In-situ Pb(2+) remediation using nano iron particles.

Originally, application of nano zero valent iron (nZVI) particles for the removal of lead (Pb(2+)) in porous media was studied. At first, stabilized nZVI (S-nZVI) was prepared and characterized, then used in batch and continuous systems. Based on the batch experiments, corresponding reaction kinetics well fitted with the pseudo-first-order adsorption model, and reaction rate ranged from 0.01 to 0.04 g/mg/min depend on solution pH and the molar ratio between Fe and Pb. In batch tests, optimal condition with more than 90% removal efficiency at 60 min was observed at a pH range of 4 to 6 and Fe/Pb ratio more than 2.5. Continuous experiments exposed that Pb(2+) remediation was as well influenced by seepage velocity, grain size, and type of porous media. The maximum Pb(2+) removal efficiency in batch and bench-scale systems were 97% and 81%, correspondingly. The results have shown the ability of S-nZVI to use in permeable reactive barriers, as an efficient adsorbent for Pb(2+), because of its excellent stability, high reducing power, and a large surface area.

Background

During the last two decades, presence of heavy metal ions in the environment, especially in water sources, was becoming a major concern due to their non-biodegradability, toxicity, wide-spread presence, and tendency to accumulate in living organisms [1]. Lead, a main concern metal pollutant, is widely used in battery manufacturing, electroplating industry, painting and printing processes, plumbing and the combustion of automobile petrol [2]. The U.S. Environmental Protection Agency (U.S.EPA) has set a permissible limit of 0.015 mg/L in drinking water and has placed it on top of the priority list of toxic pollutants [3]. Lead pollution can cause nervous system damage, renal kidney disease, mental retardation, cancer, and anemia in humans [2]. Chemical reduction, ion exchange, chemical precipitation, mineral adsorption, membrane separation, and bio-sorption are the most frequently used treatment technologies for Pb2+ removal [4] which are ex-situ techniques. Most of these methods are only suitable for the removal of Pb2+ in low concentrations and often require extensive processing as well as being too expensive.

Recently, in-situ techniques such as permeable reactive barriers (PRB) have become promising alternatives to ex-situ methods owing to their lower operating costs [5]. Nano zero valent iron particles could be used as reducing agents in PRBs for removing the wide range of pollutions that promises to be significantly more effective than granular iron, the reaction rates are 25 to 30 times faster, and the sorption capacity is much higher compared with granular iron [2].

The high reactivity of nZVI is the consequence of greater total surface area, higher density of reactive sites on the particle surface, and/or more intrinsic reactivity of the surface sites [6]. Iron nano particles have been extensively studied to remediate pollutants such as chlorinated compounds and metal ions [7], nitrate [8], carbon tetrachloride, benzoquinone [9], metalloids such as arsenic [10], and organic compounds [11]. However, there are many uncertainties regarding to the features of nZVI-based remediation technologies, which have made it difficult to engineer applications for optimal performance or to assess the risk to human or ecological health. In this study, application of surface modified nZVI (S-nZVI) for Pb2+ remediation in porous media was experimented that consists of following steps: (1) synthesis, stabilization, and characterization of S-nZVI; (2) determination of kinetics of Pb2+ removal by nZVI and the key factors affecting the reaction; (3) investigation of the effects of flow characteristics on the removal rate; (4) bench-scale modeling of lead remediation under natural conditions.

Methods

Materials

Lead nitrate (Pb(NO3)2), used as the source of Pb2+ in all experiments, and other chemical reagents, including FeCl3.6H2O, NaBH4, and NiCl2.6H2O, were supplied by Merck, Germany. The concentration of lead, divalent and total, was determined using an atomic absorption spectrometer (Varian SpectrAA 220, Germany).

NZVI preparation

The iron nano particles were prepared on-site to prevent more oxidation of nZVI surface. To synthesize the nZVI particles, 0.15 M NaBH4 solution was added slowly with the rate of 1 to 2 mL/min into 0.1 M FeCl3.6H2O aqueous solution at ambient temperature and vigorously stirred at 400 rpm [12]. During this reaction, ferric ions were reduced into black particles by sodium borohydride as the reductant, according to the following reaction [13]:

The black precipitates were filtered by vacuum filtration through 0.45 μm filter papers and then washed with DI water and ethanol three times.

NZVI stabilization

Previous researches have indicated that nZVI particles aggregate quickly, after decreasing surface area for reaction and limiting mobility. To control nano particle agglomeration, various particle stabilizing strategies have been reported that surface modification with surfactant is one of the most important approaches [14]. Surfactants, such as starch, could be coated on existing nZVI particles in a post-synthesis process; or synthesizing nZVI in the presence of polymer in a pre-synthesis process. The post-synthesis stabilization approach has been shown to decrease reactivity whereas the pre-synthesis approach has improved reactivity and significantly increased surface area [15]. In the present study, nZVI was stabilized by starch in a pre-synthesis process, according to He and Zhao method [16], which is termed here as S-nZVI.

