2015
DOI: 10.1186/s40517-015-0030-8
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Extending the persistent primary variable algorithm to simulate non-isothermal two-phase two-component flow with phase change phenomena

Abstract: In high-enthalpy geothermal reservoirs and many other geo-technical applications, coupled non-isothermal multiphase flow is considered to be the underlying governing process that controls the system behavior. Under the high temperature and high pressure environment, the phase change phenomena such as evaporation and condensation have a great impact on the heat distribution, as well as the pattern of fluid flow. In this work, we have extended the persistent primary variable algorithm proposed by (Marchand et al… Show more

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Cited by 8 publications
(8 citation statements)
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References 33 publications
(45 reference statements)
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“…In the above equations, the classical Millington (MILLINGTON, 1959) formulation is used for the effect of tortuosity. Since we also need to consider the non-isothermal effects in this study, the energy balance equation (assuming local thermal equilibrium) for a two-phase system reads (Class and Helmig, 2002;Huang et al, 2015)…”
Section: Global Conservation Equationsmentioning
confidence: 99%
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“…In the above equations, the classical Millington (MILLINGTON, 1959) formulation is used for the effect of tortuosity. Since we also need to consider the non-isothermal effects in this study, the energy balance equation (assuming local thermal equilibrium) for a two-phase system reads (Class and Helmig, 2002;Huang et al, 2015)…”
Section: Global Conservation Equationsmentioning
confidence: 99%
“…The implemented model has been validated against several benchmark problems. Since the heat and mass transfer of the original two-phase two-component model was already validated (Huang et al, 2015;Huang, 2017), only the mass transport portion for the third component (organic contaminant) is validated here. To do this, the experimental data of measured gas phase TCE concentration from McCarthy and Johnson (1993) along with the semianalytical solution given by Atteia and Höhener ( 2010) was compared with model simulation.…”
Section: Constitutive Relationshipsmentioning
confidence: 99%
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“…A number of different numerical methods have been developed to handle the gaseousaqueous phase transitions in multi-phase multi-component porous media models, e.g., primary variable switching (PVS) schemes [47,8], method of negative saturations [41], method of persistent variables [40,26], and non-linear complementary constraints (NCP) approaches P r e p r i n t An all-at-once Newton strategy for methane hydrate reservoir models 3 [36,34,3,5]. In the most widely used gas hydrate reservoir simulators, e.g., TOUGH-Hydrate [38], HYRES-C [29,28], STOMP-HYD [45], HRS [39], etc., the gaseous-aqueous phase transitions are handled using the PVS schemes, where the choice of the primary variables is adapted locally to the phase state.…”
mentioning
confidence: 99%