TSX-V: MKO
VANCOUVER, Dec. 13, 2019 /CNW/ - Mako Mining
Corp. (TSXV: MKO) ("Mako" or the "Company") is pleased to
report that it has completed further mineralogical and
metallurgical tests on its wholly-owned San Albino gold project
("San Albino") located in Nueva
Segovia, Nicaragua. The
various tests completed from 2016 to 2019 were designed to confirm
conclusions from previous work in 2013 and 2014 as well as provide
further design parameters for the mill flowsheet and the associated
mill operations and tailings management. Overall, the program
supported conclusions of previous process development work and the
current mill design parameters.
Akiba Leisman, Chief Executive
Officer of Mako states "these metallurgical results are the
culmination of a significant amount of work completed after the
Company's Preliminary Economic Assessment for the San Albino Gold
Deposit dated April 29, 2015 (the
"PEA") and available on the Mako's website and SEDAR profile at
www.sedar.com. As a result of the recent metallurgical test
work, Mako has decided to use a carbon-in-leach ("CIL") plant
design, which yielded optimized overall recoveries ranging from
86.1 to 96.9%, depending on the mineralization type and despite the
presence of carbonaceous material in these samples. Gravity
recoveries averaged 36.3% with higher gravity recoveries possible
when higher-grade material is processed through the plant.
Finally, Mako is using a dry stack tailings storage facility, which
will contain filtered tailings. It is our belief that this
tailings design will provide the highest level of safety with the
least amount of environmental impact."
As with previous process development testing, the sample
material used for the most recent testing program represented the
three styles of mineralization at San Albino recognized as oxide
and mixtures of oxide and sulphide. Four composite samples were
assembled from diamond drilling core to represent the deposit as
follows: (1) the San Albino Oxide composite; (2) the San Albino
Fresh composite; and (3) the Arras Oxide composite. A fourth
sample, (4) the Underground composite, was also tested to confirm
the metallurgical response in the chosen flowsheet.
With the recognized impact of the free gold in the deposit, the
head grade of the samples was determined in triplicate by fire
assay and crosschecked with metallic assays. The silver assays
were completed with atomic absorption spectroscopy while the
sulphur and carbon analyses were subject to microbalance
measurements and Leco furnace gas detection. The grade of the
four samples used in the testing program are shown in Table 1 and
Table 2 below.
Table 1 – Composite Gold Head Grade Analysis
|
Au (g/t) by Direct
Fire-assays on 30g Splits
|
Au (g/t) by
Metallics on
~500g Splits
|
Average
|
Composite
ID
|
Cut A
|
Cut B
|
Cut C
|
REP Cut A
|
San Albino
Oxide
|
8.69
|
12.75
|
9.38
|
11.65
|
10.14
|
10.52
|
San Albino
Fresh
|
11.60
|
11.81
|
9.99
|
11.45
|
8.57
|
10.68
|
Arras
Oxide
|
4.28
|
3.86
|
3.96
|
3.62
|
4.71
|
4.09
|
Underground
|
7.86
|
5.79
|
4.86
|
8.60
|
6.85
|
6.79
|
Overall
Average
|
8.02
|
Table 2 – Other Head Grade Analysis
|
|
Composite
ID
|
Items
|
Unit
|
San Albino
Oxide
|
San Albino
Fresh
|
Arras
Oxide
|
Underground
|
Ag
|
ppm
|
21.30
|
16.3
|
12.90
|
11.5
|
TOT/C
|
%
|
0.22
|
1.34
|
0.10
|
1.65
|
C/ORG
|
%
|
0.17
|
0.65
|
0.08
|
0.80
|
C/INORG
|
%
|
<0.01
|
0.43
|
<0.01
|
0.71
|
C/GRA
|
%
|
0.05
|
0.26
|
0.01
|
0.28
|
TOT/S
|
%
|
0.23
|
1.72
|
0.10
|
1.58
|
ELM/S
|
%
|
0.01
|
<0.01
|
<0.01
|
<0.01
|
S/S-
|
%
|
0.06
|
1.50
|
0.09
|
1.31
|
S(SO4)
|
%
|
0.21
|
0.02
|
0.21
|
0.05
|
As
|
ppm
|
2650.0
|
5368.0
|
9647.0
|
2570.0
|
Sb
|
ppm
|
7.5
|
7.1
|
10.6
|
5.2
|
Bi
|
ppm
|
34.5
|
20.9
|
<0.5
|
8.9
|
Se
|
ppm
|
18.0
|
12.0
|
22.0
|
14.0
|
SiO2
|
%
|
73.77
|
75.0
|
75.0
|
79.72
|
The program was designed to subject each of the samples to bench
scale tests of the chosen flowsheet for San Albino from
comminution, gravity concentration, CIL cyanide leaching, cyanide
destruction in tailings, and solid liquid separation of the
tailings. The leach circuit proposed employs activated carbon
to address the known carbon content at San Albino. The four
samples in this current test work had a total carbon content
ranging from 0.10 to 1.65% with the potential gold absorbing levels
ranging from <0.01 to 0.71% in-organic carbon. The Underground
composite had the highest level of potential preg-robbing carbon
with the San Albino Fresh composite somewhat less.
In addition to the metallurgical testing, the four composite
samples were subjected to mineralogical studies to characterize the
gold and silver occurrences to assess particle size and shape and
levels of liberation. The study showed that over 90% of the
gold in the four composites occurred as native gold or gold
electrum with only trace quantities in other gold
minerals. The size of the gold grains averaged 12.4 to 30
microns with more than 50% coarser than 30 microns and generally
conducive to gravity concentration. The particle shape was
mostly circular. There was a high proportion of liberation of
the gold particles at 80% passing 150 microns and conducive to
cyanide leaching. The silver occurrence had 60 to 90%
containment in the gold particles or gold minerals and could be
recovered in conjunction with the gold.
