ItsASecret
New member
- Joined
- May 1, 2021
- Messages
- 3
Greetings all.
I have been accumulating scrap with high PM content for several decades and now want to cash out.
I am hoping some of you would be willing to share insights you may have on how I might best achieve parting of the PMs. I would like to increase my return with a modest investment of time and money for PPE, glassware, etc. as well as risk - all endeavors have it. By my estimation the cost of the needed PPE and handling / processing equipment are easily justified by the increased return. I have a suitable hood / ventilation system as well that will handle the fumes.
The most immediate questions are:
??-What concentration of Nitric Acid should I purchase? This is in light of the 'special circumstance' below. I understand that I can 'always' dilute but concentration costs...
??-How much Nitric acid at the purchased concentration should I anticipate needing? Of course I would like to minimize waste and disposal issues.
??-Is my overall assessment of methods (below)correct?
I have something like 2000 grams of high purity alloy that is a mix of Au / Cu. Some is 50/50 and some 35/65. I can't reliably distinguish between the two. I also have a similar weight of Ag /Cu high purity alloy and some much smaller quantities of alloy that contain unknown portions Ag, Au, Cu and possibly other metals. All are 'high purity' virgin alloys that are used in the electronics industry. None contain tin or lead etc. All of the material is in wire and foil forms that are thin so, there is a high surface area per unit weight/volume.
According to my research so far, which is primarily focused on the highest return lot of Au/Cu, it seems that my best option is to use heated Nitric acid with agitation at high or full concentration to get the Cu into solution. I found references that suggest to me that commonly stated inquartation ratios often exceed the required level at least in some circumstances. In the reference, a button was used and there was no indication it was reformed to increase surface area before parting. Taken together these two points suggest this is at least worth a test. To the extent that it doesn't work, it will fail only for the 50/50 alloy.
?? Assuming I can actually get the Nitric acid at or to the necessary strength, is this worth attempting? Should I attempt an alternate method -inquartation with Cu? Since Nitric acid will be needed from what I can see in every case, It would seem to best to get the 'good stuff' and dilute as needed. Am I ok so far?
I have looked into electrolytic methods a little. Were I to use this method, most approaches start out melting down metal into anodes. Melting means I loose the possibly optimal state the alloy is in now. Would a stainless steel basket to hold the material as-is work? Another metal? This would seem to be an opportunity to contaminate the system with metals not otherwise present. In any event, I still end up needing Nitric acid for this process along with a donor Au anode cathode for (of less purity?) for the second electrolytic step. and I am not sure what more I will have to do with the first stage slimes which should be pure Au. I would hope wash, melt and make electrodes for purification would be all that is needed since the starting alloy had no other metals - only Au/Cu.
Another problem with electrolytic process is that I would have to cast (for parting) alloy around a pure copper core. This I can probably do. It would help prevent contamination by other metals (fasteners) while permitting complete dissolution of the alloy portion of the electrode. Not at all sure how reliably I can make a 'popsicle' that will have good fusion of alloy so the last bits of alloy won't fall off as the end of separation approaches. This is braze metal though so probably that will take care of itself.
Summing up, It appears that the electrolytic process is more complex and will leave me with an electrolyte solution and possibly sacrificial electrode pieces that will contain more than trace Au that will still need to be recovered. Since my goal is not absolute highest purity or an ongoing process, the electrolytic process may not be warranted. The acid precipitation and electrolytic methods both involve Nitric Acid at some level. So, at the limited scope and scale of this effort, my best option is probably acid precipitation. The worst case for the acid parting will leave the 50/50 alloy intact which I can then inquart to a lower concentration and proceed as before.
Thanks for your time and I look forward to any insights you all can offer.
I have been accumulating scrap with high PM content for several decades and now want to cash out.
I am hoping some of you would be willing to share insights you may have on how I might best achieve parting of the PMs. I would like to increase my return with a modest investment of time and money for PPE, glassware, etc. as well as risk - all endeavors have it. By my estimation the cost of the needed PPE and handling / processing equipment are easily justified by the increased return. I have a suitable hood / ventilation system as well that will handle the fumes.
The most immediate questions are:
??-What concentration of Nitric Acid should I purchase? This is in light of the 'special circumstance' below. I understand that I can 'always' dilute but concentration costs...
??-How much Nitric acid at the purchased concentration should I anticipate needing? Of course I would like to minimize waste and disposal issues.
??-Is my overall assessment of methods (below)correct?
I have something like 2000 grams of high purity alloy that is a mix of Au / Cu. Some is 50/50 and some 35/65. I can't reliably distinguish between the two. I also have a similar weight of Ag /Cu high purity alloy and some much smaller quantities of alloy that contain unknown portions Ag, Au, Cu and possibly other metals. All are 'high purity' virgin alloys that are used in the electronics industry. None contain tin or lead etc. All of the material is in wire and foil forms that are thin so, there is a high surface area per unit weight/volume.
According to my research so far, which is primarily focused on the highest return lot of Au/Cu, it seems that my best option is to use heated Nitric acid with agitation at high or full concentration to get the Cu into solution. I found references that suggest to me that commonly stated inquartation ratios often exceed the required level at least in some circumstances. In the reference, a button was used and there was no indication it was reformed to increase surface area before parting. Taken together these two points suggest this is at least worth a test. To the extent that it doesn't work, it will fail only for the 50/50 alloy.
?? Assuming I can actually get the Nitric acid at or to the necessary strength, is this worth attempting? Should I attempt an alternate method -inquartation with Cu? Since Nitric acid will be needed from what I can see in every case, It would seem to best to get the 'good stuff' and dilute as needed. Am I ok so far?
I have looked into electrolytic methods a little. Were I to use this method, most approaches start out melting down metal into anodes. Melting means I loose the possibly optimal state the alloy is in now. Would a stainless steel basket to hold the material as-is work? Another metal? This would seem to be an opportunity to contaminate the system with metals not otherwise present. In any event, I still end up needing Nitric acid for this process along with a donor Au anode cathode for (of less purity?) for the second electrolytic step. and I am not sure what more I will have to do with the first stage slimes which should be pure Au. I would hope wash, melt and make electrodes for purification would be all that is needed since the starting alloy had no other metals - only Au/Cu.
Another problem with electrolytic process is that I would have to cast (for parting) alloy around a pure copper core. This I can probably do. It would help prevent contamination by other metals (fasteners) while permitting complete dissolution of the alloy portion of the electrode. Not at all sure how reliably I can make a 'popsicle' that will have good fusion of alloy so the last bits of alloy won't fall off as the end of separation approaches. This is braze metal though so probably that will take care of itself.
Summing up, It appears that the electrolytic process is more complex and will leave me with an electrolyte solution and possibly sacrificial electrode pieces that will contain more than trace Au that will still need to be recovered. Since my goal is not absolute highest purity or an ongoing process, the electrolytic process may not be warranted. The acid precipitation and electrolytic methods both involve Nitric Acid at some level. So, at the limited scope and scale of this effort, my best option is probably acid precipitation. The worst case for the acid parting will leave the 50/50 alloy intact which I can then inquart to a lower concentration and proceed as before.
Thanks for your time and I look forward to any insights you all can offer.