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碳纳米管浸渍无烟煤(An/CNT)作为一种用于去除偶氮染料的优质吸附剂。

Carbon nanotube impregnated anthracite (An/CNT) as a superior sorbent for azo dye removal.

作者信息

Mohamed Fathy M, Li Zhaohui, Zayed Ahmed M

机构信息

Water and Environment Department, Faculty of Earth Sciences, Beni-Suef University Egypt.

Geosciences Department, University of Wisconsin - Parkside Kenosha WI 53144 USA.

出版信息

RSC Adv. 2020 Jul 7;10(43):25586-25601. doi: 10.1039/d0ra03869e. eCollection 2020 Jul 3.

Abstract

Raw anthracite was impregnated with a minute amount of multi-walled carbon-nanotubes at a solid/solid ratio of 50 : 1 calcination at 950 °C for 2 h to produce anthracite/carbon nanotube (An/CNT) composite with superior sorption efficiency. Both An/CNT composite and its precursor anthracite were characterized by XRD, SEM, FT-IR and BET surface area ( ). The removal efficiency of an azo dye methyl orange (MO) by the An/CNT composite was evaluated under different experimental parameters. The MO sorption isotherm data fitted to the Langmuir model well with an of 0.999 and a MO sorption capacity ( ) of 416.7 mg g. The distribution coefficient decreases from 117.9 to 16.1 L g as the initial MO concentrations increased from 40 to 140 mg L. The MO sorption kinetic data was well described by the pseudo-second-order equation with an of 1. The external (film) diffusion followed by intra-particle diffusion was the major driving process during the early stage of MO sorption. The electrostatic interaction between the oxygen- and nitrogen-bearing functional groups on the An/CNT surface and MO ions was the key controlling mechanism for the MO sorption process, particularly at pH < pH of the composite. Meanwhile, valuable contributions from Yoshida and dipole-dipole H bonding mechanisms can explain the MO sorption by the addressed composite, especially at pH > pH.

摘要

将微量多壁碳纳米管以50∶1的固/固比浸渍到原煤中,在950℃下煅烧2小时,以制备具有优异吸附效率的无烟煤/碳纳米管(An/CNT)复合材料。通过XRD、SEM、FT-IR和BET表面积( )对An/CNT复合材料及其前驱体无烟煤进行了表征。在不同实验参数下评估了An/CNT复合材料对偶氮染料甲基橙(MO)的去除效率。MO吸附等温线数据与Langmuir模型拟合良好,相关系数为0.999,MO吸附容量( )为416.7 mg/g。随着初始MO浓度从40 mg/L增加到140 mg/L,分配系数 从117.9 L/g降至16.1 L/g。MO吸附动力学数据用伪二级方程很好地描述,相关系数为1。在MO吸附的早期阶段,外部(膜)扩散随后是颗粒内扩散是主要的驱动过程。An/CNT表面含氧化合物和含氮官能团与MO离子之间的静电相互作用是MO吸附过程的关键控制机制,特别是在pH <复合材料的pH时。同时,吉田和偶极-偶极氢键机制的重要贡献可以解释所研究复合材料对MO的吸附,特别是在pH > pH时。

https://cdn.ncbi.nlm.nih.gov/pmc/blobs/ca37/9055319/f28c4f6a971c/d0ra03869e-f1.jpg

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