Abstract:Accurate prediction of pressure drops around trays or packing sections
is crucial for the optimal design of distillation columns. However,
simultaneous optimization of all operating and structural parameters
with the rigorous hydraulics consideration in MESH model is still
difficult because of both the convergence for the stage number and
integer optimization problem. In the present work, a rigorous equilibrium
stage-based pseudotransient distillation model considering stage hydraulics
is developed in the equa… Show more
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