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A Combination Process for Improved Hydrotreating and Catalytic Cracking of Hydrocarbon oils

机译:改进的烃油加氢处理和催化裂化组合工艺

摘要

Abstract: the present invention relates to an improved joint treatment with hydrogen and catalytic cracking of hydrocarbon oils, which comprises: contact with oil, residual oil, smashing recycling Catalytic distillation, an oil output to tPA treatment of hydrogen under the conditions of treatment of hydrogen in the presence of hydrogen interaction in turn separate products for the gas, naphtha and pain Hydrogenated diesel oil hydrogenation, and caudal hydrogenated oil; oil in contact with the hydrogenated tail oil are xOptional TPA or plain feed catalytic cracking cracking under conditions of catalytic cracking reaction products in turn separated to obtain hydrogenated Nftha dry gas, liquefied petroleum gas, a broken gas catalysis. Hey, crushed catalytic diesel oil, recycling oil catalytic smashing; where the hydrogenated tail oil are separated and / or normal feedstock oil catalytic cracking at least two parts, the parts are hidden. Selection and heavy or regular heavy feedstock oil catalytic cracking crude oil effective organisational culturalThe average light Dhyt catalytic cracking, prior to contact with the hydrogenated tail oil are and / or normal feedstock oil catalytic cracking cracking TPA. The process according to the present invention is specially suitable for conversion of hydrocarbon oils to produce more products, gasoline and diesel oil. Form (1).
机译:发明内容本发明涉及一种改进的氢与烃类油的催化裂化联合处理,其包括:与油接触,渣油,粉碎回收,催化蒸馏,在氢处理条件下输出到tPA处理氢的油。在存在氢相互作用的情况下,依次分离出用于气体,石脑油和痛的产物。氢化柴油加氢和尾氢化油;与氢化尾油接触的油是任选的TPA或普通进料催化裂化,在催化裂化反应产物的条件下依次分离得到氢化的Nftha干气,液化石油气,破碎气催化。嘿,粉碎催化柴油,回收催化粉碎的机油;如果分离了氢化尾油和/或普通原料油至少有两部分催化裂化,则这些部分是隐藏的。选择重质或常规重质原料油催化裂化原油的有效组织文化平均轻质Dhyt催化裂化,在与氢化尾油接触之前均和/或普通原料油催化裂化TPA。根据本发明的方法特别适合于烃油的转化以生产更多产物汽油和柴油。表格(1)。

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