Nürnberg, Universiẗat, Diss., 2003--Erlangen.

Im Zeitraum der Jahre 2012 bis 2015 beteiligte sich die TU Bergakademie Freiberg mit einem Antrag für ein \\\"Zentrum für effiziente Hochtemperatur- Stoffwandlung\\\" (ZeHS) am Wettbewerb um eine Förderempfehlung für Forschungsbauten an Hochschulen gemäß Art. 91b GG. Nach der erfolgreichen Verteidigung vor dem Wissenschaftsrat und der Bestätigung durch die gemeinsame Wissenschaftskonferenz des Bundes und der Länder stehen der Universität in den Jahren 2015 bis 2020 41,5 Mio. Euro für die Baukosten und die Beschaffung ausgewählter Großgeräte zur Verfügung. Der Forschungsbau, der für Wissenschaftler aller Fakultäten der TU Bergakademie Freiberg offen ist, ermöglicht die strukturelle Bündelung der an der Universität in den Bereichen Hochtemperatur-Prozesse und -Materialien in einzigartiger Weise vorhandenen Kompetenzen. Der Fokus des ZeHS liegt auf der Entwicklung innovativer, ressourcen- und energieeffizienter Technologien im Bereich der Grundstoffindustrie, wobei Prozess- und Materialanforderungen in der Chemischen Industrie, der Metallurgie sowie der Keramik-, Glas- und Baustoffindustrie zusammenhängend betrachtet werden und die Ergebnisse auch auf andere Branchen übertragbar sind.

Im Zeitraum der Jahre 2012 bis 2015 beteiligte sich die TU Bergakademie Freiberg mit einem Antrag für ein \\\"Zentrum für effiziente Hochtemperatur- Stoffwandlung\\\" (ZeHS) am Wettbewerb um eine Förderempfehlung für Forschungsbauten an Hochschulen gemäß Art. 91b GG. Nach der erfolgreichen Verteidigung vor dem Wissenschaftsrat und der Bestätigung durch die gemeinsame Wissenschaftskonferenz des Bundes und der Länder stehen der Universität in den Jahren 2015 bis 2020 41,5 Mio. Euro für die Baukosten und die Beschaffung ausgewählter Großgeräte zur Verfügung. Der Forschungsbau, der für Wissenschaftler aller Fakultäten der TU Bergakademie Freiberg offen ist, ermöglicht die strukturelle Bündelung der an der Universität in den Bereichen Hochtemperatur-Prozesse und -Materialien in einzigartiger Weise vorhandenen Kompetenzen. Der Fokus des ZeHS liegt auf der Entwicklung innovativer, ressourcen- und energieeffizienter Technologien im Bereich der Grundstoffindustrie, wobei Prozess- und Materialanforderungen in der Chemischen Industrie, der Metallurgie sowie der Keramik-, Glas- und Baustoffindustrie zusammenhängend betrachtet werden und die Ergebnisse auch auf andere Branchen übertragbar sind.

Die vorliegende Habilitationsschrift stellt den erreichten Stand der CFD-basierten Modellierung ein- und mehrphasiger Hochtemperaturprozesse dar. Die hierzu vorgelegten Arbeiten umfassen die Hochdruck-Partialoxidation von Erdgas, die Vergasung fester Einsatzstoffe in einem endothermen Flugstromreaktor und in einem mehrstufigen Wirbelschichtprozess sowie die Synthesegasaufbereitung in einem neuen Quenchreaktor. Der Forschungsschwerpunkt reicht dabei von der Entwicklung neuer Korrelationen zur Beschreibung der Strömungskräfte und des Wärmeübergangs basierend auf partikelaufgelösten Rechenmodellen über die Modellierung der thermochemischen Konversion reaktiver Einzelpartikel bis hin zur Berechnung und Optimierung unterschiedlicher Hochtemperaturreaktoren. / This habilitation thesis discusses the state of the art for the CFD modeling of single-phase and multi-phase high-temperature processes. The presented publications comprise the high-pressure partial oxidation of natural gas, the gasification of solid fuels in entrained-flow gasifiers and multi-stage fluidized-bed gasifier as well as the syngas treatment in a new quench reactor. The scientific approach covers the development of new correlations for flow forces and heat transfer based on particle-resolved numerical models, the modeling of the thermochemical conversion of reactive single particles, and the calculation and optimization of different high-temperature processes.

