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Heavy metal removal from acid mine drainage by calcined eggshell and microalgae hybrid system Hee-Jeong Choi & Seung-Mok Lee

Environmental Science and Pollution Research ISSN 0944-1344 Volume 22 Number 17 Environ Sci Pollut Res (2015) 22:13404-13411 DOI 10.1007/s11356-015-4623-3

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Author's personal copy Environ Sci Pollut Res (2015) 22:13404–13411 DOI 10.1007/s11356-015-4623-3

RESEARCH ARTICLE

Heavy metal removal from acid mine drainage by calcined eggshell and microalgae hybrid system Hee-Jeong Choi 1 & Seung-Mok Lee 1

Received: 8 January 2015 / Accepted: 27 April 2015 / Published online: 5 May 2015 # Springer-Verlag Berlin Heidelberg 2015

Abstract This study investigates the use of calcined eggshells and microalgae for the removal of heavy metals from acid mine drainage (AMD) and the simultaneous enhancement of biomass productivity. The experiment was conducted over a period of 6 days in a hybrid system containing calcined eggshells and the microalgae Chlorella vulgaris. The results show that the biomass productivity increased to ~8.04 times its initial concentration of 0.367 g/L as measured by an optical panel photobioreactor (OPPBR) and had a light transmittance of 95 % at a depth of 305 mm. On the other hand, the simultaneous percent removal of Fe, Cu, Zn, Mn, As, and Cd from the AMD effluent was found to be 99.47 to 100 %. These results indicate that the hybrid system with calcined eggshells and microalgae was highly effective for heavy metal removal in the AMD. Keywords Acid mine drainage . Biomass . Calcined eggshells . Heavy metal removal . Microalgae . Optical panel photobioreactor

Introduction Acid mine drainage (AMD) is a serious environmental issue that is greatly contaminating water bodies in and around abandoned mine industries. When sulfide/pyretic minerals are Responsible editor: Zhihong Xu * Hee-Jeong Choi [email protected] 1

Department of Environmental Engineering, Catholic Kwandong University, Beomil-ro 579, Gangneung 210-701, Korea

exposed to the atmosphere in the presence of water, the oxidation of sulfide produces sulfuric acid and enters into water bodies along with several toxic heavy metal ions in the effluent waters. AMD causes enhanced acidity of water bodies along with elevated levels of iron, sulfates, and heavy metals. This varies depending upon the type of originating mineral deposit. The metallic load in the effluent water is of greater concern than the acidity in terms of environmental damage (Tolonen et al. 2014; Zhang and Wang 2014). Several methods are described for the treatment of AMD. Adsorption is one of the most commonly used methods and is efficient, particularly in the removal of toxic pollutants from effluent waters (Ndlovu 2014; Kim 2015). In summary, the identification and development of low-cost and eco-friendly adsorbents are currently gaining momentum for effective and useful AMD treatment (Johnson and Hallberg 2005; Chen et al. 2014). If low-cost biosorbents are used in AMD treatment processes, the process cost may be significantly reduced. In this paper, hen eggshells are used as a low-cost biological sorbent of heavy metal ions. The Korean food industry generates 90,000 t of eggshell waste a year (Kim et al. 2009). The disposal uses for eggshell waste include 26.6 % in fertilizer, 21.1 % in animal feed ingredients, 26.3 % in waste discarded in municipal dumps, and 15.8 % in other uses (Tsai et al. 2008; Liu et al. 2013). Many landfills are unwilling to accept the waste because the eggshells and the attached membrane attract vermin. Eggshell waste has been recommended for use as an adsorbent because of its low cost, copious availability in nature, nontoxicity, high specific surface area, and high potential of ion exchange for charged pollutants and because it is safe to handle (Wei et al. 2009; Elwakeel and Yousif 2010; Zang et al. 2012). Eggshell consists of approximately 95 % CaCO3 (which is also the main ingredient in sea shells). The remaining 5 % includes calcium phosphate, magnesium carbonate, and soluble and insoluble proteins (Nys

