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@PHDTHESIS{Seebold:841492,
author = {Seebold, Sören},
title = {{E}influss der {K}ristallisation auf das {F}ließverhalten
oxidischer {S}chmelzen},
volume = {393},
school = {RWTH Aachen},
type = {Dissertation},
address = {Jülich},
publisher = {Forschungszentrum Jülich GmbH Zentralbibliothek, Verlag},
reportid = {FZJ-2017-08536},
isbn = {978-3-95806-268-9},
series = {Schriften des Forschungszentrums Jülich Reihe Energie $\&$
Umwelt / Energy $\&$ Environment},
pages = {168 S.},
year = {2017},
note = {RWTH Aachen, Diss., 2017},
abstract = {Numerous technical applications in the energy and
metallurgical industries demand a fundamental knowledge of
the flow of slags. In particular, the operation of an
entrained flow gasifier is challenging as the slag has to be
reliably discharged. The slag consists of unburned inorganic
matter, usually oxides. Crystallization in this oxide melt
influences the flow behavior of the slag because of the
occurring precipitates. In this study the mechanisms and
impact of crystallization on the flow of oxide slags were
investigated. For this purpose, isothermal viscosity
measurements were conducted on fossil and renewable solid
fuel slags in order to examine the rheological evolution
over time caused by the crystallization. It has been
demonstrated that the evolution of viscosity of a
sub-liquidus melt depends strongly on time, as well as on
temperature and composition. Using a rotational
high-temperature viscometer, it was found that the
crystallization during flow could be separated into three
time regimes: a lag-time, in which the undercooled melt
behaved as an Arrhenius-liquid; the kinetic-driven
crystallization accompanied by an increase of the viscosity;
and, finally, the rheological equilibrium that is
represented by a constant viscosity. Furthermore, an
increase of viscosity caused by crystallization was
accompanied by a shift from Newtonian to non-Newtonian flow;
here, shear thinning flow indicated the existence of
precipitates. SEM was used to examine the crystalline
precipitates. The evolution of flow was used to create
time-temperature-transformation diagrams. It was observed
that an increase of the degree of supercooling decreases the
incubation as well as the crystallization period. The
crystallization of the oxide melt follows the classical
theory of crystallization. Moreover, it was shown that the
change of viscosity might be used as morphological
information to describe kinetic parameters. The conclusions
from the experimental results regarding the influence of
crystallization on the flow of oxide melts were transferred
to an empirical model. The model considers the physical
influence of the crystals and the chemical change of the
bulk composition caused by the crystallization. Therefore,
the concept of the resulting relative viscosity was
introduced, in order to describe the physical and chemical
effects of crystallization. The evolution of viscosity from
the metastable to the equilibrium state was described by a
kinetic theory. The results of the model correlate well with
the experimental observations.},
cin = {IEK-2},
cid = {I:(DE-Juel1)IEK-2-20101013},
pnm = {111 - Efficient and Flexible Power Plants (POF3-111)},
pid = {G:(DE-HGF)POF3-111},
typ = {PUB:(DE-HGF)3 / PUB:(DE-HGF)11},
url = {https://juser.fz-juelich.de/record/841492},
}