Dawnsdad said:
The other metals are copper and zinc....probably a little ferrous metals as well, but only traces.
You can't just melt it, even with different kinds of flux. All you get is a sticky mess.
I sent samples to several major refiners and the best assays I got came to close to 1 oz/lb.
First off I am not sure why you are having a problem doing a smelt on this material - it may be because you are not using enough flux & or your flux combination is not such the it runs fluid enough to provide good circulation in the crucible when molten & thereby allowing for good collection &/or settling when poured to a cone mold
That said - I don't think I would go with trying to smelt this material to start anyway
However - I think I would still go with a cementing process because you already have the base metals to do so --- its just that they are in the form of a powder rather then a solid mass (like a buss bar)
Considering you have a constant large volume supply of this material I would set it up as a sort of "counter current" leaching/recovery process using the powders them selves to cement the silver from the first batch - then the second batch - then the third - & so on
You said you get 300 - 400 lbs/month & that you do your batches in 50 ozt Ag per batch with recovery of 1 ozt Ag per lb material so that's 50 lbs material per batch
The principle of "counter current" leaching (then recovery) is to increase yield with better chem utilization &/or less chem & therefore less waste &/or chem cost
How it works - You start with your first batch (50 lbs) - dissolve all your metal (copper/zinc/silver) --- then "before" you start your next batch - you use some of your powder (which contains copper & zinc) to cement the silver from batch one - so you get the silver back from batch one "plus" the silver in the powders used to cement the silver from batch one
So - what you have done here is you have used some of your powders to recover the silver from batch one (thereby reducing the amount of powder you have to process) AND you have also increased the yield of batch one
Now - repeat that process with each batch till you come to the end of your 300 - 400 lbs of your material & you will find that your last batch is going to be smaller in size (which means less chem over all) because you have used your powders (for the copper & zinc in them) to cement you Ag from each previous batch
Setting it all up - with the volume of material you are getting on a constant bases - I would go buy a floor model variable speed drill press with a chuck that will chuck a 1/2 inch drill bit - then have a stir rod/paddle made with a 1/2 inch SS rod & SS sheet welded on one end for paddles & a snap ring barrel (like in the pic - which is a 25 or 30 gallon drum) drill a 5/8 inch hole in the center of the lid for the stir rod to fit through & then drill another hole over to the side of the lid to set a funnel into for adding your powders to the reaction vessel (drum)
Fill the drum 1/4 - 1/3 with your 50/50 nitric/D-water - put the lid on - turn the drill press on to start stirring - put the funnel on & start adding your powders
If your material is in fact relatively consistent (as you say) you should be able to determine how much powder to ad (per volume of acid/water starting in the drum) to attain the initial complete dissolved & pregnant solution (as well as reaction time to complete it) & then how much more powder to ad for cementing - with a 90% plus silver cement as your end result --- by first doing a few 1 lb batches to come up with large batch calculations
I would also plumb the reaction vessel (drum) to vacuum the Nox through a scrubber with H2O2 in the first scrub chamber to recover nitric which can then be used for dissolving following batches --- thereby reducing the amount of "new" chem (nitric) needed for each following batch
At least as you have explained the material & the fact that you have an on going continued supply of it - this sort (or some sort) of "counter current" leaching/recovery is what I would explore - as it will reduce chem use/needed - reduce waste & increase yield per chem used
& you will not need to mess with first washing the material with a surfactant - the acid & the stirring should take care of the metals as they are added to the reaction vessel --- I use ultra fine copper (- 300 mesh) sometimes to cement values from my stock pots - between the reaction with the acid & the stirring it poses no problem even though the copper powder wants to float if just added to solution or solution added to it - without stirring
Kurt