- Open Access
Pre-concentration of microalga Euglena gracilis by alkalescent pH treatment and flocculation mechanism of Ca3(PO4)2, Mg3(PO4)2, and derivatives
Biotechnology for Biofuels volume 13, Article number: 98 (2020)
Microalgae are widely be used in carbon sequestration, food supplements, natural pigments, polyunsaturated fatty acids, biofuel applications, and wastewater treatment. However, the difficulties incurred in algae cell separation and harvesting, and the exorbitant cost required to overcome these challenges, are the primary limitations to large-scale industrial application of microalgae technology.
Herein, we explore the potential of inducing flocculation by adjusting the pH for pre-concentrating Euglena gracilis. Our results demonstrate that flocculation can be induced by increasing the medium pH to 8.5; however, most of the algae cells were broken by increasing the pH > 10. Magnesium phosphate, calcium phosphate, and their derivatives precipitation jointly led to flocculation, although calcium phosphate and its derivatives precipitation had a greater effect.
This study demonstrates that pH treatment-induced flocculation is efficient and feasible for the pre-concentration of E. gracilis under a pilot-scale culture system. Moreover, it also maintained the microalgae cells’ integrity, chlorophyll production, and increased paramylon production. These findings provide a theoretical basis for reducing the cost of large-scale E. gracilis harvesting; as well as provide a reference for harvesting other microalgae.
1.It is efficient to pre-concentrate microalga E. gracilis by alkalescent pH 8.5 treatment.
2.Magnesium phosphate, calcium phosphate and their derivatives precipitation jointly led to flocculation, although calcium phosphate and its derivatives precipitation had a greater effect.
3.This flocculation method maintains the E. gracilis cell integrity, chlorophyll production , and improves the paramylon production.
Microalgae exhibit a high biomass production and growth rate and do not compete with crops, as algae can grow on non-arable land . Microalgae biomass may be used in carbon sequestration, food supplements, natural pigments, polyunsaturated fatty acids, biofuel applications, and wastewater treatment [2,3,4,5,6]. Nevertheless, microalgae biomass is generally harvested at < 0.1% solids with cell sizes usually between 3 and 30 μm under large-scale photoautotrophic conditions . To realize the industrial utilization of algal biomass materials, the optimal solids should be > 50%. Therefore, the algal solution under conventional culture needs to be more concentrated and converted into algal mud before being applied in the industry. This separation and concentration process is the main energy consumption expense in microalgae biomass production and generally accounts for 20–60% of the total cost . Thus, the difficulties incurred in algal cell separation and harvesting, and the exorbitant cost required to overcome these challenges, are primary limitations to large-scale industrial application of microalgae technology.
The unicellular flagellated alga, Euglena gracilis, which is characterized by the absence of a cell wall, produces a wide variety of bioactive compounds (e.g., paramylon, carotenoids, tocopherol, euglenophycin, and lipids) with tremendous potential for metabolic engineering and commercialization . However, this kind of economic microalgae was pre-concentrated by ultrafiltration membrane filtration , which readily results in membrane pollution and subsequently requires a high quantity of water to clean the membrane . At the same time, according to our previous research, when the transmembrane pressure was slightly higher (0.2 MPa), the E. gracilis cells easily ruptured, leading to a low recovery efficiency and poor cost improvement. Therefore, a more economical and efficient method of pre-concentrating E. gracilis cells is urgently needed.
