Centro de Investigación y Estudios de Posgrado, Facultad de Ciencias Químicas, UASLP, Av. Dr. Manuel Nava No. 6, SLP 78210, San Luis Potosí, México.
POR2E Group, CEMHTI (UPR 3079) CNRS, Univ. Orléans, Orléans, France.
Environ Sci Pollut Res Int. 2019 Feb;26(6):6141-6152. doi: 10.1007/s11356-018-3991-x. Epub 2019 Jan 7.
A series of activated carbons (ACs) were prepared by modifying a commercial AC by physical activation using CO during different activation times. The ACs were designated as F, F12, F24, and F40 corresponding to the activation times of 0, 12, 24, and 40 h, respectively. The surface area, total pore volume, micropore volume, and mean micropore width were determined for all the ACs. The textural properties of the modified ACs increased substantially with the activation time, and the capacity of the ACs for adsorbing diclofenac (DCF) was almost linearly dependent upon the surface area of the ACS. The maximum adsorption capacities of F, F12, F24, and F40 carbons towards diclofenac (DCF) from aqueous solution were 271, 522, 821, and 1033 mg/g, respectively. Hence, the adsorption capacities of ACs were considerably enhanced with the activation time, and F12, F24, and F40 carbons presented the highest adsorption capacities towards DCF reported in the technical literature. The F40 adsorption capacity was at least twice those of other carbon materials. The adsorption capacities decreased by raising the pH from 7 to 11 due to electrostatic repulsion between the ACs surface and anionic DCF in solution. The removal of DCF from a wastewater treatment plant (WWTP) effluent was effectively carried out by adsorption on F40. Hence, the capacity of ACs for adsorbing DCF can be optimized by tailoring the porous structure of ACs.
一系列活性炭(AC)通过在不同的活化时间下使用 CO 进行物理活化来制备。这些 AC 分别被命名为 F、F12、F24 和 F40,对应于 0、12、24 和 40 h 的活化时间。所有 AC 的比表面积、总孔体积、微孔体积和平均微孔宽度都进行了测定。改性 AC 的比表面积和总孔体积随着活化时间的增加而显著增加,AC 对双氯芬酸(DCF)的吸附能力几乎与 ACS 的比表面积呈线性相关。F、F12、F24 和 F40 碳对水溶液中双氯芬酸(DCF)的最大吸附容量分别为 271、522、821 和 1033 mg/g。因此,AC 的吸附容量随着活化时间的增加而显著提高,F12、F24 和 F40 碳对 DCF 的吸附容量在技术文献中报道的是最高的。F40 的吸附容量至少是其他碳材料的两倍。由于 AC 表面和溶液中阴离子 DCF 之间的静电排斥,吸附容量随着 pH 值从 7 升高到 11 而降低。因此,通过在 F40 上吸附,有效地从污水处理厂(WWTP)废水中去除了 DCF。因此,可以通过调整 AC 的多孔结构来优化 AC 对 DCF 的吸附能力。