Valorization of olive stone as adsorbent of chromium(VI): comparison between laboratory- and pilot-scale fixed-bed columns

The main aim of this work is to study the effect of scaling in the biosorption of chromium(VI) onto olive stone in two different fixed-bed columns. Firstly, the effect of flow rate, bed depth and inlet concentration of Cr(VI) in both columns was analyzed. The results revealed a better operation for lower flow rates, higher bed heights and lower inlet concentrations of metal. When decreasing flow rate, the operation time of the column increases. Therefore, as the solution flow rate increased the breakthrough and the exhaustion times decreased. An increase in bed depth increases the quantity of chromium eliminated and thus, the higher sorption capacity of the system. A decrease in the inlet concentration of chromium produces a delay in exhaustion time, and larger volumes of solution could be treated. The results were fitted to the BDST model, obtaining that the adsorptive capacity of the bed depth is similar in laboratory- and pilot-scale fixed-bed columns, considering the biosorption capacity as a biosorption-coupled reduction process. Results also could indicate that scaling affects more to the reduction process than properly biosorption process. The experimental data were also fitted to Adams–Bohart, Thomas, Yoon–Nelson and dose–response models. A good fit of the biosorption process of Cr(VI) was found for dose–response and Adams–Bohart models.