1. Introduction
Toxic heavy metal pollution of the aquatic environment has become a notable problem across the world owing to its non-biodegradability, bioaccumulation, and biomagnification in the food chain[1-3]. Conventionally, heavy metals are defined as elements with metallic features with an atomic number > 20 and atomic weights between 63.5 and 200.6[4-6], and they include a group of metals and metalloids [7,8]. In general, the term “Heavy metal” is considered to be any metallic element with a relatively high density and toxicity or poison at low concentrations. Low concentrations of heavy metals can be harmful to living organisms including humans[9]. Some of these metals, however, are also micronutrients necessary for plant growth (e.g., Co, Cu, Mn, Ni, and Zn), while others have an unknown biological function and are toxic (e.g., Cd, Hg, and Pb)[10].
Along with industrial development, such as metal plating factories, mining operations, fertilizer and pesticides industries, tanneries, battery manufacture, and paper industries, industrial wastewater including heavy metals are directly or indirectly released into the environment. In comparison with organic contaminants, heavy metals are likely to be not biodegradable and bioaccumulated in living cells, and the heavy metal ions can be toxic or carcinogenic. Toxic heavy metals such as cadmium, nickel, zinc, copper, mercury, lead, and chromium cause a significant hazard in industrial wastewater treatment. For example, cadmium exposes human health to severe risks, and chronic exposure to it causes kidney failure, and human exposure to its high levels can result in death[11]. Nickel exceeding critical levels might result in severe lung and kidney problems as well as gastrointestinal distress, pulmonary fibrosis, and skin dermatitis[12]. Moreover, it is known that nickel is a human carcinogen. Zinc is a trace element essential to the maintenance of human health. It is also a key element to the biological functions of the living cell and controls many biochemical processes. However, high levels of zinc can cause critical health problems, such as stomach cramps, skin irritations, vomiting, and anemia[13].
To avoid adverse effects of heavy metals, contaminated wastewater must be treated before being discharged into the environment. Conventional physicochemical techniques for removing heavy metals from wastewater involve lime precipitation, chemical oxidation or reduction, ion exchange, electrochemical treatment, filtration, reverse osmosis, membrane technologies, and evaporative recovery[14]. However, these techniques have significant shortcomings, including low efficiency at low concentrations, high capital investment and operation costs of treatment systems, and production of toxic sludge[15,16]. Therefore, new technologies are required to reduce toxic heavy metal concentrations to environmentally safe levels in a cost-effective and environmentally friendly manner.
Bioremediation, which uses microorganisms to degrade contaminants in the environment, are cost-effective and environmentally friendly way to the treatment of contaminated wastewater with fewer by-products than physicochemical techniques. Bioremediation has recently received wide attention to remediating contaminated environments, including soils, lakes, streams, and groundwater[17-22] and it has been considered an alternative treatment technology[3].
Many investigators also observed that toxic heavy metals harmfully affect microbial growth, morphology, activity, and functioning, resulting in reduced microbial biomass[21,23-25]. On the other hand, microorganisms living in contaminated environments can have the capability to adapt and tolerate harsh environment in the presence of toxic heavy metals. For instance, extracellular polymeric materials or exopolymeric materials excreted by bacteria have been known as functioning as biosorbent agents by accumulating nutrients from the environment and contributing to the biosorption of toxic heavy metals[26-28].
In particular, purple nonsulfur bacteria (in taxonomy, Rhodobacteraceae) have been shown to resist toxic heavy metals[21,24,29-33]. A unique advantage of purple nonsulfur bacteria is that they can use not only solar radiation as an energy source under anaerobic conditions in the presence of light but also can use organic matter as the source of energy and carbon under aerobic and dark conditions[34]. The various metabolic activities such as photosynthesis and respiration by the Rhodobacter may permit the species to survive and thrive in diverse habitats[35,36]. Little information is still available about the removal of heavy metals by the PNAS, Rhodobacter. As far as we know, this is the first report about the removal of Cd, Ni, and Zn in industrial wastewater by R. balsticus among Rhodobacter species.
