4.7 Article

Thiophene-functional hierarchical carbons for the removal of ionic and organic mercury in light hydrocarbon liquids: Synthesis, evaluation and adsorption mechanism

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DOI: 10.1016/j.seppur.2022.120754

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Thiophene; Zeolite templated carbon; Ionic mercury; Organic mercury; Gasoline

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This study proposes a simple method for synthesizing thiophene-functional zeolite-templated carbons to remove mercury from gasoline. The effects of template type and impregnation concentration on the quality of the templated carbon were investigated. The results show that thiophene-functional zeolite-templated carbons with proper impregnation concentration exhibit excellent adsorption capacity and regeneration ability.
A simple synthesis of thiophene-functional zeolite-templated carbons (ZTCs) is proposed to remove ionic mer-cury (Hg2+) and organic mercury (Hgorg) from gasoline. Microporous zeolite (Beta) and mesoporous zeolite (MCM-41) were used to prepare porous carbon by impregnating with 2-thiophenemethanol (ThM) to explore the influence of template type on the quality of templated carbon. The amount of strong acidic sites in MCM-41 zeolite was more than Beta zeolite which promoted the catalytic polymerisation of the ThM in the pores structure of the zeolite and highly templated carbon was obtained. The impregnation concentration of ThM on the structure and functional groups of the samples was explored. It was found that increasing the concentration of ThM properly can promote the filling of zeolite pores by ThM and form more ordered templated carbons. In addition, the increased ThM promoted the formation of the S = O and C-O oxygen-containing functional groups. The optimal impregnation concentrations of ThM were 25% for B-Al (25%-B-Al-ZTC) and 75% for M-Al (75%-M- Al- ZTC). The 75%-M-Al-ZTC with sufficient S = O and C-O oxygen-containing functional groups showed excellent mercury adsorption capacity (617.49 mu g/g) and a high intra-particle diffusion rate (294.10 h-1). The simultaneous adsorption of Hg2+ and Hgorg was also conducted and it was found that Hgorg had competitive adsorption for Hg2+ which led the total adsorption capacity to decrease. In addition, the 25%-B-Al-ZTC and 75%-M- Al- ZTC adsorbents had good regeneration ability and the adsorption capacity remained over 75% and 71% for Hg2+ and Hgorg after five desorption-sorption cycles, respectively. Thus, the new adsorbents with stable and efficient Hg removal performance have the potential for practical application by oil refineries.

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