Removal of cadmium and mercury ions from aqueous solution by sorption on treated Pinus pinaster bark: kinetics and isotherms
Introduction
Since industrial effluent containing heavy metals was recognized as a major threat to the environment and to health, research on the removal of these pollutants from solution has grown rapidly. The main offenders are cationic species of mercury, lead, nickel, chromium, cadmium, copper and zinc. At high concentrations these metals can successfully be recovered from solution by precipitation as hydroxides or carbonates, by membrane filtration, and by capture on synthetic ion exchangers. However, these methods are much less efficient for concentrations lower than about 100 ppm, for which they can be prohibitively expensive and can even fail to achieve legal limits (Matheichal et al., 1997). For these low concentrations it is preferable to use sorption techniques; and since activated carbon is too expensive for large scale use, numerous alternatives have been proposed, including peat (McKay and Porter, 1997), agricultural and forest waste (Deshkar and Dara, 1988; Marañón and Sastre, 1991) and other biosorbents (Kapoor et al., 1999; Peternele et al., 1999).
The forest wastes that have been investigated in this respect include the barks of certain timber trees. These barks are inexpensive, abundant, and contain polyphenolic compounds (generically termed tannins) that under appropriate conditions of pH and temperature are capable of sorbing significant quantities of metal cations from solution (Ruf et al., 1992; Vázquez et al., 1994). Furthermore, prior treatment to bring about crosslinking and/or functionalization can improve both the stability and sorption capacity of these compounds (Randall et al., 1976; Peternele et al., 1999).
Pinus pinaster bark is a by-product of the timber industry of Galicia (N.W. Spain) that is currently used only as fuel or for horticultural purposes. However, like the barks of other conifers it contains polyhydroxylated polyphenols based on procyanidin (Vázquez et al., 1987; Laks and McKaig, 1988). Since this kind of tannin can act as an ion-exchanger (Laks, 1991), the deprotonated hydroxyls of the procyanidin ring B chelating di-cations as shown in Fig. 1, the possibility arises in using this by-product to remove heavy metal cations from wastewater.
In this work, we studied the sorption of Cd2+ and Hg2+ ions by P. pinaster bark treated with formaldehyde. The kinetics and sorption isotherms of these processes were characterized, and the influence of pH was investigated.
Section snippets
Pretreatment of bark
P. pinaster bark collected from a local sawmill was air-dried to near-equilibrium humidity and ground in a crushing mill to a particle size <1 mm, small enough to ensure satisfactory intraparticular diffusion. Adsorption studies were performed on the 0.25–0.43 mm fraction.
To polymerize and insolubilize phenolics of low molecular weight (which would stain the treated water, replacing one form of pollution with another), the ground bark was treated with formaldehyde in an acid medium (Randall et
Adsorption kinetics and effect of initial pH
Fig. 2 shows, for Cd2+ and Hg2+ solutions of the highest initial concentrations used and initial pH of 6.6–6.8, the effects of contact time on the proportion of cation adsorbed (XA) and on the pH of the solution. For both cations, there was a rapid increase in XA and a corresponding rapid decrease in pH, and both of these variables levelled off at equilibrium values within the 24 h reaction period. The behaviour observed with other initial concentrations and pH values was qualitatively similar.
Acknowledgements
The authors are grateful to the CICYT for financial support (Project AGF98-0369).
References (17)
- et al.
Removal of heavy metals using the fungus Aspergillus niger
Bioresource Technol.
(1999) - et al.
Heavy metal removal in packed beds using apple wastes
Bioresource Technol.
(1991) - et al.
Biosorptive behaviour of casein for Zn2+, Hg2+ and Cr3+: effects of physico-chemical treatments
Bioresource Technol.
(1998) - et al.
Adsorption of Cd(II) and Pb(II) onto functionalized formic lignin from sugar cane bagasse
Bioresource Technol.
(1999) - et al.
Adsorption of heavy metal ions by chemically modified Pinus pinaster bark
Bioresource Technol.
(1994) - et al.
Isotherm analyses for single component and multi-component metal sorption onto lignite
J. Chem. Technol. Biotechnol.
(1995) - et al.
Removal of cadmium(II) by low cost adsorbents
J. Environ. Eng.
(1984) - et al.
Sorption of mercury by Techtona grandis bark
Asian Environ.
(1988)
Cited by (177)
Recent advances and perspectives of tannin-based adsorbents for wastewater pollutants elimination: A review
2023, Environmental Nanotechnology, Monitoring and ManagementDual-application of novel magnetic carbon nanocomposites as catalytic liquefaction for bio-oil synthesis and multi-heavy metal adsorption
2021, Renewable EnergyCitation Excerpt :It was revealed that the removal of heavy metals including Cr, Ni, Cu and Cd increased with increasing time until 90 min when equilibrium was achieved and on increasing the contact time further did not impact on the adsorption capacity. This trend was true for all the adsorbents however the adsorption capacities of different adsorbents varied, from highest to lowest, AC > MCNC-GH > MCNC-CH > MCNC-GE > MCNC-CE dependent on the different affinities for heavy metals of adsorbents resulting in different adsorption capacities [38,39]. The initial concentration of heavy metals has a significant effect on overall absorption.
Agro and industrial residues: Potential raw materials for photocatalyst development
2021, Journal of Photochemistry and Photobiology A: ChemistryKinetics and thermodynamics of mercury adsorption onto thiolated graphene oxide nanoparticles
2019, PolyhedronCitation Excerpt :In Freundlich model, the parameter of Kf (mg.g−1 (L.mg−1))1/n and n are constants of this model that represent the capacity and adsorption intensity, respectively. The value of 1/n is between 0 and 1 which shows the adsorbent heterogeneity [67,68]. As seen the Kf and 1/n were 29.72 and 0.4, respectively proposing that adsorption capacity and heterogeneity of adsorbent is suitable.