# Experimental Study on Oxygen-Enriched Sintering of Vanadium-Titanium Magnetite

Authors: Hao Liu; Yuelin Qin; Xinlong Wu; Bing Xie
Journal: Journal of Chemistry
 (2018)

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## Abstract

The influences of various factors, such as oxygen enrichment time, oxygen enrichment load, and ignition temperature, on the technical indices and sintering performance in the vanadium-titanium magnetite sintering process are simulated using sinter pot experiments. The experiments are based on the field production parameters of a sintering trolley in a steel enterprise in southwest China. Prolonged oxygen enrichment time results in the gradual increase in vertical sintering speed, sintering utilization coefficient, sintered ore yield, sintered ore drum strength, and reductivity. However, the low-temperature reduction pulverability of the sintered ore deteriorates. Oxygen enrichment load increases from 0 m3/h to 2.9 m3/h, and yield increases by 1.1%, while the vertical sintering speed and utilization coefficient increase slightly. Sintered ore drum strength increases from 65.33% to 68.00%, antiwear index decreases to 0.47%, and low-temperature reduction pulverability decreases from 65.07% to 62.85%. The increased ignition temperature is beneficial to improve the drum strength and yield of the ore but reduces the vertical sintering speed and utilization coefficient. With the increase in ignition temperature, the low-temperature reduction pulverability tends to increase first and then decrease. Changes in oxygen time, oxygen enrichment load, and ignition temperature have no significant effects on the soft melting performance of the sintered ore.


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## Body

## 1. Introduction

Vanadium-titanium magnetite is rich in vanadium and titanium. These two elements are important strategic resources mainly for steel, nonferrous metals, and chemical raw material production. The vanadium-titanium magnetite resources in China are mostly distributed in Panzhihua, Sichuan, and Chengde, Hebei. The reserves in Panzhihua account for approximately 618 million tons, which is approximately 95% of the total reserve in China and more than 35% of global reserves. Compared with the sintering of ordinary iron ore, vanadium-titanium magnetite has lower iron, FeO, and SiO2 contents but higher TiO2, MgO, and Al2O3 contents. These characteristics are not favorable for sintering, resulting in low production, low grade, poor strength, low yield, and high solid energy consumption of the sintered ore [1, 2]. Numerous studies have shown that few bonding-phase minerals are generated during the sintering of vanadium-titanium magnetite, but abundant perovskites are found in the sinter. These phenomena lead to the deterioration of the sintered ore strength and decrease in yield. Moreover, the low-temperature reduction pulverability rate of the vanadium-titanium sintered ore RDI−3.15 is significantly higher than that of ordinary sintered ore [3–7].Oxygen-enriched sintering refers to the addition of a certain amount of oxygen in the intake of air during sintering to facilitate the sufficient burning of the sintering fuel and sintering process of the reaction. Using the ignition method of oxygen enrichment can improve the oxygen content in the flue gas and reduce the ignition temperature of the fuel. This process results in the full utilization of the solid fuel on the surface, which is beneficial in accelerating the combustion and heat transfer of the surface material solid in the ignition area. Consequently, the sintering productivity is improved, sintering is intensified, and fuel consumption is reduced [8–10]. Under high oxygen content, most of the liquid-phase reaction and mineral formation process may be completed at temperatures below 1400°C. The concentration of Fe2+ in the liquid phase is low, and the concentration of CO in the exhaust gas is also reduced. When alkalinity >1.2–1.5, a certain amount of calcium ferrite is formed in the solid phase [8]. In addition, the liquid-phase components and crystallization of various minerals are also assimilated in the air according to certain laws. The drawbacks encountered during the sintering of vanadium-titanium magnetite are the lack of strength, low yield, more return mines, and high rate of low-temperature reduction pulverability. These limitations increase the cost of production energy consumption [10]. Oxygen-enriched sintering can effectively improve vertical sintering speed, sintering process, and sintered ore yield.In this study, the effects of different oxygen enrichment times, oxygen enrichment loads, ignition temperatures, and other factors on the industrial production of the vanadium-titanium sintered ore are simulated using sinter pot experiments. Changes in performances, such as sintered ore drum strength, antiwear index, reductivity, low-temperature reduction pulverability index, and soft melting performance, are also studied and analyzed. This study provides a basis for using vanadium-titanium magnetite as a raw material in industrial productions and to obtain high-quality sintered ore with high yield.


## 2. Experimental Materials and Methods

### 2.1. Experimental Materials

All sintered raw materials are obtained from a steel enterprise in southwest China. The main components of iron ore powder, sintered flux, and sintering return mines are listed in Table1. The chemical components of coke are shown in Table 2. The full size distribution of the mix ore powder and coke powder is provided, as shown in Figure 1. The sintering proportion scheme during the experiment is shown in Table 3. The basicity of the sintered ore (R = CaO/SiO2) is set to 2.7 because the sintering characteristics of oxygen-enriched sintering are mainly explored in this study.Table 1
Chemical composition of raw materials.
Raw materials
TFe
SiO2
CaO
Al2O3
MgO
TiO2
S
P
LOI
Mix ore
52.5
5.5
4.9
2.87
2.3
5.9
0.388
0.14
2.5
Dolomite
—
3.0
30.0
—
20.5
—
0.070
—
40.0
Lime
—
2.7
77.0
—
—
—
0.070
—
15.0
Return ore
46.6
5.8
15.0
2.9
2.2
4.9
0.069
0.04
1.20Table 2
Proximate analysis and composition analysis of coke.
Composition
CFix
W
V
A
CaO
MgO
SiO2
Al2O3
Proportion (%)
79.94
7.62
9.49
1.6
0.41
14.3
6.9Figure 1
The full size distribution of the coke powder and mix ore powder.Table 3
Proportion scheme of sintering raw materials (mass fraction, %).
Raw material
Mix ore
Dolomite
Lime
Return ore
Coke
Proportion (%)
56.7
2.1
7.7
30
3.5


