Removal of copper(II) from aqueous solution by pine and base modified pine cone powder as biosorbent
Pine cone, a popular agricultural waste in South Africa has been studied for its potential application as a biosorbent in its raw and sodium hydroxide modified form. Surface modification were carried out using sodium hydroxide solution of concentration ranging from 0.01 to 0.15 mol L −1and the sampl...
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Veröffentlicht in: | Journal of hazardous materials 2009-09, Vol.168 (2), p.909-917 |
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creator | Ofomaja, A.E. Naidoo, E.B. Modise, S.J. |
description | Pine cone, a popular agricultural waste in South Africa has been studied for its potential application as a biosorbent in its raw and sodium hydroxide modified form. Surface modification were carried out using sodium hydroxide solution of concentration ranging from 0.01 to 0.15
mol
L
−1and the samples characterized. Batch kinetics were carried out on the biosorption of copper(II) from aqueous solution using the prepared samples and varying biosorption parameters such as solution pH, dose and biosorption temperature.
The results revealed that pine cone surface was modified by sodium hydroxide treatment, carboxylic and phenolic functional groups were mostly affected as seen from Boehm's titration and FTIR analysis. Surface modification reduced pH
PZC from 7.49 to 2.55 and also increased the internal surface of pine cone powder. Copper(II) biosorption studies revealed that optimum solution pH and biosorbent dose for copper(II) removal was pH 5 and 8.0
g
L
−1, for the untreated and treated samples. Copper(II) uptake followed the pseudo-second order kinetic model and the intraparticle diffusion model. Copper(II) removal increased with NaOH modification and higher NaOH concentration.
Biosorption temperature was found to increase copper(II) uptake for all samples indicating that copper(II) biosorption is endothermic in nature. Activation energy computed from the pseudo-second order rate constant increased with NaOH modification from 18.22 to 21.39
kJ
mol
−1. The thermodynamic parameters of activation (Δ
G*, Δ
H* and Δ
S*) were computed using Erying equation and the results show that the reorientation step is mostly entropy controlled at the activation state and the contribution of entropy to the reorientation step of activation tends to decrease with NaOH washing and with increase in NaOH concentration. |
doi_str_mv | 10.1016/j.jhazmat.2009.02.106 |
format | Article |
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mol
L
−1and the samples characterized. Batch kinetics were carried out on the biosorption of copper(II) from aqueous solution using the prepared samples and varying biosorption parameters such as solution pH, dose and biosorption temperature.
The results revealed that pine cone surface was modified by sodium hydroxide treatment, carboxylic and phenolic functional groups were mostly affected as seen from Boehm's titration and FTIR analysis. Surface modification reduced pH
PZC from 7.49 to 2.55 and also increased the internal surface of pine cone powder. Copper(II) biosorption studies revealed that optimum solution pH and biosorbent dose for copper(II) removal was pH 5 and 8.0
g
L
−1, for the untreated and treated samples. Copper(II) uptake followed the pseudo-second order kinetic model and the intraparticle diffusion model. Copper(II) removal increased with NaOH modification and higher NaOH concentration.
Biosorption temperature was found to increase copper(II) uptake for all samples indicating that copper(II) biosorption is endothermic in nature. Activation energy computed from the pseudo-second order rate constant increased with NaOH modification from 18.22 to 21.39
kJ
mol
−1. The thermodynamic parameters of activation (Δ
G*, Δ
H* and Δ
S*) were computed using Erying equation and the results show that the reorientation step is mostly entropy controlled at the activation state and the contribution of entropy to the reorientation step of activation tends to decrease with NaOH washing and with increase in NaOH concentration.</description><identifier>ISSN: 0304-3894</identifier><identifier>EISSN: 1873-3336</identifier><identifier>DOI: 10.1016/j.jhazmat.2009.02.106</identifier><identifier>PMID: 19386418</identifier><identifier>CODEN: JHMAD9</identifier><language>eng</language><publisher>Kidlington: Elsevier B.V</publisher><subject>Activation energy ; Adsorption ; Agriculture, rearing and food industries wastes ; Applied sciences ; Biological and medical sciences ; Biosorption temperature ; Biotechnology ; Copper - isolation & purification ; Exact sciences and technology ; Fundamental and applied biological sciences. Psychology ; Hydrogen-Ion Concentration ; Kinetics ; Methods. Procedures. Technologies ; Others ; Pine cone powder ; Pinus ; Pollution ; Pseudo-second order kinetics ; Sodium Hydroxide - chemistry ; Sodium hydroxide modification ; Solutions ; Thermodynamics ; Various methods and equipments ; Wastes ; Water</subject><ispartof>Journal of hazardous materials, 2009-09, Vol.168 (2), p.909-917</ispartof><rights>2009 Elsevier B.V.</rights><rights>2009 INIST-CNRS</rights><lds50>peer_reviewed</lds50><woscitedreferencessubscribed>false</woscitedreferencessubscribed><citedby>FETCH-LOGICAL-c455t-a477d25e9c657797b10a2c7868b40751972ba35ad1afbc682486c148efab369a3</citedby><cites>FETCH-LOGICAL-c455t-a477d25e9c657797b10a2c7868b40751972ba35ad1afbc682486c148efab369a3</cites></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><linktohtml>$$Uhttps://dx.doi.org/10.1016/j.jhazmat.2009.02.106$$EHTML$$P50$$Gelsevier$$H</linktohtml><link.rule.ids>314,780,784,3549,27923,27924,45994</link.rule.ids><backlink>$$Uhttp://pascal-francis.inist.fr/vibad/index.php?action=getRecordDetail&idt=21727624$$DView record in Pascal Francis$$Hfree_for_read</backlink><backlink>$$Uhttps://www.ncbi.nlm.nih.gov/pubmed/19386418$$D View this record in MEDLINE/PubMed$$Hfree_for_read</backlink></links><search><creatorcontrib>Ofomaja, A.E.</creatorcontrib><creatorcontrib>Naidoo, E.B.</creatorcontrib><creatorcontrib>Modise, S.J.</creatorcontrib><title>Removal of copper(II) from aqueous solution by pine and base modified pine cone powder as biosorbent</title><title>Journal of hazardous materials</title><addtitle>J Hazard Mater</addtitle><description>Pine cone, a popular agricultural waste in South Africa has been studied for its potential application as a biosorbent in its raw and sodium hydroxide modified form. Surface modification were carried out using sodium hydroxide solution of concentration ranging from 0.01 to 0.15
mol
L
−1and the samples characterized. Batch kinetics were carried out on the biosorption of copper(II) from aqueous solution using the prepared samples and varying biosorption parameters such as solution pH, dose and biosorption temperature.
The results revealed that pine cone surface was modified by sodium hydroxide treatment, carboxylic and phenolic functional groups were mostly affected as seen from Boehm's titration and FTIR analysis. Surface modification reduced pH
PZC from 7.49 to 2.55 and also increased the internal surface of pine cone powder. Copper(II) biosorption studies revealed that optimum solution pH and biosorbent dose for copper(II) removal was pH 5 and 8.0
g
L
−1, for the untreated and treated samples. Copper(II) uptake followed the pseudo-second order kinetic model and the intraparticle diffusion model. Copper(II) removal increased with NaOH modification and higher NaOH concentration.
Biosorption temperature was found to increase copper(II) uptake for all samples indicating that copper(II) biosorption is endothermic in nature. Activation energy computed from the pseudo-second order rate constant increased with NaOH modification from 18.22 to 21.39
kJ
mol
−1. The thermodynamic parameters of activation (Δ
G*, Δ
H* and Δ
S*) were computed using Erying equation and the results show that the reorientation step is mostly entropy controlled at the activation state and the contribution of entropy to the reorientation step of activation tends to decrease with NaOH washing and with increase in NaOH concentration.</description><subject>Activation energy</subject><subject>Adsorption</subject><subject>Agriculture, rearing and food industries wastes</subject><subject>Applied sciences</subject><subject>Biological and medical sciences</subject><subject>Biosorption temperature</subject><subject>Biotechnology</subject><subject>Copper - isolation & purification</subject><subject>Exact sciences and technology</subject><subject>Fundamental and applied biological sciences. Psychology</subject><subject>Hydrogen-Ion Concentration</subject><subject>Kinetics</subject><subject>Methods. Procedures. Technologies</subject><subject>Others</subject><subject>Pine cone powder</subject><subject>Pinus</subject><subject>Pollution</subject><subject>Pseudo-second order kinetics</subject><subject>Sodium Hydroxide - chemistry</subject><subject>Sodium hydroxide modification</subject><subject>Solutions</subject><subject>Thermodynamics</subject><subject>Various methods and equipments</subject><subject>Wastes</subject><subject>Water</subject><issn>0304-3894</issn><issn>1873-3336</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2009</creationdate><recordtype>article</recordtype><sourceid>EIF</sourceid><recordid>eNqFkcuKFDEUhoMoTjv6CEo2ii6qzT2p1SCDl4aBgWFch5NLYZqqSplUj8w8vdV0ocvenAM_37n-CL2lZEsJVZ_32_0veBpg3jJC2i1hi6yeoQ01mjecc_UcbQgnouGmFRfoVa17QgjVUrxEF7TlRglqNijcxSE_QI9zh32eplg-7nafcFfygOH3IeZDxTX3hznlEbtHPKUxYhgDdlAjHnJIXYrhJPu8hCn_CbFgqNilXHNxcZxfoxcd9DW-WfMl-vnt6_31j-bm9vvu-stN44WUcwNC68BkbL2SWrfaUQLMa6OME0RL2mrmgEsIFDrnlWHCKE-FiR04rlrgl-jDqe9U8rJ7ne2Qqo99D-PxEKu04FIycxbkQnKimToLMqKFkVQuoDyBvuRaS-zsVNIA5dFSYo-G2b1dDbNHwyxhi3wc8G4dcHBDDP-rVocW4P0KQPXQdwVGn-o_jlHNtGJi4a5OXFwe_JBisdWnOPoYUol-tiGnM6v8BVAjtfo</recordid><startdate>20090915</startdate><enddate>20090915</enddate><creator>Ofomaja, A.E.</creator><creator>Naidoo, E.B.</creator><creator>Modise, S.J.</creator><general>Elsevier B.V</general><general>Elsevier</general><scope>IQODW</scope><scope>CGR</scope><scope>CUY</scope><scope>CVF</scope><scope>ECM</scope><scope>EIF</scope><scope>NPM</scope><scope>AAYXX</scope><scope>CITATION</scope><scope>7ST</scope><scope>7U7</scope><scope>C1K</scope><scope>SOI</scope><scope>8FD</scope><scope>FR3</scope><scope>KR7</scope><scope>7X8</scope></search><sort><creationdate>20090915</creationdate><title>Removal of copper(II) from aqueous solution by pine and base modified pine cone powder as biosorbent</title><author>Ofomaja, A.E. ; Naidoo, E.B. ; Modise, S.J.</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-c455t-a477d25e9c657797b10a2c7868b40751972ba35ad1afbc682486c148efab369a3</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>2009</creationdate><topic>Activation energy</topic><topic>Adsorption</topic><topic>Agriculture, rearing and food industries wastes</topic><topic>Applied sciences</topic><topic>Biological and medical sciences</topic><topic>Biosorption temperature</topic><topic>Biotechnology</topic><topic>Copper - isolation & purification</topic><topic>Exact sciences and technology</topic><topic>Fundamental and applied biological sciences. Psychology</topic><topic>Hydrogen-Ion Concentration</topic><topic>Kinetics</topic><topic>Methods. Procedures. Technologies</topic><topic>Others</topic><topic>Pine cone powder</topic><topic>Pinus</topic><topic>Pollution</topic><topic>Pseudo-second order kinetics</topic><topic>Sodium Hydroxide - chemistry</topic><topic>Sodium hydroxide modification</topic><topic>Solutions</topic><topic>Thermodynamics</topic><topic>Various methods and equipments</topic><topic>Wastes</topic><topic>Water</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Ofomaja, A.E.