WO2010139961A1 - Filter medium with a multiplicity of different filter layers and use for testing filter media - Google Patents
Filter medium with a multiplicity of different filter layers and use for testing filter media Download PDFInfo
- Publication number
- WO2010139961A1 WO2010139961A1 PCT/GB2010/001102 GB2010001102W WO2010139961A1 WO 2010139961 A1 WO2010139961 A1 WO 2010139961A1 GB 2010001102 W GB2010001102 W GB 2010001102W WO 2010139961 A1 WO2010139961 A1 WO 2010139961A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- filter
- fluid
- stages
- fluid path
- filter stages
- Prior art date
Links
- 238000012360 testing method Methods 0.000 title description 5
- 239000012530 fluid Substances 0.000 claims abstract description 99
- 238000001914 filtration Methods 0.000 claims description 21
- 238000005192 partition Methods 0.000 claims description 15
- 238000000034 method Methods 0.000 claims description 10
- 239000011148 porous material Substances 0.000 claims description 5
- 239000000463 material Substances 0.000 description 25
- 239000002245 particle Substances 0.000 description 7
- 239000000706 filtrate Substances 0.000 description 4
- 238000013461 design Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 238000005259 measurement Methods 0.000 description 2
- 239000013618 particulate matter Substances 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- 230000032683 aging Effects 0.000 description 1
- 238000005520 cutting process Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 239000004744 fabric Substances 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 230000003472 neutralizing effect Effects 0.000 description 1
- 229920003023 plastic Polymers 0.000 description 1
- 239000004033 plastic Substances 0.000 description 1
- 238000007493 shaping process Methods 0.000 description 1
- 238000004513 sizing Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D29/00—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D29/00—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor
- B01D29/01—Filters 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
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D29/00—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor
- B01D29/01—Filters 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
- B01D29/05—Filters 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
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D29/00—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor
- B01D29/01—Filters 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
- B01D29/05—Filters 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
- B01D29/055—Filters 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 ring shaped
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D29/00—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor
- B01D29/50—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor with multiple filtering elements, characterised by their mutual disposition
- B01D29/56—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor with multiple filtering elements, characterised by their mutual disposition in series connection
- B01D29/58—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor with multiple filtering elements, characterised by their mutual disposition in series connection arranged concentrically or coaxially
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D46/00—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D46/00—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
- B01D46/10—Particle separators, e.g. dust precipitators, using filter plates, sheets or pads having plane surfaces
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D46/00—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
- B01D46/10—Particle separators, e.g. dust precipitators, using filter plates, sheets or pads having plane surfaces
- B01D46/106—Ring-shaped filtering elements
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D46/00—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
- B01D46/56—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours with multiple filtering elements, characterised by their mutual disposition
- B01D46/62—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours with multiple filtering elements, characterised by their mutual disposition connected in series
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D46/00—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
- B01D46/56—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours with multiple filtering elements, characterised by their mutual disposition
- B01D46/62—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours with multiple filtering elements, characterised by their mutual disposition connected in series
- B01D46/64—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours with multiple filtering elements, characterised by their mutual disposition connected in series arranged concentrically or coaxially
Definitions
- the present invention relates to methods and apparatus for fluid filtration.
- the invention provides a fluid filter element comprising:
- the fluid path may pass through at least one relatively coarse filter stage and at least one relatively fine filter stage.
- the filter characteristics of the filter stages may be increasingly fine along the fluid path.
- the filter stages may be arranged in groups with substantially the same filter characteristics, and wherein neighbouring groups along the fluid path have different filter characteristics.
- At least some of the filter stages may have different pore sizes. At least some of the filter stages may remove different filtrands.
- At least one of the filter stages may be provided by a generally planar filter structure, the fluid path crossing the plane through the structure.
- a plurality of successive filter stages may be generally planar.
- a plurality of filter stages may be generally planar filter structures arranged at generally parallel planes, the fluid path crossing each of the planes through the corresponding structure.
- partition member located between adjacent ones of the filter structures, the partition member having impervious regions and being dimensionally stable, and further having pervious regions through which fluid can flow, in use, from one filter structure to the adjacent filter structure.
