Microcoleus sp. is a versatile microorganism widely available in the environment and easily culturable. Hence, there is a progressing demand for wastewater treatment using this novel biosorption medium. The design of such a treatment method may be defined as an optimisation problem of algal dose and hydraulic retention time for attaining an adequate removal efficiency of heavy metals (Cr6+, Ni2+, and Zn2+) and nutrients (PO43- and NO3-). Batch experiments on synthetic wastewater were conducted for algal doses varying from 0.5 to 25 g/L and hydraulic retention times from 1 to 7 days. Significant removal efficiencies of greater than 90% were observed for the heavy metals, 75% of PO43- removal, and no removal of NO3- was found under continuous daylight. The single-factor ANOVA test confirms the statistical significance of the varying parameters on the pollutant removal efficiency. Langmuir and Freundlich's adsorption isotherms indicate satisfactory adsorption of the contaminants about the separation factor and the adsorption intensity constant. The R2 > 0.67 and RMSE < 0.21 suggest a good fit of the modelled data. Following this, the study suggests that the use of Microcoleus sp. is a prospective bioremediation technique for industrial and municipal wastewater.

  • Novel use of Microcoleus sp. as a means of bioremediation.

  • Detection of the pollutant removal efficiency of Microcoleus sp.

  • Removal of heavy metals and nutrients from synthetic industrial and municipal wastewater.

  • Data analysis using Langmuir and Freundlich isotherms, RMSE, and ANOVA tests.

Microcoleus sp. is a suitable model organism since it is widely available, easily identifiable, isolable, and culturable (Dvořák et al. 2012). They can be found within soil crusts, freshwater epipelon, and other subaerophytic environments (Garcia-Pichel et al. 2001; Boyer et al. 2002; Komarek & Anagnostidis 2005; Hašler et al. 2012). They are mat-forming, unbranched, uniform, and filamentous/colonial cyanobacteria. Despite being so accessible, the use of this species has not been in the limelight. Microcoleus sp. has been studied for oil degradation and soil crust restoration (Sorkhoh et al. 1995; Al-Hasan et al. 1998; Lan et al. 2012; Lababpour & Kaviani 2016). A study by Paniagua-Michel & Garcia (2003) considers the applicability of constructed microbial mats, including Microcoleus sp., in removing nutrients from shrimp culture effluent. However, no studies have been found with this specific species to determine its independent and unassisted removal efficiency of heavy metals and nutrients from effluent.

Industries, municipal wastes, and agriculture, aided by industrialisation, urbanisation, and technological development, contribute to the entrance of toxic pollutants into the environment. Two common contaminants in the environment are heavy metals and nutrients. Heavy metals in industrial effluent are hazardous to the environment. Heavy metals are metallic elements with a fairly high density, which makes them toxic even at low concentrations. The heavy metals in this study are Cr6+, Ni2+, and Zn2+ since they are the most hazardous pollutants due to their complex behaviour (DoE, Bangladesh). Correspondingly, eutrophication is caused by the presence of nutrients (nitrogen and phosphorus) in the form of nitrate, nitrite, ammonia/ammonium, or phosphate (Kosaric et al. 1974; Chan et al. 2014).

The health hazards associated with heavy metals are headache, dermatitis, lethargy, cancer, organ damage, damage of the nervous system, and even death; and those with the excessive presence of nutrients are gastric cancer caused by the conversion of nitrate to nitrosamines in the gastrointestinal tract and methaemoglobinaemia which further leads to respiratory problems, digestive problems, and even death of children (Kelter et al. 1997; Glass & Silverstein 1999; Foglar et al. 2005; Mayo & Hanai 2014). However, phosphate is only responsible for eutrophication which harms the aquatic fauna. Hence, disposing of them directly into water bodies harms all life forms. The freshwater content on Earth is 2.5%, of which only 31% is potable. Moreover, the spiralling water demand, water pollution, and the increasing shortage of freshwater resources necessitate wastewater reuse for worldwide sustainable development (Falkenmark & Widstrand 1992; Greenway 2005).

The maximum contaminated level (MCL) standards set by US EPA (Babel & Kurniawan 2003) indicate the acceptable concentrations of heavy metals along with the upper limits of the Total Nitrogen (TN) and Total Phosphorus (TP) content when being discharged into water bodies (US EPA 2012; see Table 1).

