Kiumars Hosseini - Department of Chemical, Petroleum and Gas Engineering, Shiraz University of Technology, Shiraz, Iran
Ali Dehghan Abnavi - Department of Petroleum Engineering, School of Chemical, Gas and Petroleum Engineering, Shiraz University, Shiraz, Iran

Knowing the hydrate phase equilibria in brines is critically important to assess the risk of hydrate formation, especially for conditions involving high salinity and very high pressure, which are becoming more prevalent in oil/gas exploration and production. Inorganic salts are thermodynamic hydrate inhibitors and are commonly present in produced water from oil/gas production. In the present work, after updating and re-optimization the parameters of the thermodynamic model for calculating the water activity coefficient in the presence of various electrolytes (NaCl, KCl, CaCl2 and MgCl2), the average absolute deviation of the model, is about 0.40 K for pressures ranging from 0.2 to 15 MPa. Compared to other literature models, it shows the high accuracy of the model.

Hydrate formation, Inhibitors, Electrolyte, Thermodynamic model