- the partition member may be planar and may be perforated.
- the generally planar structure may be a disc. At least one of the generally planar filter structures may have an aperture, the fluid path crossing the plane through the aperture, without filtration, and also crossing the plane through the filter structure for filtration.
- the at least one of the generally planar structures is a disc, and the aperture may be concentric with the disc. The fluid may cross the plane of the filter structure in opposite directions through the aperture and through the filter structure.
- a plurality of filter structures having apertures as aforesaid may be arranged with aligned apertures to provide a fluid path leg through the apertures, without filtration, and a fluid path leg sequentially through the structures.
- the invention provides a fluid filter comprising:
- a housing having an inlet and outlet
- the fluid path of the fluid filter element forming at least part of the fluid path from the inlet to the outlet.
- the invention provides a method of providing fluid filtration for a target fluid, comprising:
- analysing the filtrand captured including identifying the filter stage or stages in which capture has occurred;
- the filter characteristics may be modified by replacing one or more filter stages with alternative filter stages having different filter characteristics.
- Fig. 1 is a schematic perspective view of a filter element
- Fig. 2 is a schematic perspective view of a filter stage of the element of Fig. 1 ;
- Fig. 3 is a schematic perspective view of a filter including the element of Fig. 1 ;
- Fig. 4 is a perspective view of a partition member for use in an alternative example of a filter stage
- Fig. 5 is a perspective view of a filter element including partition members as shown in Fig. 4.
- Fig. 6 is a simplified flow diagram of a process for designing a filter element. Overview
- Fig. 1 illustrates one example of a fluid filter element 10.
- the element comprises a plurality of filter stages 12.
- the stages 12 are illustrated as layers of the element 10, which is constructed in a manner to be described below.
- a fluid path is indicated by an arrow 14.
- the path 14 passes sequentially through the layers of the element 10 and thus, passes sequentially through the filter stages of the element 10.
- At least some of the filter stages 12 have different filter characteristics, as will be described. This results in a staged filtration process in which the filtration being effected on the fluid passing through the filter element 10 1 changes at different positions along the path 14.
- the material to be filtered will be called “fluid” and may be liquid or gas.
- the material which is removed from the fluid will be called the “filtrand”.
- the clean fluid, after removal of the filtrand, will be called the "filtrate”.
- Fig. 2 illustrates one of the filter stages 12.
- the filter stage 12 is in the form of a generally planar disc-like filter structure, having a generally circular periphery 16 and a central aperture 18.
- the periphery 16 and the aperture 18 are substantially concentric.
- the fluid path 14 is shown crossing the plane in one direction through the structure, and in the opposite direction through the aperture 18. Other geometries could be used.
- the periphery 16 could have another shape.
- the aperture 18 could have another shape.
- the aperture 18 could be omitted.
- the structure 12 may be one or more layers of filter material such as a woven or non-woven filter cloth.
- the filter material will have a filter characteristic which represents the ability of the material to remove filtrand from fluid. Filter characteristics may be described in various different ways. In one possibility, the filter characteristic is expressed as a micron rating representing the maximum particle size which can pass through the material. For example, a filter material with a 3 micron rating will pass particles smaller than 3 microns, but will block particles with a size of 3 microns or greater.
- a micron rating may also be called a "pore size", referring to the size of pore in a perforated structure which allows the same particle size to be passed.
- the pore size or micron rating may represent a measurement from an equivalent structure providing the same filter characteristic, rather than an actual measurement of a perforation, because many techniques of filtering particles are available in addition to simple perforated sheets, meshes or the like.
- Filter materials with many different micron ratings are available. For example, materials with micron ratings as high as 100 microns are available for filtering fluids.
- Filter characteristics which refer to particle sizes represent filter materials which remove the same filtrand (particulates) but more coarsely or more finely. Other examples of filter characteristics exist. For example, different filter materials may have different characteristics representing the different filtrands which they are capable of removing from a fluid. Thus, one type of filter material may be able to remove particulates, while another type of filter material may be able to remove water from an oil. In this document, references to "different filter characteristics" are intended to encompass any change in characteristic which results in a change in the filtrand or filtrate produced.
