ISSN (0970-2083)
Nourah Hassan Alzahrani1 and Mervat Morsy Abbas Ahmed El-Gendy2*
1Faculty of Science, Department of Biological Sciences, University of Jeddah, Jeddah 80203, Saudi Arabia.
2Chemistry of Natural and Microbial Products Department, National Research Centre, Dokki, Giza 12622, Egypt
Received Date: 28 February, 2019; Accepted Date: 04 July, 2019
Visit for more related articles at Journal of Industrial Pollution Control
Zinc and mercury are causing a problem worldwide owing to highly toxicity and this problem will intensify if obligatory actions not taken. In present study searching about bioactive fungal strain can. We screened ten endophytic fungal species derived from different plants grow in polluted sites for tolerating and removing both zinc and mercury efficiently from aqueous solutions. Among these isolates Aspergillus. tubingensis Merv4 showed the highest resistant toward mercury (Hg2+) with the highest tolerance against zinc (Zn2+). Moreover, simultaneously it was tolerant to different other toxic metals like pb2+, Cr6+, Cd2+ and Ni2+ with varied degree of resistant. Dead biomass of A. tubingensis Merv4 strain showed capable of totally removing (100%) of both zinc and mercury, respectively from aqueous solution under optimized conditions. In real industrial disposal water the maximum removal values of zinc and mercury were (96% and 91%, respectively) by dead biomass of A. tubingensis Merv4 under optimized conditions. In near future these promising fungi can be used in bioremediation of mercury, zinc and other metal contaminates from industrial wastewaters onto microbial dead biomass.
Zinc, Mercury, Removal, Phylogenetic, A. tubingensis, Tolerance
Heavy metal contamination is widespread globally due to manufacturing which seriously threatens the ecosystem significantly, principally the health of individuals because of their severe toxicity. With the purpose of reduce the effects of metal pollutions; wastewater must be treated before disposal into water bodies. Recently, zinc and mercury toxicity have been increased extensively (Tahir, et al., 2017) as a result of abundant industrial purposes for example, pharmaceuticals, cosmetics, electrical appliances, pulp and paper industries (El-Gendy and El-Bondkly, 2016). Biological treatment is an important technique to reduce metal contamination because of its low cost and high efficiency. The United States environmental protection agency (EPA) reported mercury as a polluted priority because it can pass simply into the blood brain barrier and Hg2+ at high concentrations causes dysfunction in the lung, kidney, chest pain and shortness of breath.
Many previous reports recommended the isolation of resistant fungi to heavy metals and the usage of their biomass for removing metal pollutions from industrial effluents like the like Rhizopus stolonifer (lead, cadmium, copper, and zinc), Pleurotus ostreatus HAAS (lead, cadmium, and chromium), Rhodotorula mucilaginosa (mercury, copper, and lead), Aspergillus niger (removal of lead, cadmium, copper, and nickel), A. niger (aluminum, iron, lead, and zinc), immobilized cells of A. niger (copper, manganese, zinc, nickel, iron, lead, and cadmium), endophytic Drechslera hawaiiensis (cadmium, copper and lead), endophytic penicillium lilacinum (cadmium, copper and lead) (El-Gendy, et al., 2011 and 2017; Acosta-Rodríguez, et al., 2018; Martínez-Juàrez, et al., 2012). Furthermore, the World Health Organization recommended that the maximum acceptable concentration of zinc in drinking water is 0.05 mg/L. higher concentrations in humans can cause anemia, nausea, vomiting, nephritis, corrosive effect on skin, metal emission fever, damage pancreas, lungs and nerve membrane (Mali, et al., 2014).
The aim of this work is to examine some mineralresistant fungal strains that can be used to treat zinc and mercury contamination efficiently with optimizing the remediation process parameters including process time, absorbed dose, temperature and pH to improve the biological absorption of zinc and mercury under batch mode to potent safe removal of hazardous metal in the near future.
