Table 1 (a). Chemical composition of dump slags of JSC "Almalyk MMC", in%.
SiO
2
Fe
Al
2
O
3
Cu
CaO
S
Mg
Mo
Au
, g/t
Ag
, g/t
40,2 25,6
5,82
1,63
1,82
1,4 1,05 0,07
1,4
9,5
Table 1 (b). Chemical composition of dump slags of JSC "Almalyk MMC", in%.
SiO
2
Fe
2
O
3
FeO TiO
2
MnO Al
2
O
3
CaO MgO Na
2
O K
2
O
29,8
12,2
41,4 0,23
0,2
4,17
2,58
1,3
0,22
1,43
As can be seen from the data in Table 1, the basis of the dump slag is silicon dioxide SiO
2
and iron oxides, which together account for more than 80%. In the experiments, precisely these
macrocomponents of the slag were initially removed to obtain the remaining valuable
components in the remainder of the concentrate. To remove SiO
2
from the slag, ammonium
fluoride (or bifluoride) was used [17], and iron, after removing SiO
2
, was separated by magnetic
separation [18]. A sieve analysis of crushed slags from the copper-smelting production of the
Almalyk MMC was carried out, the results of which are presented in Table 2.
Table 2. Sieve analysis of crushed slag
Class, mm
Private
total
+ 20
3,6
10,6
-20 +16
7,0
48,2
Chemistry and chemical technology
27
-16 +12
37,0
54,3
-12 +10
6,1
72,3
-10 +6
18,0
87,0
-6 +2
14.7
92,2
-2 +0.59
5,2
94.48
-0,59 + 0,30
2.28
95,66
-0,30+ 0.21
1,18
97,21
-0.21 + 0,10
1,55
97,57
- 0,10 +0.071
0,36
100
- 0,071
2,43
total
The experimental setup is a furnace-reactor in the form of a cylinder with a diameter of 220 mm
and a height of 520 mm and is equipped with thermoelements for heating the samples. It has
three compartments; in the lower part of the installation there is a test sample (slag), previously
homogenized with ammonium fluoride or bifluoride in a stoichiometric ratio to the content of
silicon dioxide. The two upper parts are designed to collect ammonium hexafluorosilicate (NH
4
)
2SiF
6
, which is formed in the sublimation compartment from the sample base. The installation
included a system of traps - condensers. The condenser for collecting (NH
4
) 2SiF
6
is equipped
with a special baffle to prevent the (NH
4
) 2SiF
6
from falling into the starting material. The
installation is also equipped with a system for capturing ammonia gas, which is formed during
the reaction:
NH
4
F + 6SiO
2
= (NH
4
)
2
SiF
6
+ 4NH3 + 2H
2
O
(1)
A weighed portion of copper slag in the amount of 100 g, which passed the stage of charge
preparation, was mixed with ammonium fluoride taken in a stoichiometric ratio with respect to
SiO
2
and placed in the lower segment of the installation intended for sublimation sublimation of
(NH
4
) 2SiF
6
.
The temperature in the furnace was raised to 140 ° -150 ° C and held for 1 hour, then the
temperature was brought to 350 ° -370 ° C and the samples were heat-treated for 1.5 hours. The
temperature was measured with a thermocouple. After removing SiO
2
from the slag base, iron
was separated by magnetic separation. The remainder after processing was a collective
concentrate containing such valuable components as copper, zinc, noble and light non-ferrous
metals. Processing of concentrates for the recovery of these metals is carried out by standard
pyro and hydrometallurgical methods.
For the regeneration of ammonium fluoride, the formed (NH
4
) 2SiF
6
was placed in a flask and
dissolved in a 10% ammonia solution with a 20% excess of the required stoichiometric amount
according to the reaction:
(NH
4
)
2
SiF
6
+ 4NH
4
OH = 6NH
4
F + SiO
2
+ 2H
2
O. (2)
The resulting mixture was stirred for 1 hour at room temperature, after which the precipitate was
separated from the filtrate, washed three times and dried at 110 ° C. The result is a highly
dispersed silicon oxide of high purity. The ammonium hexafluorosilicate wash solution had a
blue tint, characteristic of copper compounds. Before evaporation, the solution was purified with
a group precipitator (NH
4
)
2
S.
Based on the data obtained, the material balance of desiliconization of the dump slag of the
copper-smelting production was compiled, which is shown in Figure 1.
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