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Vapour-liquid-liquid and vapour-liquid equilibrium of the system water plus ethanol plus heptane at 101.3 kPa

机译:系统水+乙醇+庚烷在101.3 kPa时的汽-液-液和汽-液平衡

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Consistent vapour-liquid (VLE) and vapour-liquid-liquid (VLLE) data for the ternary system water (1) + ethanol (2) + n-heptane (3) are reported at 101.3 kPa at temperatures in the range of 341-352 K. An all-glass, dynamic recirculating still equipped with an ultrasonic homogenizer has been used in the determination of the VLLE. The experimental data indicates that a ternary heterogeneous azeotrope is present at 341.83 K with a composition of 0.205, 0.432, and 0.363 mole fractions of water, ethanol, and heptane, respectively. The experimental results have been used to test the accuracy of the UNIFAC, UNIQUAC, and NRTL models in the calculation and prediction of the equilibrium data. None of these methods properly correlate and approximate the top zone of the non-isothermal solubility curve, which is important for the simulation of the azeotropic distillation. (c) 2006 Elsevier B.V. All rights reserved.
机译:三元水(1)+乙醇(2)+正庚烷(3)的三态系统水蒸气液(VLE)和蒸气液液(VLLE)的数据在101.3 kPa和341- 352K。全玻璃动态循环仍然配备了超声波均质器,用于测定VLLE。实验数据表明,三元均相共沸物存在于341.83 K,分别具有0.205、0.432和0.363摩尔分数的水,乙醇和庚烷。实验结果已用于测试UNIFAC,UNIQUAC和NRTL模型在平衡数据的计算和预测中的准确性。这些方法均未正确关联和逼近非等温溶解度曲线的顶部区域,这对于模拟共沸蒸馏非常重要。 (c)2006 Elsevier B.V.保留所有权利。

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