Microorganisms and culture conditions Ten endophytic fungal strains belong to different 8 genera namely, Rhizopus oryzea (Merv2), Aspergillus luchuensis (Merv3), Aspergillus tubingensis (Merv4), Monacrosporium elegans (Merv5), Penicillium duclauxi (Merv6), Curvularia lunata (Merv7), Penicillium lilacinum (Merv8), Drechslera hawaiiensis (Merv9), Verticillium Fungicola (Merv10) and Pestalotiopsis clavispora (Merv11) were isolated and identified according to morphological, physiological and biochemical characterizations in a previous study (El-Gendy, et al., 2011). Fungal inoculums were obtained after culturing in potato dextrose broth in dark for 10 days at 28ºC and 180 rpm. Endophytic fungi were maintained on potato dextrose agar and reserved at 4°C.
Experimental reagents and apparatus
Metals under study, sodium hydroxide and nitric acid were of analytical grade (Merck), stock solutions of mercury and zinc as well as the standard calibration were performed, pH was amended using HNO3. Preparation of adsorbent for uptake experiments Inoculum of 106 spore/mL ten days old culture of each fungal strain were inoculated into 250 mL Erlenmeyer flasks containing 100 mL of YMG medium (yeast extract, 5; malt extract, 10; glucose, 10, g/L) under static conditions in dark for ten days at 28ºC and then fungal biomasses were harvested by passing 100 mL of each fungal culture through a previously weighted filter papers (Whatman No. 1). The harvested mycelia were washed, autoclaved at 121°C, dried in oven at 60°C until reach constant weights and then stored at - 20°C (El-Gendy and El- Bondkly, 2016; El-Gendy, et al., 2011 and 2017).
Adsorbate solution preparations
Various concentrations of metal solutions 100 mg/L, 200 mg/L, 300 mg/L, 400 mg/L and 500 mg/L of mercury chloride and zinc chloride were prepared.
Phylogenetic analysis of the selected biosorbent fungal strain
Extraction and purification of genomic DNA of the most active biosorbent endophytic fungal strain (Merv4), amplification of ribosomal DNA and the PCR program were done according to a previous study (El-Bondkly, 2006 and 2012; El-Bondkly and El-Gendy, 2012; White, et al., 1990). Sequence relationships were recognized by the BLAST tool from the National Center for Biotechnology Information (NCBI). Phylogenetic analyses were conducted with the neighbor-joining method through MEGA6 software.
Batch mode adsorption experiment
In this study, biosorption capacity of fungus was determined in batch conditions. Adsorption was performed using died fungal biomass wherein weighed amount of fungal biomasses were added to constant concentration of zinc and mercury metal solution, individually. Mixtures were then kept at room temperature, taken sample were withdrawn at different contact time intervals. The adsorbent and adsorbate were separated through centrifugation at 3000 rpm for 5 min. The residual metal ion concentration was determined by A Perkin-2380 atomic absorption spectrophotometry.
Removal of zinc and mercury under different adsorption mathematical models
Adsorption data achieved in this study were defined using Langmuir and Freundlich isotherms. Langmuir isotherm equation stated as RL= 1/1+bCâÃâæ, where RL and C are equilibrium parameter and initial heavy metal concentration. The RL refer to the profile of isotherm if it unfavorable (RL > 1), linear (RL= 1), favorable (0 < RL < 1) or irreversible (RL= 0). The Freundlich equation is prvided as: qexp= n Ce Kf, where qexp refer to quantity of absorbed metal at time (mg/g), Ce is the equilibrium concentration (mg/L) but Kf (mg/g) and n (g/L) are the equilibrium constants (Muneer, et al., 2013; El-Morsy, et al., 2013).
Effect of initial metal concentration
Zn2+ and Hg2+ solutions of 100, 200, 300, 400 and 500 mg/L at pH 5 were added individually a fixed biomass of 200 mg/L in 250 mL Erlenmeyer flasks in triplicate at room temperature for different times (1, 2, 4, 6, 8, 12 and 24 h) with shaking at 180 rpm for mixing the samples well. Experimental and control (contain no biomass) were analyzed using A Perkin-2380 atomic absorption spectrophotometry (Mali, et al., 2014; Muneer, et al., 2013; El-Morsy, et al., 2013).
