2006
DOI: 10.1016/j.biortech.2005.04.030
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Biosorption of aqueous chromium(VI) by Tamarindus indica seeds

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Cited by 258 publications
(134 citation statements)
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References 26 publications
(37 reference statements)
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“…At this point the total removal of the metal is carried out. The results are coincident for tamarind Shell with 95% of remotion at 58˚C and 3 hours [22], for the adsorption of Cadmium(II) from aqueous solution on natural and oxidized corncob (40˚C and 5 days) [27], but this are different for the mandarin waste [25], Caladium bicolor (wild cocoyam) biomass [28], and Saccharomyces cerevisiae [29]. The increase in temperature increases the rate of removal of Chromium(VI) and decreases the contact time required for complete removal of the metal, to increase the redox reaction rate [22].…”
Section: Effect Of Temperaturesupporting
confidence: 60%
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“…At this point the total removal of the metal is carried out. The results are coincident for tamarind Shell with 95% of remotion at 58˚C and 3 hours [22], for the adsorption of Cadmium(II) from aqueous solution on natural and oxidized corncob (40˚C and 5 days) [27], but this are different for the mandarin waste [25], Caladium bicolor (wild cocoyam) biomass [28], and Saccharomyces cerevisiae [29]. The increase in temperature increases the rate of removal of Chromium(VI) and decreases the contact time required for complete removal of the metal, to increase the redox reaction rate [22].…”
Section: Effect Of Temperaturesupporting
confidence: 60%
“…Also, we observed the development of a blue-green and a white precipitate, which changes more rapidly at higher temperatures (date not shown). The results are coincident for tamarind Shell [13,22]. With respect to other biomass used, most authors report lower removal efficiencies of metal, for example: 45 mg/L for eucalyptus bark [16] acetate [31].…”
Section: Effect Of Initial Metal Concentrationmentioning
confidence: 56%
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“…Entretanto, a maioria dos estudos investiga o processo de preparação de bioadsorbente carbonizado visando o emprego no tratamento de efluentes aquosos contaminados por metais pesados 12,13 . Porém, o processo de reciclagem do material carbonizado é bastante oneroso 14 . Por outro lado, poucos pesquisadores têm se dedicado ao estudo de adsorbentes não carbonizados 15 .…”
Section: Introductionunclassified
“…Mostly untreated and pretreated lignocellulosic industrial byproducts and agricultural residues have been employed as adsorbents for hexavalent chromium removal from water. These materials include sawdust (Baral et al 2006;Aliabadi et al 2006;Vinodhini and Das 2010), coir pith (Sumathi et al 2005), oil palm fiber (Isa et al 2008), wheat straw carbon (Chand et al 2009), barley straw carbon (Chand et al 2009), leaf mould (Sharma and Forster, 1996), wheat bran (Nameni et al, 2008;Singh et al 2009), cotton stalk peel , maize tassel (Zvinowanda et al 2009), walnut shell (Pehlivan and Altun 2008), walnut hull ), hazelnut shell (Pehlivan and Altun 2008), almond shell (Pehlivan and Altun 2008), rice bran (Oliveira et al 2005), rice husk (Sumathi et al 2005), soybean hulls (Marshall and Wartelle 2004), eucalyptus bark (Sarin and Pant 2006), Tamarindus indica seeds (Agarwal et al 2006), tea factory waste (Vinodhini and Das 2010), spent mushroom modified by cationic surfactant (Jing et al 2011), and olive stone (Blázquez et al 2009). Furthermore, since lignocellulosic materials are used in the bioethanol industry as source of sugars (Mosier et al 2005), the process solid residue can be, also, implemented as adsorbent.…”
Section: Introductionmentioning
confidence: 99%