2016
DOI: 10.1007/s11743-016-1877-9
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Robust Flash Calculation Algorithm for Microemulsion Phase Behavior

Abstract: The HLD‐NAC model was recently modified to match and predict microemulsion phase behavior experimental data for Winsor type III regions. Until now, the HLD‐NAC model could not generate realistic phase behavior for type II− and type II+ two‐phase regions, leading to significant saturation and composition discontinuities when catastrophe theory is applied. These discontinuities lead to significant failures in modeling surfactant applications. We modify the HLD‐NAC equations to ensure consistency over the entire … Show more

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Cited by 34 publications
(28 citation statements)
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“…An analogous description can be made for γ mw . This approach for the critical tie line calculation is consistent with that of Khorsandi and Johns. , The simplest expressions that satisfy the required limits in eq are For the type II– environment, the oil–microemulsion interfacial tension reaches a maximum at the oil–water boundary of the ternary diagram and a minimum at the critical point. That is, Similar observations can be made for the microemulsion–water interfacial tension in the type II+ environment.…”
Section: Methodssupporting
confidence: 71%
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“…An analogous description can be made for γ mw . This approach for the critical tie line calculation is consistent with that of Khorsandi and Johns. , The simplest expressions that satisfy the required limits in eq are For the type II– environment, the oil–microemulsion interfacial tension reaches a maximum at the oil–water boundary of the ternary diagram and a minimum at the critical point. That is, Similar observations can be made for the microemulsion–water interfacial tension in the type II+ environment.…”
Section: Methodssupporting
confidence: 71%
“…The oil–microemulsion and microemulsion–water interfacial tension models for type III are based on the bicritical points at HLD L and HLD U where the tie triangle merges to a two-phase tie line. Therefore, the following conditions must hold: These limits are consistent with the earlier models developed by Ghosh and Johns and Khorsandi and Johns. , Using the model for γ ow in eq and the principal curvature definitions shown in Appendix S1, a simple model that satisfies the conditions in eq is where c c 2 (κ + κ̅) = ( c γ HLD U 2 + γ ow min )/(2HLD U 2 ) from eq . This observation allows for the estimation of oil–microemulsion and microemulsion–water interfacial tensions from oil–water interfacial tensions or vice versa.…”
Section: Methodssupporting
confidence: 60%
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“…The effects of the change of any of the variables directly appearing in the HLD equation (temperature, S, ACN, single surfactant Cp) on the WIII body of a pure component SOW ternary are fairly understood through 2D representations, but not at a higher dimension. The computer simulation models, which are in progress, contain few variables and are often experimentally verified only by changing salinity [30,[256][257][258][259]. Additionally, this is still a too simple approach, not enough to easily deal with a real system containing commercial surfactants, and even surfactant mixtures, crude oil, and reservoir brine.…”
Section: Combination Of Three Single Effects Produced By Three Variabmentioning
confidence: 99%
“…For the type II+ lobe, the data is captured assuming the critical point is located in negative composition space, resulting in a non-vanishing tie-line length as the critical point is approached. This behavior is relevant for systems that exhibit phase separation between a micelle-rich and a micelle-poor phase as the critical point is approached (Kamei et al, 2002;Khorsandi and Johns, 2016).…”
Section: Model Propertiesmentioning
confidence: 99%