Effects of pH and temperature at different treatment times
We evaluate the impact of pH values equal to 4.0, 4.5, 5.0, 5.5, 6.0 and 6.5 at various time periods (1, 2, 4, 6, 8, 12 and 24 h) on Zn2+ and Hg2+ adsorption by Merv4 dead biomass to assess optimum pH and the equilibrium time for removing Zn2+ and Hg2+. On the other hand, the impact of different temperature values (30°C, 35°C, 40°C and 45°C) on reduction potentially of Zn2+ and Hg2+ was evaluated. 200 mg/L of biomass was added to 50 mL of Zn2+ or Hg2+ solution at an optimum concentration for each metal in triplicate and then analyzed at different treatment times.
Factory effluents
The heavy metals of wastewater resulted from electrical instruments electroplating industries in Egypt removal by the selected strain were evaluated under optimized conditions.
Determination of zinc and mercury tolerance of endophytic fungi
Metal tolerance was estimated in terms of minimum inhibitory concentration (MIC) in agar plates supplemented with different concentration ranged from 50 to 1000 μg/mL of Cd (II), pb (II), Cu (II), Hg (II), Ag (I), Cr (VI), Ni (II), Zn (II), Fe (III) or Al (III) and inoculated with 106 spore/ml incubated at 30 ºC for 10 days as previously described (El-Gendy, et al., 2011; Bedioui, et al., 2015; Akhtar, et al., 2013).
Evaluation the bioremoval potentiality of isolated endophytic fungi as biosorbents
Studies in Table 1 showed the quantity of zinc and mercury metals removed (%) from aqueous solutions by the biomasses of different endophytic fungi. Among them, Aspergillus tubingensis Merv4 showed the highest removal of zinc (80.13%) followed by Penicillium lilacinum MERV8 (71.69%) and Monacrosporium elegans MERV5 (70.09%), respectively but the highest biosorption of mercury from aqueous solutions was obtained by A. tubingensis Merv4 (70.52%) followed by M. elegans Merv5 (61.25%) and Pestalotiopsis clavispora Merv11 (51.74%), respectively. So the hyperactive strain A. tubingensis Merv4 was selected for the further bioremoval studies. The comparison of the most active biosorbent strain Merv4 with the previous sequences data of fungi within genomic database banks supported 100% similarity with A. tubingensis (Fig. 1). Accordingly the effective strain Merv4 was identified and designated as A. tubingensis Merv4.
Fungal strain | Removal (%) | |
---|---|---|
Zn2+ | Hg2+ | |
Rhizopus oryzea Merv2 | 52.16 | 28.84 |
Aspergillus luchuensis Merv3 | 67.37 | 50,08 |
Aspergillus tubingensis Merv4 | 80.13 | 70.52 |
Monacrosporium elegans Merv5 | 70.09 | 61.25 |
Penicillium duclauxi Merv6 | 48.48 | 37.10 |
Curvularia lunata Merv7 | 35.81 | 49.32 |
Penicillium lilacinum Merv8 | 71.69 | 44.00 |
Drechslera hawaiiensis Merv9 | 65.42 | 49.95 |
Verticillium fungicolaMerv10 | 35.32 | 11,97 |
Pestalotiopsis clavispora Merv11 | 59.00 | 51.74 |
Table 1. Efficiency of different fungal strains in the removal (%) of Zn2+ and Hg2+ from aqueous solution.
In the mercury detoxification process, work is still necessary to explain the occurrence and biodiversity of microbiome under pressure of metal ions for use in the biological treatment of these toxic contaminants, individually or collectively to achieve greater efficiency. Also, some mercury biosorbent fungi can detoxify mercury with ability to remove other toxic metals such as cadmiumand lead (Joo and Hussein, 2012). Martínez-Juàrez, et al. (2012) evaluated the adsorption ability of 14 fungal biomasses toward mercury including Aspergillus flavus, A. fumigatus, Helminthosporium sp., Cladosporium sp., Mucor rouxii, and Candida albicans and they supported the biomasses of M. rouxii for efficient removing of metal in solution. The efficiency of endophytic fungi as biosorbet materials for toxic heavy metals was reported by many authors such as El-Gendy, et al. (2011) and Pietro-Souza, et al. (2017).