Table 1

Acceptable levels of contaminants for disposal in the environment

ContaminantAcceptable level (mg/L)
Cr6+ 0.05 
Ni2+ 0.20 
Zn2+ 0.80 
TN 
TP 
ContaminantAcceptable level (mg/L)
Cr6+ 0.05 
Ni2+ 0.20 
Zn2+ 0.80 
TN 
TP 

Conventional methods of heavy metal remediation include membrane filtration, coagulation and flocculation, oxidation, photocatalysis, and adsorption; those for nutrient removal are filtration, facultative ponds, advanced oxidation, adsorption, coagulation, activated sludge process, ion exchange, soil percolation, and constructed wetlands. Contrary to their effective pollutant removal efficiencies, these methods are not positively adopted by industries or treatment facilities since they require massive operation and maintenance expenditure, land area, and proficient operators. Consequently, the cost-effective alternative of the microalgae-based wastewater treatment process is gaining popularity.

Most algae can physically adsorb heavy metal ions to their bodies at the cell surface, both dead and alive (Aksu 1998; Satya et al. 2020). The proteins, lipids, and carbohydrates create a net negative charge on the cell surface, allowing them to act as binding groups for the positively charged heavy metals (Crist et al. 1981; Khummongkol et al. 1982; Gardea-Torresdey et al. 1990; Aksu 1998). Correspondingly, the study conducted by Sandau et al. (1996) reinforces the theory of biosorption of heavy metals by microalgae using a combined mechanism of extracellular and intracellular accumulation (Crist et al. 1988; Kuyucak & Volesky 1990; Sandau et al. 1996). Additionally, due to the photosynthetic property of microalgae, they uptake nutrients from wastewater for their metabolism and cellular growth. Microalgae form organic nitrogen from inorganic nitrogen (peptides, proteins, enzymes, chlorophyll, adenosine diphosphate, adenosine triphosphate), while inorganic phosphate generates adenosine triphosphate from adenosine diphosphate (Martinez et al. 1999; Gualtieri & Barsanti 2014). Blue-green microalgae can efficiently uptake pollutants in the range of 56–100% (Sibi 2016; Daneshvar et al. 2019; Moreira et al. 2019; Arias et al. 2020; Pham et al. 2020; Rueda et al. 2020; Touliabah et al. 2022). These data reinforce that phycoremediation is an excellent choice for an eco-friendly alternative.

Microalgae remove heavy metals and nutrients through the process of biosorption. The advantages offered by this method, out of many, include reduced energy costs and required chemicals, utilisation of the harvested biomass in food, feed, fertilisers and chemical production, reduction of carbon footprint, and zero toxic sludge generation (Schumacher & Sekoulov 2002; Brinza et al. 2007; Pittman et al. 2011; Singh & Olsen 2011; Arbib et al. 2014; Imanthi et al. 2023).

This study aims to fill in the knowledge gap and evaluate the adsorption capacity of Microcoleus sp. to see if it may be a state-of-the-art asset in the bioremediation field. Therefore, the efficiency of Microcoleus sp. as a low-cost biosorption medium is tested and analysed to apprehend the effect of different microalgal doses and hydraulic retention times on the uptake of the pollutants.

Microalgae sample preparation

The microalgae strain was collected in January 2021 from a pond near Shahjalal University of Science and Technology (Bangladesh, Sylhet, 24.9172° N, 91.8319° E). It was collected in a 1 L plastic bottle from which 100 mL was added to a synthetic BG-11 medium (Stanier et al. 1971). The BG-11 medium composition was as follows: K2HPO4·3H2O 0.04 g/L, MgSO4·7H2O 0.075 g/L, CaCl2·2H2O 0.036 g/L, Citric acid 0.006 g/L, Ferric ammonium citrate 0.006 g/L, EDTA (disodium magnesium salt) 0.001 g/L, Na2CO3 0.02 g/L, NaNO3 1.5 g/L, trace metal mix 1 mL/L; the trace metal mix consisted of H3BO3 2.86 g/L, MnCl2·4H2O 1.81 g/L, ZnSO4·7H2O 0.22 g/L, CuSO4·5H2O 0.079 g/L, NaMoO4·2H2O 0.39 g/L, and CoCl2·6H2O 0.05 g/L. The environmental factors that impact the culture are temperature, pH, oxygen, light intensity, and CO2. The surrounding temperature directly influences photosynthesis and the biochemical processes. Most algal species thrive at a temperature of 20–30 °C, a luminous intensity of 5,000–7,000 lx, and a pH of 6–8 (Béchet et al. 2017; Nouri et al. 2021). Photosynthesis is directly affected by extreme temperatures, pH, and light intensities. As a result, inhibition of microalgal growth occurs (Atkinson et al. 2003; Juneja et al. 2013; Krzemińska et al. 2014). Hence, the batch cultures were conducted in 1 L Erlenmeyer flasks for 7 days at 26 °C, pH of 7, light intensities of 5,000 lumens at a 16:8 photocycle (simulating natural daylight for synchronised light and dark phases), and continuous aeration using aquarium pumps for atmospheric CO2 supply.

