Bio-adsorption of triadimenol pesticide from aqueous solutions using activated sludge of dairy plants

被引:35
|
作者
Al-Shawabkah, R. [1 ]
Al-Qodah, Z. [2 ,3 ]
Al-Bsoul, A. [4 ]
机构
[1] King Fahd Univ Petr & Minerals, Dept Chem Engn, Dhahran 31261, Saudi Arabia
[2] Taibah Univ, Dept Chem Engn, Madinah, Saudi Arabia
[3] Al Balqa Appl Univ, Dept Chem Engn, Amman 11134, Marka, Jordan
[4] Al Balqa Appl Univ, Al Huson Univ Coll, Dept Chem Engn, Irbid, Jordan
关键词
Triadimenol; Adsorption; Adsorption isotherms; Activated sludge; Adsorption kinetics; SHALE OIL ASH; WASTE-WATER; SEWAGE-SLUDGE; REMOVAL; ACID; FUNGICIDES; SURFACE; BIOSORBENT; SORPTION; LINDANE;
D O I
10.1080/19443994.2013.865565
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
In the present study, activated sludge has been utilized for the removal of triadimenol pesticide from water. The maximum adsorption capacity was 42.9mg triadimenol per gram activated sludge obtained at 298K. The equilibrium data were fitted to Langmuir Freundlich models and it was found that Freundlich model best fit these data with regression coefficient R-2 =( )0.947. The kinetic data showed that the rate of triadimenol adsorption is increased with increasing the initial concentration and mixing speed, while decreased with increasing temperature. The two-resistance mass transfer model based on the film resistance homogeneous solid-phase diffusion was used to fit the experimental data. A computer program has been developed to estimate the theoretical concentration-time- dependent curves and to compare them with the experimental curves by means of the best-fit approach. The model predicts that the external mass transfer coefficient k(f) was affected by varying the initial triadimenol concentration, the agitation speed and temperature, whereas the diffusion coefficient D-e was affected by the initial triadimenol concentration and temperature.
引用
收藏
页码:2555 / 2564
页数:10
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