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The issue of magnesium hydroxide absorbing sulfur dioxide

2009-03-30View Original

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I have a question regarding tray towers. The process involves digesting magnesium oxide to produce a slurry with a mass concentration of 10%, which is then fed into a tray tower for counter-current absorption with gas containing 12% sulfur dioxide. The gas flow rate is 20,000 Nm3/h. I would like to know whether a tray tower is an appropriate choice for this application How to prevent blockages? Could someone with experience help determine the tower diameter, pore velocity, and circulation rate?

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