Generally, microalgae cells are concentrated by centrifugation . However, due to the high energy consumption requirement, centrifugation cannot be directly used in large-scale engineering. Therefore, algae cells need to be pre-concentrated. Algae cells can be pre-concentrated through various methods, including the electrolytic method , foam fractionation , gravity sedimentation , ultrafiltration membrane filtration , and flocculation . In particular, flocculation is a promising approach to reducing the cost of microalgae harvesting, as it is an effective, yet simple technique. Flocculation enables the rapid separation of microalgae from the medium using simple gravity-based sedimentation . Although the algae cells do not meet industrial application requirements directly after flocculation–sedimentation, the inclusion of this technique can significantly reduce the energy consumption and cost of subsequent concentration processing. Therefore, flocculation is regarded as the best way to achieve large-scale separation and pre-concentration of microalgae . Moreover, adjusting the medium’s pH to > 8 leads to algae cell flocculation without the need for additional flocculant. However, the mechanism that drives this process is not yet clearly understood. A small group of researchers supports the notion that when the medium is weak alkaline (pH 8–10), a large number of positively charged calcium phosphate precipitates are formed, which can neutralize the negatively charged algae cells [7, 18]; however, Branyikova et al.  found that flocculation of negatively charged Chlorella vulgaris was induced not only by positively charged but also by negatively charged calcium phosphate precipitates at an early phase of nucleation. The driving force for interactions between oppositely charged cells and precipitate particles was electrostatic attraction, while the attraction between equally charged entities may have resulted from a negative total balance of apolar (Lifsitz–van der Waals) and polar (acid–base) interactions. By contrast, most researchers support the view that when the medium pH is > 10.5, it can produce positive magnesium hydroxide precipitation, neutralize the algae cells with a negative charge, and then form flocculation [1, 16, 20,21,22]. In this case, magnesium hydroxide, as opposed to calcium phosphate, is the key precipitate that induces algae cell flocculation. Moreover, Formosa-Dague et al.  suggested that the magnesium-hydroxide flocculation mechanism of Phaeodactylum tricornutum is a two-partner system, both the changes are undertaken by the cell wall and the interactions with hydroxide particles are needed to successfully flocculation. Due to this unresolved controversy, the flocculation mechanism of no-cell wall algae, E. gracilis, is required elucidation.
Nevertheless, the activity and subsequent utilization of algae cells are often adversely affected by a high pH. For example, the high-yield lipid algae species Skeletoma costatum reached 80% flocculation efficiency at pH 10 after 2 h, but a considerable part of the cells in the recovered algae body disintegrated and the intracellular components leaked out, which drastically affected the subsequent eicosapentaenoic acid (EPA) extraction process . When the pH of Spirulina platensis suspensions was > 13, the cells flocculated quickly and thoroughly, but the cells’ pigment turned yellow, indicating that the “pH” seriously damaged the cells . Also, high pH value is likely to exceed the effluent discharge standard; thus the pH must be adjusted to within the allowable range. Therefore, the optimal harvesting technique should be independent of the cultured species, consume little energy and chemicals, and harmless to the valuable products obtained during the extraction process .
In this study, we attempted to (1) determine the optimal flocculation pH value by adjusting the suspension pH with sodium hydroxide solution (NaOH) and hydrochloric acid (HCl) to induce flocculation of E. gracilis cells; (2) investigate potential flocculation mechanisms; and (3) verify and evaluate the method of pre-concentration of E. gracilis and cells’ biochemical components under a pilot-scale culture, respectively.
Results and discussion
The growth curve of E. gracilis and pH changes in culture conditions
Under photoautotrophic conditions, generally, the pH gradually increases as algae cells grow; thus, pH levels are > 7 throughout the culture process. As such, CO2 is often used to control the pH within an appropriate range to prevent a decrease in photosynthetic efficiency [27, 28]. However, the varying pH culture conditions of E. gracilis differ from many microalgae. For example, the strain’s maximum biomass is 2.3 by OD750 under photoautotrophic conditions, yet the medium’s pH gradually decreased from the original 3.6, reaching 1.9 in the platform period by day 6 (Fig. 1). This result suggests that E. gracilis is always growing in an acidic environment.
Microalgae flocculation in the absence of flocculant is generally referred to as “auto-flocculation”. Essentially, the algae cells’ high photosynthetic efficiency facilitates large quantities of CO2 absorption, which increases the algae suspensions’ pH. When the medium’s pH is raised to a certain threshold without CO2, positively charged precipitates (mainly calcium phosphate) are formed from specific metal ions in the algae suspensions, which can neutralize the algae cells’ negatively charged surface, and enable flocculation . In contrast to “auto-flocculation”, flocculation can also be artificially induced by adding alkaline substances to improve the algae suspensions’ pH. Based on the above results, the medium with E. gracilis cells is acidic. According to Ozkan  and Liu et al. , the algae cells’ surface is generally positively charged when algae cells are in acidic conditions. Therefore, E. gracilis harvesting is unable to be performed with auto-flocculation. As such, the medium’s pH must be artificially increased, by adding alkaline substances, to convert the algae cell surfaces from positive to negative charges.
