Solvent extraction settler arrangement

Abstract

A solvent extraction settler arrangement comprises a settler (1) having a feed end (2) and a discharge end (3), said settler being arranged to separate solution phases from a dispersion fed from the feed end while the dispersion flows to the discharge end. Elongated discharge launders (4, 5) are arranged at the discharge end (3) of the settler for each solution phase to be separated from the dispersion, each discharge launder (4, 5) including a first end (6), an outlet (7, 8) arranged at the first end, and a closed second end (9). At least one of the discharge launders (4, 5) has a form of a conical tube with a cross-section converging from the first end (6) towards the second end (9) and an inclined bottom (10, 11) descending from the second end (9) towards the first end (6).

Claims

1. A solvent extraction settler arrangement adapted for hydrometallurgical liquid-liquid extraction processes, the settler arrangement comprising a settler having a feed end and a discharge end, said settler being arranged to separate solution phases from a dispersion fed from the feed end while the dispersion flows to the discharge end, first and second elongated discharge launders arranged at the discharge end of the settler, the first discharge launder collecting a separated lighter solution phase as an overflow from the settler and discharging the lighter solution phase to a first outlet, the second discharge launder collecting a separated heavier solution phase as an underflow from the settler and discharging the heavier solution phase to a second outlet, the second outlet having a terminal portion opening to the inner space of the discharge launder, each discharge launder including a first end, an outlet arranged at the first end, and a closed second end, characterized in that at least one of the discharge launders has a form of a conical tube with a cross-section converging from the first end towards the second end and an inclined bottom descending from the second end towards the first end; and a level control valve comprising: an extendable and collapsible tube member having a lower end rigidly connected to the terminal portion of the second outlet, and an overflow lip attached to an upper end of the tube member, and an actuator connected to the overflow lip capable of vertically adjusting the height of the overflow lip relative to the lower end.

2. The settler arrangement according to claim 1, where the first outlet is located at the first end of the first discharge launder.

3. The settler arrangement according to claim 2, where the second discharge launder is arranged beside and in parallel with the first discharge launder and the second outlet is located at the first end of the second discharge launder.

4. The settler arrangement according to claim 3, where the arrangement comprises a plurality of second outlet pipes arranged along the length of the second discharge launder at a distance from each other, each second outlet pipe having a fifth end opening to the settler to receive the heavier solution phase as an underflow from the settler, and a sixth end opening to the inner space of the second discharge launder at the bottom of the second discharge launder.

5. The settler arrangement according to claim 4, where a respective level control valve is connected to the sixth end of each second outlet pipe inside the second discharge launder.

6. The settler arrangement according to claim 4, where the settler consists of one tank having a single uniform flow space; and where all first and second outlet pipes open to said single flow space.

7. The settler arrangement according to claim 4, where the settler is divided into a plurality of mutually separated elongated parallel settler sections each extending from the feed end to the discharge end and forming a plurality of parallel flow spaces; and where at least one first outlet pipe and at least one second outlet pipe are connected to each settler section.

8. The settler arrangement according to claim 2, where the settler arrangement comprises a plurality of first outlet pipes arranged along the length of the first discharge launder at a distance from each other, each first outlet pipe having a third end opening to the settler to receive the lighter solution phase as an overflow from the settler, and a fourth end opening to the inner space of the first discharge launder.

9. The settler arrangement according to claim 1, where at least one of the first discharge launder and the second discharge launder is a hollow body made of a fibre-reinforced plastic composite and manufactured by filament winding technology.

10. The settler arrangement according to claim 1, where at least one of the first discharge launder and the second discharge launder is a hollow body made of steel.

11. The settler arrangement according to claim 1, where the level control valve comprises a bellows.

Description

BRIEF DESCRIPTION OF THE DRAWINGS

(1) The accompanying drawings, which are included to provide a further understanding of the invention and constitute a part of this specification, illustrate embodiments of the invention and together with the description help to explain the principles of the invention. In the drawings:

(2) FIG. 1 shows a plan view of a settler arrangement according to a first embodiment of the invention,

(3) FIG. 2 shows a section II-II from FIG. 1,

(4) FIG. 3 shows a plan view of a settler arrangement according to a second embodiment of the invention,

(5) FIG. 4 shows a section IV-IV from FIG. 1,

(6) FIG. 5 shows a section V-V from FIG. 1,

(7) FIG. 6 shows an enlarged detail A from FIG. 2,

(8) FIGS. 7 and 8 show a level control valve in two positions.

DETAILED DESCRIPTION OF THE INVENTION

(9) FIGS. 1 and 3 show solvent extraction settler arrangements which are adapted for hydrometallurgical liquid-liquid extraction processes.

