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Journal of Minerals & Materials Characterization & Engineering, Vol. 6, No.2, pp 103-108, 2007
jmmce.org Printed in the USA. All rights reserved
Processing of the Pyrite Concentrates to Generate Sulfurous
Anhydride for Sulfuric Acid Production
T.A. Chepushtanova, V.A. Luganov
Kazakh National Technical University after K. I. Satpayev
Contact: + 011-7-327-2680139, Satpayev St., b.22, zip code – 050013,
E-mail: firstname.lastname@example.org, email@example.com
The results of two-stage roasting of pyrite concentrate with air blowing and
the principle scheme of the process are presented in the report.
The results of experimental sulfuric acid production tests using pyrite
concentrate to generate sulfurous rich gas containing 0.1 – 0.15% of sulphur trioxide
are shown. Comparative characteristics with technologies known for the present are
Keywords: roast, pyrite, sulfuric anhydride, sulfurous anhydride
Traditionally the basic sources of raw material for production of sulfuric
acid are sulphur and iron (sulfuric) pyrites. About half of sulfuric acid is produced
from sulfur and one third is from pyrite. Discharge gases from the processing of non-
ferrous metals which contain sulphur dioxide make up the rest .
With the purpose of environment protection all over the world measures are
being taken to use industrial wastes containing sulphur. Sulfur dioxide discharged
from the waste gases of power plants and metallurgical plants amounts considerably
more than that is used for production of sulfuric acid. Due to the low SO
concentration in these waste gases, their processing is not always possible for the
present [2-3]. Among the raw materials for sulfuric acid production, the waste gas is
the cheapest; the wholesale prices for pyrites are also low, while sulfur is the most
expensive . Therefore, to achieve the economic expediency of sulfuric acid from
sulfur, the scheme should be developed where the cost of sulfuric acid processing
must be essentially lower than the cost of processing pyrites or waste gases.
In this work, a two-stage roasting technology of pyrite with sulfurous anhydride
production by economically and ecologically expedient method is presented.
104 T.A. Chepushtanova and V.A. Luganov Vol.6, No.2
2. MATERIALS AND METHODS
Initial pyrite concentrate contained 49.8% sulphur, 43-86% of iron, 0.133%
of cobalt, 2.4% of SiO
, 0.57% of Al
, and 0.72% of CaO. 89.5% of the material
had the size less than 0.1 мм. The moisture content was 1.2%.
Semi-industrial tests of pyrrhotite roasting in autogenous regime at 22%
blowing oxygen content and 20–25ºC lattice temperature were conducted on the
device as shown in Fig. 1. The device includes the furnace, fluidized bed (operation
area 0, 33 m
) with the mobile heating chamber, loading and unloading system and
dust trapping system.
3. RESULTS AND DISCUSSION
Concentration of sulphur dioxide in the roasting gas depends on the ratio of
sulphur and air fed for burning. If the air is taken in stoichiometric quantity, that is, 1
mole of oxygen for every mole of sulfur, the concentration of sulfur dioxide will be
equal to the volume share of the oxygen in the air (Сso2.max = 21%) in case of the
full sulfur burning. However, the air is usually taken in excess because otherwise the
temperature in the furnace will be too high.
In the case of adiabatic sulphur burning, the roasting temperature for
reaction mixture of stoichiometric composition will be 1500ºC. In practical
conditions, possibilities of temperature rise in the furnace are limited by the fact that
the lining of the furnace and gas pipes is quickly destroyed if the temperature is
higher than 1300 ºC. Usually, the roasting gas during sulfur burning is produced with
13–14% of SO
We know that the method of sulphatizing roasting of sulfide material
containing non-ferrous metals with sulfurous gas production in the furnace of
fluidized bed use oxygen-air blowing in 2 stages. The first stage takes place during
the roasting of initial material up to pyrrhotite with the shortage of the oxygen in the
blowing. The second stage involves the sulfatizing roasting of this product with the
excess of the oxygen. The distributions of the total oxygen-air blowing in two stages
are in parallel . The roasting gases from both stages are joined, and the cinder is
removed at the second stage. Production gas contains 12–18 % of SO
, 4 – 9 % of O
0,4 – 1.5 % of SO
, and the dust of iron sulfates. But such a method has a lot of
shortcomings: significant content of sulfur anhydride in production gas, not high
concentration of sulphurous anhydride in it (12–18 %), and a small extent of the
consumption of the blowing oxygen.
There is also a method where a production gas contains 15 % of SO
and 6 %
, 0,5–2.5 % of SO
, with the use of 70 % of oxygen, and also the dust of iron
sulfates [5-6]. But this method also has a number of essential shortcomings: increased
Vol.6, No.2 Processing of Pyrite Concentrates 105
content of elemental sulphur in gases at the pyrrhotizing (the first) stage, and
complexity in apparatus for the dust collection system.
Thus, the purpose of this work is to obtain the production gas which
practically doesn’t contain sulphur anhydride while simultaneously has an increase of
the sulfurous anhydride content in it.
We developed a technology of two-stage roasting of pyrite concentrate on the
basis of the air blowing with production of the rich sulphurous gas containing
minimal quantity of sulphur trioxide. This involves autogenous two-stage pyrrhotizing
roasting with 60–65% of elemental sulfur removal and transforming it into SO
first stage and the removal of the remained 35–40% sulfur with produced Fe
the cinder at the second stage.
