Two-Phase Flow in Pipes: Numerical Improvements and Qualitative Analysis for a Refining Process

Autor: Argimiro Resende Secchi, Evaristo C. Biscaia, Rodrigo G. D. Teixeira
Přispěvatelé: Petrobras [Rio de Janeiro], Instituto Alberto Luiz Coimbra de Pós-Graduação e Pesquisa de Engenharia (COPPE-UFRJ), Universidade Federal do Rio de Janeiro (UFRJ)
Jazyk: angličtina
Rok vydání: 2015
Předmět:
Zdroj: Oil & Gas Science and Technology, Vol 70, Iss 3, Pp 497-510 (2015)
Oil & Gas Science and Technology-Revue d'IFP Energies nouvelles
Oil & Gas Science and Technology-Revue d'IFP Energies nouvelles, Institut Français du Pétrole, 2015, 70 (3), pp.497-510. ⟨10.2516/ogst/2013191⟩
ISSN: 1953-8189
1294-4475
DOI: 10.2516/ogst/2013191⟩
Popis: International audience; Two-phase flow in pipes occurs frequently in refineries, oil and gas production facilities and petrochemical units. The accurate design of such processing plants requires that numerical algorithms be combined with suitable models for predicting expected pressure drops. In performing such calculations, pressure gradients may be obtained from empirical correlations such as Beggs and Brill, and they must be integrated over the total length of the pipe segment, simultaneously with the enthalpy-gradient equation when the temperature profile is unknown. This paper proposes that the set of differential and algebraic equations involved should be solved as a Differential Algebraic Equations (DAE) System, which poses a more CPU-efficient alternative to the “marching algorithm” employed by most related work. Demonstrating the use of specific regularization functions in preventing convergence failure in calculations due to discontinuities inherent to such empirical correlations is also a key feature of this study. The developed numerical techniques are then employed to examine the sensitivity to heat-transfer parameters of the results obtained for a typical refinery two-phase flow design problem.
Databáze: OpenAIRE