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2003
DOI: 10.1021/es0346431
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Arsenic Removal Using Mesoporous Alumina Prepared via a Templating Method

Abstract: The health threat of arsenic is well-known, and the U.S. EPA recommends the maximum contaminant level to be 0.01 ppm or less for arsenic in drinking water. Therefore, advanced treatment processes are needed for finished water to meet the required regulations. Adsorption is considered to be a less expensive procedure that is safer to handle than precipitation, ion exchange, and membrane filtration. Activated alumina (AA) is the most commonly used adsorbent for the removal of arsenic from aqueous solutions. Howe… Show more

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Cited by 610 publications
(360 citation statements)
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References 39 publications
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“…coefft (R 2 ), b, and Q0 of 0.99, 18.59 L mmol -1 , and 2.00 mmol g -1 , respectively, indicating that adsorption of As(V) onto Fe-Ce08 obeys the Langmuir isotherm model at the given range of As(V) concentration. It is clear that the Q0 (2.00 mmol g -1 ) of FeCe08 was significantly higher than those of the two referenced materials (0.35 mmol g -1 for the Fe oxide and 0.45 mmol g -1 for the Ce oxide), the iron hydroxides, and some other arsenate adsorbents reported recently (24)(25)(26)(27)(28)(29)(30). In the next section, the differences in adsorption performance will be discussed in relation to the differences in structures between the Fe-Ce adsorbent and its referenced oxide materials.…”
Section: Resultsmentioning
confidence: 84%
“…coefft (R 2 ), b, and Q0 of 0.99, 18.59 L mmol -1 , and 2.00 mmol g -1 , respectively, indicating that adsorption of As(V) onto Fe-Ce08 obeys the Langmuir isotherm model at the given range of As(V) concentration. It is clear that the Q0 (2.00 mmol g -1 ) of FeCe08 was significantly higher than those of the two referenced materials (0.35 mmol g -1 for the Fe oxide and 0.45 mmol g -1 for the Ce oxide), the iron hydroxides, and some other arsenate adsorbents reported recently (24)(25)(26)(27)(28)(29)(30). In the next section, the differences in adsorption performance will be discussed in relation to the differences in structures between the Fe-Ce adsorbent and its referenced oxide materials.…”
Section: Resultsmentioning
confidence: 84%
“…The determination of surface morphological characteristics of the used MgO by the BET method showed a specific surface area of 59 m 2 /g, a pore volume 0.14 mL/g and a mean pore diameter 156Å. The large pore size of MgO allows arsenate ions to diffuse into the pore channel of the mesoporous material with relevant convenience, since their radius is significantly smaller (H 2 AsO 4 − : 4.16Å, HAsO 4 2− : 3.97Å) [35] than the corresponding of MgO. Therefore, arsenic can potentially be initially adsorbed onto the surface of the MgO and when the exterior surface reached saturation it can enter into the pores and bind to the interior surfaces of the particles.…”
Section: Surface Characterizationmentioning
confidence: 99%
“…Arsenic exists in natural water predominantly as inorganic arsenate, As (V) and arsenite, As (III) [3][4][5][6][7]. Elevated concentrations of arsenic are found in groundwater in many regions around the world, which are caused by the release of arsenic from As-bearing sediments or anthropogenic sources [8][9][10].…”
Section: Introductionmentioning
confidence: 99%
“…Natural materials such as zeolite [11], natural iron ores [7,12,13], siderite [14] and red mud [15] have been examined intensively for arsenic removal. Although these materials are regarded as cheap and effective adsorbents, there are several problems (their impurities, unknown stability and regeneration, low adsorption capacity and slow kinetics) associated with their use [4,13,16]. An ideal adsorbent should have suitable particle size or uniformly accessible pores, high surface area, and physical and/or chemical stability [4].…”
Section: Introductionmentioning
confidence: 99%
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