3.1 First stage of roasting
The essence of the method is in the following: the autogenous roasting
production of sulfide materials of the cinder and the pure production of gas suitable
for direct processing to produce sulfuric acid without containing sulfur anhydride and
oxygen is achieved by transformation of 60–65% of sulfur of pyrite into SO
first stage. A number of reactions take place in this process and after this, sulfur
anhydride which came with the gas is completely destroyed and the total oxygen of
the blowing is used up. Semi-industrial tests of pyrrhotizing roasting in autogenous
regime were conducted on the device as shown in Fig. 1.
In the process of tests we regulated: velocity of concentrate feeding, mazut
and air consumption; and controlled: resistance of the layer; discharge under the arch,
temperature under the lattice, in the layer (3 locations), under the lattice, in cyclone, in
the chamber of final burning, and in accumulating coolers; the content of the oxygen,
carbon dioxide and sulphurous anhydride in gases.
The study has achieved autogenous pyrrhotizing roasting at specific capacity
of 26-29 t/m
·day with desulphurization of 60-65%. Produced solid roasting product
is pyrrhotite (Fe
S) with 20-25% iron oxides. The extent of oxygen use exceeds
95%. Average sulphur extraction into gas: 49,34% from the cinder, 40,10% from the
dust. Iron and sulphur content in cinder corresponds to the extent of pyrite
dissociation 95-96.5%, and in cyclone dust 74-75%. Concentrate of different size
classes are present with layers created from different time, and it has different extent
of pyrite dissociation. Fine dust trapped in the electrical filter is partly oxidized while
coming through the chamber of final sculpture burning. Gases produced in the process
contain in the average of 16.7–17% sulfurous anhydride and 0.1 – 0.5% of oxygen.
This corresponds to the extent of oxygen use in the layer with more than 95%.
106 T.A. Chepushtanova and V.A. Luganov Vol.6, No.2
Fig. 1 – Plant for pyrrhotizing roasting
(1 – Fluidized bed furnace; 2 – fire-chamber; 3-bunker for concentrate;
4 – Feeder; 5 – unloading; 6 – accumulator-cooler; 7 – container; 8 –
3.2 The second stage of roasting
Fig.2 shows the schematics for the two stage roasting operation. In the second
stage, gasification of the remained sulphur takes place. It produces the Fe
with the use of the cold air blowing on the layer at the temperature of 685–700°С. The
blowing air consumption is 900–1000 Nm
·hour. The oxygen consumption in the
blowing was 0.14–0.175 Nm
/kg of the concentrate.
At the second stage of roasting which is also carried out in furnaces of KC on
the principle of the cold air blowing gases, waste gases are produced containing 8-
10% of SO
, 9-10 % of O
and nearly 0.5 % of SO
. As a result of mixing of waste
gases of two stages, gases are produced containing 16-17% of SO
, 0.1–0.5 % of O
and 0.1–0.15% of SO
. Processing of gases containing decreased quantity of SO
get less quantity of the washing acid, decrease corrosion influence on the dust
trapping and gas piping systems, and increase the output of the finished product –
Vol.6, No.2 Processing of Pyrite Concentrates 107
Fig. 2 – Principle scheme of two-stage roasting of pyrite concentrate
Decreased consumption of the blowing air in comparison with known
technologies generate more concentrated gases and this is accompanied with less
power consumption for lower blowing volume, less operational expenses for
purification of produced gases, and the technology becomes more profitable.
We developed and checked in stages at an industrial-experimental scale for the
technology of two-stage roasting of pyrite concentrates for producing rich sulphurous
gas containing 0.1-0.15% of sulfur trioxide. The characteristics of the technology
- raise the temperature of roasting gases for 50-70
С, which improves the
corrosion resistance of the equipment and increases the productivity of
- lower the required roasting area of furnaces for 30-40%;
- lower the blowing consumption by 30% at the expense of increasing the
extent of the oxygen use and correspondingly raise the content of sulphur
dioxide in roasting gases;
- simplify the system of dust-gas purification at the expense of decreasing the
volume of roasting gases; lower the content of sulphur trioxide in roasting
- make the technology more universal, suitable for processing raw materials
containing different non-ferrous metals;
- lower the capital and operational expenses for roasting remake.
Thus, the use of the offered technology enables the production of sulfuric acid
more economically by decreasing the concentration of sulfur trioxide from 0.5 to 0.1–
108 T.A. Chepushtanova and V.A. Luganov Vol.6, No.2
0.15%, which improves the work of apparatuses of cooling and purification of
roasting gases and increasing the sulfur dioxide concentration from 15 % to 17%.
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roasting of pyrite concentrate”. J. Chemistry and technology of chalcogenes and
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2. Vanyukov, A.V., Zaitsev, V.Ya., 1993, Theory of pyrometallurgical processes:
Metallurgy, pp. 320, Moscow.
3. Tarasov, A.V., 2001, Production of non-ferrous metals and alloys: Metallurgy,
v.1., pp. 410, Moscow.
4. Method of processing of cobalt containing pyrite concentrates: Patent № 1591497,
5. Method of processing of sulfide raw materials. Preliminary patent. № (19) KZ
(13) А(11) 16457 (51) С22В 1/02. Almaty: 2005.
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