TiCl4 preparation process and system
A technology of preparation process and mass ratio, applied in the direction of titanium tetrachloride, titanium halide, etc., can solve problems such as difficulty, increased energy consumption, waste of titanium resources, etc., to improve the recovery rate of titanium, improve comprehensive utilization, and reduce chlorination The effect of energy consumption
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Embodiment 1
[0055] The TiCl of the embodiment 1 of the present invention 4 The preparation process comprises the following steps:
[0056] Agglomeration: Mix vanadium-titanium magnetite concentrate, binder, and water at a mass ratio of 100:1:7.5 to obtain green pellets, which are dried, preheated, and roasted to obtain oxidized pellets. Among them, vanadium-titanium magnetite concentrate The main components and contents of the ore are shown in Table 1;
[0057] Table 1
[0058] TF
Fe 2 o 3
FeO
CaO
MgO
SiO 2
Al 2 o 3
V 2 o 5
TiO 2
MnO
54.55
54.41
21.22
0.56
3.58
3.98
3.26
0.65
10.50
0.51
[0059] Direct reduction: send the oxidized pellets into the shaft furnace for direct reduction, and obtain vanadium-titanium metallized pellets with a metallization rate of 89.65%. Gas effective gas volume ratio (CO+H 2 ) / (CO+H 2 +N 2 +CO 2 +H 2 O) = 0.8;
[0060] Melting: Feed the vanadium-titaniu...
Embodiment 2
[0068] The TiCl of the embodiment 2 of the present invention 4 The preparation process comprises the following steps:
[0069] Agglomeration: Mix vanadium-titanium magnetite concentrate, binder, and water at a mass ratio of 100:2:9 to obtain green pellets. The green pellets are dried, preheated, and roasted to obtain oxidized pellets. Among them, vanadium-titanium magnetite concentrate The main components and contents of ore are shown in Table 3;
[0070] table 3
[0071] TF
Fe2O3
FeO
V2O5
TiO2
MnO
CaO
MgO
SiO2
Al2O3
59.00
56.57
25.00
0.65
12.25
0.51
0.33
1.89
0.98
1.21
[0072]Direct reduction: send the oxidized pellets into the shaft furnace for direct reduction, and obtain vanadium-titanium metallized pellets with a metallization rate of 83.65%. Gas effective gas volume ratio (CO+H 2 ) / (CO+H 2 +N 2 +CO 2 +H 2 O) = 0.9;
[0073] Melting: Feed the vanadium-titanium metallized pellets a...
Embodiment 3
[0081] The TiCl of the embodiment 3 of the present invention 4 The preparation process comprises the following steps:
[0082] Agglomeration: Mix vanadium-titanium magnetite concentrate, binder, and water at a mass ratio of 100:2:9 to obtain green pellets, which are dried, preheated, and roasted to obtain oxidized pellets.
[0083] Direct reduction: send the oxidized pellets into the shaft furnace for direct reduction, and obtain vanadium-titanium metallized pellets with a metallization rate of 83.65%. Gas effective gas volume ratio (CO+H 2 ) / (CO+H 2 +N 2 +CO 2 +H 2 O) = 0.9;
[0084] Melting: Feed the vanadium-titanium metallized pellets and semi-coke into the melting furnace at a mass ratio of 100:5. The charge is heated to 1700°C in the melting furnace and kept at a constant temperature for 45 minutes to complete the separation of slag and iron to obtain titanium-containing slag.
[0085] Chlorination: The titanium slag after separation of slag and iron is crushed an...
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Abstract
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