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在间歇模式下使用化学活化枣核炭去除合成废水中的亮绿染料。

Removal of brilliant green dye from synthetic wastewater under batch mode using chemically activated date pit carbon.

作者信息

Mansour Ramadan Abd El-Ghany, Simeda Mohamed Gamal, Zaatout Ahmed Amin

机构信息

Basic Sciences and Engineering Department, Higher Institute of Engineering and Technology New Damietta Egypt

Chemical Engineering Department, Higher Institute of Engineering and Technology New Damietta Egypt

出版信息

RSC Adv. 2021 Feb 17;11(14):7851-7861. doi: 10.1039/d0ra08488c.

Abstract

In this research, a single-stage batch adsorber was designed for removal of brilliant green dye (BG) from aqueous solutions using activated carbon derived from date pits (ADPC) based on the Freundlich isotherm which was the best-fitted isotherm model. Experimental work was carried out within the range of 10-50 ppm initial dye concentration to determine the optimum operating conditions which were 55 min contact time, 0.06 g adsorbent mass, 25 °C, and pH = 8. Process kinetics was best-fitted with the pseudo-second order model, which revealed that the intra-particle diffusion stage is the rate-controlling stage for the process. The process efficiency was assessed by infrared spectroscopy (FTIR), scanning microscopy (SEM), X-ray spectroscopy (EDXS), and Brunauer-Emmett-Teller (BET) where the latter showed that the specific surface area of the adsorbent is 311.38 m g, which gives a favorable maximum monolayer adsorption capacity (77.8 mg g). The thermodynamic study proved that BG adsorption on ADPC was physiosorptive (Δ = -5.86 kJ mol) and spontaneous at low temperature (Δ = -17.7 kJ mol, Δ = -0.04 kJ mol K).

摘要

在本研究中,基于弗伦德利希等温线(该等温线模型拟合效果最佳),设计了一种单级间歇吸附器,用于使用枣核衍生的活性炭(ADPC)从水溶液中去除亮绿染料(BG)。实验工作在初始染料浓度为10 - 50 ppm的范围内进行,以确定最佳操作条件,即接触时间55分钟、吸附剂质量0.06 g、温度25°C和pH = 8。过程动力学与伪二级模型拟合效果最佳,这表明颗粒内扩散阶段是该过程的速率控制阶段。通过红外光谱(FTIR)、扫描显微镜(SEM)、X射线光谱(EDXS)和布鲁诺尔-埃米特-泰勒(BET)对过程效率进行了评估,其中BET表明吸附剂的比表面积为311.38 m²/g,这给出了良好的最大单层吸附容量(77.8 mg/g)。热力学研究证明,BG在ADPC上的吸附是物理吸附(ΔH = -5.86 kJ/mol),并且在低温下是自发的(ΔG = -17.7 kJ/mol,ΔS = -0.04 kJ/mol·K)。

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