The algal strain was isolated by serial dilution 30 times. The dilution gave us fresh and pure microalgal biomass for mass culture. The mass culture was cultivated for 30 days under the same culture conditions. A large 60 cm × 20 cm tank with a capacity of 10 L was used for this purpose: a larger surface area allowed the mat forming Microcoleus sp. to expand easily. The growth rate of the microalgae in the mass culture tank had to be visually observed by its expansion and microscopic observation for healthy cells since the cells were not in a suspended state for spectrophotometric measurement. The microalgal strain was identified based on the morphological features of the species.

Synthetic wastewater

Chemically derived wastewater was used in this experiment. Usually, heavy metal ion concentrations in industrial effluents vary widely. However, a challenge in industrial effluent treatment is that low concentrations of heavy metals become difficult to remove and very few processes can successfully bring the levels below the MCL. Hence, to ascertain whether post-treatment is required, the Cr6+, Ni2+, and Zn2+ concentrations have all been kept at a low concentration of 20 mg/L to simulate industrial effluent. The stock solutions containing heavy metals and nutrients were prepared using K2Cr2O7 for Cr6+ ion, NiCl2·6H2O for Ni2+ ion, ZnCl2 for Zn2+ ion, K2HPO4·3H2O for PO43− ion, NaNO3 for NO3 ion, and (NH4)2SO4 for NH4+ ion. For the representation of industrial wastewater, 20 mL of each metal solution was mixed to obtain 1 L of synthetic wastewater with a concentration of 20 mg/L each. To simulate the difficult condition of municipal wastewater, the PO43− concentration was set at 170 mg/L, NO3 was set at 17 mg/L, and that of NH4+ was set at 100 mg/L (de-Bashan 2002; Olguín 2003; Zhou et al. 2012; Chaitee et al. 2022) by taking 170, 17, and 100 mL, respectively, from each of the stock solutions and adding them together to get 1 L in total finally.

Experimental procedure

Laboratory-scale batch experiments were done with synthetic wastewater. The algal mats were harvested using a spatula and sieve cloth and then washed with distilled water. The excess water from the mats was removed using a vacuum filter. The biomass was then divided into the required doses. A magnetic stirrer was used to constantly stir the biomass within the reactor to maintain the mat evenly distributed. For each data collection (variable dose-constant HRT and variable HRT-constant dose), three 1 L solutions of synthetic wastewater were used. The hydraulic retention time (HRT) was fixed at 3 days for the first experiment set with variable algal dose, with doses ranging from 0.5 to 25 g/L. For the second experiment set with variable HRT, the dose was fixed at 20 g/L with HRT varying from 1 to 7 days. The environmental conditions remained the same as the culture period conditions, except the light was continuously provided during the entire treatment. The initial and final data were then collected spectrophotometrically using the HACH DR6000™ UV Spectrophotometer; the system programs for Chromium (Hexavalent), Nickel, Zinc, Ammonia (Nitrogen), Nitrate (Nitrogen), and Phosphorous (Total) were adopted. A dilution factor of 10 was used to detect all the contaminants since the spectrophotometer has specific detection ranges.