The pH of the E. gracilis cells’ culture medium was adjusted by adding NaOH and HCl solution. An extended time analysis showed that algae cells achieved a greater flocculation efficiency (FE) (> 80%) at pH 8, 9, and 10 (Fig. 2a, Additional file 1: Fig. S1). What’s more, based on the algae cells’ FE at pH 8, 8.5, and 9, the critical pH value (CPV) was determined as 8.5 (p < 0.05) (Fig. 2b). These results are similar to those specific results given by Beuckels et al.  about harvesting the freshwater microalgae C. vulgaris; although, it has been suggested that the pH adjustment treatment is more efficient for harvesting E. gracilis cells.
However, when the pH value was > 8.5, the FE gradually decreased (Fig. 2a). Unexpectedly, microscopic observation of the E. gracilis cells’ morphology showed significant algal cell morphological changes, based on the medium’s pH level. For example, at pH 3.5, the cells were slender, and the chloroplasts were flat (Fig. 3a); whereas, at pH 8.5, the chloroplasts were spherical (Fig. 3b). At pH > 10, the algal cells were completely ruptured and the cells’ components were suspended in the liquid (Fig. 3c, Additional file 1: Fig. S1). This phenomenon rarely occurs in other green algae, such as C. vulgaris and Scenedesmus obliquus [7, 16, 20]. A potential explanation for the cell rupture may be related to the fact that the E. gracilis cells have no cell wall. Due to the absence of cell wall support, when the osmotic pressure became too intense, the cell ruptured, obviously indicating that E. gracilis cells are unable to flocculate at higher pHs.
To investigate the effect of the CPV on E. gracilis cell biomass, the cells’ FE was measured at 0.8, 1.3, 1.8, 2.3, and 2.8 g/L. The results showed that the FEs of all the different cell densities reached > 90% after 1 h, with no significant difference between them (p > 0.05) (Fig. 4). As such, the CPV has no distinctive impact on cell growth of varying biomass densities; possibly because key ions in the culture medium are always redundant, although some of them are absorbed by algae cells during the culturing process.
Mechanism of the flocculation
When the algal suspension’s pH was adjusted to 7, precipitate generation gradually began. Thus, at pH 10, after 1 h, there was a sizeable amount of deposited precipitate at the bottom of the centrifuge tube containing the suspension (Additional file 1: Fig. S1). Simultaneously, we found that Mg2+ and Ca2+ exhibited the highest and second-highest metal ion concentration in the PEM medium (Additional file 1: Table S1). Therefore, this study focused on the role of these two metal ions. To reduce interference in the precipitate analysis from the algal cells’ pigment, the experiments were performed in a fresh medium as opposed to previously prepared algal suspensions. After the fresh culture medium’s pH had been adjusted to 8.5 for 1 h, a large number of white precipitates were deposited at the bottom of the centrifuge tube (Fig. 5a). Interestingly, while precipitates were produced when Ca2+ was absent from the culture medium (Fig. 5b), only a small number of precipitates were deposited when Mg2+ was absent (Fig. 5c). When both Ca2+ and Mg2+ were absent, no precipitate formed in the culture medium (Fig. 5d). Meanwhile, the turbidity of the solutions from the central of centrifuge tubes was 3.2,2.6,1.7, and 0.2 FUT under PEM, PEM-Mg2+, PEM-Ca2+, and PEM-Mg2+, -Ca2+ conditions, respectively (Fig. 5e). These results demonstrated that precipitate formation was primarily controlled by the presence or absence of Ca2+ and Mg2+.
To unequivocally demonstrate the role these bivalent cations play in the flocculation process, all-metal ions in the PEM medium were chelated with a saturated concentration of EDTA. The results showed that the pH 8.5 algae solution supplemented with EDTA depicted no significant difference in the FE compared to the control group (p > 0.05). However, the same algae solution with no EDTA depicted an FE increase ranging from 42.2 to 93.3% (p < 0.01) (Fig. 6). Thus, it confirmed that the metal ions such as Ca2+ and/or Mg2+ were the main cause of flocculation; the results were similar to the previous study except for those algae solutions at > pH 10.5 by Vandamme et al. .
