Agglomeration Technology of Fine Manganese Concentrates with the
Application of Granulation
Volodymyr Krivenko
11
, Evhen Chuprinov
22
, Maryna Korenko
13
, Daria Kassim
14
and Inna Trus
25
1
State University of Economics and Technology, 5, Stepana Til`gi str., Kryvyi Rih, 50006, Ukraine
2
Igor Sikorsky Kyiv Polytechnic Institute, 37/4, Peremogy Avenu, Kyiv, 03056, Ukraine
Keywords: High-Intensity Magnetic Separation, Technology, Manganese Ore, Output Parameters, Sintering Process.
Abstract: The technology for processing the HIMS concentrate, including its partial regrinding and drying, mixing,
granulating and agglomeration in a high layer, has been developed. A technological scheme for the recon-
struction of the Bogdanovskaya sinter plant of the JSC "Pokrovskiy GZK" was developed. Studies have shown
that it is impossible to obtain strong, non-destructible (in the process of transportation) and handling granules
from this concentrate due to an insufficient amount (6-8 %) of fine particles with a particle size of -0,056 mm,
which mainly affect the lumpiness of raw materials. A new technology for the preparation and agglomeration
of fine concentrates, including preliminary granulation was developed.
1 INTRODUCTION AND
ANALYSIS OF PREVIOUS
STUDIES
The introduction of deeper and more advanced
enrichment schemes is one of the ways to increase the
manganese extraction during the manganese ores
enrichments in Ukraine in the situation of a constant
decline of the original ore qualities. It includes both
flotation and high-intensity magnetic separation
(HIMS) (Wu, 2015). As a result, it causes an increase
in the amount of fine particles and moisture in the
concentrates.
Deposits of manganese ores on the globe are
distributed very unevenly, just as uneven their
material composition, which is associated with the
genesis of ores (Kuleshov, 2011). A distinctive
feature of manganese ores from domestic deposits is
the relatively low manganese content and high
concentration of phosphorus and silica (Kutsin,
2012), which does not allow, unlike most foreign
1
https://orcid.org/0000-0001-7822-6358
2
https://orcid.org/0000-0001-8605-3434
3
https://orcid.org/0000-0002-4582-1756
4
https://orcid.org/0000-0002-1750-1237
5
https://orcid.org/0000-0001-6368-6933
ores, to use raw materials without prior enrichment
and storage.
A large number of works (You, 1999; Kwon,
2021; DeFerreira, 2021) are devoted to the study of
the manganese minerals recoverabilities, ores and
concentrates, while the work (DeFerreira, 2021) is
devoted to the study of Brazilian ores. However, the
data available in the literature are often ambiguous. It
is known that MnO2 and MnCO3 dissociate at
relatively low temperatures 510 and 176 °C,
respectively.
In (Kutsin, 2012; Yuanbo, 2017; Singh, 2020) the
issues of mineralogical research of manganese ores of
sedimentary genesis are considered, the issues of
mineralogy and physicochemical properties of
manganese component of iron-manganese modules
are studied, as well as the method of thermochemical
determination of manganite in manganese ores and
the recommendation for Nikopol basin. In the article
(Kulik, 1996) the research of modern tendencies of
development of the manganese mining industry of the
world and Ukraine is executed, the ways of increase
of competitiveness of the domestic enterprises on
256
Krivenko, V., Chuprinov, E., Korenko, M., Kassim, D. and Trus, I.
Agglomeration Technology of Fine Manganese Concentrates with the Application of Granulation.
DOI: 10.5220/0011351500003350
In Proceedings of the 5th International Scientific Congress Society of Ambient Intelligence (ISC SAI 2022) - Sustainable Development and Global Climate Change, pages 256-264
ISBN: 978-989-758-600-2
Copyright
c
2022 by SCITEPRESS Science and Technology Publications, Lda. All rights reserved
increase of competitiveness of the domestic
enterprises on extraction of manganese ore depending
on a modern market situation are offered. The authors
of (Kulik, 1996) made an important conclusion that
the sources of relatively high-quality ores for
manganese and related components are man-made
deposits (sludge storages), the development of which
can be one of the most promising areas, which will
also solve current environmental problems.
