Modeling of Phase Equilibria in the H2S−H2O System with the Statistical Associating Fluid Theory
- 15 October 2010
- journal article
- research article
- Published by American Chemical Society (ACS) in Energy & Fuels
- Vol. 24 (11), 6208-6213
- https://doi.org/10.1021/ef100847j
Abstract
No abstract availableThis publication has 15 references indexed in Scilit:
- Modeling the phase behavior, excess enthalpies and Henry's constants of the H2O+H2S binary mixture using the SAFT-VR+D approachFluid Phase Equilibria, 2010
- Cubic‐plus‐association equation of state for water‐containing mixtures: Is “cross association” necessary?AIChE Journal, 2009
- Densities of the CO2–H2O and CO2–H2O–NaCl Systems Up to 647 K and 100 MPaEnergy & Fuels, 2008
- Ion-Based Statistical Associating Fluid Theory (SAFT2) to Represent Aqueous Single-Salt Solutions at Temperatures and Pressures up to 473.15 K and 1000 barIndustrial & Engineering Chemistry Research, 2007
- Ion-Based SAFT2 to Represent Aqueous Single- and Multiple-Salt Solutions at 298.15 KIndustrial & Engineering Chemistry Research, 2006
- Statistical Associating Fluid Theory Coupled with Restrictive Primitive Model Extended to Bivalent Ions. SAFT2: 2. Brine/Seawater Properties PredictedThe Journal of Physical Chemistry B, 2006
- Statistical Associating Fluid Theory Coupled with Restrictive Primitive Model Extended to Bivalent Ions. SAFT2: 1. Single Salt + Water SolutionsThe Journal of Physical Chemistry B, 2006
- SAFT1-RPM Approximation Extended to Phase Equilibria and Densities of CO2−H2O and CO2−H2O−NaCl SystemsIndustrial & Engineering Chemistry Research, 2005
- Statistical Associating Fluid Theory Coupled with Restricted Primitive Model to Represent Aqueous Strong Electrolytes: Multiple-Salt SolutionsIndustrial & Engineering Chemistry Research, 2005
- Experimental Measurement and Phase Behavior Modeling of Hydrogen Sulfide−Water Binary SystemIndustrial & Engineering Chemistry Research, 2005