The Effect of Regeneration Conditions on the Properties of CeO2 Desulfurization Sorbent in SO2 Atmosphere

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CeO2 desulfurization sorbent was prepared by calcination of Ce(NO3)3 ● 6H2O and the effect of regeneration conditions on its properties in SO2 atmosphere was investigated in a fixed bed reactor. The regeneration conversion and the yield of elemental sulfur for CeO2 desulfurization sorbent were tested and calculated. And the composition and the morphology of CeO2 desulfurization sorbent before and after regeneration were obtained by X-ray diffraction and scanning electron microscope. It was found that the main components of the regeneration products of Ce2O desulfurization sorbent were solid CeO2 and gaseous elemental S in SO2 atmosphere. The optimum regeneration condition of CeO2 desulfurization sorbent is that the regeneration temperature of 750 °C and the SO2 concentration of 4.25 %, under which the CeO2 desulfurization sorbent shows the higher regeneration conversion of 96 % and the yield of elemental sulfur of 68.95 wt. %.

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155-161

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March 2017

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© 2017 Trans Tech Publications Ltd. All Rights Reserved

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[1] H. Liu, W. Ni, Z. Li, et al. Strategic thinking on IGCC development in China, J. Energy policy. 36(2008) 1-11.

Google Scholar

[2] N. Ikenaga, Y. Ohgaito, H. Matsushima, et al. Preparation of zinc ferrite in the presence of carbonmaterial and its application to hot-gas cleaning, J. Fuel. 83 (2004) 661-669.

DOI: 10.1016/j.fuel.2003.08.019

Google Scholar

[3] N. K. Park, D. H. Lee, J. H. Jun, et al. Two-stage desulfurization process for hot gas ultra cleanup in IGCC, J. Fuel. 85 (2006) 227-234.

DOI: 10.1016/j.fuel.2005.04.033

Google Scholar

[4] W. J. W. Bakker, F. Kapteijn, J. A. Moulijn. A high capacity manganese-based sorbent for regenerative high temperature desulfurization with direct sulfur production: Conceptual process application to coal gas cleaning, J. Chemical Engineering Journal. 96 ( 2003) 223-235.

DOI: 10.1016/j.cej.2003.08.022

Google Scholar

[5] D. Y. Choi, J. W. Lee, S. C. Jang, et al. Adsorption dynamics of hydrogen sulfide in impregnated activated carbon bed, J. Adsorption. 14 (2008) 533-538.

DOI: 10.1007/s10450-008-9118-9

Google Scholar

[6] W. Xie, L. Chang, D. Wang, et al. Removal of sulfur at high temperatures using iron-based sorbents supported on fine coal ash, J. Fuel. 89 (2010) 868-873.

DOI: 10.1016/j.fuel.2009.01.006

Google Scholar

[7] R. B. Slimane, J. Abbasian. Utilization of metal oxide-containing waste materials for hot coal gas desulfurization, J. Fuel Processing Technology. 70 (2001) 97-113.

DOI: 10.1016/s0378-3820(00)00148-x

Google Scholar

[8] B. Guo, L. Chang, K. Xie. Desulfurization Behavior of Cerium–Iron Mixed Metal Oxide Sorbent in Hot Coal Gas, J. Industrial & Engineering Chemistry Research. 53 (2014) 8874-8880.

DOI: 10.1021/ie500752n

Google Scholar

[9] J. Zhang , Y. Wang, R. Ma, et al. A study on regeneration of Mn–Fe–Zn–O supported upon γ-Al2O3 sorbents for hot gas desulfurization, J. Fuel Processing Technology. 84 (2003) 217-227.

DOI: 10.1016/s0378-3820(03)00057-2

Google Scholar

[10] Y. Zeng, S. Kaytakoglu, D. P. Harrison. Reduced cerium oxide as an efficient and durable high temperature desulfurization sorbent, J. Chemical Engineering Science. 55 (2000) 4893-4900.

DOI: 10.1016/s0009-2509(00)00117-2

Google Scholar

[11] J. Mi, M. Yu, F. Yuan, et al. Regeneration characteristics and kinetics of modified semi-coke supported (Fe, Zn, Ce) desulfurization sorbents, J. Energy & Fuels. 26 (2012) 6551-6558.

DOI: 10.1021/ef301222c

Google Scholar