This work aimed to investigate: (i) the influence played by toxic heavy metals [Cd(II), Ni(II), and Zn(II)] on the photosynthetic growth of purple nonsulfur bacteria, especially Rhodobacter species; (ii) the potential of different Rhodobacter species for bioremediation of Cd(II), Ni(II), and Zn(II) in liquid media; and (iii) active and passive removal efficiencies of toxic heavy metals to reveal their biological removal mechanisms possibly through the intracellular uptake (bioaccumulation) and surface binding (biosorption).
2. Materials and methods
2.1. Bacteria and cultivation
Three Rhodobacter species used in this study were provided by the Korean Collection for Type Cultures (KCTC). Rhodobacter blasticus (KCTC 15056), Rhodobacter sphaeroides (KCTC 1434), and Rhodobacter capsulatus (KCTC 2583) were used in this study. The cells were inoculated in 100 mL modified ATCC medium No. 1170 at 2% (by volume). The cells were incubated in a shaking incubator having white LED (Light-emitting diode) lamps in properly controlled conditions. The optimum growth conditions were initial pH of 6.5~7; shaking speed of 200 rpm (rev/min); temperature of 30 °C on incubation; and light intensity of 3,000 lux (lm/m2). To keep a culture for inoculation a live fresh culture, a new modified ATCC medium No. 1170 was inoculated every seven days. Five-day-old cells were inoculated for the growth experiment.
2.2. Liquid media contaminated with toxic heavy metals
To investigate the effects of toxic heavy metals on the growth and removal of toxic heavy metal by Rhodobacter species, the bacterial cell cultures grown in the exponential stage were inoculated into the bottles including modified ATCC medium No. 1170 added with Cd(II), Ni(II), and Zn(II). A 1000 mg/L stock solution of Cd(II), Ni(II), and Zn(II) were manufactured by solubilizing 1.2457 g CdCl2 ‧2½H2O, 1.8341 g NiCl2 ‧6H2O, and 1 g ZnCl2, respectively, in 1 L of deionized water. The analytical grade of chemicals was used in the experiment.
2.3. Preparation of cell pellets of Rhodobacter species
Harvesting of cells in the exponential growth phase was performed by centrifugation at 8,000 rpm for 15 min and was washed twice with 0.1% of sterilized peptone water to acquire the cell pellets for evaluating the bioremediation of heavy metals.
2.4. Bioremoval of Cd(II), Ni(II), and Zn(II) by Rhodobacter species
All experiments were performed using the 200 mL culture flasks with a 150 mL sample of wastewater containing toxic heavy metals. The initial cell concentration was established at about 0.1 g dry wt./L. The culture flasks were grown at 30 °C and shaked at 200 rpm and illuminated at 3000 lux of light intensity by white LED lamps. All the culture flasks were prepared in duplicates.
2.5. Metabolism-independent (metabolic inhibition) study
The cell pellets obtained from each culture in the experiment were collected from a late log phase culture (60 hours) and were suspended in 1 M sodium azide (NaN3) solution for 45 min to inhibit metabolic activity[33,37-39]. Sodium azide was known to enhance the production of 1O2 in an aqueous solution as the nontoxic antimicrobial agent[38]. Cell suspensions were centrifuged and then washed with the sterilized 0.1% of peptone water to acquire the cell pellets to test the bioremediation of toxic heavy metals.
2.6. Metabolism-dependent study
Wet cell suspensions were manufactured as previously explained except that peptone, yeast extract, Na2SO4, and KH2PO4 were added to the toxic heavy metal solution at concentrations of 10 mg/L[33,37] and a control set contained no supplement of nutrients added and showed a clear solution.
2.7. Analysis methods
Samples were taken during the treatment for Cd(II), Ni(II), and Zn(II) analysis and photosynthetic bacterial growth measurement. For the analysis of heavy metals, the centrifugation of samples was performed at 3000 rpm for 30 min to prepare the supernatant with no biomass, and the resulting supernatant was then analyzed by following APHA standard methods. The supernatant was sterilized by a filter membrane (0.22 μm) and stored at 4 °C. The heavy metals were analyzed by inductively coupled plasma-optical emission spectroscopy (ICP-OES 8000, PerkinElmer, America). The photosynthetic bacterial growth was measured at 535 nm[31] using a UV-VIS spectrophotometer (UV Mini 1240 Shimadzu, Japan).