### 2.2. Experimental Methods and Devices

The effects of different oxygen enrichment conditions on the sintering performance of vanadium-titanium magnetite are investigated by changing the factors, such as oxygen enrichment time, oxygen enrichment load, and sintering ignition temperature. The influences of these factors on the technical indices and sintered ore quality during sintering are explored. The time and load to enrich the oxygen in the sinter pot experiment are determined by conversion based on 260 m2 of the effective suction area of a sintering trolley and the actual air volumes of the two main exhaust fans (11000 m3/h for each exhaust fan) in a steel enterprise in southwest China.The influence of sintering oxygen enrichment time is evaluated. The sintering trolley limits the oxygen-enriched flow rate to 2000 m3/h, and the converted oxygen-enriched flow rate is 1.93 m3/h on the sinter pot area. The oxygen enrichment in the bellow is changed. The length of the bellow is 2.3 m. The numbers of bellows are 2, 4, 6, 8, and 10. The converted times of the sintering process are approximately 3.2, 6.4, 9.6, 12.8, and 16.0 min.The oxygen enrichment load is based on the three kinds of loads of the sintering trolley, namely, 1000 (low load), 2000 (medium load), and 3000 m3/h (high load). The converted equivalent sinter pot area oxygen enrichment loads are 0.97, 1.93, and 2.90 m3/h, respectively. According to the fixed six-bellow oxygen enrichment system, the converted time of the sintering process in the sinter pot is approximately 9.6 min.In the experiment for sintering oxygen-enriched ignition, increased oxygen enrichment will increase the theoretical sintering ignition temperature. In addition, the ignition fuel used in the laboratory sinter pot experiment is liquefied petroleum gas with a quite different calorific value and composition from those of blast furnace gas used by the sintering trolley. Therefore, the influence of ignition temperature on the sintering process is also studied experimentally.The specific experimental scheme of oxygen-enriched sintering of vanadium-titanium magnetite is shown in Table4.Table 4
Experimental scheme.
Sample
Oxygen-enriched time length (min)
Oxygen-enriched volume (m3·h−1)
Temperature of ignition (°C)
S0
0
0
1100
S1-1
3.2
1.93
1100
S1-2
6.4
1.93
1100
S1-3
9.6
1.93
1100
S1-4
12.8
1.93
1100
S1-5
16
1.93
1100
S2-1
9.6
0.97
1100
S2-2
9.6
1.93
1100
S2-3
9.6
2.90
1100
S3-1
0
0
1000
S3-2
0
0
1050
S3-3
0
0
1100
S3-4
0
0
1150
S3-5
0
0
1200
S3-6
0
0
1250After the raw materials are prepared in accordance with the proportion scheme in Table3, the materials are first artificially mixed evenly on an iron plate. Then, the materials are put into a cylinder mixer (diameter × length of 600 mm × 800 mm) and mixed for a mixed granulation time of 5 min. An appropriate amount of water is sprayed during mixing to wet the mixture, and the final moisture content of the mixture is controlled at 8.0% ± 0.5%. Then, the mixed raw materials are added into the sinter pot of Ø300 mm × 900 mm. The thickness of the control material layer is approximately 600 mm. Approximately 3 kg of the sintered ore is paved at the bottom of the sinter pot as the bottom material before that. The particle size of the sintered ore is 10∼16 mm. The excess oxygen during sintering is provided by an additional oxygen distribution device (Figure 2). This device is equipped with a stainless steel cone-shaped oxygen supply cover and a bottom hole for oxygen. The holes are evenly distributed at an angle of 60°, and the oxygen supply channel is naturally formed. After charging, the exhaust fan is controlled, in which the ignition negative pressure is 8.0 kPa, ignition time is 2 min, and the sinter negative pressure is 14 kPa. After sintering is completed, the technical indices, mechanical performance, and metallurgical performance of the sintered ore are determined. The phase composition of the sintered ore is analyzed by a Zeiss Axioskop 40 polarizing microscope and LEICA Q500 image analyzer.Figure 2
Schematic diagram of the sintering pot device and oxygen enrichment device.The sintered ore drum strength is detected using GB 8209-87. The proportion of the amount in excess of 6.3 mm of the drum sample total mass is considered as the drum strength, and the proportion of the amount that is less than 0.5 mm of the drum sample total mass is the antiwear index. Reductivity is tested by experiments according to GB/T 13241-91. A weight loss method is used to determine the iron ore reductivity. The average of the double specimen is considered, and the absolute value of the range is not more than 5%. The low-temperature reduction pulverability (RDI>3.15) is determined according to the GB/T13242-91 method. After the experiment is completed, the ratio of the mass of the particles with the size greater than 3.15 mm grade and the total mass of the drum sample after reduction is considered as the evaluation standard.No uniform test for determining the softening property is available. This property can be determined using the following parameters: sample size, 10–12.5 mm; stock column height, 40 mm; upper coke, 15 g; lower coke, 20 g; load, 1.0 kg/cm2; and gas flow rate, 15 L/min. The reduction gas composition is CO/N2 = 30/70. The heating rate when it is below 900°C is 10°C/min. However, when it is at 900°C, it is placed under constant temperature for 60 min. When it is above 900°C, the rate is 5°C/min. When it is below 400°C, N2 is injected to protect the test sample. When it is at 400°C, reduction gas is provided. The temperature at which the rate of shrinkage of the stock column is 10% is considered as the start softening temperature (Ta), while that at which the rate of shrinkage is 40% is the softening end temperature (Ts). The softening temperature range is ΔTsa = Ts − Ta, and Tm is the temperature at which the slag iron starts to drip.


