TORONTO, Oct. 26, 2023 (GLOBE NEWSWIRE) -- Discovery Silver Corp. (TSX: DSV, OTCQX: DSVSF) (“Discovery” or the “Company”) is pleased to announce results from its Feasibility Study (“FS”) metallurgical test program from its Cordero project (“Cordero” or “the Project”) located in Chihuahua State, Mexico. Highlights from the test work include:
- Increased silver recoveries of up to 7% to the precious metals concentrate where higher payabilities are received.
- Significant reductions in reagent consumption while achieving improved metallurgical performance than outlined in the Preliminary Feasibility Study (“PFS”)
- Excellent metallurgical performance achievable for oxide-sulphide blending of up to 15% oxides (the PFS assumed a cap of up to 10% oxides).
- Primary grind sensitivity confirmed a coarse grind size of 200 micron passing p80 is the optimal grind size (unchanged from the PFS).
- Blasting study showed run-of-mine material to be smaller than previously estimated allowing for a smaller primary crusher.
Tony Makuch, CEO, states: “Our Feasibility Study test work demonstrates the exceptional metallurgical characteristics of our Cordero deposit. Previous test work established excellent recoveries for different mining phases and variable grade profiles to generate clean, saleable concentrates. This current program was focused on optimization and was successful in significantly increasing silver recoveries to the precious metals concentrate, where higher payabilities are received, and significantly reducing reagent consumption. The program also established that co-processing of oxides can be increased to up to 15% oxides allowing for flexibility for mine planning and potentially extending the 18-year mine life that was outlined in the PFS. Meanwhile, our other feasibility study work programs continue to advance well and we remain on track for delivering our study in the first quarter of next year.”
PFS METALLURGICAL TEST PROGRAM
Summary: the Company’s two previous metallurgical test programs were primarily focused on variability testwork. Results from these programs established excellent recoveries for all major rock types, rock type blends, different mining phases, variable grade profiles and for oxide-sulphide blending of up to 10% oxides. The FS metallurgical test program was focused on optimizing metallurgical performance for a run-of-mine composite with process variables such as reagent dosage and type, grind size and the testing of oxide-sulphide blends with oxides above 10%.
In total 12 locked cycles test were completed. Optimization testwork was completed on a master composite representing a blend of rock types consistent with the life-of-mine average and an oxide-sulphide blend of 10% oxides and 90% sulphides. The grade of this composite was approximately 35 g/t Ag, 0.5% Pb and 0.7% Zn. Local treated water and well water were also used in select locked cycle tests to confirm that local water quality would not impact metal recoveries. The testwork was conducted by Blue Coast Research Ltd. (“Blue Coast”), an independent third party, with oversight from Libertas Metallurgy Ltd. (“Libertas”), Chris Martin (Independent Consulting Metallurgist) and Ausenco Engineering Canada Inc. (“Ausenco”).
Recoveries: silver recoveries to the precious metals (“PM”) concentrate increased by up to 7% in comparison to the PFS testwork through reagent optimization. Payabilities for silver in the PM concentrate of 95% are significantly higher than payabilities for silver in the zinc concentrate of 70% after a deduction of three silver ounces per tonne. Silver recoveries into the zinc concentrate were approximately 4% lower resulting in an increase in overall silver recoveries of up to 3%. Recoveries for lead were slightly higher than the PFS testwork while zinc recoveries were slightly lower. A comparison of the FS and PFS test results, which were based on the same composite sample, are summarized in the table below.
Sample | Recoveries | Concentrate Grades | |||||||
Ag | Pb | Zn | PM con | Zn con | |||||
PM con | Zn con | Total | Ag | Pb | Ag | Zn | |||
(%) | (%) | (%) | (%) | (%) | (g/t) | (%) | (g/t) | (%) | |
FS composite – ground water | 79 | 6 | 85 | 86 | 84 | 2,717 | 47 | 183 | 52 |
FS composite – treated water | 81 | 6 | 87 | 86 | 83 | 3,033 | 47 | 170 | 53 |
PFS master composite | 74 | 10 | 84 | 84 | 86 | 3,522 | 56 | 328 | 52 |
Reagents: the FS testwork was successful in achieving improved recoveries as outlined above at significantly reduced consumption of key reagents. Consumption of MIBC and CuSO4, the two most expensive reagents as per the PFS, was lowered by 88% and 16% respectively. Material reductions were also achieved for NaCN and Aero 5100. Test results including the costs that each reagent represented in the PFS are summarized in the table below.