In (Samal, 2021; Eom, 2016) the characteristics of
the mineral components of oxidative and carbonate
manganese ores are given. It is determined that the
nature of transformations during heat treatment
(agglomeration, firing of pellets and briquettes,
preheating) is largely determined by chemical,
mineralogical and particle size distribution, as well as
other properties of raw ore.
For the adequacy of raw material evaluation, it is
necessary to compare the quality indicators of
manganese concentrates produced in Ukraine and
abroad (Table 1).
Table 1: Technical requirements for the quality of manganese ores and concentrates for smelting ferroalloys
Component
Mass fraction, %
For
p
heromar
g
anese* For silicoman
g
anese *
Ukraine
I grade
Western
Europe
USA
grade «А»
Ukraine
II grade
Western
Europe
USA
grade «B»
I
g
rade
II
g
rade
I
g
rade
II
g
rade
Mn, no less 43,0 48,0 46,0 46,0 34,0 44,0 40,0 40,0
Fe, no more - - 7,5 8,0 - 9,0 12,0 16,0
SiO
2
, no more - 7,0 9,0 12,0 - 10,0 12,0 15,0
P, no more - 0,12 0,15 0,18 - 0,15 0,15 0,30
*the requirements to Nikopol oxide concentrates and ores and concentrates of foreign producers are specified
Table 2: Chemical composition of the studied samples of manganese ores
Producing
country
Mass fraction of components, %
Mn SiO
2
Al
2
O
3
CaO MgO Fe
2
O
3
P
2
O
5
Na
2
O K
2
O
Losses
during
calcination
1 Geor
g
ia 47,20 12,09 1,88 1,92 0,75 1,86 0,47 0,21 0,59 3,29
2 Brazil 47,60 9,30 1,20 1,03 1,34 9,30 0,14 0,23 1,15 2,29
3 Australia 47,00 13,05 1,63 2,67 0,98 8,94 0,07 0,12 0,03 3,88
4 Ghana-I 30,00 14,05 2,65 4,65 5,08 1,72 0,16 0,28 0,24 31,6
5 Ghana-II 39,79 19,30 4,20 0,40 0,12 7,10 0,32 0,19 0,63 5,02
6 Ghana-III 30,50 13,52 2,20 4,81 4,85 1,05 0,25 0,24 0,21 32,6
Table 3: The results of studies of the general physical properties of manganese ores
Producing
country
Mass
fraction of
moisture, %
Density, kg/m
3
Total
porosity, %
Strength (DSTU
3200-95) on
impact on
fraction more than
5 mm, %
bulk imaginary true
1 Georgia 4,0 1740 2400 3880 38,14 31,0
2 Brazil 8,4 2940 4210 4270 10,92 58,0
3 Australia 2,8 2110 3850 4020 4,23 75,6
4 Ghana-I* 1,6 2300 3240 3270 1,4 71,0
5 Ghana-II 7,2 2090 - 3670 - -
6 Ghana-III 1,6 2120 3190 3370 5,3 72,0
* manganese ore Ghana I and III - carbonate, Ghana II - oxide.
Agglomeration Technology of Fine Manganese Concentrates with the Application of Granulation
257
Table 4: Mineralogical composition of the studied samples of manganese ores
Producing
country
Distribution of man
g
anese b
y
mineral
p
hases, %
Ore phase Pyrolusite
Minerals of
the
psilomelan
group
Brownite Manganite
Manganese
carbonates
(rhodochrosite,
calcium
rhodochrosite
)
Mn M Mn M Mn M Mn M Mn M Mn M
1 Georgia 47,20 76,4 43,7 69,1 - - - - 3,2 6,1 0,3 1,2
2 Brazil 47,60 78,6 16,3 25,8 14,6 25,3 16,7 27,5 - - - -
3 Australia 47,00 77,2 2,5 3,9 3,2 5,4 40,5 66,0 - - 0,8 1,9
4 Ghana-I 30,00 78,5 1,1 1,7 - - 1,2 1,9 - - 27,7 74,9
5 Ghana-II 39,7 66,2 18,3 29,0 17,0 29,4 3,8 6,0 - - 0,6 1,8
6 Ghana-III 30,5 77,8 - - - - - - - - 30,5 77,8
М – the amount of manganese mineral in the ore part of the sample, %.
Samples of manganese ores of different chemical
and fractional compositions (Tables 2, 3, 4), which are
currently widely used in the production of manganese
ferroalloys at domestic enterprises, were studied.
