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Hydrate Decomposition Conditions for Liquid Water and Propane
13
Citations
26
References
2017
Year
Chemical KineticsEngineeringChemistryNatural Gas HydrateLiquid HydrateThermodynamic ModellingChemical EngineeringFluid PropertiesMolecular ThermodynamicsThermodynamicsMaterials ScienceHydrogenGas HydrateLiquid WaterPhase Boundary DissociationPhase EquilibriumHydrate PhaseNatural Gas Hydrate SystemChemical Thermodynamics
Because of the industrial importance of C3H8 and because C3H8 hydrate is a reference material for other sII hydrates, the C3H8 hydrate dissociation conditions were independently measured using the phase boundary dissociation and isochoric methods for T = 273.63–278.75 K and p = 0.1887–18.2622 MPa. Along the liquid water Lw–H–C3H8(g) phase boundary, two different purities of 99.5 and 99.999 mol % C3H8 were studied. Data have been used to optimize two semiempirical correlations for rapid calculation of the phase dissociation conditions for p < 20 MPa. For a more rigorous model, the highest purity data have been fit using the van der Waals and Platteuw model and reference quality reduced Helmholtz equations-of-state (EOSs) for the hydrate phase and fluid phases, respectively. The optimized thermodynamic-based model agrees with the experimental data to within the estimated uncertainty of δT = ±0.1 K. The results were also compared to the highly variant literature data for the Lw–H–C3H8(l) phase boundary, where the deviations can be attributed to measurement difficulties when a hydrate is less dense than the liquid hydrate former in the liquid region.
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