Analysis procedure

The removal efficiency of the microalgae is calculated as a measure of percent sorption using the following formula:
(1)
where C0 (mg/L) and Ce (mg/L) are the pollutant concentrations before and after treatment, respectively.
The bio-uptake coefficient is defined as the amount of pollutant removed (mg) by the applied mass of microalgae (g) during a prescribed time (day). It is given by the following equation:
(2)

To express the feasibility of the treatment, biosorption modelling is done using the Langmuir and Freundlich isotherm models.

The Langmuir isotherm model (Ruthven 1984; Hamdaoui & Naffrechoux 2007) is linearly presented as
(3)
where the maximum adsorption capacity inferred from the intercept of the plot is given by Qm (mg/g), and the constant related to the free energy of adsorption is given by KL (L/mg).
Qe (mg/g) is the quantity of pollutants adsorbed by the microalgae. The following mass balance equation gives the measure of Qe (Vanderborght & Van Grieken 1977):
(4)
where the biomass dose is given by m (g) and the total volume of wastewater in the reactor is given by V (L).
A dimensionless separation factor, RL, represents the characteristics of Langmuir isotherm. For RL > 1, the adsorption is unfavourable; for RL = 1, the adsorption is linear; for 0 < RL < 1, the adsorption is favourable; for RL = 0, the adsorption is irreversible (Ayawei et al. 2017). RL is given as
(5)
where KF (L/mg) is the adsorption capacity determined from the intercept of the plot; n−1 is an adsorption intensity indicative constant determined from the slope of the plot; it is a constant indicating the strength of the adsorbent. For n−1 > 1, the adsorption is cooperative; for n−1 < 1, the adsorption is normal (Aziz et al. 2004).

Moreover, analysis of variance (ANOVA) for a single factor is used to determine the statistical significance of the variable parameters on the output; all the tests are conducted for a significance level of α = 0.05. Finally, to judge the fitness of the models, the coefficient of determination (R2) and root-mean-square error (RMSE) is calculated. R2 is a non-negative quantity, and its limits are 0 ≤ R2 ≤ 1. If it is close to zero, it indicates that the prediction is not much improved by knowing the independent variable. While it moves away from 0 to 1, knowing the independent variable will be increasingly useful in predicting the dependent variable (Islam 2004). As the value of RMSE approaches zero, the modelled and the experimented data are defined to be increasingly closely fitted with each other; when it is zero, they are exactly fitted with each other.

Biosorption capacity of Microcoleus sp.

Experiments were carried out in batches: three experimental setups for each variable. The average of the three readings was taken as Ce (mg/L). Additionally, the single-factor ANOVA test confirms the statistical significance of the varying algal doses and hydraulic retention times on the remediation efficiency.

For constant HRT and variable algal dose

The HRT was kept constant at 3 days, and the algal doses were taken as 0.5, 1, 3, 5, 7, 10, 15, 20, and 25 g/L. The removal efficiency of the biomass increased linearly with increasing dose in the case of Cr6+ and the maximum removal of 94% was found with 25 g/L of algal biomass. Similar results were found for Ni2+ and Zn2+, where 98% of Ni2+ and 97% of Zn2+ were removed at 15 and 25 g/L algal dose, respectively; also, 70% removal was found for PO43− at 25 g/L. Unfortunately, this particular species of algae showed very poor to zero removal of NO3 and NH4+. This can be explained by the study by Omoregie et al. (2004), where they found that Microcoleus sp. could not fixate nitrogen from the environment during the day.

From the obtained results, we can conclude that the microalgae could bring down the concentration of Zn2+ below MCL and could significantly lower the levels of Cr6+ and Ni2+. Phosphate levels lowered from 170 to 41.3 mg/L (see Figure 1(a)). A peak of biological activity was observed upon the first application of an algal dose to the wastewater at 0.5 g/L for all the contaminants (3.18 mg/g-day for Cr6+, 2.89 mg/g-day for Ni2+, 8.67 mg/g-day for Zn2+, and 11.78 mg/g-day for PO43−) (see Figure 1(b)). However, a reduction occurs afterward and continues to decrease steadily from 3 to 25 mg/L.
Figure 1

(a) Adsorption of contaminants for variable algal dose (g/L) at 5% error. (b) Steady-state uptake of contaminants for variable algal dose (g/L) at 5% error.

Figure 1

(a) Adsorption of contaminants for variable algal dose (g/L) at 5% error. (b) Steady-state uptake of contaminants for variable algal dose (g/L) at 5% error.