Reagent | Consumption (g/t) | % change | PFS Cost | |||||
FS testwork | PFS testwork | $/t processed | US$M (LOM) | |||||
CuSO4 | 130 | 155 | -16 | % | $ | 0.33 | $ | 103 |
MIBC | 16 | 133 | -88 | % | $ | 0.23 | $ | 71 |
Lime | 1,907 | 1,597 | 19 | % | $ | 0.22 | $ | 68 |
ZnSO4 | 150 | 150 | 0 | % | $ | 0.20 | $ | 61 |
X5000 | 17 | 17 | 0 | % | $ | 0.14 | $ | 42 |
NaCN | 30 | 50 | -40 | % | $ | 0.13 | $ | 38 |
Aero 5100 | 16 | 14 | -13 | % | $ | 0.09 | $ | 27 |
Comminution: an additional 10 bond work index (“BWI”) tests and 15 SAG mill comminution (“SMC”) tests were completed to increase the previous data set and increase confidence in the process design assumptions for the comminution circuit. Locked cycle flotation tests were completed on the run-of-mine composite with primary grind sizes of 150 µm, 200 µm and 230 µm. Regrind sensitivity testing and energy input per tonne assessment work was also completed. Results from this testwork were consistent with the process design assumptions for the PFS, including confirmation that a coarse grind size of 200 µm is the optimal primary grind size for the Project.
Oxide-sulphide blends: locked cycle tests were completed on blends of 15% oxides / 85% sulphides and 20% oxides / 80% sulphides. Results demonstrate that excellent metallurgical performance can be achieved with blending of up to 15% oxides (the PFS assumed a cap of 10% oxides). At a blend of up to 20% oxides, recoveries for lead and zinc start to become less economic.
Increasing the blend to up to 15% oxides offers more flexibility for mine planning purposes and has the potential to increase the mine life given there was approximately 30 million tonnes of unprocessed stockpiled oxide material above cut-off in the PFS mine plan.
Sample | Recoveries | Concentrate Grades | |||||||
Ag | Pb | Zn | PM con | Zn con | |||||
PM con | Zn con | Total | Ag | Pb | Ag | Zn | |||
(%) | (%) | (%) | (%) | (%) | (g/t) | (%) | (g/t) | (%) | |
FS – 15% Ox / 85% Sx | 77 | 6 | 83 | 82 | 85 | 3,231 | 50 | 198 | 53 |
FS – 20% Ox / 80% Sx | 75 | 6 | 81 | 78 | 81 | 2,948 | 43 | 209 | 50 |
PFS – 10% Ox / 90% Sx | 74 | 10 | 84 | 84 | 86 | 3,522 | 56 | 328 | 52 |
PROCESS DESIGN
The process design for the FS will consist of conventional flotation with staged expansions, consistent with the PFS approach. The first phase consists of a conventional grinding circuit made up of a primary crusher, SAG mill and ball mill, followed by a flotation circuit. The planned throughput rate of this initial phase is expected to be approximately 25,500 tonnes per day (“tpd”).
The second phase of the plant expansion will include the addition of a parallel circuit consisting of a SAG mill and a ball mill and a duplicate flotation circuit. The planned throughput rate of this expanded phase is expected to be approximately 51,000 tpd.
The proposed process design for the FS is a conventional, well-proven flowsheet that is capital-efficient, robust and delivers comparatively reasonable operating costs with reliability of operations. The design is effectively the same as what was assumed for the PFS with the main change being the incorporation of a smaller primary crusher. This change was based on results from an ore blasting study that demonstrated run-of-mine material to be delivered to the plant is smaller than what was assumed in the PFS.
About Discovery
Discovery’s flagship project is its 100%-owned Cordero project, one of the world’s largest silver deposits. The PFS completed in January 2023 demonstrates that Cordero has the potential to be developed into a highly capital efficient mine that offers the combination of margin, size and scalability. Cordero is located close to infrastructure in a prolific mining belt in Chihuahua State, Mexico.
On Behalf of the Board of Directors,
Tony Makuch, P.Eng
President, CEO & Director
For further information contact:
Forbes Gemmell, CFA
VP Corporate Development
Phone: 416-613-9410
Email: forbes.gemmell@discoverysilver.com
Website: www.discoverysilver.com
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CAUTIONARY NOTE REGARDING FORWARD-LOOKING STATEMENTS
This news release contains “forward-looking information” and “forward-looking statements” (collectively, “forward-looking statements”) within the meaning of the applicable Canadian and U.S. securities legislation. All statements, other than statements of historical fact, are forward-looking statements and are based on expectations, estimates and projections as at the date of this news release. Any statement that involves discussion with respect to predictions, expectations, beliefs, plans, projections, objectives, assumptions, future events or performance (often, but not always using phrases such as “plans”, “expects”, “is expected”, “budget”, “scheduled”, “estimates”, “forecasts”, “intends”, “anticipates”, or “believes” or variations (including negative variations) of such words and phrases, or state that certain actions, events or results “may”, “could”, “would”, “might” or “will” be taken, occur or be achieved) are not statements of historical fact and may be forward-looking statements. In this news release, forward-looking statements relate, among other things, to: the anticipated use of the net proceeds from the Offering; anticipated advancement of mineral properties or programs; future operations; future growth potential of Discovery; and future development plans.
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