## 2.1. Experimental Materials

All sintered raw materials are obtained from a steel enterprise in southwest China. The main components of iron ore powder, sintered flux, and sintering return mines are listed in Table1. The chemical components of coke are shown in Table 2. The full size distribution of the mix ore powder and coke powder is provided, as shown in Figure 1. The sintering proportion scheme during the experiment is shown in Table 3. The basicity of the sintered ore (R = CaO/SiO2) is set to 2.7 because the sintering characteristics of oxygen-enriched sintering are mainly explored in this study.Table 1
Chemical composition of raw materials.
Raw materials
TFe
SiO2
CaO
Al2O3
MgO
TiO2
S
P
LOI
Mix ore
52.5
5.5
4.9
2.87
2.3
5.9
0.388
0.14
2.5
Dolomite
—
3.0
30.0
—
20.5
—
0.070
—
40.0
Lime
—
2.7
77.0
—
—
—
0.070
—
15.0
Return ore
46.6
5.8
15.0
2.9
2.2
4.9
0.069
0.04
1.20Table 2
Proximate analysis and composition analysis of coke.
Composition
CFix
W
V
A
CaO
MgO
SiO2
Al2O3
Proportion (%)
79.94
7.62
9.49
1.6
0.41
14.3
6.9Figure 1
The full size distribution of the coke powder and mix ore powder.Table 3
Proportion scheme of sintering raw materials (mass fraction, %).
Raw material
Mix ore
Dolomite
Lime
Return ore
Coke
Proportion (%)
56.7
2.1
7.7
30
3.5


## 2.2. Experimental Methods and Devices

The effects of different oxygen enrichment conditions on the sintering performance of vanadium-titanium magnetite are investigated by changing the factors, such as oxygen enrichment time, oxygen enrichment load, and sintering ignition temperature. The influences of these factors on the technical indices and sintered ore quality during sintering are explored. The time and load to enrich the oxygen in the sinter pot experiment are determined by conversion based on 260 m2 of the effective suction area of a sintering trolley and the actual air volumes of the two main exhaust fans (11000 m3/h for each exhaust fan) in a steel enterprise in southwest China.The influence of sintering oxygen enrichment time is evaluated. The sintering trolley limits the oxygen-enriched flow rate to 2000 m3/h, and the converted oxygen-enriched flow rate is 1.93 m3/h on the sinter pot area. The oxygen enrichment in the bellow is changed. The length of the bellow is 2.3 m. The numbers of bellows are 2, 4, 6, 8, and 10. The converted times of the sintering process are approximately 3.2, 6.4, 9.6, 12.8, and 16.0 min.The oxygen enrichment load is based on the three kinds of loads of the sintering trolley, namely, 1000 (low load), 2000 (medium load), and 3000 m3/h (high load). The converted equivalent sinter pot area oxygen enrichment loads are 0.97, 1.93, and 2.90 m3/h, respectively. According to the fixed six-bellow oxygen enrichment system, the converted time of the sintering process in the sinter pot is approximately 9.6 min.In the experiment for sintering oxygen-enriched ignition, increased oxygen enrichment will increase the theoretical sintering ignition temperature. In addition, the ignition fuel used in the laboratory sinter pot experiment is liquefied petroleum gas with a quite different calorific value and composition from those of blast furnace gas used by the sintering trolley. Therefore, the influence of ignition temperature on the sintering process is also studied experimentally.The specific experimental scheme of oxygen-enriched sintering of vanadium-titanium magnetite is shown in Table4.Table 4
Experimental scheme.
Sample
Oxygen-enriched time length (min)
Oxygen-enriched volume (m3·h−1)
Temperature of ignition (°C)
S0
0
0
1100
S1-1
3.2
1.93
1100
S1-2
6.4
1.93
1100
S1-3
9.6
1.93
1100
S1-4
12.8
1.93
1100
S1-5
16
1.93
1100
S2-1
9.6
0.97
1100
S2-2
9.6
1.93
1100
S2-3
9.6
2.90
1100
S3-1
0
0
1000
S3-2
0
0
1050
S3-3
0
0
1100
S3-4
0
0
1150
S3-5
0
0
1200
S3-6
0
0
1250After the raw materials are prepared in accordance with the proportion scheme in Table3, the materials are first artificially mixed evenly on an iron plate. Then, the materials are put into a cylinder mixer (diameter × length of 600 mm × 800 mm) and mixed for a mixed granulation time of 5 min. An appropriate amount of water is sprayed during mixing to wet the mixture, and the final moisture content of the mixture is controlled at 8.0% ± 0.5%. Then, the mixed raw materials are added into the sinter pot of Ø300 mm × 900 mm. The thickness of the control material layer is approximately 600 mm. Approximately 3 kg of the sintered ore is paved at the bottom of the sinter pot as the bottom material before that. The particle size of the sintered ore is 10∼16 mm. The excess oxygen during sintering is provided by an additional oxygen distribution device (Figure 2). This device is equipped with a stainless steel cone-shaped oxygen supply cover and a bottom hole for oxygen. The holes are evenly distributed at an angle of 60°, and the oxygen supply channel is naturally formed. After charging, the exhaust fan is controlled, in which the ignition negative pressure is 8.0 kPa, ignition time is 2 min, and the sinter negative pressure is 14 kPa. After sintering is completed, the technical indices, mechanical performance, and metallurgical performance of the sintered ore are determined. The phase composition of the sintered ore is analyzed by a Zeiss Axioskop 40 polarizing microscope and LEICA Q500 image analyzer.Figure 2
Schematic diagram of the sintering pot device and oxygen enrichment device.The sintered ore drum strength is detected using GB 8209-87. The proportion of the amount in excess of 6.3 mm of the drum sample total mass is considered as the drum strength, and the proportion of the amount that is less than 0.5 mm of the drum sample total mass is the antiwear index. Reductivity is tested by experiments according to GB/T 13241-91. A weight loss method is used to determine the iron ore reductivity. The average of the double specimen is considered, and the absolute value of the range is not more than 5%. The low-temperature reduction pulverability (RDI>3.15) is determined according to the GB/T13242-91 method. After the experiment is completed, the ratio of the mass of the particles with the size greater than 3.15 mm grade and the total mass of the drum sample after reduction is considered as the evaluation standard.No uniform test for determining the softening property is available. This property can be determined using the following parameters: sample size, 10–12.5 mm; stock column height, 40 mm; upper coke, 15 g; lower coke, 20 g; load, 1.0 kg/cm2; and gas flow rate, 15 L/min. The reduction gas composition is CO/N2 = 30/70. The heating rate when it is below 900°C is 10°C/min. However, when it is at 900°C, it is placed under constant temperature for 60 min. When it is above 900°C, the rate is 5°C/min. When it is below 400°C, N2 is injected to protect the test sample. When it is at 400°C, reduction gas is provided. The temperature at which the rate of shrinkage of the stock column is 10% is considered as the start softening temperature (Ta), while that at which the rate of shrinkage is 40% is the softening end temperature (Ts). The softening temperature range is ΔTsa = Ts − Ta, and Tm is the temperature at which the slag iron starts to drip.


