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Excess Enthalpy and Vapor-Liquid Equilibria with the MHV2 and Soave Mixing Rules

机译:具有MHV2和Soave混合规则的过量焓和汽液平衡

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Calculations and predictions of excess enthalpy (H~E ) and vapor-liquid equilibrium ( VLE) were performed using the Gibbs energy mixing rules MH V2 and a modification of it by Soave. The Soave-Redlich-Kwong equation of state was combined with the UNIQUAC equation. Four sets of parameters estimated in the UNIQUAC model were used for each of seven binary systems: the first estimated from VLE data, the second and the third estimated from H data for two versions of the UNIQUAC equation, and the fourth estimated from both H~E and VLE data simultaneously. It was found that H~E calculations can be performed with the mixing rules; the average relative errors fell from around 200% for the conventional mixing rule to around 60% for MHV2 combined with DECHEMA UNIQUAC parameters and was as little as 20% when the UNIQUAC parameters had been estimated from H~E and VLE data simultaneously. However, the approach suffers from the same shortcomings as far as cross-prediction between H~E and VLE data is concerned, as does the UNIQUAC equation used alone. There is a discrepancy between values obtained with the mixing rule and those obtained with the UNIQUAC equation directly. This discrepancy is smaller for the Soave modification of the mixing rule.
机译:使用吉布斯(Gibbs)能量混合规则MH V2并通过Soave对其进行了修改,对过剩焓(H〜E)和气液平衡(VLE)进行了计算和预测。 Soave-Redlich-Kwong状态方程与UNIQUAC方程组合在一起。在七个二元系统中,分别使用了UNIQUAC模型中估计的四组参数:第一类是从VLE数据估计的,第二种和第三种是从H数据估计的,用于两个版本的UNIQUAC方程,第四组是从两个H〜 E和VLE数据同时。结果发现,可以用混合规则进行H〜E计算。当结合DECHEMA UNIQUAC参数时,平均相对误差从常规混合法则的200%左右下降到MHV2的60%左右,而同时根据H〜E和VLE数据估算UNIQUAC参数时,平均相对误差仅为20%。然而,就H〜E和VLE数据之间的交叉预测而言,该方法也存在相同的缺点,就像单独使用UNIQUAC方程一样。通过混合规则获得的值与直接通过UNIQUAC方程获得的值之间存在差异。对于混合规则的Soave修改,此差异较小。

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