- the element 10 is formed from a stack of planar filter stages 12 arranged at generally parallel planes to form a cylindrical structure, as shown.
- the apertures 18 of the stages 12 are arranged to be aligned and are therefore centred on the cylindrical access of the structure. This results in a fluid path leg 15 available through all of the apertures 18, without filtration, and a fluid path leg 14 which returns back along the cylinder and sequentially through the filter material of each of the stages 12, in turn.
- Impervious outer surfaces may be provided around the peripheries 16 and around the apertures 18 to prevent fluid leaking from the path leg 15 into the stages 12, or leaving the stages 12 before passing along the whole of the path leg 14.
- Fluid passing along the path leg 14 will undergo a filter process which depends on the filter characteristics of the various filter stages 12. At least some of the filter stages have different filter characteristics. For example, the fluid may first encounter at least one relatively coarse (relatively high micron rating) filter stage 12. This would remove relatively large particulate matter from the fluid. The fluid may subsequently encounter at least one relatively fine (relatively low micron rating) filter stage. This would remove relatively small particulate matter from the fluid. In a practical example, the use of a large number of stages 12 allows the micron rating of the filter stages 12 to reduce progressively along the leg 14.
- the micron rating of the stages 12 may reduce in the sequence: 100 microns; 50 microns; 25 microns; 10 microns; 5 microns and finally 3 microns.
- filter characteristics which are increasingly fine along the fluid path will result in particles of various different sizes being captured in various different stages 12, at various different positions along the length of the path leg
- the various stages 12 may be chosen to have different filter characteristics in relation to the filtrands they are capable of removing, so that various different filtrands are captured in various different stages 12, at various different positions along the length of the path leg 14.
- the filter characteristics of the filter stages 12 may change between each filter stage 12 and the next filter stage 12 along the fluid path.
- the filter stages 12 may be arranged in groups with substantially the same filter characteristics, and with neighbouring groups along the fluid path having different filter characteristics.
- Typical filter materials for a wide range of common filter tasks may have a thickness in the region of 1 mm or 2 mm, allowing an element to be constructed with as many as 60 stages within a relatively small volume. This allows the filtration process to take place in a graduated set of 60 steps, or in a smaller number of steps provided by groups of filter stages.
- the filter element 10 is shown in Fig. 3 incorporated in a filter 20.
- the filter 20 comprises a housing 22 having an inlet 24 and outlet 26.
- a lid 27 (shown almost completely cut away in Fig. 3) closes the housing 22 so that the housing 22 is substantially fully enclosed except at the inlet 24 and outlet 26.
- Fluid path means in the form of a central pipe 28 define a fluid path from the inlet 24 to the outlet 26, in the following manner.
- the housing 22 is cylindrical and the pipe 28 is concentric with the housing.
- the filter element 10 is installed in the housing 22 by placing it around the pipe 28, that is, by placing the apertures 18 over the pipe 28. Fluid which enters the inlet 24 passes along the length of the pipe 28, to the other end of the filter element 10. The fluid can then return to the first end of the filter element 10 by passing through the filter stages 12 and then leaving the housing 22 through the outlet 26.
- the geometries of the housing, filter stages and other components can be varied widely in order to change the geometry of the fluid path, and the outside geometry of the filter, including its size, and the number and locations of its inlet(s) and outlet(s), location of access for maintenance etc.
- filter stages 12 results in a staged filtration effect as fluid moves through the filter element 10, in which different filtrands are removed at different stages of the process and therefore at different positions within the filter element 10.
- This is expected to have a number of possible advantages. For example, when particulate filtrands of various different sizes are being removed, the use of increasingly fine filtering results in the first filter stages removing only the relatively large particulate filtrands, while relatively small particulate filtrands pass through to be removed by a later stage. This is expected to reduce problems of filter stages clogging. For example, the first filter stages are unlikely to clog with fine filtrands, which pass through, and the large filtrands will not be present to clog later stages which have finer ratings.
- Figs 4 and 5 illustrate an alternative example in which partition members 44 (Fig. 4) are included in the filter element 10a.
