This paper investigates the influence of the air flow rate in a three-phase
air-lift reactor on the sorption of toxic dye, Brilliant green, onto a
promising and efficient sorbent, sour cherry stone biochar. In order to gain
a comprehensive insight into the sorbent/sorption behaviour, sour cherry
stone biochar was characterized by Fourier transform infrared spectroscopy
with attenuated total reflection, pH of the suspension, point of zero
charge, scanning electron microscopy with energy-dispersive X-ray
spectroscopy and X-ray diffraction. The experiments were performed in an
air-lift reactor using airflows of 2.50 and 5.55 dm3 h-1. The experimental
data of sorption kinetics experiments were fitted by non-linear form of
pseudo-first and, pseudo-second models as well as the Weber-Morris model
based on intraparticle diffusion. The overall sorption rate was found to be
limited by the Brilliant Green mass transport rate to the sorbent at a lower
airflow and thus mixing intensity, while it was kinetically controlled at a
higher rate following the pseudo-second order kinetic model. Furthermore,
sorption at lower air flow was delayed by mass transfer resistance through
the liquid boundary layer surrounding sorbent particles. Presented results
clearly indicate that airflow intensity plays a significant role in the
overall sorption kinetics and support possible application of the applied
biochar for efficient Brilliant Green sorption.