This file was created by the TYPO3 extension bib --- Timezone: CET Creation date: 2021-02-12 Creation time: 13-07-34 --- Number of references 13 article Wilbrandt2016 Par<prt>M</prt>ooN -- a modernized program package based on mapped finite elements Computers & Mathematics with Applications 2017 U.Wilbrandt C.Bartsch N.Ahmed N.Alia F.Anker L.Blank A.Caiazzo S.Ganesan S.Giere G.Matthies R.Meesala A.Shamin J.Venkatesan V.John article Meyer2017 Determination of particle exchange rates at over-flow weirs in horizontal fluidised beds by particle tracking velocimetry Particuology 2017 A3 10.1016/j.partic.2016.09.007 KMeyer ABück E.Tsotsas article Bueck2016 Influence of operation parameters on process stability in continuous fluidised bed layering with external product classification Powder Technology 2016 300 37 - 45 Abstract Several studies—theoretical and experimental—show that continuous fluidised bed layering granulation with external classification can show instability in the form of self-sustained oscillations. Recent results show that the process stability does not only depend on product-related process parameters but also on the formation of functional zones in the fluidised bed chamber, especially the formation of a spray and drying zone. In this work a systematic evaluation of zone formation in different apparatus designs (e.g., top- and bottom-spray in cylindrical apparatuses) and its influence on process stability is performed, resulting in a stability regime map for the different apparatus designs and key operation parameters. 7th International Granulation Workshop 2015: Granulation across the length scales Layering, Fluidised bed, Process stability, External classification, Bifurcation analysis A3 //www.sciencedirect.com/science/article/pii/S0032591016301127 0032-5910 http://dx.doi.org/10.1016/j.powtec.2016.03.019 A.Bück C.Neugebauer K.Meyer S.Palis E.Diez A.Kienle S.Heinrich E.Tsotsas article Feinauer2015 <prt>Structural characterization of particle systems using spherical harmonics</prt> Materials Characterization 2015 106 123--133 http://dx.doi.org/10.1016/j.matchar.2015.05.023 10.1016/j.matchar.2015.05.023 J.Feinauer A.Spettl I.Manke S.Strege A.Kwade A.Pott V.Schmidt article Reinhold2015 Modeling and measurement of abraded particles Powder Technology 2015 271 134 - 140 Particle shape model C1 http://www.sciencedirect.com/science/article/pii/S0032591014008900 0032-5910 http://dx.doi.org/10.1016/j.powtec.2014.10.040 AlexanderReinhold StefanSchorsch MarcoMazzotti HeikoBriesen article Meyer2015 Dynamic Multi-Zone Population Balance Model of Particle Formulation in Fluidized Beds Procedia Engineering 2015 102 1456 - 1465 Abstract In this work a generic multi-compartment, multi-zone population balance model (PBM) is developed which allows predicting the process dynamics of particle formation in a horizontal fluidized bed. It focuses on the particle size distribution (PSD) which is an important quality parameter in solids process industry. It is influenced by different factors, e.g. apparatus design (weir and nozzle assembly) and process conditions (mass flow rate), respectively. In this study the apparatus design by an over and under flow weir configuration, used separately or in combination, is investigated to obtain the product properties at the outlet of the apparatus. Simulation results show how characteristic product data depend on the process conditions and apparatus design. The obtained trends can then be used for an inverse apparatus design of horizontal fluidized beds to obtain particles with desired properties. New Paradigm of Particle Science and Technology Proceedings of The 7th World Congress on Particle Technology horizontal fluidized bed, spray granulation, population balance modeling, particle size distribution. A3 //www.sciencedirect.com/science/article/pii/S1877705815002982 1877-7058 http://dx.doi.org/10.1016/j.proeng.2015.01.279 KatjaMeyer AndreasBück EvangelosTsotsas article Metzger2014 On the transient flow characteristics in Confined Impinging Jet Mixers - CFD simulation and experimental validation Chemical Engineering Science 2014 10.1016/j.ces.2014.12.056 LukasMetzger MatthiasKind inproceedings Meyer2016a Multi-compartment model for study of thermal effects during granulation in a continuously operated horizontal fluidized bed 2016 A3 Gifu (JP) Proceedings of International Drying Symposium (IDS 2016) KMeyer ABück ETsotsas inproceedings Meyer2014 Multi-zone model for layering granulation in horizontal fluidized beds 2014 A3 J. Andrieu und P. Perré Proc. 19th International Drying Symposium (IDS 2014) KMeyer ABück ETsotsas inproceedings Metzger2014a Supersaturation buildup in Confined Impinging Jet Mixers - A multi-scale coupling of CFD and population balance 2014 Proc. 19th International Symposium on Industrial Crystallization Toulouse, France ISIC 19 16.9 - 19.09. 2014 LukasMetzger MatthiasKind inproceedings Metzger2014b Compartment Method for Dynamic Multi-Scale Simulation of Precipitation Reactors 2014 1A, Applications in CFD pp. V01AT03A013 Proc. 4th Joint US-European Fluids Engineering Division Summer Meeting Chicago, Illinois 4th Joint US-European Fluids Engineering Division Summer Meeting 03.8 - 07.08. 2014 10.1115/FEDSM2014-21547 LukasMetzger MatthiasKind misc Segets2014a Processing concepts for small nanoparticles: classification on a nanometer scale by tailoring particle interactions 2014 ProcessNet-Jahrestagung Aachen ProcessNet-Jahrestagung D.Segets K.Yamamoto C.Lutz Y.Mori W.Peukert misc Metzger2014c Vernetzte Methoden zur dynamischen Simulation von Fällungsreaktoren 2014 ProcessNet-Jahrestreffen der Fachgruppe Kristallisation, Münster Münster ProcessNet-Jahrestreffen der Fachgruppe Kristallisation 27.3 - 28.3. 2014 LukasMetzger mKind