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作 者:马涛 MA Tao(Sinopec(Dalian)Research Institute of Petroleum and Petrochemicals Co.,Ltd.,Dalian Liaoning 116045,China)
机构地区:[1]中石化(大连)石油化工研究院有限公司,辽宁大连116045
出 处:《当代化工》2024年第7期1630-1633,共4页Contemporary Chemical Industry
基 金:中国石化重点科技项目(项目编号:123020)。
摘 要:考察了减压蜡油在加氢裂化条件下,转化深度与产物变化情况,通过精细切割与表征探究烃类分布规律。结果表明:加氢裂化产物中<220℃组分收率随转化率提高而增加,>400℃组分收率随转化率提高逐渐降低。烃类组成变化符合多环芳烃优先进行加氢转化并向轻组分迁移、链烷烃得以保留的规律,明确了加氢裂化产品收率和质量的相互关系。The conversion depth and product changes of Vacuum wax oil under hydrocracking conditions were investigated,and the distribution patterns of hydrocarbons were explored through fine cutting and characterization.The results showed that the yield of <220 ℃ components in hydrocracking products increased with increasing of conversion rate,while the yield of >400 ℃ components gradually decreased with increasing of conversion rate.The change in hydrocarbon composition conformed to the principle that polycyclic aromatics were preferentially hydrogenated and migrated towards light components,while alkanes were retained,clarifying the relationship between the yield and quality of hydrocracking products.
关 键 词:加氢裂化 转化率 芳烃 烃类组成 蒸馏 选择性 色谱
分 类 号:TQ032.41[化学工程] TE624.432[石油与天然气工程—油气加工工程]
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