- Each partition member 44 is a planar disc made of an impervious material which is dimensionally stable, such as a synthetic plastics material. Regions 46 of the disc 44 are rendered pervious by the provision, in this example, of apertures in the material of the disc 44. The apertures 46 leave a continuous ring 48 around the outer circumference of the disc 44. A central aperture 50 is surrounded by a continuous inner ring 52. In this example, the rings 48, 52 are connected by spokes 54.
- the discs 44 are included in the stack of filter stages 12.
- the outer diameter of the discs 44 is approximately the same as the initial diameter of the filter stages 12.
- the diameter of the central aperture 50 is approximately the same as the initial diameter of the central aperture 18 in the filter stages 12. Accordingly, the discs 44 can be included in the stack of filter stages 12 by placing each disc 44 between two adjacent filter stages 12.
- an inner cylinder 56 and an outer cylinder 58 resist fluid leaving the filter element 10a unless it has passed through the filter stages 12 by flowing through the filter stages 12 in a direction generally parallel with the cylindrical axis of the filter element 10a.
- the filter stages 12 are not sealed to the cylinders 56, 58. This reduces the risk of damage to the filter stages 12 if they shrink during use, which some filter media may do. Shrinkage of the filter stages 12 would open gaps between the filter stages 12 and one or both of the cylinders 56, 58, potentially leaving open a path through which fluid can bypass the filter stages 12.
- Gaps between the filter stages 12 and the cylinders 56, 58 could also arise for other reasons, such as production tolerances, inaccurate cutting, sizing or shaping of the material, or the like.
- the partition members 44 are dimensionally stable and have dimensions chosen to be a close fit to the cylinders 56, 58. Consequently, even if the filter stages 12 leave gaps, the gaps between the partition members 44 and the cylinders 56, 58 will remain small. The path of least resistance for fluid flowing through the filter element 10, across a partition member 44, will remain the paths through the apertures 46. Thus, each time the fluid encounters a partition member 44, it will be encouraged back to the main body of the filter stages 12, away from their edges, by virtue of the position of the apertures 46.
- a filter element 10 of the type described above is provided as a test element.
- Target fluid is passed through the test filter element 10 at step 34. This results in the target fluid being filtered by the filter stages 12, removing filtrand as has been described.
- the fluid is then stopped at step 36.
- the test filter element 10 is removed (step 38) and the captured filtrand is analysed (step 40). In particular, the filter stage or stages in which capture has occurred is identified for each filtrand (each size or range of sizes of particulate filtrand, or each filtrand material, for example).
- the filter characteristics of the various filter stages 12 can then be modified in accordance with the outcome of the analysis.
- they can be modified (step 42) to cause filtrand to be captured more evenly across all of the filter stages.
- the analysis step 40 reveals that filtrand has been captured primarily in the early filter stages
- the early filter stages can be modified (e.g. by replacement by a different filter material) to be more coarse so that more filtrand will be captured in later filter stages.
- the modified arrangement can then be tested further by reverting to step 32. This provides an ability to tune the filter element 10 to the particular task required.
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Lubrication Details And Ventilation Of Internal Combustion Engines (AREA)
- Filtration Of Liquid (AREA)
Abstract
Description
Claims
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB1121338.6A GB2483199A (en) | 2009-06-05 | 2010-06-03 | Filter medium with a multiplicity of different filter layers and use for testing filter media |
Applications Claiming Priority (4)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB0909732.0 | 2009-06-05 | ||
GBGB0909732.0A GB0909732D0 (en) | 2009-06-05 | 2009-06-05 | Improvements in or relating to methods and apparatus for fluid filtration |
