Modification of Grape Pulp With Citric Acid for the Production of Natural Ion Exchanger Resin and Removal of Pb (ii) and Cd (ii) From Aqueous Solutions: Kinetic, Thermodynamics, and Mechanism
| dc.contributor.author | Arslanoğlu, E. | |
| dc.contributor.author | Eren, M.Ş.A. | |
| dc.contributor.author | Arslanoğlu, H. | |
| dc.contributor.author | Çiftçi, H. | |
| dc.date.accessioned | 2023-11-11T08:56:13Z | |
| dc.date.available | 2023-11-11T08:56:13Z | |
| dc.date.issued | 2023 | |
| dc.description.abstract | In this study, grape pulp (MGP) modified with NaOH and citric acid was used in the production of natural ion exchangers. The effects of parameters such as initial pH, MGP dosage, temperature, initial metal ion concentration, and contact time on the removal of Pb (II) and Cd (II) ions from aqueous solutions using modified materials were investigated by batch experiments. It was found that the experimental kinetic data fit the second-order model, and the activation energy for Pb (II) and Cd (II) adsorption processes were 20.68 and 38.61 kj mol−1, respectively. Although the initial adsorption rate increases with increasing temperature, the adsorption efficiency slightly decreases. It was calculated that the equilibrium data fit the Langmuir isotherm better, and the maximum adsorption capacities for Pb (II) and Cd (II) adsorption processes were approximately 1.496 and 1.022 mmol g−1 at 25 °C, respectively. Thermodynamic analysis has shown that the adsorption processes of Pb (II) and Cd (II) are exothermic (ΔH°Pb = −35.68 kj mol−1, ΔH°Cd = −21.19 kj mol−1) and have a self-developing character. Graphical abstract: [Figure not available: see fulltext.]. © 2021, The Author(s), under exclusive licence to Springer-Verlag GmbH Germany, part of Springer Nature. | en_US |
| dc.identifier.doi | 10.1007/s13399-021-01521-x | |
| dc.identifier.issn | 2190-6815 | |
| dc.identifier.issn | 2190-6823 | |
| dc.identifier.scopus | 2-s2.0-85105508240 | |
| dc.identifier.uri | https://doi.org/10.1007/s13399-021-01521-x | |
| dc.identifier.uri | https://hdl.handle.net/11147/14005 | |
| dc.language.iso | en | en_US |
| dc.publisher | Springer Science and Business Media Deutschland GmbH | en_US |
| dc.relation.ispartof | Biomass Conversion and Biorefinery | en_US |
| dc.rights | info:eu-repo/semantics/closedAccess | en_US |
| dc.subject | Adsorption–ion exchange | en_US |
| dc.subject | Desorption | en_US |
| dc.subject | Grape pulp waste | en_US |
| dc.subject | Ion exchange resin | en_US |
| dc.subject | Isotherm–kinetic–thermodynamic | en_US |
| dc.subject | Lead (II) and cadmium (II) removal | en_US |
| dc.subject | Activation energy | en_US |
| dc.subject | Cadmium compounds | en_US |
| dc.subject | Chemicals removal (water treatment) | en_US |
| dc.subject | Citric acid | en_US |
| dc.subject | Ion exchange | en_US |
| dc.subject | Ion exchange resins | en_US |
| dc.subject | Isotherms | en_US |
| dc.subject | Kinetics | en_US |
| dc.subject | Lead compounds | en_US |
| dc.subject | Metal ions | en_US |
| dc.subject | Metals | en_US |
| dc.subject | Sodium hydroxide | en_US |
| dc.subject | Thermoanalysis | en_US |
| dc.subject | Adsorption process | en_US |
| dc.subject | Adsorption–ion exchange | en_US |
| dc.subject | Data fits | en_US |
| dc.subject | Grape pulp waste | en_US |
| dc.subject | Ion-exchange resins | en_US |
| dc.subject | Isotherm–kinetic–thermodynamic | en_US |
| dc.subject | Lead (II) and cadmium (II) removal | en_US |
| dc.subject | Natural ion exchanger | en_US |
| dc.subject | Solution kinetic | en_US |
| dc.subject | Solution thermodynamics | en_US |
| dc.subject | Adsorption | en_US |
| dc.title | Modification of Grape Pulp With Citric Acid for the Production of Natural Ion Exchanger Resin and Removal of Pb (ii) and Cd (ii) From Aqueous Solutions: Kinetic, Thermodynamics, and Mechanism | en_US |
| dc.type | Article | en_US |
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| gdc.description.department | İzmir Institute of Technology | en_US |
| gdc.description.departmenttemp | Arslanoğlu, E., Faculty of Engineering, Department of Chemical Engineering, Atatürk University, Erzurum, Turkey; Eren, M.Ş.A., Faculty of Engineering, Department of Chemical Engineering, Izmir Institute of Technology, İzmir, Turkey; Arslanoğlu, H., Faculty of Engineering and Architecture, Department of Chemical Engineering, Kırşehir Ahi Evran University, Kırşehir, Turkey; Çiftçi, H., Faculty of Medicine, Department of Medical Biochemistry, Kırşehir Ahi Evran University, Kırşehir, Turkey | en_US |
| gdc.description.endpage | 2362 | en_US |
| gdc.description.issue | 3 | en_US |
| gdc.description.publicationcategory | Makale - Uluslararası Hakemli Dergi - Kurum Öğretim Elemanı | en_US |
| gdc.description.scopusquality | Q2 | |
| gdc.description.startpage | 2349 | en_US |
| gdc.description.volume | 13 | en_US |
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| gdc.oaire.keywords | Ion exchange resin | |
| gdc.oaire.keywords | Lead (II) and cadmium (II) removal | |
| gdc.oaire.keywords | Adsorption–ion exchange | |
| gdc.oaire.keywords | Desorption | |
| gdc.oaire.keywords | Isotherm–kinetic–thermodynamic | |
| gdc.oaire.keywords | Grape Pulp Waste | |
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