“…The results from the control experiments showed that the adsorption of the species of interest was due to the functional groups on the biomass, as reported by Oke, Ndlovu, and Sibanda, (2014), and not affected in any way by the POP.…”
supporting
confidence: 61%
“…The technical viability and biosorption capacity of the Saccharomyces cerevisiae waste biomass for the removal of PGMs from synthetic solution in a batch system has been investigated previously (Oke, Ndlovu, and Sibanda, 2014). However, for practical and large-scale operation, a packed column is preferred since a batch system is usually limited to the treatment of small quantities of wastewater.…”
mentioning
confidence: 99%
“…Glass beads were introduced at the top and the bottom of the packed column to prevent the adsorbent from floating. The dilute PGM process solution was conditioned to pH 3 (the optimum pH for adsorption obtained in the batch experiments (Oke, Ndlovu, and Sibanda, 2014) using 0.1 M NaOH and HCl solutions. The solution, with known concentration of solutes, was pumped through the column in an upflow direction using a peristaltic pump (Watson Marlow 5045) with variable speed adjustment.…”
mentioning
confidence: 99%
“…The flow rates and bed depths were chosen based on information from the literature (Calero et al, 2009;Danny, Porter, and McKay, 2000). The pH and the time used were based on the information gathered from the batch studies (Oke, Ndlovu, and Sibanda, 2014).…”
mentioning
confidence: 99%
“…The species of interest include sulphates, chlorides, Na, Ni, Se, Ru, Pd, Pt, and Ir. For the test work, the dilute process stream was conditioned to pH 3 (the optimum pH for PGM adsorption in the batch studies (Oke, Ndlovu, and Sibanda, 2014).…”
SO4(2-) >Te2+>Pt2+>Ir3+>Ni²+>Cl->.Ru3+>Se2+> Na+. The data from the column studies was fitted to Adam-Bohart and Thomas models. The Adam-Bohart model showed a superior prediction of the experimental data. COD analysis of the effluent was also carried out at different time intervals. The measured COD decreased from 200 mg/l to less than 68 mg/l after 30 minutes, which corresponds to the removal efficiency of about 66%.]]>
“…The results from the control experiments showed that the adsorption of the species of interest was due to the functional groups on the biomass, as reported by Oke, Ndlovu, and Sibanda, (2014), and not affected in any way by the POP.…”
supporting
confidence: 61%
“…The technical viability and biosorption capacity of the Saccharomyces cerevisiae waste biomass for the removal of PGMs from synthetic solution in a batch system has been investigated previously (Oke, Ndlovu, and Sibanda, 2014). However, for practical and large-scale operation, a packed column is preferred since a batch system is usually limited to the treatment of small quantities of wastewater.…”
mentioning
confidence: 99%
“…Glass beads were introduced at the top and the bottom of the packed column to prevent the adsorbent from floating. The dilute PGM process solution was conditioned to pH 3 (the optimum pH for adsorption obtained in the batch experiments (Oke, Ndlovu, and Sibanda, 2014) using 0.1 M NaOH and HCl solutions. The solution, with known concentration of solutes, was pumped through the column in an upflow direction using a peristaltic pump (Watson Marlow 5045) with variable speed adjustment.…”
mentioning
confidence: 99%
“…The flow rates and bed depths were chosen based on information from the literature (Calero et al, 2009;Danny, Porter, and McKay, 2000). The pH and the time used were based on the information gathered from the batch studies (Oke, Ndlovu, and Sibanda, 2014).…”
mentioning
confidence: 99%
“…The species of interest include sulphates, chlorides, Na, Ni, Se, Ru, Pd, Pt, and Ir. For the test work, the dilute process stream was conditioned to pH 3 (the optimum pH for PGM adsorption in the batch studies (Oke, Ndlovu, and Sibanda, 2014).…”
SO4(2-) >Te2+>Pt2+>Ir3+>Ni²+>Cl->.Ru3+>Se2+> Na+. The data from the column studies was fitted to Adam-Bohart and Thomas models. The Adam-Bohart model showed a superior prediction of the experimental data. COD analysis of the effluent was also carried out at different time intervals. The measured COD decreased from 200 mg/l to less than 68 mg/l after 30 minutes, which corresponds to the removal efficiency of about 66%.]]>
BACKGROUND: The aim of this study was to investigate the feasibility of utilizing a continuous-flow anaerobic granular sludge bed (UASB) reactor for the removal of palladium (II) from aqueous streams and the recovery of this precious metal as biogenic Pd(0). Anaerobic methanogenic granular sludge has been recently shown to reduce Pd(II) in the presence of a suitable electron donor leading to the formation of biomass-associated Pd(0).
RESULTS:Two laboratory-scale UASB reactors were fed with ethanol or acetate, in order to compare their performance in terms of Pd removal and reduction. Pd(II) was added in two periods of increasing concentration, 5 mg Pd(II) L −1 and then 15 mg Pd(II) L −1 . Extensive removal of Pd (up to 99%), was attained in both reactors. X-ray diffraction (XRD) and energy-dispersive X-ray spectroscopy (EDS) analysis confirmed significant differences in the content of Pd(0) in the biomass, depending on the electron donor used. The main mechanisms of Pd(II) removal when acetate and ethanol were used as electron donor were biosorption and reduction to Pd(0) by biogenic H 2 released as fermentation product, respectively.
CONCLUSIONS:The results obtained demonstrate that it is possible to apply a continuous process for Pd reduction and recovery using a methanogenic consortium.
Scanning electron microscopySludge samples obtained from both reactors were prepared for scanning electron microscopy (SEM) by fixation in 2.5% glutaraldehyde for 30 min, washed with two changes in 0.1 mol L −1 PIPES wileyonlinelibrary.com/jctb
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