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Supercritical extraction and local composition equation of state.

机译:超临界萃取和局部组成状态方程。

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Extraction equilibria of two liquids (1-methylnaphthalene and m-cresol) separately with two supercritical solvents (carbon dioxide and ethane) were determined in a semi-flow apparatus. For each system, measurements were performed at three temperatures, 308.2, 318.2 and 328.2 K, and pressures from 15 up to 240 bar. The experimental data correlated with the local composition embedded Soave equation of state.; The local composition was determined for mixtures of square-well molecules of various sizes and energies by Monte Carlo simulation. The coordination numbers, internal energy, and pressure were also determined from the simulation. The calculations covered molecular diameter ratios up to two and a wide density range from a dilute gas to dense liquids for various interaction energies.; A model was proposed to express the coordination numbers as a function of molecular diameters, characteristic energies, temperature, and density. From the expression of the coordination numbers, a model equation of state, internal energy, and Helmholtz free energy were obtained for squarewell fluids. Several local composition models were examined with the simulated data, leading to the development of a new density dependent local composition model. The proposed model was found to better describe the simulated results than the other previous models.; The local composition model obtained from computer simulation of molecular fluid mixtures was embedded in the Soave, Patel-Teja, and Cubic Chain-of-Rotators equations of state. Representation of vapor-liquid equilibrium with the embedded equations was investigated at high pressures as well as low pressures for diverse polar mixture systems including aqueous, non-aqueous, hydrogen-bonded, or not hydrogen-bonded. Extensive comparison with data shows that equations of state with local composition mixing rules improve the representation of vapor-liquid equilibria of highly polar or non-ideal mixtures. The local composition embedded Soave equation is able to correlate the new extraction data of this work well.
机译:在半流动装置中确定两种液体(1-甲基萘和间甲酚)分别与两种超临界溶剂(二氧化碳和乙烷)的萃取平衡。对于每个系统,在308.2、318.2和328.2 K的三个温度以及15至240 bar的压力下进行测量。实验数据与嵌入Soave状态方程的局部成分相关。通过蒙特卡洛模拟确定了各种大小和能量的方阱分子混合物的局部组成。配位数,内部能量和压力也由模拟确定。该计算涵盖了分子直径比最高为2的情况,并且具有从稀薄气体到稠密液体的各种相互作用能的宽密度范围。提出了一个模型来表示配位数作为分子直径,特征能量,温度和密度的函数。通过配位数的表达式,获得了方井流体的状态,内部能量和亥姆霍兹自由能的模型方程。使用模拟数据检查了几个局部组成模型,从而导致了新的依赖密度的局部组成模型的开发。发现提出的模型比其他先前模型更好地描述了模拟结果。通过计算机模拟的分子流体混合物获得的局部组成模型被嵌入到Soave,Patel-Teja和三次旋转链状态方程中。在包括水,非水,氢键或不氢键在内的各种极性混合物系统的高压和低压下研究了具有嵌入式方程的气液平衡表示形式。与数据的大量比较表明,具有局部成分混合规则的状态方程可改善高极性或非理想混合物的气液平衡表示。本地组成的嵌入式Soave方程能够很好地关联这项工作的新提取数据。

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