Adsorptive Separation of Lead (Pb2+) from Aqueous Solution Using Tri-n-octylamine Supported Montmorillonite
dc.authorid | Datta, Dipaloy/0000-0002-2048-9064 | |
dc.contributor.author | Datta, Dipaloy | |
dc.contributor.author | Uslu, Hasan | |
dc.date.accessioned | 2025-03-26T17:35:10Z | |
dc.date.available | 2025-03-26T17:35:10Z | |
dc.date.issued | 2017 | |
dc.department | İstanbul Esenyurt Üniversitesi | |
dc.description.abstract | Divalent lead present in the water stream was removed by using adsorption techniques with montmorillonite clay (Mt) modified with tri-n-octylamine (Mt-TOA). Batch adsorption data at equilibrium were determined with different initial Pb2+ ions concentration (8, 10, 12, 14, and 16 mg.L-1) in the aqueous solution at 298 K, and these results were correlated by using three different isotherm models, for instance, the Langmuir, the Freundlich, and the Temkin. The two-parameter Langmuir model was the best fit to the equilibrium data with a coefficient (R-2) greater than 0.99. The maximum capacities for monolayer adsorption of Mt and Mt-TOA were determined to be 3.37 mg.g(-1) and 33.1 mg.g(-1), respectively, as estimated from Langmuir. Also, experimental values were generated to evaluate the influence of adsorbent amount (w, 0.05-0.3 g for Mt, 0.01-0.06 g for Mt-TOA), starting Pb2+ ion concentration (C-0,8 mg.L-1 to 16 mg.L-1), pH (between 1 and 9), and contact period (t, from 10 to 110 min) on the removal effectiveness and adsorption capability of Mt and Mt-TOA adsorbents. In respect to kinetic studies, the removal efficiency of Pb2+ ion reached to a fixed value of 81.42% with Mt (0.1 g) and 80.67% by Mt-TOA (0.01 g) next 100 and 80 min, respectively. Pseudo-first order, pseudo-second order, and intraparticle diffusion models were studied to obtain the kinetic parameters of the adsorption practice. It is observed that the rate of mass transfer of Pb2+ ions was mainly governed by the intraparticle diffusion mechanism. | |
dc.identifier.doi | 10.1021/acs.jced.6b00716 | |
dc.identifier.endpage | 375 | |
dc.identifier.issn | 0021-9568 | |
dc.identifier.issue | 1 | |
dc.identifier.scopus | 2-s2.0-85024832326 | |
dc.identifier.scopusquality | Q2 | |
dc.identifier.startpage | 370 | |
dc.identifier.uri | https://doi.org/10.1021/acs.jced.6b00716 | |
dc.identifier.uri | https://hdl.handle.net/20.500.14704/1082 | |
dc.identifier.volume | 62 | |
dc.identifier.wos | WOS:000392035300042 | |
dc.identifier.wosquality | Q2 | |
dc.indekslendigikaynak | Web of Science | |
dc.indekslendigikaynak | Scopus | |
dc.language.iso | en | |
dc.publisher | Amer Chemical Soc | |
dc.relation.ispartof | Journal of Chemical and Engineering Data | |
dc.relation.publicationcategory | Makale - Uluslararası Hakemli Dergi - Kurum Öğretim Elemanı | |
dc.rights | info:eu-repo/semantics/closedAccess | |
dc.snmz | KA_WOS_20250326 | |
dc.subject | Activated Carbon; Heavy-Metals; Chromium Vi; Removal; Adsorbent; Ions; Sorption; Kinetics; Pb(Ii); Copper | |
dc.title | Adsorptive Separation of Lead (Pb2+) from Aqueous Solution Using Tri-n-octylamine Supported Montmorillonite | |
dc.type | Article |