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and Guyot 2011; Guru and Dash 2014). Because eggshell is mainly composed of calcium carbonate, it should behave like known sorbents that also contain this compound, such as calcite or calcareous soil (Tsai et al. 2006; Gao and Chunli 2012; Wang et al. 2013). Sorption by eggshells occurs mainly by an exchange reaction, and it should be usable as a new biological sorbent of metal ions. Natural eggshells are less porous than calcined eggshells; therefore, in this paper, calcined eggshells are used to increase the heavy metal removal in the AMD. Microalgae can sequester heavy metal ions by the same adsorption and absorption mechanisms as other microbial biomass (Yang et al. 2015). Algae are a renewable natural biomass that proliferate ubiquitously and abundantly in the littoral zones of the world and have attracted the attention of many investigators as organisms that can be tested and used as new adsorbents to adsorb metal ions. Several advantages in applying algae as a biosorbent include its wide availability, low cost, high metal sorption capacity, and reliable quality (Fu and Wang 2011; Kumar et al. 2015). There is much research about the metal biosorption using algal biomass. Examples of recent reports include the biosorption of Cu and Zn using Chlorella minutissima (Yang et al. 2015); the biosorption of Cu, Cd, Pb, and Zn using Caulerpa lentillifera (Kumar et al. 2015); the biosorption of chromium from wastewater using Ulva lactuca (El-Silaily et al. 2007); and the biosorption of lead(II) from wastewater by Cladophora fascicularis (Deng et al. 2007). Many researchers reported several biological, chemical, and physical processes for heavy metal removal from AMD. However, it seems that there is no report examining the effect of calcined eggshell and microalgae hybrid system for the treatment of AMD. The novelty in this study is to propose an effective use of a hybrid system using calcined eggshells and microalgae for the removal of heavy metals and biomass productivity in AMD.

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C. vulgaris was added. The cultures were maintained in a dark and light cycle of 8 and 16 h, respectively. Calcined eggshells Waste eggshell samples were collected from a chicken farm in Gangneung City in Korea. To remove any adhesion and interference materials, such as organics and salts, the sample was rinsed several times with deionized water and boiled in water. After cleaning, eggshells were dried in an oven at 105 °C for 24 h and crushed into fine powder using a mortar and pestle. This raw eggshell powder (325 mesh) was then calcined in a Muffle furnace to 900 °C, and the temperature was maintained for 2 h. This fraction was approximately 60 % of the total dried sample. The thermal treatment had two parts: for the first 30 min, most of the organic materials were burnt off, and during in the second part, the eggshells were transformed into a soft white powder that was designated as calcined eggshells. The high cationic charge density of eggshells allows it to strongly adsorb the negative regions of other particles. The main ingredient in eggshells is calcium carbonate (the same brittle white material that chalk, limestone, cave stalactites, sea shells, coral, and pearls are made of). Approximately 85–95 % of the eggshell is calcium carbonate, 1.4 % is magnesium carbonate, 0.76 % is phosphate, and 4 % is organic matter. Eggshells also contain traces of sodium, potassium, zinc, manganese, iron, and copper. If calcium from the shell is removed, the organic materials that are left possess calcium (or other metal cation)-binding properties (Chojnacka 2005). Because eggshell is composed mainly of calcium carbonate, it should behave like known sorbents that also contain this compound, such as calcite (Witoon 2011) and calcareous soil (Park et al. 2013). Sorption by eggshells should occur mainly by an exchange reaction, and it should be possible to use it as a new biological sorbent of metal ions. Characteristics of AMD

Materials and methods Microalgae cultures and medium Seed cultures of Chlorella vulgaris were cultivated in Jaworski’s medium (JM) under light-emitting diode (LED) lamps at ambient temperature. JM consisted of 4.0 g of Ca(NO3)2·H2O, 2.48 g of KH2PO4, 10.0 g of MgSO4·7H2O, 3.18 g NaHCO3, 0.45 g of EDTAFeNa, 0.45 g of EDTANa2, 0.496 g of H3BO3, 0.278 g of MnCl2·4H2O, 0.20 g of (NH4)6Mo7O24·4H2O, 0.008 g of cyanocobalamin, 0.008 g of thiamine HCl, 0.008 g of biotin, 16.0 g of NaNO3, and 7.2 g of Na2HPO4·12H2O in 200 ml of deionized water. The microalgae were cultured in a 200-mL conical flask containing 100 mL of JM, pH (7.2 ± 0.3), and then, 10 mL of

