Citation: Weijie Liu, Liu Cong, Hongli Yuan, Jinshui Yang. The mechanism of kaolin clay flocculation by a cation-independent bioflocculant produced by Chryseobacterium daeguense W6[J]. AIMS Environmental Science, 2015, 2(2): 169-179. doi: 10.3934/environsci.2015.2.169
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Flocculants are widely used in various industrial processes, such as wastewater treatment, drinking water purification and downstream fermentation processes [1,2,3]. Chemically synthetic flocculants are predominantly used because of their effectiveness and low cost, but most of them are harmful to human health, such as acrylamide monomer from one of the most popular synthetic flocculants poly-acrylamide that is categorized as both neurotoxin and highly carcinogenic to humans [4,5,6]. Bioflocculants are mainly composed of extracellular polymeric substances, such as glycoprotein, polysaccharide, protein and nucleic acid produced by microorganisms during their growth [7,8,9,10]. Compared with chemically synthetic flocculants, bioflocculants are not toxic, harmless and biodegradable [11,12,13]. However, major bottlenecks for the commercialization of bioflocculants include the higher production cost and uncertain flocculating mechanism. The study on flocculating mechanism could help us to elucidate the role of bioflocculant in process applications and hence improve the overall treatment efficiency [6]. In recent years, many extracellular bioflocculant have been reported, and it has also been reported that certain cations such as Ca2+ can improve their flocculation [3,14,15,16]. Generally, bridging mediated by cations and charge neutralization are the two main mechanisms for these cation-dependent bioflocculants [17,18]. For example, the treatment of kaolin suspension by a bioflocculant secreted by Bacillus mucilaginosus GY03 served as a model for studying flocculating mechanism characterized by bridging mediated by cations and charge neutralization [17]. Bioflocculant HBF-3 produced by Halomonas sp. V3a’ are mainly composed of extracellular polysaccharides. Flocculation of kaolin suspension with bioflocculant HBF-3 served as a model to investigate the flocculating mechanism in which bridging mediated by Ca2+ was proposed [6]. However, the addition of cations can cause the secondary contamination. In recent years, several novel cation-independent bioflocculants have been reported. For instance, Bacillus sp. F19 produces a cation-independent bioflocculant, whose flocculating activity is inhibited by the presence of Fe3+ ions [3]. The bioflocculants produced by Klebsiella pneumoniae and Aspergillus flavus show a good flocculating activity in kaolin clay suspension without cation addition [19,20]. However, the flocculating mechanism of these cation-independent bioflocculants is largely unexplained.
Our previous study discovered a bioflocculant producing strain Chryseobacterium daeguense W6 which produces a cation-independent bioflocculant MBF-W6 and Fe3+ ions inhibit its flocculating activity [21]. Therefore in this study, the MBF-W6 was used as a model to elucidate the flocculating mechanism of cation-independent bioflocculants. Specifically, we found that (i) the major flocculating component of MBF-W6 is a complex mixture of proteins and polysaccharides; (ii) the charge neutralization and bridging mediated by cations are not the underlying flocculating mechanism of MBF-W6, which is consistent with the fact that the flocculant of MBF-W6 is cation-independent; (iii) kaolin clay particles may get attached and bridged by MBF-W6 directly and form a tight packed structure; (iv) Fe3+ ions can inhibit the flocculating activity of MBF-W6 by influencing –COO− and –NH groups of these polymers. Therefore this study can improve our understanding to flocculating mechanism of cation-independent bioflocculants.
Chryseobacterium daeguense W6 was cultured in 500 mL flasks containing 100 mL fermentation medium with 180 rpm agitation at 30 °C. The composition of the fermentation medium were as follows: glucose 1 g/L, Tryptone 2 g/L, Mg(NO3)2 0.2 g/L at pH 6.0. The fermentation broth corresponding to 72 h incubation was used to extract the bioflocculant MBF-W6. The fermentation broth was centrifuged at 8000 rpm at 4 °C for 20 min to remove residual cells, and then the supernatant was collected, dialysed at 4 °C for 24 h in distilled water, and lyophilized to obtain the purified bioflocculant MBF-W6.
