The treatment of oily wastewater produced from Farashband gas refinery through adsorption process
has been presented using activated carbon (AC) and natural zeolite (NA). For the purpose of
identifying the characteristics of the adsorbents, scanning electron microscopy, X-ray diffraction,
and Brunauer–Emmett–Teller analysis were performed. According to the results, since the specific
surface area of AC was around 897 m2/g which was much greater than 19.87 m2/g of NA, AC had
considerably better performance than NA for oily wastewater treatment. The comparison between
the adsorptive capacity of adsorbents revealed that using 30 g/L of activated carbon at 300 rpm
reduced the amount of chemical oxygen demand (COD) from 848 to less than 60 ppm (93% removal)
while within the examined dosage range of NA (5–40 g/L), the COD decreased only from 848 to
756 ppm (10% removal). Moreover, the modification of AC with phosphoric acid improved the
adsorption efficiency significantly in terms of adsorbent consumption. The removal percentage
which was acquired by applying 20 g/L of the modified AC (33% reduction in AC consumption)
was equivalent to that attained by 30 g/L of unmodified AC. Kinetic analysis signified that the
adsorption for both adsorbents followed the pseudo-first-order kinetic model equation.