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Effect of Na(2)CO(3), HF, and CO(2) Treatment on the Regeneration of Exhausted Activated Carbon Used in Sintering Flue Gas

[Image: see text] The method of continuous treatment with Na(2)CO(3) solution, HF solution, and CO(2) was proposed for the regeneration of the exhausted activated carbon (EAC) produced in the sintering flue gas purification process. In order to obtain the optimal operation conditions, the effect of...

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Detalles Bibliográficos
Autores principales: Zheng, Jianlu, Xing, Xiangdong, Pang, Zhuogang, Wang, Sunxuan, Du, Yueli, Lv, Ming
Formato: Online Artículo Texto
Lenguaje:English
Publicado: American Chemical Society 2021
Acceso en línea:https://www.ncbi.nlm.nih.gov/pmc/articles/PMC8495852/
https://www.ncbi.nlm.nih.gov/pubmed/34632232
http://dx.doi.org/10.1021/acsomega.1c04182
Descripción
Sumario:[Image: see text] The method of continuous treatment with Na(2)CO(3) solution, HF solution, and CO(2) was proposed for the regeneration of the exhausted activated carbon (EAC) produced in the sintering flue gas purification process. In order to obtain the optimal operation conditions, the effect of key parameters such as Na(2)CO(3) solution concentration, HF solution concentration, and CO(2) activation temperature on the sulfur conversion rate and regeneration efficiency was analyzed. Also, the N(2) adsorption, Brunauer–Emmett–Teller analysis, scanning electron microscopy-energy dispersive spectrometry, X-ray diffraction, X-ray fluorescence, and Fourier transform infrared spectroscopy were adopted to investigate the deactivation reason and the change of the physical–chemical properties. The results showed that the deactivated EAC was mainly due to the deposition of inorganic compounds such as CaSO(4), SiO(2), and KCl to block the pores. Continuous treatment with Na(2)CO(3) solution and HF solution could remove the inorganic compounds effectively. CO(2) activation treatment further developed the blocked porosity and decreased the surface acidity. The optimal conditions for the regeneration of EAC were a Na(2)CO(3) concentration of 0.5 mol/L, an HF concentration of 0.8 mol/L, and a CO(2) activation temperature of 1073 K with the activation time of 1 h, corresponding to the specific surface area of 607.91m(2)/g. In the fourth regeneration cycle, the adsorption performance during the successive adsorption–regeneration process could still maintain a high level and the regeneration efficiency was 95.31%.