A New Process for Azeotropic Mixture Separation by Phase Behavior Tuning Using Pressurized Carbon Dioxide

被引:0
|
作者
Ye, Kongmeng [1 ]
Freund, Hannsjoerg [1 ,2 ]
Sundmacher, Kai [1 ,3 ]
机构
[1] Max Planck Inst Dynam Complex Tech Syst, D-39106 Magdeburg, Germany
[2] Univ Erlangen Nurnberg, D-91058 Erlangen, Germany
[3] Univ Magdeburg, D-39106 Magdeburg, Germany
关键词
LIQUID-EXTRACTION PROCESS; SWING BATCH DISTILLATION; EQUATION-OF-STATE; ACETONITRILE-WATER; HEAT INTEGRATION; EQUILIBRIA; SOLVENT; SYSTEMS; BINARY;
D O I
10.1021/ie4017122
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
A fundamental approach to separate azeotropic mixtures by tuning the phase behavior using pressurized CO2 as a tunable solvent was studied. Following this new process concept, two process variants were put forward to separate aqueous pressure-insensitive and pressure-sensitive azeotropic mixtures. The two process variants were studied in process simulations, and the potential was evaluated by comparison with a conventional pressure-swing distillation process for the acetonitrile water system. The new process shows significant potential to reduce the separation costs by 30.5% up to 68.9% for a broad variety of mixtures with water fractions in the range of 0.1 <= x(H2O) <= 0.9. Thus, these results clearly indicate that the novel fundamental separation approach is a promising alternative to conventional processes for the separation of azeotropic mixtures.
引用
收藏
页码:15154 / 15164
页数:11
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