Solvent extraction mixer settler apparatus
A mixer settler [ 1 ] comprises a settling tank [ 30 ], an organic launder [ 40 ] provided within the settling tank [ 30 ], an aqueous launder [ 50 ] provided within the settling tank [ 30 ], and an isolated aqueous weir box [ 70 ] which is positioned internally or externally relative to an outer profile of the mixer settler [ 1 ], the isolated aqueous weir box [ 70 ] being at least partially operatively isolated from the settling tank [ 30 ] by the aqueous launder [ 50 ]. The isolated aqueous weir box [ 70 ] comprises an adjustable weir [ 76 ] which separates a recycle chamber [ 72 ] from an advance chamber [ 74 ] therein. The organic launder [ 40 ] is operably connected to an organic advance effluent pipe [ 80 ], and the aqueous launder [ 50 ] is operably connected to the isolated aqueous weir box [ 70 ]. The organic launder [ 40 ] may be operably connected to an isolated organic weir box [ 60 ] which is separate from the isolated aqueous weir box [ 70 ], and may further comprise an adjustable weir [ 66 ] which separates a collection chamber [ 62 ] from an advance chamber [ 64 ]. Also disclosed, is a kit for modifying or fabricating a mixer settler [ 1 ], as well as a solvent extraction process.
1. A co-current mixer settler [ 1 ] comprising:
a settling tank [ 30 ];
an organic launder [ 40 ] provided within the settling tank [ 30 ], the organic launder being operably connected to an organic advance effluent pipe [ 80 ] and provided adjacent a distal downstream portion of the settling tank [ 30 ]; and,
an aqueous launder [ 50 ] provided within the settling tank [ 30 ] and being positioned lower than the organic launder [ 40 ] so as to allow submersion during operation, the aqueous launder [ 50 ] being operably connected to an isolated aqueous weir box [ 70 ] which is positioned internally or externally relative to an outer profile of the mixer settler [ 1 ] and which is separated from the settling tank [ 30 ] by a wall [ 36 ], the isolated aqueous weir box [ 70 ] communicating with the settling tank [ 30 ] via the aqueous launder [ 50 ];
wherein said isolated aqueous weir box [ 70 ] comprises a recycle chamber [ 72 ], an advance chamber [ 74 ], and an adjustable weir [ 76 ] which separates the recycle chamber [ 72 ] from the advance chamber [ 74 ]; and,
wherein at least one of the organic launder [ 40 ] and the aqueous launder [ 50 ] comprises a pipe [ 42 , 52 ] having one or more perforations, apertures, or slits [ 44 , 54 ] therein, the pipe [ 42 , 52 ] having a tubular cross-section mounted to and extending across a width of the settling tank [ 30 ].
2. The mixer settler [ 1 ] according to claim 1 , wherein the organic launder [ 40 ] is operably connected to an isolated organic weir box [ 60 ], which is separate from the isolated aqueous weir box [ 70 ] and which is separated from the settling tank [ 30 ] by a wall [ 36 ], said isolated organic weir box [ 60 ] comprising a collection chamber [ 62 ], an advance chamber [ 64 ], and an adjustable weir [ 66 ] which separates the collection chamber [ 62 ] from the advance chamber [ 64 ].
3. The mixer settler [ 1 ] according to claim 1 , wherein the organic launder [ 40 ] and the aqueous launder [ 50 ] are completely submerged in an organic phase [ 800 ] and an aqueous phase [ 900 ], respectively, during operation.
4. The mixer settler [ 1 ] according to claim 1 , wherein the recycle chamber [ 72 ] of the isolated aqueous weir box [ 70 ] is operably connected to a mixer [ 10 ] via an outlet port [ 79 ] and an aqueous recycle effluent pipe [ 94 ].
5. The mixer settler [ 1 ] according to claim 1 , wherein the organic launder [ 40 ] and the aqueous launder [ 50 ] extend across a width of the settling tank [ 30 ].
6. The mixer settler [ 1 ] according to claim 1 , wherein at least one of the organic launder [ 140 ] and the aqueous launder [ 350 ] comprise a plurality of pipes [ 142 , 352 ] having one or more perforations, apertures, or slits [ 144 , 354 ] therein.
7. The mixer settler [ 1 ] according to claim 6 , wherein the organic launder [ 240 ] comprises a weir [ 242 ] and the aqueous launder [ 250 ] comprises a pipe [ 252 ] having one or more perforations, apertures, or slits [ 254 ].
8. The mixer settler [ 1 ] according to claim 7 , wherein said pipe [ 252 ] comprises one or more bends [ 641 , 651 ] or branches [ 643 , 653 ].
9. The mixer settler [ 1 ] according to claim 1 , wherein both of the organic launder [ 40 ] and the aqueous launder [ 50 ] comprise pipes [ 42 , 52 ] having one or more perforations, apertures, or slits [ 44 , 54 ] therein.
