Title :
Notice of Retraction
Adsorption Removal of COD from Wastewater by the Activated Carbons Prepared from Sugarcane Bagasse
Author :
Yan Pan ; Yinian Zhu ; Zelong Xu ; Rongrong Lu ; Zonglan Zhang ; Meina Liang ; Huili Liu
Author_Institution :
Coll. of Environ. Sci. & Eng., Guilin Univ. of Technol., Guilin, China
Abstract :
Notice of Retraction
After careful and considered review of the content of this paper by a duly constituted expert committee, this paper has been found to be in violation of IEEE´s Publication Principles.
We hereby retract the content of this paper. Reasonable effort should be made to remove all past references to this paper.
The presenting author of this paper has the option to appeal this decision by contacting TPII@ieee.org.
The activated carbons were prepared by soaking sugarcane bagasse in 0.39% AlCl3 solution and followed by carbonization in a charcoal kiln at 400°C for 2 days and then by activation in a muffle furnace at 900°C for 100 minutes. The adsorption removal of chemical oxygen demand (COD) from molasses alcohol wastewater by the prepared activated carbons was then studied in a batch adsorption system. The amount of COD adsorbed per unit mass of adsorbent decreased with increasing adsorbent dose from 18.97 to 8.18 mg/g and the percentage of COD removed from solution increased continuously from 6.90 to 58.73% with increasing adsorbent dose from 100 to 2000 mg in 50 mL solution with the initial COD concentration of 557 mg/L. With increasing COD concentration from 55 to 549 mg/L, the amount of COD adsorbed per unit mass of adsorbent increased from 1.04 to 13.57 mg/g. The dynamical data fit very well with both the pseudo-first-order kinetic model and the pseudo-second-order kinetic model. The Freundlich model showed higher correlation with the experimental adsorption data in comparison with the Langmuir model.
Keywords :
activated carbon; adsorption; charcoal; crops; industrial waste; kilns; recycling; wastewater treatment; COD concentration; Freundlich model; Langmuir model; activated carbon; adsorbent dose; adsorption removal; batch adsorption system; carbonization; charcoal kiln; chemical oxygen demand; molasses alcohol wastewater; muffle furnace; pseudofirst-order kinetic model; pseudosecond-order kinetic model; soaking; sugarcane bagasse; temperature 400 degC; temperature 900 degC; time 100 min; Carbon; Carbon dioxide; Chemicals; Data models; Kinetic theory; Mathematical model; Wastewater;
Conference_Titel :
Bioinformatics and Biomedical Engineering, (iCBBE) 2011 5th International Conference on
Conference_Location :
Wuhan
Print_ISBN :
978-1-4244-5088-6
DOI :
10.1109/icbbe.2011.5781097