Adsorption isotherms
To define the affinity among the metal ions and the waste biomass Langmuir and Freundlich adsorption models were used. Obtained results showed that the Langmuir equation describes well equilibrium adsorption data of zinc and mercury by dead biomass of A. tubingensis Merv4 (Table 2). The values of Qo (95.23 and 147.05 mg/g for Zn2+ and Hg2+, respectively), R2 (0.94 and 0.98 for Zn2+ and Hg2+, respectively) and the small b values (0.085 L/mg for Zn2+ and 0.040 L/mg for Hg2+) obtained in this research implicit strong binding of metal ions into A. tubingensis Merv4 biomass. El-Morsy, et al. (2013) and Muneer, et al. (2013) examined the biosorption capacity of fungal strains for Zn (II) and Hg (II) biosorption from aqueous effluents and they also stated that the Langmuir equation describes well the biosorpton procedure with the highest biosorption capability for the dead sorbents.
Metal ions | Freundlich isotherm model | Langmuir isotherm model | |||||
---|---|---|---|---|---|---|---|
Qexp (mg/g) | n (g/L) | KF (mg/g) | R2 | QâÃâæ (mg/g) | b (L/mg) | R2 | |
Zn2+ | 35.51 | 5.37 | 4.75 | 0.60 | 95.23 | 0.085 | 0.94 |
Hg2+ | 31.25 | 2.56 | 3.38 | 0.069 | 147.05 | 0.040 | 0.98 |
Table 2. The Langmuir and Freundlich isotherm models for adsorption constants for Zn2+ and Hg2+ by autoclaved A. tubingensis Merv4.
Effect of various concentrations of Zn2+ and Hg2+ in aqueous solutions
The biosorption efficiency was evaluated with variable initial metal concentrations from 100 to 500 mg/L, individually. We observed that with the increased concentration of metal ion, its absorption increased and a plateau occurred for both heavy metals. Total removal 100% of 400 and 500 mg/L of zinc was obtained after treatment for 24 and 8 h of incubation periods, respectively while removing of 85% and 98% of 100 and 200 mg/L of mercury occurred after 24 h of treatment (Table 3). These results may be clarified by increasing the number of competing ions on the available binding sites as well as because of the inadequate active sites on biomass at greater concentrations. Similar findings were described for the deletion of zinc from effluents by adsorption into fungal biomass by Mali, et al. (2014) and Hg (II) utilization of mercury contaminant by A. flavus strain KRP1 (Kurniatia, et al., 2014).
Contact time(h) | Metal concentration (mg/L) | |||||||||
---|---|---|---|---|---|---|---|---|---|---|
100 | 200 | 300 | 400 | 500 | ||||||
Removal potentiality (%) | ||||||||||
Zn2+ | Hg2+ | Zn2+ | Hg2+ | Zn2+ | Hg2+ | Zn2+ | Hg2+ | Zn2+ | Hg2+ | |
1 | 38 | 40 | 41 | 38 | 45 | 30 | 50 | 18 | 52 | 12 |
2 | 50 | 51 | 55 | 49 | 61 | 41 | 64 | 31 | 70 | 29 |
4 | 59 | 59 | 60 | 60 | 65 | 52 | 73 | 33 | 80 | 31 |
6 | 68 | 69 | 73 | 72 | 80 | 61 | 83 | 37 | 90 | 33 |
8 | 74 | 80 | 80 | 80 | 87 | 65 | 92 | 39 | 100 | 39 |
12 | 77 | 82 | 80 | 85 | 90 | 71 | 97 | 40 | 100 | 40 |
24 | 81 | 85 | 90 | 98 | 97 | 75 | 100 | 42 | 100 | 42 |
Table 3. The effect of the concentration of zinc and mercury in solution on the removal by A. tubingensis Merv4 at different contact times.