2.8. Calculation of removal efficiency (%)
The removal performance (removal efficiency) by three Rhodobacter species was assessed by using the toxic heavy metal removal rate, R (in percent), which was defined by the following equation[40,41]:
Where, Ci and Cf were the concentration of toxic heavy metals in the initial and final stages after treatment in the solution, respectively.
2.9. Data presentation and statistical analysis
All results were obtained from independent triplicates from a single culture. These experiments were simultaneously carried out and results were expressed as mean values with the standard deviations, which were shown by the error bars in the figures.
All data were statistically analyzed by SAS Version 8.2 (SAS Institute, Cary, NC, USA). The significant differences in mean values were statistically analyzed through the use of Fisher’s least significant difference test (LSD; P = 0.05).
3. Results
3.1. Effect of Cd(II), Ni(II), and Zn(II) on the photosynthetic bacterial growth
Figure 1 shows the growth curves of three species of Rhodobacter (R. blasticus, R. capsulatus, and R. sphaeroides) in the presence of Cd(II). After the cultures were inoculated, they showed an initial density of about 0.03-0.04 absorbance units (a.u) at 535 nm. R. blasticus tended to have long lag periods among three Rhodobacter species and entered exponential growth after an average of 75 hours in the presence of Cd(II); the lag period in the presence of Cd(II) was about three times greater than that in plain media without Cd. The maximum absorbance measurements obtained in plain (0 mg/L Cd), 5 mg/L Cd, 10 mg/L Cd, 20 mg/L Cd, and 80 mg/L Cd were 2.21, 1.41, 1.21, 0.27, and 0.30 a.u, respectively. For R. capsulatus, exponential growth started concurrently after a lag period of 51 hours on average in the presence of Cd(II), whereas it entered exponential growth after about 24 hours in the absence of Cd(II). Maximum absorbance observed in plain, 5 mg/L Cd, 10 mg/L Cd, 20 mg/L Cd, and 80 mg/L Cd were 2.01, 1.30, 1.17, 0.34, and 0.20 a.u, respectively. For R. sphaeroides, exponential growth started after a lag period of 39 hours on average in the presence of Cd(II). Maximum absorbance observed in plain, 5 mg/L Cd, 10 mg/L Cd, 20 mg/L Cd, and 80 mg/L Cd were 2.47, 1.67, 1.47, 0.54, and 0.48 a.u, respectively.
The growth curves for three species of Rhodobacter with Ni(II) added were shown in Figure 2. Exposure of the three species to Ni(II) showed similar patterns as observed in the presence of Cd(II) discussed above, with absorbance generally lower with increasing Ni(II) concentrations. The average lag times of the three microorganisms in the presence of Ni(II) were 54 hours, 48 hours, and 39 hours for R. capsulatus, R. blasticus, and R. sphaeroides, respectively.
Figure 3 shows the growth curves of the three Rhodobacter species in the presence of Zn(II). Exposure of the three species to Zn(II) again showed similar patterns with absorbance generally lower with increasing Zn(II) concentrations. The average lag time of the three microorganisms in the presence of Zn(II) was 48 hours, 36 hours, and 39 hours for R. capsulatus, R. blasticus, and R. sphaeroides, respectively. In the case of R. capsulatus, the absorbance value did not increase by more than 0.1 in 80 mg/L Zn, which means that it did not grow.
3.2. Bioremoval of toxic heavy metals [Cd(II), Ni(II), and Zn(II)] by Rhodobacter species
Comparisons between the ability of Rhodobacter species for the removal of toxic heavy metals [Cd(II), Ni(II), and Zn(II)] are shown in Figure 4. The removal efficiencies for Cd by R. blasticus, R. capsulatus, and R. sphaeroides under different concentrations of Cd(II) solution (5, 10, 20, and 80 mg/L) were as follows: for 5 mg/L Cd: R. blasticus, R. sphaeroides > R. capsulatus; for 10 mg/L Cd: R. blasticus > R. capsulatus, R. sphaeroides; for 20 mg/L Cd: no significant differences were found for the removal efficiency of Cd by Rhodobacter species, and removal rates were 66% or more; and finally in 80 mg/L Cd: R. blasticus > R. capsulatus > R. sphaeroides.
