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Process for increasing deasphalted oil production from upgraded oil residua

机译:从提质的渣油中增加脱沥青油产量的方法

摘要

A process in fuels production for increasing the yield of deasphalted oil production from upgraded residua and improving deasphalter (42) operability involving mixing the upgraded residua with an aromatics solubilizing aid to prevent the formation of an immiscible third phase during deasphalting. The aromatics solubilizing aid may be selected from a cat-cracker (36) fractionator stream of initial boiling point (IBP) from 260 to 430°C, a heavy cycle gas oil, a heavy coker gas oil and a distilled non-upgraded residuum having an IBP not less than 370°C.
机译:一种用于生产燃料的方法,该方法用于提高来自提质残油的脱沥青油的产量并改善脱沥青剂(42)的可操作性,该方法包括将提质残油与芳烃增溶剂混合以防止脱沥青过程中形成不可混溶的第三相。芳族化合物增溶剂可以选自起始沸点(IBP)为260至430°C的催化裂化器(36)分馏器物流,重循环瓦斯油,重焦化瓦斯油和蒸馏的非升级渣油。 IBP不低于370°C。

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