Coking process raw materials
A raw material and process technology, which is applied in the field of coal raw materials for the coking process using the existing tamping furnace, can solve the problems of expensive coking process raw materials, low-rank coal cannot be used on a large scale, and low economic benefits in the coking industry, and achieve development and take advantage of significant, easy-to-pull, non-chalking effects
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Embodiment 1
[0025] (1) Pulverize the sub-bituminous coal and mix it with auxiliary agents, and use tamping equipment to carry out tamping and molding of the raw coal, wherein the added quality of the auxiliary agent is 40wt% of the quality of the sub-bituminous coal, and the G value of the sub-bituminous coal is 45. The part content is 65%, and the auxiliary agent is asphaltene with a softening point of 105°C, and the asphaltene loses 45% in dry distillation at 850°C in the absence of air;
[0026] (2) Push the formed raw coal into the coke oven for coking, control the coking temperature to 850°C, and coking time for 16 hours, collect the overflowing mixture of crude gas, tar and crude benzene, and obtain coke as a by-product;
[0027] Adopt conventional process to separate crude gas and tar, and further separate crude benzene from tar, the amount of said crude gas obtained is 650Nm 3 / t dry coal, the amount of the tar is 109kg / t dry coal, the amount of the by-product coke is 390kg / t dry ...
Embodiment 2
[0029] (1) Pulverize the sub-bituminous coal and mix it with auxiliary agents, and use tamping equipment to carry out tamping and molding of the raw coal, wherein the added quality of the auxiliary agent is 35wt% of the quality of the sub-bituminous coal, and the G value of the sub-bituminous coal is 40. The content is 70%, and the additive is asphaltene with a softening point of 115°C, and the asphaltene loses 40% in dry distillation at 850°C in the absence of air;
[0030] (2) Push the formed raw coal into the coke oven for coking, control the coking temperature to 900°C, and coking time for 15.5 hours, collect the overflowing mixture of crude gas, tar and crude benzene, and obtain coke as a by-product;
[0031] Adopt conventional process to separate crude gas and tar, and further separate crude benzene from tar, the amount of said crude gas obtained is 680Nm 3 / t dry coal, the amount of the tar is 117kg / t dry coal, the amount of the by-product coke is 360kg / t dry coal, and ...
Embodiment 3
[0033] (1) Pulverize the sub-bituminous coal and mix it with auxiliary agents, and use tamping equipment to carry out tamping and molding of the raw coal, wherein the added quality of the auxiliary agent is 30wt% of the quality of the sub-bituminous coal, and the G value of the sub-bituminous coal is 35. The part content is 45%, and the auxiliary agent is asphaltene with a softening point of 120°C, and the weight loss of the asphaltene is 42% at 850°C in isolated air dry distillation;
[0034] (2) Push the formed raw coal into the coke oven for coking, control the coking temperature to 950°C, and coking time for 17 hours, collect the overflowing mixture of crude gas, tar and crude benzene, and obtain coke as a by-product;
[0035] Adopt conventional process to separate crude gas and tar, and further separate crude benzene from tar, the amount of said crude gas obtained is 450Nm 3 / t dry coal, the amount of the tar is 45kg / t dry coal, the amount of the by-product coke is 586kg / t...
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