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|Title:||Measurement of drop size and distribution in an annular two-phase, two-component flow occurring in a venturi scrubber||Authors:||Viswanathan, S.
|Issue Date:||14-Sep-2005||Citation:||Viswanathan, S., Lim, D.S., Ray, M.B. (2005-09-14). Measurement of drop size and distribution in an annular two-phase, two-component flow occurring in a venturi scrubber. Industrial and Engineering Chemistry Research 44 (19) : 7458-7468. ScholarBank@NUS Repository. https://doi.org/10.1021/ie0489195||Abstract:||Drop size and distribution in an annular two-phase flow occurring in a venturi scrubber were measured using a phase Doppler particle analyzer (PDPA) as a function of operating conditions such as gas velocity and liquid-to-gas ratio. At low throat-gas velocities, the maximum measured drop diameter and Sauter mean diameter increased when the liquid-to-gas ratio increased. However, at a fixed liquid-to-gas ratio, the maximum measured drop diameter and Sauter mean diameter decreased with the increase in throat-gas velocity. The experimental data tested with two theoretical distributions, namely, the upper-limit distribution function and the root-normal distribution function in terms of the shape of the drop-size distribution and the frequency values, produced a better agreement with the former than with the latter. It was observed that, in a highly dispersed drop-size distribution produced at a low throat-gas velocity of 45 m/s, a single average drop size is inadequate to describe the entire drop-size distribution, whereas at a high throat-gas velocity, 60 m/s, a single average drop size was found sufficient to describe the entire drop-size distribution formed. © 2005 American Chemical Society.||Source Title:||Industrial and Engineering Chemistry Research||URI:||http://scholarbank.nus.edu.sg/handle/10635/89365||ISSN:||08885885||DOI:||10.1021/ie0489195|
|Appears in Collections:||Staff Publications|
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