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INAUGURAL–DISSERTATION zur Erlangung der Doktorwürde der ...

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7<br />

equations are written in terms of volume fraction of each phase such that the sum of<br />

the volume fractions is unity. When the phases are equally distributed in the domain of<br />

interest with only mo<strong>der</strong>ate separation between the phases, the classical Euler – Euler<br />

approach is appropriate.<br />

Euler – Euler methods offer significant advantages over the Euler – Lagrange approach,<br />

e.g. the two-continua method is independent of disperse phase mass loading,<br />

and also the coupling between dispersed and carrier phase does not require averaging<br />

over the parcels unlike in Euler – Lagrangian.<br />

The merits of Euler – Euler methods play an important role when unsteady, turbulent<br />

gas-liquid flows with high dispersed phase mass loading are consi<strong>der</strong>ed. Additionally,<br />

Euler – Euler methods can outperform the Euler – Lagrange in case of unsteady<br />

spray flows and the computational cost do not depend on the droplet mass loading.<br />

Most of the Euler – Euler methods in the field of spray flows are based on the description<br />

of dispersed phase as a number density function (NDF) and the evolution of<br />

this NDF due to physical processes of spray flows are described by the NDF transport<br />

equation, also known as population balance equation (PBE) [41]. This NDF transport<br />

equation is <strong>der</strong>ived based on the kinetic equation [42] similar to the molecular kinetic<br />

theory, and it is known as general particle-dynamic equation in the field of aerosol<br />

science [43, 44].<br />

There exists several Euler – Euler methods based on the kinetic equation such as<br />

Williams’ spray equation and are categorized mainly as multi-fluid methods [45–47] and<br />

moment based methods [48–54]. In the multi-fluid approach, the distribution function<br />

is discretized using a finite volume technique that yields conservation equations for mass<br />

and momentum of droplets in fixed size intervals called sections or fluids [46]. This<br />

approach has recently been extended to higher or<strong>der</strong> of accuracy [55], but discretization<br />

of droplet size space is still a problem that needs to be addressed. On the contrary,<br />

moment based methods such as quadrature method of moments (QMOM) [51, 52, 56–<br />

58] or direct quadrature method of moments (DQMOM) [53, 54, 59] do not pose this<br />

problem and they are found to be efficient and robust in the poly-disperse multiphase<br />

flow problems.<br />

The scope of this work is modeling and simulation of mono and bi-component evaporating<br />

spray flows in an Euler – Euler framework. The focus is on the description of<br />

the characteristics of the spray flows and spray drying process, and the influence of the<br />

droplet size distribution on the droplet properties. In particular, spray inhomogeneity<br />

associated with the atomization process and its transport in the convective medium is<br />

not well un<strong>der</strong>stood. Subtle information is available about the particle formation and<br />

its influence on the properties of the resulting pow<strong>der</strong> in spray drying.<br />

The present study aims to develop a comprehensive spray model, which can be

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