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首页> 外文期刊>The Journal of Chemical Thermodynamics >Vapor-liquid equilibrium of the (water + ethanol + glycerol) system: Experimental and modelling data at normal pressure
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Vapor-liquid equilibrium of the (water + ethanol + glycerol) system: Experimental and modelling data at normal pressure

机译:(水+乙醇+甘油)系统的气液平衡:常压下的实验和模型数据

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摘要

In this work, vapor-liquid equilibrium data of the ethanol-water-glycerol system were measured in an Othmer-type ebulliometer at normal pressure. The choice for this system was due to the importance of the ethanol-water separation. The samples analyses were done in a digital densimeter, and the methodology was previously validated with data available in the literature. Since the mean relative deviation was less than 5% in temperature and vapor composition, new data from mixtures of ethanol-water-glycerol were obtained. The experiments showed that glycerol is a promising solvent to ethanol dehydration since it eliminates the azeotrope and promotes the production of anhydrous ethanol. A thermodynamic model for this system was developed using the NRTL model to describe the non-ideality of the liquid phase. The modeling results were compared with experimental data and the deviations were lower than 7%. In this way, the model developed in this work can be used for simulation of ethanol dehydration.
机译:在这项工作中,乙醇-水-甘油系统的气液平衡数据是在Othmer型沸腾仪中在常压下测量的。该系统的选择是由于乙醇-水分离的重要性。样品分析是在数字密度计中完成的,该方法先前已通过文献中的数据进行了验证。由于温度和蒸气组成的平均相对偏差小于5%,因此从乙醇-水-甘油的混合物中获得了新的数据。实验表明,甘油是乙醇脱水的有希望的溶剂,因为它消除了共沸物并促进了无水乙醇的产生。使用NRTL模型开发了该系统的热力学模型,以描述液相的非理想性。将建模结果与实验数据进行比较,偏差低于7%。这样,在这项工作中开发的模型可以用于模拟乙醇脱水。

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