1999
DOI: 10.1016/s0009-2509(99)00170-0
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Simulation of the population balances for liquid–liquid systems in a nonideal stirred tank. Part 1 Description and qualitative validation of the model

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Cited by 166 publications
(107 citation statements)
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“…(28)) is not very sensitive to changes in the values of the constant C 4 . This constant may vary +/-50%, which agrees to the reported results in the published literature (Alopaeus et al [18,65]). Second, the estimated parameters above were used to simulate a pilot plant RDC column with the total active height of 1.76 m, where its characteristic dimensions are shown in Table 3.…”
Section: Sample Problems Parameter Estimation Using An Rdc Column (Dnsupporting
confidence: 91%
“…(28)) is not very sensitive to changes in the values of the constant C 4 . This constant may vary +/-50%, which agrees to the reported results in the published literature (Alopaeus et al [18,65]). Second, the estimated parameters above were used to simulate a pilot plant RDC column with the total active height of 1.76 m, where its characteristic dimensions are shown in Table 3.…”
Section: Sample Problems Parameter Estimation Using An Rdc Column (Dnsupporting
confidence: 91%
“…A mixer designed to serve this dual purpose of mixing and pumping is called a pump-mixer (Coplan et al, 1954). Though the pump-mixers are essentially used for producing dispersions of a liquid phase in another immiscible liquid phase, single-phase characteristics are equally important as, with the present status of computing hardware, a practical way of solving population balance in agitated vessels calls for pseudo-single-phase modeling to get the parameters that eventually control drop breakage and coalescence and hence dictate the drop size distributions (Alopaeus et al, 1999;Maggioris et al, 2000;Alexopoulos et al, 2002;Alopaeus et al, 2002). The two important design or performance parameters of a pump-mixer are its power consumption and head generation both of which are affected by several parameters which can be classified either as geometric or process parameters.…”
Section: Introductionmentioning
confidence: 99%
“…The initial droplet size distribution is affected by the collision, coalescence and breakage frequencies. These frequencies were calculated using the expressions and parameters by Alopaeus et al [22] while the energy dissipation rate, influenced by some properties of the impeller such as impeller speed, impeller diameter, power number of impeller, and naturally the properties of mixed phase, the volume and density of the mixture was computed as discussed by Nere et al [23]. Figure 3 represents the monomer droplet size distribution computed for impeller speed is 350 rpm and dispersed phase volume fraction is 0.3.…”
Section: Yesmentioning
confidence: 99%