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为了探討前报中催化剂活性下降的原因,因此研究了重油加氫裂化的动力学規律。結果表明茂名全餾分頁岩油在本試驗条件下。325℃以上餾分轉化为
In order to investigate the reason why the activity of catalyst in the former report declines, the kinetics of hydrocracking of heavy oil has been studied. The results show that the Maoming whole-cut shale oil in this test conditions. 325 ℃ above distillate into