## 3. Results and Discussion

### 3.1. Effects of Different Oxygen Enrichment Times on the Sintering Performance of Vanadium-Titanium Magnetite

Table5 shows the main technical indices of the sintering of vanadium-titanium magnetite at different oxygen enrichment times. Compared with the absence of oxygen enrichment, the sintered ore drum strength, antiwear properties, and yield improved after oxygen-enriched sintering. This phenomenon is due to the fact that oxygen-enriched sintering increases the oxidizing atmosphere during sintering. Consequently, fuel combustion is more sufficient, resulting in the formation of the sintering liquid phase. Thus, favorable conditions for the production of more high-quality calcium ferrite bonding phases are provided, resulting in the improvement of aforementioned indices. In addition, oxygen-enriched sintering ensures full combustion of fuel to reduce the local reduction, combustion layer temperature, and thickness. This process also reduces the increase in the amount of liquid phases, which is conducive to agglomeration and mineralization of sintered ore powder, and can also improve the strength and yield of the sintered ore.Table 5
Technical indices of the sintering process for different oxygen enrichment times.
Sample
Time (min)
DI (%)
%
Field (%)
SS (mm/min)
Utilization factor of effective area (UFEA) t/(m2·h)
WT (°C)
S0
0
65.33
5.27
82.29
22.57
1.58
463
S1-1
3.2
66.65
4.13
83.74
22.9
1.61
537
S1-2
6.4
65.53
5.03
82.72
23.17
1.64
549
S1-3
9.6
65.39
4.78
83.09
22.98
1.59
487
S1-4
12.8
65.33
4.8
83.66
24.64
1.72
495
S1-5
16
66.67
5.02
82.57
22.8
1.61
467
SS: sintering speed; WT: waste gas temperature.In addition, the vertical sintering rate and sintering utilization coefficient are improved after oxygen-enriched sintering, which are all higher than 22.57 mm/min and 1.58 t/(m2·h). These characteristics are caused by the more sufficient fuel combustion during oxygen-enriched sintering, resulting in increased combustion layer temperature. This process accelerates the solid-phase reaction of the sintered material layer and the vertical sintering speed, such that the sintering utilization coefficient is improved.The main components and FeO content of the sintered ore after different sintering oxygen enrichment times are shown in Table6 and Figure 3. The main components of the sintered ore are slightly changed after oxygen enrichment time, but the FeO content in the finished sintered ore is reduced from 6.50% to 5.95%. These characteristics are caused by the more adequate fuel combustion during oxygen-enriched sintering, which decreases the CO produced by incomplete combustion of coke. Thus, oxygen-enriched sintering reduces the local reduction reaction, resulting in lowered FeO content. In addition, iron ore powder used during sintering is mainly magnetite (Fe3O4). After oxygen-enriched sintering, the oxidizing atmosphere increases during sintering, and some Fe3O4 is oxidized into Fe2O3, further reducing the FeO in the sintered ore.Table 6
Analysis of the composition of the finished sintered ore for different oxygen enrichment times.
Sample
Time (min)
TFe
FeO
SiO2
CaO
MgO
Al2O3
TiO2
R
S0
0
46.99
6.50
6.08
15.66
3.50
3.06
4.59
2.58
S1-1
3.2
46.80
6.36
6.04
15.81
3.49
3.00
4.54
2.62
S1-2
6.4
46.76
6.25
6.12
14.00
3.54
3.09
4.38
2.29
S1-3
9.6
46.87
6.14
5.98
15.22
3.53
3.04
4.53
2.55
S1-4
12.8
46.93
6.14
6.12
15.25
3.50
3.03
4.33
2.49
S1-5
16
46.83
5.95
6.14
15.66
3.51
3.06
4.62
2.55Figure 3
FeO content in the sintered ore for different oxygen enrichment times.Figure4 shows the test results of the sintered ore reductivity and reduction pulverability for different sintering oxygen enrichment times. The reductivity of the sintered ore increases from 78.10% to 80.08%, while the reduction pulverability decreases from 65.07% to 62.86% with the increase in sintering oxygen enrichment time. These results are due to the decreased FeO content in the sintered ore caused by the prolonged sintering oxygen enrichment time. This process will reduce the phase production of perovskite, kirschsteinite, and other minerals with poor reductivity but increase hematite, calcium ferrite, and other minerals with good reductivity, thereby improving the reduction of the sintered ore [11–13]. However, the hematite in the sintered ore undergoes crystal transformation during reduction (Fe2O3-Fe3O4-FeO), leading to great internal stress. This process causes the pulverization of the sintered ore by mechanical force, resulting in poor reduction pulverability of the sintered ore [14, 15]. During sintering, the time of oxygen enrichment is increased, and the hematite produced by reoxidation in the sintered ore increases. Thus, a great amount of hematite undergoes lattice transformation and pulverability during reduction, which reduces the RDI>3.15.Figure 4
Reductivity and reduction pulverability of the sintered ore for different sintering oxygen enriched times.Table7 shows the test results of the softening performance of the sintered ore for different oxygen enrichment times. No remarkable changes are observed in Ta and Ts of the sintered ore with prolonged oxygen enrichment time. However, the softening interval decreases from 51°C to 39°C, and Tm decreases by 33°C.Table 7
Softening performance of the sintered ore for different oxygen enrichment times.
Sample
Time (min)
T
a (°C)
T
s (°C)
ΔTsa (°C)
T
m (°C)
S0
0
1145
1196
51
1388
S1-1
3.2
1155
1199
44
1359
S1-2
6.4
1158
1198
40
1356
S1-3
9.6
1155
1197
42
1360
S1-4
12.8
1150
1199
49
1356
S1-5
16
1153
1192
39
1355


### 3.2. Effects of Different Oxygen Enrichment Loads on the Sintering Performance of Vanadium-Titanium Magnetite

The main technical indices of the vanadium-titanium magnetite sintering process for different oxygen enrichment loads are shown in Table8. With the increase in oxygen enrichment load, the drum strength of the sintered ore increases from 65.33% to 68.00%, antiwear index decreases from 5.27% to 4.80%, and yield increases from 82.29% to 83.39%. These phenomena are due to the enhanced oxidizing atmosphere during sintering caused by the increased oxygen enrichment load. This process results in more sufficient combustion of coke in the sintering mixture, increased temperature of the combustion layer, and increased thickness. Consequently, the sintering liquid phase is formed and increased, and this phase is conducive to the agglomeration and mineralization of the sintered ore, thereby improving the strength and yield of the sintered ore. The vertical sintering rate and utilization coefficient increase first and then decrease with increased oxygen enrichment load. This phenomenon is due to the more complete combustion process caused by oxygen-enriched sintering. Thus, the solid-phase reaction of the sintered material layer and the vertical sintering speed are accelerated, thereby increasing the sintering utilization coefficient. However, the sintering temperature remarkably increases because of the very high oxygen content. This process results in the early formation of the sintering liquid phase, leading to the increase in the volume of the liquid phase. Consequently, the sintered mixture gap becomes jammed, and this condition reduces the vertical sintering speed and sintering utilization coefficient.Table 8
Technical indices of the sintering process with different oxygen enrichment loads.
Sample
Oxygen enriched (m3/h)
DI (%)
AI (%)
Yield (%)
SS (mm/min)
UC (m2·h)
WT (°C)
S0
0
65.33
5.27
82.29
22.57
1.58
463
S2-1
0.97
65.36
5.07
83.09
24.70
1.73
516
S2-2
1.93
66.00
5.03
82.34
22.49
1.59
487
S2-3
2.9
68.00
4.80
83.39
21.90
1.54
466
IT: ignition temperature; DI: drum index; AI: antiwear index; SS: sintering speed; UC: utilization coefficient; WT: waste gas temperature.Table9 shows the main components of the sintered ore with different oxygen enrichment loads. The main component of the sintered ore does not remarkably change with the increase in sintering oxygen enrichment load. However, the FeO content in the sintered ore decreases from 6.50% to 6.14%. The increase in oxygen enrichment load results in the sufficient combustion of coke in the sintered mixture to reduce the local reduction reaction and the amount of FeO produced. Increasing the oxygen enrichment load enhances the oxidizing atmosphere during sintering, and this process can oxidize part of the magnetite into hematite and reduce the FeO content in the sintered ore.Table 9
Composition of the finished sintered ore with different oxygen enrichment loads.
Sample
Oxygen enrichment load (m3/h)
TFe
FeO
SiO2
CaO
MgO
Al2O3
TiO2
R2
S0
0
46.99
6.50
6.08
15.66
3.50
3.06
4.59
2.58
S2-1
0.97
46.88
6.42
6.14
15.20
3.51
3.09
4.55
2.48
S2-2
1.93
46.87
6.24
6.08
15.03
3.54
3.03
4.55
2.47
S2-3
2.9
46.87
6.14
5.98
15.22
3.53
3.04
4.53
2.55Figure5 shows the phase diagram of the finished sintered ore with different oxygen enrichment loads. The main components of the sintered ore are hematite, magnetite, calcium ferrite, calcium silicate, and a small amount of perovskite. Increasing the oxygen-enriched content of the sintered ore results in increased hematite content but decreased magnetite content in the sintered ore, but magnetite content decreases. After oxygen enrichment of the sintered ore, the sintering atmosphere shows a certain degree of oxidability. At the same time, the magnetite content in the sintered ore after the oxygen enrichment is decreased.Figure 5
Phase diagrams of finished sintered ores with different oxygen enrichment loads: (a) 0; (b) 0.97; (c) 1.93; (d) 2.9. H: hematite; M: magnetite; P: perovskite; CF: calcium ferrite; S: calcium silicate.
(a)
(b)
(c)
(d)Figure5 shows the test results of RDI>3.15 of the sintered ore with different oxygen enrichment loads. RDI>3.15 decreases from 65.07% to 62.85% with the increase in sintering oxygen enrichment load (Figure 3). The greater the oxygen enrichment load is, the more obvious the decrease in RDI>3.15 is. Figure 6 shows that the sintering oxygen enrichment load increases, and the hematite content in the sintered ore increases. During reduction, a large amount of hematite changes into the crystal form, resulting in internal stress, and this process deteriorates the sintered ore RDI>3.15.Figure 6
Low-temperature reduction pulverability (RDI>3.15) of the sintered ore with different oxygen enrichment loads.Table10 shows the test results of the softening performance of the sintered ore with different oxygen enrichment loads. Ta and Ts of the sintered ore show no obvious changes as the oxygen enrichment load increases. The softening interval is reduced by 9°C, and Tm has declined.Table 10
Softening performance of the sintered ore with different oxygen enrichment loads.
Sample
Oxygen enrichment load (m3/h)
T
a (°C)
T
s (°C)
ΔTsa (°C)
T
m (°C)
S0
0
1145
1196
51
1388
S2-1
0.97
1150
1193
43
1357
S2-2
1.93
1152
1195
43
1358
S2-3
2.9
1155
1197
42
1360


