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Adsorption isotherms, kinetics and mechanism for the adsorption of cationic and anionic dyes onto carbonaceous particles prepared from Juglans regia shell biomass

机译:核桃壳生物质制得的碳质颗粒上阳离子和阴离子染料的吸附等温线,动力学和机理

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摘要

In the present study, Juglans regia shells were used to prepare activated carbon by acid treatment method. J. regia shell-based activated carbon was used for the adsorption of two synthetic dyes namely, a basic dye malachite green and an acid dye amido black 10B. The prepared adsorbent was crushed and sieved to three different mesh sizes 100, 600 and 1,000 mu m. The adsorbent was characterized by scanning electron microscopy, surface acidity and zero-point charge. Batch experiments were carried out by varying the parameters like initial aqueous phase pH, adsorbent dosage and initial dye concentration. The equilibrium data were tested with Langmuir, Freundlich, Redlich-Peterson and Sips isotherm at three different temperatures 293, 300 and 313 K and it was found that the Freundlich isotherm best fitted the adsorption of both the dyes. Kinetic data were tested with pseudo first-order model and pseudo second-order model. The mechanism for the adsorption of both the dyes onto the adsorbent was studied by fitting the kinetic data with intraparticle diffusion model and Boyd plot. External mass transfer was found to be the rate-determining step. Based on the ionic nature of the adsorbates, the extent of film diffusion and intraparticle diffusion varied; both being system specific. Thermodynamic parameters were also calculated. Finally, the process parameters of each adsorption system were compared to develop the understanding of the best suitable system.
机译:在本研究中,胡桃壳被用于通过酸处理法制备活性炭。 J. regia壳基活性炭用于吸附两种合成染料,即碱性染料孔雀石绿和酸性染料酰胺黑10B。将制得的吸附剂压碎并筛分成三种不同的筛孔尺寸,分别为100、600和1,000微米。通过扫描电子显微镜,表面酸度和零点电荷对吸附剂进行表征。通过改变诸如初始水相pH,吸附剂剂量和初始染料浓度等参数进行批量实验。用Langmuir,Freundlich,Redlich-Peterson和Sips等温线在293、300和313 K的三个不同温度下测试了平衡数据,发现Freundlich等温线最适合两种染料的吸附。用伪一级模型和伪二级模型测试动力学数据。通过将动力学数据与颗粒内扩散模型和博伊德图拟合,研究了两种染料吸附到吸附剂上的机理。发现外部传质是决定速率的步骤。基于被吸附物的离子性质,膜扩散和颗粒内扩散的程度有所不同。两者都是系统特定的。还计算了热力学参数。最后,比较每个吸附系统的工艺参数,以发展对最合适系统的理解。

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