Gas hydrates are ice-like crystals formed from gas and water under high pressure and low temperature, is a source of energy and causes pipeline flow assurance issue risking shutdowns, equipment damage, and safety hazards in oil and gas operations. To mitigate these issues, flow assurance strategies often involve using hydrate inhibitors (like ethylene glycol), insulation, and heating systems to maintain conditions that prevent hydrate formation, ensuring safe and continuous gas transport. Molecular dynamics (MD) simulations offer a powerful tool to investigate the behaviour of gas hydrates at the atomic level, providing insights into their formation, stability, and interactions. This study explores the impact of ethylene glycol on the dissociation and stability of CO2 and methane hydrates together in a system through MD simulations. While inhibitors are commonly used in the industry to prevent hydrate formation and assist in dissociation, their precise role in this gas exchange mechanism demands more detailed exploration. In this study, we investigated the potential of ethylene glycol as a chemical additive to promote gas hydrate dissociation, though its effects are not yet fully understood. Using molecular dynamics (MD) simulations, we explored parameters such as radial distribution function (RDF), mean square displacement (MSD), and diffusion coefficients to examine the impact of ethylene glycol across various temperatures (270.15 K–300 K) and concentrations (0–15 % V/V). The results indicate that gas dissociation accelerates by 150 % with rising temperatures, allowing methane to escape more rapidly into the simulation box, thereby enabling controlled gas production. Additionally, a 10 % increase in glycol concentration destabilizes hydrate structure. Based on these findings, we recommend using ethylene glycol at 10 % v/v for gas hydrate dissociation at 280.15 K.

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