After the algae cells underwent flocculation–sedimentation, the Ca2+ and Mg2+ concentration in the culture medium decreased from 0.19 mM to 0.14 mM, and 3.2 mM to 2.1 mM, respectively, thereby depicting a significant (p < 0.01) decrease of 26.3% and 34.4%, respectively (Fig. 7). Meanwhile, we predicted and analyzed the compounds synthesized by these two metal ions at pH 8.5 through Visual MINTEQ software, and found that there were as many as 7 compounds, that were included of 3 variants of Ca3(PO4)2 (β-Ca3(PO4)2, am1-Ca3(PO4)2, am2-Ca3(PO4)2) and 4 derivatives (Ca10(PO4)6(OH)2, Ca4H(PO4)3·3H2O, CaHPO4, CaHPO4·2H2O) related to calcium ion synthesis with SI (Saturation index) > 1, and only both Mg3(PO4)2 and MgHPO4·3H2O, that were included of related to magnesium ion synthesis (Table 1). It showed that these two metal ions may be more inclined to form a precipitate with phosphate at such a pH value. Thus, these two metal ions may simultaneously play a role in algae cell flocculation. This result conflicts with that of Sukenik et al. [18, 31], who reported that when the pH was adjusted to 8.9, the Ca2+ concentration decreased, while that of Mg2+ remained unchanged. In this study, we found that magnesium ion can also form precipitates at the CPV under an alkalescent pH.
To more specifically determine which of the two divalent metal cations plays a more significant role, different concentrations of Ca2+ and Mg2+ were added to the algal cell suspensions. The results showed that when the Mg2+ and Ca2+ concentration was doubled (5 mM Mg2+, 0.2 mM Ca2+), the FE was 59.1% and 54.8%, respectively, meaning that neither ion by itself could induce algae cell flocculation. Interestingly, regardless of how much Mg2+ was added, the FE remained at 56–59% (p > 0.05); however, the FE gradually increased in response to an increasing Ca2+ concentration. In fact, the FE reached 100% (p < 0.01) after the Ca2+ concentration was increased fourfold (20 mM Mg2+, 0.8 mM Ca2+) (Fig. 8). Besides, the dissolved Ca2+ and Mg2+ in the fresh medium were analyzed by ICP-OES. Results showed that the dissolved Mg2+ concentration gradually increased with the addition of Mg2+ (Fig. 9a). In contrast, the concentration of dissolved Ca2+ remained between 0.1 and 0.2 mM (p < 0.05) (Fig. 9b) regardless of how much calcium ion was added. The combined results depicted in Figs. 8 and 9 confirm that Ca2+ and Mg2+ play comparable key roles in the flocculation of algae cells at the CPV.
Next, we set out to determine what anions combined with the Ca2+ and Mg2+ to form sediment, and ultimately induce algae cell flocculation. Based on the published literature, calcium phosphate precipitates easily form [7, 18] when there is a high PO43− concentration and the medium’s pH is weak alkaline. In our study, we found that when a fourfold (0.8 mM) concentration of Ca2+ was added to the medium without onefold (4.4 mM) PO43−, the FE was only 42.24%, and there was no significant difference (p > 0.05) compared with the control group (35.35%). Contrarily, when PO43− was present, the FE reached 100%. Notably, we also found that when a fourfold (20.0 mM) concentration of Mg2+ was added to the medium without PO43−, the FE was 43.12%; and when PO43− was added, the FE only increased to 62.98% far lower than the effect observed with Ca2+ (Fig. 10). Through Visual MINTEQ software prediction and analysis, the logarithmic Solubility Product Constants (lg Ksp) of the solubility products of the three calcium phosphate derivatives β-Ca3(PO4)2, am1-Ca3(PO4)2, and am2-Ca3(PO4)2 were − 28.92, − 25.2, and − 28.25, respectively, which are lower than − 23.28 of magnesium phosphate. The lg Ksp of the derivatives are − 44.33, − 47.95, − 19.28, and − 19.00, which are also lower than − 18.18 of the magnesium phosphate derivative MgHPO4·3H2O, and the SI of all compounds were > 1 (Table 1), meaning calcium phosphate and their derivatives were easier to form than magnesium phosphate and their derivatives. These results verify that the flocculation was caused by calcium phosphate, magnesium phosphate and both their derivatives’ precipitate formation, in which the calcium phosphate and derivatives’ effect plays a larger role.
