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作 者:肖磊[1] 曹睿[2] 王俊[2] 刘艳升[2] 严超宇[2]
机构地区:[1]中国石油大学(北京)数理系,北京市102249 [2]中国石油大学(北京)化学科学与工程学院,北京市102249
出 处:《炼油技术与工程》2009年第12期49-53,共5页Petroleum Refinery Engineering
摘 要:对常压下石油馏分的实沸点蒸馏曲线与平衡汽化曲线以及恩氏蒸馏曲线与平衡汽化曲线的换算图表进行了回归,同时总结了文献中已有的常压下各蒸馏曲线的换算模型,从而建立了一套完整的常压蒸馏曲线换算模型,该模型可用于双向计算。误差分析表明该模型具有可靠的计算精度。选取实测数据对该模型进行验证,结果表明新模型的计算值与实测数据吻合较好,计算准确性优于文献模型。The diagrams of inter-conversion between TBP and EFV curves and those between ASTM and EFV curves for petroleum fractions at atmospheric pressure were regressed. Moreover, the corresponding inter-conversion models for distillation curves at atmospheric pressure in the literatures were also reviewed. Therefore, a set of integrated inter-conversion models among TBP, ASTM and EFV curves were proposed, which can be applied to bidirectional numerical simulation with reliable accuracy approved by error analysis. The resuits show that the model-predicted values agree well with the measured data, and the precision of the models is higher than that of the cited models.
关 键 词:数学模型 实沸点蒸馏 平衡汽化 恩氏蒸馏 常压 石油馏分
分 类 号:TE622.5[石油与天然气工程—油气加工工程]
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