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Farshid Ghorbani

Farshid Ghorbani

Academic rank: Associate Professor
ORCID:
Education: PhD.
ScopusId: 23027283400
Faculty: Faculty of Natural Resources
Address: Department of Environmen, Faculty of Natural Resource, University of Kurdistan, P.O. Box: 416, 66177-15175 Sanandaj, Iran
Phone: 087-6620551

Research

Title
Aqueous Cadmium Ions Removal by Adsorption on APTMS Grafted Mesoporous Silica MCM-41 in Batch and Fixed Bed Column Processes
Type
JournalPaper
Keywords
Sedge (Carex riparia) MCM-41 Batch Adsorption Fixed-bed Column
Year
2013
Journal International Journal of Engineering
DOI
Researchers Farshid Ghorbani ، HABIBOLLAH Younesi ، Zahra Mehraban ، Mehmet Sabri Celik ، Ali Asghar Ghoreyshi ، Mansoor Anbia

Abstract

Highly ordered mesoporous MCM-41silica with hexagonal structure was synthesized using extracted amorphous silica from sedge (Carex riparia ) ash. Obtained mesoporous materials functionalized by 3- (Aminopropyl) trimethoxysilane (APTMS) and their structures characterized by means of X-ray diffraction (XRD), nitrogen adsorption-desorption, thermogravimetric analysis (TGA) and Fourier transform infrared (FT-IR) spectroscopy. The synthesized material were applied for adsorption of Cd(II) metal ions from aqueous solution in batch and fixed bed column systems. Batch adsorption process was carried out to evaluate initial ion concentrations, sorbent dose, contact time, pH and temperature. The equilibrium data were analyzed using the Langmuir and Freundlich isotherm by nonlinear regression analysis. The kinetics study reviled that data from the experiments fitted well to the pseudo-second order equation than pseudo-first order. Thermodynamic parameters reviled that the adsorption process strongly depended on temperature and the adsorption capacity increased by increasing the temperature of the system, indicating the endothermic behavior and spontaneous nature of adsorption. For continuous adsorption experiments, NH2-MCM-41 adsorbent was used and breakthrough curves were analyzed at different bed heights, flow rates and initial metal ion concentrations. Thomas and bed depth service time (BDST) models were used to determine the kinetic constants and to predict the breakthrough curves of each component.