| |
Q: What are the
specific uses for EMEW® in the application of silver
recovery from high grade ores?
A: EMEW® is appropriate for either partial or complete
replacement of the Merrill Crowe process. Its specific
uses include:
- Direct recovery of silver and gold from the low
tenor cyanide solutions (50-400 ppm Ag)
- Retreatment and purification of Merrill Crowe precipitate
(prevention of slag losses)
- Retreatment and purification of ‘raw’
EMEW® silver powder
- Direct recovery of dore from higher concentration
cyanide solutions (+400 ppm Ag)
Q: What is the maximum solids (TSS) that can
be put through the plant?
A: The EMEW technology is capable of tolerating
a high concentration of solids without affecting the
efficiency of the electrowinning process. When operating
the cells in powder production there is a possibility
of contamination of the product which is automatically
harvested from the cell. It is therefore recommended
that solids be maintained below approximately 500 ppm.
Q: What is the typical quality of the product?
A: The quality of product will be largely governed by
the composition of your target solution and the levels
of contained metals - such as lead, zinc and copper.
The product from a highly contaminated solution will
generally be in the region of 65% silver, with quality
of >95% silver being possible from relatively clean
solutions.
Q: What form is the product in, and what steps
are needed to produce dore?
A: If your application requires single step recovery
down to less than 1 ppm Ag, Electrometals will recommend
installation of a plant designed to produce powder rather
than cathode. The silver powder is periodically automatically
harvested from the cells. If you have a requirement
to produce a solid silver dore, the powder can be readily
redissolved in cyanide and electrowon in a small EMEW
cathode plant. The result is a high purity dore which
can be sold directly to a refiner.
Q: What is the concentration of the barren
solution?
A: The EMEW technology is capable of stripping metals
to very low concentration. The silver tenor of the barren
solution will be dependant on the design of a particular
flow sheet. Electrometals can offer a plant which will
operate in any concentration window, and which will
strip silver to less than 1 ppm.
Q: Is de-aeration required?
A: One of the attractive features of the EMEW technology
in this application is that many of the steps required
in Merrill Crowe, such as de-aeration, are no longer
required.
Q: Is the system capable of continuos operation?
A: The EMEW plant operates continuously, with metal
harvesting being automatically controlled through a
simple PLC.
Q: Are any filter aids required
A: No filter aids are required
Q: What improvements can EMEW® make to
an existing brownfield Merrill Crowe plant?
A: The EMEW technology is perfectly suited to expanding
silver production from an existing operation, even if
Merrill Crowe is currently the primary installation
at the site. Installation of EMEW facility does not
add significant complexity to the project. Rather it
has the capacity to take operating pressure off a Merrill
Crowe facility and thereby both extend its life and
increase its efficiency. The technology is capable also
of completely replacing the smelting step in a Merrill
Crowe plant – thereby achieving increase silver
recovery (no slag losses) and, again, simplifying the
total circuit.
Q: What is the typical operational cost ?
A: Between 0.08 to 0.15 US $ per ounce.
A typical comparison of operational costs is shown
in the table below;
| |
EMEW®
US$/annum |
M-C
US$/annum |
| |
|
|
| Labour |
126,000 |
212,250 |
| Zinc powder |
|
48,600 |
| Reagents |
|
11,250 |
| General consumables |
|
22,500 |
| Filter
aid and cloths |
|
28,360 |
| maintenance |
36,188 |
78,750 |
| Crucibles |
|
44,250 |
| Power |
93,820 |
150,848 |
| Fluxes |
|
6,160 |
| General services |
|
37,500 |
| Diesel |
|
22,500 |
| |
|
|
| Total |
256,007 |
662,967 |
| |
|
|
| US$/oz |
0.12 |
0.32 |
|
|