Nickel(II) biosorption by Rhodotorula glutinis

Suazo-Madrid, Alicia; Morales-Barrera, Liliana; Aranda-García, Erick; Cristiani‐Urbina, Eliseo

doi:10.1007/s10295-010-0828-0

Cited by 45 publications

(22 citation statements)

References 54 publications

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“…The opposite behavior occurred for Cr 3+ removal. Our results are in agreement with several recent studies which present the same pattern of Ni 2+ and Cr 3+ removal, even when using different types of adsorbents (Nehrenheim and Gustafsson, 2008;Calero et al, 2009;Karaoğlu et al, 2010;Anoop Krishnan et al, 2011;Fernandes and Gando-Ferreira, 2011;Suazo-Madrid et al, 2011;Alomá et al, 2012). The statistical parameters obtained show that all models were in good agreement with the experimental data, the maximum calculated AADs were 5.50%.…”

Section: Mono-component Systemsupporting

confidence: 92%

Biosorption study of Ni2+ and Cr3+ by Sargassum filipendula: kinetics and equilibrium

Seolatto

Martins

Tavares

et al. 2014

Braz. J. Chem. Eng.

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-In this work, the biosorption of Cr 3+ and Ni 2+ by Sargassum filipendula pre-treated with CaCl 2 was studied. Kinetic and equilibrium experiments were carried out for mono-and multi-component solutions in a batch reactor at pH 3.0 and 30 ºC. The results from the kinetic experiments showed that Cr 3+ adsorbs slower than Ni 2+ . This behavior was explained by means of a mechanistic analysis, which showed that Cr 3+ uptake presented three adsorption stages, whereas Ni 2+ adsorption presents only two. The mono-component equilibrium data, along with binary kinetic data obtained from mono-component experiments, showed that, although the kinetics for Cr 3+ removal are slower, the biomass had a stronger affinity for this ion. Almost all Ni 2+ is desorbed from the biomass as Cr 3+ adsorbs. The binary equilibrium data also presented this behavior. The binary data was also modeled by using modified forms of the Langmuir, Jain and Snoeyink, and Langmuir-Freundlich isotherms. However, the prediction obtained presented low accuracy. An alternative modeling with artificial neural networks was presented and the results showed that this technique could be a promising tool to represent binary equilibrium data. The main contribution of this work was to obtain experimental data for Cr 3+ /Ni 2+ adsorption, which is a system rarely found in the literature and that provides information that could be used in process modeling and simulation.

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Section: Mono-component Systemsupporting

confidence: 92%

Biosorption study of Ni2+ and Cr3+ by Sargassum filipendula: kinetics and equilibrium

Seolatto

Martins

Tavares

et al. 2014

Braz. J. Chem. Eng.

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“…A much lower maximum sorption capacity was observed by Sari et al 20 and Celaya et al 37 who used Cladonia furcata and Thiobacillus ferrooxidans; the corresponding values were 7.9 mg/g (nickel) and 9.7 mg/g (zinc). On the other hand, a higher biosorption of Ni(II) was observed by Shinde et al 3 and Suazo-Madrid et al 31 , at 48.3 and 112.9 mg/g, respectively, using Y. lipolytica and Rhodotorula glutinis as biosorbents. In the case of Zn(II) biosorption, the maximum sorption capacity obtained in the studies by Joo et al 1 and Li et al 23 were 83.3 and 75.8 mg/g, respectively, using Pseudomonas aeruginosa and Streptomyces ciscaucasicus, respectively.…”

Section: Biosorption Isotherm Modelsmentioning

confidence: 85%

Biosorption of nickel (II) and zinc (II) from aqueous solutions by the biomass of yeast Yarrowia lipolytica

