Method for modifying petroleum coke, modified petroleum coke obtained therefrom, carbonaceous reducing agent and smelting method for industrial silicon
A technology of petroleum coke and modifier, which is applied in the field of carbonaceous reducing agent, smelting of industrial silicon, and modified petroleum coke. It can solve the problems that the reactivity of petroleum coke needs to be improved, so as to protect forest resources and ecological environment and reduce production. The effect of high cost and productivity
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Embodiment 1
[0044] Petroleum coke with a volatile content of 8.9% by weight and an ash content of 0.29% by weight and petroleum pitch with an ash content of 0.06% by weight were heated at 105°C and stirred at 100rpm to make them evenly mixed, wherein the petroleum coke and petroleum The weight ratio of the asphalt was 4:1, and then the mixture was dried at 150° C. for 2 hours and shaped to obtain a modified petroleum coke A with a volatile content of 14.2% by weight and an ash content of 0.25% by weight.
[0045] The reactivity of the unmodified petroleum coke and the obtained modified petroleum coke A were measured respectively, and the results were 60% and 78%, respectively. That is, the petroleum coke is modified by the method of this example, the volatile content of the modified petroleum coke is increased by 5.3% by weight, and the reactivity is increased by 18%, which can better meet the requirements of industrial silicon-carbon reducing agents .
Embodiment 2
[0047] The petroleum coke with a volatile content of 8.9% by weight and an ash content of 0.29% by weight and a catalytic cracking oil slurry with an ash content of 0.24% by weight were heated at 80°C and stirred at 100rpm to make them evenly mixed, wherein the petroleum coke The weight ratio to the catalytic cracking oil slurry was 1:1, and then the mixture was dried at 100°C for 4 hours and shaped to obtain modified petroleum coke B with a volatile content of 14.8% by weight and an ash content of 0.27% by weight.
[0048] The reactivity of the unmodified petroleum coke and the obtained modified petroleum coke B were measured respectively, and the results were 60% and 82%, respectively. That is, the petroleum coke is modified by the method of this example, the volatile content of the modified petroleum coke is increased by 5.9% by weight, and the reactivity is increased by 22%, which can better meet the requirements of industrial silicon-carbon reducing agents .
Embodiment 3
[0050] Heat petroleum coke with a volatile content of 9.1% by weight and an ash content of 0.21% by weight and a modifier with an ash content of 0.12% by weight at 95°C and stir at 100rpm to make them evenly mixed, wherein the modifier It is a mixture of petroleum asphalt and ethylene tar, the weight ratio of petroleum asphalt and ethylene tar is 3:1, and the weight ratio of petroleum coke to modifier is 10:1, and then the mixture is dried at 180°C for 1 hour and shaped to obtain Modified petroleum coke C with a volatile content of 14.5% by weight and an ash content of 0.20% by weight.
[0051] The reactivity of the unmodified petroleum coke and the obtained modified petroleum coke C were measured respectively, and the results were 62% and 84%, respectively. That is, the petroleum coke is modified by the method of this example, the volatile content of the modified petroleum coke is increased by 5.4% by weight, and the reactivity is increased by 22%, which can better meet the r...
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