Effect of different pH values in removing Zn2+ and Hg2+ processes
pH of the solutions plays a major role in the biosorption process because it affects the balance by influencing the differentiation of ions in the solution. Metal ions charge in the solution and the availability of active sites for heavy metals attraction onto the surface of biosobent depend mainly onto pH of the working solution. With a pH increase of 4.0 to 6.5 zinc removal increased (Table 4). Zinc at pH 5.0, 5.5, 6.0 and 6.5 was totally removed after (8, 12, and 24 h), (6, 8, and 12 h), (4, 6, and 8 h) and (4, and 6 h), respectively (Table 4). The highest Hg (II) biosorption was detected at pH 5.5 after 12, and 24 h of treatment ( 100%, Table 4) and then decreased by (13% and 20%) and (25% and 40%) at pH 6.0 and 6.5 after 12, and 24 h contact times in aqueous solution, respectively. At lower or higher pHs the bioremoval of these heavy metals was decrease due to in acidic pH, protonated cell wall components negatively influenced the adsorption capacity of biomass and with increase in pH the negative charge density on the cell surface increased by the deprotonating of the metal binding sites. Then the efficient use of fungal genera and species in biological treatment of Zn2+ and Hg2+ is greatly affected by pH (El-Gendy and El- Bondkly, 2016; El-Gendy, et al., 2011and 2017). Effect of varying temperatures on removal of Zn2+ and Hg2+
Contact time (h) | Reduction (%) of zn2+ and Hg2+ + at different pHs | |||||||||||
---|---|---|---|---|---|---|---|---|---|---|---|---|
4 | 4.5 | 5.0 | 5.5 | 6.0 | 6.5 | |||||||
Zn2+ | Hg2+ | Zn2+ | Hg2+ | Zn2+ | Hg2+ | Zn2+ | Hg2+ | Zn2+ | Hg2+ | Zn2+ | Hg2+ | |
1 | 20 | 29 | 23 | 40 | 29 | 45 | 38 | 50 | 38 | 50 | 38 | 50 |
2 | 38 | 33 | 40 | 49 | 45 | 62 | 50 | 64 | 64 | 64 | 54 | 64 |
4 | 39 | 44 | 41 | 52 | 50 | 69 | 60 | 73 | 100 | 93 | 100 | 73 |
6 | 42 | 47 | 46 | 59 | 62 | 77 | 100 | 83 | 100 | 93 | 100 | 63 |
8 | 45 | 50 | 50 | 59 | 100 | 81 | 100 | 92 | 100 | 92 | 60 | 82 |
12 | 48 | 58 | 57 | 64 | 100 | 85 | 100 | 100 | 63 | 87 | 52 | 75 |
24 | 49 | 65 | 60 | 70 | 100 | 85 | 93 | 100 | 50 | 80 | 49 | 60 |
Table 4. Reduction potentially of Zn2+ and Hg2+ by A. tubingensis Merv4 at different pHs with different contact times.
Maximum zinc absorption capacity was found at 30°C after 12 to 24 h contact time (100%) as well as at 35°C after 8 h of incubation and then the adsorption capacity of died A. tubingensis Merv4 biomass reduced with temperature higher than 35°C (62% and 60% at 40°C and 45°C, respectively, Table 5).
Contact time (h) | Reduction (%) of Zn2+and Hg2+ at different temperatures | |||||||
---|---|---|---|---|---|---|---|---|
30°C | 35°C | 40°C | 45°C | |||||
Zn2+ | Hg2+ | Zn2+ | Hg2+ | Zn2+ | Hg2+ | Zn2+ | Hg2+ | |
1 | 38 | 50 | 39 | 50 | 20 | 41 | 13 | 33 |
2 | 50 | 64 | 60 | 64 | 28 | 52 | 21 | 39 |
4 | 59 | 73 | 76 | 73 | 39 | 56 | 32 | 42 |
6 | 70 | 83 | 89 | 83 | 49 | 61 | 43 | 44 |
8 | 80 | 92 | 100 | 92 | 52 | 70 | 49 | 50 |
12 | 100 | 100 | 100 | 100 | 74 | 75 | 63 | 57 |
24 | 100 | 100 | 100 | 100 | 62 | 80 | 60 | 70 |
Table 5. The effect of temperature on reduction potentially of Zn2+ and Hg2+ by A. tubingensis Merv4 at different contact times.
On the other hand, Hg2+ was totally adsorbed from aqueous solution (100% removal) after 12 to 24 h of treatment at 30-35°C then adversely affected (80% at 40°C and 70% at 45°C, Table 5). Temperature of the process can be crucial in energy-based mechanisms in heavy metal absorption by fungi as reported by Martínez-Juàrez, et al. (2012) for mercury absorption by fungus M. rouxii IM-80.
