Adsorption of Metformin on Activated Carbon Produced from the Water Hyacinth Biowaste Using H3PO4 as a Chemical Activator

被引:12
|
作者
Mohammad, Ahmad Hakky [1 ]
Radovic, Ivona [1 ]
Ivanovic, Marija [2 ]
Kijevcanin, Mirjana [1 ]
机构
[1] Univ Belgrade, Fac Technol & Met, Karnegijeva 4, Belgrade 11120, Serbia
[2] Univ Belgrade, Vinca Inst Nucl Sci, Natl Inst Republ Serbia, Dept Mat, Mike Petrovica Alasa 12-14, Belgrade 11000, Serbia
关键词
water hyacinth biowaste; activated carbon; metformin hydrochloride adsorption; isotherm; kinetics; EURYALE-FEROX SHELL; PHOSPHORIC-ACID; AGRICULTURAL RESIDUES; RICE HUSK; REMOVAL; KINETICS; PERFORMANCE; SUBSTANCES; CAPACITY; EQUATION;
D O I
10.3390/su141811144
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
Water hyacinth biomass was used for the synthesis of activated carbons in the process of chemical activation with H3PO4, followed by controlled carbonization. The study investigates the effect of various impregnation weight ratios of H3PO4 and dry hyacinth (0.5-3.0), as well as different carbonization temperatures (T = 400-800 degrees C), on the surface characteristics of the produced activated carbons (AC). The activated carbon obtained with an impregnation ratio of 1.5 and a carbonization temperature of 600 degrees C (1.5 AC/600) showed the highest values of specific surface area of 1421 m(2) g(-1), representing a selected adsorbent for metformin removal. The chosen sample was characterized by elemental analysis, adsorption-desorption isotherms of nitrogen at -196 degrees C, via FTIR spectroscopy and the SEM method. The modeling of the experimental adsorption data showed that metformin adsorption: (i) can be best described by the Langmuir isotherm model, with the value of q(max) = 122.47 mg g(-1); (ii) led the pseudo-second order kinetic model; and (iii) is a spontaneous (Delta G degrees = -3.44 kJ mol(-1)) and endothermic (Delta H degrees = 8.77 kJ mol(-1)) process. A desorption study has shown that 92% of metformin was successfully desorbed in the presence of a 0.1 MHCl/ethanol mixture (volume ratio 2:1). The recovery of the adsorbent of 84%, after five successive cycles, indicated that the 1.5 AC/600 has potential to be applied in the real systems for water treatment.
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页数:22
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