Geo Posted
Do not use AR. Leach MLCC;s in nitric acid only. Then you drop the silver as silver chloride with HCl and that leaves a relatively pure palladium solution to work with. If you can't source nitric acid, use poor man's nitric acid.
Then Rreyes097 asked
But doesn't that form aqua regia,?
Rreyes097 --- I think you miss understand what Geo is saying here - so to clarify
IF (the BIG IF) you are going to leach MLCCs - do NOT use AR to leach the MLCCs --- that is because the AR will create silver chloride which will then end up being tied up in
& lost in the ceramic mud during the leach process
So - you need to use nitric ONLY for the leaching part of the process as the nitric ONLY will dissolve both the Ag & the Pd
Then you wash/filter the nitric leach out of the ceramic mud
Then - once you have the nitric ONLY Ag/Pd solution washed out of ceramic mud you add HCl (or salt water) to the solution in order to drop the Ag as AgCl
Then - after you have dropped the Ag out of the solution as AgCl - the Pd is still dissolved in the solution
So - you then wash/filter the still dissolved Pd out of the AgCl
You can then drop the (still dissolved) Pd you just washed out of the AgCl by using ether the cementing process - or the sodium carbonate/formic acid process - or precipitation with DMG --- &/or other (more complicated) processes that recover Pd from solution
I said -----
IF (the BIG IF) you are going to leach MLCCs
The reason I posted that in bold print is that IMO (In My Opinion) leaching MLCCs - even in small batches is one of the worst ways to go about recovering the Ag & Pd from MLCCs for a number of reasons
1) during the leaching - the ceramic breaks down into an ULTRA fine mud - like clay
which is impossible to filter --- so you have to let the ceramic mud settle then decant the leach - then wash with water - let settle & decant again AND you have to do that
multiple times AND it is next to impossible to get all the Ag/Pd washed out - at the very best at least traces of Ag/Pd will stay tied up in the ceramic mud
2) So you will end up with a LOT of VERY diluted Ag/Pd solution which you will then want to evaporate back down - otherwise when you go to drop the Ag as AgCl - the AgCl will come down ULTRA fine - so fine it will likely cause washing/filtering problems when you go to wash the still dissolved Pd out of the AgCl
3) washing the Pd out of the AgCl presents the same problem as washing the Ag/Pd out of the ceramic mud - it takes a LOT of washing to get all the Pd washed out resulting in a VERY diluted solution again (if you are not set up to vacuum filter --- vacuum filtering does NOT work on the ceramic mud - but will on the AgCl)
4) then you still need to deal with the chem waste in the end of the above
5) then - you still need to convert AgCl to actual silver - a whole other process in & of its self
IMO - its a long & tedious process that creates chem waste that needs to be dealt with for safe disposal
I am not saying it can't be done - just not the best way
IMO - smelting is the best way to go for processing MLCCs - even in small batches
Kurt