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• W3095844335 abstract "Gas holdup (εg) and power correlations in gas-liquid (G-L) systems, apart from the physicochemical properties of the liquid phase, are dependent on impeller-sparger-vessel geometry. To date, reported correlations do not specifically address this issue, and it must be investigated with a unified approach. Here, we propose a correlation via the use of a normalized εg that involves the impeller-sparger system geometry for a vessel of standard geometry expressed as a function of an easily measurable and independent operational parameter, that is, (1 - Pg/Pl), where Pg/Pl is the gassed to ungassed power ratio. Furthermore, our work demonstrates that Pg/Pl can be used as a tool for the identification of hydrodynamic regimes. Radial and axial impellers with ring spargers were used in a stirred and sparged contactor (SSTC) of 0.25 m diameter containing 1 × 10-2 m3 water. The oxygen flowrate (Qg) was varied from 2.5 to 40 LPM or (4.17 to 66.7) × 10-5 m3 s-1, and the agitation intensity (N0) was varied from 1.67 to 50 rps at the temperature (θ) = 313 K under atmospheric pressure. This novel correlation is easy to use, offers reasonable precision, and can serve as a valuable alternative to more complex correlation models." @default.
• W3095844335 created "2020-11-09" @default.
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• W3095844335 date "2020-11-03" @default.
• W3095844335 modified "2023-10-16" @default.
• W3095844335 title "Estimation of Gas Holdup Using the Gassed to Ungassed Power Ratio of an Oxygen–Water System in a Stirred and Sparged Tank Contactor" @default.
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• W3095844335 doi "https://doi.org/10.1021/acsomega.0c02292" @default.
• W3095844335 hasPubMedCentralId "https://www.ncbi.nlm.nih.gov/pmc/articles/7675537" @default.
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