These include samples of manganese ores from
deposits in Georgia, Brazil and Ghana (Grishenko,
2015).
Analyzing the studies results of the manganese
ores physical properties, given in table. 3, it should be
noted that the ores have low porosity, except for ores
from Georgia, and a higher actual density compared
to domestic manganese concentrates. Mechanical
strength (fraction more than 5 mm) of lump
manganese ores is low and inferior in strength to
manganese agglomerate made from domestic
concentrates. For fluxed and non-fluxed manganese
agglomerates of domestic production, the mechanical
strength is 76-80 % and the porosity is 8-22 %.
2 METHODOLOGY, PURPOSE
AND OBJECTIVES OF THE
STUDY
Analytical, laboratory and industrial methods were
used as research methods. A comparison of quality
indicators of manganese concentrates produced in
Ukraine and abroad was performed. Chemical and
mineralogical composition studies of the of dust and
sludge of JSC "Nikopol Ferroalloy Plant" was
conducted in the laboratory. The study of the
agglomeration process was carried out at the
experimental production facilities in the
Mechanobrchormet Institute.
Difficulties with the production of competitive
manganese alloys on domestic raw materials have
intensified in recent years, when, on the one hand,
domestic enterprises began to increase production of
low-phosphorus grades of silicomanganese and
ferromanganese, and on the other hand, increasing
energy costs acted before. This required the use of
imported manganese ores at Ukrainian ferroalloy
plants. Thus, the problem of complex studies of
physical and chemical properties and metallurgical
value of manganese raw materials with their
subsequent aggregation has become extremely
relevant for Ukrainian metallurgists.
The objectives of the article are to perform
comprehensive studies of physicochemical properties
and metallurgical value of manganese raw materials
of various deposits used in the production of
ferroalloys in high-capacity ore reduction furnaces, to
consider returning to the production of enrichment
products lumping is not possible. It is also necessary
to compare the requirements for the quality of
manganese ores and concentrates according to the
regulations of different countries.
3 RESULTS OF THE STUDY
Manganese concentrates sintering with increased
moisture capacity (12.0-26.5 %) and low bulk density
(1350-1750 kg/m
3
) results in high losses on ignition
(up to 10.5-25.5 %). To compare with the iron ores
agglomeration, there is a significant shrinkage of the
layer, and the specific yield of sintering products is
1.5-2.0 times lower.
Since the sintering of such raw materials requires
an increased mass fraction in the return charge as well
as coke breeze (by 1.5-2.0 times), an increase in the
proportion of thin and moisture-consuming
concentrates in the sinter charge makes the sintering
process even more difficult due to a decrease in the
gas permeability of the charge.
Foreign specialists at their sinter plants don’t have
any experience in sintering manganese charges that
ISC SAI 2022 - V International Scientific Congress SOCIETY OF AMBIENT INTELLIGENCE
258
include thin concentrates with high moisture capacity
either. Thin concentrates in various quantities are
added to gravity concentrates at domestic manganese
sintering plants. Such materials are supplied to the
sinter mixture in an unprepared form.
Laboratory and industrial studies have established
that the introduction of an unprepared HIMS
concentrate into the sinter charge in an amount of
more than 15% reduces the technological parameters
of the agglomeration process.
The urgency of the problem is confirmed by the
fact that the production volumes from thin
concentrates at the Pokrovskiy Ore Mining and
Processing Plant (JSC "Pokrovskiy GZK") will
increase to 300 thousand tons per year. The existing
capacities of the sinter plant will not be able to
process such a quantity.
The «Mekhanobrchermet Institute» specialists
with specialists from «State University of Economics
and Technology» and «Igor Sikorsky Kyiv
Polytechnic Institute» have developed a new
technology for the preparation and agglomeration of
fine concentrates, including preliminary granulation.
During the research manganese concentrates of
the current production of Pokrovskiy Ore Mining and
Processing Plant were used. Chemical and
granulometric composition of materials, as well as
their physical properties are presented in the table 5
and 6.
