wall. The liquid inlet line 120 extends through the wall of the filter cylinder 112 and through the filter element 114 so that liquid is introduced into the interior chamber 122 of the cylinder 112. As the liquid fills 12 the chamber, it is forced radially outwardly through the filter element 114 so as to remove suspended s.olids from the liquid. The cleaned liquid, which is substantially free from susp ended solids, is drained through an outlet conduit 124 which is in s communication with the drainage area 118 adjacent the bottom of the cylinder 112.
The device of the alternative embodiment shown in Figures 10-12 operates substantially similar to the device 10 described above,, except that there is no back-flushing of the filter element 114,, as described above with respect to Figure 8. During the compression cycle,- the piston 126, which is solid and has no filter element therein, scraps the inside of the filter element 114 to remove solids therefrom and to compact the solids in the bottom of the chamber 122. The compression cycle and purge cycle for the alternative device is similar to those cycles as described above.
It is understood that many modifications, substitutions and additions may be made, which are within the intended broad scope of the invention, to the embodiment described with reference to the drawings. it can be seen from that description that the present invention accomplishes at least all of the stated objectives.
13 claims 1. A device for removing suspended solids from a liquid, the device comprising a chamber having an inlet for introducing a liquid containing suspended solids, an outlet for releasing liquid substantially free from suspended solids, and a discharge opening for removing solids from the chamber; filter means within the chamber through which the liquid passes to remove suspended solids therefrom; and compression means for compressing the solids in the chamber.

Claims (1)

