用分隔壁精馏塔分离松节油中蒎烯的模拟  被引量:5

Simulation of dividing wall column for separating pinene from turpentine

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作  者:郭志强[1] 阮奇[1] 丁珌[2] 李峰 

机构地区:[1]福州大学化学化工学院,福建福州350108 [2]福建省林业科学研究院,福建福州350012 [3]中石化森美(福建)石油有限公司,福建福州350003

出  处:《计算机与应用化学》2012年第6期687-691,共5页Computers and Applied Chemistry

基  金:福建省林业厅科研项目“共沸精馏隔壁塔高效分离松节油中的蒎烯”(闽林科[2011]3号)

摘  要:提出采用分隔壁精馏塔代替常规精馏塔序列分离松节油以得到α-蒎烯和β-蒎烯的新工艺。为了选择适合松节油体系的分隔壁塔结构,采用Aspen软件分别模拟计算了DWC、DWC-SS和DWC-SR三种塔型,结果表明,与常规工艺相比DWC塔可节能26%,DWC-SS塔可节能16.6%,DWC-SR塔可节能12.5%。在此基础上考察了DWC塔进料位置、回流比、隔板位置、气液相分配比和中间产品出料位置对分离效果和热负荷的影响,得出气液相分配比是影响分隔壁塔操作稳定性的主要因素。A novel process was proposed for the separation of α-pinene and β-pinene from turpentine, in which a dividing wall column was adopted instead of the conventional distillation column. To choose the structure suitable for turpentine mixture, three types of divided wall distillation columns were simulated with the software of Aspen plus. Results shows that, compared with the conventional distillation process, DWC could save energy 26.0%, DWC-SS could save energy 16.6%, DWC-SR could save energy 12.5%. And the effect of feed stage, reflux ratio, interconnection stage, side product stage, and distribution ratio of vapor and liquid on the separation efficiency and reboil duty were investigated especially through sensitive analysis, then the main parameter of the column was determined.

关 键 词:分隔壁塔 精馏 松节油 模拟 节能 

分 类 号:TQ018[化学工程] TQ02

 

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