This file was created by the TYPO3 extension bib --- Timezone: CET Creation date: 2021-02-12 Creation time: 13-46-26 --- Number of references 25 article WiedmeyerVSABJAL2019 PARTEC International Congress on Particle Technology, Nürnberg 2019 V.Wiedmeyer A.Voigt K.Sundmacher F.Anker S.Bartsch V.John R.Ahrens S.Le Borne article AhrensABVWSJL2018 PBM 2018, Ghent Belgium 2018 R.Ahrens F.Anker C.Bartsch A.Voigt V.Wiedmeyer K.Sundmacher V.John S.Le Borne article WiedmeyerVLS2018 ProcessNet Jahrestreffen der Fachgruppe "Kristallisation", Bremen 2018 V.Wiedmeyer A.Voigt S.Le Borne K.Sundmacher article VoigtWS2018 2018 AIChE Annual Meeting (Particle Technology Forum), Pittsburgh 2018 A.Voigt V.Wiedmeyer K.Sundmacher article HausHHW2018 International Journal of Greenhouse Gas Control 2018 72 26-37 J.Haus E.-U.Hartge S.Heinrich J.Werther article WiedmeyerVS2017 ISIC20. Dublin 2017 V.Wiedmeyer A.Voigt K.Sundmacher article Kovacevic2016b Journal of Crystal Growth 2017 T.Kovačević V.Wiedmeyer J.Schock A.Voigt F.Pfeiffer K.Sundmacher H.Briesen article Wiedmeyer2016a Industrial & Engineering Chemistry Research 2017 V.Wiedmeyer F.Anker C.Bartsch A.Voigt V.John K.Sundmacher article Wiedmeyer2016 Chemical Engineering & Technology 2017 V.Wiedmeyer A.Voigt K.Sundmacher article Wilbrandt2016 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 Haus2016 Powder Technology 2016 Abstract A novel flowsheet simulation environment is applied to simulate a system of interconnected fluidized bed reactors as they are used for the process of chemical looping combustion of solid fuels. Dynamic models of the main process equipment are used in order to capture dynamic behavior of hydrodynamics inside an actual system, which delivers the experimental validation data. The process itself is carried out in a pair of strongly coupled fluidized bed reactors. Furthermore, a cyclone is used for gas-solid separation and two loop seal siphons prevent gas leakages from one reactor to another. The experimental plant operated at Hamburg University of Technology, which is modeled here, comprises a circulating fluidized bed air reactor and a two-stage bubbling bed fuel reactor. Operation of the plant is carried out at ambient condition and so are the simulations. All the mentioned process units are connected into a flowsheet via material streams and the whole process is simulated for 750 s of runtime. Within this time, the fluidization velocity of the fuel and the air reactor are changed to mimic effects, which occur during actual operation. The simulation was closely accompanied by experiments at the experimental facility and the results of simulation and experiments were compared. The bed mass, solid circulation and pressure profiles were simulated with good agreement to experimental findings. Dynamic effects were captured by the simulations and the system’s response to varying the fluidization speed, that is the change of bed masses, was predicted correctly. Time scales, in which these changes occur, were in the same range for experiments and simulations. A2 http://www.sciencedirect.com/science/article/pii/S0032591016308890 Elsevier 00325910 10.1016/j.powtec.2016.12.022 JohannesHaus Ernst-UlrichHartge StefanHeinrich JoachimWerther article Haus2016a Energy Technology 2016 4 10 1263--1273 chemical looping;coal;copper oxide;solid fuel;two-stage reactor A2 http://dx.doi.org/10.1002/ente.201600102 Wiley Online Library 2194-4296 10.1002/ente.201600102 JohannesHaus KaiLyu Ernst-UlrichHartge StefanHeinrich JoachimWerther inproceedings LindmuellerHHHW2018 2018 5th International Conference on Chemical Looping L.Lindmueller J.Haus E.-U.Hartge S.Heinrich J.Werther inproceedings Haus2016b 2016 A2 Chaouki, Jamal and Berruti, Franco and Bi, Xiatao and Cocco, Ray Fluidization XV JohannesHaus Ernst-UlrichHartge StefanHeinrich JoachimWerther inproceedings Hartge2015 2015 A2 Proc. of the 22nd Int. Conf. on Fluidized Bed Conversion Turku, Finland 22nd Int. Conf. on Fluidized Bed Conversion Ernst-UlrichHartge JohannesHaus StefanHeinrich JoachimWerther inproceedings Komossa2014 2014 Proceedings of the 11th Int. Conf. on Heat Transfer, Fluid Mechanics and Thermodynamics South Africa 11th Int. Conf. on Heat Transfer, Fluid Mechanics and Thermodynamics July 20-23, 2015 submitted H.Komossa S.Wirtz V.Scherer A.I.Nafsun F.Herz E.Specht misc Haus2016c 2016 A2 Jahrestreffen der ProcessNet-Fachgruppen Agglomerations- und Schüttguttechnik, Computational Fluid Dynamics und Mehrphasenströmungen Bingen Jahrestreffen der ProcessNet-Fachgruppen Agglomerations- und Schüttguttechnik, Computational Fluid Dynamics und Mehrphasenströmungen 29. Februar– 02. März 2016 JohannesHaus Ernst-UlrichHartge JoachimWerther StefanHeinrich misc Hartge2015a 2015 A2 ProcessNet. Jahrestreffen der Fachgruppen Computational Fluid Dynamics und Mehrphasenströmungen Lüneburg Jahrestreffen der Fachgruppen Computational Fluid Dynamics und Mehrphasenströmungen 19. – 20. März 2015 Ernst-UlrichHartge JohannesHaus StefanHeinrich JoachimWerther misc Komossa2014a 2014 DGMK-Fachbereichstagung: Konversion von Biomassen Rotenburg, Germany DGMK-Fachbereichstagung: Konversion von Biomassen Mai 12-14, 2014 H.Komossa D.Höhner S.Wirtz V,Scherer E.Specht F.Herz misc Wiedmeyera Summer School on Crystal Shape Engineering V.Wiedmeyer A.Voigt K.Sundmacher misc Wiedmeyerb PARTEC 2016 - International Congress on Particle Technology V.Wiedmeyer A.Voigt K.Sundmacher misc Wiedmeyerc ProcessNet Jahrestreffen der Fachgruppe "Kristallisation" V.Wiedmeyer A.Voigt K.Sundmacher misc Voigt 2016 AIChE Annual Meeting A.Voigt V.Wiedmeyer K.Sundmacher misc Kovacevic C1 BIWIC 2016 - 23rd International Workshop on Industrial Crystallization T.Kovačević V.Wiedmeyer J.Schock F.Pfeiffer A.Voigt K.Sundmacher H.Briesen misc Wiedmeyer ECCE10 - 10th European Congress of Chemical Engineering V.Wiedmeyer F.Anker A.Voigt V.John K.Sundmacher