Abolfazl Mohammadi - Department of Chemical Engineering, University of Bojnord, Bojnord, Iran

Natural gas holds significant importance as a prospective energy source for meeting growing energy demands in the future. Gas hydrates offer a solution for the transportation and storage of natural gas. Within the sphere of gas hydrate formation, both the kinetics and thermodynamics play crucial roles and directly impact the economic feasibility of the process. In our current study, we focus on examining one specific kinetic parameter related to hydrate formation: the methane hydrate volume fraction (HVF) produced within a stirred batch reactor operating at a speed of ۱۰ rpm. Our experiments were done out in a double-walled reactor with a capacity of ۱۶۹ cm۳, maintaining a temperature of ۲۷۵.۱۵ K and a pressure of ۷.۵ MPa, utilizing a constant volume-constant temperature methodology. The experimental findings indicated that the utilization of SDS, noticeably, increases the amount of water to hydrate conversion, and the amount of combined volume of unreacted water and formed hydrate during hydrate growth. The addition of ۳۵۰ ppm and ۷۰۰ ppm SDS resulted in an increase in HVF by ۴۹۱.۲% and ۴۹۵.۷%, respectively, after ۱ hour of hydrate growth.

Methane, Gas hydrates, Energy, Hydrate volume fraction, Conversion