Elimination performance of Nile blue from wastewater using by carboxymethyl cellulose-graft-poly(methacrylic acid-co-acrylamide)/kaolin nanocomposite hydrogel
In this study, we synthesized carboxymethyl cellulose-graft-poly(methacrylic acid-co-acrylamide) copolymer hydrogels and carboxymethyl cellulose-graft-poly(methacrylic acid-co-acrylamide)/kaolin nanocomposite with a free radical mechanism to adsorb pollutants of Nile blue dye. Nanocomposite hydrogels performed best at pH = 11, a temperature of 25 & DEG;C, a contact time of 90 min, a concentration of pollutant 10 ppm, and an adsorbent dose of 1.5 mg. The increased adsorption rate of NB dye pollutants after adding kaolin-type clay nanoparticles from 96.49 to 98.91% showed the successful addition of nanoparticles to hydrogel copolymer structures. The best isotherm performance was the Langmuir isotherm model, and maximum adsorption capacity for carboxymethyl cellulose-graft-poly(methacrylic acid-co-acrylamide) copolymer hydrogels and for carboxymethyl cellulose-graft-poly(methacrylic acid-co-acrylamide) nanocomposite hydrogel was 138.49 and 149.82, respectively. In the analysis of kinetic models, Elovich's kinetic model had the best performance, where the & alpha; value for carboxymethyl cellulose-graft-poly(methacrylic acid-co-acrylamide) copolymer hydrogels are 0.783 and for carboxymethyl cellulose-graft-poly(methacrylic acid-co-acrylamide)/kaolin nanocomposite hydrogel obtained a value of 9.58, which indicates a high adsorption value. On the other hand, the enthalpy parameters (& UDelta;H & DEG;) for adsorption process using carboxymethyl cellulose-graft-poly(methacrylic acid-co-acrylamide) and carboxymethyl cellulose-graft-poly(methacrylic acid-co-acrylamide)/kaolin nanocomposite hydrogels were - 61.512 kJ/mol and - 77.281 kJ/mol, respectively. The negativity of & UDelta;H & DEG; indicates that the process is exothermic at 5-50 & DEG;C using both adsorbers. Furthermore, this process could be spontaneous because the Gibbs free energy (& UDelta;G & DEG;) for adsorption processes was negative in experiment temperature range.
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Khalifa Univ Sci & Technol, Dept Mech Engn, POB 12778, Abu Dhabi, U Arab EmiratesKhalifa Univ Sci & Technol, Dept Mech Engn, POB 12778, Abu Dhabi, U Arab Emirates
Mittal, Hemant
Al Alili, Ali
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Khalifa Univ Sci & Technol, Dept Mech Engn, POB 12778, Abu Dhabi, U Arab EmiratesKhalifa Univ Sci & Technol, Dept Mech Engn, POB 12778, Abu Dhabi, U Arab Emirates
Al Alili, Ali
Alhassan, Saeed M.
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Khalifa Univ Sci & Technol, Dept Chem Engn, POB 127788, Abu Dhabi, U Arab EmiratesKhalifa Univ Sci & Technol, Dept Mech Engn, POB 12778, Abu Dhabi, U Arab Emirates
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Midnapore Coll Autonomous, Postgrad Div Chem, Midnapore 721101, W Bengal, IndiaMidnapore Coll Autonomous, Postgrad Div Chem, Midnapore 721101, W Bengal, India
Samanta, Santu Kumar
Adak, Shubhadeep
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Midnapore Coll Autonomous, Midnapore Coll Res Ctr Sci, Midnapore, W Bengal, IndiaMidnapore Coll Autonomous, Postgrad Div Chem, Midnapore 721101, W Bengal, India
Adak, Shubhadeep
Tripathy, Tridib
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Midnapore Coll Autonomous, Postgrad Div Chem, Midnapore 721101, W Bengal, IndiaMidnapore Coll Autonomous, Postgrad Div Chem, Midnapore 721101, W Bengal, India
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Egyptian Atom Energy Author, Hot Labs Ctr, Nucl Chem Dept, POB 13759, Cairo, EgyptEgyptian Atom Energy Author, Hot Labs Ctr, Nucl Chem Dept, POB 13759, Cairo, Egypt
Dakroury, G. A.
Murad, G. A.
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Egyptian Atom Energy Author, Hot Labs Ctr, Nucl Fuel Chem Dept, Cairo 13759, EgyptEgyptian Atom Energy Author, Hot Labs Ctr, Nucl Chem Dept, POB 13759, Cairo, Egypt
Murad, G. A.
Abu Elgoud, E. M.
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Egyptian Atom Energy Author, Hot Labs Ctr, Nucl Fuel Chem Dept, Cairo 13759, EgyptEgyptian Atom Energy Author, Hot Labs Ctr, Nucl Chem Dept, POB 13759, Cairo, Egypt