乙烷相平衡线

S. Rykov, I. Kudryavtseva, V. Rykov, M. Nurysheva, B. Kurbanov
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引用次数: 0

摘要

根据修正的克拉珀龙-克劳修斯方程、Rykov弹性线方程和尺度理论,计算了乙烷相在T = T = 90.368 K到T = T = c = 305.322 K温度范围内的相线,其中T T和T c分别为三相点温度和临界温度。弹性线p s = p s (T)、蒸汽ρ - = ρ - (T)、液体ρ + = ρ + (T)方程和饱和线分支具有共同的临界指数和临界参数,饱和线在临界点附近的平均直径f d用模型[2β, 1 - α](杨-杨修正模型)来描述。结果表明,该方程系统能在不确定度范围内传递饱和蒸汽的压力和密度以及乙烷饱和液体的密度的实验数据,均方根误差(RMS):均方根误差(RMS) p = 0.08%;RMS ρ - = 0.67%;RMS ρ + = 0.02%。在温度范围从T T到T c,计算表,包括值p s, ρ -, ρ +和“表观”汽化热。
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Ethane phase equilibrium line
On the basis of the modified Clapeyron–Clausius equation, the Rykov elastic line equation, and scale theory, the line of phase ethane in the temperature range of from T = T t = 90.368 K to T = T c = 305.322 K, where T t and T c are the temperatures of triple point and critical pint, has been calculated. The equations of the elastic line, p s = p s (T), vapor, ρ – = ρ – (T), and liquid, ρ + = ρ + (T), and the branches of the saturation line have common critical exponents and critical parameters, and the average diameter f d of the saturation line in the vicinity of the critical point is described by the model [2β, 1 – α] (The Yang-Yang modified model). It is shown that this system of equations conveys experimental data on the pressure and density of saturated vapor, and the density of a saturated liquid of ethane within the uncertainty of these data with a root-mean-square error (RMS): RMS p s = 0,08 %; RMS ρ – = 0,67 %; RMS ρ + = 0,02 %. In the temperature range of from T t to T c , the tables are calculated, including the values p s , ρ – , ρ + and «apparent» heat of vaporization.
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