Characteristics and Regeneration Properties of Manganese Oxide Sorbent under O2 Atmosphere

Article Preview

Abstract:

The regeneration behavior of manganese oxide sorbent under O2 atmosphere was investigated in a fixed bed micro-reactor under the influence of different temperatures and O2 concentrations. The change in phase of the sulfided and the regenerated sorbents was analyzed by X-ray photoelectron spectroscopy (XPS) and X-ray diffraction (XRD) techniques. MnS, Mn3O4 and MnSO4 were found in regenerated sorbent at 400 °C, which indicated that the regeneration of the sulfided sorbent was not complete, however, MnS was converted to Mn3O4, Mn2O3 and few MnSO4 at 800 °C. The manganese sulfate formed during the regeneration but decomposed to Mn2O3 at 800 °C. MnS reacts with O2 to form Mn3O4 and MnSO4, and then MnSO4 was decomposed at 800 °C. The results show that the optimum regeneration temperature and O2 concentration obtained from this experiment are 800 °C and 2.2 vol %, respectively, and the regeneration conversion ratio was about 95%.

You might also be interested in these eBooks

Info:

Periodical:

Pages:

134-139

Citation:

Online since:

May 2016

Export:

Price:

Permissions CCC:

Permissions PLS:

Сopyright:

© 2016 Trans Tech Publications Ltd. All Rights Reserved

Share:

Citation:

* - Corresponding Author

[1] W. J. W. Bakker, F. Kapteijn and 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, Chemical Engineering Journal 96 (2003).

DOI: 10.1016/j.cej.2003.08.022

Google Scholar

[2] H. X. Cheng and X. L. Luo: Mechanic Automation and Control Engineering (MACE), 2011 Second International Conference on (Hohhot, 15-17 July 2011) 7170-7172.

Google Scholar

[3] C. Descamps, C. Bouallou and M. Kanniche, Efficiency of an Integrated Gasification Combined Cycle (IGCC) power plant including CO2 removal, Energy 33 (2008) 874–881.

DOI: 10.1016/j.energy.2007.07.013

Google Scholar

[4] Y. Zhang, B. S. Liu, F. M. Zhang and Z. F. Zhang, Formation of (FexMn2−x) O3 solid solution and high sulfur capacity properties of Mn-based/M41 sorbents for hot coal gas desulfurization, Journal of Hazardous Materials 248- 249 (2013) 81- 88.

DOI: 10.1016/j.jhazmat.2012.12.053

Google Scholar

[5] H. L. Fan, K. C. Xie, J. Shangguan, F. Shen and C. H. Li, Effect of Calcium Oxide Additive on the Performance of Iron Oxide Sorbent for High-Temperature Coal Gas Desulfurization, Journal of Natural Gas Chemistry 16 (2007) 404–408.

DOI: 10.1016/s1003-9953(08)60012-2

Google Scholar

[6] P. R. Westmoreland and D. P. Harrison, Evaluation of candidate solids for high-temperature desulfurization of low-Btu gases, Environ. Sci. Technol. 10 (1976) 659–661.

DOI: 10.1021/es60118a010

Google Scholar

[7] J. Mi, M. Yu, F. Y. Yuan and J. C. Wang, Regeneration Characteristics and Kinetics of Modified Semi-coke Supported (Fe, Zn, Ce) Desulfurization Sorbents, Energy Fuels 26 (2012) 6551–6558.

DOI: 10.1021/ef301222c

Google Scholar

[8] J. Wang, B. Liang and R. Parnas, Manganese-based regenerable sorbents for high temperature H2S removal, Fuel 107 (2013) 539–546.

DOI: 10.1016/j.fuel.2012.10.076

Google Scholar

[9] V. Girard, A. Baudot, D. Chiche, D. Bazer-Bachi, C. Bounie, C. Geantet, Rational selection of single oxide sorbents for syngas desulfurization regenerable at reduced temperature: Thermochemical calculations and experimental study, Fuel 128(2014).

DOI: 10.1016/j.fuel.2014.02.058

Google Scholar

[10] J. Mu, D.D. Perlmutter, Thermal decomposition of inorganic sulfates and their hydrates, Ind Eng Chem Proc Des Dev, 20 (1981) 640–646.

DOI: 10.1021/i200015a010

Google Scholar

[11] H. F. Su, J. L. Gao, Y. X. Wen, Z. F. Tong and X. H. Li, Preparation of High Purity Hausmannite by Solid Phase Decomposition of Manganese Sulphate, Nonferrous Metals. 4 (2008) 47-50.

Google Scholar

[12] D. Karayilan, T. Dogu, S. Yasyerli, G. Dogu, Mn–Cu and Mn–Cu–V mixed oxide regenerable sorbents for hot gas desulfurization, Ind. Eng. Chem. Res. 44 (2005) 5221–5226.

DOI: 10.1021/ie0492496

Google Scholar