青岛科技大学化工学院,山东省化工过程模拟与优化工业软件重点实验室,山东 青岛 266042
颜蕾(2000—),女,硕士研究生,18865371400@163.com
王丽丽(1989—),女,博士,副教授,liliw@qust.edu.cn
项曙光(1963—),男,博士,教授,xsg@qust.edu.cn
收稿:2026-02-28,
修回:2026-07-13,
录用:2026-07-15,
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颜蕾, 徐盼, 李国选, 等. 基于多尺度溶剂筛选与多性能评价的共沸物先进分离工艺研究[J/OL]. 化工学报, 2026.
YAN Lei, XU Pan, LI Guoxuan, et al. Advanced separation processes of azeotropes based on multi-scale solvent screening and multi-performance evaluation[J/OL]. CIESC Journal, 2026.
颜蕾, 徐盼, 李国选, 等. 基于多尺度溶剂筛选与多性能评价的共沸物先进分离工艺研究[J/OL]. 化工学报, 2026. DOI: 10.11949/0438-1157.20260272.
YAN Lei, XU Pan, LI Guoxuan, et al. Advanced separation processes of azeotropes based on multi-scale solvent screening and multi-performance evaluation[J/OL]. CIESC Journal, 2026. DOI: 10.11949/0438-1157.20260272.
针对传统单一相对挥发度筛选方法难以揭示萃取剂选择性分子机制及潜在共沸风险的问题,本文采用一种多尺度萃取剂筛选策略,将宏观相对挥发度分析与微观 σ-profile 表面电荷密度分布及分子间相互作用能计算相结合。该方法不仅能够评价萃取剂对汽液平衡行为的调控能力,还可从氢键供受体特征和分子间作用强度角度阐明萃取剂的选择性来源,从而提高萃取剂筛选的可靠性和机理可解释性。研究发现,由于N-甲基甲酰胺(NMF)与组分间存在强相互作用且表现出优异的分离性能,其被确定为分离六甲基二硅氧烷(HMDSO)/1
2-二氯乙烷(DCE)共沸混合物的高效萃取剂。为进一步提高能量利用效率,本文提出并系统优化了热集成萃取精馏工艺。通过权衡经济与环境目标,对塔板数、进料位置、回流比及萃取剂流量等关键工艺参数进行了优化。与无热集成的常规萃取精馏工艺相比,热集成工艺的年度总成本(TAC)降低了1.24%,运行成本降低了1.67%。优化后的热集成流程其TAC为178万美元/年,运行成本为132万美元/年,证明了该工艺在高效、可持续共沸分离方面的潜力。
To address the limitations of conventional screening methods based solely on relative volatility
which are insufficient to reveal the molecular origin of entrainer selectivity and potential azeotrope-formation risks
this study adopts a multiscale entrainer screening strategy that integrates macroscopic relative volatility analysis with microscopic σ-profile surface charge density distributions and intermolecular interaction energy calculations. This approach not only evaluates the ability of an entrainer to regulate vapor-liquid equilibrium behavior
but also elucidates the origin of entrainer selectivity in terms of hydrogen-bond donor/acceptor characteristics and intermolecular interaction strength
thereby improving the reliability and mechanistic interpretability of entrainer screening. N-methylformamide (NMF) was identified as a highly effective entrainer for the separation of the Hexamethyldisiloxane (HMDSO)/1
2-dichloroethane (DCE) azeotropic mixture due to its strong interaction with both components and superior separation performance. To further enhance energy efficiency
a heat-integrated extractive distillation process was proposed and systematically optimized. The key process parameters including the number of trays
feed stage locations
reflux ratio
and entrainer flow rate were optimized by balancing economic and environmental objectives. Compared with the conventional extractive distillation process without heat integration
the heat-integrated process reduced the total annual cost (TAC) by 1.24% and the operating cost by 1.67%. The optimized heat-integrated flowsheet resulted in a TAC of $1.78 million/year and an operating cost of $1.32 million/year
demonstrating its potential for efficient and sustainable azeotropic separation.
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