This article investigated the hydrodesulfurization of shale oil over NiMo/Al2O3 catalyst in a fixed bed reactor downstream a methanol steam reformer that provides H2-rich gas containing CO2 and steam. Under the optimal conditions of hydrogenation, say, at 380 °C, 4 MPa, a gas/oil volume ratio of 600:1, and an oil hourly space velocity of 4.0 h−1, the sulfur content in the upgraded shale oil varied around 4400 ppm, showing a sulfur removal efficiency above 66 % and the satisfaction of the international standard for marine fuel oil (ISO 8217). The oil exhibited significant improvement on quality, including enhanced calorific value, reduced density and viscosity, increased fraction of light oil, and decreased proportion of heavy oil. Through characterization of catalysts, it was found that steam in H2-rich gas did not significantly affect hydrodesulfurization efficiency. The presence of steam not only promoted hydrocracking of heavy fractions but reduced also carbon deposition on the catalyst during hydro-processing. A 125-h continuous test on stability of performance further corroborated the technical feasibility of the investigated process, establishing essentially a practical pathway to upgrade shale oil by using the as-generated methanol-reformed gas without removal of its containing CO2 and steam as the hydrogen source.
扫码关注我们
求助内容:
应助结果提醒方式:
