Nickel recycling through bioleaching of a Ni/Al2O3 commercial catalyst

dc.contributor.authorTayar, Samir Prioto [UNESP]
dc.contributor.authorYeste, Maria Pilar
dc.contributor.authorRamirez, Martin
dc.contributor.authorCabrera, Gema
dc.contributor.authorBevilaqua, Denise [UNESP]
dc.contributor.authorGatica, Jose Manuel
dc.contributor.authorVidal, Hilario
dc.contributor.authorCauqui, Miguel Angel
dc.contributor.authorCantero, Domingo
dc.contributor.institutionUniversidade Estadual Paulista (Unesp)
dc.contributor.institutionUniv Cadiz
dc.date.accessioned2020-12-10T17:37:22Z
dc.date.available2020-12-10T17:37:22Z
dc.date.issued2020-08-01
dc.description.abstractBioleaching studies were carried out on a commercial nickel-based reforming catalyst using two acidophilic bacteria (Acidithiobacillus ferrooxidans and Acidithiobacillus thiooxidans) under several types of bioleaching mode (one-step, two-step and spent medium-step) and catalyst pretreatment (with and without reduction). The highest percentage of nickel extraction was achieved using A. thiooxidans under spent medium-step (94.4 +/- 0.1%). The percentage of nickel extracted was constant (85.6 +/- 3.9%) up to a pulp density of 5% w v(-1), and it decreased at higher pulp densities due to acid depletion. In order to assess the potential reuse of the recovered metal, the nickel solution obtained by bioleaching was recycled by using it to prepare a new Ni/Al2O3 catalyst by impregnation of a commercial alumina support. Characterization of the catalyst prepared from recycled nickel showed that it had a high purity along with a suitable texture and metallic dispersion. Indeed, the activity of the new catalyst in the dry reforming of methane provided a high conversion of methane (99%) with good stability over time under the experimental conditions employed.en
dc.description.affiliationSao Paulo State Univ, Inst Chem, UNESP, BR-14800900 Araraquara, SP, Brazil
dc.description.affiliationUniv Cadiz, Dept Mat Sci Met Engn & Inorgan Chem, Cadiz 11510, Spain
dc.description.affiliationUniv Cadiz, Inst Electron Microscopy & Mat IMEYMAT, Fac Sci, Cadiz 11510, Spain
dc.description.affiliationUniv Cadiz, Inst Univ Invest Vitivinicola & Agroalimentario I, Fac Sci, Dept Chem Engn & Food Technol, Cadiz 11510, Spain
dc.description.affiliationUnespSao Paulo State Univ, Inst Chem, UNESP, BR-14800900 Araraquara, SP, Brazil
dc.description.sponsorshipSpanish Government (Ministerio de Economia y Competitividad)
dc.description.sponsorshipJunta de Andalucia
dc.description.sponsorshipIdSpanish Government (Ministerio de Economia y Competitividad): CTM2016-79089-R
dc.description.sponsorshipIdSpanish Government (Ministerio de Economia y Competitividad): MAT2017-87579-R
dc.description.sponsorshipIdJunta de Andalucia: TEP-105
dc.description.sponsorshipIdJunta de Andalucia: FQM-110
dc.format.extent8
dc.identifierhttp://dx.doi.org/10.1016/j.hydromet.2020.105350
dc.identifier.citationHydrometallurgy. Amsterdam: Elsevier, v. 195, 8 p., 2020.
dc.identifier.doi10.1016/j.hydromet.2020.105350
dc.identifier.issn0304-386X
dc.identifier.urihttp://hdl.handle.net/11449/195519
dc.identifier.wosWOS:000549135400003
dc.language.isoeng
dc.publisherElsevier B.V.
dc.relation.ispartofHydrometallurgy
dc.sourceWeb of Science
dc.subjectBioleaching
dc.subjectNi/Al2O3
dc.subjectMetal recycling
dc.subjectMethane dry reforming
dc.subjectNickel
dc.titleNickel recycling through bioleaching of a Ni/Al2O3 commercial catalysten
dc.typeArtigo
dcterms.licensehttp://www.elsevier.com/about/open-access/open-access-policies/article-posting-policy
dcterms.rightsHolderElsevier B.V.
unesp.author.orcid0000-0002-5929-8783[3]

Arquivos

Coleções