Magnetic biochars were prepared using Fe 3 O 4 nanoparticle composites onto the surface of biochar derived from rice husk. The characteristics of magnetic biochar were characterized by scanning electron microscope, x-ray powder diffraction and Fourier-transform infrared techniques. The removal of rhodamine 6G dye by magnetic biochar, compared to pristine biochar was studied. The effects of pyrolysis temperature on rhodamine 6G adsorption was evaluated. Kinetic, isotherms and thermodynamic studies were carried out to investigate the adsorption mechanism of rhodamine 6G dye on magnetic biochar surface. The rhodamine 6G removal efficiency of Fe 3 O 4 -composited biochar (pyrolyzed at 500°C) is higher than that of pristine biochar with maximum efficiency of 94% removal. The adsorption isotherm and kinetic studies indicated that the langmuir model, pseudo-first order and pseudo-second order models described well the rhodamine adsorption onto magnetic Fe 3 O 4 -biochar.
Abbreviations
BCBiochar C 0 Initial dye concentration (mg/L) C e Equilibrium concentration of dye (mg/L) ΔG 0 The Gibbs free energy) and f ΔH 0 The change of enthalpy MB Magnetic biochar q e Adsorbed dye amount per gram of sorbent at equilibrium (mg/g) q e,cal Calculated amount of dye adsorbed per gram of adsorbent at equilibrium (mg/g) q e,exp Experimental amount of dye adsorbed per gram of adsorbent at equilibrium (mg/g) q t Adsorbed dye amount per gram of adsorbent at time t (mg/g) K Thermodynamic equilibrium constant K L Langmuir isotherm equilibrium constant representing the energy of sorption (L/mg) K F Freundlich constant representing sorption capacity ((mg/g)(L/mg)/n) k 1 Pseudo-first order rate constant (1/min) k 2 Pseudo-second order rate constant (g/mg·min) n Freundlich isotherm constant representing sorption intensity R The ideal gas constant (8.314 J mol −1 ·K −1 )