The chemical characteristics of the AMD used for this investigation are shown in Table 1. A pilot scale AMD treatment plant was installed at the Yongdong mine located in Gangneung city, Korea. This AMD contained excesses of Fe, Cu, Zn, Mn, As, and Cd content and was low in nutrients compared to the municipal wastewaters. The average pH and electrical conductivity of AMD were measured to be 2.41 and 2295 μS/cm, respectively. Experimental design A schematic diagram of the hybrid calcined eggshell and microalgae system for the treatment of AMD is shown in Fig. 1. The operation period of the pilot plant was 180 days. The reactor contained two compartments. The first

Author's personal copy 13406 Table 1

Environ Sci Pollut Res (2015) 22:13404–13411 The characteristics of AMD

Composition

Concentration

pH

2.41 (2.28–2.50)

DO (mg/L)

4.35 (3.10–4.88)

Water temp. (°C) Eh (mV) EC (μS/cm) Cu (mg/L)

12.10 (10.80–14.7) 322.28 (305.1–351.40) 2295.00 (2070.35–2570.52) 22.78 (20.11–26.78)

Fe (mg/L)

137.48 (140.83–225.80)

Zn (mg/L) As (mg/L)

19.77 (17.39–23.57) 0.45 (0.16–0.67)

Cd (mg/L) Mn (mg/L)

0.27 (0.15–0.36) 10.35 (9.23–11.95)

Eh oxidation-reduction potential, EC electric conductivity

compartment was filled with the calcined eggshell powder, and the AMD water was introduced here first. The calcined eggshell technique relies on the suspension of small particles that flow upward in the wastewater. This process is capable of neutralizing and removing heavy metals from the AMD. Then, the supernatant is transferred to a microalgae reactor for the treatment of the remaining heavy metals. The hybrid calcined eggshell and microalgae process treated a total volume of 40 L with calcined eggshells at 120 g/L for 3 h for the neutralization phase and a 40-L working volume for 6 days for the microalgae phase to cultivate microalgae and for the removal of the investigated heavy metal ions. After 6 days, grown microalgae were harvested using chitosan.

OPPBR construction and operation The optical panel photobioreactor (OPPBR) is operated with a 40-L working volume and is equipped with an optical panel Fig. 1 A schematic diagram of calcined eggshell and the microalgae hybrid system

(OP) (Fig. 1). The initial concentration of the inoculated microalgae C. vulgaris is 0.367±0.6 g/L. The experiments are conducted at neutral pH (7.2±0.3) under dark and light cycles of 8 and 16 h, respectively. The temperature is maintained at 23±1 °C using LEDs for 20 days. The OPPBRs are aerated continuously at an aeration rate of 0.5 L/min. CO2 at the equivalent aeration rate of 0.02 vvm is used for cultivation. CO2 with a flow rate of 0.74 L/min is introduced into the reactor. The OPPBR is designed such that the light source (22 LEDs), an LED panel (bar type), is placed in the OPPBR. A v-grooved OP is inserted underneath in the photobioreactor (PBR). The OP exhibits 94 % transmittance and 1.19 specific gravity. The OP dimensions are 210 mm (L)×290 mm (H)×6 mm (W) and are constructed from a transparent panel of pure poly-methylmethacrylate (PMMA). This material is fairly transparent, and it has almost negligible light absorption in the visible region (Choi 2014; Choi and Lee 2014). The thickness of the OP is 6 mm. The incident light is uniformly distributed across both sides of the OP in the reactor and provides greater functionality. The LED light source is used because it is efficient and provides a required wavelength of light from 430 to 670 nm, which is selective for microalgal growth. The light intensity, which represents the amount of light used for photosynthesis, is 200~250 μmol photons/m2/s. Analytical methods To characterize the calcinations of eggshell, a thermal gravimetric analyzer (TGA-951 DuPont Instruments Co., USA) was used. A portion of the dried eggshell previously freed of impurities and interfering materials, such as organics and salts, was loaded in the TGA analyzer, and then, pyrolysis was performed at up to 900 °C, raising the temperature 40/min with a continuous injection of N2. X-ray fluorescence (XRF1500, Shimadzu, Japan) was used for the qualitative and

