Gasification, dry distillation and carbonization integrated system carbonization
A semi-coke and gas-coal technology, which is applied in the field of coking products, can solve the problems of insufficient raw material sources, amorphous products, and low utilization rate, and achieve considerable economic benefits, low cost, and improved coal utilization rate. Effect
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Embodiment 1
[0024] (1) Heat the non-caking coal under the condition of anaerobic carbonization temperature of 750° C.±50° C. for 3 hours to obtain non-caking coal semi-coke.
[0025] (2) Crushing and screening non-caking coal semi-coke and binder to a particle size of less than 1.5 mm. The binder used has a cohesive index G≥90, ash content≤9%, and sulfur≤0.42% (weight). The binder is selected from at least one of fat coal, coking coal, coal tar pitch, petroleum pitch, and high-temperature coal tar or a mixture of high-temperature coal tar.
[0026] (3) Fully and evenly mix non-caking coal semi-coke, binder and tar according to 55-75% of non-caking coal semi-coke, 15-25% of binder and 10-20% of tar.
[0027] (4) At normal temperature, the pressure is P=30MPa±10MPa.
[0028] (5) Carbonize under the condition of anaerobic high temperature of 1000±50° C., and after 4 hours of carbonization, the product first-grade metallurgical coke is obtained.
Embodiment 2
[0030] Long-flame coal is dry-distilled into semi-coke, crushed according to the proportion of semi-coke 55-75%, binder 15-25%, and tar 10-20%, fully and evenly mixed, pressurized and formed at room temperature, and carbonized into first-grade metallurgical coke. Others are the same as embodiment 1.
Embodiment 3
[0032] The fat coal is dry-distilled into semi-coke, crushed according to the proportion of semi-coke 55-75%, binder 15-25%, and tar 10-20%, fully and evenly mixed, pressurized and formed at room temperature, and carbonized into first-grade metallurgical coke. Others are the same as embodiment 1.
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