TY - JOUR
T1 - Reductive Gaseous (H2/NH3) Desulfurization and Gasification of High-Sulfur Petroleum Coke via Reactive Force Field Molecular Dynamics Simulations
AU - Zhong, Qifan
AU - Zhang, Yu
AU - Shabnam, Sharmin
AU - Xiao, Jin
AU - Van Duin, Adri C.T.
AU - Mathews, Jonathan P.
N1 - Funding Information:
This work was financially supported by the National Natural Science Foundation of China (Projects 51904349, 51374253, and 41572144) and the National Key Research and Development Program of China (Project 2017YFC0210402). The Scholarship from the China Scholarship Council (201606370109) is also acknowledged.
Publisher Copyright:
© 2019 American Chemical Society.
PY - 2019/9/19
Y1 - 2019/9/19
N2 - The use of high-sulfur petroleum coke (petcoke) as raw material in the carbon industry requires an effective desulfurization process. Hydrodesulfurization (HDS) and NH3 gaseous desulfurization are the most effective approaches. However, the S/N removal and the gasification ability of HDS and NH3 desulfurization have not been well-explored. Here, petcoke transitions were examined using the reactive force field simulation approach at a constant volume and temperature (3000 K for 250 ps). The S/N removal and transformations in HDS were thiophenic S → C1-4S, H1-2S → H2S, and pyrrolic and pyridinic N → C1-4N → HCN. Given the large H2 production from NH3 decomposition, the S/N removal and transformations in NH3 desulfurization were similar to those of HDS. However, NH compounds (NH3) directly bonded with C atoms in petcoke, adding to the coke yield but adding an additional heteroatom challenge with utilization after NH3 desulfurization. Produced C1-4N (CN, mostly) and H2 were transformed into HxC1-4N (0 < x < 5). The final stable gaseous compounds were HCN and H2S. For NH3 treatment, some NH compounds bonded with C atoms, resulting in an increased N content after NH3 desulfurization (higher coke yield compared to HDS).
AB - The use of high-sulfur petroleum coke (petcoke) as raw material in the carbon industry requires an effective desulfurization process. Hydrodesulfurization (HDS) and NH3 gaseous desulfurization are the most effective approaches. However, the S/N removal and the gasification ability of HDS and NH3 desulfurization have not been well-explored. Here, petcoke transitions were examined using the reactive force field simulation approach at a constant volume and temperature (3000 K for 250 ps). The S/N removal and transformations in HDS were thiophenic S → C1-4S, H1-2S → H2S, and pyrrolic and pyridinic N → C1-4N → HCN. Given the large H2 production from NH3 decomposition, the S/N removal and transformations in NH3 desulfurization were similar to those of HDS. However, NH compounds (NH3) directly bonded with C atoms in petcoke, adding to the coke yield but adding an additional heteroatom challenge with utilization after NH3 desulfurization. Produced C1-4N (CN, mostly) and H2 were transformed into HxC1-4N (0 < x < 5). The final stable gaseous compounds were HCN and H2S. For NH3 treatment, some NH compounds bonded with C atoms, resulting in an increased N content after NH3 desulfurization (higher coke yield compared to HDS).
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U2 - 10.1021/acs.energyfuels.9b01425
DO - 10.1021/acs.energyfuels.9b01425
M3 - Article
AN - SCOPUS:85072654200
SN - 0887-0624
VL - 33
SP - 8065
EP - 8075
JO - Energy and Fuels
JF - Energy and Fuels
IS - 9
ER -