### 3.3. Effects of Different Ignition Temperatures on the Sintering Performance of Vanadium-Titanium Magnetite

Table11 shows the technical indices in the sinter pot experiment with different ignition temperatures. The sintering drum strength and yield increase with the sintering ignition temperature, but the vertical sintering speed and sintering utilization coefficient gradually decrease. These results may have been caused by the insufficient supply of heat at low ignition temperature. Consequently, the sintered mixture cannot form a good melt such that the sintered raw material cannot be well formed into blocks and results in low strength. At high ignition temperature, the sintering material layer temperature is high and can form more liquid phases to better bond the ore powder. Thus, the strength of the sintered ore is increased. However, the increase in the amount of liquid phase is not conducive to the gas permeability of the sintered material layer, and the sintering rate is lowered, resulting in a decrease in the sintering utilization coefficient.Table 11
Technical indices of the sintering process at different ignition temperatures.
Sample
IT (°C)
DI (%)
AI (%)
Yield (%)
SS (mm/min)
Utilization factor of effective area (UFEA) t/(m2·h)
WT (°C)
S3-1
1000
62.67
4.00
82.31
25.67
1.78
454
S3-2
1050
62.87
3.41
81.70
25.21
1.75
453
S3-3
1100
65.33
5.27
82.29
22.57
1.58
463
S3-4
1150
69.33
3.53
82.20
19.51
1.37
447
S3-5
1200
65.33
3.17
83.69
22.14
1.55
459
S3-6
1250
69.33
4.13
85.00
19.80
1.42
473
IT: ignition temperature; DI: drum index; AI: antiwear index; SS: sintering speed; UC: utilization coefficient; WT: waste gas temperature.Figure7 shows the test results of the reductivity and RDI>3.15 of the finished sintered ore at different ignition temperatures. No evident changes are found in the reduction of the sintered ore with the increase in ignition temperature, but RDI>3.15 increases first and then decreases. When the ignition temperature is 1150°C, the sintering RDI>3.15 reaches the maximum value of 66.29%. This phenomenon may have been caused by the insufficient heat at low ignition temperature, resulting in the nonformation of a good melt from the sintered mixture. The sintered ore has remarkable assimilation degree and low strength. An appropriate increase in ignition temperature is conducive to the formation of the sintered liquid phase, increasing the sintered ore strength. Too high sintering temperature overburns the sintered ore, resulting in a high amount of the vitreous material. Cracking easily occurs during low-temperature reduction, leading to the deterioration of sintered ore RDI>3.15.Figure 7
Sintered ore reductivity and RDI>3.15 at different ignition temperatures.Table12 shows the soft melting performance of the sintered ore at different ignition temperatures. The sintered ore Ta, softening interval, and Tm do not change significantly. Only Ts slightly increases, indicating that the increase in ignition temperature has little effect on sintered ore soft melting performance.Table 12
Sintered ore softening performance in the sintering pot experiment at different ignition temperatures.
Sample
Ignition temperature (°C)
T
a (°C)
T
s (°C)
ΔTsa (°C)
T
m (°C)
S3-1
1000
1148
1189
41
1385
S3-2
1050
1146
1192
46
1380
S3-3
1100
1145
1196
51
1388
S3-4
1150
1150
1193
43
1378
S3-5
1200
1153
1197
44
1379
S3-6
1250
1151
1199
48
1381


## 3.1. Effects of Different Oxygen Enrichment Times on the Sintering Performance of Vanadium-Titanium Magnetite

Table5 shows the main technical indices of the sintering of vanadium-titanium magnetite at different oxygen enrichment times. Compared with the absence of oxygen enrichment, the sintered ore drum strength, antiwear properties, and yield improved after oxygen-enriched sintering. This phenomenon is due to the fact that oxygen-enriched sintering increases the oxidizing atmosphere during sintering. Consequently, fuel combustion is more sufficient, resulting in the formation of the sintering liquid phase. Thus, favorable conditions for the production of more high-quality calcium ferrite bonding phases are provided, resulting in the improvement of aforementioned indices. In addition, oxygen-enriched sintering ensures full combustion of fuel to reduce the local reduction, combustion layer temperature, and thickness. This process also reduces the increase in the amount of liquid phases, which is conducive to agglomeration and mineralization of sintered ore powder, and can also improve the strength and yield of the sintered ore.Table 5
Technical indices of the sintering process for different oxygen enrichment times.
Sample
Time (min)
DI (%)
%
Field (%)
SS (mm/min)
Utilization factor of effective area (UFEA) t/(m2·h)
WT (°C)
S0
0
65.33
5.27
82.29
22.57
1.58
463
S1-1
3.2
66.65
4.13
83.74
22.9
1.61
537
S1-2
6.4
65.53
5.03
82.72
23.17
1.64
549
S1-3
9.6
65.39
4.78
83.09
22.98
1.59
487
S1-4
12.8
65.33
4.8
83.66
24.64
1.72
495
S1-5
16
66.67
5.02
82.57
22.8
1.61
467
SS: sintering speed; WT: waste gas temperature.In addition, the vertical sintering rate and sintering utilization coefficient are improved after oxygen-enriched sintering, which are all higher than 22.57 mm/min and 1.58 t/(m2·h). These characteristics are caused by the more sufficient fuel combustion during oxygen-enriched sintering, resulting in increased combustion layer temperature. This process accelerates the solid-phase reaction of the sintered material layer and the vertical sintering speed, such that the sintering utilization coefficient is improved.The main components and FeO content of the sintered ore after different sintering oxygen enrichment times are shown in Table6 and Figure 3. The main components of the sintered ore are slightly changed after oxygen enrichment time, but the FeO content in the finished sintered ore is reduced from 6.50% to 5.95%. These characteristics are caused by the more adequate fuel combustion during oxygen-enriched sintering, which decreases the CO produced by incomplete combustion of coke. Thus, oxygen-enriched sintering reduces the local reduction reaction, resulting in lowered FeO content. In addition, iron ore powder used during sintering is mainly magnetite (Fe3O4). After oxygen-enriched sintering, the oxidizing atmosphere increases during sintering, and some Fe3O4 is oxidized into Fe2O3, further reducing the FeO in the sintered ore.Table 6
Analysis of the composition of the finished sintered ore for different oxygen enrichment times.
Sample
Time (min)
TFe
FeO
SiO2
CaO
MgO
Al2O3
TiO2
R
S0
0
46.99
6.50
6.08
15.66
3.50
3.06
4.59
2.58
S1-1
3.2
46.80
6.36
6.04
15.81
3.49
3.00
4.54
2.62
S1-2
6.4
46.76
6.25
6.12
14.00
3.54
3.09
4.38
2.29
S1-3
9.6
46.87
6.14
5.98
15.22
3.53
3.04
4.53
2.55
S1-4
12.8
46.93
6.14
6.12
15.25
3.50
3.03
4.33
2.49
S1-5
16
46.83
5.95
6.14
15.66
3.51
3.06
4.62
2.55Figure 3
FeO content in the sintered ore for different oxygen enrichment times.Figure4 shows the test results of the sintered ore reductivity and reduction pulverability for different sintering oxygen enrichment times. The reductivity of the sintered ore increases from 78.10% to 80.08%, while the reduction pulverability decreases from 65.07% to 62.86% with the increase in sintering oxygen enrichment time. These results are due to the decreased FeO content in the sintered ore caused by the prolonged sintering oxygen enrichment time. This process will reduce the phase production of perovskite, kirschsteinite, and other minerals with poor reductivity but increase hematite, calcium ferrite, and other minerals with good reductivity, thereby improving the reduction of the sintered ore [11–13]. However, the hematite in the sintered ore undergoes crystal transformation during reduction (Fe2O3-Fe3O4-FeO), leading to great internal stress. This process causes the pulverization of the sintered ore by mechanical force, resulting in poor reduction pulverability of the sintered ore [14, 15]. During sintering, the time of oxygen enrichment is increased, and the hematite produced by reoxidation in the sintered ore increases. Thus, a great amount of hematite undergoes lattice transformation and pulverability during reduction, which reduces the RDI>3.15.Figure 4
Reductivity and reduction pulverability of the sintered ore for different sintering oxygen enriched times.Table7 shows the test results of the softening performance of the sintered ore for different oxygen enrichment times. No remarkable changes are observed in Ta and Ts of the sintered ore with prolonged oxygen enrichment time. However, the softening interval decreases from 51°C to 39°C, and Tm decreases by 33°C.Table 7
Softening performance of the sintered ore for different oxygen enrichment times.
Sample
Time (min)
T
a (°C)
T
s (°C)
ΔTsa (°C)
T
m (°C)
S0
0
1145
1196
51
1388
S1-1
3.2
1155
1199
44
1359
S1-2
6.4
1158
1198
40
1356
S1-3
9.6
1155
1197
42
1360
S1-4
12.8
1150
1199
49
1356
S1-5
16
1153
1192
39
1355