Table 5: Chemical composition of manganese concentrates from JSC "Pokrovskiy GZK"
Concentrate
Mass fraction of com
onents, %
Мn SiO
2
, А1
2
O
3
СаО МgО Fe
2
O
3
Na
2
O K
2
O P
2
O
5
СО
2
passing breeds
Oxide, gravity 36.30 22.68 1.98 2.12 1.18 3.40 0.60 1.20 0.40 1.94 0.20
Carbonate, gravity 28.00 14.75 4.08 8.38 1.70 3.85 0.62 1.40 0.47 19.56 25.50
HIMS 31.70 26.80 2.10 3.4 1.20 3.70 0.58 1.34 0.378 2.14 13.10
Table 6: Granulometric composition and physical properties of concentrates from JSC "Pokrovskiy GZK"
Material
Mass fraction, %, size classes, mm
Moisture
content, %
Specific
s
urface area
,
m
2
/kg
True
density,
kg/m
3
B
ulk density
,
kg/m
3
+ 10 10-5 5-3 3-1 1-0.5
0.5-
0.25
0.25-
0.16
0.16-
0.1
0.1-0
Oxide
gravity
concentrate
22.0 13.3 7.0 30.9 6.8 9.8 10.2 17.5-22.5 3430 1600-1700
Carbonate
Gravity
concentrate
14.7 21.9 57.4 6.3 12.0-19.0 3230 1650-1750
Concentrate
HIMS
23.8 11.7 10.6 23.6 24.1 6.2-21.5 88.0-98.0 3600 1350-1450
Gravitational oxide and carbonate concentrates
are mainly represented by a fraction of 1-10 mm. The
HIMS concentrate has a particle size of -1.0 mm and
a moisture content of 24-26 %. Studies have shown
that it is impossible to obtain strong, non-destructible
(in the process of transportation) and handling
granules from this concentrate due to an insufficient
amount (6-8 %) of fine particles with a particle size
of -0.056 mm, which mainly affect the lumpiness of
raw materials. It is possible to increase the proportion
of fine particles by grinding a part of the HIMS
concentrate in dry grinding mills with simultaneous
drying.
The refinement of the grinding technology was
carried out on a plant operating in a closed cycle with
an air-pass separator and equipped with a gas burner.
A batch of crushed product with a mass fraction of a
fraction of -0.056 mm equal to 70-75 % and a specific
surface area of 265-280 m
2
/kg was obtained at the
installation in the spent mode in order to conduct
research on its pelletizing into granules with a particle
size of 2-8 mm. Such granules absolutely meet the
requirements of the sintering process.
Agglomeration Technology of Fine Manganese Concentrates with the Application of Granulation
259
Figure 1: Dependence of the physical properties of the sinter charge and the sintering coefficient on the mass fraction of the
HIMS concentrate in the ore part of the charge during sintering of the agglomerate with oxide grade II (a) and carbonate (b)
gravity concentrates: 1 - concentrate of HIMS in the form of microgranules; 2 - HIMS concentrate in its original form
The crushed material in various amounts was
dosed to the original HIMS concentrate, mixed and
pelletized in a bowl pelletizer with the addition of
water. Strength tests of granules were carried out in
order to determine their resistance to destruction
during overloading and mixing with larger and more
abrasive components that make up the sinter charge,
as well as during intermediate storage in a hopper
under conditions close to industrial ones. The
research results are shown in the table 7.
ISC SAI 2022 - V International Scientific Congress SOCIETY OF AMBIENT INTELLIGENCE
260
Figure 2: Dependence of the technological parameters and the strength of the agglomerate on the mass fraction of the HIMS
concentrate in the ore part of the charge during sintering of the agglomerate with oxide grade II (a) and carbonate (b) gravity
concentrates:
1 - HIMS concentrate in the form of microgranules;
2 - HIMS concentrate in its original form.
The dependence of the physical properties of the
sinter charge and the sintering coefficient in the
production of manganese agglomerate on the mass
fraction of the HIMS concentrate in the initial and
prepared form is shown in Fig. 1. The dependence of
the technological parameters of the agglomeration
process on the mass fraction of the HIMS concentrate
is shown in Fig. 2.
An increase in the mass fraction of the HIMS
concentrate over 15-20 % leads to a deterioration in
the physical and gas-dynamic properties of the sinter
charge, which in turn reduces the technological
parameters of sintering and the quality of the sinter.
When the mass fraction of the HIMS concentrate in
an unprepared form in the sinter batch is equal to 40-
60%, the agglomeration process becomes unfeasible.