Close modal

For constant algal dose and variable HRT

Keeping the dose constant at 20 g/L, the HRT for experimentation was set at 1, 2, 3, 5, and 7 days. After 3 days, 92% removal was seen for Cr6+; 98% removal was seen for Ni2+ after 2 days; 99% of Zn2+ was removed after 7 days; however, the concentration went below MCL after 5 days; a maximum of 60% removal of PO43− was seen after 7 days; again, the algal mass was unable to efficiently uptake any nitrogen content in the wastewater. Likewise, levels of Zn2+ were brought down below the MCL, and Cr6+ and Ni2+ levels were brought down significantly, while phosphate was reduced from 170 to 33 mg/L (see Figure 2(a)).
Figure 2

(a) Adsorption of contaminants for variable HRT (days) at 5% error. (b) Steady-state uptake of contaminants for variable HRT (days) at 5% error.

Figure 2

(a) Adsorption of contaminants for variable HRT (days) at 5% error. (b) Steady-state uptake of contaminants for variable HRT (days) at 5% error.

Close modal

The biosorption activity for all trends peaks on the 1st day (0.65 mg/g-day for Cr6+, 0.83 mg/g-day for Ni2+, 0.72 mg/g-day for Zn2+, and 4.22 mg/g-day for PO43−) (see Figure 2(b)), decreases steadily on the 2nd and 3rd day while a drastic reduction is observed from the 5th day onwards.

Isotherm analysis

Langmuir isotherm model defines the monolayer adsorption feasibility and the Freundlich isotherm model defines surface heterogeneity. Since no significant data were found for TN, no further discussions will be made.

For constant HRT and variable algal dose

In the Langmuir isotherm, the RL obtained from the plot shows that favourable adsorption occurs for all four contaminants with good fit according to RMSE values (see Table 2) and great R2 values (see Figure 3).
Table 2

Speculations from the Langmuir isotherm parameter

PollutantRLCommentRMSEComment
Cr6+ 0.1263 0 < RL < 1; favourable adsorption 0.139 Good fit 
Ni2+ 0.0552 0 < RL < 1; favourable adsorption 0.167 Good fit 
Zn2+ 0.3789 0 < RL < 1; favourable adsorption 0.0967 Good fit 
PO43− 0.999 0 < RL < 1; favourable adsorption 0.0166 Good fit 
PollutantRLCommentRMSEComment
Cr6+ 0.1263 0 < RL < 1; favourable adsorption 0.139 Good fit 
Ni2+ 0.0552 0 < RL < 1; favourable adsorption 0.167 Good fit 
Zn2+ 0.3789 0 < RL < 1; favourable adsorption 0.0967 Good fit 
PO43− 0.999 0 < RL < 1; favourable adsorption 0.0166 Good fit 
Figure 3

Adsorption isotherms of Cr6+, Ni2+, Zn2+, and PO43− with variable algal dose (mg/L) fitted to Langmuir isotherm at 5% error.

Figure 3

Adsorption isotherms of Cr6+, Ni2+, Zn2+, and PO43− with variable algal dose (mg/L) fitted to Langmuir isotherm at 5% error.

Close modal
In the Freundlich isotherm, the n parameter indicates normal adsorptions for Cr6+ and Ni2+ and cooperative adsorption for Zn2+ and PO43− contaminants. Additionally, the RMSE suggests a good fit (see Table 3) and the R2 values suggest a good fit for all (see Figure 4).
Table 3

Speculations from the Freundlich isotherm parameter

Pollutantn−1CommentRMSEComment
Cr6+ 0.6625 n−1 < 1; normal adsorption 0.1688 Good fit 
Ni2+ 0.4453 n−1 < 1; normal adsorption 0.1758 Good fit 
Zn2+ 1.1317 n−1 > 1; cooperative adsorption 0.2128 Good fit 
PO43− 1.164 n−1 > 1; cooperative adsorption 0.1184 Good fit 
Pollutantn−1CommentRMSEComment
Cr6+ 0.6625 n−1 < 1; normal adsorption 0.1688 Good fit 
Ni2+ 0.4453 n−1 < 1; normal adsorption 0.1758 Good fit 
Zn2+ 1.1317 n−1 > 1; cooperative adsorption 0.2128 Good fit 
PO43− 1.164 n−1 > 1; cooperative adsorption 0.1184 Good fit 
Figure 4

Adsorption isotherms of Cr6+, Ni2+, Zn2+, and PO43− with variable algal dose (mg/L) fitted to Freundlich isotherm at 5% error.

