698
J Surfact Deterg (2016) 19:693–699
70 °C, which indicates that the novel gemini surfactants
are capable of reducing the interfacial tension to ultra-low
levels even at extremely high salinity and high degree of
mineralization, and it promises the basis for future
exploitation of oil fields.
0.018
0.016
0.014
0.012
0.010
0.008
0.006
Conclusion
4,40-Di(n-tetradecanoyl) diphenyl methane was produced
by using diphenyl methane and tetradecanoyl chloride as
raw materials by a Friedel–Crafts acylation reaction. Then
by means of the Clemmensen reduction, sulfonation with
chlorosulfonic acid and neutralization with NaOH aqueous
solution, the final product was synthesized.
The CMC of 4,40-di(n-tetradecyl) diphenyl methane
disulfonate salt aqueous solution is 1.00 9 10-3 mol/L,
and its surface activity is good enough. The interfacial
tension of 4,40-di(n-tetradecyl) diphenyl methane disul-
fonate salt aqueous solution reaches ultra-low values sug-
gesting t is a suitable surfactant for EOR applications.
40
45
50
55
60
65
70
T/(°C)
Fig. 5 Oil–water interfacial tension of C14-DSDM at different
temperature
is very small, the molecules can lie flat on the interface
[32]. The decrease of interfacial tension is caused by the
adsorption of surfactant molecules at the water/oil inter-
face. It usually takes time for surfactant molecules to dif-
fuse and adsorb at the interface. Therefore, the dynamic
interfacial tension will change over time [33]. Dynamic
interfacial tension often shows the lowest point corre-
sponding to the maximum amount of interfacial adsorption.
Aqueous samples of C14-DSDM gemini surfactant were
prepared in 300 mg/L hard water and 6 g/L salinity base
solution. The interfacial tensions between the solution and
crude oil were measured over a range of temperatures. The
most important thing worth attention here is that the
solution had an extremely high salinity (6 g/L) and a high
degree of mineralization (300 mg/L). Even under this
extreme condition, no precipitation or phase separation
happened for any of the test temperatures. In contrast,
conventional (monomeric) surfactants used in the petro-
leum industry today generally show poor aqueous solu-
bility/stability under such harsh conditions (high
mineralized degree or salinity). Thus, complex surfactant
formulations are studied in which a co-surfactant and/or
co-solvent are added to enhance the solubility [34]. This
unfortunately generates a lot of issues, including design
complexity, elevated cost, and chromatographic separation
[35].
Acknowledgments We are grateful for the financial support from the
Fundamental Research Funds for the Central Universities
(JUSRP51513).
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