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@PHDTHESIS{Ginsberg:82629,
      author       = {Ginsberg, Tobias},
      othercontributors = {Modigell, Michael},
      title        = {{D}ynamische {M}odellierung von {D}rehrohröfen},
      address      = {Aachen},
      publisher    = {Publikationsserver der RWTH Aachen University},
      reportid     = {RWTH-CONV-143017},
      pages        = {V, 140 S. : graph. Darst.},
      year         = {2011},
      note         = {Zsfassung in dt. und engl. Sprache; Aachen, Techn.
                      Hochsch., Diss., 2010},
      abstract     = {In the work at hand it is investigated whether the dynamic
                      behaviour of industrial rotary kiln plants can be reproduced
                      with quantitative accuracy by means of mathematical models.
                      For this purpose the relevant heat and mass-transfer
                      mechanisms in the kilns are identified and physically
                      founded sub-models are provided that are capable of mapping
                      these phenomena. A model of an entire plant results from
                      combining these sub-models. As a demonstration case a rotary
                      kiln for calcination of titanium dioxide is considered. The
                      developed model for this plant is validated by means of
                      operational data that were captured during a measurement
                      campaign over several weeks. In the model it is assumed that
                      the solid bed as well as the gas phase are ideally mixed in
                      every kiln cross section. Temperatures and compositions thus
                      only depend on the axial coordinate. Heat transfer by
                      radiation and convection, regenerative heat transfer in the
                      kiln wall and the flow velocity of the solid bed are
                      described by means of proper sub-models. The chemical
                      processes within the kiln are described by reaction kinetic
                      expressions that are available in the literature. The
                      respective reaction enthalpies are determined in
                      calorimetric measurements. The model is validated by means
                      of a dynamic test case representing kiln operation over a
                      15-day period. The test case comprises a change in the
                      operational state of the kiln due to breakdown of a plant
                      component. The model quality is evaluated based on the
                      measured temperatures of the solid product and the off gas,
                      among others. An error analysis yields that due to uncertain
                      model parameters and operational measurement data the
                      model's predictive accuracies equal +/-244°C and +/-19°C,
                      respectively, for the mentioned temperatures. However, the
                      product temperature is actually reproduced with a mean
                      deviation of +/-35°C at an average value of 920°C. A mean
                      deviation of +/-12°C results for the off gas temperature at
                      an average value of 370°C. Hence, the model's predictive
                      accuracy is considerably better than it was to be expected
                      from the parameter and measurement uncertainties.
                      Furthermore the error analysis shows, that most of the
                      measurement values required in the model are captured
                      sufficiently accurate by the standard industrial measurement
                      equipment applied at the considered plant. Improving the
                      measurement accuracy of the false air flow rate, the
                      reactand composition and mass flow, and the fuel flow rate
                      offer the biggest potential to significantly improve the
                      model's accuracy. All in all the simulation results indicate
                      that the dynamic behaviour of industrial rotary kilns can be
                      reproduced by rigorous mathematical models at moderate
                      computational effort.},
      keywords     = {Drehrohrofen (SWD) / Dynamische Modellierung (SWD) /
                      Titandioxid (SWD) / Titandioxidherstellung (SWD) /
                      Calcinieren (SWD)},
      cin          = {416220},
      ddc          = {620},
      cid          = {$I:(DE-82)416220_20140620$},
      typ          = {PUB:(DE-HGF)11},
      urn          = {urn:nbn:de:hbz:82-opus-38307},
      url          = {https://publications.rwth-aachen.de/record/82629},
}