Figure 4

Adsorption isotherms of Cr6+, Ni2+, Zn2+, and PO43− with variable algal dose (mg/L) fitted to Freundlich isotherm at 5% error.

Close modal

For constant algal dose and variable HRT

In the Langmuir isotherm, the RL obtained from the plot shows that irreversible adsorption occurs for all four contaminants with good fit according to RMSE values (see Table 4). The R2 shows a satisfactory fit, with Ni2+ showing the highest value of 0.84 (see Figure 5).
Table 4

Speculations from the Langmuir isotherm parameter

PollutantRLCommentRMSEComment
Cr6+ −0.01 RL < 0; irreversible adsorption 0.1126 Good fit 
Ni2+ −0.003 RL < 0; irreversible adsorption 0.0285 Good fit 
Zn2+ −0.006 RL < 0; irreversible adsorption 0.079 Good fit 
PO43− −4.985 RL < 0; irreversible adsorption 0.0136 Good fit 
PollutantRLCommentRMSEComment
Cr6+ −0.01 RL < 0; irreversible adsorption 0.1126 Good fit 
Ni2+ −0.003 RL < 0; irreversible adsorption 0.0285 Good fit 
Zn2+ −0.006 RL < 0; irreversible adsorption 0.079 Good fit 
PO43− −4.985 RL < 0; irreversible adsorption 0.0136 Good fit 
Figure 5

Adsorption isotherms of Cr6+, Ni2+, Zn2+, and PO43− with variable HRT (days) fitted to Langmuir isotherm at 5% error.

Figure 5

Adsorption isotherms of Cr6+, Ni2+, Zn2+, and PO43− with variable HRT (days) fitted to Langmuir isotherm at 5% error.

Close modal
In the Freundlich isotherm, the n parameter indicates normal adsorptions for all four contaminants. Additionally, the RMSE suggests a good fit as well (see Table 5). The R2 values suggest a satisfactory fit with PO43− demonstrating the highest value (see Figure 6).
Table 5

Speculations from the Freundlich isotherm parameter

Pollutantn−1CommentRMSEComment
Cr6+ −0.159 n−1 < 1; normal adsorption 0.0213 Good fit 
Ni2+ −0.067 n−1 < 1; normal adsorption 0.0066 Good fit 
Zn2+ −0.115 n−1 < 1; normal adsorption 0.0146 Good fit 
PO43− −0.501 n−1 < 1; normal adsorption 0.0163 Good fit 
Pollutantn−1CommentRMSEComment
Cr6+ −0.159 n−1 < 1; normal adsorption 0.0213 Good fit 
Ni2+ −0.067 n−1 < 1; normal adsorption 0.0066 Good fit 
Zn2+ −0.115 n−1 < 1; normal adsorption 0.0146 Good fit 
PO43− −0.501 n−1 < 1; normal adsorption 0.0163 Good fit 
Figure 6

Adsorption isotherms of Cr6+, Ni2+, Zn2+, and PO43− with variable HRT (days) fitted to Freundlich isotherm at 5% error.

Figure 6

Adsorption isotherms of Cr6+, Ni2+, Zn2+, and PO43− with variable HRT (days) fitted to Freundlich isotherm at 5% error.

Close modal

The novelty of this study is the initiatory use of Microcoleus sp. in the treatment of heavy metals and nutrients in wastewater. This specific species of blue-green microalgae can tolerate extreme temperature conditions and salinity. They can be found in arctic areas, deserts, and saline water bodies; therefore, using this species in those regions may bring revolutionary advancements. Microcoleus sp. has shown a promising removal efficiency of Cr6+, Ni2+, Zn2+, and PO43−. It could not remove the nitrogen content in the wastewater since the experiments were conducted with continuous lighting and they cannot perform nitrogen fixation during the day. Future studies may be carried out to validate the findings of this study.

All relevant data are included in the paper or its Supplementary Information.

The authors declare there is no conflict.

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