## 3.2. Effects of Different Oxygen Enrichment Loads on the Sintering Performance of Vanadium-Titanium Magnetite

The main technical indices of the vanadium-titanium magnetite sintering process for different oxygen enrichment loads are shown in Table8. With the increase in oxygen enrichment load, the drum strength of the sintered ore increases from 65.33% to 68.00%, antiwear index decreases from 5.27% to 4.80%, and yield increases from 82.29% to 83.39%. These phenomena are due to the enhanced oxidizing atmosphere during sintering caused by the increased oxygen enrichment load. This process results in more sufficient combustion of coke in the sintering mixture, increased temperature of the combustion layer, and increased thickness. Consequently, the sintering liquid phase is formed and increased, and this phase is conducive to the agglomeration and mineralization of the sintered ore, thereby improving the strength and yield of the sintered ore. The vertical sintering rate and utilization coefficient increase first and then decrease with increased oxygen enrichment load. This phenomenon is due to the more complete combustion process caused by oxygen-enriched sintering. Thus, the solid-phase reaction of the sintered material layer and the vertical sintering speed are accelerated, thereby increasing the sintering utilization coefficient. However, the sintering temperature remarkably increases because of the very high oxygen content. This process results in the early formation of the sintering liquid phase, leading to the increase in the volume of the liquid phase. Consequently, the sintered mixture gap becomes jammed, and this condition reduces the vertical sintering speed and sintering utilization coefficient.Table 8
Technical indices of the sintering process with different oxygen enrichment loads.
Sample
Oxygen enriched (m3/h)
DI (%)
AI (%)
Yield (%)
SS (mm/min)
UC (m2·h)
WT (°C)
S0
0
65.33
5.27
82.29
22.57
1.58
463
S2-1
0.97
65.36
5.07
83.09
24.70
1.73
516
S2-2
1.93
66.00
5.03
82.34
22.49
1.59
487
S2-3
2.9
68.00
4.80
83.39
21.90
1.54
466
IT: ignition temperature; DI: drum index; AI: antiwear index; SS: sintering speed; UC: utilization coefficient; WT: waste gas temperature.Table9 shows the main components of the sintered ore with different oxygen enrichment loads. The main component of the sintered ore does not remarkably change with the increase in sintering oxygen enrichment load. However, the FeO content in the sintered ore decreases from 6.50% to 6.14%. The increase in oxygen enrichment load results in the sufficient combustion of coke in the sintered mixture to reduce the local reduction reaction and the amount of FeO produced. Increasing the oxygen enrichment load enhances the oxidizing atmosphere during sintering, and this process can oxidize part of the magnetite into hematite and reduce the FeO content in the sintered ore.Table 9
Composition of the finished sintered ore with different oxygen enrichment loads.
Sample
Oxygen enrichment load (m3/h)
TFe
FeO
SiO2
CaO
MgO
Al2O3
TiO2
R2
S0
0
46.99
6.50
6.08
15.66
3.50
3.06
4.59
2.58
S2-1
0.97
46.88
6.42
6.14
15.20
3.51
3.09
4.55
2.48
S2-2
1.93
46.87
6.24
6.08
15.03
3.54
3.03
4.55
2.47
S2-3
2.9
46.87
6.14
5.98
15.22
3.53
3.04
4.53
2.55Figure5 shows the phase diagram of the finished sintered ore with different oxygen enrichment loads. The main components of the sintered ore are hematite, magnetite, calcium ferrite, calcium silicate, and a small amount of perovskite. Increasing the oxygen-enriched content of the sintered ore results in increased hematite content but decreased magnetite content in the sintered ore, but magnetite content decreases. After oxygen enrichment of the sintered ore, the sintering atmosphere shows a certain degree of oxidability. At the same time, the magnetite content in the sintered ore after the oxygen enrichment is decreased.Figure 5
Phase diagrams of finished sintered ores with different oxygen enrichment loads: (a) 0; (b) 0.97; (c) 1.93; (d) 2.9. H: hematite; M: magnetite; P: perovskite; CF: calcium ferrite; S: calcium silicate.
(a)
(b)
(c)
(d)Figure5 shows the test results of RDI>3.15 of the sintered ore with different oxygen enrichment loads. RDI>3.15 decreases from 65.07% to 62.85% with the increase in sintering oxygen enrichment load (Figure 3). The greater the oxygen enrichment load is, the more obvious the decrease in RDI>3.15 is. Figure 6 shows that the sintering oxygen enrichment load increases, and the hematite content in the sintered ore increases. During reduction, a large amount of hematite changes into the crystal form, resulting in internal stress, and this process deteriorates the sintered ore RDI>3.15.Figure 6
Low-temperature reduction pulverability (RDI>3.15) of the sintered ore with different oxygen enrichment loads.Table10 shows the test results of the softening performance of the sintered ore with different oxygen enrichment loads. Ta and Ts of the sintered ore show no obvious changes as the oxygen enrichment load increases. The softening interval is reduced by 9°C, and Tm has declined.Table 10
Softening performance of the sintered ore with different oxygen enrichment loads.
Sample
Oxygen enrichment load (m3/h)
T
a (°C)
T
s (°C)
ΔTsa (°C)
T
m (°C)
S0
0
1145
1196
51
1388
S2-1
0.97
1150
1193
43
1357
S2-2
1.93
1152
1195
43
1358
S2-3
2.9
1155
1197
42
1360