Although the extended DLVO (XDLVO) theory is traditionally used to describe colloidal stability in colloidal chemistry, it also suitably describes the aggregation process of algae cells in microalgae suspension [29, 32, 33]. According to this theory, the interaction forces within algae cell suspensions include the Lifshitz–van der Waals interaction (LDWI), electrostatic interaction (EI), and lewis acid–base interaction (LABI). In general, LDWI is an attraction force. In pH > 7 microalgae culture systems, negative charges develop on the algae cells’ surface, so the EI behaves as a repulsion force . Most algae cells are hydrophilic and thus have a tendency to disperse in aqueous solution. As such, the LABI behaves as a repulsion force [29, 33]. In essence, algae suspensions are stabilized through a combination of all three forces. Therefore, the basic principle of microalgae flocculation is to reduce or eliminate the repulsive EI and LABI forces, so that algae cells can aggregate and form flocculation.
Therefore, to induce algae cell flocculation by adjusting the medium pH, the main ions’ types in the medium and the resulting precipitates must be identified. Auto-flocculation induction only occurs if there is enough PO43− and Ca2+ in the medium from the start. When the algae solution pH is weakly alkaline (8–10), positively charged sediment can be formed to neutralize the negative charge on the algae cells’ surface, which enables algae cell flocculation . However, most studies report that microalgae culture mediums generally contain an overabundance of PO 34 and Mg2+, as opposed to PO43− and Ca2+ [1, 16, 20,21,22], which prevents it from flocculating under weak alkalinity. Large quantities of positively charged magnesium hydroxide only form when the algae solution’s pH value is very high (> 10.5). Once precipitated, they can neutralize the negative charge on the algae cells’ surface; and then physical methods, such as net catching and sweeping, can be used to accelerate the gravity precipitation and harvest the algae cells.
As previously discussed, the algae cell flocculation mechanism differs depending on the ion and pH value present in the suspension. E. gracilis cells’ PEM medium contained a high concentration of PO43− and Mg2+, and a small concentration of Ca2+. The CPV in the algae suspension was determined to be 8.5, which is considered weak alkaline; thus flocculation and sedimentation can occur.
In this work, we found that Mg2+ formed magnesium phosphate precipitates and induced a flocculation effect at a weakly alkali pH of 8.5, without raising the pH high enough to form magnesium hydroxide precipitate. However, magnesium phosphate’s flocculation effect is limited at such CPV. Regardless of the magnesium ion concentration, the flocculation efficiency essentially remains the same; perhaps because the magnesium ion can promote movement of E. gracilis cells  and subsequently reduce the FE.
Although most of the precipitates were magnesium phosphate and its derivatives, except for a small amount of calcium phosphate and its derivatives, the occurrence of algae cell flocculation is influenced by both metal ions’ precipitate, as opposed to only calcium phosphate precipitates as previously reported [7, 18]. Thus, the calcium phosphate sediment still plays a key role, as it can neutralize the negative charge, and maybe net catch and sweep cells by a lot of derivatives, and also inhibit E. gracilis cell movement . Therefore, this mechanism provides a theoretical basis for harvesting other algae, and for optimization of microalgae culture mediums conducive to flocculation.
Pilot-scale culture performance and chemical compounds
To verify the feasibility of harvesting Euglena gracilis cells by adjusting the CPV in a pilot-scale culture, we used an E. gracilis pre-concentration from the 60 L column photobioreactors. The FE reached 82.4%, 2.5-fold that of the control group (32.9%) (p < 0.01) by 2 h (Fig. 11a), clearly demonstrating the positive effect of pre-concentrating E. gracilis cells. Thus, it has been suggested that this is a feasible method for harvesting E. gracilis cells in a pilot-scale culture. Flocculation of other microalgae requires a high pH (> 10) to achieve a good FE [1, 16, 20,21,22]. However, in this study, only a small amount of sodium hydroxide was necessary to adjust the pH to 8.5, and the resulting flocculation achieved good results. The pre-concentrated algae suspensions were successfully concentrated by centrifugation after adding a small amount of acid to restore the acidic medium. Thus, pre-concentrating greatly reduces the energy and monetary cost. Yet, the mechanism studied in the laboratory-scale culture cannot always reach the desired FE in the pilot-scale cultures. For example, in the laboratory-scale level experiments, the FE reached > 90% within a short time; whereas, the FE was only 82.4% in the pilot-scale culture that was conducted for 2 h. There are numerous additional influencing factors, such as the dissolved organic matter (DOM) secreted by algae cells, which can significantly inhibit flocculation. These DOM may take the form of humic acid produced by cell rupture, an organic acid produced by algae metabolism, or organic acid secreted by bacteria, etc. [16, 35,36,37,38]. Naturally, different algae species cultured under varied conditions may have different primary inhibitors to flocculation. Thus, it is important to determine which abiotic factors can reduce the FE of E. gracilis cells, as it will provide a theoretical basis for harvesting E. gracilis cells on a larger scale in the future.
