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De-SO sub x catalyst; An XRD study of magnesium aluminate spinel and its solid solutions

Journal Article · · Industrial and Engineering Chemistry Research; (United States)
DOI:https://doi.org/10.1021/ie00055a007· OSTI ID:5877267
; ;  [1]
  1. Amoco Chemical Co., Naperville, IL (United States). Research and Development Dept.
This paper reports on a systematic X-ray diffraction study that was undertaken to characterize the stoichiometric spinel (MgAl{sub 2}O{sub 4}), alumina excess spinel (MgAl{sub 2}O{sub 4} {center dot} xAl{sub 2}O{sub 3}) and magnesia excess spinel (MgAl{sub 2}O{sub 4} {center dot} MgO). A Vegard's plot, lattice parameter vs the composition of these solid solutions, reveals that, in alumina excess spinel, a continuous solid solution (x = 0 {minus} {infinity}) exists, while, in magnesia excess material, the solid solution is limited to y = 0-1. When y = 1, a solid solution assumes the composition of MgAl{sub 2}O{sub 4} {center dot} MgO. If y {gt} 1, both periclase and stoichiometric spinel (MgAl{sub 2}O{sub 4}) phases coexist. The SO{sub x} removal activity of various hydrothermally stable cerium oxide containing solid solution spinels was evaluated. In the magnesia excess solid solutions, SO{sub x} removal activity increased as MgO increased and reached maximum at y = 1, which is the CeO{sub 2}/MgAl{sub 2}O{sub 4} {center dot} MgO system. This catalyst is the most widely used SO{sub x} reduction catalyst today.
OSTI ID:
5877267
Journal Information:
Industrial and Engineering Chemistry Research; (United States), Journal Name: Industrial and Engineering Chemistry Research; (United States) Vol. 30:7; ISSN 0888-5885; ISSN IECRE
Country of Publication:
United States
Language:
English