Congrats Harold, on your career and work ethics. I started my career at the age of seven by taking over my older brother's paper route -- which, by age fifteen, turned into four routes and by age eighteen, turned into my first back surgery. I was the "news guy", my, late brother, God bless him, was the quarterback guy.
Enough on work ethics, etc., I'm going to take a flying leap and ask a question related to this string of topics. I, too, did not note Comrade Hokes' making any mention of SMB as a precipitant and found the previous dialogue interesting and a bit informative as well --- I understand that H2SO4 will allow AR to thicken as it is heated and will also prevent lead from becoming an issue; however, I'm still not getting the recovery from karat gold that I anticipated.
To set the record straight, I will, ultimately, be working with ore (last assay - 1.5 oz's/ton) and for the past eight plus months have been designing and fabricating a small columnar leach plant as a test of concept devise --- volume wise, definately NOT going to be a money maker --- Sodium Thiosulfate leach agent, well I don't even want to go there.
After the plant and the electrolytic cell that was incorporated in line with the system failed to produce with the thiosulfate leach, I came to the realization that, even if the thio worked, I had no idea as to how to approach the refining of whatever "product" happened to cling to the copper cathodes, sans getting rid of the iron with dilute nitric and digesting whatever is left with AR -----.
Questions are really coming up soon
Following the "rules of engagement," I have been reading and greatly appreciating Comrade Hokes' treatise on waste recovery and have been successful in my efforts to refine karat Au utilizing AR as a digester of gold rolls, AND the addition of H2SO4 (for previously mentioned reasons), and --- here comes the BIG one --- EVAPORATION !!!!!! ( NO BOILING, heat below 200 degrees F from 12 volt coffe cup warmer), EVAPORATION, and EVAPORATION until syrupy, whence HCL is slowly added as a "nitro chaser."
SMB has been my precip. of choice; however, I have a supply of sulfamic acid that someone highly recomended (can't seem to find the thread) and I would greatly appreciate a compare & contrast of the two as precipitation agents. Finally, per "the rules/VERY WELCOME suggestions," I have kept my HCL:HNO2 ratios above 8:1 just to be on the safe side AND incinerated and redigested all prior to the final melt.
Here come the questions:
Question #1
Is karat gold homogeneous? I comitted 6.0gm of 14 karat material (tuxedo pins, links, and tacks) that had been "partially digested" in AR. Realizing that I wanted to get a quantitative measure, I neutralized the digestion and "ribbonized" 2.7 gm of material and recommensed AR digestion. From the 2.7 gm of material that I worked, I expected to net 1.575 gm 24 K (yea, we all wish) Au. Unfortunately, I yielded just about 1/3 that amount of some VERY prety product (will be tested by jeweler friend tomorrow), but not the expected mass. At no step in the process did ANY material come to a boil, sans the fizzing that accompanies the Au/AR reaction that "looks" like boiling (but is not, or ---?) and I'm just a bit confused by the outcome. I actually did recover a relatively large volume from the first run on the tux gear before I decided to get quantitative, but I assumed that ALL would be equal until ALL was digested. Am I wrong in this assumption?
Question #2:
Is 195- 201 degrees F. sufficient to boil Au off? I thought that I had a pretty sweet system with the coffee mug warmer, but if I'm getting too close to the "see ya later temp," I'd sure like to know about it.
Love the forum and, thanks to Palladium who provided a pic, believe that I'm developing a thing for our dear Comrade Calm. Will greatly appreciate any and all input.
Regards, Lance