The flocculating activity of bioflocculant MBF-W6 at different conditions was monitored by calculating the flocculating activity as previously described with slight modification [21]. Briefly, 4 g/L kaolin clay suspension (pH 7.0) was used as the solid phase to which the storage bioflocculant solution (1 g/L) was added, and stirred for 2 min. After settling for 1 min, the absorbance (OD) of the sample was recorded by using a spectrophotometer (Unic-7200) at 550 nm. A control, without the addition of any agent, was measured in the same manner. The flocculating activity was calculated according to the following equation: flocculating activity = (A0 – A1)/A0 × 100%, where A1 is the absorbance of the supernatant sample at 550 nm and A0 is the absorbance of the control at 550 nm.
Thermal stability of MBF-W6 was analyzed as follows: the purified MBF-W6 was dissolved in water to a concentration of 1 g/L and heated at 100 °C for 0, 10, 20, 30 and 60 min in the boiling water bath. After cooling the MBF-W6 solution to the room temperature (24 °C), different volume of bioflocculant solution was added into kaolin clay suspension, and the flocculating activity was determined.
To test whether the charge neutralization occurs during the flocculation, the zeta potentials of the flocculating systems with different concentration of MBF-W6 were recorded. MBF-W6 solution was added into 4 g/L kaolin clay suspension. The zeta potentials of kaolin suspension containing different concentrations of MBF-W6 were measured respectively using a Zeta Potential Sizer (Zetasizer Nano ZS England). To analyze the effect of Ca2+ on flocculating activity, the flocculating activity of MBF-W6 was compared with that of MBF-W6 plus CaCl2 at different concentrations.
The bioflocculant solution was introduced into the kaolin clay suspension to reach a concentration of 1.2 mg/L and stirred for 2 min. After settling for 1 min, the supernatant was removed and the flocs were collected for bonding type assay. Three kinds of chemical treatments were performed to test the bonding type in MBF-W6 induced flocs. The flocs were treated by 2 mol/L Ethylenediaminetetraacetic acid disodium salt (EDTA-2Na) (pH 7.8), 2 mol/L HCl and 5.0 mol/L urea, respectively. The individual mixture was gently stirred, and then the flocculating activity was determined. One drop of kaolin suspension or MBF-W6-induced flocs was added onto a slide and it was fixed by air drying. The fixed specimen was observed with a Scanning Electron Microscope (SEM) (Hitachi S-570, Japan).
1 mL 10 g/L FeCl3 was mixed to 9 mL 1 g/L purified MBF-W6 solution, and incubated at 4 °C for 1 h. The mixture was lyophilized directly or lyophilized after dialyzing at 4 °C for 12 h in distilled water (change fresh distilled water every 2 h) to remove Fe3+. The flocculating activity of MBF-W6 before and after removing Fe3+ was determined. The functional groups in the MBF-W6 before and after removing Fe3+ were compared using the Fourier Transform Infrared (FTIR) spectrophotometer (Bio-Rad FTIR Model FTS135). The spectrum of the sample was recorded on the spectrophotometer over a wave-number range of 650–4000 cm−1 under ambient conditions.
Our previous report showed that the main components of the purified MBF-W6 are total proteins (32.4%), total sugar (13.1%) and nucleic acid (6.8%) [21]. In order to analyze the major flocculating components of MBF-W6, purified MBF-W6 was heated at 100 °C for different time, and the flocculating activity was determined. As shown in Figure 1, the flocculating activity of MBF-W6 decreased from 90% to 30% in the first 30 min, after which, the treated MBF-W6 maintained 30% flocculating activity, suggesting that both the proteins and polysaccharides are the major flocculating components. Previous study has reported that the bioflocculant produced by Klebsiella pneumoniae is mainly composed of extracellular polysaccharides that exhibited significant resistance to heat [22]. Bioflocculant produced by Klebsiella mobilis is a polysaccharide as no amino acids were detected [16]. Bioflocculant from Proteus mirabilis TJ-1 is a complex mixture of polysaccharides and proteins [15]. Nocardia amarae and Rhodococcus erythropolis secrete an extracellular protein bioflocculant [23,24]. Here we found out that the MBF-W6 is a complex mixture of polysaccharides and proteins, with the proteins showing more flocculating activity than the polysaccharides.