## 3.3. Effects of Different Ignition Temperatures on the Sintering Performance of Vanadium-Titanium Magnetite

Table11 shows the technical indices in the sinter pot experiment with different ignition temperatures. The sintering drum strength and yield increase with the sintering ignition temperature, but the vertical sintering speed and sintering utilization coefficient gradually decrease. These results may have been caused by the insufficient supply of heat at low ignition temperature. Consequently, the sintered mixture cannot form a good melt such that the sintered raw material cannot be well formed into blocks and results in low strength. At high ignition temperature, the sintering material layer temperature is high and can form more liquid phases to better bond the ore powder. Thus, the strength of the sintered ore is increased. However, the increase in the amount of liquid phase is not conducive to the gas permeability of the sintered material layer, and the sintering rate is lowered, resulting in a decrease in the sintering utilization coefficient.Table 11
Technical indices of the sintering process at different ignition temperatures.
Sample
IT (°C)
DI (%)
AI (%)
Yield (%)
SS (mm/min)
Utilization factor of effective area (UFEA) t/(m2·h)
WT (°C)
S3-1
1000
62.67
4.00
82.31
25.67
1.78
454
S3-2
1050
62.87
3.41
81.70
25.21
1.75
453
S3-3
1100
65.33
5.27
82.29
22.57
1.58
463
S3-4
1150
69.33
3.53
82.20
19.51
1.37
447
S3-5
1200
65.33
3.17
83.69
22.14
1.55
459
S3-6
1250
69.33
4.13
85.00
19.80
1.42
473
IT: ignition temperature; DI: drum index; AI: antiwear index; SS: sintering speed; UC: utilization coefficient; WT: waste gas temperature.Figure7 shows the test results of the reductivity and RDI>3.15 of the finished sintered ore at different ignition temperatures. No evident changes are found in the reduction of the sintered ore with the increase in ignition temperature, but RDI>3.15 increases first and then decreases. When the ignition temperature is 1150°C, the sintering RDI>3.15 reaches the maximum value of 66.29%. This phenomenon may have been caused by the insufficient heat at low ignition temperature, resulting in the nonformation of a good melt from the sintered mixture. The sintered ore has remarkable assimilation degree and low strength. An appropriate increase in ignition temperature is conducive to the formation of the sintered liquid phase, increasing the sintered ore strength. Too high sintering temperature overburns the sintered ore, resulting in a high amount of the vitreous material. Cracking easily occurs during low-temperature reduction, leading to the deterioration of sintered ore RDI>3.15.Figure 7
Sintered ore reductivity and RDI>3.15 at different ignition temperatures.Table12 shows the soft melting performance of the sintered ore at different ignition temperatures. The sintered ore Ta, softening interval, and Tm do not change significantly. Only Ts slightly increases, indicating that the increase in ignition temperature has little effect on sintered ore soft melting performance.Table 12
Sintered ore softening performance in the sintering pot experiment at different ignition temperatures.
Sample
Ignition temperature (°C)
T
a (°C)
T
s (°C)
ΔTsa (°C)
T
m (°C)
S3-1
1000
1148
1189
41
1385
S3-2
1050
1146
1192
46
1380
S3-3
1100
1145
1196
51
1388
S3-4
1150
1150
1193
43
1378
S3-5
1200
1153
1197
44
1379
S3-6
1250
1151
1199
48
1381


## 4. Conclusion

(1)
The technical indices, such as yield, vertical sintering speed, utilization coefficient, and drum strength, gradually increase with the increase in oxygen enrichment time during sintering. However, the FeO content in the sintered ore is gradually reduced. The increase in oxygen enrichment time is beneficial in improving the reducibility of the sintered ore, but this process will deteriorate the RDI>3.15 of the sintered ore. Prolonging the oxygen enrichment time has no significant effect on the soft melting performance of the sintered ore.
(2)
Increasing the oxygen enrichment load during sintering results in increased drum strength from 68.33% to 68.00%, decreased antiwear index from 5.27% to 4.80%, and increased yield from 82.29% to 83.39%. However, the vertical sintering speed and utilization coefficient are reduced.
(3)
Increasing the oxygen enrichment load during sintering will increase the hematite content but reduce the magnetite content in the sintered ore. This process results in the gradual decrease of the RDI>3.15 of the sintered ore. However, no significant effect on soft melting performance of the sintered ore is found.
(4)
Increasing the ignition temperature is beneficial in improving the strength and yield of the sintered ore. However, too high ignition temperature will reduce the vertical sintering speed and utilization coefficient. The RDI>3.15 of the sintered ore first increases and then decreases when the ignition temperature is increased. No evident changes are observed in the reductivity and soft melting performance.



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*Source: 9342760-2018-11-22.xml*