10. The mixer settler [ 1 ] according to claim 1 , wherein said tubular cross-section comprises a rectangular or box shape.
11. A solvent extraction process comprising:
providing a co-current mixer settler apparatus [ 1 ] having a settling tank [ 30 ]; an organic launder [ 40 ] provided within the settling tank [ 30 ] adjacent a distal downstream portion of the settling tank [ 30 ], the organic launder being operably connected to an organic advance effluent pipe [ 80 ]; and, an aqueous launder [ 50 ] provided within the settling tank [ 30 ], the aqueous launder [ 50 ] being operably connected to an isolated aqueous weir box [ 70 ] which is positioned internally or externally relative to an outer profile of the mixer settler [ 1 ] and which is separated from the settling tank [ 30 ] by a wall [ 36 ], the isolated aqueous weir box [ 70 ] communicating with the settling tank [ 30 ] via the aqueous launder [ 50 ]; wherein said isolated aqueous weir box [ 70 ] comprises a recycle chamber [ 72 ], an advance chamber [ 74 ], and an adjustable weir [ 76 ] which separates the recycle chamber [ 72 ] from the advance chamber [ 74 ]; and, wherein at least one of the organic launder [ 40 ] and the aqueous launder [ 50 ] comprises a pipe [ 42 , 52 ] having one or more perforations, apertures, or slits [ 44 , 54 ] therein, the pipe [ 42 , 52 ] having a tubular cross-section mounted to and extending across a width of the settling tank [ 30 ];
mixing an organic phase [ 800 ] with an aqueous phase [ 900 ];
separating the organic phase [ 800 ] from the aqueous phase [ 900 ];
capturing the organic phase [ 800 ] utilizing the organic launder [ 40 ]; and
capturing the aqueous phase [ 900 ] utilizing the aqueous launder [ 50 ].
12. The solvent extraction process of claim 11 , wherein the step of capturing the aqueous phase [ 900 ] comprises collecting aqueous phase [ 900 ] in the recycle chamber [ 72 ].
13. The solvent extraction process of claim 12 , further comprising recycling aqueous phase [ 900 ] collected in the recycle chamber [ 72 ] by sending the aqueous phase [ 900 ] to a mixer [ 10 ] via an aqueous recycle effluent pipe [ 94 ].
14. The solvent extraction process of claim 11 , further comprising advancing the organic [ 800 ] and aqueous [ 900 ] phases to a downstream process by way of advance effluent pipes [ 80 , 90 ].
15. The solvent extraction process of claim 11 , further comprising adjusting the adjustable weir [ 66 ] at a single location utilizing means for controlling or adjusting [ 67 ].
16. The solvent extraction process of claim 11 , wherein the organic launder [ 40 ] is operably connected to an isolated organic weir box [ 60 ], which is separate from the isolated aqueous weir box [ 70 ] and which is separated from the settling tank [ 30 ] by a wall [ 36 ], said isolated organic weir box [ 60 ] comprising a collection chamber [ 62 ], an advance chamber [ 64 ], and an adjustable weir [ 66 ] which separates the collection chamber [ 62 ] from the advance chamber [ 64 ].
17. The solvent extraction process of claim 11 , wherein the organic launder [ 40 ] and the aqueous launder [ 50 ] are completely submerged in an organic phase [ 800 ] and an aqueous phase [ 900 ], respectively, during operation.
18. The solvent extraction process of claim 11 , wherein the recycle chamber [ 72 ] of the isolated aqueous weir box [ 70 ] is operably connected to a mixer [ 10 ] via an outlet port [ 79 ] and an aqueous recycle effluent pipe [ 94 ].
19. The solvent extraction process of claim 11 , wherein the organic launder [ 40 ] and the aqueous launder [ 50 ] extend across a width of the settling tank [ 30 ].
20. The solvent extraction process of claim 11 , wherein at least one of the organic launder [ 140 ] and the aqueous launder [ 350 ] comprise a plurality of pipes [ 142 , 352 ] having one or more perforations, apertures, or slits [ 144 , 354 ] therein.
21. The solvent extraction process of claim 11 , wherein the organic launder [ 240 ] comprises a weir [ 242 ] and the aqueous launder [ 250 ] comprises a pipe [ 252 ] having one or more perforations, apertures, or slits [ 254 ].
22. The solvent extraction process of claim 11 , wherein said pipe [ 42 , 52 ] comprises one or more bends [ 641 , 651 ] or branches [ 643 , 653 ].
23. The solvent extraction process of claim 11 , wherein both of the organic launder [ 40 ] and the aqueous launder [ 50 ] comprise pipes [ 42 , 52 ] having one or more perforations, apertures, or slits [ 44 , 54 ] therein.
24. The solvent extraction process of claim 23 , wherein said tubular cross-section comprises a rectangular or box shape.