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首页> 外文期刊>Chemical Engineering and Processing >Conceptual Design of Distillation-Pervaporation in Single Unit Columns Using Residue Curve Map Methodology
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Conceptual Design of Distillation-Pervaporation in Single Unit Columns Using Residue Curve Map Methodology

机译:使用残留曲线地图方法学单位柱蒸馏 - 蒸发概念设计

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A short-cut design method based on Residue Curve Maps (RCMs) is applied to the conceptual design of Distillation-Pervaporation in a Single Unit (DPSU) columns. Unlike to a conventional hybrid distillation-pervaporation column, in a DPSU system the pervaporation module is located inside the column. The distillation and pervaporation mechanisms are fully coupled, allowing overcoming azeotropic conditions of non-ideal mixtures inside the distillation column. The simplified design method is applied to four non-ideal mixtures with different Serafimov's topological classification: acetone-isopropanol-water (1.0-2), ethyl acetate-ethanol-methanol (2.0-2b), acetone-methyl acetate-methanol (3.1-2) and acetone-methanol-chloroform (3.1-4). The results show that it is possible to achieve a feasible separation through a DPSU column with product compositions split by distillation boundaries. Besides, the regions of a feasible separation with a DPSU column are identified. Thermodynamic limitations for a DPSU column are observed when the azeotropes generate isovolatility lines, producing different separation paths for a specified membrane selectivity. DPSU columns promise to strongly reduce the number of units and associated energy consumption in distillation trains for separating complex mixtures.
机译:基于残留曲线图(RCMS)的短切设计方法应用于单个单元(DPSU)柱中蒸馏蒸发的概念设计。与传统的杂交蒸馏 - 鸟类孔不同,在DPSU系统中,PERVAPORATION模块位于柱内。蒸馏和渗透散热机构完全偶联,允许克服蒸馏塔内的非理想混合物的共沸条件。简化的设计方法应用于四种非理想混合物,具有不同的Serafimov拓扑分类:丙酮 - 异丙醇 - 水(1.0-2),乙酸乙酯 - 乙醇 - 甲醇(2.0-2B),丙酮 - 甲酯 - 甲醇(3.1- 2)和丙酮 - 甲醇 - 氯仿(3.1-4)。结果表明,可以通过通过蒸馏边界分裂的产品组合物来实现可行的分离。此外,鉴定了与DPSU柱的可行分离的区域。当共沸物产生离子溶胀率线时,观察到DPSU柱的热力学限制,产生用于指定膜选择性的不同分离路径。 DPSU列承诺强烈减少蒸馏培训中的单位数和相关能耗,用于分离复杂的混合物。

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