1999
DOI: 10.1016/s0304-386x(99)00017-1
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A comparative study of the mass transfer kinetics of metal biosorption by microbial biomass

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Cited by 120 publications
(64 citation statements)
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“…This indicates that the smaller particle size have higher surface area and mass transfer coefficient, and hence, lower external mass transfer resistance. However, the values of a K L were in the same magnitude to that reported (0.03 to 0.1 min -1 ) by Puranik et al (1999). In addition, nickel uptake was higher at pH values of 6 and 7, and indicates that at the higher pH AWBS possesses more anionic charge and favors higher adsorption uptake.…”
Section: Mass Transfer Modelingsupporting
confidence: 67%
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“…This indicates that the smaller particle size have higher surface area and mass transfer coefficient, and hence, lower external mass transfer resistance. However, the values of a K L were in the same magnitude to that reported (0.03 to 0.1 min -1 ) by Puranik et al (1999). In addition, nickel uptake was higher at pH values of 6 and 7, and indicates that at the higher pH AWBS possesses more anionic charge and favors higher adsorption uptake.…”
Section: Mass Transfer Modelingsupporting
confidence: 67%
“…Mass transfer modeling has been performed based on the assumption that the external mass transfer is the rate limiting step for the nickel ion and AWBS system (Loukidou et al 2004;Koumanova et al 2002;Puranik et al 1999). In this work, the volumetric mass transfer (Table 5.3) when the AWBS particles were decreased from 1.18-3.35 mm to less than 0.425 mm; the a K L was the same magnitude as that reported (0.03 to 0.1 min -1 ) by Puranik et al (1999). This indicates that the smaller particle size have higher surface area and mass transfer coefficient, and hence, lower external mass transfer resistance.…”
Section: Mass Transfer Modelingmentioning
confidence: 99%
“…Table 1, it can be observed that the External Film Model describes better the system based on its higher regression coefficient. This model considers that the limiting step is the diffusion from the solution to a tiny liquid film formed on the adsorbent particle (Puranik et al, 1999). It may indicate that the operating parameters such as agitation speed could have important effects on the adsorption efficiency.…”
Section: Kinetic Studiesmentioning
confidence: 99%
“…[5][6][7] Entretanto, a remoção de íons metálicos presentes em baixas concentrações, bem como de outras substâncias poluentes, como corantes industriais e agrotóxicos, demanda o desenvolvimento de novos materiais e processos, com destaque para o emprego de materiais absorventes de baixo custo, principalmente aqueles presentes na biomassa. [6][7][8][9] A desacetilação de quitina, um polissacarídeo que ocorre abundantemente na natureza e que é extraído comercialmente de rejeitos da indústria pesqueira, tais como carapaças de caranguejos e cascas de camarões, resulta em quitosana, um polímero que possui boas propriedades de adsorção de íons metálicos devido às interações que estes estabelecem com grupos amino, presentes em grande número nas cadeias de quitosana.10 O uso de quitosana também tem sido sugerido para a adsorção de corantes 11 e de ácidos húmicos, 12 na separação de metais pesados, 13-16 na descontaminação de efluentes contendo Escherichia coli e pesticidas, 17,18 entre outras aplicações. No caso da interação com cátions, a elevada capacidade de adsorção da quitosana é devida à formação de complexos entre os cátions e o…”
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