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Phase behaviour of water plus nonionic surfactant systems: experiments and modelling applying the Peng-Robinson equation of state with the Wong-Sandler mixing rules and the UNIQUAC g(E)-model

机译:水和非离子表面活性剂系统的相行为:使用Peng-Robinson状态方程,Wong-Sandler混合规则和UNIQUAC g(E)模型进行实验和建模

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In this work, experimental liquid-liquid phase equilibrium data of the systems water+C6E4 and water+C7E4 at pressures up to 100 MPa and in a temperature range between 315 and 355 K are presented. Further, modelling results of several water+nonionic surfactant systems at various pressure are shown. The investigated binary water+surfactant systems contained besides C6E4 and C7E4 the following other surfactants: C4E1, C6E3 , C7E3, and C7E5. As a model, the Peng-Robinson equation of state with the Wong-Sandler mixing rules and the UNIQUAC g(E)-model was used. The model parameters were adjusted to experimental phase equilibrium data at 0.1 MPa. The resulting parameter sets were used for the prediction of the phase behaviour at higher pressures. The fitted model expresses the experimentally found type of phase behaviour quite correctly. However, the pressure influence on the phase behaviour of these systems could only be described qualitatively. (C) 2000 Elsevier Science B.V. All rights reserved. [References: 26]
机译:在这项工作中,提供了水+ C6E4和水+ C7E4在压力高达100 MPa且温度范围为315和355 K之间时的实验液-液相平衡数据。此外,显示了几种水和非离子表面活性剂体系在不同压力下的建模结果。研究的二元水+表面活性剂体系除C6E4和C7E4外还包含以下其他表面活性剂:C4E1,C6E3,C7E3和C7E5。作为模型,使用具有Wong-Sandler混合规则和UNIQUAC g(E)模型的Peng-Robinson状态方程。将模型参数调整为0.1 MPa时的实验相平衡数据。所得参数集用于预测较高压力下的相行为。拟合模型非常正确地表达了实验发现的相行为类型。但是,压力对这些系统的相行为的影响只能定性地描述。 (C)2000 Elsevier Science B.V.保留所有权利。 [参考:26]

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