Pressure Drop in Randomly Packed Absorption Tower in Transient Flow Regime
In this work computational fluid dynamics is used to describe the fluid flow across a randomly packed absorption tower. The CFD simulation method is employed on a packed tower that is packed with 1cm Raschig rings. Tower is 175cm in height. Air flow rate range was 1.5 to 5 m/s. The measured pressure drops were in 1.5 to 12 Pascal per height of tower in meter. The Klerks approach is examined to define the influence of confining walls on pressure drop in packed areas. It is concluded that CFD model that uses the Klerks definition of radial porosity distribution is a successful way for pressure drop prediction in packed beds. Model prediction of dry pressure drop is about 4% lower than the experimental measurements. Erguns pressure drop prediction is compared with that of Reichelts using averaged and distributed porosity profiles. In both methods Erguns approach in comparison with Reichelts approach has %6 lesser error in dry pressure drop prediction.
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Simulation of Natural Gas Transmission in the Pipeline in Two-Phase and Supercritical Conditions
Moslem Abrofarakh, *, Davod Mohebbi-Kalhori
Iranian Gas Engineering Journal,