</creatorcontrib><creatorcontrib>Naidoo, E.B.</creatorcontrib><creatorcontrib>Modise, S.J.</creatorcontrib><collection>Pascal-Francis</collection><collection>Medline</collection><collection>MEDLINE</collection><collection>MEDLINE (Ovid)</collection><collection>MEDLINE</collection><collection>MEDLINE</collection><collection>PubMed</collection><collection>CrossRef</collection><collection>Environment Abstracts</collection><collection>Toxicology Abstracts</collection><collection>Environmental Sciences and Pollution Management</collection><collection>Environment Abstracts</collection><collection>Technology Research Database</collection><collection>Engineering Research Database</collection><collection>Civil Engineering Abstracts</collection><collection>MEDLINE - Academic</collection><jtitle>Journal of hazardous materials</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Ofomaja, A.E.</au><au>Naidoo, E.B.</au><au>Modise, S.J.</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Removal of copper(II) from aqueous solution by pine and base modified pine cone powder as biosorbent</atitle><jtitle>Journal of hazardous materials</jtitle><addtitle>J Hazard Mater</addtitle><date>2009-09-15</date><risdate>2009</risdate><volume>168</volume><issue>2</issue><spage>909</spage><epage>917</epage><pages>909-917</pages><issn>0304-3894</issn><eissn>1873-3336</eissn><coden>JHMAD9</coden><abstract>Pine cone, a popular agricultural waste in South Africa has been studied for its potential application as a biosorbent in its raw and sodium hydroxide modified form. Surface modification were carried out using sodium hydroxide solution of concentration ranging from 0.01 to 0.15
mol
L
−1and the samples characterized. Batch kinetics were carried out on the biosorption of copper(II) from aqueous solution using the prepared samples and varying biosorption parameters such as solution pH, dose and biosorption temperature.
The results revealed that pine cone surface was modified by sodium hydroxide treatment, carboxylic and phenolic functional groups were mostly affected as seen from Boehm's titration and FTIR analysis. Surface modification reduced pH
PZC from 7.49 to 2.55 and also increased the internal surface of pine cone powder. Copper(II) biosorption studies revealed that optimum solution pH and biosorbent dose for copper(II) removal was pH 5 and 8.0
g
L
−1, for the untreated and treated samples. Copper(II) uptake followed the pseudo-second order kinetic model and the intraparticle diffusion model. Copper(II) removal increased with NaOH modification and higher NaOH concentration.
Biosorption temperature was found to increase copper(II) uptake for all samples indicating that copper(II) biosorption is endothermic in nature. Activation energy computed from the pseudo-second order rate constant increased with NaOH modification from 18.22 to 21.39
kJ
mol
−1. The thermodynamic parameters of activation (Δ
G*, Δ
H* and Δ
S*) were computed using Erying equation and the results show that the reorientation step is mostly entropy controlled at the activation state and the contribution of entropy to the reorientation step of activation tends to decrease with NaOH washing and with increase in NaOH concentration.</abstract><cop>Kidlington</cop><pub>Elsevier B.V</pub><pmid>19386418</pmid><doi>10.1016/j.jhazmat.2009.02.106</doi><tpages>9</tpages></addata></record> |
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source | Elsevier ScienceDirect Journals Complete - AutoHoldings; MEDLINE |
subjects | Activation energy Adsorption Agriculture, rearing and food industries wastes Applied sciences Biological and medical sciences Biosorption temperature Biotechnology Copper - isolation & purification Exact sciences and technology Fundamental and applied biological sciences. Psychology Hydrogen-Ion Concentration Kinetics Methods. Procedures. Technologies Others Pine cone powder Pinus Pollution Pseudo-second order kinetics Sodium Hydroxide - chemistry Sodium hydroxide modification Solutions Thermodynamics Various methods and equipments Wastes Water |
title | Removal of copper(II) from aqueous solution by pine and base modified pine cone powder as biosorbent |
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