Agglomeration Technology of Fine Manganese Concentrates with the Application of Granulation
261
Due to the lower moisture capacity of the carbonate
gravity concentrate, the larger average particle size
and their greater roughness in comparison with the
oxide gravity concentrate of the II grade, the effect of
the addition of the HIMS concentrate to the charge
has a lesser effect on the deterioration of
technological parameters. When sintering carbonate
concentrate with additives of HIMS concentrate, due
to the high mass fraction of volatiles, the yield of
suitable agglomerate decreases and the rate of
filtration of exhaust gases. In combination with
thermal destruction of lump carbonate concentrate,
this causes to a significant increase in dust removal in
the process of sintering.
Table 7: Characteristics of the properties of the initial charge from the HIMS concentrate and granules obtained from it
Indicator
Ex
p
eriment o
p
tions
1 2 3 4 5
Moisture mass fraction in the HIMS concentrate before
mixin
g
, %:
in the original
16.0 16.0 25.0 25.0 25.0
in shredded
3.0 3.0 3.0 3.0
Mass fraction in the charge, %:
HIMS concentrate 100 80 60 40 20
crushed HIMS concentrate
20 40 60 80
Mass fraction -0,056 mm in the charge, %
6.2 25.9 37.3 48.7 60.1
Bulk density of granules.
1330 1350 1390 1430 1510
Mechanical strength of granules, after dropping twice
from a height of 2 m onto a metal plate (fraction yield
+2 mm
)
, %
32.4 68.7 86.8 96.9 96.4
When using HIMS concentrate in the sinter
charge in the form of granules, the characteristics of
the sintered layer are improved. Due to the increase
in the gas permeability of the charge, it is possible to
carry out the sintering process in a higher layer with
an unlimited amount of the proportion of granules in
the ore part of the sinter charge. With this technology,
rolling of solid fuel into granules is eliminated, which
reduces the specific consumption of coke breeze.
It has been established that the addition of HIMS
concentrate to the sinter charge in an unprepared form
in an amount of 15 to 30 % and of 30 to 50 % reduces
the specific productivity of the sinter plant by 25 and
50 % respectively, as well as the strength of the sinter
and increases the loss of the initial material.
The results of sintering class II oxide gravity
concentrate with the addition of HIMS concentrate in
the form of granules were processed on a computer
using the program of multiple correlation-regression
analysis. A mathematical model of the agglomeration
process has been created, which is described by the
regression equations connecting the output
parameters with the controlled ones:
Q = 2.7288 + 0.0471τ + 0.000799SV -
- 0.018642G - 0.014В - 0.15201С;
Р = 77.4465 + 1.06765τ - 0.0019413SV -
- 0.079485G - 0.0033346В + 0.21690С,
where Q - unit specific productivity, t/(m
2
·h); τ -
ignition time, min; SV - sintering vacuum, Pа; G -
mass fraction of granules of the HIMS concentrate (in
relation to the oxide gravitational concentrate of the
II class), %; В - mass fraction of return in the charge,
%; С - mass fraction of coke breeze in the charge, %;
Р - agglomerate impact strength, %.
The obtained regression equations were used to
optimize the sintering process. The optimization
problem consisted in determining such values of τ,
SV, G, B and C within the specified limits, at which
the specific productivity of the installation and the
mechanical strength of the agglomerate reached the
maximum values.
The conditions and results of optimization of the
sintering process are given in table 8.
The second method of pre-coating of fine
concentrates was investigated - the method of
briquetting, the feature of which was the absence of
binder and increasing the pressing pressure to 30
MPa. A batch of briquettes was obtained to conduct
research on sintering the sinter using a sinter batch of
raw briquettes measuring 15×15×20 mm.
Experiments on agglomeration have shown that with
a content of 30-40 % of briquettes in the charge, the
height of the sintered layer can be increased to 700-
900 mm.
In the process of processing the sludge formed
during the enrichment of oxidized manganese ores on
high-intensity magnetic separators, a concentrate
ISC SAI 2022 - V International Scientific Congress SOCIETY OF AMBIENT INTELLIGENCE
262
with a high specific surface area and high moisture
content was obtained. Concentrate of high-intensity
magnetic separation of manganese sludge contains,
%: 33,0 Mn; 24.8 SiO
2
; 2.9 Al
2
O
3
; 6.2 FeO; 0.435
P
2
O
5
and other components. The true density of the
concentrate is 3420 kg/m
3
, the specific surface area is
250 m
2
/kg; bulk density 1500 kg/m
3
, angle of natural
slope 43.5 degrees.
