Abstract (EN):
Recirculating cyclone systems, combining a numerically optimized reverse flow gas cyclone (RS_VHE
geometry) with a straight-through cyclone concentrator, were employed as reaction chambers for the dry
scrubbing of gaseous hydrogen chloride with solid hydrated lime particles. The performance of this technology
was tested at laboratory scale with two differently sized RS_VHE cyclones (0.020 and 0.026 m internal
diameter) coupled to the same recirculator of 0.020 m internal diameter. The experimental conditions were
the following: reaction temperature ≈ 326 K, gas flow rate ≈ 2.9 × 10-4 m3 ·s-1 at STP, and relative humidity
of the gas ≈ 8.5%. The experimental variables were the solids feed rate [(1.0-9.2) × 10-7 kg·s-1
] and HCl
concentration in the inlet gas [(0.35-2.8) × 10-2 mol·m-3
], giving different values for the ratio between the
amount of fresh hydrated lime and HCl feed at the inlet of the recirculating cyclone systems (R) and that
corresponding to the stoichiometric quantity (SR). The acid removal efficiencies ranged from 10 to 96%, and
the best performances were obtained for high values of the ratio R/SR. Increasing the cyclone diameter while
maintaining cyclone geometry improved the performance of the acid gas removal as well as the solid reactant
conversion, but the average particle collection efficiency was lowered from (98.0 ( 0.7)% to (89.3 ( 1.7)%.
Language:
English
Type (Professor's evaluation):
Scientific