Bentonite sample
enriched in organic matters (oil shale) was functionalized
with −SO3H sulfonated carbonaceous bentonite (S-CB)
by sulfonation process as a low-cost and effective acidic catalyst
for the transesterification spent sunflower oil (SFO). The sulfonation
effect was followed by several analytic techniques including X-ray
diffraction, Fourier transform infrared, and scanning electron microscopy
analysis. The catalytic performance of the sulfonated product was
evaluated based on a statistical design which was built according
to the response surface methodology and the central composite rotatable
design. Using the S-CB acidic catalyst in the transesterification
of spent SFO resulted in an actual biodiesel yield of 96% at studied
conditions of 85 min at reaction interval, 50 °C as temperature,15:1
as methanol/oil ratio, and 3.5 wt % as S-CB loading. Moreover, the
optimization function suggested enhancement to obtained yield up to
97.9% by selecting the values of temperature at 62 °C, the time
at 98.5 min, the methanol/SFO ratio at 14.4:1, and S-CB loading at
3.4 wt %. The technical evaluation of the SFO biodiesel reflected
the suitability of the product to be used as biofuels according to
international standards. The kinetic behavior of the SFO transesterification
reaction over S-CB is of pseudo-first order properties and of low
activation energy. Finally, the synthetic S-CB as a solid acidic catalyst
is of significant reusability and was reused five times with remarkable
biodiesel yields.