Abstract:
A continuous electrowinning system (100) comprising a cell body (106) configured to maintain electrolyte solution at a high pressure and/or temperature within the cell body (106); anodes (174); cathode s (172); an inlet 110 for receiving an influent stream (200) of electrolyte solution; a first outlet (120) discharging an effluent stream (220) of spent electrolyte; a second outlet (130) for removing cathode slime/sludge concentrate (230); and a residence chamber (160) to continuously transfer electrolyte solution from said inlet (110) to said first outlet (120) and increase residence time of said electrolyte solution, the residence chamber (160) comprising one or more channels (162) which are configured to provide a forced flow (212) of electrolyte therein which is strong enough to continuously dislodge and/or move cathode slime/sludge concentrate (204, 206) along and out of said one or more channels (162).
Abstract:
A zinc precipitation circuit is disclosed. The circuit comprises a vessel configured to carry clarified pregnant solution comprising a dissolved precious metal, the vessel further comprising means for delivering zinc particles; a precipitate filter downstream of the vessel configured for solid-liquid separation; at least one classifier downstream of the vessel and upstream of the precipitate filter and further being configured to separate the zinc particles from other precipitates from the clarified pregnant solution; and, a recycle feed stream configured to deliver the zinc particles separated from other precipitates to the vessel. A method of recovering a precious metal via a zinc precipitation is also disclosed. The method comprises the steps of: providing zinc particles to a clarified pregnant solution; forming a precipitate by precipitating said precious metal from the clarified pregnant solution by virtue of the zinc particle addition; separating the zinc particles from other portions of the precipitate, thereby forming a concentrate of the precious metal; recycling the zinc particles separated out by using them for providing to the clarified pregnant solution; and, smelting the concentrate to recover the precious metal.
Abstract:
A system [100'] and process [100] for the continuous recovery of metals is disclosed. The system [100'] comprises a continuous acid wash system [10'], a holding tank [60], a continuous elution system [20'], a continuous electrowinning system [40'], a carbon regeneration system [30'], and a continuous carbon loading/adsorption system [70']. The systems and methods disclosed overcome the disadvantages associated with current systems and processes which utilize batch process steps and equipment designed for batch processes. The systems [10', 20', 30'] are each configured to receive a continuous inflow of a solution or slurry and deliver a continuous outflow of a solution or slurry, without interruptions which are common with conventional metal recovery systems [9000'].
Abstract:
A continuous elution system 100 comprises, in accordance with some embodiments of the invention, a first vessel 200 having a first inlet 204, a second inlet 208, and a first outlet 212; a second vessel 300 having a third inlet 304 and a second outlet 328; and, a third vessel 400 having a fourth inlet 404 and a third outlet 408. The first outlet 212 of the first vessel 200 is operably connected to the third inlet 304 of the second vessel, the second outlet 328 of the second vessel 300 is operably connected to the fourth inlet 404 of the third vessel, and the third outlet 408 of the third vessel 400 is operably connected to the second inlet 208 of the first vessel 200. Also disclosed, is a continuous elution process 1000.
Abstract:
A washer for a particulate material comprises, in accordance with some embodiments of the invention, a chamber 20, 220 adapted for retaining a fluidization medium 130; an inlet 22, 222 adapted for receiving a feed containing particulate 120; a fluidized bed distribution panel 21, 221 for suspending the particulate 120 within the chamber 20, 220 in the presence of said fluidization medium 130; a discharge opening 28, 228 adapted to pass particulate 120 and fluidization medium 130 from the chamber 20, 220; and a screen 26, 226 adapted to separate particulate 120 from the fluidization medium 130. A method of washing and a washing tank for modular washers is also disclosed.