In support of comminution in the crushing and grinding of the
San Albino mineralization, the crusher work index tests averaged
4.72 kW/t with the abrasion index average at 0.2882. The work
index for grinding averaged 15.4 kW/t indicating a moderately hard
rock to grind to liberation of the gold and silver at 80% passing
75 microns. Gravity recovery of the four composites showed
good results and ranged from 28.8 to 50.1% with the highest gravity
recovery result on the Arras Oxide composite.
Metallurgical response tests were carried out on the four
samples for grinding, gravity recovery and cyanidation of the
gravity tails with CIL. Four different grind sizes were tested
for each composite sample. The testing showed gold recoveries
by gravity ranging from 24.7 to 50.1% with overall gold recoveries
from combined gravity and CIL ranging from 70.2 to 96.8%. The
oxide samples showed the highest recoveries and the fresh composite
sample showed the lowest. Although there were four size
distributions used in the testing from 80% passing 50 microns to
150 microns there was no appreciable trend in recoveries on the
finer sizes as would be expected. The cyanide leach conditions
were maintained with NaCN consumption ranging from 0.97 kg/t to
2.65 kg/t and lime consumption ranging from 0.62 to 1.89
kg/t. The lowest reagent consumption indicated was on the San
Albino Fresh composite sample. Preliminary optimization
testing showed no improvement with the addition of lead nitrate but
some improvement with extension of the leach time from 24 to 48 hr
for the San Albino Fresh composite sample with the leach time
extension increasing the cyanide consumption.
The optimized leach tests on the three composites showed overall
gold recoveries averaging 86.1% for the San Albino Fresh composite,
92.3% for the Arras Oxide composite and 96.9% for the San Albino
Oxide composite (each averages of four CIL tests,
respectively). Gravity recovery for the three samples averaged
36.3%. Silver recovery was relatively constant for the three
samples tested averaging 67.5% with the highest silver recovery at
74.1% reported on the lower grade Arras Oxide composite. The
leach conditions were optimized for three tests on each sample with
the grind at 80% passing 75 microns.
Comparisons of the overall flowsheet performance to the sulphur
content of the mineralization and the acid insoluable carbon
showed strong correlations with both constituents in the
mineralization contributing to decreases in gold
recovery. Detoxification of the leach circuit tailings showed
that the INCO/SO2 treatment could achieve less than 1 mg/l of WAD
CN in the tailings with cyanide lowered to less than the compliance
level. Settling and filtration testing of the leach tailings showed
that pressure filtration would be required to achieved a tailings
moisture level suitable for conveying and dry stacking. Work
is continuing on defining tailings treatment procedures.
Sampling, Assaying, QA/QC and Data Verification
All sample preparation, compositing, and test work was performed
or overseen by Bureau Veritas Laboratories in Vancouver, Canada. Their processes and
assaying results met the requirements of the Company and its
employees, including Senior Metallurgical Engineer Craig L. McKenzie, and are traceable and well
documented.
Qualified Person
Ross MacFarlane P. Eng Watts,
Griffis and McOuat Limited ("WGM"), Associate Metallurgist and
Joe Hinzer, P.Geo., the President
and Director of WGM both independent of Mako and "Qualified
Persons" under NI 43-101 have reviewed and approved the written
scientific and technical disclosure contained in this press
release.
On behalf of the Board,
Akiba
Leisman
CEO
About Mako
Mako Mining Corp. is a publicly listed gold mining, development
and exploration firm. The Company is developing its high-grade San
Albino gold project in Nueva
Segovia, Nicaragua. Mako's
primary objective is to bring San Albino into production quickly
and efficiently, while continuing exploration of prospective
targets in Nicaragua.
Forward-Looking Statements: Statements
contained herein, other than of historical fact, may be considered
"forward-looking information" within the meaning of applicable
securities laws. Forward-looking information is based on certain
expectations and assumptions, including that the Company's
exploration and metallurgical and mineralogical testing and studies
will be successfully completed; that any outstanding metallurgical
test results, mineralogical studies and recoveries will be as
anticipated; that the Company will be able to successfully adjust
its mine plan based on anticipated successful test results; that
the geological model will continue to yield highly
predicable results; that the carbon-in-leach plant design will
yield anticipated results and be successful and such other risk
factors as outlined in the continuous disclosure documents of the
Company filed on SEDAR at www.sedar.com. Such forward-looking
information is subject to a variety of risks and uncertainties
which could cause actual events or results to differ materially
from those reflected in the forward-looking information, including,
without limitation, the risks that additional satisfactory
exploration and test and study results at San Albino will not be
obtained; that the PEA is preliminary in nature and there is no
certainty that the PEA will be realized; the risk of economic
and/or technical failure at the San Albino project associated with
basing a production decision on the PEA without demonstrated
economic and technical viability; that exploration results will not
translate into the discovery of an economically viable deposit;
risks and uncertainties relating to political risks involving the
Company's exploration and development of mineral properties
interests; the inherent uncertainty of cost estimates and the
potential for unexpected costs and expense; commodity price
fluctuations, the inability or failure to obtain adequate financing
on a timely basis and other risks and uncertainties. Such
information contained herein represents management's best judgment
as of the date hereof, based on information currently available and
is included for the purposes of providing investors with the
Company's plans and expectations at its San Albino project and may
not be appropriate for other purposes. Mako does not undertake
to update any forward-looking information, except in accordance
with applicable securities laws.
Neither the TSX Venture Exchange nor its Regulation Services
Provider (as that term is defined in the policies of the TSX
Venture Exchange) accepts responsibility for the adequacy or
accuracy of this release.
SOURCE Mako Mining Corp.