The Ca2+ is regarded as a promoting factor for most extracellular polysaccharide bioflocculant. Bridging mediated by Ca2+ ions was considered to be one of the main flocculating mechanisms [6].However, the addition of Ca2+ ions can cause secondary pollution and the cost increases. In this study, the flocculating activity of MBF-W6 was compared in the presence and absence of CaCl2. As shown in Figure 2A, the addition of Ca2+ showed no positive effects on the flocculating activity of MBF-W6, on the contrary, the flocculating activity of MBF-W6 slightly decreased when the MBF-W6 concentration was lower than 1.0 mg/L. No significant effect was observed when the Ca2+ concentration was increased from 0 to 600 mg/L (MBF-W6 concentration is 1.2 mg/L) (Figure 2B). Our previous study also showed that other ions such as K+, Na+, Ba2+ Mg2+, Al3+ cannot improve the flocculating activity, and certain cations such as Fe3+ can distinctly decrease the flocculating activity of MBF-W6 [21].These results suggested that the flocculating activity is highly cation-independent, which avoids cost increase and secondary pollution. Several cation-independent bioflocculants have been reported in recent years. For example, the bioflocculant produced by Bacillus sp. F19 can achieve a flocculating activity without the addition of any cations [3]. Although the cations bound groups, such as carboxyl groups, present in these cation-independent bioflocculants, the flocculating activity is not enhanced by cations. This phenomenon could be explained by the carboxyl groups buried deep within protein structure, reducing the interaction between the carboxyl group and cations. In this case, the bridging mediated by cation is not the major flocculating mechanism, and some other novel flocculating mechanism might be driving these bioflocculants.
The charge neutralizationis regarded as one of the underlying flocculating mechanisms for certain cation-dependent bioflocculants. For example, the charge neutralization plays an important role during the kaolin clay flocculation by a Ca2+-dependent bioflocculant HBF-3, which is produced by a deep-sea bacterium mutant Halomonas sp. V3a’ [6]. To test whether the charge neutralization occurs during the MBF-W6 induced flocculation, the zeta potentials and the flocculating activity of the flocculating systems with different concentrations of MBF-W6 were determined. As shown in Table 1. The flocculating activity over 90% was achieved for systems within the range of 0.6 to 11.6 mg/L MBF-W6 and the zeta potentials remained negative and decreased slightly with the increase of MBF-W6 concentration. These findings suggest that static repulsive forces are present among the particles. Kaolin clay particles bear a negative charge on the surface that enables it to be suspended well in solution due to the formation of electrical double layer (the Zeta potential of kaolin clay particles in the solution was −14.8 mV). Polysaccharides and proteins contain the negative charged groups, such as carboxyl groups. The zata potential of bioflocculant solution (10 mg/L, pH 7) is −33.8 ± 1.5 mV. The addition of MBF-W6 further decreased the Zeta potentials of the flocculant system. When the MBF-W6 dosage was enhanced from 1.2 mg/L to 11.6 mg/L, the zeta potential decreased from #8722;20.4 mV to −25.2 mV, indicating that the increase of repulsive force between particles is an adverse factor for the flocculant of kaolin clay particles. As expected, the flocculating activity decreased from 96.27% to 92.14%. Therefore, the charge neutralization is not the principal mechanism behind the flocculating process of the negatively charged kaolin particles. This result is consistent with the cation independent theory as supplementation with positive charged cation is required to neutralize the negatively charged bioflocculant and kaolin clay.
Bioflocculant dosage (mg/L) | Zeta potential (mV) | Flocculating activity (%) |
0 | −14.8 ± 1.2 | |
0.6 | −21.9 ± 1.7 | 94.99 ± 0.13 |
1.2 | −20.4 ± 0.9 | 96.27 ± 1.22 |
2.3 | −22.3 ± 1.1 | 96.47 ± 0.35 |
4.1 | −22.1 ± 1.4 | 96.53 ± 0.87 |
5.8 | −22.6 ± 1.0 | 95.09 ± 0.98 |
11.6 | −25.2 ± 1.3 | 92.14 ± 1.84 |
The bonding types in MBF-W6-induced flocs were tested by EDTA-2Na, HCl and urea treatment. Urea is known to disrupt hydrogen bonds, while EDTA-2Na and HCl destroy the ionic bonds [6,25]. It can be seen from Figure 3 that MBF-W6-induced flocs were not disintegrated in 5 mol/L urea, suggesting that hydrogen bonds does not exist predominantly in MBF-W6 induced flocs. When the MBF-W6-induced flocs were treated with 2 mol/L HCl, the flocculating activity decreased slightly from 92.43% to 75.09%, also indicating that the bonding in MBF-W6 induced flocs is not of ionic nature as well. This result is consistent with the fact that the flocculation of MBF-W6 is cation-independent. In previous studies, the bridging mediated by some ions has been reported as a major mechanism for cation-dependent bioflocculants [6,17,26]. In addition, we found out that MBF-W6 induced flocs were sensitive to 2 mol/L EDTA-2Na. This can be explained by the fact that high concentration of EDTA-2Na affect the stability of the protein components or disrupt the interaction between the proteins and polysaccharides. This confirmed that proteins were one of the major flocculating components in MBF-W6.