Wierzba

2017

Polish Journal of Chemical Technology

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This study examined the biosorption process of Ni(II) and Zn(II) from an aqueous solution by dead biomass of Yarrowia lipolytica. Optimum biosorption conditions were determined as a function of pH, biomass dosage, contact time, and temperature. The biosorbent was characterized by FTIR, which indicated the participation of hydroxyl, carboxyl, amide and amine groups in the process of binding the metal ions. The results showed that the biosorption processes of both metal ions closely followed pseudo-second order kinetics. The equilibrium data of Ni(II) and Zn(II) ions at 20, 30 and 40 o C fi tted the Langmuir and Freundlich isotherm models. Langmuir isotherm provided a better fi t to the equilibrium data, with a maximum biosorption capacity of the Y. lipolytica biomass for Ni(II) and Zn(II) of 30.12 and 44.44 mg/g respectively. The calculated thermodynamic parameters demonstrated that the biosorption of Ni(II) and Zn(II) ions onto the Y. lipolytica was feasible, spontaneous and endothermic.

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“…The capacity to biosorb Ni(II) from aqueous solutions has been analyzed in some microorganisms as well as in biomaterials such as agroindustrial, forestry, and fishery by-products and biowastes (Gialamouidis et al 2009;Malkoc 2006;Pradhan et al 2005;Suazo-Madrid et al 2011;Vinod et al 2010).…”

Section: Introductionmentioning

confidence: 99%

“…Divalent nickel [Ni(II)] is frequently encountered in raw wastewater streams from industrial processes such as nickel mining, metallurgy and electroplating, steel foundries and stainless steel production, electroforming and sintered metal coating production, non-ferrous metal, mineral processing, paint formulation, porcelain enameling, battery and accumulator manufacture, and steamelectric power plants (Pahlavanzadeh et al 2010;Shroff and Vaidya 2011a;Suazo-Madrid et al 2011). Although living organisms require trace amounts of Ni(II) for certain enzyme systems that participate in metabolic reactions such as ureolysis, hydrogen metabolism, methane biogenesis, and acidogenesis (Alomá et al 2012), long-term exposure to high Ni(II) levels may cause acute and chronic health disorders such as skin dermatitis, allergic sensitization, gastrointestinal distress (nausea, vomiting, and diarrhea), pulmonary fibrosis, renal edema, and severe damage to the lungs, kidney, nervous system, and mucous membranes (Borba et al 2006;Vinod et al 2010).…”

Section: Introductionmentioning

confidence: 99%

Nickel(II) biosorption from aqueous solutions by shrimp head biomass

Hernández-Estévez

Cristiani‐Urbina

2014

Environ Monit Assess

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The present study evaluates the capacity of shrimp (Farfantepenaeus aztecus) head to remove toxic Ni(II) ions from aqueous solutions. Relevant parameters that could affect the biosorption process, such as shrimp head pretreatment, solution pH level, contact time and initial Ni(II) concentration, were studied in batch systems. An increase in Ni(II) biosorption capacity and a reduction in the time required to reach Ni(II) biosorption equilibrium was manifested by shrimp head biomass pretreated by boiling in 0.5 N NaOH for 15 min; this biomass was thereafter denominated APSH. The optimum biosorption level of Ni(II) ions onto APSH was observed at pH 7.0. Biosorption increased significantly with rising initial Ni(II) concentration. In terms of biosorption dynamics, the pseudo-second-order kinetic model described Ni(II) biosorption onto APSH best. The equilibrium data adequately fitted the Langmuir isotherm model within the studied Ni(II) ion concentration range. According to this isotherm model, the maximum Ni(II) biosorption capacity of APSH was 104.22 mg/g. Results indicate that APSH could be used as a low-cost, environmentally friendly, and promising biosorbent with high biosorption capacity to remove Ni(II) from aqueous solutions.

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Nickel(II) biosorption by Rhodotorula glutinis

Cited by 45 publications

References 54 publications

Biosorption study of Ni2+ and Cr3+ by Sargassum filipendula: kinetics and equilibrium

Biosorption study of Ni2+ and Cr3+ by Sargassum filipendula: kinetics and equilibrium

Biosorption of nickel (II) and zinc (II) from aqueous solutions by the biomass of yeast Yarrowia lipolytica

Nickel(II) biosorption from aqueous solutions by shrimp head biomass

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