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首页> 外文期刊>Journal of natural gas science and engineering >Theoretical and experimental study of phase equilibrium of semi-clathrate hydrates of methane plus tetra-n-butyl-ammonium bromide aqueous solution
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Theoretical and experimental study of phase equilibrium of semi-clathrate hydrates of methane plus tetra-n-butyl-ammonium bromide aqueous solution

机译:甲烷与四正丁基溴化铵水溶液的半包合物水合物相平衡的理论和实验研究

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In this study, the phase stability conditions of semi-clathrate hydrate of methane + tetra-n-butyl-ammonium bromide (TBAB) + water system is investigated. New experimental data on the hydrate liquid vapor equilibrium conditions of this system is measured. The measured data is for the pressure range of 2.88-14.1 MPa, temperature range of 285.6-295.9 K and TBAB mass fractions of 0.05, 0.15 and 0.3. A thermodynamic model is also developed to predict the phase stability conditions of hydrate for this system. In the developed model, the phase equilibrium of the hydrate of pure TBAB in water is predicted based on the Gibbs free energy minimization technique. This model is then combined with the statistical thermodynamic model of van der Waals-Platteeuw (vdW-P) to predict the phase stability conditions of semi-clathrate hydrate of methane with TBAB in aqueous solution. Binding mean spherical approximation (BiMSA) electrolyte model is used for aqueous phase properties prediction and modified Peng -Robinson equation of state (PR-EoS) is used for calculation of the gaseous phase properties. The results show that the developed model satisfactorily predicts the experimental data with Average Absolute Relative Deviation (AARD) of 12%. Moreover, the model is able to predict the different types of pure TBAB semi-clathrate hydrates and also the inhibition and promotion effects of this salt. The results also show that considering the association effect in the electrolyte model, can improve the predictions of the developed thermodynamic model for hydrate phase equilibrium of methane in the presence of TBAB aqueous solution. (C) 2015 Elsevier B.V. All rights reserved.
机译:在这项研究中,研究了甲烷+四正丁基溴化铵(TBAB)+水体系的半包合物水合物的相稳定性条件。测量了有关该系统水合物液体蒸气平衡条件的新实验数据。测量的数据适用于压力范围为2.88-14.1 MPa,温度范围为285.6-295.9 K和TBAB质量分数为0.05、0.15和0.3的情况。还开发了一个热力学模型来预测该系统水合物的相稳定性条件。在开发的模型中,基于吉布斯自由能最小化技术预测了纯TBAB在水中的水合物的相平衡。然后将该模型与范德华斯-普拉特乌夫(vdW-P)的统计热力学模型相结合,以预测甲烷与TBAB在水溶液中的半水合物的水合相稳定性条件。结合平均球形近似(BiMSA)电解质模型用于预测水相特性,并使用修正的Peng -Robinson状态方程(PR-EoS)来计算气相特性。结果表明,所开发的模型能够以12%的平均绝对相对偏差(AARD)令人满意地预测实验数据。而且,该模型能够预测不同类型的纯TBAB半包合物水合物,以及该盐的抑制和促进作用。结果还表明,考虑到电解质模型中的缔合效应,可以改善已开发的TBAB水溶液中甲烷水合物相平衡热力学模型的预测。 (C)2015 Elsevier B.V.保留所有权利。

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