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quantitative analyses of the inorganic compositions in the natural and calcined eggshells. The mineralogy of the natural and calcined eggshells was characterized by an X-ray diffractor (X-ray Diffractometer, Rigaku PMG-S2, 30 kV×10 mA). Images of the surface of natural and calcined eggshells were obtained by a scanning electron microscope (SM-300, Topcon, Japan). To determine the biomass concentration, a sample of microalgae in growth medium was centrifuged for 10 min at 628g, washed with distilled water, and then dried in an oven at 105 °C for 24 h to a constant weight. The biomass productivity P (g/L/day) was calculated from the variation in biomass concentration (g/L) within a cultivation time (in days) according to the following equation:

calcination, the major inorganic composition was identified as lime (99.54 %), and K, P, and Sr were minor components. This result indicates that the compositions of eggshell can be changed by calcination, as shown in Table 2, and suggests that a relatively pure sample can be obtained from eggshells by removal of more organic compositions. SEM images of eggshell samples before and after calcinations are shown in Fig. 2a, b, respectively. Before calcination, natural eggshells had a generally irregular crystal structure. After calcinations at 800 °C for 2 h, as shown in Fig. 2b, the crystal structure changed and a developed pore was observed, resulting from the emission of CO2. The formation of CO2 is assumed to follow an endothermic reaction, as described in reaction (4).

P ¼ ðX 1 −X 0 Þ=ðt 1 −t 0 Þ

CaCO3 →CaO þ CO2 ðcalcinationsÞ

ð1Þ

ð4Þ

The specific growth rate μ (in days) was calculated using Eq. (2) μ ¼ InðX 1 =X 0 Þ=ðt 1 −t 0 Þ

ð2Þ

where X1 and X0 are the biomass concentrations (g/L) on days t1 and t0, respectively. Uniformity was calculated using Eq. (3) Uniformity ¼ Lmin =Lmax

ð3Þ

where Lmin is the minimum light intensity and Lmax is the maximum light intensity. All samplings and measurements were conducted at the same time every day. The Fe, Cu, Zn, Mn, As, and Cd were analyzed using an inductively coupled plasma optical emission spectrometry (ICP-OES: Optima 3300XL, PerkinElmer, MA, USA), following the standard method of measurements (vide APHA 2012). The Eh and EC were measured using a pH/ORP meter (ISTEK, pH-20N) and an EC/TDS/salinity meter (ISTEK, EC-40N), respectively.

Results and discussion Neutralization process and heavy metal removal using eggshells in the AMD Calcination of eggshells Before calcinations, Ca2+ as limestone (91.86 %) and Si (4.32 %) were the important inorganic compositions of eggshells. A similar result has been reported for the chemical composition of natural and boiled hen and duck eggshells, as determined by X-ray fluorescence spectrometry (Liu et al. 2013). They reported that all eggshells had similar chemical contents and were mainly composed of CaCO3 and a few of other elements, such as S, Mg, P, Al, K, and Sr. After