GBGB0920683.0A GB0920683D0 (en) | 2009-06-05 | 2009-11-26 | Improvements in or relating to methods and apparatus for fluid filtration |
GB0920683.0 | 2009-11-26 |
Publications (2)
Publication Number | Publication Date |
---|---|
WO2010139961A1 true WO2010139961A1 (en) | 2010-12-09 |
WO2010139961A8 WO2010139961A8 (en) | 2012-02-23 |
Family
ID=40936991
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/GB2010/001102 WO2010139961A1 (en) | 2009-06-05 | 2010-06-03 | Filter medium with a multiplicity of different filter layers and use for testing filter media |
Country Status (2)
Country | Link |
---|---|
GB (3) | GB0909732D0 (en) |
WO (1) | WO2010139961A1 (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2011064525A1 (en) * | 2009-11-26 | 2011-06-03 | Hydrotechnik Uk Limited | Filter medium with a multiplicity of different filter layers and use for testing filter media |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN104406035A (en) * | 2014-12-05 | 2015-03-11 | 山东蓬翔汽车有限公司 | External lubricating oil filter |
Citations (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2288426A (en) * | 1939-10-30 | 1942-06-30 | Nat Automotive Fibres Inc | Filter material |
US3003643A (en) * | 1957-10-28 | 1961-10-10 | Johnson & Johnson | Filter media |
US4025438A (en) * | 1974-10-21 | 1977-05-24 | Gelman Instrument Company | Water filter device |
US4115277A (en) * | 1977-06-17 | 1978-09-19 | Pioneer Filters, Inc. | Blood filtering apparatus of graduated fiber density |
DE3516341A1 (en) * | 1985-05-07 | 1986-11-13 | Johann Dr. Hinterberger | Layer filter apparatus for clarification and disinfection of liquids (for example contaminated water) and alternatively for testing filter combinations (for example made of depth filters and screen filters) for defined applications |
US5468847A (en) * | 1994-03-10 | 1995-11-21 | Minnesota Mining And Manufacturing Company | Method of isolating and purifying a biomacromolecule |
US5472600A (en) * | 1995-02-01 | 1995-12-05 | Minnesota Mining And Manufacturing Company | Gradient density filter |
US5595653A (en) * | 1994-07-15 | 1997-01-21 | Cera, Inc. | Microcolumn for extraction of analytes from liquids |
GB2418872A (en) * | 2004-10-06 | 2006-04-12 | Ford Global Tech Llc | A filter assembly operable with one or two filter elements |
-
2009
- 2009-06-05 GB GBGB0909732.0A patent/GB0909732D0/en not_active Ceased
- 2009-11-26 GB GBGB0920683.0A patent/GB0920683D0/en not_active Ceased
-
2010
- 2010-06-03 WO PCT/GB2010/001102 patent/WO2010139961A1/en active Application Filing
- 2010-06-03 GB GB1121338.6A patent/GB2483199A/en not_active Withdrawn
Patent Citations (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2288426A (en) * | 1939-10-30 | 1942-06-30 | Nat Automotive Fibres Inc | Filter material |
US3003643A (en) * | 1957-10-28 | 1961-10-10 | Johnson & Johnson | Filter media |
US4025438A (en) * | 1974-10-21 | 1977-05-24 | Gelman Instrument Company | Water filter device |
US4115277A (en) * | 1977-06-17 | 1978-09-19 | Pioneer Filters, Inc. | Blood filtering apparatus of graduated fiber density |
DE3516341A1 (en) * | 1985-05-07 | 1986-11-13 | Johann Dr. Hinterberger | Layer filter apparatus for clarification and disinfection of liquids (for example contaminated water) and alternatively for testing filter combinations (for example made of depth filters and screen filters) for defined applications |
US5468847A (en) * | 1994-03-10 | 1995-11-21 | Minnesota Mining And Manufacturing Company | Method of isolating and purifying a biomacromolecule |
US5595653A (en) * | 1994-07-15 | 1997-01-21 | Cera, Inc. | Microcolumn for extraction of analytes from liquids |
US5472600A (en) * | 1995-02-01 | 1995-12-05 | Minnesota Mining And Manufacturing Company | Gradient density filter |
GB2418872A (en) * | 2004-10-06 | 2006-04-12 | Ford Global Tech Llc | A filter assembly operable with one or two filter elements |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2011064525A1 (en) * | 2009-11-26 | 2011-06-03 | Hydrotechnik Uk Limited | Filter medium with a multiplicity of different filter layers and use for testing filter media |
Also Published As
Publication number | Publication date |
---|---|
GB201121338D0 (en) | 2012-01-25 |
WO2010139961A8 (en) | 2012-02-23 |
GB2483199A (en) | 2012-02-29 |
GB0920683D0 (en) | 2010-01-13 |
GB0909732D0 (en) | 2009-07-22 |
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