Fig. 6 shows that both the limestone process and the red mud-limestone process with different solid–liquid ratios can achieve the standard SO 2 discharge. As the particle size of red mud is larger than that of limestone powder the high solid–liquid ratio leads to greater wear of pipelines and conveying pumps leading to higher operation and maintenance costs.
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Get PriceOptimum values of the process parameters for different conditions of running flue gas desulfurization system were found. The process and cost model can be useful when designing the wet limestone FGD systems and carrying out economic analysis of the flue gas desulfurization plants.
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