WO2000061260A1 - Apparatus for cleaning of liquids comprising a granulated filter material - Google Patents
Apparatus for cleaning of liquids comprising a granulated filter material Download PDFInfo
- Publication number
- WO2000061260A1 WO2000061260A1 PCT/NO2000/000120 NO0000120W WO0061260A1 WO 2000061260 A1 WO2000061260 A1 WO 2000061260A1 NO 0000120 W NO0000120 W NO 0000120W WO 0061260 A1 WO0061260 A1 WO 0061260A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- filter
- grains
- filter bed
- density
- grain
- Prior art date
Links
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D39/00—Filtering material for liquid or gaseous fluids
- B01D39/02—Loose filtering material, e.g. loose fibres
Definitions
- filter beds When removing particles from liquids by means of deep bed filters, it is known that filter beds operates at its optimum when the efficiency of filtration, or the filter coefficient for the filter, increases in the direction of flow of the liquid, and this can be achieved by letting the filter grain size decrease in the direction of flow of the liquid through the filter bed.
- Up- stream filtration has certain disadvantages relating to its operation, and will not be described further.
- Downstream filterbeds are based on a combination of two- or several different filter materials with different grain size and density, such as anthrasite, silica sand and garnet sand. Normally, are one or several relatively thin support layers of coarse material situated underneath the main filter bed. The support layers are not a part of the filter bed and have no function except from keeping the filter bed in place, and to contribute to an even distribution of the backwash water, etc. and will not be further dealt with.
- This material may be haydite or light clinker of expanded clay or plastic material with properties such as density and a grain size of the filter material can be adapted during production so that the density of the filter grains is reduced with increasing grain size.
- a filter bed can be designed with one single raw material with substantially continuous or stepwise (stratified) gradation or size from large to smaller grains in the direction of flow of the liquid.
- the invention is intended to encompass filter beds with the above material alone or in combination with other filter media such as sand or anthrasite.
- the backwash (cleaning) of the filter bed can be performed with lower flushing velocities and less backwash water than what is normally used, and this is achieved by letting the filter bed comprise easily fluidised material with low density and low a sinking rate.
- Fig. 1 shows the sinking rate of grains of various filter media, with an example of a composition of multimedia (Mehr Anlagen/multilayer) filters, where the sinking rate of the filter grains is given as a function of grain size and density.
- Fig. 2 shows a typical deep bed filter with a granulated material according to the invention.
- Table 1 shows an example of results after direct filtration of drinking water containing humus in two partial filters with filter beds comprising the granulated grain material of expanded clay (LK) according to the invention in two fractions of grain sizes and densitites, and a traditional two-media filter bed with anthrasite over sand (A/S) respectively.
- the table shows that the LK filter gives results that fulfil the quality standards according to the Norwegian drinking water regulations with a good margin, and furthermore that results from the LK filter can be compared with a parallelly run traditional anthrasite sand filter in otherwise similar conditions.
- the filter beds have the same total depth whereas the grain sizes are as follows:
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Filtering Materials (AREA)
- Filtration Of Liquid (AREA)
Priority Applications (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
EP00917501A EP1194209A1 (en) | 1999-04-13 | 2000-04-13 | Apparatus for cleaning of liquids comprising a granulated filter material |
CA002367516A CA2367516A1 (en) | 1999-04-13 | 2000-04-13 | Apparatus for cleaning of liquids comprising a granulated filter material |
AU38461/00A AU3846100A (en) | 1999-04-13 | 2000-04-13 | Apparatus for cleaning of liquids comprising a granulated filter material |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
NO19991750 | 1999-04-13 | ||
NO19991750A NO314291B1 (no) | 1999-04-13 | 1999-04-13 | Kombinasjon av fraksjoner av lettklinkerkorn av ekspandert leire for tilberedning av en filterseng |
Publications (1)
Publication Number | Publication Date |
---|---|
WO2000061260A1 true WO2000061260A1 (en) | 2000-10-19 |
Family
ID=19903197
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/NO2000/000120 WO2000061260A1 (en) | 1999-04-13 | 2000-04-13 | Apparatus for cleaning of liquids comprising a granulated filter material |
Country Status (5)
Country | Link |
---|---|
EP (1) | EP1194209A1 (no) |
AU (1) | AU3846100A (no) |
CA (1) | CA2367516A1 (no) |
NO (1) | NO314291B1 (no) |
WO (1) | WO2000061260A1 (no) |
Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4225443A (en) * | 1978-03-22 | 1980-09-30 | The Taulman Company | Sintered-glass-granule filter medium |
WO1981002844A1 (en) * | 1980-04-04 | 1981-10-15 | G Hirs | Filter medium and method of making same |
US5292436A (en) * | 1992-05-13 | 1994-03-08 | Kansas State University Research Foundation | Tapered bed filtration apparatus |
WO1997046493A1 (en) * | 1996-06-07 | 1997-12-11 | Rc Enwa A/S | A method and a device for the purification of fluids |
WO1998015349A1 (en) * | 1996-10-07 | 1998-04-16 | A.S Norsk Leca | Light expanded clay aggregates for phosphorus removal |
-
1999
- 1999-04-13 NO NO19991750A patent/NO314291B1/no not_active IP Right Cessation
-
2000
- 2000-04-13 AU AU38461/00A patent/AU3846100A/en not_active Abandoned
- 2000-04-13 WO PCT/NO2000/000120 patent/WO2000061260A1/en not_active Application Discontinuation
- 2000-04-13 CA CA002367516A patent/CA2367516A1/en not_active Abandoned
- 2000-04-13 EP EP00917501A patent/EP1194209A1/en not_active Withdrawn
Patent Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4225443A (en) * | 1978-03-22 | 1980-09-30 | The Taulman Company | Sintered-glass-granule filter medium |
WO1981002844A1 (en) * | 1980-04-04 | 1981-10-15 | G Hirs | Filter medium and method of making same |
US5292436A (en) * | 1992-05-13 | 1994-03-08 | Kansas State University Research Foundation | Tapered bed filtration apparatus |
WO1997046493A1 (en) * | 1996-06-07 | 1997-12-11 | Rc Enwa A/S | A method and a device for the purification of fluids |
WO1998015349A1 (en) * | 1996-10-07 | 1998-04-16 | A.S Norsk Leca | Light expanded clay aggregates for phosphorus removal |
Also Published As
Publication number | Publication date |
---|---|
CA2367516A1 (en) | 2000-10-19 |
NO991750D0 (no) | 1999-04-13 |
NO991750L (no) | 2000-10-16 |
EP1194209A1 (en) | 2002-04-10 |
NO314291B1 (no) | 2003-03-03 |
AU3846100A (en) | 2000-11-14 |
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