  1. 2. A device as claimed in Claim 1 wherein liquid is forced through the
    filter in one direction to remove is solids from the liquid and the liquid is back-flushed through the filter in the opposite direction to remove solids from the filter.
    3. A device as claimed in Claim 1 or Claim 2 and including processor means for controlling the introduction and release of the liquid, and for controlling the compression and discharge of the solids.
    4. A device as claimed in any one of Claims 1 to 3 wherein the compression means includes a double acting piston mounted within the chamber for axial movement therein.
    14 5. A device as claimed in Claim 4 wherein the filter means includes a filter element mounted on the piston, the piston including one or more ports therein through which the liquid flows.
    6. A device as claimed in Claim 4 or Claim 5 wherein the piston is movable between an first position and a second position, the liquid being forced through the filter as the piston moves between the first and second positions.
    7. A device as claimed in any one of Claims 4 to 6 wherein a plurality of proximity switches are operatively connected to the piston for sensing the position of the piston relative to the chamber.
    8. A device as claimed in any one of Claims 4 to 7 wherein pneumatic means are provided for moving the piston within the chamber. 20 9. A device as claimed in any preceding claim and including first and second valve means operatively connected to the inlet and outlet, respectively, for controlling flow of liquid into and out of the chamber. 25 10. A device as claimed in any preceding claim and including sensing means for sensing the level of solids within the chamber.
    11. A device as claimed in any preceding claim wherein the chamber has a cylindrical wall and the filter means includes a cylindrical filter element matingly fitted within the chamber to define with a wall of the chamber a liquid drainage area between the filter element and the chamber wall.
    12. A device as claimed in Claim 11 wherein the compression means includes a double acting piston mounted within the filter element and being movable between first and second positions.
    13. A device as claimed in Claim 12 wherein the piston is disposed and arranged to engage the filter element to scrape solids therefrom during movement from the first to the second position.
    14. A method for screening solids from a liquid, the method comprising introducing a liquid into a chamber, the liquid containing suspended solids therein; forcing the liquid through a filter in the chamber so as to remove solids from the liquid; and compressing the solids within the chamber.
    15. A method as claimed in Claim 14 and including the step of releasing liquid from the chamber, the released liquid being substantially free from suspended 16 solids.
    16. A method as claimed in Claim 14 or Claim 15 and including back-flushing the filter with the liquid to remove solids from the filter.
    17. A method as claimed in any one of Claims 14 to 16 and including sensing the level of solids in the chamber and discharging the solids from the chamber after the level reaches a predetermined valve.
    18. A method as claimed in any one of Claims 14 to 17 and including discharging the solids from the chamber.
    19. A method as claimed in Claim 18 and including controlling the flow of fluid into and out of the chamber and controlling the compression and discharge of solids from the chamber with a processor means.
    Amendments to the claims have been filed as follows 1. A device for removing suspended solids from a liquid, the device comprising a chamber having an inlet for introducing a liquid containing suspended solids, a liquid outlet for releasing liquid substantially free from suspended solids, and a discharge opening for removing solids from the chamber; movable filter means within the chamber through which the liquid passes to remove suspended solids therefrom; and means for moving the filter means between first and second positions within the chamber; and the filter means dividing the chamber into first and second compartments, each compartment having a volume which varies as the filter means moves between the first and second positions, the inlet being in communication with the first compartment at least during the introduction of liquids containing suspended solids into the first compartment, and the liquid outlet being in communication with the second compartment.
    2. A device as claimed in Claim 1 wherein liquid is forced through the filter in one direction to remove solids from the liquid and the liquid is back-flushed through the filter in the opposite direction to remove solids from the filter.
    3. A device as claimed in Claim 1 or Claim 2 and including processor means for controlling the introduction and release of the liquid, and for controlling the movement of the filter means and discharge of the solids.
    4. A device as claimed in any one of Claims 1 to 3 wherein the filter means is mounted on a double acting piston mounted within the chamber for axial movement therein.
    5. A device as claimed in Claim 4 wherein the filter means includes a f ilter element mounted on the piston, the piston including one or more ports therein through which the liquid flows.
    6. A device as claimed in claim 4 or claim 5 wherein the liquid is forced through the filter as the piston moves between the first and second positions.
    7. A device as claimed in any one of Claims 4 to 6 wherein a plurality of proximity switches are operatively connected to the piston for sensing the position of the piston relative to the chamber.
    8. A device as claimed in any one of Claims 4 to 7 wherein pneumatic means are provided for moving the piston within the chamber.
    9. A device as claimed in any preceding claim and including first and second valve means operatively controlling flow of liquid into and out of the chamber.
    10. A device as claimed in any preceding claim and including sensing means for sensing the level of solids within the chamber.
    11. A method for screening solids from a liquid, the method comprising introducing a liquid into a first compartment of a chamber, the liquid containing suspended solids therein; forcing the liquid through a movable filter located in the chamber and into a second compartment of the chamber so as to remove solids from the liquid, the solids remaining in the first compartment of the chamber; and moving the filter between first and second positions within is the chamber.
    12. A method as claimed in Claim 11 and including the step of releasing liquid from the chamber, the released liquid being substantially free from suspended solids.
    13. A method as claimed in Claim 11 or Claim 12 and including backflushing the filter with the liquid to remove solids from the filter.
    14. A method as claimed in any one of Claims 11 to 13 and including sensing the level of solids in the chamber and discharging the solids from the chamber after the level reaches a predetermined valve.
    1.7 0 15. A method as claimed in any one of Claims 11 to 14 and including discharging the solids from the chamber.
    16. A method as claimed in Claim 15 and including controlling the flow of fluid into and out of the chamber and controlling the movement of the filter and discharge of solids from the chamber with a processor means. 10 17. A method as claimed in any one of claims 11 to 16 wherein the solids form a plug to prevent liquid escaping through a discharge opening through which the solids are periodically discharged.
    1
GB9325252A 1993-02-16 1993-12-09 Solids from a liquid medium Expired - Fee Related GB2275000B (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US1775493A 1993-02-16 1993-02-16

Publications (3)

Publication Number Publication Date
GB9325252D0 GB9325252D0 (en) 1994-02-09
GB2275000A true GB2275000A (en) 1994-08-17
GB2275000B GB2275000B (en) 1996-11-20

Family

ID=21784358

Family Applications (1)

Application Number Title Priority Date Filing Date
GB9325252A Expired - Fee Related GB2275000B (en) 1993-02-16 1993-12-09 Solids from a liquid medium

Country Status (5)

Country Link
DE (1) DE4345018A1 (en)
GB (1) GB2275000B (en)
IE (1) IE930968A1 (en)
IT (1) IT1271860B (en)
NL (1) NL9302286A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2008144290A2 (en) * 2007-05-15 2008-11-27 Pitco Frialator, Inc. Continuously operating filtering apparatus

