molecular simulation of fluid phase student(s): bikai jin ......bikai j., hadi n. (2016). phase...

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Molecular Simulation of Fluid Phase Behavior in Shale Systems OBJECTIVE SIGNIFICANCE APPROACH ACHIEVEMENTS In this project, we will use molecular simulation to accurately model the effect of solid-fluid and fluid-fluid interactions in shale, and calculate the confined phase behavior. 1: Liquid-vapor phase coexistence of pure substance; 2: Liquid-vapor phase coexistence of multi-component fluid; 3: Simulation of PVT properties for hydrocarbons in model I (slit pore model) with unique diameters; 4: Repeating above processes in model II (cylindrical pore model) by considering different pore size distributions. 1. Single-component fluid: 2. Two-component fluid: 3. Multi-component fluid: 5. Under confinement: 1) Critical density is increased while critical temperature is reduced for pure fluid; 2) Critical density is increased while C 1 composition is reduced for C 1 /C 2 system; 3) Critical density is increased while C 3 composition is reduced for C 1 /C 3 /nC 5 mixture; 6. A new method is developed for multi-component fluid simulation. 4. Publication Bikai J., Hadi N. (2016). Phase behavior of multi-component hydrocarbon systems in nano-pores using gauge-GCMC molecular simulation, Fluid Phase Equilibria, 425: 324- 334. Student(s): Bikai Jin [email protected] Advisor(s): Hadi Nasrabadi [email protected] Group Web: http://www.hadinasrabadi.com/ ACKNOWLEDGEMENTS All computations are supported by Texas A&M High Performance Research Computing 1. Ada cluster in HPRC is used; 2. Open source code Towhee and GOMC are used in this project; 3. Typical job size: 20 jobs / 20 cores, 22 MB memory 3 hour per million Monte Carlo steps 4. Liquid-vapor phases coexistence in nano pore;

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  • Molecular Simulation of Fluid Phase

    Behavior in Shale Systems

    OBJECTIVE SIGNIFICANCE

    APPROACHACHIEVEMENTS

    In this project, we will use molecularsimulation to accurately model the effectof solid-fluid and fluid-fluid interactionsin shale, and calculate the confinedphase behavior.

    1: Liquid-vapor phase coexistence ofpure substance;

    2: Liquid-vapor phase coexistence ofmulti-component fluid;

    3: Simulation of PVT properties forhydrocarbons in model I (slit poremodel) with unique diameters;

    4: Repeating above processes in modelII (cylindrical pore model) byconsidering different pore sizedistributions.

    1. Single-component fluid:

    2. Two-component fluid:

    3. Multi-component fluid:

    5. Under confinement:

    1) Critical density is increasedwhile critical temperature isreduced for pure fluid;

    2) Critical density is increasedwhile C1 composition is reducedfor C1/C2 system;

    3) Critical density is increasedwhile C3 composition is reducedfor C1/C3/nC5 mixture;

    6. A new method is developed formulti-component fluid simulation.

    4. PublicationBikai J., Hadi N. (2016). Phase behavior of multi-component hydrocarbon systems in

    nano-pores using gauge-GCMC molecular simulation, Fluid Phase Equilibria, 425: 324-334.

    Student(s): Bikai Jin [email protected](s): Hadi Nasrabadi [email protected] Web: http://www.hadinasrabadi.com/

    ACKNOWLEDGEMENTS

    All computations are supported by TexasA&M High Performance ResearchComputing

    1. Ada cluster in HPRC is used;

    2. Open source code Towhee andGOMC are used in this project;

    3. Typical job size:

    20 jobs / 20 cores, 22 MBmemory

    3 hour per million Monte Carlosteps

    4. Liquid-vapor phases coexistencein nano pore;