Generally, the algae cells’ biochemical substances (such as pigment) were destroyed by a high pH , but whether those biochemical substances are also destroyed by a weak alkaline pH remains unknown. The fact that there was no significant change in chlorophyll production when compared with the control group after 2 and 12 h of flocculation (p > 0.05) (Fig. 11b) indicates that the CPV had no effect on chlorophyll production, yet it produced a good harvesting effect compared with results in the literature . What’s more, the paramylon production was significantly higher than that of the control group. The highest production was 0.6 g/L after 12 h (p < 0.05), which is 2.4-fold that of the control group (Fig. 11c). The results are similar to those specified given by Masahiro et al. . These results verify that paramylon synthesis is induced by pH treatment. In summary, this method not only enables feasible harvesting of E. gracilis cells, but also scarcely affects the chlorophyll production, and thereby increases the paramylon production from pH treatments. These benefits will provide solid theoretical guidance for the production of active substances from industrial-size cultures of E. gracilis and other microalgae.
Our study demonstrates that pre-concentrating microalga E. gracilis via alkalescent pH 8.5 treatment is both productive and cost-efficient. Essentially, E. gracilis cells’ flocculation is influenced by a combination of calcium phosphate, magnesium phosphate, and their derivatives. Calcium phosphate and its derivatives’ precipitate play a key role in the flocculation process, although very little concentration is needed, as it has the greatest impact on flocculation efficiency. This flocculation method has the potential to optimize flocculation conditions in the future, as it was validated in a pilot-scale culture system. Finally, this method maintains the algae cell integrity, chlorophyll production, and improves paramylon production. These findings will both reduce the cost of industrially harvesting E. gracilis cells, and provide a theoretical basis for harvesting other microalgae.
Materials and methods
Strain and growth conditions
Euglena gracilis CCAP 1224/5Z was purchased from the Culture Collection of Algae and Protozoa (CCAP) and maintained in our lab at Shenzhen University . This strain was cultured in a modified photoautotrophic euglena medium (PEM), according to Cramer and Myers . The PEM medium contained 1.8 g/L NH4Cl, 0.6 g/L KH2PO4, 1.2 g/L MgSO4·7H2O, 0.02 g/L CaCl2·2H2O, 0.55 μg/L Na2EDTA·2H2O, 2 μg/L Fe2(SO4)3, 0.05 μg/L CuSO4·5H2O, 0.4 μg/L ZnSO4·7H2O, 1.3 μg/L Co(NH3)·H2O, 1.8 μg/L MnCl2·4H2O, 0.01 μg/L Vitamin B1, and 0.0005 μg/L Vitamin B12. Additional file 1: Table S1 shows the concentration of the main ions (> 1 mg/L) in the PEM medium. The pH value of the PEM medium was 3.6 adjusted with 3 M sodium hydroxide (NaOH) and 1 M hydrochloric acid (HCl). The microalgae cells were grown in 2-L glass column photobioreactors with a 10 cm internal column diameter. The photobioreactors contained 1.5 L PEM medium that was stirred with 0.2 μm-filtered mixed gas (2% CO2, v/v, the gas flow rate was 6 L/min) and illuminated with an LED lamp at a light intensity of 150 μmol photons m−2 s−1. The temperature of the cultivation remained 25 °C.
