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Application of activated biomass waste as an adsorbent for the removal of lead (II) ion from wastewater

机译:活性生物质废料作为吸附剂从废水中除去铅(II)离子的吸附剂

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This work focuses on the application of activated biomass as an alternative to conventional adsorbents for the removal of Pbsup2+/sup from wastewater. The biomass was carbonized at 800?°C before chemical activation. Scanning Electron Microscope (SEM) and UV/VIS Spectrophotometer were used in characterizing the adsorbents. Batch adsorption studies were carried out to determine the effect of process conditions on the percentage removal. The kinetic studies were carried out using Pseudo-first order, Pseudo-second order, Elovich and Weber morris kinetic models while the thermodynamics studies were carried out using Gibbs free energy equation. SEM characterization revealed that micro porous space on the surface of the adsorbents (biomass wastes) increased significantly after activation. The composites maintained high surface area after chemical activation. pH of point zero charge revealed negative charge predominance on the surface of the adsorbents and adsorption was found to be very fast due to strong electrostatic force between Pbsup2+/sup and ion diffusion on the biomass surface. Cassava peel demonstrated highest potential for lead (II) ion removal from solution with 96.83% removal after 80?min with 50?mg/l lead concentration and adsorbent/liquid ratio of 0.3?g/30?ml?at 60 °C and pH of 7.6. The highest adsorption capacities recorded with cassava peels, groundnut shell and yam peel at initial concentration of 50?mg/g were 50. 1?mg?g, 46.6?mg/g and 38.5?mg/g Δ H , Δ S and Rsup2/sup values for the adsorption with cassava peels are: 12762?J/mol, 67.2?J/kmol.K and 0.945; for groundnut shell adsorbent, the Δ H , Δ S and Rsup2/sup values are; 36756?J/mol, 130?J/mol.K and 0.997; while for yam peels adsorbent, the Δ H , Δ S and Rsup2/sup values are 12163?J/mol, 46?J/mol.K and 0.9278. Thus, the sorption process was feasible, spontaneous and endothermic. Adsorption of Pbsup2+/supwas rapid and showed high kinetic performance. The experimental data were well fitted with pseudo second order kinetic model. However, the present approach has the advantage of simplicity, less time consuming and most importantly, low cost.
机译:该工作侧重于活性生物量作为常规吸附剂的替代方法,用于从废水中除去Pb 2 + / sup>。在化学活化之前,将生物质在800℃下碳化。扫描电子显微镜(SEM)和UV / VIS分光光度计用于表征吸附剂。进行批量吸附研究以确定工艺条件对去除百分比的影响。通过伪第一顺序,伪二阶,ELOVICH和Weber Morris动力学模型进行动力学研究,同时使用Gibbs自由能方程进行热力学研究。 SEM表征揭示了在活化后吸附剂表面(生物质废物)表面上的微孔空间显着增加。化学活化后复合材料保持高表面积。点零电荷的pH显示在吸附剂表面上的负电荷优势,并且发现吸附是由于Pb 2 + / sup>与生物质表面上的离子扩散之间的强静电力而非常快。木薯果皮展示了从溶液中除去的最高潜力(II)离子除去90.83%的溶液中除去,50〜Mg / L铅浓度和0.3Ω··克/30Ωml的吸附剂/液体比在60℃和pH下7.6。在初始浓度为50Ω·mg / g的初始浓度下记录的最高吸附容量为50Ωmg/ g为50. 1×mg?g,46.6Ωmg/ g和38.5?mg /gδh,δs和r 2 用木薯剥离的吸附值是:12762?j / mol,67.2?j / kmol.k和0.945;对于磨料壳吸附剂,δH,δS和R 2 值是; 36756?j / mol,130?j / mol.k和0.997;虽然对于山药剥离吸附剂,但δh,δs和r 2 值是12163?j / mol,46?j / mol.k和0.9278。因此,吸附过程是可行,自发性和吸热的。 Pb 2 + 的吸附迅速,显示出高动力学性能。实验数据很好地配备了伪二阶动力学模型。然而,本方法具有简单性,耗时较少,最重要的是,低成本的优点。

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