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作 者:莫昌艺 赵广乐[1] 赵阳[1] 任亮[1] 钱继志 胡志海[1] Mo Changyi;Zhao Guangle;Zhao Yang;Ren Liang;Qian Jizhi;Hu Zhihai(SINOPEC Research Institute of Petroleum Processing,Beijing 100083)
机构地区:[1]中国石化石油化工科学研究院,北京100083
出 处:《石油炼制与化工》2021年第2期7-11,共5页Petroleum Processing and Petrochemicals
基 金:中国石油化工股份有限公司合同项目(115049-3)。
摘 要:为通过调整加氢裂化装置反应条件来控制喷气燃料馏分收率和质量,以中间基蜡油为原料,在双剂串联一次通过流程下考察了裂化反应温度、氢分压、体积空速和氢油比对喷气燃料馏分收率和性质的影响。结果表明:不同反应条件下蜡油原料中大于350℃馏分转化率影响喷气燃料馏分收率,蜡油原料中大于350℃馏分转化率越高,喷气燃料馏分收率越高;不同氢分压下,喷气燃料馏分的芳烃加氢饱和程度影响其烟点,其他反应条件参数对烟点的影响均和蜡油原料的转化深度相关。In order to satisfy the quality demand of jet fuel fraction from hydrocracking unit by adjusting reaction conditions,the effect of reaction parameters of hydrocracking temperature,hydrogen pressure,volume velocity and volume ratio of hydrogen to oil on jet fuel yield and properties were tested using intermediate-base gas oil as feedstocks in single stage once through mode in a hydrocracking device packed with two catalysts in series.The result showed that the jet fuel fraction yield was affected by conversion rate of gas oil under different reaction conditions,the higher the conversion rate of gas oil above 350℃,the higher the jet fuel fraction yield,and that at the same conversion ratio under different hydrogen pressures,the jet fuel fraction smoke point was effected by aromatic saturation extent,while the effects of other reaction conditions on the smoke point were all related to the conversion depth of gas oil feedstock.
分 类 号:TE626.23[石油与天然气工程—油气加工工程]
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