Gold Trail
Well-known member
After months of failed non sense attempting to process low grade wastes (such as eproms, memory after finger removal, low grade pins, fiber processors, BGA chips, flat packs, ect)
I have been looking into Thiosulphate recovery of the PM's .
Questions i cant seem to find answers for (yes i have looked outside this site as well)
all lowgrade electronic scrap will contain mostly copper as the base metal. With nitric acid pushing 100.00 a gollon delivered, and a gallon disolving / holding about 2 lbs of copper, just isnt practical. period. YOU WILL NEVER RECOVER YOUR MONEY FROM DOING THIS.
so.... I have researched the hell out of this Thiosulphate leaching, and its looking good. heres some problems ive been experiancing / learning about that no one seems to be talking about.
I understand that copper will plate silver as well as gold from the thiosulphate.
and thats the problem. the PM's are plating right back out onto my shreaded materials. Is there a solution for this? my tests as of now are nothing more than a bucket. is the agitaion / continuous movment of the solution required to prevent this? (seems most commercial units pump the solution around)
assuming the agitation would prevent the premature plating of PM's, would it make sense to have two tanks, one as a leach tank and the other as the electrowinning tank, with the thiosulphate being slowly pumped between the two? kinda like a continuous feed process.
the only question i have with electrowinning is the anode (i think) recovery. i dont see how plating gold onto steel wool is a good idea by any means. Copper will work, but were right back at the original problem of the high content of copper in the boards to start with.
I dont understand (havent came accross decent info yet) the further processes for the coconut or carbon
i look forward to any insight on this. I think we can all benifit from this
Ryan
I have been looking into Thiosulphate recovery of the PM's .
Questions i cant seem to find answers for (yes i have looked outside this site as well)
all lowgrade electronic scrap will contain mostly copper as the base metal. With nitric acid pushing 100.00 a gollon delivered, and a gallon disolving / holding about 2 lbs of copper, just isnt practical. period. YOU WILL NEVER RECOVER YOUR MONEY FROM DOING THIS.
so.... I have researched the hell out of this Thiosulphate leaching, and its looking good. heres some problems ive been experiancing / learning about that no one seems to be talking about.
I understand that copper will plate silver as well as gold from the thiosulphate.
and thats the problem. the PM's are plating right back out onto my shreaded materials. Is there a solution for this? my tests as of now are nothing more than a bucket. is the agitaion / continuous movment of the solution required to prevent this? (seems most commercial units pump the solution around)
assuming the agitation would prevent the premature plating of PM's, would it make sense to have two tanks, one as a leach tank and the other as the electrowinning tank, with the thiosulphate being slowly pumped between the two? kinda like a continuous feed process.
the only question i have with electrowinning is the anode (i think) recovery. i dont see how plating gold onto steel wool is a good idea by any means. Copper will work, but were right back at the original problem of the high content of copper in the boards to start with.
I dont understand (havent came accross decent info yet) the further processes for the coconut or carbon
i look forward to any insight on this. I think we can all benifit from this
Ryan