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New process for the conversion of heavy petroleum fractions containing sulphur

机译:含硫重质石油馏分转化的新工艺

摘要

A new process for the conversion of a hydrocarbon fraction having a S content of at least 0.5%, an initial B.Pt of at least 360 deg C. and final B.Pt. of at least 500 deg C., comprises the stages :- a) treatment of the charge, in the presence of H2, in a reactor containing a hydrodesulphurisation catalyst in a fixed bed, in conditions which produce a liquid effluent of reduced S content ; b) treatment of the effluent in a triphasic reactor in the presence of H2 and a hydrotreatment catalyst on a mobile bed, with an ascending flow of liquid and gas.The reactor has an outlet for the withdrawal of catalyst near the base and a catalyst supply point near the top of the reactor ; c) withdrawal of the treated product to a distillation zone from which gaseous, petrol and gasoil fractions are recovered, together with a liquid fraction heavier than gasoil.
机译:用于转化具有至少0.5%的S含量,至少360℃的初始B.Pt和最终的B.Pt的烃馏分的新方法。至少500℃的温度包括以下步骤:-a)在H 2存在下,在含有加氢脱硫催化剂的反应器中,在固定床中,在产生S含量降低的液体流出物的条件下,处理进料; b)在三重反应器中,在H2和加氢处理催化剂存在的情况下,在流动床上以液态和气体的上升流量处理三相反应器中的废水。反应器有一个出口,用于在碱附近抽出催化剂和提供催化剂点在反应堆顶部附近; c)将处理​​过的产物排出蒸馏区,从中回收气态,汽油和粗柴油馏分以及比粗柴油重的液体馏分。

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