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Diffusion coefficients of carbon dioxide in eight hydrocarbon liquids at temperatures between (298.15 and 423.15) K at pressures up to 69 MPa

机译:八种烃类液体中二氧化碳的扩散系数,温度在(298.15和423.15)K之间,压力高达69 mpa

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摘要

We report experimental measurements of the mutual diffusion coefficients in binary systems comprising CO2 + liquid hydrocarbon measured at temperatures between (298.15 and 423.15) K and at pressures up to 69 MPa. The hydrocarbons studied were the six normal alkanes hexane, heptane, octane, decane, dodecane and hexadecane, one branched alkane, 2,6,10,15,19,23-hexamethyltetracosane (squalane), and methylbenzene (toluene). The measurements were performed by the Taylor dispersion method at effectively infinite dilution of CO2 in the alkane, and the results have a typical standard relative uncertainty of 2.6%. Pressure was found to have a major impact, reducing the diffusion coefficient at a given temperature by up to 55% over the range of pressures investigated. A correlation based on the Stokes–Einstein model was investigated in which the effective hydrodynamic radius of CO2 was approximated by a linear function of the reduced molar volume of the solvent. This represented the data for the normal alkanes only with an average absolute relative deviation (AAD) of 5%. A new universal correlation, based on the rough-hard-sphere theory, was also developed which was able to correlate all the experimental data as a function of reduced molar volume with an AAD of 2.5%.
机译:我们报告了在包括(CO 2 +)液态烃在内的二元系统中,在(298.15和423.15)K之间的温度和高达69 MPa的压力下测量的相互扩散系数的实验测量值。所研究的烃为六种正构烷烃:己烷,庚烷,辛烷,癸烷,十二烷和十六烷,一种支链烷烃,2,6,10,15,19,23-六甲基四cos烷(角鲨烷)和甲基苯(甲苯)。通过泰勒分散法在有效无限量稀释烷烃中的条件下进行测量,结果的典型标准相对不确定度为2.6%。发现压力具有重大影响,在给定温度下,在研究的压力范围内,扩散系数最多降低了55%。研究了基于斯托克斯-爱因斯坦模型的相关性,其中通过减少溶剂的摩尔体积的线性函数来估算CO2的有效流体动力学半径。这仅代表正构烷烃的数据,平均绝对相对偏差(AAD)为5%。还开发了基于粗糙硬球理论的新的通用关联,该关联能够将所有实验数据关联为摩尔体积减少的函数,且AAD为2.5%。

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