The behavior of different mixed oxides, including zinc
titanates (ZT) and zinc ferrites modified
with CuO (ZFC) or TiO2 (ZFT), as hot gas desulfurizing
sorbents was investigated. The sorbents
were prepared by calcination at 650 °C of a mixture of bulk oxides in
three different
stoichiometries in order to form new phases and modify their textural
properties. Tests of
stability against reduction were obtained by thermoprogrammed
reduction, and kinetic studies
of the sulfidation reaction were carried out in a thermobalance in the
temperature range of
550−650 °C. Kinetic parameters of the intrinsic reaction were
obtained assuming a grain model.
The sulfidation behavior of the sorbents as extrudates was
investigated in a fixed-bed reactor
in terms of breakthrough curves. Fresh and sulfided samples were
characterized by Hg
porosimetry, X-ray diffraction, and SEM-EDX. The study shows that
the addition of TiO2 or
CuO to zinc ferrite based sorbents calcined at 650 °C has little
effect on the stability against
reduction but markedly influences their textural properties. The
stabilizing effect of Ti is
observed in samples calcined at higher temperature or in
non-iron-containing sorbents. The
calculated kinetic constants indicate that the Zn content and the
incorporation of Cu have an
enhancing effect on the kinetics of the sulfidation process.
Including H2 in the feed gas decreases
the reactivity and increases the activation energy. Extrudated
sorbents showed a good
performance as desulfurizing agents and maintained the H2S
concentration in the outlet gas
below 20 ppm. ZT sorbent exhibited a poor efficiency, which makes
the addition of Ti
questionable.
The effect of aging in nitrogen upon the regeneration characteristics of the coke deposits on chromia-alumina catalysts has been investigated. To this end, the coked catalysts have been subjected to various treatments in nitrogen, and the chemical composition and reactivity of the deposits have been investigated. The results show that the process of aging in nitrogen gives rise to significant changes in both the composition and reactivity of the coke deposits, due to the stripping of the coke fractions with a higher volatility. This obviously has important consequences upon the subsequent regeneration, which are also discussed and tested in regeneration experiments using coked catalyst of different ages.
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