Change of pH by various dosages of calcined eggshells and mixing times Figure 3 depicts the change in AMD effluent pH in the presence of calcined eggshells. These results show that a fast initial increase of pH occurred for AMD effluents in presence of calcined eggshells and that the pH rose to 7.0±0.23 from 2.41 ±0.11 within just 30 min of contact with calcined eggshells. After 30 min, the pH increased slowly and reached a value of 7.6±0.87 after 3 h of contact. The pH rose to 7.2±0.19 and 7.51±0.21 for 2.5 and 3 g/L calcined eggshells, respectively. Up to 3 g/L of calcined eggshell concentration did not significantly change the pH value, and the highest pH value obtained was 7.5±0.21 for 5 g/L calcined eggshells. To neutralize the AMD using the calcined eggshells, a 30-min mixing time and a 2.5–3 g/L dose were recommended. Natural eggshell has the major constituent CaCO3. A calcium carbonate feedstock is used to neutralize the acidity in AMD systems by removing free hydrogen ions from the AMD, thereby increasing the effluent pH (Köse and KivanÇ 2011). Calcium carbonate changes to CaO when eggshells are calcined. CaO remains in the solution to play an important role in correcting the adverse effects of acidic conditions. In solution, the carbonate anion is very active in neutralizing H+ cations. While its mode of action is quite different from eggshell, the ability of CaO to neutralize acid solutions is equivalent to eggshell. The resultant high solution pH could be explained by the dissolution of CaO as described in reaction (5). CaOðsÞ þ H2 OðlÞ→CaðOHÞ2 ðsÞ

ð5Þ

Moreover, the surface of calcined eggshell provides active sites that are capable of adsorbing several heavy metal toxic ions from aqueous solutions, and this ability is further

Author's personal copy 13408 Table 2 Composition of eggshells (natural and calcined) by X-ray fluorescence

Environ Sci Pollut Res (2015) 22:13404–13411

Compound

Natural (%)

Calcined (%)

Compound

Natural (%)

Calcined (%)

Ca Si

91.86 4.32

99.54 –

P Cl

0.30 0.22

0.08 –

Al

1.45



Sr

0.19

0.14

Na K

0.51 0.52

– 0.24

Fe Zn

0.08 0.09

– –

F

0.44



Zr

0.02



enhanced under elevated solution pH conditions (Tsai et al. 2006). Heavy metal removal using calcined eggshells The adsorption of several heavy metals by the calcined eggshells in the AMD is shown in Table 3. In this study, the results indicate that the heavy metal adsorption efficiency is 80.30, 82.31, 80.27, 80.58, 82.22, and 81.48 % for Fe, Cu, Zn, Mn, As, and Cd, respectively, using calcined eggshells. Cu

apparently has a higher percent adsorption than As. The removal rate of natural eggshell also had some removal capacity of heavy metal, 42 % for Fe, 37 % for Cu, 48 % for Pb, 24 % for Cd, and 30 % for Cr (Liu et al. 2013). The calcined eggshell provides a good medium that not only increases the pH of the AMD effluent but also significantly adsorbs heavy metal toxic ions simultaneously. Calcined eggshell is a nontoxic, noncorrosive, and safe-to-handle material; hence, it has wider potential applications in wastewater treatment technologies. It is biocompatible and has attractive adsorption properties and polyelectrolicity; additionally, it can be regenerated by a number of applications. The high cationic charge density of calcined eggshells allows it to strongly adsorb negative regions on other particles. Biomass productivity and heavy metal removal using microalgae Biomass productivity

180

6

120

4

60

2

Amount of eggshell [g/L]

Mixing time [min]

Light is one of the most vital factors that influences the growth and productivity of microalgae. The uniformity was defined in Eq. 3, and hence, the luminance uniformity (%) was obtained as a function of the varied depth level of OP. The light transmittance is found to be 95 % at 305-mm depth in the OPPBR. The OP radiates light with adequate uniformity, prevailing from the top to the bottom of the PBR. The results clearly demonstrate that enhanced light intensity is achieved even

0

0 0

2

4

6

8

pH

Fig. 2 SEM images for natural eggshells (a) and calcined eggshell (b)

Fig. 3 Change of pH with mixing time and dosage of calcined eggshells

Author's personal copy Environ Sci Pollut Res (2015) 22:13404–13411 Table 3

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Heavy metal removal by calcined eggshells

