@ARTICLE{Cudak_Magdalena_The_2020,
 author={Cudak, Magdalena},
 volume={vol. 41},
 number={No 4},
 pages={241-256},
 journal={Chemical and Process Engineering},
 howpublished={online},
 year={2020},
 publisher={Polish Academy of Sciences Committee of Chemical and Process Engineering},
 abstract={The aim of the research presented in this paper was to determine the effect of vessel scale on gas hold- up in gas-liquid systems. The agitated vessel with internal diameters of T = 0:288 m and T = 0:634 m was filled with a liquid up to the height H = T. For the purpose of measurements, two high-speed impellers were used: Rushton turbine impeller (RT) or A 315 impeller.Within the study, the following parameters were altered: superficial gas velocity, impeller speed, impeller type and concentration of aqueous sucrose solution. In addition, influence of the vessel scale on gas hold-up value was analysed. Experimental results were mathematically described. Equations (5)–(7) do not have equivalents in the literature.},
 type={Article},
 title={The effect of vessel scale on gas hold-up in gas-liquid systems},
 URL={http://ochroma.man.poznan.pl/Content/118937/PDF/art01.pdf},
 doi={10.24425/cpe.2020.136010},
 keywords={agitated vessel, mixing, gas hold-up, aqueous sucrose solution},
}