Method for operating a filter press and a filter press
US-2020330903-A1 · Oct 22, 2020 · US
US10737200B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10737200-B2 |
| Application number | US-202016793000-A |
| Country | US |
| Kind code | B2 |
| Filing date | Feb 18, 2020 |
| Priority date | Aug 23, 2017 |
| Publication date | Aug 11, 2020 |
| Grant date | Aug 11, 2020 |
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A method of operating a filter press, wherein filter material is fed into a filter chamber so as to form a filter cake between at least two sides of a flexible said filter medium. Filtrate is received from the filter chamber and the filter cake formed the filter chamber is discharged. Prior to discharging the filter cake, compression is applied on the filter cake formed within the filter chamber by providing compression fluid gas at a compression pressure exceeding a prevailing pressure within the filter chamber, directly on a side of the filter medium exterior to the filter chamber, so as to exert said compression pressure directly on said side of the filter medium, thereby causing the filter medium to yield against the filter cake.
Opening claim text (preview).
The invention claimed is: 1. A method of operating a filter press, comprising the steps of: feeding filter material into a filter chamber at a feed pressure so as to separate filtrate from solids with a flexible filter medium, and to form a filter cake within said filter chamber between at least two sides of said filter medium, receiving filtrate from the filter chamber via the filter medium, discharging the filter cake formed within the filter chamber, and prior to discharging the filter cake, applying compression on the filter cake formed within the filter chamber by providing compression gas at a compression pressure exceeding a prevailing pressure within the filter chamber, directly on a side of the filter medium exterior to the filter chamber, so as to exert said compression pressure directly on said side of the filter medium, thereby causing the filter medium to yield against the filter cake, wherein the feed pressure is maintained within the filter chamber at least until the compression pressure is achieved on the side of the filter medium exterior to the filter chamber. 2. The method according to claim 1 , wherein the compression gas is provided on the side of the filter medium exterior to the filter chamber at least until a compression gas flow through the filter medium and the filter cake is achieved. 3. The method according to claim 1 , wherein the compression pressure exceeds the pressure prevailing in the filter chamber by at least 1 bar. 4. The method according to claim 1 , wherein the compression gas is alternatingly provided on opposite sides of the filter chamber. 5. The method according to claim 1 , wherein the filter chamber is formed by opposing filter plates held stationary with respect to each other during the whole of the filtration cycle, including discharge of the filter cake. 6. The method according to claim 5 , wherein the filter cake is discharged from the filter chamber by opening a closing member of the discharge arrangement, said closing member being configured to selectively open or close a discharge opening of the filter press. 7. The method according to claim 1 , wherein the filter material is tailings. 8. The method according to claim 1 , wherein the filter material is slurry resulting from bulk mining, such as slurry containing iron ore content, phosphate ore content, or apatite ore content. 9. A filter press, comprising: a filter chamber configured for receiving filter material to be filtered; a flexible filter medium having at least two sides, said filter medium being positioned within said filter chamber, and configured for receiving filter material to be filtered between the at least two sides, so as to separate filtrate from solids of said filter material by filtration; a feed arrangement comprising: a filter material supply, and a filter material flow route, the feed arrangement being configured to feed filter material at a feed pressure from a filter material supply to the filter chamber to be filtered therein by the filter medium, thereby forming a filter cake within the filter chamber, between the at least two sides of the filter medium; a drainage arrangement configured to receive filtrate from the filter chamber through the filter medium; a discharge arrangement for discharging the filter cake formed within the filter chamber; a compression arrangement having: a compression gas flow route for enabling fluid communication for a compression gas form a compression gas supply directly to a side of the filter medium, exterior to the filter chamber, and a compression gas supply for providing, via the compression gas flow route, compression gas to directly a side of the filter medium exterior to the filter chamber, a compression gas control means for selectively enabling or disabling gas flow from the compression gas supply via the compression gas flow route, wherein the compression arrangement is configured to provide compression gas at a compression pressure exceeding a prevailing pressure within the filter chamber, directly on a side of the filter medium exterior to the filter chamber, so as to exert said compression pressure directly on said side of the filter medium, thereby causing the filter medium to yield against the filter cake, wherein feed arrangement being further configured to maintain said feed pressure within the filter chamber at least until the compression pressure is achieved on the side of the filter medium exterior to the filter chamber wherein the filter chamber is horizontal, and formed by an upper filter plate and a lower filter plate one above the other, said filter plates being retractable away from each other for filter cake discharge, the filter medium comprising: an upper side fixed to the upper filter plate and a lower side movable with respect to the lower filter plate for filter cake discharge. 10. The filter press according to claim 9 , wherein the compression arrangement is further configured to: provide compression gas on the side of the filter medium exterior to the filter chamber at least until a compression gas flow through the filter medium and the filter cake is achieved. 11. The filter press according to claim 9 , wherein the feed arrangement and the compression arrangement are further arranged such that the compression pressure exceeds the pressure prevailing in the filter chamber by at least 1 bar. 12. The filter press according to claim 9 , wherein the compression arrangement is further configured to provide compression gas alternatingly on opposite sides of the filter chamber. 13. The filter press according to claim 9 , wherein the drainage arrangement comprises drainage flow route for conducting filtrate, wherein said drainage flow route is a separate entity from the compression gas flow route. 14. The filter press according to claim 9 , wherein wherein the compression gas flow route is configured for enabling fluid communication for a compression gas form a compression gas supply directly to the upper side of the filter medium exterior to the filter chamber, and wherein the drainage arrangement is configured in connection with the lower filter plate, so as to receive filtrate from the filter chamber through the lower side of filter medium. 15. The method according to claim 3 , wherein the compression pressure exceeds the pressure prevailing in the filter chamber by 2-6 bar. 16. The method according to claim 3 , wherein the compression pressure exceeds the pressure prevailing in the filter chamber by 3-5 bar. 17. The method according to claim 3 , wherein the compression pressure exceeds the pressure prevailing in the filter chamber by 4 bar. 18. The filter press according to claim 11 , wherein the feed arrangement and the compression arrangement are further arranged such that the compression pressure exceeds the pressure prevailing in the filter chamber by 2-6 bar. 19. The filter press according to claim 9 , wherein the feed arrangement and the compression arrangement are further arranged such that the compression pressure exceeds the pressure prevailing in the filter chamber 3 - 5 . 20. The filter press according to claim 9 , wherein the feed arrangement and the compression arrangement are further arranged such that the compression pressure exceeds the pressure prevailing in the filter chamber by 4 bar.
Chamber-plate presses, i.e. the sides of the filtering elements being clamped between two successive filtering plates (B01D25/127, B01D25/172, B01D25/176, B01D25/19 take precedence) · CPC title
using membranes · CPC title
by gases or by heating · CPC title
by compression using inflatable membranes · CPC title
by direct contact with a fluid · CPC title
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