Mansfield Elisabeth, Bell Ian H, Outcalt Stephanie L
Applied, Chemicals and Materials Division, National Institute of Standards and Technology, Boulder, CO 80305.
J Chem Eng Data. 2016 Jul 14;61(7):2573-2579. doi: 10.1021/acs.jced.6b00258. Epub 2016 Jul 1.
To develop comprehensive models for multicomponent natural gas mixtures, it is necessary to have binary interaction parameters for each of the pairs of constituent fluids that form the mixture. The determination of accurate mixture interaction parameters depends on reliably collected experimental data. In this work, we have carried out an experimental campaign to measure the bubble-point pressures of mixtures of -propane and -decane, a mixture that has been thus far poorly studied with only four existing data sets. The experimental measurements of bubble-point states span a composition range (in -propane mole fraction) from 0.269 to 0.852, and the bubble-point pressures are measured in the temperature range from 270 K to 370 K. These data, in conjunction with data from a previous publication on mixtures of -butane + -octane and -butane + -nonane, are used to determine binary interaction parameters. The newly-obtained binary interaction parameters for the mixture of -propane and -decane represent the experimental bubble-point pressures given here to within 8% (coverage factor, =2), as opposed to previous deviations up to 19%.
为了开发多组分天然气混合物的综合模型,对于构成混合物的每对组成流体,都需要有二元相互作用参数。准确的混合物相互作用参数的确定取决于可靠收集的实验数据。在这项工作中,我们开展了一项实验活动,以测量丙烷和癸烷混合物的泡点压力,到目前为止,该混合物研究较少,仅有四个现有数据集。泡点状态的实验测量涵盖了丙烷摩尔分数从0.269到0.852的组成范围,泡点压力在270 K至370 K的温度范围内测量。这些数据与之前关于丁烷+辛烷和丁烷+壬烷混合物的一篇出版物中的数据一起,用于确定二元相互作用参数。新获得的丙烷和癸烷混合物的二元相互作用参数表示此处给出的实验泡点压力在8%以内(覆盖因子,k = 2),而之前的偏差高达19%。