The growth curve of E. gracilis and pH changes in culture conditions
To determine the flocculation method of pre-concentrated E. gracilis cells, each day, we measured the cells’ growth curve and pH changes in the PEM medium under the above culture conditions until the cells reached the plateau phase. The microalgae’s growth curve was monitored by measuring the absorbance at 750 nm (OD750) using a UV–Vis spectrometer (UV2350, UNICO, China) and the culture medium’s pH value was monitored with a pH meter (pH 30, Clean-Leau Instruments, China).
As the pH of the medium increases and the flocculation efficiency (FE) of cells’ suspension reaches its maximum at a certain point in time (25 °C), the value of pH is a critical point, which is called CPV. To determine the CPV required for achieving a high FE (FE > 90%), 0.8 g/L biomass dry weight (DW) of microalgal suspensions was prepared in 45-mL centrifuge tubes. 3 M NaOH and 1 M HCl were used to adjust the pH value. The DW of microalgal cells was measured according to Lee et al. . Experiments were conducted to determine the FE at pH values 3, 4, 5, 6, 7, 8, 9, 10, 11, and 12; at different time intervals of 10, 20, 30, 40, 50, and 60 min.
The FE of each suspension was calculated according to the following equation:
OD750, the optical density by absorbance at 750 nm; where “ODb” is the OD750 of the cells’ suspension before pH adjustment and “ODa” is the OD750 after the complete treatment; all of “ODb” and “ODa” were measured from the center of the centrifuge tubes.
After verifying that the algae biomass FE was optimized at a basic pH, further study was conducted via precipitate and morphological cell analysis. A microscope (Leica DMi1, Leica Microsystems, Germany) was used to observe the morphological changes in cells from the different pH level experiments. Similarly, the FE of different algae biomass concentrations (Dry weight = 0.8, 1.3, 1.8, 2.3, and 2.8 g/L) was determined at 20, 40, and 60 min.
Determination of the flocculation mechanism
Precipitates on the bottom of the centrifuge tubes and the turbidity of the solutions from the central of centrifuge tubes were observed and measured using a laboratory hazemeter (NDH2000, Shenzhen University, China) under the PEM-Mg2+ (without MgSO4·7H2O), PEM-Ca2+ (without CaCl2·2H2O), and PEM-Mg2+-Ca2+ (without MgSO4·7H2O, CaCl2·2H2O) after 1 h, respectively, to determine whether precipitates formed in the absence of Mg2+ or Ca2+, both Mg2+ and Ca2+, respectively, from the culture medium.
Next, to unequivocally demonstrate the role of divalent cations in the flocculation process, we assessed whether flocculation induced by the CPV could be inhibited by adding 30 mM EDTA, a chelating agent that can sequester polyvalent cations. This experiment was performed using four test groups: a control group A at the CPV without EDTA,a control group B with added EDTA; a solution at the CPV with added EDTA; and a solution at the CPV without added EDTA. After the algae cells under CPV conditions were removed by centrifugation and filtered using Whatman GF/C glass microfiber filters, the dissolved Ca2+ and Mg2+ concentrations from the center of the centrifuge tubes were analyzed. Meanwhile, the Saturation Indices (SI) and the logarithmic Solubility Product Constant (lgKsp) of compounds related to Ca2+ and Mg2+ in the PEM medium by pH 8.5, 25 °C treatment were predicted and analyzed with Visual MINTEQ, ver. 3.0 software.
To further investigate the relative importance of Ca2+ and Mg2+ in the CPV flocculation process, we tested whether flocculation at the CPV could be induced in a medium lacking Ca2+ or Mg2+. To do so, algae cells were separated from the medium using centrifugation and resuspended in a fresh medium without Ca2+ and Mg2+. In the first series, algae cells were resuspended in a medium without Mg2+ and containing varying Ca2+ concentrations of 0—(0 mM), 1—(0.2 mM), 2—(0.4 mM), and 4—(0.8 mM) fold that of the control group. In a second series, Ca2+ was omitted and Mg2+ was added in concentrations of 0—(0 mM), 1—(5.0 mM), 2—(10.0 mM), and 4—(20.0 mM) fold that of the control group. The FE of dissolved Ca2+ and Mg2+ concentrations of all the above groups were analyzed. Finally, the FE was determined under the PEM-PO43− [without KH2PO4, adding fourfold (0.8 mM) Ca2+ and (20.0 mM) Mg2+, respectively], PEM + PO43− (with 4.4 mM KH2PO4, adding fourfold Ca2+and Mg2+, respectively) and the control (without MgSO4·7H2O, CaCl2·2H2O) at the CPV. Dissolved Ca2+ and Mg2+ ion quantification was performed using inductively coupled plasma optical emission spectroscopy (ICP-OES) (Optima 7000 DV, PerkinElmer, USA). The specific steps were performed according to Trevelin et al. .
