Interfacial
tension (IFT) plays a vital role in the petroleum industry
for enhanced oil recovery. In recent years, a new technology called
“low salinity water flooding” has captured the attention
of researchers because of its ability to alter IFT. However, the role
of salt types and their impact on the IFT of pure hydrocarbon–water
systems are not well understood which could help to develop robust
models and processes. In the present investigation, we have considered
both aliphatic (heptane) and aromatic (toluene) hydrocarbons along
with set of nine mixed brine systems containing monovalent (NaCl,
KCl) and divalent (MgCl2, MgSO4) salts with
a wide range of compositions and concentrations for IFT studies which
are otherwise not reported in the literature. Various combinations
of monovalent salts (NaCl:KCl::25:75, NaCl:KCl::50:50, NaCl:KCl::75:25) divalent salts (MgSO4:MgCl2::25:75, MgSO4:MgCl2::50:50,
MgSO4:MgCl2::75:25), and monovalent and divalent
salts (NaCl:MgCl2::25:75, NaCl:MgCl2::50:50,
NaCl:MgCl2::75:25) along with varying concentrations (0,
500, 750, 1 000, 2 000, 5 000, 10 000,
20 000 ppm) have been used. The experimental result reveals
that combination of monovalent (NaCl) and divalent (MgCl2) salt in brine has significant impact on the reduction of the IFT
of the n-heptane–brine system, and combination
of divalent salts (MgSO4 and MgCl2) shows better
impact on IFT reduction for the toluene–brine system. The mechanism
of IFT variation at different salt concentrations and compositions
has also been explained based on the Gibbs adsorption isotherm and
specific ion effect based on the Hofmeister series. The study will
be useful to understand the synergetic effect of these salts on the
hydrocarbon–brine systems and also will help to develop robust
models of IFT suitable for low salinity water flooding and other industrial
operations.