Removal efficiencies for Ni by R. blasticus, R. capsulatus, and R. sphaeroides under different concentrations of Ni(II) solution (5, 10, 20, and 80 mg/L) were about 50%, in the following order: in 5 mg/L Ni, R. capsulatuss ≥ R. blasticus > R. sphaeroides; in 10 mg/L Ni, no significant differences were found; in 20 mg/L Ni: R. blasticus, R. capsulatus > R. sphaeroides; and finally in 80 mg/L Ni: R. blasticus, R. capsulatus > R. sphaeroides.
Overall, R. blasticus exhibited a higher ability for removal of Cd(II) and Ni(II) compared to Zn(II). The removal efficiencies for Zn by R. blasticus, R. capsulatus, and R. sphaeroides at 5, 10, 20, and 80 mg/L of Zn (II) concentrations were less than 20%. No significant differences were found in the removal efficiency of Zn(II) by Rhodobacter species.
3.3. Metabolic study of bioremediation of Cd(II), Ni(II), and Zn(II) by Rhodobacter species
3.3.1. Metabolic inhibition study
Sodium azide was known to enhance the production of 1O2 in an aqueous solution as the nontoxic antimicrobial agent[38]. The experimental results obtained from the use of sodium azide as a metabolic inhibitor in Figure 5 indicate that it strongly inhibited the removal of Cd(II) (Figure 5-A), Ni(II) (Figure 5-B), and Zn(II) (Figure 5-C) at concentrations of 10 mg/L by all Rhodobacter species. Percentage reductions of Cd removal efficiencies were 63, 55, and 44% in R. blasticus, R. capsulatus, and R. sphaeroides respectively, compared to a set of untreated cells. Percentage reductions of Ni removal efficiencies were 38, 35, and 29% by R. blasticus, R. capsulatus, and R. sphaeroides, respectively. Finally, percentage reductions of Zn removal efficiencies were 6, 6, and 2% by R. blasticus, R. capsulatus, and R. sphaeroides, respectively.
3.3.2. Metabolic dependent study
Results of the removal of toxic heavy metals by Rhodobacter species showed that all strains removed toxic heavy metals in the presence of nutrients when compared with those of no added nutrients (Figure 6). When the nutrients were added to the medium, R. blasticus, R. capsulatus, and R. sphaeroides eliminated 85, 68, and 66% of Cd(II), respectively. In the absence of nutrients, the removal efficiencies for Cd (II) by R. blasticus, R. capsulatus, and R. sphaeroides decreased by about 69, 56, and 45%, respectively. The removal efficiencies for Ni (II) by R. blasticus, R. capsulatus, and R. sphaeroides were reduced by 42, 39, and 31%, respectively; the removal efficiencies for Zn removal efficiencies by R. blasticus, R. capsulatus, and R. sphaeroides were decreased by 8, 7, and 4%, respectively.
4. Discussion
Both growth rates and biomass generation rates of microorganisms are profoundly influenced by metal ion concentrations. Usually, growth rates and biomass generation rates are inversely proportional to the toxicity of heavy metals. Our findings corresponded well to this notion; Figures 1~3 showed that growth rates decrease with increasing toxic metal concentration in modified ATCC medium supplemented with Cd(II), Ni(II), and Zn(II). The decline in growth due to toxic heavy metal stress differed in the three Rhodobacter species; growth rate declines were highest in R. blasticus, followed by R. capsulatus and lowest in R. sphaeroides in the presence of Cd(Figure 1), Ni(Figure 2), and Zn(Figure 3). Our study's results agree with those of numerous investigations, although the types of microorganisms used were different[42-45]. Acikel and Ersan[44] documented that the growth rates of R. delemar declined with increases in Ni concentrations in concentration ranges of 0 mg/L to 50 mg/L. Dursun [42] reported that two species of fungi (Aspergillus niger and Rhizopus arrhizus) were examined for their growth rate in the presence of cadmium ion (Cd2+) and copper ions (Cu2+) in the concentration ranges 0~100 mg/L. While growth inhibition was observed in both fungi species, biomass production in R. arrhizus was higher than that in A. niger, so Dursun et al.[42] concluded that R. arrhizus seemed to be a more active and sturdy means for removal of Cd2+ and Cu2+ from wastewaters than A. niger.
