Method for increasing coal pyrolysis tar yield by return catalytic conversion of pyrolysis gas
A technology for catalytic conversion and tar yield, applied in coke ovens, petroleum industry and other directions, can solve problems such as increased cost and low tar yield, and achieve the effects of improving yield and quality, simple production process and convenient operation
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Embodiment 1
[0016] N 2 Atmosphere pyrolysis
[0017] The 30-60 mesh granular coal sample is in the pyrolysis temperature range of 500°C-650°C, N 2 Pyrolysis at a space velocity of 2400mL / g·h and a residence time of 30min. The tar yields at 500°C, 550°C, 600°C, and 650°C were 4.14%, 4.12%, 4.43%, and 4.55%, respectively. The corresponding yields of n-hexane solubles are 64.26%, 59.32%, 57.13%, 53.63%.
Embodiment 2
[0019] Pyrolysis under pyrolysis atmosphere
[0020] The 30-60 mesh granular coal sample is pyrolyzed at a pyrolysis temperature range of 500°C-650°C, a pyrolysis gas space velocity of 2400mL / g·h, and a residence time of 30min. The tar yields at 500°C, 550°C, 600°C, and 650°C were 4.61%, 5.17%, 5.03%, and 4.46%, respectively. The corresponding yields of n-hexane solubles are 73.96%, 65.35%, 58.45%, 66.44%.
Embodiment 3
[0022] Ni / Al 2 o 3 Catalytic activation of pyrolysis gas pyrolysis
[0023] The selected catalyst is Ni / Al 2 o 3 , and its preparation method is: at 20-40 mesh Al 2 o 3 impregnated with 10-20wt% Ni(NO 3 ) 2 , dried at 110°C for 12h, calcined at 800°C for 4h, and reduced at 600°C for 4h.
[0024] The 30-60 mesh granular coal sample is pyrolyzed at a pyrolysis temperature range of 500°C-650°C, a pyrolysis gas space velocity of 2400mL / g·h, and a residence time of 30min. The tar yields at 500°C, 550°C, 600°C, and 650°C were 3.45%, 5.02%, 4.90%, and 4.57%, respectively. The corresponding yields of n-hexane solubles are: 74.68%, 81.51%, 78.46%, 77.50%.
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