Biosorption of chromium(VI) by spent cyanobacterial biomass from a hydrogen fermentor using Box-Behnken model
Highlights
► Biomass waste from a hydrogen bioreactor is reused as biosorbent. ► Cr(VI) biosorption by immobilized biomass is maximized using Box-Behnken model. ► The biosorption efficiency is high at ambient temperatures and low biomass dose. ► Its biosorption capacity at low Cr concentrations is superior to others reported. ► Suggests possible integration of bioenergy production and bioremediation processes.
Introduction
Contamination of surface waters with heavy metals due to industrial discharge has emerged as a major problem in recent years that needs to be tackled in view of several health hazards associated with them. Once released into the environment, the heavy metals accumulate in living tissues through food chain that has humans at the top. The human beings have, therefore, to face the toxic effects of the pre-concentrated metals. Chromium is one of the most hazardous metals entering surface waters from the effluent of textile, tannery, electroplating, mining and metal cleaning industries and nuclear power plants (Arica et al., 2004). Toxicity of Cr(VI) ions is due to the negatively charged hexavalent Cr ion complexes that easily pass through cellular membranes by means of sulfate ionic channels and then undergo immediate reduction reactions leading to the formation of various harmful reactive intermediates (Wang and Shen, 1995). Chromium(VI) may not only cause allergies, eczema, and respiratory tract disorders, but is also known to be a powerful carcinogenic agent that may cause cancer in the digestive tract and lungs of human beings (Kaufman, 1970, Katz and Salem, 1993). It is therefore, very important to remove Cr(VI) from wastewaters before discharging into the environment.
The common techniques used for Cr(VI) removal from industrial effluents include chemical precipitation, ion exchange and membrane transfer methods; however, due to expensive nature their large scale application is hindered (Brasil et al., 2006). Amongst the commercial adsorbents activated carbon is most widely employed (Goel et al., 2005), but it is also expensive. Further, it requires the use of chelating agents for removal of inorganic species, making the process even more expensive for Cr(VI) bisorption (Cooney, 1999). Biosorbents are found to be more suitable for metal removal at relatively lower concentrations (10–100 mg/L), where other methods usually fail; and also, they are cost effective and environmentally benign (Tunali et al., 2006). Removal of Cr(VI) has been reported using several algal species (Travieso et al., 1999, Ayse et al., 2005) and cyanobacteria (Khattar et al., 2002, Anjana et al., 2007). Cyanobacterial cells in live as well as dead forms have been tried in recent years for removal of chromium ions from water, and more than 80% removal of Cr(VI) has been reported using these organisms at low metal concentrations (Kiran et al., 2007). Simple growth requirements, autotrophic mode of nutrition, fast growth and non-toxic nature of cyanobacteria favor their use as biosorbents.
In comparison to dry powdered biomass use of cell biomass in immobilized form has been found to be more useful as it not only avoids biomass-liquid separation, but also allows higher local cell density and retention of biomass within a definite working system that can be reused (Lu and Wilkins, 1995). Entrapment of microbial cells in some polymeric matrix, usually a gel, involving formation of beads provides mechanical strength and rigidity to the system thus making metal removal more efficient (Kuyucak and Volesky, 1989, Garrido et al., 2005) as compared to free cell system where separation of the biosorbent from the wastewaters after use becomes a major problem, while low strength and small particle size of the biosorbent also pose hinderance in its column applications (Vijayaraghavan et al., 2005).
Since microbial biomass is utilized in several fermentation industries, large quantity of biomass is generated, which instead of dumping as waste should be used as a commercial commodity. Cyanobacteria, which are known to produce hydrogen, and are being viewed by many as next generation hydrogen producers (Dutta et al., 2005) are under trial for commercial use. During microbial hydrogen production, large amount of waste biomass is generated, but till now very little attention has been paid to tap the potential of biomass waste of fermentors (Vijayaraghavan and Yun, 2007).
In the present study waste biomass of Nostoc linckia from a lab-scale hydrogen fermentor was utilized for removal of Cr(VI) from aqueous solution. The authors have already reported on the hydrogen production potential of N. linckia under different physico-chemical conditions (Mona et al., 2011a). The waste biomass has been found to remove upto 72% of crystal violet dye, a common triphenyl methane dye found in textile effluent (Mona et al., 2011b). The present study was conducted to examine the biosorption potential of the waste biomass for a carcinogenic heavy metal, Cr(VI) found in the textile wastewaters.
The study was aimed at achieving maximum sequestration of Cr(VI) by the waste biomass immobilized in calcium alginate matrix, for which kinetic parameters and adsorption capacity (qe) of the biosorbent were studied followed by RSM based optimization of parameters. Box-Behnken model was used to analyze the effectivity of the system under different combinations of four important operating parameters. There are several advantages of using statistical models like RSM over classical models particularly in terms of rapid and more reliable information on interacting factors important in the process. Four factorial Box-Behnken experimental design was applied to investigate and validate pH, temperature, algal dose and initial metal concentration of the aqueous solution influencing the removal of chromium by N. linckia. The data was analyzed by fitting to a second-order polynomial model, which was statistically validated by performing Analysis of Variance (ANOVA) and lack-of-fit test to evaluate the significance of the model. Surface characteristics of the biosorbents were studied before and after Cr biosorption using scanning electron microscope (SEM), while Fourier transform infrared (FTIR) analysis was done to understand the involvement of various functional groups present on the surface of the cyanobacterium in Cr(VI) biosorption.
Section snippets
The biosorbent and the sorbate
Biosorbent from the spent biomass of N. linckia collected from a lab-scale hydrogen fermentor was prepared by immobilizing in calcium alginate matrix as describe in detail elsewhere (Mona et al., 2011b). A stock solution (1000 mg L−1) of the sorbate i.e. Cr(VI) was prepared using AR grade K2Cr2O7 and desired concentrations of the metal were obtained by further dilutions.
Kinetic studies
Batch studies were performed to determine the equilibrium time required for the maximum adsorption of chromium onto the
Biosorption kinetics
Biosorption of Cr(VI) onto the immobilized beads of the cyanobacterium as a function of contact time (5–180 min) for two initial metal concentrations of 20 and 50 mg/L are depicted in Fig. 1. At both the concentrations, metal removal increased with increasing contact time till 135 min after which equilibrium was attained. In the initial period, sorption of the metal was relatively more rapid suggesting the involvement of a passive process like physical adsorption or ion exchange on the
Conclusions
Reutilization of waste biomass of cyanobacterium (N. linckia) from hydrogen fermentor immobilized in alginate beads for biosorption of Cr(VI) from dilute solutions (10–100 mg/L) seems feasible. Percent Cr(VI) removal by the spent biomass of N. linckia was comparable or even superior to that reported with fresh cyanobacterial biomass for removal of the metal. By applying Box-Behnken design for the optimization experiments, it was possible to investigate the process variables completely and a high
Acknowledgment
Financial assistance to Ms Mona Sharma by CSIR, New Delhi in the form of Senior Research Fellowship and infrastructure facilities created by funding from UGC, New Delhi under SAP (DRS II) are gratefully acknowledged.
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