Furthermore, increases in concentrations of toxic heavy metals led to prolonged lag phases and reduced microbial biomass in all three Rhodobacter species (Figures 1~ 3). R. blasticus showed a maximum prolonged lag phase of 63 hours in the presence of Cd(II), 54 hours in the presence of Ni(II), and 48 hours in the presence of Zn(II), compared to 24 hours in plain media. R. capsulatus showed a prolonged lag phase of 54 hours during the log phase in the presence of Cd(II), 48 hours in the presence of Ni(II), and 36 hours in the presence of Zn(II) compared to 24 hours in plain media. Finally, R. sphaeroides showed a prolonged lag phase of 39 hours in the log phase in the presence of Cd(II), Ni(II), and Zn(II), compared to 24 hours in plain media. Similarly, Bar et al.[43] showed an extended lag phase in K. pneumoniae of 16 hours in the presence of Co2+ compared to 4 hours in the presence of Pb2+ and 2 hours in the absence of toxic metals. Wei et al.[46] also reported that low concentrations of heavy metals (0.5 mM Pb and 1.0 mM Zn) showed little impact on biomass growth, although at high concentrations ( > 1.5 mM Pb and > 2.0 mM Zn) lengthened lag phase and decreased biomass concentrations were observed in bacterial isolates. In summary, it appears that all Rhodobacter species investigated in this study showed relatively high specific growth rates and biomass compared to other bacteria and fungi even in the presence of toxic heavy metal stress for concentrations below 20 mg/L (Figures 4, 5, and 6) and therefore possessed an ability for potential bio removal and further bioremediation of heavy metals in the industrial wastewater.
Unlike organic pollutants, toxic heavy metals are not biodegraded into less toxic or non-toxic substances by bacteria because of their chemical characteristics[22]. These metals can not be non-degradable and tend to bioaccumulate in the cells eventually causing health risks. Purple nonsulfur bacteria are a group of microorganisms that are known for removing toxic heavy metals. The present study demonstrated that three Rhodobacter species (R. blasticus, R. capsulatus, and R. sphaeroides) could effectively remove Cd(II) and Ni(II) from an aqueous solution (Figure 4). In particular, R. blasticus showed a higher removal efficiency of Cd(II) and Ni(II) compared to R. capsulatus and R. sphaeroides. There have been few studies on the removal of toxic heavy metals by R. blasticus. On the other hand, R. sphaeroides is the most studied microorganism for hydrogen production and bioremediation among purple nonsulfur bacteria[21,31,47,48]. Like other species of Rhodobacter, R. sphaeroides is a metabolically diverse organism that is capable of many modes of growth including aerobic respiration, anaerobic anoxygenic photosynthesis, fermentation, and diazotrophic growth[49]. Bai et al.,[14] reported that Rhodobacter sphaeroides was involved in the uptake and the bioremediation of synthetic solutions of cadmium sulfate. Soluble cadmium (40 mg/L) was almost completely removed from the solution after 42 h (removal rate: 97%). They concluded that abiotic precipitate did not play a great part in the whole process of removal, while bio removal of Cd by the sulfide precipitate was a significant contributor. This result agreed with that reported in the literature[50-52].
The removal efficiency for Ni(II) by R. blasticus, R. capsulatus, and R. sphaeroides at 5, 10, 20, and 80 mg/L of concentrations of Ni solution was approximately 50%. On the other hand, the use of three Rhodobacter species to remove Zn(II) was not practical as Zn(II) removal efficiencies were below 20% (Figure 4) for all three species and under different concentrations of Zn solution (5, 10, 20, and 80 mg/L). The removal efficiencies for heavy metals used by all Rhodobacter species were in the following order: Cd (II) > Ni (II) > Zn (II). Previously, Panwichian et al.,[53] reported that strains of R. sphaeroides KMS24 and Rhodobium marium NW16 could get rid of toxic heavy metal ions (Cu2+, Zn2+, Cd2+) in the polluted shrimp pond in the aerobic-dark and microaerobic-light conditions. They suggested that the exopolymeric substances produced by the two strains played a great role in the accumulation of those heavy metals, and even they grew much better in the liquid medium including the higher concentration of toxic heavy metals than that of contaminated shrimp pond. R. capsulatus also absorbed the metal trivalent aurum[32]. In a separate study, Rhodovulum sp. PS88 and R. spaheroides S were also shown to eliminate the cadmium in the batch culture system. Under both heterotrophic (aerobic-dark) and photoheterotrophic (anaerobic-light) conditions, the strain PS88 demonstrated a higher constant value and hence the higher uptake of Cd compared to R. sphaeroide S[30].
