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首页> 外文期刊>Journal of natural gas science and engineering >Thermodynamic modeling and experimental measurement of semi-clathrate hydrate phase equilibria for CH4 in the presence of cyclohexane (CH) and tetra-n-butyl ammonium bromide (TBAB) mixture
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Thermodynamic modeling and experimental measurement of semi-clathrate hydrate phase equilibria for CH4 in the presence of cyclohexane (CH) and tetra-n-butyl ammonium bromide (TBAB) mixture

机译:在己烷(CH)和四正溴化铵(TBAB)混合物存在下CH4半包合物水合物相平衡的热力学建模与实验测量

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摘要

In the current study, the effect of tetra-n-butyl ammonium bromide (TBAB) and cyclohexane mixture on CH4 semi-clathrate hydrate formation was studied. Semi-clathrate dissociation conditions for CH4 + TBAB + cyclohexane + water were investigated at different concentrations of TBAB (0.05, 0.10, and 0.15) mass fraction in the presence of cyclohexane at the pressure and temperature ranges of 1-8 MPa and 275.1-295 K, respectively. In addition, a thermodynamic model was suggested to predict the phase equilibria of our system, which is divided into four phases, where the van der Waals-Platteeuw Solid Solution Theory has been used to predict the hydrate phase. For gas phase, The SRK equation of state was applied. For oil phase, the cyclohexane activity coefficient in the organic phase was calculated by the non-random two-liquid model (NRTL). Finally, to determine the activity coefficient of the electrolyte species in the aqueous phase, the semi-empirical electrolyte NRTL (eNRTL) activity model was used. The results showed that the proposed model has an acceptable agreement with the experimental semi-clathrate hydrate dissociation data with an approximately average absolute relative deviation of 5.4%.
机译:在目前的研究中,研究了四丁基溴化铵(TBAB)和环己烷混合物对CH4半包合物水合物形成的影响。在压力和温度范围为1-8MPa和275.1-295的环己烷的情况下,在不同浓度的Tbab(0.05,0.10和0.15)质量分数下,在不同浓度的Tbab(0.05,0.10和0.15)质量分数下进行半包合物解离条件k分别。此外,建议热力学模型预测我们的系统的相平衡,分为四个阶段,其中Van der Waals-platteeuw固体解决方案理论已被用于预测水合物相。对于气相,施加了SRK状态的SRK方程。对于油相,通过非随机双液模型(NRT1)计算有机相中的环己烷活性系数。最后,为了确定水相中电解质物种的活性系数,使用半经验电解质NRT1(EnRTL)活性模型。结果表明,该拟议模型具有可接受的一致性与实验半包合物水合物解离数据,其近似平均绝对相对偏差为5.4%。

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