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Freundlich exponent describing biosorption capacity and biosorption intensity.
Q_{e} = K_{text{F}} C_{e}^{1/n} (5 where K F is the Freundlich constant [ mg g−1)/ mg L−1)1/n] and n F the Freundlich exponent describing biosorption capacity and biosorption intensity, respectively.
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The effects of flow rate, influent concentration of 2,4-DCP and bed depth on breakthrough curves and biosorption capacity were investigated.
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The maximum biosorption was found to be 90.02% at pH 5.5 and biosorption capacity (q e) of Cd+2 is 9.2506 mg g−1.
The Freundlich isotherm is used for modeling the biosorption of metal ions on heterogeneous surfaces and the linearized form of the isotherm is as follows: log q_{text{e}} = log K_{text{f}} + frac{1}{n}log C_{text{e}} (8 where Kf (mg/g) is a constant relating the biosorption capacity and 1/n is an empirical parameter relating the biosorption intensity.
In Freundlich isotherm model, K F is the measurement of the biosorption capacity and n is the measurement of the intensity of biosorption (Sawalha et al. 2006).
An appropriate larger-is-better criterion was adopted to maximize the biosorption capacity and bioremoval efficiency along with S/Nratio, ANOVA and desirability approach.
We evaluate pretreatment, immobilization, and factors affecting biosorption capacity, such as initial metal ion concentration, biomass concentration, initial pH, time, temperature, and interference of multi metal ions and introduce molecular tools to develop engineered algal strains with higher biosorption capacity and selectivity.
Molecular biotechnology is a potent tool to elucidate the mechanisms at molecular level, and to construct engineered organisms with higher biosorption capacity and selectivity for the objective metal ions.
frac{t}{qt} = frac{1}{{K_{2} qe^{2} }} + frac{1}{qe}twhere qe is the equilibrium biosorption capacity and K2 (g/mg min) is the pseudo-second-order rate constant.
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