Table 8: Conditions and results of optimization of the sintering process
Parameters Parameter type
Symbol
Restrictions
Optimal value
Bottom
line
Upper
b
ounds
Specific
productivity,
t/
(
m
2
·h
)
Output Q 0.9 1.6 1.33
Agglomerate
im
p
act stren
g
th
P 74.0 81.0 79.2
Ignition time, min. Adjustable τ 3.0 5.5 5.0
Vacuum, Pa SV 5000 11000 6500
Mass fraction of
g
ranules, %
G 25.0 60.0 30.0
Mass fraction of
return, %
В 15.0 35.0 20.0
Mass fraction of
fines, %
С 7.0 9.5 9.0
The concentrate is characterized by high moisture
content - the moisture content in it after filtration is
30-40 %. The concentrate was pelleted in bowl
pelletizers with a diameter of 1 and 2 m to obtain raw
pellets of uniform particle size distribution (diameter
14-18 mm) without the use of reinforcing additives,
and then subjected to heat treatment. The optimal
parameters of heat treatment of pellets are given in
table. 9.
Table 9: Optimal parameters of heat treatment of pellets
Technological modes
Duration of heat
treatment, min
Temperature of the
heat carrie
r
, °С
Filtration speed,
m
3
/(m
2
·s)
Lquefaction,
×10
3
Pa
At the entrance At the exit
Heating the top
of the layer
90-120 200 30-40 0,3-0,5 2,00
Blow drying from below 12 350 80-90 1,2-1,4 5,00
Blow dr
y
in
g
on to
p
3-4 350 80-90 1,1-1,2 5,00
Heatin
g
6-7 700-900 200-350 1,1 5,00
Burnin
g
12-15 1150-1180 400-500 0,9-1,0 5,00
Recuperation 3 1000 500 0,9 5,00
Cooling 15-16 20-25 800-300 1,3-1,4 5,00
The introduction of 1.0-1.2 % of finely ground
solid fuel into the charge intensifies the firing process,
reduces the temperature interval between the horizons
of the fired layer, and increases the specific
productivity of the installation. The main average
quality indicators of pellets are as follows:
compressive strength,
kN
/
p
ellet
impact strength
(fr. +5 mm), %
specific
p
roductivity, t/(
m
2
·h)
without solid fuel 1,7 90 0,57
with the addition of 1% anthracite: 1,27 87 0,72
Agglomeration Technology of Fine Manganese Concentrates with the Application of Granulation
263
4 CONCLUSIONS
1. One of the ways to increase the rate of manganese
extraction in the enrichment of manganese ores in
Ukraine in a constantly declining quality of source
ore is the introduction of deeper and more advanced
enrichment schemes, including flotation and high-
intensity magnetic separation (HIMS), although this
leads to increased fine particles and moisture in
concentrates.
2. A comparative analysis of chemical,
mineralogical compositions and physical
characteristics of imported and domestic manganese
ores and concentrates, as well as the laws of
transformation of the phase composition in the
process of regenerative heat treatment. It is confirmed
that the main distinguishing feature of the studied
manganese raw materials from foreign producers is
the low value of the modulus of phosphorus (P/Mn <
0.0035) and silica (SiO
2
/Mn from 0.5 and below),
which allows to achieve high technical and economic
performance.
3. On the basis of the studies performed, it was
established that with the introduction of 30-50 % of
the HIMS concentrate into the sinter batch, the
productivity of the sinter plant decreases by 25-50 %,
the strength indicators of the agglomerate deteriorate,
and the removal of dust increases.
4. The technology for processing the HIMS
concentrate has been developed, including its partial
regrinding and drying, mixing, granulating and
agglomeration in a high layer. The optimal
parameters of agglomeration have been determined,
which make it possible to carry out the process
without reducing the technological parameters when
using 30-45 % HIMS concentrate in the sinter batch.
5. A technological scheme was developed for the
reconstruction of the Bogdanovskaya sinter plant of
the JSC "Pokrovskiy GZK". The technical and
economic assessment of the developed technology
that was carried out indicates its high efficiency.
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