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High-value utilization of H2-containing gas in low-rank oil catalytic hydroupgrading

Author

Listed:
  • Zhang, Mengjuan
  • Guan, Hao
  • Wang, Chao
  • Zheng, Peng
  • Han, Zhennan
  • Wang, Kangjun
  • Zhang, Zhanguo
  • Wang, Jianxi
  • Lu, Yuan
  • Abudula, Abuliti
  • Guan, Guoqing
  • Xu, Guangwen

Abstract

Simulated H2-rich reactant gases containing one or more impurity gases, (CO, CO2, and CH4) were used as the hydrogen source to investigate the performance of Ni-Mo/TiO2-Al2O3 catalyst for the hydrodesulfurization (HDS) of shale oil. The simulated gas (45% H2, 20% CO, 20% CO2, and 15% CH4) was on-line synthesized under the optimal conditions of a reaction temperature of 380 °C, a pressure of 4.0 MPa, a gas/oil (v/v) ratio of 600: 1, and an LHSV of 4.0 h−1. The sulfur content in the upgraded shale oil reached a steady-state value of about 4300 ppm, which met the requirement of national standard marine fuel oil (GB17411–2015, China) that requires <0.5 wt% in sulfur content. Meanwhile, the outlet gas showed a higher heating value than the inlet gas, which had almost no effect on its use as a fuel gas. This work provides a novel idea for the high-value utilization of H2-rich industrial vents and a fresh approach for reducing the costs of hydrogen supply during low-rank oil upgrading.

Suggested Citation

  • Zhang, Mengjuan & Guan, Hao & Wang, Chao & Zheng, Peng & Han, Zhennan & Wang, Kangjun & Zhang, Zhanguo & Wang, Jianxi & Lu, Yuan & Abudula, Abuliti & Guan, Guoqing & Xu, Guangwen, 2024. "High-value utilization of H2-containing gas in low-rank oil catalytic hydroupgrading," Applied Energy, Elsevier, vol. 371(C).
  • Handle: RePEc:eee:appene:v:371:y:2024:i:c:s030626192400970x
    DOI: 10.1016/j.apenergy.2024.123587
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