分离乙腈-乙醇-水三元物系的变压/萃取耦合精馏工艺及系统优化设计

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针对乙腈-乙醇-水物系常压下存在三个二元和一个三元共沸物的特殊情况,设计了节能型变压-萃取精馏四塔流程(PS-ED)和萃取-变压精馏四塔流程(E-PSD)两类工艺,利用Aspen Plus软件进行了以上两种流程模拟,在此基础上以年度总费用(TAC)最低为优化目标对两种工艺分别进行全局优化,并比较两种工艺流程的经济性,结果表明PS-ED流程TAC值比E-PSD节省约6.69%,说明PS-ED流程更具经济性.
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