2017 Annual Meeting
(589d) Measurement and Modeling of Competitive Sorption of Methane/Ethane Mixtures on Marcellus Shale – Isotherms and Kinetics
Authors
In this work, measurements of pure component sorption isotherms for CH4 and C2H6 for pressures up to 114 bar and 35 bar, respectively, have been performed using a thermogravimetric method in the temperature range (40-60 oC). Sorption experiments of binary (CH4-C2H6) gas mixtures containing up to 10% (mole fraction) of C2H6, typical of shale-gas compositions, for pressures up to 125 bar under the aforementioned temperature conditions have also been conducted.
To facilitate investigation of depletion dynamics (e.g. via application of the Extended Langmuir Model), excess sorption measurements must be converted to absolute sorption. This conversion requires accurate estimates of the adsorbate density. Here we investigate the performance of several of such methods proposed for evaluating the adsorbate density. We demonstrate that the equilibrium constant and hence the adsorption and desorption kinetic constants are sensitive to the choice of the adsorbate density model and conclude by providing recommendations for selection of adsorbate density modeling. Lastly, we apply the best-fit adsorbate density method to model the sorption dynamics of pure and binary gas mixtures on to the shale.
To the best of our knowledge, this is the first time that systematic measurements of CH4, C2H6 pure and binary mixture sorption on the Marcellus shale have been conducted, thus providing a comprehensive set of CH4-C2H6 competitive sorption data, which can help to improve the fundamental understanding of shale-gas storage mechanisms and its subsequent production.