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 - 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 -