Supported
sorbent for flue gas desulfurization was prepared by
a process of hydrating and drying a mixture of carrier particles and
lumps of CaO in previous studies. Supported sorbent achieves high
desulfurization efficiency in a Circulating Fluidized Bed (CFB) reactor
at moderate temperature. However, the preparation process is complicated,
which makes industrial application difficult. In this study, supported
sorbent is prepared in situ in a CFB reactor by a coating process,
in combination with SO2 removal. The experiments are conducted
in a pilot-scale CFB experimental facility at 700–750 °C.
The influence of operation parameters on supported sorbent formation
and desulfurization efficiency is tested, including bed inventory,
sprayer location, and spray method. The results show that the present
process achieves 85.3% desulfurization efficiency with a Ca/S molar
ratio of 2.01 when the bed inventory is 25 kg. This result is approximately
10 times higher than that of a zero bed inventory. The scanning electron
microscope and energy dispersive spectrometer results show that the
supported sorbent forms when fine Ca(OH)2 particles in
the lime slurry adhere to the bed material surface. The residence
time of the supported sorbent in the CFB reactor is significantly
longer than that of the fine Ca(OH)2 particles. The adhesion
efficiency is influenced by the spray location and spray method. The
desulfurization performance of the supported sorbent prepared by the
original hydration and drying method is also tested. The desulfurization
efficiency is 25–35% higher than the present process because
there is better adhesion in the original method than the in situ method.
But the process complexity is significantly reduced when using the
present process. The present process is a substantial attempt toward
the application of supported sorbent.