Solvent extraction method and solvent extraction settler
View Patent ↗A solvent extraction method for hydrometallurgical liquid-liquid extraction processes, in which method solution phases are separated from a dispersion while the dispersion flows horizontally in a settler from a feed end to a discharge end. The mass flow of the dispersion and solution phases is divided into a plurality of parallel and mutually separated plug flows flowing in the settler from the feed end to the discharge end. The settler ( 1 ) comprises a plurality of elongated settler sections ( 4 ) which are mutually separated and side by side in parallel to each other, Inc settler sections ( 4 ) extending from the feed end ( 2 ) to the discharge end ( 3 ), forming a plurality of mutually separated parallel plug flow channels.
1. A solvent extraction method for hydrometallurgical liquid-liquid extraction processes, in which method solution phases are separated from a dispersion while the dispersion flows horizontally in a settler from a feed end to a discharge end, characterized in that the mass flow of the dispersion and solution phases is divided into a plurality of parallel and mutually separated plug flows flowing in the settler from the feed end to the discharge end, the settler including two consecutively interconnected first and second settler elements, the first settler element having at least one coalescing member to coalesce the dispersion into different phases and the second settler element comprising a retention module to increase residence time of the dispersion in the settler.
2. A solvent extraction settler configured to perform hydrometallurgical liquid-liquid extraction processes, the settler having a feed end and a discharge end, said settler being arranged to separate solution phases from a dispersion while the dispersion flows horizontally from the feed end towards the discharge end, characterized in that the settler comprises a plurality of elongated settler sections which are mutually separated and side by side in parallel to each other, the settler sections extending from the feed end to the discharge end, forming a plurality of mutually separated parallel plug flow channels, the settler including two consecutively interconnected first and second settler elements, the first settler element having at least one coalescing member to coalesce the dispersion into different chases and the second settler element comprising a retention module to increase residence time of the dispersion in the settler.
3. The settler according to claim 2 , where the settler comprises a plurality of feed inlets, and where one feed inlet is arranged to feed dispersion individually to each settler section.
4. The settler according to claim 2 , where the settler sections are formed of tubular shells.
5. The settler according to claim 2 , where the settler comprises a bottom, a vertical feed end wall at the feed end, a vertical discharge end wall at the discharge end, and vertical side walls extending between the ends of the feed end wall and the discharge end wall, together forming a rectangular tank having an inner space; and where a plurality of partitions are arranged in parallel in the tank at a distance from each other to extend between the feed end wall and the discharge end wall so that the inner space is divided by said partitions into the settler sections.
6. The settler according to claim 5 , where the partitions are rigid structures.
7. The settler according to claim 5 , where the partitions are flexible.
8. The settler according to claim 2 , where the settler comprises a plurality of separate chutes arranged side by side in parallel to each other, said chutes forming said settler sections, each chute comprising a bottom and vertical side walls.