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Poster Session, Tuesday, June 15<br />

Theme A1 - B702<br />

Mercury (II) removal from Aqueous Solution by Us<strong>in</strong>g Modified Ordered Mesoporous Carbon<br />

Nuran Böke 1,2 , Ziboneni Godongwana 1 , Leslie Petrik 1 *<br />

1 Department of Chemistry, University of the Western Cape, Cape Town 7535, South Africa<br />

2 Department of Chemical Eng<strong>in</strong>eer<strong>in</strong>g, Ege University 35100, Turkey<br />

Abstract- Modified mesoporous carbon (MOMC) was applied to remove Hg (II) from contam<strong>in</strong>ated model aqueous solutions. Batch adsorption<br />

experiments were carried out to evaluate the adsorption behaviour of Hg (II) onto MOMC. The Langmuir adsorption model fitted to the<br />

experimental data with a regression coefficient of R 2 =0.9796.<br />

Ordered mesoporous carbons (OMC) exhibit both well –<br />

ordered mesoporosity and graphitic character. Because of their<br />

regular pore size and pore shape and also large surface area,<br />

these materials have great potential <strong>in</strong> environmental<br />

processes. But <strong>in</strong> some processes, such as adsorption, the<br />

material must have some additional specifications such as<br />

b<strong>in</strong>d<strong>in</strong>g sites. In this study we prepared an modified OMC<br />

(MOMC) which has functional groups for Hg (II) b <strong>in</strong>d<strong>in</strong>g and<br />

used it <strong>in</strong> adsorption of Hg (II) from model contam<strong>in</strong>ated<br />

aqueous solutions.<br />

In the first stage of the work SBA-15 was synthesized by<br />

us<strong>in</strong>g a triblock copolymer (P123) [1]. OMC materials have<br />

been synthesized us<strong>in</strong>g SBA-15 as ordered mesoporous silica<br />

template. Chemical vapour deposition (CVD) was applied<br />

us<strong>in</strong>g liquid petroleum gas (LPG) as the carbon source as a<br />

rapid and simple route to prepare OMC [2]. LPG <strong>in</strong>filtrated<br />

the mesoporous silica template, and thermally decomposed to<br />

form a structurally robust, ordered mesoporous carbon<br />

material analogous to SBA-15 after removal of the silica<br />

template.<br />

In an effort to enhance mercury removal from the aqueous<br />

solution, OMC was modified by a comb<strong>in</strong>ed treatment of<br />

nitric acid and (3-mercaptopropyl) triethoxysilane to <strong>in</strong>troduce<br />

sulphur conta<strong>in</strong><strong>in</strong>g functional groups <strong>in</strong>to the structure of<br />

mesoporous carbon [3].<br />

Batch adsorption test were done for adsorption of<br />

mercury(II) onto MOMC. 10 mg adsorbent and 50 mL of<br />

Hg(II) solution with the desired concentration at pH=5.5<br />

placed <strong>in</strong>to the capped flasks [4]. Duplicates for each<br />

concentration were placed <strong>in</strong> a shaker at 25 o C.<br />

After a predeterm<strong>in</strong>ed time of shak<strong>in</strong>g the solid adsorbent<br />

and liquid were separated by filtration through a filter paper.<br />

Filtered solutions collected <strong>in</strong> capped bottles. These solutions<br />

were diluted <strong>in</strong> 100 mL volumetric flasks to adjust the<br />

concentrations of them <strong>in</strong>to the measurement range of the<br />

UV/VIS spectrophotometer. For measur<strong>in</strong>g Hg(II)<br />

concentration of the samples and standard solutions the<br />

method given by Ramakirishna et al. was followed [5]. In this<br />

method Hg(II) is determ<strong>in</strong>ed as ternary complex with<br />

rhodam<strong>in</strong>e 6G and iodide.<br />

The adsorption isotherm of Hg(II) removal by MOMC is<br />

shown <strong>in</strong> Figure 1 as dots.<br />

The Langmuir isotherm model was applied to analyze the<br />

adsorption equilibriu m of Hg (II) on M OMC[6].<br />

and rate of adsorption, respectively. The l<strong>in</strong>ear plot of C e /Q e<br />

versus C e showed that the adsorption follows the Langmuir<br />

isotherm model for Hg (II) adsorption. The values of Q o and b<br />

were calculated from the slope and <strong>in</strong>tercept of the plot, and<br />

the values obta<strong>in</strong>ed were Q o =250 mg/g and b=0.0386 L/mg,<br />

respectively. Us<strong>in</strong>g Q o and b values the Langmuir isotherm<br />

was obta<strong>in</strong>ed. The Langmuir isotherm can be seen <strong>in</strong> Fig. 1 as<br />

a cont<strong>in</strong>uous curve.<br />

Figure 1. Adsorption isotherms of Hg(II) removal by MOMC. Ce :<br />

equilibrium Hg(II) concentration, Qe: amount of Hg(II) adsorbed at<br />

equilibr ium time<br />

In summary, adsorption of Hg (II) could be described by<br />

Langmuir model, (regression coefficient R 2 =0.9796). The<br />

Langmuir isotherm constants were found as Q o =250 mg/g and<br />

b=0.0386 L/mg, respectively.<br />

*Correspond<strong>in</strong>g author: 1Tlpetrik@uwc.ac.za<br />

[1] J. Parmentier et al., J Phys. and Chem. of Solids 65 139–146<br />

(2004).<br />

[2] P. Ndungu et al., Microporous and Mesoporous Materials 116<br />

593–600 (2008).<br />

[3] A. Walcarius, Analytica Chim. Acta 508 87–98(2004).<br />

[4] Chemosphere 52 835–841 (2003).<br />

[5] T.V. Ramakirishna et al., Anal. Chim. Acta 84 369-375 (1976).<br />

[6] K. Kadirvelu et al., Carbon 42 745–752 (2004).<br />

C e /Q e = C e /Q o + (1/b* Q o )<br />

[1]<br />

where, C e is the equilibriu m concentration (mg/L) and Q e is<br />

the amount of Hg(II) adsorbed (mg/g) at equilibriu m time. Qo<br />

and b are Langmuir constants related to adsorption capacity<br />

6th Nanoscience and Nanotechnology Conference, zmir, 2010 340

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