TY - JOUR
T1 - Multiphase flow simulation in fractional flow approach with general boundary condition considering phase configuration change in the system
AU - Suk, Heejun
AU - Yeh, Gour Tsyh (George)
N1 - Funding Information:
This research is supported, in part, by Department of Energy's NABIR program under contact No. DE-FG02-98ER62691 with the Pennsylvania State University, and, in part, by U.S. Environmental Protection Agency under grant No. R-82795602 with University of Central Florida.
PY - 2002
Y1 - 2002
N2 - The multiphase flow simulator, MPS, is developed based on the fractional flow approach originated in the petroleum engineering literature considering the fully three phase flow with general boundary condition. The fractional flow approach employs water saturation, total liquid saturation, and total pressure as primary variables. Most existing fractional flow-based models are limited to two-phase flow and specific boundary conditions. Although there appears a number of three-phase flow models, they were mostly developed using pressures based approaches. As a result, these models require cumbersome variable-switch techniques to deal with phase appearance and disappearance. use use of fractional flow-based approaches in MPS makes it unnecessary to use variable switches to handle the change of phase configurations, because the water saturation, total liquid saturation, and total pressure exist throughout the solution domain regardless of whether certain phases are present or not. Also most existing fractional flow-based models consider only specific boundary conditions, which are usually Dirichlet type pressure for water phase, and flux type boundary for NAPL phase or particular combinations for individual phase. The present model considers general boundary conditions of most possible and plausible cases that consist of eight cases. These are the combinations of the phase pressure or phase flux of each of the three individual phases. Thus, the model's capabilities of handling general boundary conditions extend the simulators' usefulness in the field system.
AB - The multiphase flow simulator, MPS, is developed based on the fractional flow approach originated in the petroleum engineering literature considering the fully three phase flow with general boundary condition. The fractional flow approach employs water saturation, total liquid saturation, and total pressure as primary variables. Most existing fractional flow-based models are limited to two-phase flow and specific boundary conditions. Although there appears a number of three-phase flow models, they were mostly developed using pressures based approaches. As a result, these models require cumbersome variable-switch techniques to deal with phase appearance and disappearance. use use of fractional flow-based approaches in MPS makes it unnecessary to use variable switches to handle the change of phase configurations, because the water saturation, total liquid saturation, and total pressure exist throughout the solution domain regardless of whether certain phases are present or not. Also most existing fractional flow-based models consider only specific boundary conditions, which are usually Dirichlet type pressure for water phase, and flux type boundary for NAPL phase or particular combinations for individual phase. The present model considers general boundary conditions of most possible and plausible cases that consist of eight cases. These are the combinations of the phase pressure or phase flux of each of the three individual phases. Thus, the model's capabilities of handling general boundary conditions extend the simulators' usefulness in the field system.
KW - Fractional flow approach
KW - General boundary conditions
KW - Multiple phase flow
KW - Phase configuration change
UR - http://www.scopus.com/inward/record.url?scp=77956686946&partnerID=8YFLogxK
U2 - 10.1016/S0167-5648(02)80070-3
DO - 10.1016/S0167-5648(02)80070-3
M3 - 期刊論文
AN - SCOPUS:77956686946
SN - 0167-5648
VL - 47
SP - 257
EP - 264
JO - Developments in Water Science
JF - Developments in Water Science
IS - C
ER -