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首页> 外文期刊>Fluid Phase Equilibria >Experimental study of the LL, VL and VLL equilibria of water?+ 1-butanol?+ 2-octanol at 101.3?kPa
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Experimental study of the LL, VL and VLL equilibria of water?+ 1-butanol?+ 2-octanol at 101.3?kPa

机译:LL,VL和vll均衡水的实验研究?+ 1-丁醇α+ 2-辛醇101.3?KPA

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Equilibrium data for the water?+ 1-butanol?+ 2-octanol system is determined in this work. Liquid-liquid equilibrium (LLE) data are obtained at 303.15?K and 313.15?K, with a view to investigating the influence of temperature.Vapour-liquid-liquid equilibrium (VLLE) and vapour-liquid equilibrium (VLE) data of the same system are also determined at 101.3?kPa, by means of a modified Fisher Labodest recirculating still that is coupled to an ultrasonic probe. Additionally, the heterogeneous binary azeotrope of the pair water?+ 2-octanol is determined.Correlation parameters are obtained from the experimental results for use in the universal quasichemical (UNIQUAC) and non-random two-liquid (NRTL) thermodynamic models in CHEMCAD 7. The UNIQUAC, NRTL and original universal functional group activity coefficient (UNIFAC) models are then, in turn, used to predict the LLE and VLLE data from these correlation parameters.
机译:水的平衡数据?在这项工作中确定了+ 1-丁醇?+ 2-辛醇系统。 液 - 液平衡(LLE)数据在303.15〜33.15℃下获得,以研究温度的影响。相同的温度。液 - 液 - 液平衡(VLLE)和蒸汽液平衡(VLE)数据的影响 通过改进的Fisher Labodest再循环静止,系统也在101.3 kPa处测定的系统。 另外,确定了一对水的异质二元共沸物α+ 2-辛醇。从ChemCAD 7中的通用正种(Uniquac)和非随机双液(NRTL)热力学模型中使用的实验结果获得了康塞参数。 。然后,uniquac,NRTL和原始通用功能组活动系数(Unifac)模型又用于预测来自这些相关参数的LLE和VLLE数据。

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