TY - JOUR
T1 - Evaluation of crystalline structure and SO2 storage capacity of a series of composition-sensitive De-SO2 catalysts
AU - Wang, J. A.
AU - Chen, L. F.
AU - Limas-Ballesteros, R.
AU - Montoya, A.
AU - Dominguez, J. M.
N1 - Funding Information:
J.A. Wang would like to thank the financial support from CONACyT-31282-U (Mexico) and FEIS-98-29-III (IMP-IPN-Mexico) and a scientific advisor fellowship of the Proyect-IMP-D.1234.03.012. L.F. Chen thanks the fellowship of visiting professor supported by the CONACyT and FIES projects in the Instituto Plitecnico Nacional de Mexico. The technical assistance from Professor H. L. Zhou for the AES analysis and from Ms. Y. F. Chen for the IR experiments is greatly appreciated.
PY - 2003/3/3
Y1 - 2003/3/3
N2 - A series of non-stoichiometric magnesium-aluminate solid solution spinels, used as sulfur-transfer catalysts in the fluid catalytic cracking units for SOx emissions abatement, were prepared by using coprecipitation method and characterized with BET, TGA, AES, XRD and in situ IR techniques. It was found that both the crystalline structures and De-SOx activities of magnesium-aluminate spinels are very sensitive to catalyst compositions. Several phase domains were produced by changing the mole ratio of alumina to magnesia in the preparation process. Owing to substitution of magnesium or aluminum ions in the spinel structure, that leads to a polarization of Al3+ or Mg2+ ions to adjacent oxygen lattices, the lattice cell parameter of spinel structure regularly varied with chemical compositions, producing a contraction or expansion effect in the lattice cell, that strongly affects De-SOx activity. TG analysis showed that during SO2 oxidative adsorption, most of sulfur species were captured on the surface and some sulfur species were stored in bulk of the solids. The IR and AES results confirmed that both surface and bulk-like sulfates with different H2-reducibilities were formed on the catalysts, which is in good agreement with results of SO2 monolayer adsorption measurement. Ten-cycle tests of SO2 oxidative adsorption and reductive decomposition of the formed sulfate showed that the sample with XAl = 0.33 is the optimum catalyst, its SO2 capturing capacity reached 124.4 mg/g.
AB - A series of non-stoichiometric magnesium-aluminate solid solution spinels, used as sulfur-transfer catalysts in the fluid catalytic cracking units for SOx emissions abatement, were prepared by using coprecipitation method and characterized with BET, TGA, AES, XRD and in situ IR techniques. It was found that both the crystalline structures and De-SOx activities of magnesium-aluminate spinels are very sensitive to catalyst compositions. Several phase domains were produced by changing the mole ratio of alumina to magnesia in the preparation process. Owing to substitution of magnesium or aluminum ions in the spinel structure, that leads to a polarization of Al3+ or Mg2+ ions to adjacent oxygen lattices, the lattice cell parameter of spinel structure regularly varied with chemical compositions, producing a contraction or expansion effect in the lattice cell, that strongly affects De-SOx activity. TG analysis showed that during SO2 oxidative adsorption, most of sulfur species were captured on the surface and some sulfur species were stored in bulk of the solids. The IR and AES results confirmed that both surface and bulk-like sulfates with different H2-reducibilities were formed on the catalysts, which is in good agreement with results of SO2 monolayer adsorption measurement. Ten-cycle tests of SO2 oxidative adsorption and reductive decomposition of the formed sulfate showed that the sample with XAl = 0.33 is the optimum catalyst, its SO2 capturing capacity reached 124.4 mg/g.
KW - FCC unit
KW - Magnesium-aluminate spinel
KW - SO emission control
KW - Sulfur-storage capacity
KW - Sulfur-transfer catalyst
UR - http://www.scopus.com/inward/record.url?scp=0037416067&partnerID=8YFLogxK
U2 - 10.1016/S1381-1169(02)00515-0
DO - 10.1016/S1381-1169(02)00515-0
M3 - Artículo
AN - SCOPUS:0037416067
SN - 1381-1169
VL - 194
SP - 181
EP - 193
JO - Journal of Molecular Catalysis A: Chemical
JF - Journal of Molecular Catalysis A: Chemical
IS - 1-2
ER -