A New Homogeneous Non-Equilibrium Model to Compute Vapor-Liquid Two-Phase Critical Pressure Ratios of Multicomponent Hydrocarbon Mixtures. (November 2020)

• Record Type: Journal Article
• Authors: Jia, Wenlong; Ban, Jiuqing; Liang, Fangjian; Cheng, Tingting; He, Yufa; Li, Changjun
• Is Part Of: Journal of loss prevention in the process industries. Volume 68(2020)
• Publication Date: 2020-11
• Subjects: Multi-component gas mixture -- Vapor-liquid two-phase flow -- Critical pressure ratio -- Mathematical model; Chemical industries -- Safety measures -- Periodicals; 660.2804
• DOI: 10.1016/j.jlp.2020.104338
• Languages: English
• ISSNs: 0950-4230

Abstract

Abstract: The critical pressure ratio (ηc ) is an essential parameter for computing the vapor-liquid two-phase critical pressure and mass flow rate of multicomponent hydrocarbon mixtures flowing through valves and leakage orifices. The Homogeneous Non-Equilibrium Diener-Schmidt (HNE-DS) model widely used to calculate ηc assumes that the fluid's volume linearly changes with the pressure (using the Clausius-Clapeyron equation), which is not suitable for multicomponent gas mixtures. In this paper, a new Homogeneous Non-Equilibrium (new-HNE) model is proposed to calculate ηc of gas mixtures. Firstly, a new critical flow compressibility factor (ωc ) is developed from its thermodynamic definition and the Peng-Robinson equation of state (EOS), overcoming the inherent limitations of the Clausius-Clapeyron equation. Then, ηc is correlated to the newly derived ωc by fitting experimental data at various pressures and gas mass fractions of both single-component and multicomponent gas mixtures, yielding the new HNE-DS model. Results show that, for the water-steam and air-water two-phase flow, the average relative deviations (ARD) between the calculated critical pressure ratios and experimental values are equal to 2.8% and 4.93%, respectively, which represents a significant improvement in comparison with the original HNE-DS model. Moreover, this new model is extended to the applications of Liquefied natural gas (LNG)/liquefied petroleum gas (LPG) fluids, and will further contribute to the calculation of the leakage mass flow rate of fluid flowing through the orifices/valves. Highlights: A new model is built to calculate the two-phase critical pressure of mixtures. A new critical compressibility factor correlation is proposed. The new model is validated by experimental data at various conditions. The new model has high accuracy for multicomponent gas mixtures.