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间歇萃取精馏操作过程的实验研究
引用本文:周洋,李文秀. 间歇萃取精馏操作过程的实验研究[J]. 化学工业与工程技术, 2004, 25(6): 32-34
作者姓名:周洋  李文秀
作者单位:沈阳化工学院,化学工程学院,辽宁,沈阳,110142
摘    要:采用复合式精馏塔实现了萃取精馏的间歇操作,塔顶产品物质的量分数达95%以上。以取得合格产品的量与时间之比作为目标函数,研究了回流比R、中间回流量Vm(中间罐向提馏段进料流量)、萃取剂用量S对萃取精馏过程的影响,在R=5~10,Vm=3.2~7.2mL/min,S=1.2~2.2mL/min范围内,随以上操作参数的增大,目标函数均呈先增大后减小的趋势。

关 键 词:间歇精馏  间歇萃取精馏  回流比  中间回流量  萃取剂用量
文章编号:1006-7906(2004)06-0032-03
修稿时间:2004-08-19

Experimental study of batch extractive distillation process
ZHOU Yang,LI Wen-xiu. Experimental study of batch extractive distillation process[J]. Journal of Chemical Industry & Engineering, 2004, 25(6): 32-34
Authors:ZHOU Yang  LI Wen-xiu
Abstract:Complex column is applied in batch extractive distillation, the purity of the top product is over 95%. The ratio of yield to operating time is defined as objective function, in order to provide experimental data for simulation and industrialization. The main factors that influence the batch extractive distillation such as reflux ratio R, the middle reflux quantity V_(m) (the reflux quantity from middle vessel to stripping section), and the solvent quantity S are studied. The experimental results show that when R is 5 ~10, V_(m) is 3.2~7 2 mL/min, S is 1.2~2.2 mL/min, with the increase of the above factors, the objective function increases at first but decreases latter.
Keywords:Batch distillation  Batch extractive distillation  Reflux ratio  Reflux quantity of middle  Solvent quantity
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