2015
DOI: 10.1016/j.apm.2014.09.027
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Adomian decomposition method solution of population balance equations for aggregation, nucleation, growth and breakup processes

Abstract: Please cite this article as: A. Hasseine, H.-J. Bart, Adomian decomposition method solution of population balance equations for aggregation, nucleation, growth and breakup processes, Appl. Math. Modelling (2014), doi: http:// dx. AbstractThe dynamic behavior of particulate processes under the influence of the nonlinear aggregation term, nucleation, growth and breakup is studied. Analytic solutions are obtained from the integro-differential population balance equation governing the particle size distribution de… Show more

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Cited by 19 publications
(11 citation statements)
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References 26 publications
(20 reference statements)
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“…Figure ( 1) shows the geometry of the MHD Jeffery-Hamel flow. The walls stretch/shrink at a rate s with radial distance of r and the velocity at the walls is: The constitutive equation describing an incompressible non-Newtonian Casson fluid is written as follow 22 : In Eq. ( 2 ), where μ B denotes the plastic dynamic viscosity of the non-Newtonian fluid, P y is the yield stress of the fluid, π is the product of the component of deformation rate with itself, namely, π = e ij e ij where e ij is the ( i , j ) th component of the deformation rate and π c is a critical value of this product based on the non-Newtonian model.…”
Section: Mathematical Formulationmentioning
confidence: 99%
“…Figure ( 1) shows the geometry of the MHD Jeffery-Hamel flow. The walls stretch/shrink at a rate s with radial distance of r and the velocity at the walls is: The constitutive equation describing an incompressible non-Newtonian Casson fluid is written as follow 22 : In Eq. ( 2 ), where μ B denotes the plastic dynamic viscosity of the non-Newtonian fluid, P y is the yield stress of the fluid, π is the product of the component of deformation rate with itself, namely, π = e ij e ij where e ij is the ( i , j ) th component of the deformation rate and π c is a critical value of this product based on the non-Newtonian model.…”
Section: Mathematical Formulationmentioning
confidence: 99%
“…Polydisperse multiphase flows are present in several industrial technologies, such as spray combustion, bubble column reactor, fluidized bed reactor, and so on . This is one of the reasons why the academia has been devoting a significant amount of effort on this topic . Basically, there are three main approaches to predict the polydisperse multiphase flow behaviour: the fully resolved, the Lagrangian point‐particle, and the Eulerian‐Eulerian (E‐E) models …”
Section: Introductionmentioning
confidence: 99%
“…[21]. Considerable research studies on particle dynamics are carried out by many researchers [7,[24][25][26][27][28][29][30][31] to overcome the complexity and difficulty in theoretical and experimental studies on PBE. Generally, PBE proposed by Friedlander [22] is adequate to describe typical aerosol dynamic processes including nucleation, condensation, and coagulation etc.…”
Section: Introductionmentioning
confidence: 99%
“…The popular numerical methods for the solution of PBE mainly include sectional methods [32][33][34][35], Monte Carlo methods [30,[36][37][38][39][40], and moment methods [7,[41][42][43][44]. On the other hand, the exact and analytical solutions of PBE can also be obtained by e.g., the group analysis [28,31] and the separate variable method [45]), respectively. As far as fractal aggregates are concerned, a modified coagulation kernel including a pre-specified fractal dimension for the entire aggregate population is often used due to the computing limitations [46].…”
Section: Introductionmentioning
confidence: 99%