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE102007063240A1 (en) * 2007-12-31 2009-07-02 Mahle International Gmbh separation device
DE102020206657A1 (en) 2020-05-28 2021-12-02 BSH Hausgeräte GmbH System for filtering a liquid, water-bearing household appliance with the system and method for filtering a liquid
CN113209690B (en) * 2021-03-26 2023-07-07 南京悦之新新材料有限公司 Extraction treatment method of nanocrystalline cellulose filter cake

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB695605A (en) * 1950-08-05 1953-08-12 Johann Hoffmann Pressure filtering process and apparatus
GB1080501A (en) * 1964-05-05 1967-08-23 Suedwestfalen Ag Stahlwerke Piston-type filter press
GB1491108A (en) * 1975-06-19 1977-11-09 Vickerys Ltd Apparatus for separating liquids and solids
GB2119670A (en) * 1982-03-08 1983-11-23 Kuri Chem Eng Continuous filter
EP0232952A1 (en) * 1986-02-13 1987-08-19 Beheermaatschappij B. Bosman B.V. A filter apparatus having a tubular filter

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB695605A (en) * 1950-08-05 1953-08-12 Johann Hoffmann Pressure filtering process and apparatus
GB1080501A (en) * 1964-05-05 1967-08-23 Suedwestfalen Ag Stahlwerke Piston-type filter press
GB1491108A (en) * 1975-06-19 1977-11-09 Vickerys Ltd Apparatus for separating liquids and solids
GB2119670A (en) * 1982-03-08 1983-11-23 Kuri Chem Eng Continuous filter
EP0232952A1 (en) * 1986-02-13 1987-08-19 Beheermaatschappij B. Bosman B.V. A filter apparatus having a tubular filter

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2008144290A2 (en) * 2007-05-15 2008-11-27 Pitco Frialator, Inc. Continuously operating filtering apparatus
WO2008144290A3 (en) * 2007-05-15 2009-04-23 Pitco Frialator Inc Continuously operating filtering apparatus
US8828223B2 (en) 2007-05-15 2014-09-09 Pitco Frialator, Inc. Continuously operating filtering apparatus
US9532681B2 (en) 2007-05-15 2017-01-03 Pitco Frialator, Inc. Continuously operating filtering apparatus
US10433674B2 (en) 2007-05-15 2019-10-08 Pitco Frialator, Inc. Continuously operating filtering apparatus

Also Published As

Publication number Publication date
GB9325252D0 (en) 1994-02-09
ITRM940069A0 (en) 1994-02-15
IE930968A1 (en) 1994-08-24
IT1271860B (en) 1997-06-09
NL9302286A (en) 1994-09-16
ITRM940069A1 (en) 1995-08-15
DE4345018A1 (en) 1994-08-18
GB2275000B (en) 1996-11-20

Similar Documents

Publication Publication Date Title
US5364539A (en) Method and means for screening solids from a liquid medium
CA1096782A (en) Cyclone separator with plunger-rod cleaners
EP0038643A2 (en) Filter with backwashing device
CA2034006A1 (en) Method and apparatus for clarifying liquids
JPH03151068A (en) Device for separation of water containing waste
US5028326A (en) Apparatus for separating organic material from sludge
JP2010279860A (en) Method and apparatus for deliquoring and solidifying liquid-containing sludge
US3796316A (en) Water filtering apparatus
US5407574A (en) Filter media for filter systems
US5575913A (en) Filtration apparatus and method for removing particulate contaminants from commercial laundry waste water
GB2275000A (en) Method and means for screening solids from a liquid
US4795570A (en) Two-stage batch filter apparatus and filtration process
US4525275A (en) Concentric filter elements
CA3140157C (en) Grease recovery unit
US20010002006A1 (en) Bag filter with wash down system
US4622144A (en) Pressure filter apparatus
US3289839A (en) Filtering equipment for fluids
CN116943305A (en) Filter-pressing self-cleaning filtering method, device and storage medium
US5228987A (en) Method and apparatus for clarifying liquids
DK172223B1 (en) Device for filtering liquids
EP0091822B1 (en) Filter method and apparatus
JP2019118911A (en) Bag-like filter member
WO2000059601A1 (en) Fluid optimization and waste management system
EP0817667A1 (en) Dewatering device
EP0883576B1 (en) Particle dewatering device

Legal Events

Date Code Title Description
PCNP Patent ceased through non-payment of renewal fee

Effective date: 19971209