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氟苯 + 正辛烷 + 聚苯乙烯混合物的液滴蒸发过程

Droplet Evaporation Process of a Fluorobenzene + n-Octane + Polystyrene Mixture.

作者信息

Wang Wei, Zhou Zhendong, Zhou Bo

机构信息

Jiangsu Key Laboratory of Micro and Nano Heat Fluid Flow Technology and Energy Application, School of Environmental Science and Engineering, Suzhou University of Science and Technology, Suzhou 215009, China.

出版信息

Molecules. 2023 Jul 26;28(15):5659. doi: 10.3390/molecules28155659.

Abstract

The vapor-liquid equilibrium of the fluorobenzene-polystyrene binary polymer solution at 303.15 K was measured using a static pressure device. The vapor-liquid equilibrium of the fluorobenzene-n-octane-polystyrene ternary solution in a partial concentration range under normal pressure was determined using an improved Othmer equilibrium still, in which the octane concentration was low. Three activity coefficient models, poly-NRTL, UNIQUAC, and M-UNIQUAC-LBY, were utilized to correlate the experimental data of binary and ternary solutions, and the component activities of the fluorobenzene-n-octane-polystyrene solution at 303.15 K were predicted. A mathematical model based on the Stefan flow was developed to simulate the evaporation process of composite spherical droplets. The activity predicted by the activity coefficient model was used for numerical simulations, and compared with simulations using the activity following Raoult's law. The comparative analysis revealed that simulations based on Raoult's law and activity coefficient models yielded similar results when the mass fraction of fluorobenzene exceeded 0.6. However, in the later stages of evaporation, the calculations based on Raoult's law predicted a 10% shorter drying time for fluorobenzene. The activity coefficient models provided a better approximation and exhibited similar droplet diameter shrinking behaviors to the actual evaporation process.

摘要

使用静态压力装置测量了303.15 K下氟苯 - 聚苯乙烯二元聚合物溶液的气液平衡。使用改进的奥思默平衡釜测定了常压下部分浓度范围内氟苯 - 正辛烷 - 聚苯乙烯三元溶液的气液平衡,其中正辛烷浓度较低。利用多NRTL、UNIQUAC和M - UNIQUAC - LBY三种活度系数模型关联二元和三元溶液的实验数据,并预测了303.15 K下氟苯 - 正辛烷 - 聚苯乙烯溶液的组分活度。建立了基于斯特凡流的数学模型来模拟复合球形液滴的蒸发过程。将活度系数模型预测的活度用于数值模拟,并与使用拉乌尔定律活度的模拟进行比较。对比分析表明,当氟苯的质量分数超过0.6时,基于拉乌尔定律和活度系数模型的模拟结果相似。然而,在蒸发后期,基于拉乌尔定律的计算预测氟苯的干燥时间短10%。活度系数模型提供了更好的近似,并且与实际蒸发过程表现出相似的液滴直径收缩行为。

https://cdn.ncbi.nlm.nih.gov/pmc/blobs/f525/10420279/43c64f529c2f/molecules-28-05659-g001.jpg

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