Influence of Pressure on the Hydrodynamics and Mass Transfer Parameters of an Agitated Bubble Reactor

Abstract

The present study deals with the pressure effects on the hydrodynamic flow and mass transfer within an agitated bubble reactor operated at pressures between 105 and 100 × 105 Pa. In order to clarify the flow behavior within the reactor, liquid phase residence time distributions (RTD) for different operating pressures and gas velocities ranging between 0.005 m/s and 0.03 m/s are determined experimentally by the tracer method for which a KCl solution is used as a tracer. The result of the analysis of the liquid‐phase RTD curves justifies the tank‐in‐series model flow for the operating pressure range. Good agreement is obtained between theoretical and experimental results assuming the reactor is operating as perfectly mixed. Two parameters characterizing the mass transfer are identified and investigated in respect to pressure: the gas‐liquid interfacial area and volumetric liquid‐side mass transfer coefficient. The chemical absorption method is used. For a given gas mass flow rate, the interfacial area as well as the volumetric liquid mass transfer coefficient decrease with increasing operating pressure. However, for a given pressure, a and kLa increase with increasing gas mass flow rates. The mass transfer coefficient kL is independent of pressure.

Characterizing the effects of shaking intensity on the kinetics of metallic iron dissolution in EDTA

“…Like all precipitation processes, this reaction is influenced by mixing. Mixing liquids to precipitate solid particles is a common multiphase chemical process that comprises several complex phenomena [47][48][49][50][51][52][53][54][55][56][57].…”

Review of Mass-Transfer Correlations for Packed Columns

“…Danckwerts 77 also proposed chemical absorption theory and reviewed 78 two-phase systems employed to measure the interfacial areas of interphase mass transfer. Many workers adopted this method to investigate the effective interfacial areas in packed columns, − bubble columns, − and agitated reactors …”

The effect of system pressure on gas‐liquid slug flow in a microchannel

“…Moreover, the system pressure can have a considerable influence on the flow and mass‐transfer behavior in gas‐liquid systems due to gas compressibility. Many literatures have reported the influence of the system pressure in bubble columns. Letzel et al studied the gas hold‐up and mass transfer in bubble columns at elevated pressures from 0.1 to 1.3 MPa and found that the gas hold‐up and the volumetric mass‐transfer coefficient both increased with the increasing system pressure.…”