Calcined eggshell process

Heavy metals

Fe

Cu

Zn

Mn

Initial concentration (mg/L)

137.48

22.78

19.77

10.35

0.45

0.27

27.14

4.03

3.90

2.01

0.08

0.05

Removal (%)

80.30

82.31

80.27

80.58

82.22

81.48

Biomass productivity [g/L/d]

3

2

1

0 1

2

Cd

End concentration (mg/L)

deep inside of the PBR using an OP. Moreover, the performance of the PBR containing OP is better than the PBR that does not have an OP unit. The OP of PBR increases the illumination surface to volume ratio as well, providing efficient utilization of light radiation for biomass production. The use of OP provides an equal amount of light energy passing through the reactor, and the irradiance profile is redistributed due to diffuse light from the OP (Choi and Lee 2014). The redistributed irradiance profile results in the higher photosynthetic efficiency of microalgae and leads to effective light utilization. Consequently, the photobioreactor with OP not only increases the illumination area for cultivation but also provides conditions for the effective utilization of light energy to increase the growth rate of microalgae compared with OP unused PBR. The average biomass growth in the AMD is shown in Fig. 4. The biomass productivity growth reaches 2.95 g/L/ day 6 days from the initial concentration of 0.367±0.6 g/L. It is observed that the biomass growth is approximately 8.04 times higher than the initial concentration. It is further noted that the biomass growth in OPPBR is significantly increased during the initial 1–3 days and slows at the latter period and attains an almost constant growth after 5–6 days. The specific biomass growth rate is known as the increase in cell mass per unit time. This is calculated using Eq. (2). This rate is also considered to be an indicator of the photosynthetic efficiency of the microalgae. The maximum specific growth rate from the initial cell concentration is found to be significant as 0.98±0.015 1/day. This is because the OP affects the high transparent surfaces, high illumination surfaces, and high mass transfer rates, which enable an increased specific growth

0

As

3

4

Time [day]

Fig. 4 Biomass productivity using C. vulgaris in the AMD

5

6

rate in the OPPBR. Hsieh and Wu (2009) reported 1.745 1/day of specific growth rate using Chlorella sp. in transparent rectangular chamber PBR. Ong et al. (2010) obtained a 0.238 1/day specific growth rate using Chlorella sp. during an 8-day cultivation in an outdoor photobioreactor. Heavy metal removal by microalgae in the AMD The removal percentage of heavy metal ions in AMD using C. vulgaris is represented in Table 4. The results show that the average percent of investigated heavy metal removal is 98.27, 97.02, 99.49, 99.00, 100, and 100 % for Fe, Cu, Zn, Mn, As, and Cd, respectively, in the OPPBR using microalgae. Microalgae require heavy metal ions as trace elements for growth. However, large amounts of heavy metal ions have inhibited effect on the microalgae growth (Romera et al. 2007). Microalgae are one of the most important biosorbents. Metals are taken up by algae through adsorption. First, the metal ions are quickly adsorbed over the cell surface; this process is called physical adsorption. Then, these ions are transported slowly into the cytoplasm in a process called chemisorptions (Deng et al. 2007; Fu and Wang 2011). In the present investigation, by increasing the exposure time, the rate of the percent of metal ion removal slowed down gradually and an apparent equilibrium was established. After the equilibrium period, the metal ion sorption by the microalgae biomass was not changed significantly, further increasing the operation time. The results are in agreement with those obtained by Shanab et al. (2012). Various studies have been carried out to show the role of microalgae in the bioremediation of heavy metals. Johnson and Hallberg (2005) reported that the percentage adsorbed by microalgae is 90.26, 90.21, 93.48, 91.26, 90.87, and 90.12 % for Fe, Cu, Zn, Mn, As, and Cd, respectively. Similarly, Yang et al. (2015) removed 90.24 % Cu and 98.42 % Zn from aqueous solutions using C. minutissima. The mechanism of binding metal ions by inactivated algal biomass may depend on the species and the ionic changes of the metal ion, the algal organism, and the chemical composition of the metal ion solution (Fu and Wang 2011). To use algal biomass effectively for water purification and metal reclamation, it is important to understand the chemical nature of the metal-binding process (Kumar et al. 2015). Microalgae biomass has been successfully used as a sorbing agent.

