Khairuddin Khairuddin , Muhammad Akbar Ridhawansa , Ruslan Ruslan , Bambang Sardi
{"title":"Efficient activation of bentonite clay for cyanide adsorption using sulfuric acid and sodium ion intercalation","authors":"Khairuddin Khairuddin , Muhammad Akbar Ridhawansa , Ruslan Ruslan , Bambang Sardi","doi":"10.1016/j.clwas.2025.100225","DOIUrl":null,"url":null,"abstract":"<div><div>This study aims to investigate the most effective way to activate bentonite clay using H<sub>2</sub>SO<sub>4</sub> and Na<sup>+</sup> intercalation. The outcomes were assessed using XRD, XRF, and FTIR analyses. The adsorption process was carried out in batches, and the cyanide adsorbate solution was analyzed using UV–VIS spectrophotometry and a ninhydrin reagent. The optimal concentration of H<sub>2</sub>SO<sub>4</sub> was established at 1.5 M, whereas the ideal pH for cyanide was identified as 10.2. XRD analysis provided insights into the Miller indices (d<sub>hkl</sub>) of mineral components, variations in crystallinity, shifts in 2Ɵ, and a decrease in basal spacing. The FTIR analysis showed vibrations associated with the hydroxyl group, methylenes, carbonate, water-related vibrations, silica-related groups, and metal-oxygen bonds. These findings confirmed the chemical structure and composition of the activated bentonite clay after treatment. XRF analysis revealed a decrease in the concentrations (wt%) of SiO<sub>2</sub>, Fe<sub>2</sub>O<sub>3</sub>, CaO, TiO<sub>2</sub>, and other impurities, as well as an increase in K<sub>2</sub>O, compared to the pre-intercalation and pure states. During the post-cyanide adsorption phase, the -OH wavenumber shifted to the left, and the intensity of -CN decreased due to competition between CO<sub>3</sub><sup>2-</sup> ions in the adsorbate and CN<sup>-</sup> ion adsorbate, limited contact time, and suboptimal pH conditions. Under optimal pH conditions, the H-OH wavenumber shifted to the left, the -OH intensity decreased, and the -CN intensity increased for cyanide removal from water.</div></div>","PeriodicalId":100256,"journal":{"name":"Cleaner Waste Systems","volume":"10 ","pages":"Article 100225"},"PeriodicalIF":0.0000,"publicationDate":"2025-02-06","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":"0","resultStr":null,"platform":"Semanticscholar","paperid":null,"PeriodicalName":"Cleaner Waste Systems","FirstCategoryId":"1085","ListUrlMain":"https://www.sciencedirect.com/science/article/pii/S2772912525000235","RegionNum":0,"RegionCategory":null,"ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":null,"EPubDate":"","PubModel":"","JCR":"","JCRName":"","Score":null,"Total":0}
引用次数: 0
Abstract
This study aims to investigate the most effective way to activate bentonite clay using H2SO4 and Na+ intercalation. The outcomes were assessed using XRD, XRF, and FTIR analyses. The adsorption process was carried out in batches, and the cyanide adsorbate solution was analyzed using UV–VIS spectrophotometry and a ninhydrin reagent. The optimal concentration of H2SO4 was established at 1.5 M, whereas the ideal pH for cyanide was identified as 10.2. XRD analysis provided insights into the Miller indices (dhkl) of mineral components, variations in crystallinity, shifts in 2Ɵ, and a decrease in basal spacing. The FTIR analysis showed vibrations associated with the hydroxyl group, methylenes, carbonate, water-related vibrations, silica-related groups, and metal-oxygen bonds. These findings confirmed the chemical structure and composition of the activated bentonite clay after treatment. XRF analysis revealed a decrease in the concentrations (wt%) of SiO2, Fe2O3, CaO, TiO2, and other impurities, as well as an increase in K2O, compared to the pre-intercalation and pure states. During the post-cyanide adsorption phase, the -OH wavenumber shifted to the left, and the intensity of -CN decreased due to competition between CO32- ions in the adsorbate and CN- ion adsorbate, limited contact time, and suboptimal pH conditions. Under optimal pH conditions, the H-OH wavenumber shifted to the left, the -OH intensity decreased, and the -CN intensity increased for cyanide removal from water.