采用CFD模型优化SO2洗涤塔

The reduction of environmental contaminants that contribute to smog and soot is a worldwide goal that has seen an increased focus in recent
years. In the United States, for example, it is estimated that by 2014 new rules will lead to a 71% reduction of sulfur dioxide emissions and 52%
of nitrogen oxide emissions as compared to 2005 level. Thus, medium-sized plants (100-500MW) that currently do not have flue gas
desulfurization (FGD) units or selective catalytic reduction systems (SCRs) will be required to adapt. Similar emission reduction efforts are
expected to be adopted globally, albeit at different levels. Wet-scrubber FGD is characterized as one of the most effective SO2 removal techniques
with low operating costs. However, capital cost for implementation is considered high. Hence an effective optimization procedure is required to
reduce these capital costs of conversion.
Power plants commonly use a lime slurry spray reaction to reduce SO2 emissions. Control of the droplets throughout the tower geometry is
essential to ensuring maximum reduction while minimizing scale. The liquid slurry is known to have density, surface tension and viscosity values
that deviate from standard water spray characteristics, which complicates process optimization. In order to improve the scrubber, nozzle
characteristics and placement must be optimized to reduce the cost of the system implementation and mitigate risks of inadequate pollution
reduction. A series of large flow rate, hydraulic, hollow cone sprays were investigated for this study.
A Computational Fluid Dynamics (CFD) model was used to examine potential scrubber designs for optimization of the system. Nozzle parameters
were modeled to allow particle tracking through the system. An ANSYS Fluent Lagrangian particle tracking method was used with heat and
mass transfer. The alkaline sorbent material and SO2 reaction is modeled to determine uniformity and efficacy of the system. Volumetric
chemistry mechanisms were used to simulate the reaction. These results demonstrate the expected liquid-gas interaction relative to the system
efficiency. Drop size, liquid rheology, and spray array layout were examined to achieve SO2 removal above 90%. Wall impingement and flow
pattern results were evaluated due to their impact in minimizing equipment plugging and corrosion required as for long-term scrubber utilization.