Column height will be dependent on the amount of trays required and the spacing between the trays. Column diameter is influenced by the vapor flow rate in the column.
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Tray design for absorber column hysys. Ludwigs classic text to further enhance its use as a chemical engineering process design manual of methods and proven. This complete revision of Applied Process Design for Chemical and Petrochemical Plants Volume 1 builds upon Ernest E. Normally tray spacing of 015 m to 1 m is used.
A simulation with more rigorous VLE computations using the SoaveRedlichKwong SRK equation of state has been carried out using the HYSYS Hypnotech Ltd simulation package. The result is a slightly lower vapour flow due to a higher relative volatility α in the range 399426 with an average of 414. For columns above 1 meter in diameter 05 m can be used as an initial estimate.
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