(10) The settler arrangement comprises a mixing unit 24 for preparing a dispersion from mutually immiscible solutions. The mixing unit 24 includes, in this case, a pumping unit 25 and two mixers 26. A settler 1 is arranged to separate solution phases from a dispersion which is fed from the feed end 2 while the dispersion flows towards the discharge end 3. A feeding device 27 is arranged at the feed end 2 for feeding the dispersion prepared by the mixing unit 24 to the settler 1.

(11) Elongated discharge launders 4 and 5 are arranged at the discharge end 3 to collect and discharge the separated solutions. Each discharge launder 4, 5 includes a first end 6, an outlet 7, 8 arranged at the first end 6, and a closed second end 9.

(12) As can be seen in FIGS. 1, 2, 4 and 5, both discharge launders 4, 5 have a form of a conical tube with a cross-section converging from the first end 6 towards the second end 9 and an inclined bottom 10, 11 descending from the second end 9 towards the first end 6. The discharge launders 4, 5 have a form of a conical tube which has substantially a form of a square pyramid with cambered edges.

(13) The discharge launders include a first discharge launder 4 for receiving a separated lighter solution phase (typically organic solution phase) as an overflow from the settler 1. The first discharge launder 4 discharges the lighter solution phase to a first outlet 7 located at the first end 6 of the first discharge launder 4.

(14) The discharge launders further include a second discharge launder 5 arranged beside and in parallel with the first discharge launder 4 for receiving a separated heavier solution phase (typically aqueous solution phase) from the settler 1 as an underflow. The second discharge launder 5 discharges the heavier solution phase to a second outlet 8 at the first end 6 of the second discharge launder.

(15) Preferably the first discharge launder 4 and the second discharge launder 5 are hollow bodies made of a fibre-reinforced plastic composite and manufactured by filament winding technology. As can be seen in FIGS. 6 to 8, the cross-section of the discharge launders is substantially rectangular with cambered corners. Such a form allows it to be easily detached from the mandrel on which it is wound.

(16) A plurality of first outlet pipes 12 are arranged along the length of the first discharge launder 4 at a distance from each other. Each first outlet pipe 12 has a third end 13 which opens to the settler 1 to receive the lighter solution phase as an overflow from the settler 1. A fourth end 14 of each first outlet pipe 12 opens to the inner space of the first discharge launder 4 to conduct the lighter solution phase to the first outlet pipe.

(17) A plurality of second outlet pipes 15 are also arranged along the length of the second discharge launder 5 at a distance from each other. Each second outlet pipe 15 has a fifth end 16 which opens to the settler 1 to receive the heavier solution phase as an underflow from the settler 1. A sixth end 17 of each second outlet pipe 15 opens to the inner space of the second discharge launder 5 at the bottom 11 of the second discharge launder to conduct the heavier solution phase to the second discharge launder.

(18) In the embodiment shown in FIG. 1 the settler 1 consists of one large tank which has a single uniform flow space which extends widthwise over the whole area of the tank and lengthwise from the feed end 2 to the discharge end 3. In this case, all first and second outlet pipes 12, 15 open to said single flow space.

(19) In the embodiment shown in FIG. 3 the settler 1 consists of a plurality of widthwise mutually separated elongated parallel settler sections 1′ each extending from the feed end 2 to the discharge end 4 and forming a plurality of parallel flow spaces. At least one first outlet pipe 12 and at least one second outlet pipe 15 are connected to each settler section 1′.

(20) As shown in FIGS. 6 to 8, the arrangement comprises a level control valve 18 connected to the sixth end 17 of each second outlet pipe 15 inside the second discharge launder 5. The level control valve 18 comprises an extendable and collapsible tube member 19, such as a bellows tube, having a lower end 20 connected to the sixth end 17 of the second outlet pipe 15. An overflow lip 22 is attached at the upper end 21 of the tube member 19. An actuator 23 is connected to the overflow lip for vertical adjustment of the height position of the overflow lip.

(21) FIG. 7 shows the level control valve 18 in a position in which the overflow lip 22 is adjusted to a certain level which determines the level of the heavier phase in the settler. The heavier solution flows from the second outlet pipe 15 over the overflow lip 22 into the inner space of the second discharge launder 5.

(22) FIG. 8 shows the level control valve 18 being adjusted so that the overflow lip 22 is at a higher position than in FIG. 7.

(23) It is obvious to a person skilled in the art that with the advancement of technology, the basic idea of the invention may be implemented in various ways. The invention and its embodiments are thus not limited to the examples described above; instead, they may vary within the scope of the claims.