The principal mechanisms used by purple nonsulfur bacteria for the removal of metal ions are considered to include biosorption and bioaccumulation processes[54-56]. The difference between the two is dependent on the energy required. The former does not need the energy whereas the latter requires the energy. In other words, biosorption is the entrapment of metal ions by binding sites on the cellular surface, which is a non-specific, fast, and metabolic-independent uptake, known as “bioabsorption” or “passive uptake”, performed by both living and dead cells[14,57-60]. Bioaccumulation is the result of interaction with the metabolic cycle after the cell enters. This mode of action, slower than subsequent biosorption, also is known as “the active uptake” and is performed only by the actively growing cell cultures[19,61]. It is well known that both these processes are involved in removing the toxic heavy metals from water as not only living cells but also dead cells which could be bound to the toxic heavy metals either actively, or passively or by a combined two processes[21,62,63].
Some purple nonsulfur bacteria may use more than one mechanism to eliminate the metal ions and hence are to be more effective as compared to the ones that use only one mechanism[22]. The type of mechanism to be used by the organism is dependent on the properties of the metal ion that it is exposed to. Our metabolic inhibition (Figure 5) and metabolic-dependent (Figure 6) studies showed that the removal processes of toxic heavy metals by Rhodobacter species might involve both bioaccumulation (intracellular uptake) and biosorption (surface binding). In other words, Both bioaccumulation (intracellular uptake inside cell and biosorption-energy dependent process-metabolic dependent activity-active removal) (attachment to bacterial cell surface-energy independent process-metabolic independent activity-passive removal) were involved in the removal of three metals.
It is evident from Figure 5 that sodium azide (1 M) significantly reduced the ability of all strains to remove Cd(II), Ni(II), and Zn(II). In other words, when living cells were used, it meant that bioaccumulation was involved in the removal of toxic heavy metals. The results of the present study corresponded well with those found in the earlier experimental study in purple nonsulfur bacteria[33]. It appears that the intracellular accumulation of toxic heavy metals is governed by energy-dependent transport systems. This was also supported by the increment of the toxic heavy metal removal ability after supplementing nutrients to the toxic heavy metal solution(Figure 6). This indicated that metabolic processes promoted the uptake of toxic heavy metals into the cells. Prado Acosta et al.[64] indicated that metabolic-dependent processes were also energy-dependent, demanding an active energycreating system by the cells and presumably via particular transport systems.
The results of this study suggest that R. blasticus could be the most potential means of bioremediation to remove cadmium in the industrial wastewater. On the other hand, the tolerance observed towards heavy metals allows proposing the employment of R. blasticus in the degradation of organic pollutants in metal-contaminated environments. Furthermore, future work should focus on the modification in the outer membrane proteins of R. blasticus with potential bioremediation properties for improving metal binding abilities and the factors involved in improving in situ bioremediation strategies.
4. Conclusions
Our results demonstrated the potential bioremediation capacity of toxic heavy metals from liquid media by different Rhodobacter species. Addition of toxic divalent cations such as cadmium (II), nickel (II), and zinc (II) produced a reduced growth rate at the stationary phase, whereas the lag period may become longer. In this study, it was shown that three Rhodobacter species (R. blasticus, R. capsulatus, and R. sphaeroides) could effectively eliminate Cd(II) and Ni(II) from an aqueous solution. In particular, R. blasticus showed a higher removal efficiency of Cd(II) than R. capsulatus and R. sphaeroides. It appears that the processes of toxic heavy metals removal by purple nonsulfur bacteria involve intracellular uptake (bioaccumulation) and surface binding (biosorption). Overall, our results suggest that R. blasticus may be the most potent means of bioremediation to remove cadmium in the water of the three tested Rodobacter species. It appears that this may be due to the more resistance and resulting greater growth rate of R. blasticus to Cd than the tested other species, resulting in the increased removal of cadmium.