Removal mechanisms of cadmium and lead ions in contaminated water by stainless steel slag obtained from scrap metal recycling

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Abstract

In this work, steel slag was shown to be a successful filter material for the removal of lead and cadmium from natural waters with a removal efficiency of >95 %, even under acidic conditions (pH 3.5). Overall, precipitation was found to be the main removal mechanism over adsorption with a tight relationship with the final matrix pH. Batch experiments showed fast removal kinetics with >98 % removal efficiency for lead and cadmium in 5 and 15 min, respectively. The removal kinetics followed a pseudo second-order reaction (R2 = 0.999), and the K2 was calculated to be 927 h−1 and 204 h−1 for lead and cadmium, respectively. A strong interference for the removal was observed with ethylenediaminetetraacetic acid (EDTA) but slightly with fulvic and humic acids, and non-significant with polymeric acid e.g. isosaccharinic acid. In addition, the column experiment showed spontaneous removal kinetics for lead and cadmium with a contact time of 3.6–36 seconds depending on loading flow-rates. Column experiments at similar liquid to solid ratios showed a high removal capacity with gradient over isocratic solution loading. The high removal efficiencies in combination with limited hazardous metals leaching led to the conclusion that slag is an appropriate filter material for treating contaminated waters. Moreover, the slag treated solutions with alkaline conditions showed reacted efficiently with CO2 in flue gas. Consequently, the pH of the treated solution is neutralized making it easier to waste and this reaction may contribute to reducing CO2 gas emissions.

Introduction

Cadmium and lead contamination are considered serious threats to the environment and human health due to their high toxicity and persistent characteristics [1]. They enter the food chain mainly through crop irrigation and soil contamination [2]. According to the World Health Organization (WHO), inorganic lead and cadmium compounds have been placed in Group 2A and are described as probable human carcinogens with a recommended maximum concentration of 10 μg L−1 and 3 μg L−1 in drinking water, respectively [3]. Exceedingly high lead and cadmium exposure can cause bone degeneration, liver damage, lung insufficiency, hypertension, and renal dysfunction in humans. Human exposure is mainly through consuming contaminated food and drinking water [4,5]. Industrial activities such as mining, electroplating, pigment manufacturing, metallurgy and agricultural activities increase the flux of heavy metals to local water bodies. More attention has been paid to reduce the concentrations of the dissolved metals in sewage, industrial, and mining wastes [6,7]. Several removal approaches have been proposed, among those adsorption and precipitation are considered to be the most suitable methods [[8], [9], [10], [11]]. Costs for treating contaminated water by synthesized materials are typically high, thus limiting their application on larger scales. Therefore, a robust, cheap and efficient method for removing the toxic metals is essential to mitigate the risk for society.

Currently, global crude steel production is around 1808 million tons per year (2018 estimate) [12]. Steel slag, a byproduct of steel manufacturing, makes up approximately 15 % by mass of the steel output, giving approx. 270 million tons produced per year [13,14]. Currently, use of the slag is limited. The majority is disposed of in landfills which occupy massive land areas and potentially pollute the environment [15]. Steel slag is mainly composed of the oxides of calcium, silicon, aluminum and iron, giving it very strong alkaline properties as well as a high adsorption and precipitation capacity. It has been reported that steel-making slag can be used as adsorbent for the removal of heavy metals and various contaminants [[16], [17], [18], [19]]. Few studies have reported the use of steel slag as adsorbent for treating lead and cadmium contamination [[20], [21], [22]]. However, steel slag is a complex system of oxides and typically has low specific surface area and poor pore structure caused by crystallization, limiting its adsorption efficiency [21]. A modified steel slag showed a sorption capacity for cadmium of 10 mg g−1 (25 °C) [21] whereas other materials like iron oxide activated red mud was only 0.12 mg g−1 [23]. The reported sorption capacities of lead by iron oxide nanoparticles and iron-coated filters were 36 mg g−1 [24] and 1.2 mg g−1 [25], respectively. A study on the removal of copper in contaminated water by steel slag indicated that the removal is a result of both adsorption and precipitation [26]. Adsorbents were shown to be effective for treating wastewater containing a low heavy metal concentration while precipitation with lime (CaO) has been found as one of the most effective method for treating extremely contaminated solutions (>1000 mg L−1) [27].

In this study, the in situ removal of lead and cadmium by slag filled filtration columns was examined in order to assess the efficiency of using slag as a filter material for contaminated water treatment. The stainless steel slag in our study was obtained from scrap metal recycling which is considered environmentally friendly because it requires limited mining activities. Heavy metal removal efficiency by slag was tested under various conditions including pH, competition of ligands and liquid to solid ratios, and by the slag column with different solution loading flow-rates. Isotherm and kinetics for the heavy metal removal were investigated with these tests, and the contribution of adsorption and precipitation to the removal were examined. A natural water sample spiked with lead and cadmium was used to test the application of the slag material in heavy metals filtration. Ultimately, it was found that steel slag is a successful filter material for the removal of lead and cadmium from natural water with a removal efficiency of >95%.

Section snippets

Materials

Cadmium and lead stock solutions were prepared by dissolving Cd(NO3)2.4H2O and Pb(NO3)2 (98%, Sigma Aldrich) in deionized water (18.2 MΩ). Concentrations of the prepared stock solutions were confirmed by comparison with 1.0 g L−1 commercial standards solutions (Perkin Elmer). Nitric acid (HNO3) from Merck was purified in house by sub-boil distillation (35 °C) prior to use. Hydrochloric acid (HCl, 30 %) and ethylenediaminetetraacetic acid (EDTA) were purchased from Fisher Scientific. Aquatic

Properties of the slag

The slag has a BET specific surface area of 4.24 m2 g−1, micropore area: 0.3448 m²/g, volume of pores between 1.7 nm and 300 nm diameter of 0.023289 cm³/g and a total void volume of 0.42 cm3 g-1 in the filled column without pressing. The elemental composition of the slag is summarized in Table 1 with calcium as the major component, accounting for about 33% of the composition by weight, followed by Mg, Al, and Si (about 4% each). By recalculating calcium as its simplest oxide, CaO, its weight

Conclusion

A cheap and efficient method for the removal of lead and cadmium in water has been successfully established. Precipitation was the main process for the removal with an important role of pHfin. Strong complexing ligands to lead and cadmium, like EDTA, strongly interfered with the removal while the affect is minor for weaker ligands such as ISA, fulvic and humic acids. In batch experiments, the removal capacity of lead and cadmium reach was most efficient at an L/S ratio of 2000. In the column

Declaration of Competing Interest

The authors declare that they have no known competing financial interests or personal relationships that could have appeared to influence the work reported in this paper.

Acknowledgements

The financial support from the Ton Duc Thang University, Ho Chi Minh City, Viet Nam, the EnForce profile (KKS, The Knowledge Foundation), and the Örebro University, Sweden. Viktor Sjöberg and Stefan Karlsson, Örebro University, are greatly acknowledged for SEM and EDS measurements.

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