A prediction model for the yield of coking products
A prediction model and technology of tar yield, applied in the coking industry, can solve problems such as large deviation and inaccurate prediction results, and achieve scientific prediction results
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[0071] The experimental furnace type is 7.63m, the coking time is 25 hours, and the dry basis volatile matter V d is 22.05, the coal caking index G is 78.1, and the active component E is 70.
[0072] In actual production, the yield of tar is 2.56, the yield of crude benzene is 0.70, and the yield of net gas is 309.5.
[0073] Calculate the yield through the chemical product yield prediction model:
[0074] Comparing with Table 1, the influence coefficient of furnace type and coking time on tar oil yield can be obtained from a=c*d
[0075] a=0.85*0.8=0.68
[0076] Comparing with Table 2, from b=0.95*c, the influence coefficient of furnace type on crude benzene yield
[0077] b=0.95*0.85=0.8075
[0078] Calculate tar yield (%): = 0.68*[0.18*V d *(G+0.25*E)+0.8] / 100
[0079] =0.68*[0.18*22.05*(78.1+0.25*70)+0.8] / 100
[0080] =2.58
[0081] Calculate crude benzene yield (%) = 0.8075*[0.043*V d *(G+0.18*E)+0.6] / 100
[0082] =0.8075*[0.043*22.05*(G+0.18*70)+0.6] / 100
[00...
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