Batch experiments

The batch experiments were conducted to find the finest condition for columns tests. In addition, useful information could be obtained about the effect of some key parameters. As listed in Table 1, the effects of several main variables were investigated in batch tests, one parameter changed while others were kept constant. Batch experiments were carried out in sealed flasks at 20°C. Predefined S-nZVI and 125 mL buffered Pb2+ solution with initial concentration of 200 mg/L and pH 4.0 were added to each flask, and the suspension was stirred. Aliquots of the samples were taken at certain time intervals and analyzed immediately following paper filtration. All experiments were conducted in duplicate and the results were averaged.

Table 1

Experimental design in present study* all experiments were conducted in ambient temperature 15–20 °C

Experimental set			Variable parameter						Controlled conditions
Batch		1-1	Controlled pH	2.0	4.0	6.0	8.0		S-nZVI: 0.5 g/L, Co: 200 mg/L
		1-2	Initial Pb2+ (mg/L)	100	200	400	800		S-nZVI: 0.5 g/L, pH: 4.0
		1-3	S-nZVI con.(g/L)	0.1	0.2	0.5	1.0	2.0	Co: 200 mg/L, pH: 4.0
continuous experiments	Transparent column	2-1	Seepage velocity (m/d)	5	10	20	40		Co = 200 mg/L, pH: 4, Seepage velocity: 10 m/d
		2-2	S-nZVI loading (g)	1	2	5	10		nZVI: 5 g, pH: 4, Co = 200 mg/L
	Bench-scale	3-1	Seepage velocity (m/d)	10	20	40			nZVI: 15 g, pH: 4, Co = 200 mg/L

Continuous experiments

Continuous experiments were performed in two configurations:

1 - Transparent column with 55 mm diameter and 650 mm length filled with glass beads (Figure 1);

Figure 1

Picture and schematic of transparent column model filled with glass beads.

2 - bench-scale apparatus consisted of two PVC columns with 300 mm diameter and 1250 mm height filled with packed sand (Figure 2).

Figure 2

Picture of bench-scale model.

Prior to each run, in the first system, glass beads were soaked in hydrogen peroxide solution for 10 hr, washed with de-ionized water, and finally baked at 105°C for 24 hr [17]. For the continuous system, sands were prepared by baking at 500°C for 24 hr to eliminate adsorbed organic matter. In this set of experiments, the pH of the solution was adjusted to 4 ± 0.2 using 0.1 N HCl.

The effects of some flow parameters were investigated by transparent column model, including seepage velocity and S-nZVI loading. Seepage velocity tests, consisted of 5, 10, 20, and 40 m/d, were conducted by distilled water with initial Pb2+ concentrations of 200 mg/L, and 5 g S-nZVI injection. S-nZVI loading tests were experimented by initial Pb2+ concentrations of 200 mg/L, seepage velocity of 10 m/d, and frequent 5, 10, and 15 g S-nZVI injection.

The bench-scale experiments were planned based on the results of the batch and transparent column tests. The S-nZVI injected into the bottom center of the column forms a permeable reactive zone which reduced inlet pb2+. This configuration is applicable to study the effects of groundwater ionic strength, porous media type, seepage velocity, initial concentration of pb2+ and nano particle loading, at the same time. Three treatments, consisted of 5, 10, and 15 g initial S-nZVI loading, were carried out in the bench-scale model. Other conditions were kept as seepage velocity 10 m/d, pH 4, and were used wastewater with initial Pb2+ concentration of 200 mg/L.

Results and discussion

Characteristics of S-nZVI

To characterize the stabilized iron nano particles, X-ray powder diffraction (XRD), scanning electron microscopy (SEM), and dynamic light scattering (DLS) were recorded as the results shown in Figure 3. The starched nZVI particles displayed much less agglomeration than those prepared without a stabilizer while S-nZVI remained suspended in water for several hours, non-starched particles agglomerated and precipitated within minutes. XRD results, obtained by a D8 Advanced Bruker diffractometer, indicated the presence of Fe° (peaked at 2θ = 42, 67, 82), and Fe2O3 (2θ = 35, 53). SEM analyses, by a S4160 FE-SEM device, denoted that the S-nZVI were present as discrete particles as opposed to dendritic flocs for non-starched particles. DLS was performed using a S-red Badge model ZEN1600. The mean particle size was estimated to be 78 nm with a standard deviation of 14 nm, which translated to a surface area of at least 25 m2/g.