Preliminary application of pilot-scale culture
The pilot-scale (60-L column photobioreactors) culture FE was determined by alkalescent pH 8.5 treatment at 0.5, 1, 1.5, 2, and 12 h. Next, the algae biomass DW was analyzed before and after flocculation, while chlorophyll production and paramylon production were analyzed at 2 and 12 h.
Chlorophyll production determination was conducted as described by Price , using the following modification. 1 mL cell suspension was mixed with 4 mL of acetone in centrifuge tubes that were cooled in ice water. After 1 h in the dark, the samples were remixed and centrifuged. The extinction of the clear suspension solution was determined with a UV–Vis spectrometer at 663 nm (the residue from a single extraction was colorless and further extractions did not increase the yield). The concentration and amounts of chlorophyll were then calculated from the extinction coefficient for chlorophyll, as reported by MacKinney .
Paramylon production quantification was described by Takenaka et al.  using the following modification. To improve the quantification accuracy, 30 mM of EDTA chelating agent was added to the cells’ suspension, in both the experimental group and the control group, to prevent the precipitation from affecting the paramylon content. After the cells’ suspensions were centrifuged and freeze–dried, ~ 5–10 mg of freeze–dried algae powder and 5 mL of acetone solution were transferred to a 15-mL centrifuge tube, and shaken for 10 s, then placed in a shaker for 2 h. After the tube was centrifuged at 2000g for 5 min, the supernatant was removed. 1.5 mL of 1% SDS solution was added to the tube, after which the contents were transferred into a 1.5-mL centrifuge tube and heated in a water bath at 85 °C for 2 h. Again, the supernatant was removed after the centrifuge tube was centrifuged at 2000g for 5 min. The precipitate was washed and centrifuged in 1 mL deionized water, then oven-dried at 70 °C to a constant weight. The obtained precipitate was paramylon. The paramylon production (g/L) was calculated as shown in Eq. (2):
where “PM” and “AP” are the dry weight of the paramylon and algae powder, respectively.
Each growth curve, pH value, flocculation efficiency test, ion concentration, paramylon production, and chlorophyll content test were performed in triplicate and the average was reported. All data were statistically analyzed by Student’s t test analysis to investigate the difference compared to the control group. p values less than 0.01 (p < 0.01) were considered significantly different, p < 0.05 statistically different, and p values more than 0.05 (p > 0.05) not significant. Standard errors were included in all the graphs.
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Sodium hydroxide solution
The critical point of pH value
- PEM medium:
Photoautotrophic euglena medium
Inductively coupled plasma optical emission spectroscopy
The Lifshitz–van der Waals interaction
Lewis acid–base interaction
The dissolved organic matter
Culture Collection of Algae and Protozoa
Cellular dry weight
Ion activity product
- KSP :
Solubility product constant
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We acknowledge TopEdit LLC (www.topeditsci.com) for the linguistic editing and proofreading during the preparation of this manuscript.
This work was supported by the National Natural Science Foundation of China (Grant number 31670116), and the National Natural Science Foundation of China (41876188), Guangxi Innovation Drive Development Special Fund (Gui Ke AA18242047) and Grant Plan for Demonstration Project for Marine Economic Development in Shenzhen to Dr. Zhangli Hu; National Key R&D Program of China (2018YFA0902500), the Guangdong Innovation Research Team Fund (Grant number, 2014ZT05S078), and the Shenzhen Grant Plan for Science & Technology (Grant number, JCYJ20160308095910917, JCYJ20170818100339597).
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Wu, M., Li, J., Qin, H. et al. Pre-concentration of microalga Euglena gracilis by alkalescent pH treatment and flocculation mechanism of Ca3(PO4)2, Mg3(PO4)2, and derivatives. Biotechnol Biofuels 13, 98 (2020). https://doi.org/10.1186/s13068-020-01734-8
- Euglena gracilis
- Magnesium phosphate
- Calcium phosphate