Determination of A. tubingensis Merv4 resistance profile against different heavy metals
Aspergillus tubingensis Merv4 showed resistance to heavy metals at variable level as indicated by the MIC value of these metals towards them (Table 6). MIC values of cadmium, lead, copper, mercury, silver, chromium (VI), nickel, zinc, ferric and aluminum ions were found to be 650, 510, 700, 615, 430, 500, 1000, 810, 422, and 1000 μgmL-1, individually. These data have confirmed endophytic fungi isolated from manufacturing zone as potential multi-metal resisted fungi. It seems that the constant exposure of fungal community in the manufacturing zone against the heavy metals of effluents has exerted selective pressure on the fungal population, leading to the development of multi resistance to different heavy metals. Our results are consistent with the previous study of El-Gendy, et al. (2017); Bedioui, et al. (2015); Akhtar, et al. (2013) and Alzahrani, et al. (2017).
Metal ions | MIC (µg/mL) | Reduction of metal from industrial waste water (%) |
---|---|---|
Cd2+ | 650 | 70 |
Pb2+ | 510 | 81 |
Cu2+ | 700 | 65 |
Hg2+ | 615 | 91 |
Ag+ | 430 | 93 |
Cr6+ | 500 | 92 |
Ni2+ | 1000 | 90 |
Zn2+ | 810 | 96 |
Fe3+ | 422 | 70 |
Al3+ | 1000 | 91 |
Table 6. Minimum inhibition concentration (MIC) of different heavy metals against A. tubingensis Merv4 and removal of different heavy metals from industrial wastewater.
Removal of different metal ions from industrial wastewater using endophytic A. tubingensis Merv4 The biosorption activities of different metals including Zn2+ and Hg2+, which are the focus of our study from real effluents, were estimated with wastewater of electroplating industry using dead fungal biomass of A. tubingensis Merv4 under the optimized conditions (Table 6). It reduce metals ions as follow Cd2+ (70%), pb2+ (81%), Cu2+ (65%), Hg2+ (91%), Ag+ (93%), Cr6+ (92%), Ni2+ (90%), Zn2+ (96%), Fe3+ (70%) and Al3+ (91%), respectively from the real industrial wastewater. Our results are in agreement with the previous study of El-Gendy and El-Bondkly, (2016) and El-Gendy, et al. (2011 and 2017).
FTIR spectral analysis
Light shift was observed for other distinctive bands, which showed the involvement of functional groups in the adsorption process. The predominant peaks were attributed to OH (3200, 3500, 3442/cm), CH2 (2930, 2918, 2920/cm), C=O (1651, 1656, 1658/cm), amides (1447, 1440, 1431/cm), CO (1360, 1374, 1382/ cm) and C-O-C (1079, 1083, 1071/cm) for unloaded biomass, biomass loaded with zinc and biomass loaded with mercury, respectively (Table 7). Our data were in consistent with El-Gendy, et al. (2017) study.
Treatment | Functional groups/cm | |||||
---|---|---|---|---|---|---|
OH | CH2 | C=O | Amides | C-O | C-O-C | |
Unloaded Biomass | 3200 | 2930 | 1651 | 1447 | 1360 | 1079 |
Biomass + Zn2+ | 3500 | 2918 | 1656 | 1440 | 1374 | 1083 |
Biomass + Hg2+ | 3442 | 2920 | 1658 | 1431 | 1382 | 1071 |
Table 7. Wave numbers of the dominant peaks obtained by FTIR spectral analysis of unloaded biomasses and loaded biomasses with zinc and mercury individually.
This investigation indicated that mercury and zinc removal by different autoclaved fungal biomasses was estimated and then A. tubingensis Merv4 was selected as the hyperactive strain. The performance of the biosorbent was studied as a function of the operating circumstances, especially initial metal concentration, biomass dose, incubation time, different operation pH, temperature and time. It was proved that A. tubingensis Merv4 is a very promising biological material to remove the metal ion studied.
Copyright © 2024 Research and Reviews, All Rights Reserved