Publication Type : Journal Article
Thematic Areas : Biotech
Publisher : Desalination and Water Treatment
Source : Desalination and Water Treatment, Taylor and Francis Inc., p.1-9 (2016)
Campus : Coimbatore
School : School of Engineering
Center : Biotechnology, Green Energy
Department : biotechnology, Chemical
Year : 2016
Abstract : The contact time in two batch adsorbers were optimized using unreacted shrinking core model for the adsorption of biopolymeric pigments in distillery spentwash by fly ash adsorbent. The total optimal contact time obtained was 40 min for 3nbsp;m3 adsorbate volume having initial biopolymer concentration of 1.5nbsp;mg/dm3. The film pore diffusion model was used to determine the external mass transfer coefficient, effective diffusion coefficient, and bed capacity for continuous adsorption process. The adsorbent bed capacities at different initial biopolymeric concentrations (2,000, 5,500, 8,700, and 12,500nbsp;mg/ml) are 69.26, 114.41, 143.64, and 172nbsp;mg/g, respectively. The effective diffusion coefficients at various bed heights were determined for continuous adsorption process. © 2016 Balaban Desalination Publications. All rights reserved.
Cite this Research Publication : D. Aravind and Dr. Krishna Prasad R., “Film pore diffusion modeling and contact time optimization for adsorption of distillery spentwash on fly ash”, Desalination and Water Treatment, pp. 1-9, 2016.