Activated carbon from industrial solid waste as an adsorbent for the removal of Rhodamine-B from aqueous solution: Kinetic and equilibrium studies

被引:190
作者
Kadirvelu, K
Karthika, C
Vennilamani, N
Pattabhi, S
机构
[1] PSG Coll Arts & Sci, Dept Environm Sci, Coimbatore 641014, Tamil Nadu, India
[2] PSGR Krishnammal Coll Women, Dept Chem, Coimbatore 641004, Tamil Nadu, India
关键词
sago waste; adsorption equilibrium; pH; particle size; desorption;
D O I
10.1016/j.chemosphere.2005.01.047
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
The activated carbon was prepared using industrial solid waste called sago waste and physico-chemical properties of carbon were carried out to explore adsorption process. The effectiveness of carbon prepared from sago waste in adsorbing Rhodamine-B from aqueous solution has been studied as a function of agitation time, adsorbent dosage, initial dye concentration, pH and desorption. Adsorption equilibrium studies were carried out in order to optimize the experimental conditions. The adsorption of Rhodamine-B onto carbon followed second order kinetic model. Adsorption data were modeled using both Langmuir and Freundlich classical adsorption isotherms. The adsorption capacity Q(0) was 16.12 mg g(-1) at initial pH 5.7 for the particle size 125-250 mu m. The equilibrium time was found to be 150 min for 10, 20 mg l(-1) and 210 min for 30, 40 mg l(-1) dye concentrations, respectively. A maximum removal of 91% was obtained at natural pH 5.7 for an adsorbent dose of 100 mg/50ml of 10 mg l(-1) dye concentration and 100% removal was obtained when the pH was increased to 7 for an adsorbent dose of 275 mg/50 ml of 20 mg l(-1) dye concentration. Desorption studies were carried out in water medium by varying the pH from 2 to 10. Desorption studies were performed with dilute HCl and show that ion exchange is predominant dye adsorption mechanism. This adsorbent was found to be both effective and economically viable. (C) 2005 Elsevier Ltd. All rights reserved.
引用
收藏
页码:1009 / 1017
页数:9
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