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Intrinsic Kinetic Modeling of Thermal Dimerization of C5 Fraction 被引量:4

Intrinsic Kinetic Modeling of Thermal Dimerization of C_5 Fraction
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摘要 This work aims to investigate the intrinsic kinetics of thermal dimerization of C_5 fraction in the reactive distillation process. Experiments are conducted in an 1000-m L stainless steel autoclave under some selected design conditions. By means of the weighted least squares method, the intrinsic kinetics of thermal dimerization of C_5 fraction is established, and the corresponding pre-exponential factor as well as the activation energy are determined. For example, the pre-exponential factor A is equal to 4.39×105 and the activation energy E4 a is equal to 6.58×10J/mol for the cyclopentadiene dimerization reaction. The comparison between the experimental and calculated results shows that the kinetics model derived in this work is accurate and reliable, which can be used in the design of reactive distillation columns. This work aims to investigate the intrinsic kinetics of thermal dimerization of C5 fraction in the reactive distillation process. Experiments are conducted in an 1000-m L stainless steel autoclave under some selected design conditions. By means of the weighted least squares method, the intrinsic kinetics of thermal dimerization of C5 fraction is established, and the corresponding pre-exponential factor as well as the activation energy are determined. For example, the pre-exponential factor A is equal to 4.39×105 and the activation energy E4 a is equal to 6.58×10J/mol for the cyclopentadiene dimerization reaction. The comparison between the experimental and calculated results shows that the kinetics model derived in this work is accurate and reliable, which can be used in the design of reactive distillation columns.
出处 《China Petroleum Processing & Petrochemical Technology》 SCIE CAS 2016年第1期92-99,共8页 中国炼油与石油化工(英文版)
关键词 steam cracking C5 fraction thermal dimerization intrinsic kinetics 本征动力学模型 二聚反应 C5馏分 动力学建模 加权最小二乘法 反应精馏过程 设计条件 反应精馏塔
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