Comparison of Separation Performance of a Structured Packed Column with a Tray-Type Column for H2S and CO2
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چکیده
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چکیده ندارد.
Efficient Approximate Method for Packed Column Separation Performance Simulation
Packed distillation and absorption columns are often modeled using equilibrium stages. However, determination of the packing height that corresponds to an equilibrium stage is not easy. For binary systems HETP values can be used, but these are not applicable to multicomponent systems because mass transfer rates of different components deviate from each other. Rate-based non-equilibrium models c...
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ژورنال
عنوان ژورنال: Oil & Gas Science and Technology - Revue de l'IFP
سال: 2009
ISSN: 1294-4475,1953-8189
DOI: 10.2516/ogst/2008052