Much of the silver if it is thicker in coating or contact points they can remain as pieces and flakes along with powders and salts of silver in the anode bag.
Silver sulfate is quite insoluble in water, temperature plays a minor role (so try not letting the cell overheat by trying to push too much current), the solubility of silver comes up to being quite soluble in strong or hot concentrated H2SO4 (the more free acid in the electrolyte the more the silver or its ions become soluble.
I find a raw Dc power supply works better than a filtered fancy lab supply or a computer supply which are basically switching power supplies switching high-frequency AC and then heavily filtering it for a very smooth DC output, a single diode battery charger has a pulsed DC coming on and off 60 times a second, this pulsed DC single diode rectified supply is helpful to the operation of the cell, a better option I have not tried yet is a supply that pulses a varying DC duty cycle with changing of currents with long positive polarity and with fast short negative polarity in the pulse stream.
The current density will work over a wide range or even cell voltages, much depending on the size of the cell and your operation.
When electrowinning copper they can use 8 to 10 times more power than they do electrorefining copper(2KW h/kg) for electrowinning, for copper refining cells power at around 0.25KW h/Kg.
Lower current where purity is a concern.
I am more focused on the recovery of silver and copper in these discussions, as old copper pipe bus bars and dirty motor contactor points are not a feedstock for refining, although the cathode copper from the cell can be used as an anode in a refining cell basically running it back into a copper cell with better electrolyte, I have no need for pure copper at this point I have enough electrical copper.
Silver sulfate is quite insoluble in water, temperature plays a minor role (so try not letting the cell overheat by trying to push too much current), the solubility of silver comes up to being quite soluble in strong or hot concentrated H2SO4 (the more free acid in the electrolyte the more the silver or its ions become soluble.
I find a raw Dc power supply works better than a filtered fancy lab supply or a computer supply which are basically switching power supplies switching high-frequency AC and then heavily filtering it for a very smooth DC output, a single diode battery charger has a pulsed DC coming on and off 60 times a second, this pulsed DC single diode rectified supply is helpful to the operation of the cell, a better option I have not tried yet is a supply that pulses a varying DC duty cycle with changing of currents with long positive polarity and with fast short negative polarity in the pulse stream.
The current density will work over a wide range or even cell voltages, much depending on the size of the cell and your operation.
When electrowinning copper they can use 8 to 10 times more power than they do electrorefining copper(2KW h/kg) for electrowinning, for copper refining cells power at around 0.25KW h/Kg.
Lower current where purity is a concern.
I am more focused on the recovery of silver and copper in these discussions, as old copper pipe bus bars and dirty motor contactor points are not a feedstock for refining, although the cathode copper from the cell can be used as an anode in a refining cell basically running it back into a copper cell with better electrolyte, I have no need for pure copper at this point I have enough electrical copper.