IRON OXIDES FROM ELECTROFILTER ASH FOR WATER TREATMENT (ARSENIC REMOVAL)

2009 ◽  
Vol 8 (4) ◽  
pp. 895-900 ◽  
Author(s):  
Ionel Balcu ◽  
Adina Segneanu ◽  
Marius Mirica ◽  
Mirela Iorga ◽  
Catalin Badea ◽  
...  
2016 ◽  
Vol 11 (4) ◽  
pp. 702-711 ◽  
Author(s):  
Collivignarelli Maria Cristina ◽  
Canato Matteo ◽  
Sorlini Sabrina ◽  
Crotti Barbara Marianna

Many water treatment plants (WTPs) were designed to remove ammonia, iron, and manganese simultaneously using biofilters. In some cases (especially in the Pianura Padana area, in Italy) such plants were designed without a specific treatment stage for arsenic removal because its concentration in the groundwater (i.e. 10 to 20 μg/L) was lower than the previous maximum contaminant level (MCL) of 50 μg-As/L; therefore, specific treatments for arsenic removal must be introduced or upgraded in WTPs. In this work, the results of a 19-month monitoring campaign are reported for a pilot granular ferric oxide (GFO) filter installed in an Italian WTP as a polishing stage. The aim was to investigate the performance of GFO with low arsenic concentrations. The results show that, if the groundwater arsenic concentration is close to the MCL, GFO treatment can be cost effective (approximately 80,000 bed volumes have been treated). It was confirmed that GFO can be effective for the removal of both As(III) and As(V) species.


2019 ◽  
Vol 20 (7) ◽  
pp. 1609 ◽  
Author(s):  
Vasile Mînzatu ◽  
Corneliu-Mircea Davidescu ◽  
Petru Negrea ◽  
Mihaela Ciopec ◽  
Cornelia Muntean ◽  
...  

The aim of this paper was to produce a new composite material based on carbon and iron oxides, starting from soluble starch and ferric chloride. The composite material was synthesized by simple thermal decomposition of a reaction mass obtained from starch and iron chloride, in an inert atmosphere. Starch used as a carbon source also efficiently stabilizes the iron oxides particles obtained during the thermal decomposition. The reaction mass used for the thermal decomposition was obtained by simultaneously mixing the carbon and iron oxide precursors, without addition of any precipitation agent. The proper composite material can be obtained by rigorously adhering to the stirring time, temperature, and water quantity used during the preparation of the reaction mass, as well as the thermal regime and the controlled atmosphere used during the thermal decomposition. Synthesized materials were characterized using thermogravimetric analysis, X-Ray Diffraction (XRD), scanning electron microscopy (SEM), and Fourier transform infra-red spectroscopy (FT-IR). The performances of the obtained material were highlighted by studying their adsorbent properties and by determining the maximum adsorption capacity for arsenic removal from aqueous solutions.


2012 ◽  
Vol 46 (21) ◽  
pp. 11702-11709 ◽  
Author(s):  
Giridhar Upadhyaya ◽  
Tara M. Clancy ◽  
Jess Brown ◽  
Kim F. Hayes ◽  
Lutgarde Raskin

2020 ◽  
Author(s):  
Elvis Eugene ◽  
William Phillip ◽  
Alexander Dowling

The scarcity of potable water is an imminent threat to at least half the world's population. Engineered nanomaterials (ENMs) have the potential to treat water from polluted sources to mitigate the scarcity of potable water. However, the performance demands on these materials in practical applications has not been studied in detail. This is but one of the challenges that hinder the widespread implementation of ENMs for water treatment. The emerging fit-for-purpose paradigm which encourages water treatment at the point-of-use (POU) or point-of-entry (POE) could lower the barrier for the use of ENMs in water technology by incorporating smaller, decentralized ENM-based treatment systems. This work develops a bottom-up and top-down modeling framework to facilitate the design of nanoporous membrane-based sorbents, a promising class of ENMs, for POU and POE water treatment applications. Langmuir isotherm and membrane structure-property calculations provide the multiscale link between molecular properties, including affinity, saturation capacity, and pore size, device design decisions, including membrane area and thickness, and system design decisions, including sorbent mass and number of parallel modules. The framework predicts that for lead contaminants, existing materials are near molecular and systems limitations; improvements in the properties of adsorptive materials to treat lead will yield few benefits for POU and POE treatment systems. Moreover, the framework provides dimensionless formulas that apply to all adsorptive systems that exhibit (near) equilibrium behavior as an easy-to-use tool for the broader membrane science and environmental engineering communities to assess the feasibility of emerging materials to meet process demands. A case study regarding materials for arsenic removal demonstrates how to apply the modeling framework to calculate material properties targets and predict system performance for an arbitrary single-solute adsorption process. Finally, these dimensionless models are used to identify three distinct regions of relative performance between batch and semi-continuous processes. These results give caution to applying scale-up heuristics outside their valid region, which can lead to under- or over-design during bottom-up studies. The presented modeling framework is a crucial step to fully optimize engineered nanomaterials across material, device, and system scales.


2019 ◽  
Vol 25 (5) ◽  
pp. 735-741
Author(s):  
Yong-Jun Jung ◽  
Yuki Kamimoto

As(V) removal properties of manganese dioxides which are commonly used for the removal of manganese in water treatment processes were evaluated in this paper. The following manganese dioxides were used: two types of powdered manganese dioxides powdered or electrolyzed MnO<sub>2</sub> (g-structure) and calcined MnO<sub>2</sub> (b-structure), and a granular MnO<sub>2</sub>, which was prepared by coating MnO<sub>2</sub> onto a ceramic particle. The maximum arsenate adsorption capacity of the electrolyzed and calcined MnO<sub>2</sub> was 2.22 and 2.26 mg-As g<sup>-1</sup>, respectively. The adsorption capacity of the granular MnO<sub>2</sub> was 0.543 mg-As g<sup>-1</sup> and this value corresponded to the MnO<sub>2</sub> content (23.2%) of the granular adsorbent. When an arsenate solution of 0.1 mg-As L<sup>-1</sup> was fed into the column (10 mm i.d.; 100 mm long) packed with the granular MnO<sub>2</sub> at SV = 20 h<sup>-1</sup>, the column received 28.9 L of the feed solution (3,580 times the bed volume) before the breakthrough point (0.01 mg-As L<sup>-1</sup>). The adsorption isotherms for the electrolyzed and granular MnO<sub>2</sub> were approximated by the modified Langmuir equations. On the other hand, the adsorption isotherm for the calcined MnO<sub>2</sub> was approximated by the Freundlich equation. Based on the adsorption isotherms, the As(V) adsorption amounts at 0.01 mg-As L<sup>-1</sup> of the equilibrium concentration were evaluated as follows: 1.27 mg-As g<sup>-1</sup> for the electrolyzed MnO<sub>2</sub>, 1.20 mg-As g<sup>-1</sup> for the calcined one, and 0.29 mg-As g<sup>-1</sup> for the granular one. Since granular MnO<sub>2</sub> has been commonly used for the removal of manganese from water treatment systems, the process can be also applied to arsenate removal.


1995 ◽  
Vol 87 (4) ◽  
pp. 105-113 ◽  
Author(s):  
Laurie S. McNeill ◽  
Marc Edwards

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