Characterization of biochar prepared from slow pyrolysis of Jordanian olive oil processing solid waste and adsorption efficiency of Hg2+ ions in aqueous solutions

被引:26
作者
El Hanandeh, Ali [1 ]
Abu-Zurayk, Rund A. [2 ]
Hamadneh, Imad [3 ]
Al-Dujaili, Ammar H. [2 ]
机构
[1] Griffith Univ, Sch Engn, Nathan, Qld 4111, Australia
[2] Univ Jordan, Hamdi Mango Ctr Sci Res, POB 11942, Amman, Jordan
[3] Univ Jordan, Fac Sci, Dept Chem, POB 11942, Amman, Jordan
关键词
adsorption; biochar; Hg2+; mercury (II); olive husk; slow pyrolysis; ACTIVATED CARBON; HG(II) IONS; REMOVAL; SORPTION; MERCURY; EQUILIBRIUM; INDUSTRY;
D O I
10.2166/wst.2016.378
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
Solid waste from Jordanian olive oil processing (OOSW) was used to prepare biochar samples by slow pyrolysis at terminal temperatures of 350, 450, 550 and 630 degrees C; henceforth known as BC-350, BC-450, BC-550 and BC-630, respectively. These samples were characterized by Fourier transform infrared spectroscopy, scanning electron microscopy and X-ray diffraction, ash content, moisture content and surface area. The ability of the biochar to remove Hg2+ ions from aqueous solutions was investigated in laboratory scale batch experiments. The kinetics, effect of pH and temperature were studied. The optimum pH value for Hg2+ adsorption was 5. Dubinin-Radushkevich (D-R) isotherm model was the best fit for the experimental results. Based on the D-R model, the maximum adsorption capacities at 25 degrees C were 84.93, 94.48, 96.11 and 104.59 mg.g(-1), for BC-350, BC-450, BC-550 and BC-630, respectively. The pseudo-second-order kinetic model was a good fit for the experimental data. The calculated change in free energy Delta G and enthalpy Delta H indicated that the adsorption process was spontaneous and exothermic in nature. The positive value of Delta S showed increased randomness of the solid/solution interface during the adsorption. The results indicated that biochar derived from OOSW can be a good adsorbent for treatment of water contaminated with Hg2+.
引用
收藏
页码:1899 / 1910
页数:12
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