In previous studies, some proteins or polysaccharides with high molecular weight have been reported as adhesins, which can promote the cells initial attachment on the solid surface to form biofilms [27,28]. So we speculated that the flocculation of cation-independent bioflocculants may be achieved by adhesion mechanism, in which the proteins or polysaccharides can attach on the surface directly and bridge the kaolin clay particles, and thus promoting their flocculation. SEM observation was performed to aid in interpreting the mechanism of kaolin suspension flocculation. Figure 4a shows the loose structure of kaolin clay before the addition of the bioflocculant MBF-W6. Compared with the kaolin clay without MBF-W6 treatment, the kaolin clay particles were bridged by the MBF-W6 directly and form tight packed structure(Figure 4b).This result confirmed our hypothesis that kaolin clay particles are attached and bridged by MBF-W6 directly.
Our previous study showed that the Fe3+ ions can significantly inhibit flocculating activity of MBF-W6 [21]. Similar results were reported for other bioflocculants [3,24]. But the mechanism of inactivation of bioflocculant by Fe3+ was unexplained. The flocculating activities and FTIR spectrophotometer readings of MBF-W6 after addition and removal of Fe3+ by dialysis were compared. It can be seen from Figure 5, the readings showed that the absorbance of MBF-W6 treated by Fe3+ changed at 1660 and 3360 cm−1 in comparison to that of untreated MBF-W6, suggesting that the –COO− and –NH groups were influenced by the presence of Fe3+. The –COO− and –NH groups have been reported as major functional groups during the flocculating process [9,21,29,30,31,32,33]. The flocculating activity of MBF-W6 was reduced to 37.9% on exposure to Fe3+ and was further decreased to 35.4% after Fe3+ removal by dialysis, although the FTIR spectrophotometer reading of MBF-W6 after removal of Fe3+ ions showed similar absorption peaks as that of untreated MBF-W6, indicating that the effects of Fe3+ was irreversible, and maybe achieved by influencing the stability of proteins and polysaccharide.
This study demonstrated that cation-independent bioflocculantMBF-W6 produced by Chryseobacterium daeguense W6 showed a different flocculating behavior from most cation-dependentextracellular bioflocculant. The major flocculating component is a complex of proteins and polysaccharides. The negatively charged kaolin particles are not precipitated by charge neutralization. And the bridging mediated by ions is not the major flocculating mechanism, which is consistent with the fact that the flocculation of MBF-W6 is cation-independent. The flocculation of MBF-W6 may be achieved by a novel mechanism, in which the kaolin clay particles are attached and bridged directly by cation-independent bioflocculantand promote their flocculant. Furthermore, the inactivation of Fe3+ on MBF-W6 was achieved by influencing –COO− and –NH groups. These results broaden understanding to flocculating mechanism of cation-independentbioflocculants. In future, the efforts, such as molecular methods, should be taken to further increase the yield of MBF-W6.
This research was supported by National Natural Science Foundation of China (31300054; 31370646), Youth Fund of the Natural Science Foundation of Jiangsu Province of China (BK20130228), Grants from Natural Science Foundation by Xuzhou Normal University (13XLR032), Priority Academic Program Development of Jiangsu Higher Education Institutions (PAPD) and Open Project of State Key Laboratory of agricultural biotechnology in 2014.
All authorsdeclare no conflicts of interest in this paper.
