Hey there, I'm here once again....
I'm having trouble finding a way to size a decanter. It is quite big (Volume = 6371 m3, Height = 41.796m and diameter = 14m). It is a horizontal process vessel and operates at 22bar. The trouble is that all the correlations I could use do not go up to this size and don't have a pressure correction factor. I could use the sixth tenths rule if all else fails, but I would like to know if there is another way.
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Decanter Costing
Started by Cariemb0, Aug 26 2008 02:27 AM
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Posted 26 August 2008 - 02:27 AM
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