On the computation of compressible multiphase flows with heat and mass transfer in elastic pipelines

被引:2
|
作者
Zhang C. [1 ,2 ]
Su H. [3 ]
Zhang J. [3 ]
机构
[1] Institute of Applied Physics and Computational Mathematics (IAPCM), Beijing
[2] Lomonosov Moscow State University, Moscow
[3] National Engineering Laboratory for Pipeline Safety/MOE Key Laboratory of Petroleum Engineering/Beijing Key Laboratory of Urban Oil & Gas Distribution Technology, China University of Petroleum
基金
中国国家自然科学基金;
关键词
Approximate Riemann solver; Compressible multiphase flow; Elasticity; Heat exchange; Pump station; Unsteady wall friction;
D O I
10.1016/j.jcp.2023.112257
中图分类号
学科分类号
摘要
The present work is motivated by the engineering need to simulate the multiphase flows in the course of the start-up of a long-distance crude oil pipeline. We propose a model for compressible multiphase flows with heat and mass transfer and diffusion processes in elastic pipelines. The model is derived with two approaches, i.e., (a) the spatial averaging procedure of a single phase model and (b) the Arbitrary Lagrangian Eulerian (ALE) formulation of the Baer-Nunziato model with quasi-1D approximation. The diffusion processes include the viscous dissipation, wall friction, heat conduction, and heat exchange with external environment. In particular, the wall friction consists of steady friction term calculated by Darcy-Weisbach formula, and the unsteady friction determined by the instantaneous-acceleration-based (IAB) model. The unsteady friction modifies the characteristic structure of the hyperbolic part of the model. For the solution of the hyperbolic part, we propose a three-wave approximate Riemann solver incorporating the unsteady friction term. Mass and heat transfer are realized via instantaneous relaxations of the chemical potential and temperature, respectively. Efficient iterative relaxation procedures for N-phase flows have been proposed. We have validated the proposed model and numerical methods against some benchmark multiphase problems and applied the model to calculate the start-up of a realistic liquid pipeline with intermediate pump station boundary condition. © 2023 Elsevier Inc.
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