On the operational flexibility of cyclone separators
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I would like to ask experts: when using a cyclone separator for gas-liquid separation, does the separation efficiency decline when the processing volume is 20% of the designed value? And by how much does it decline?
When the gas flow rate drops to only 20% of the design value, the efficiency of gas-liquid separation should decline significantly. A cyclone separator relies on the centrifugal force generated by high-speed airflow as it passes through the separator to separate liquids or dust; since centrifugal force is proportional to the square of the flow velocity, such a significant drop in flow velocity should result in a marked decrease in separation efficiency.