Figure 3

Characteristic of synthesized nZVI, (a) XRD diagram, (b) SEM image, (c) DLS results, (d) stabilization status.

a. Effect of solution pH

Generally, pH of solution is an important factor for heavy metal ions removal by nZVI. It is widely accepted that low pH has a negative effect on metal adsorption by nZVI [18]. When pH is lower than zero point charge (pHzpc), the positive charge surface of nZVI will repulse metal cations, and results lower removal efficiency [19]. On the other hand, it is found out from equation 2 that H+ is strongly produced along the Pb2+ reduction reaction that point to an alkaline environment is preferred by the Pb2+ removal in aqueous solution [20].

Figure 4a presents the results of batch experiments in which S-nZVI are exposed to Pb2+ buffered solution with different pH values. At pH <4.0 or >6.0 after 60 min, less than 60% of Pb2+ was degraded, while more than 80% removal efficiency was obtained after 60 min at pH 5 ± 1. The results suggest that rapid reduction of Pb2+ into Pbo occurs while pH < 6, and adsorption was optimized by adjusting the pH > 4. Thus, it can be concluded that pH around 5 favors for Pb2+ removal by nZVI.

Figure 4

Results of Pb removal by experiments in batch, column and bench- scale models.

b. Effect of initial Pbconcentration

As shown in Figure 4b, the effect of initial concentration of Pb2+ on removal efficiency was investigated in the range of 100 to 800 mg/L. The equilibrium time became longer and the final removal efficiency of Pb2+ decreased as the initial Pb2+ concentration increased; So, the percentage of Pb2+ removed within 60 min at an initial concentration of 100 mg/L was nearly 85%, and it was only 58% at an initial concentration of 800 mg/L. Furthermore, as revealed in Figure 5b, the plot well fitted to the pseudo first order adsorption model, where the observed rate constant decreased significantly as the initial Pb2+ concentration increased. Generally, when nZVI concentration was constant, the lower efficiency and slower rate of Pb2+ removal were found at higher initial concentrations of Pb2+.These results suggest that the capacity of the S–nZVI for lead removal is about 430 mg Pb/g S-nZVI.

Figure 5

Pseudo first-order adsorption kinetic plots (corresponding to Figure a, b and c, respectively).

c. Effect of S-nZVI concentration

As shown in Figure 4c, the Pb2+ removal efficiency improved as the S-nZVI concentration increased. The removal efficiency of Pb2+ was about 50% using S-nZVI at 0.1 g/L for 60 min, but was nearly 95% when the S-nZVI concentration was higher than 1 g/L. In the same conditions, Kobs raised as the S-nZVI concentration increased. These phenomena can be attributed to the increase in available active sites resulting from the increase in S-nZVI concentration, where the lead reduction occurred. Additionally, lead ions removal sharply enhanced by increasing contact time for the first 60 min, and then gradually approached equilibrium after approximately 120 min.

d. Kinetics of the Pbreduction

The adsorption kinetics of Pb2+ ions was studied to determine the required time to achieve equilibrium adsorption of lead ions on the adsorbents. It was reported that nZVI can remove metal ions from aqueous solutions by various mechanisms, including electrostatic adsorption, complex formation, reduction, and precipitation [21]. It seems that when nZVI was used, the nano particles captured aqueous lead ions easily and rapidly because of their large surface areas and high reactivity.

In this research, the kinetics was investigated experimentally under different values of initial Pb2+ concentration, solution pH, and S-nZVI dosage by using pseudo first-order reaction model that can be represented as following:

where C and C are the concentration of Pb2+ (mg/g) at initial and time t (min), respectively. K (min−1) is the equilibrium rate constant for first order adsorption. Therefore, by plotting ln(C/C) against t, the values of K can be found from the slope of the revealed plots.

Several studies have investigated the kinetic of Pb2+ removal by nZVI. Among a number of kinetic models, such as pseudo zero-order, pseudo first-order and pseudo second-order kinetic models, the pseudo first-order kinetic model was the most suitable which approves the best fit with the experimental data of Pb2+ removal compared to the rest of models [2]. As seen in Figure 5, the experimental data were well fitted to the pseudo first-order adsorption model with the high correlation coefficients. The parameters obtained by linear regression analysis were offered in Table 2. The results indicated a decrease in K values from 0.04 to 0.01 g/mg/min, when initial Pb2+ concentration increased from 100 to 800 mg/L. The rate constant K also increased by increasing S-nZVI dosage, and by approaching to a solution pH of 5.