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2. | Mohammad Raouf Hosseini, Seyed Mohammad Sadeghieh, Mohammad Reza Azizinia, Seyed Hassan Tabatabaei, Biological separation of quartz from kaolinite using Bacillus licheniformis, 2020, 55, 0149-6395, 2061, 10.1080/01496395.2019.1617738 | |
3. | Weijie Liu, Yan Hao, Jihong Jiang, Aihua Zhu, Jingrong Zhu, Zhen Dong, Production of a bioflocculant from Pseudomonas veronii L918 using the hydrolyzate of peanut hull and its application in the treatment of ash-flushing wastewater generated from coal fired power plant, 2016, 218, 09608524, 318, 10.1016/j.biortech.2016.06.108 | |
4. | Weijie Liu, Rongnan He, Cong Liu, An alkali-tolerant strain Microbacterium esteraromaticum C26 produces a high yield of cation-independent bioflocculant, 2016, 3, 2372-0352, 408, 10.3934/environsci.2016.3.408 | |
5. | Faouzi Ben Rebah, Wissem Mnif, Saifeldin M. Siddeeg, Microbial Flocculants as an Alternative to Synthetic Polymers for Wastewater Treatment: A Review, 2018, 10, 2073-8994, 556, 10.3390/sym10110556 | |
6. | Weijie Liu, Yan Hao, Jihong Jiang, Cong Liu, Aihua Zhu, Jingrong Zhu, Zhen Dong, Biopolymeric flocculant extracted from potato residues using alkaline extraction method and its application in removing coal fly ash from ash-flushing wastewater generated from coal fired power plant, 2017, 4, 2372-0352, 27, 10.3934/environsci.2017.1.27 | |
7. | Nidhi Joshi, Manali Rathod, Dhruva Vyas, Raghawendra Kumar, Kalpana Mody, Multiple Pollutants Removal from Industrial Wastewaters Using a Novel Bioflocculant Produced by Bacillus licheniformis NJ3, 2019, 38, 19447442, S306, 10.1002/ep.13027 | |
8. | Arpit Shukla, Paritosh Parmar, Dweipayan Goswami, Baldev Patel, Meenu Saraf, Characterization of novel thorium tolerant Ochrobactrum intermedium AM7 in consort with assessing its EPS-Thorium binding, 2020, 388, 03043894, 122047, 10.1016/j.jhazmat.2020.122047 | |
9. | Jibrin Ndejiko Mohammed, Wan Rosmiza Zana Wan Dagang, Role of Cationization in Bioflocculant Efficiency: a Review, 2019, 6, 2198-7491, 355, 10.1007/s40710-019-00372-z | |
10. | Weijie Liu, Chenchu Zhao, Jihong Jiang, Qian Lu, Yan Hao, Liang Wang, Cong Liu, Bioflocculant production from untreated corn stover using Cellulosimicrobium cellulans L804 isolate and its application to harvesting microalgae, 2015, 8, 1754-6834, 10.1186/s13068-015-0354-4 | |
11. | Sidney Maliehe Tsolanku, Tlou Selepe Nelson, Ntombela Golden, Simonis Jean, Kotze Basson Albertus, Ngema Siyanda, Samukelisiwe Xaba Petunia, Mpanza Fanelesibonge, Production and characteristics of bioflocculant TPT-1 from a consortium of Bacillus pumilus JX860616 and Alcaligenes faecalis HCB2, 2016, 10, 1996-0808, 1561, 10.5897/AJMR2016.8258 | |
12. | Shifa M.R. Shaikh, Mustafa S. Nasser, Ibnelwaleed Hussein, Abdelbaki Benamor, Sagheer A. Onaizi, Hazim Qiblawey, Influence of polyelectrolytes and other polymer complexes on the flocculation and rheological behaviors of clay minerals: A comprehensive review, 2017, 187, 13835866, 137, 10.1016/j.seppur.2017.06.050 | |
13. | Teik-Hun Ang, Kunlanan Kiatkittipong, Worapon Kiatkittipong, Siong-Chin Chua, Jun Wei Lim, Pau-Loke Show, Mohammed J. K. Bashir, Yeek-Chia Ho, Insight on Extraction and Characterisation of Biopolymers as the Green Coagulants for Microalgae Harvesting, 2020, 12, 2073-4441, 1388, 10.3390/w12051388 | |