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Table 4 Heavy metal removal by C. vulgaris Microalgae process

Heavy metals

Fe

Cu

Zn

Mn

As

Cd

Initial concentration (mg/L)

27.14

4.03

3.90

2.01

0.08

0.05

End concentration (mg/L)

0.47

0.12

0.02

0.02

0.00

0.00

Removal (%)

98.27

97.02

99.49

99.00

100

100

Because microalgae use light as an energy source, facilitating the maintenance of metabolism in the absence of organic carbon sources, an electron acceptor is required by bacteria or fungi (Deng et al. 2007). Relationship between biomass productivity and the removal of heavy metal ions Figure 5 shows the linear relationship of Cu, Zn, Mn, As, and Cd and biomass productivity. The coefficient (R2) of determination is an important tool for determining the degree of linear correlation of variables in regression analysis (Song et al. 2005). In this experiment, a relatively high correlation coefficient (R2) of 0.9958 for Cu, 0.9905 for Zn, 0.975 for Mn, 0.9941 for As, 0.9203 for Cd, and 0.968 for Fe is obtained. The investigated heavy metal concentration in the AMD is decreased linearly with the increasing biomass productivity. Specifically, the obtained percentage removal of As and Cd with microalgae was higher than that of other heavy metal ions. However, the relationship between biomass productivity and the As and Cd concentrations is relatively lower than other investigated heavy metal ions. Total heavy metal removal by calcined eggshell and the microalgae hybrid system The experimental results indicate that the total percent removal of the investigated heavy metal ions from the AMD effluents using the calcined eggshell and microalgae hybrid system is 99.66, 99.47, 99.90, 99.81, 100, and 100 % for Fe, Cu, Zn,

Conclusions This study investigated the heavy metal removal and biomass productivity in acid mine drainage (AMD) using calcined eggshell and microalgae hybrid systems. Calcined eggshells effectively neutralized the acidity and partially removed heavy metals from AMD effluents. The biomass productivity increased from 0.367 to 2.95 g/L within 6 days of operation. The biomass growth was ~8.04 times higher than that of the initial concentration. The total removal rate of Fe, Cu, Zn, Mn, As, and Cd was 99.66, 99.47, 99.90, 99.81, 100, and 100 %, respectively, from the AMD effluent using calcined eggshell and a microalgae hybrid system. A fairly good linear relationship was achieved between the investigated heavy metal removal and the biomass productivity because a high value of correlation coefficient (R2) was obtained. The calcined eggshell and microalgae hybrid system was highly effective for heavy metal removal. Therefore, the calcined eggshell and microalgae system is a useful alternative for a large-scale treatment of effluent waters emanating from AMDs.

100

10

Cu Cd

Zn Mn

Removal [%]

R² = 0.9958 Concentration [mg/L]

Mn, As, and Cd, respectively (Fig. 6). These results clearly demonstrate that the calcined eggshell and microalgae hybrid process is effective for heavy metal removal and is comparable to the individual application of calcined eggshells or microalgae process. Moreover, an enhanced growth of C. vulgaris could further be utilized as a potential biodiesel source.

R² = 0.9905 R² = 0.975 5

50

R² = 0.9203

Fe

0 0

1

2

Cu

3

Biomass productivity [g/L/d]

Fig. 5 The relationship between Cu, Zn, Mn, and Cd and biomass productivity

with calcined eggshells

Zn

Mn

Heavy metals with microalgae

As

Cd

Total removal

Fig. 6 Total removal of heavy metal ions by calcined eggshell and microalgae hybrid system

Author's personal copy Environ Sci Pollut Res (2015) 22:13404–13411 Acknowledgments This study was supported by the Basic Science Research Program through the National Research Foundation of Korea (NRF) funded by the Ministry of Education, Science and Technology (2013006899).

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