Synthesis and Characterization of γ‑Fe<sub>2</sub>O<sub>3</sub> for H<sub>2</sub>S Removal at Low Temperature
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Abstract
The performance of γ-Fe<sub>2</sub>O<sub>3</sub> as sorbent for H<sub>2</sub>S removal at low
temperatures (20–80 °C) was investigated. First, γ-Fe<sub>2</sub>O<sub>3</sub>/SiO<sub>2</sub> sorbents with a three-dimensionally
ordered macropores (3DOM) structure were successfully prepared by
a colloidal crystal templating method. Then, the performance of the
γ-Fe<sub>2</sub>O<sub>3</sub>-based material, e.g., reference
γ-Fe<sub>2</sub>O<sub>3</sub> and 3DOM γ-Fe<sub>2</sub>O<sub>3</sub>/SiO<sub>2</sub> sorbents, for H<sub>2</sub>S capture
was compared with that of α-Fe<sub>2</sub>O<sub>3</sub> and
the commercial sorbent HXT-1 (amorphous hydrated iron oxide). The
results show that γ-Fe<sub>2</sub>O<sub>3</sub> has an enhanced
activity compared to that of HXT-1 for H<sub>2</sub>S capture at temperatures
over 60 °C, whereas α-Fe<sub>2</sub>O<sub>3</sub> has little
activity. Because of the large surface area, high porosity, and nanosized
active particles, 3DOM γ-Fe<sub>2</sub>O<sub>3</sub>/SiO<sub>2</sub> sorbent shows the best performance in terms of sulfur capacity
and utilization. Moreover, it was found that moist conditions favor
H<sub>2</sub>S removal. Furthermore, it was found that the conventional
regeneration method with air at high temperature was not ideal for
the composite regeneration because of the transmission of some amount
of γ-Fe<sub>2</sub>O<sub>3</sub> to α-Fe<sub>2</sub>O<sub>3</sub>. However, simultaneous regeneration by adding oxygen in the
feed stream allowed the breakthrough sulfur capacity of FS-8 to increase
up to 79.1%, which was two times the value when there was no O<sub>2</sub> in the feed stream