255130 Thermodynamic Model for Phase Boundary of Gas Hydrates with and without Additives

Wednesday, October 31, 2012: 12:30 PM
412 (Convention Center )
Min-Kang Hsieh1, Yen-Ting Yeh1, Wan-Yi Ting1, Po-Chun Chen2, Yan-Ping Chen1, Shiang-Tai Lin1 and Li-Jen Chen1, (1)Department of Chemical Engineering, National Taiwan University, Taipei, Taiwan, (2)Central Geological Survey, P. O. Box 968, New Taipei City, Taiwan

In this work, we propose a new Langmuir adsorption constant for the modeling of the phase boundary of clathrate hydrates over a wide range of conditions. The proposed pressure- and temperature- dependent Langmuir adsorption constant is designed to produce a reduced free volume available to the encapsulated gas molecules as the pressure increases. The Peng-Robinson-Stryjek-Vera (PRSV) equation of state, combined with the COSMO-SAC activity coefficient liquid model through the modified Huron–Vidal (MHV1) mixing rule and with this new Langmuir model  can be used to describe various types of three phase coexisting conditions of gas hydrates, from vapor-ice-hydrate equilibrium (VIHE) at low temperatures, to vapor-liquid-hydrate equilibrium (VLHE) at higher temperatures, and to liquid-liquid-hydrate equilibrium (LLHE) at high pressures, using a single set of parameters. The average relative deviations in the equilibrium pressure are found to be 4.57 % for 12 pure gas hydrates over a large range of temperatures (148.8 K to 323.9 K) and pressures (5.35x102 Pa to 8.27x108 Pa). Furthermore, the retrograde behavior observed in CH4, CO2, C3H8, and i-C4H10pure gas hydrate systems can all be successfully modeled by the change of free volume at high pressures.

By using this method, the prediction of phase boundary change in gas hydrates with the addition of organic inhibitors and electrolytes is achieved. We examined the accuracy of this method using 5 organic inhibitors and 9 electrolytes, and over a range of temperature (259.0 K to 303.6 K) and pressure (1.37x105 Pa to 2.08x108 Pa). The average relative deviations in the predicted equilibrium temperatures are found to be 0.72 % with organic inhibitors and 0.18 % with electrolytes, respectively. We believe that this method is useful for many gas hydrate related engineering problems such as the screening of inhibitors for gas hydrates in flow assurance.

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See more of this Session: Thermophysical Properties and Phase Behavior IV
See more of this Group/Topical: Engineering Sciences and Fundamentals