I then add an aquarium bubbler like in the ap process to keep the solution agitated and after a couple of days i decant the solution and move it to another bucket. This is where i add steel and drop the copper that i will use for the stock pot cementing and when the process is done then the solution is ready for disposal in the next step.
This is essentially the process used for waste treatment which has been discussed on the forum. With the exception that the pH need be increased to 2.5 before adding the iron.
I have never used a stock pot per se. If I processed a lot for gold and the lot had payable platinum I would always zinc the entire lot, add HCl to get rid of the excess zinc, roast the sludge and process the sludge accordingly. This saved me the time of evaporating the solution down as I was able to keep the volume of the solution used to digest sludges down to a minimum so the Pt (and Pd) was concentrated enough to drop easily. Another benefit of this procedure is the metals you recover from the sludges are finely divided and will dissolve in HCl and sodium chlorate so there is no need to get rid of any excess nitric. The waste from this process went into the standard flow for aqua regia waste.
All solutions that had been precipitated were placed into a cementation tank and all waste acids were cemented with copper. This essentially was my stock pot. The solution from there went to the next tank for the pH increase and the iron to recover the copper. The copper recovered was dried and melted and cast in an anode mold to be used in the cementation tank.
The waste was now essentially ferric chloride so it was easy to drop out the iron as a hydroxide and neutralize the waste for discharge. The classic metal hydroxide method involves raising to a pH of 10 to drop all of the metals as hydroxides and then it has to come back down (by acid additions) to neutral for discharge. This method eliminates that step because the iron comes out around pH 3 to 3.5 and after filtration to remove the iron cake the solution only needs additional alkaline to get to discharge pH. Back when I did this the waste met discharge standards, today it would likely need some carbon polishing. Often refiners use this process to clean up their waste and have the "process water" removed for a fraction of the cost it would cost for the waste acid removal and it is removed as a non-hazardous waste.