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Generalized binary interaction parameters for hydrogen-heavy-n-alkane systems using Peng-Robinson equation of state

机译:鹏 - 罗宾逊方程的氢重-N-烷烃系统的广义二元相互作用参数

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摘要

The Peng-Robinson equation of state (PR EOS) is used to model the vapor-liquid equilibria (VLE) of binary systems of hydrogen with five heavy-n-alkanes: n-decane (n-C10H22), n-hexadecane (n-C16H34), n-octacosane (n-C28H58), n-hexatriacontane (n-C36H74), and n-hexatetracontane (n-C46H94). Using literature experimental data for these systems, binary interaction parameters (BIPs) were calculated using the PR EOS coupled with three different alpha () functions (Soave, Twu, and Gasem). The calculated BIPs have been fitted to a generalized correlation that can be used to estimate the BIPs and model the VLE within the temperature range of 283.2-449.6K, pressure range of 1.151-15.970MPa, and hydrogen solubility range of 0.016-0.257mole fraction. It is found that PR EOS combined with one specific form of function is capable of reproducing the experimental VLE data with an overall %AARD of 1.1%.
机译:状态(Pr EOS)的彭罗宾逊方程用于模拟氢气液体平衡(VLE)的氢气液体升温(VLE)用五种重N-烷烃:N-癸烷(N-C10H22),N-十六烷(n -C16H34),N-八氰烷(N-C28H58),N-六磷酸乙烷(N-C36H74)和N-六己二酮(N-C46H94)。 使用这些系统的文献实验数据,使用与三种不同的alpha()函数(Soave,Twu和Gasem)耦合的PR EOS计算二进制交互参数(BIP)。 计算出的横梁已经安装在广义相关的广义相关性,该横穿相关性可用于估计在283.2-449.6k的温度范围内,压力范围为1.151-15.970MPa的横梁和型号,以及0.016-0.257摩尔分数的氢溶解度范围内 。 发现Pr EOS与一种特定形式的功能相结合,能够以1.1%的总%AARD再现实验VLE数据。

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