Calcining method for preparing aluminum-electrolytic pre-baked carbon anode petroleum coke
A technology of prebaked carbon anode and petroleum coke, which is applied in the field of calcination of petroleum coke, which can solve the problems of increased carbon slag, large calcination production capacity, and poor oxidation resistance, and achieves enhanced oxidation resistance and conductivity, and uniform anode quality The effect of stabilization and optimization of calcination process
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Embodiment 1
[0011] The calcining temperature of the rotary kiln is 1330°C, the temperature fluctuation is within 20°C, and the second and third air distribution volumes are respectively 2400m 3 / h and 2000m 3 / h, negative pressure 25Pa, true coke density after calcining 2.07g / cm 3 , resistivity 449.45μΩm, air reaction rate and carbon dioxide reaction rate were 0.28% / min and 18.73% / min.
Embodiment 2
[0013] The calcining temperature of the rotary kiln is 1320°C, the temperature fluctuation is less than 20°C, and the second and third air distribution volumes are respectively 2150m 3 / h and 1850m 3 / h, negative pressure 20Pa, true coke density after calcining 2.06g / cm 3 , resistivity 466.21μΩm, air reaction rate and carbon dioxide reaction rate were 0.28% / min and 20.68% / min.
Embodiment 3
[0015] The calcining temperature of the rotary kiln is 1300°C, the temperature fluctuation is within 30°C, and the second and third air distribution volumes are respectively 2350m 3 / h and 1900m 3 / h, negative pressure 40Pa, true coke density after calcining 2.06g / cm 3 , resistivity 467.88μΩm, air reaction rate and carbon dioxide reaction rate were 0.32% / min and 15.64% / min.
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