Table 2

Pseudo first-order adsorption kinetics constants for Pb removal by S-nZVI

Parameters	pH: 2.0	4.0	6.0	8.0
Kobs (1/min)	−0.015	−0.024	−0.022	−0.011
R2	1.0	0.999	0.998	0.991
Fixed conditions: Initial Pb2+ 200 mg/L, S-nZVI 0.5 g/L
Parameter	Initial Pb 2+ : 100 mg/ L	200	400	800
Kobs (1/min)	−0.035	−0.023	−0.011	−0.012
R2	0.999	0.999	0.999	0.997
Fixed conditions: S-nZVI 0.5 g/L, pH 4.0,
Parameter	S-nZVI:0.1 g/ L	0.25	0.5	1.0	2.0
Kobs (1/min)	−0.012	−0.020	−0.024	−0.033	−0.026
R2	0.999	0.981	0.999	1.0	1.0
Fixed conditions: Initial Pb2+ 200 mg/L, pH 4.0,

e. Adsorption isotherms

Experimental data were modeled using the well known adsorption models described by the Freundlich and Langmuir equations to study the ability of Pb2+ ions to adsorb on S-nZVI [22].

Based on the results of our experimental data fitting on these isotherms, in Table 3, nZVI has the good ability to reduce Pb2+ to Pbo which can then be absorbed by the nZVI easily. Furthermore, data fitting by using the Langmuir model give a better fit than by using the Freundlich model. This can be seen from the fitting data obtained that the correlation coefficient is higher for the Langmuir adsorption isotherm (~0.92) compared to that of the Freundlich model (~0.84).

Table 3

Freundlich and Langmuir adsorption isotherms constants for Pb removal by S-nZVI

Parameters	pH:2.0		4.0	6.0	8.0
Freundlich	1/n	−0.51	−0.18	−0.21	−0.65
	Kn	1996	571	629	3662
Langmuir	qmax	0.14	0.24	0.23	0.12
	Kl	0.05	0.21	0.16	0.04
Fixed conditions: Initial Pb2+ 200 mg/L, S-nZVI 0.2 g/L
Parameter		Initial Pb 2+: 100 mg/L	200	400	800
Freundlich	1/n	−0.11	−0.17	−0.45	−0.67
	Kn	208	564	4615	43143
Langmuir	qmax	0.13	0.24	0.33	0.50
	Kl	0.71	0.20	0.03	0.01
Fixed conditions: S-nZVI 0.2 g/L, pH 4.0,
Parameter		S-nZVI:0.1 g/L	0.25	0.5	1.0	2.0
Freundlich	1/n	−0.85	−0.39	−0.18	−0.05	−0.03
	Kn	43228	2335	571	204	38
Langmuir	qmax	0.42	0.29	0.24	0.16	0.09
	Kl	0.02	0.06	0.21	1.43	2.83
Fixed conditions: Initial Pb2+ 200 mg/L, pH 4.0,

Transparent column

a. Effect of seepage velocity

The results of seepage velocity tests are shown in Figure 4c. It was observed that a seepage velocity of 10 m/d yielded the maximum removal rate. Furthermore, any variation, increasing or decreasing of this velocity, had a negative effect on the Pb2+ removal. Higher seepage velocities enhanced the mobility of nano particles through porous media and reduced the contact time and as a result, reduced the remediation efficiency.

b. Effect of S-nZVI loading

As shown in Figure 4e, when S-nZVI loading rose from 1 to 10 g, the Pb2+ removal efficiency within 60 min increased from about 50% to 80%. It is found out that when further amount of S-nZVI was injected, the Pb2+ removal has been improved.

Bench-scale model

The results of bench-scale experiments, illustrated in Figure 4f, indicated that the removal efficiency through sand materials were higher than glass beads. In addition, increasing seepage velocity had a decreasing effect on the Pb2+ remediation. Through bench-scale experiments, the best Pb2+ remediation efficiency was achieved, i.e. about 81%. In pH of 4, initial concentration of 200 mg/L, and 15 g S-nZVI injection, finally 31 L of treated water with Pb2+ concentration less than 20 mg/L was acquired. Therefore, it could be proposed that the capacity of S-nZVI for in-situ lead removal is about 300 mg Pb2+/g S-nZVI.

Conclusions

Findings of this study indicated that starched nZVI has a good feasibility for in-situ lead remediation in contaminated water. Batch experiments proved that pH of solution was an important parameter while kinetics coefficients were directly related to pH with correlation coefficients R2 > 0.90. In addition, increasing of S-nZVI dosage or decreasing Pb2+ initial concentration, both lead to enhancement in removal efficiency. It means that if mass-ratio between nZVI and Pb is kept constant, i.e. about 2.5, the removal rate would be invariable.

Transparent column experiments revealed that Pb2+ remediation also was mostly influenced by seepage velocity, grain size, and type of porous media. Bench-scale results confirmed the batch and transparent column outcomes. As a final point, because of the fast reaction kinetics and high Pb2+ removal capacity, S-nZVI has the fine potential to become an effective remedial agent in PRB for in-situ immobilization of lead in polluted groundwater resources.