14. | Zhi Min Ng, Uganeeswary Suparmaniam, Man Kee Lam, Jun Wei Lim, Siew Hoong Shuit, Steven Lim, Bridgid Lai Fui Chin, Peck Loo Kiew, A. Nzihou, R. Boopathy, M. Nasef, S. Yusup, D.C.W. Tsang, N.A. Amran, B. Abdullah, Assessing the effects of operating parameters on flocculation of Chlorella vulgaris using bioflocculants extracted from miscellaneous waste biomass, 2021, 287, 2267-1242, 04004, 10.1051/e3sconf/202128704004 | |
15. | Mohammad Mohammad Alnawajha, Setyo Budi Kurniawan, Muhammad Fauzul Imron, Siti Rozaimah Sheikh Abdullah, Hassimi Abu Hasan, Ahmad Razi Othman, Plant-based coagulants/flocculants: characteristics, mechanisms, and possible utilization in treating aquaculture effluent and benefiting from the recovered nutrients, 2022, 29, 0944-1344, 58430, 10.1007/s11356-022-21631-x | |
16. | Jayaprakash Arulraj, Ashokraj Kattur Venkatachalam, Revathy Soundararajan, Rajesh Embranahalli Mani, Microbial flocculants as an excellent alternative to synthetic flocculants for industrial application: A comprehensive review, 2023, 2672-7277, 79, 10.35118/apjmbb.2022.030.4.08 | |
17. | Setyo Budi Kurniawan, Muhammad Fauzul Imron, Che Engku Noramalina Che Engku Chik, Amina Adedoja Owodunni, Azmi Ahmad, Mohammad Mohammad Alnawajha, Nurul Farhana Mohd Rahim, Nor Sakinah Mohd Said, Siti Rozaimah Sheikh Abdullah, Nor Azman Kasan, Suzylawati Ismail, Ahmad Razi Othman, Hassimi Abu Hasan, What compound inside biocoagulants/bioflocculants is contributing the most to the coagulation and flocculation processes?, 2022, 806, 00489697, 150902, 10.1016/j.scitotenv.2021.150902 | |
18. | Cong Liu, Di Sun, Jiawen Liu, Jingrong Zhu, Weijie Liu, Recent advances and perspectives in efforts to reduce the production and application cost of microbial flocculants, 2021, 8, 2197-4365, 10.1186/s40643-021-00405-2 | |
19. | Haolin Huang, Jingsong Li, Weiyi Tao, Shuang Li, A Functionalized Polysaccharide from Sphingomonas sp. HL-1 for High-Performance Flocculation, 2022, 15, 2073-4360, 56, 10.3390/polym15010056 | |
20. | Magdalena Czemierska, Aleksandra Szcześ, Anna Jarosz-Wilkołazka, Physicochemical factors affecting flocculating properties of the proteoglycan isolated from Rhodococcus opacus, 2021, 277, 03014622, 106656, 10.1016/j.bpc.2021.106656 | |
21. | Melody Ruvimbo Mukandi, Moses Basitere, Seteno Karabo Obed Ntwampe, Boredi Silas Chidi, Bioflocculant Producing Bacillus megaterium from Poultry Slaughterhouse Wastewater: Elucidation of Flocculation Efficacy and Mechanism, 2024, 14, 2076-3417, 3031, 10.3390/app14073031 | |
22. | Matthias J. Orchard, Guangze Yang, Grant B. Webber, George V. Franks, Chun-Xia Zhao, Development of bioflocculants for mineral processing, 2024, 28, 25892347, 100965, 10.1016/j.mtsust.2024.100965 | |
23. | Qin Peng, Xinyue Gong, Ruixin Jiang, Na Yang, Ruiting Chen, Binglin Dai, Rui Wang, Performance and characterization of snail adhesive mucus as a bioflocculant against toxic Microcystis, 2024, 270, 01476513, 115921, 10.1016/j.ecoenv.2023.115921 | |
24. | An-Sofie Christiaens, Robin Daenen, Ilse Smets, Bioaugmentation of a structural extracellular polymeric substances (EPS) producer to improve activated sludge bioflocculation: lessons learned, 2023, 18, 1751-231X, 1663, 10.2166/wpt.2023.103 | |
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Bioflocculant dosage (mg/L) | Zeta potential (mV) | Flocculating activity (%) |
0 | −14.8 ± 1.2 | |
0.6 | −21.9 ± 1.7 | 94.99 ± 0.13 |
1.2 | −20.4 ± 0.9 | 96.27 ± 1.22 |
2.3 | −22.3 ± 1.1 | 96.47 ± 0.35 |
4.1 | −22.1 ± 1.4 | 96.53 ± 0.87 |
5.8 | −22.6 ± 1.0 | 95.09 ± 0.98 |
11.6 | −25.2 ± 1.3 | 92.14 ± 1.84 |