4.7 Article

Selenate removal via continuous fixed-bed column with nanoscale zero-valent iron supported on bentonite-zeolite pellets

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DOI: 10.1016/j.jwpe.2023.103843

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Bentonite-zeolite; Fixed -bed column; Nanoscale zero-valent iron; Selenate; Selenium

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Excessive levels of selenium in water are mainly caused by fossil fuels combustion, coal-fired power plant activity, and mining operations. Selenium contamination poses significant risks to human health. Zeolite-supported nanoscale zero-valent iron coated onto bentonite-zeolite pellets has shown promising potential for the removal of selenium in contaminated water.
Excessive levels of selenium in water are caused by discharging from fossil fuels combustion, coal-fired power plant activity, and mining operations. Selenium contamination poses considerable hazards to human health. Selenate (Se6+) is the most oxidized and common form of selenium in contaminated water. Zeolite-supported nanoscale zero-valent iron (Z-NZVI) coated onto bentonite-zeolite pellets (BZ-NZVI) was prepared for the removal of Se6+. The BZ pellets were coated with Z-NZVI powder at a ratio of 1:5. The BZ-NZVI was characterized using X-ray diffraction, point of zero charge analysis, Brunauer-Emmett-Teller method, field emission scanning electron microscopy, and X-ray fluorescence spectrometry techniques. The BZ-NZVI samples were tested in the batch reactor for kinetics and adsorption isotherm studies and subsequently in a continuous fixedbed column. The kinetic models and adsorption isotherms were best described by the pseudo-first-order kinetics and Langmuir adsorption isotherm, respectively. Both boundary layer diffusion and intraparticle diffusion appeared to affect the intraparticle diffusion process. The efficiency of Se6+ removal in fixed-bed column of BZNZVI fitted well with Yoon-Nelson model. The adsorption rate decreased according to the Se6+ breakthrough proportion. The maximum Se6+ adsorption breakthrough capacity was 0.034 mg/g under the test run of 0.5 mg/ L-Se6+ solution, pH 7, the flow rate of 5 mL/min, and the temperature of 303 K. Breakthrough times increased with decreasing flow rate and Se6+ initial concentration but decreased as the mass of BZ-NZVI increased. Se6+ contaminated in wastewater was removed by reduction and adsorption mechanisms over BZ-NZVI, which is a promising new area of research.

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