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  5. Honeycomb-like porous-activated carbon derived from gasification waste for malachite green adsorption: equilibrium, kinetic, thermodynamic and fixed-bed column analysis
 
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Honeycomb-like porous-activated carbon derived from gasification waste for malachite green adsorption: equilibrium, kinetic, thermodynamic and fixed-bed column analysis

Journal
Desalination and Water Treatment
ISSN
1944-3986
Date Issued
2020
Author(s)
Anis Atikah Ahmad
Universiti Malaysia Perlis
Mohd Azmier Ahmad
Universiti Sains Malaysia
Nasehir Khan E.M. Yahaya
National Hydraulic Research Institute of Malaysia (NAHRIM)
Azam Taufik Mohd Din
Universiti Sains Malaysia
Ahmad Radi Wan Yaakub
Universiti Malaysia Perlis
DOI
10.5004/dwt.2020.26067
Handle (URI)
https://www.sciencedirect.com/science/article/pii/S1944398624102172/pdf?md5=ba3f5cfe7a6988ae4513287cf15605bf&pid=1-s2.0-S1944398624102172-main.pdf
https://www.sciencedirect.com/science/article/pii/S1944398624102172?pes=vor&utm_source=scopus&getft_integrator=scopus
https://hdl.handle.net/20.500.14170/14326
Abstract
In this study, the preparation conditions for the gasification waste-based activated carbon (GWAC) were optimized with malachite green (MG) dye removal and GWAC yield as responses. The adsorption equilibrium, kinetic behavior, and thermodynamics properties were also ana-lyzed. The optimum conditions for synthesizing GWAC were found at a radiation power, time, and impregnation ratios of 616 W, 1 min, and 1.06 g g–1, respectively, which resulted in an 89.98% yield of GWAC and 99.01% MG removal. This sample shows the surface area and total pore volume of 351.92 m2 g–1 and 0.22 cm3, respectively. For the isotherm study, the Fritz–Schlünder model fitted the adsorption data very well with an R2 value of 0.9919–0.9932. The results of the kinetic study showed that the MG adsorption followed a pseudo-first-order kinetic model (R2 = 0.9625–0.9871). The film diffusion was found to be the rate-limiting step of MG adsorption. The adsorption of the MG dye onto GWAC was an endothermic and spontaneous process with ΔH of 9.183 kJ mol–1. In continuous mode, Thomas and Yoon–Nelson models successfully predicted the MG adsorption on the GWAC. GWAC demonstrates its commercial feasibility based on a low production cost of 0.23 USD kg–1.
Subjects
  • Activated carbon

  • Adsorption

  • Adsorption kinetic

  • Gasification waste

  • Malachite green

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Honeycomb-like porous-activated carbon derived from gasification waste for malachite green adsorption.pdf (91.81 KB) Honeycomb-like porous-activated carbon derived from gasification waste for malachite green.pdf (1.11 MB)
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