Die vorliegende Habilitationsschrift stellt den erreichten Stand der CFD-basierten Modellierung ein- und mehrphasiger Hochtemperaturprozesse dar. Die hierzu vorgelegten Arbeiten umfassen die Hochdruck-Partialoxidation von Erdgas, die Vergasung fester Einsatzstoffe in einem endothermen Flugstromreaktor und in einem mehrstufigen Wirbelschichtprozess sowie die Synthesegasaufbereitung in einem neuen Quenchreaktor. Der Forschungsschwerpunkt reicht dabei von der Entwicklung neuer Korrelationen zur Beschreibung der Strömungskräfte und des Wärmeübergangs basierend auf partikelaufgelösten Rechenmodellen über die Modellierung der thermochemischen Konversion reaktiver Einzelpartikel bis hin zur Berechnung und Optimierung unterschiedlicher Hochtemperaturreaktoren. / This habilitation thesis discusses the state of the art for the CFD modeling of single-phase and multi-phase high-temperature processes. The presented publications comprise the high-pressure partial oxidation of natural gas, the gasification of solid fuels in entrained-flow gasifiers and multi-stage fluidized-bed gasifier as well as the syngas treatment in a new quench reactor. The scientific approach covers the development of new correlations for flow forces and heat transfer based on particle-resolved numerical models, the modeling of the thermochemical conversion of reactive single particles, and the calculation and optimization of different high-temperature processes.

Slags plays a significant role at high temperature processes. The estimation of the slag viscosity is vital for the safe run of e.g. entrained flow gasifiers. One opportunity of determination is rotational viscometry. This technique is disadvantageous in view of elevated temperatures, applied materials and the necessary time. Additionally, the viscosity can be predicted by the help of viscosity models, where viscosity is a function of slag composition and temperature. Due to changing slag properties within the technical processes, the calculated viscosities can hugely differ from measured ones. In this work, the viscosities of 42 slags where measured up to 100 Pa s and temperatures up to 1700 °C. Oxidizing and reducing conditions were applied. Additionally, selected slag samples were quenched at defined temperatures to qualitatively and quantitatively determine the formed minerals by X-ray diffraction (XRD). Differential temperature analysis (DTA) was applied to find the onset of crystallization for the complementation of investigations. The Einstein-Roscoe equation was chosen to improve the classic viscosity models. Reducing atmosphere decreased viscosity and the number of formed minerals was increased. Slags show a shear-thinning behavior above ca. 10 vol.-% of solid mineral matter. Also, Newtonian behavior was observed up to 60 vol.-%. To overcome problems with the kinetic cooling behavior of the slags, a viscosity approximation method was applied afterwards. This can result in optimized viscosity predictions when several preconditions are fulfilled.

Slags plays a significant role at high temperature processes. The estimation of the slag viscosity is vital for the safe run of e.g. entrained flow gasifiers. One opportunity of determination is rotational viscometry. This technique is disadvantageous in view of elevated temperatures, applied materials and the necessary time. Additionally, the viscosity can be predicted by the help of viscosity models, where viscosity is a function of slag composition and temperature. Due to changing slag properties within the technical processes, the calculated viscosities can hugely differ from measured ones. In this work, the viscosities of 42 slags where measured up to 100 Pa s and temperatures up to 1700 °C. Oxidizing and reducing conditions were applied. Additionally, selected slag samples were quenched at defined temperatures to qualitatively and quantitatively determine the formed minerals by X-ray diffraction (XRD). Differential temperature analysis (DTA) was applied to find the onset of crystallization for the complementation of investigations. The Einstein-Roscoe equation was chosen to improve the classic viscosity models. Reducing atmosphere decreased viscosity and the number of formed minerals was increased. Slags show a shear-thinning behavior above ca. 10 vol.-% of solid mineral matter. Also, Newtonian behavior was observed up to 60 vol.-%. To overcome problems with the kinetic cooling behavior of the slags, a viscosity approximation method was applied afterwards. This can result in optimized viscosity predictions when several preconditions are fulfilled.:List of Tables ............................................................................................................ vi List of Figures ........................................................................................................ viii Symbols and Abbreviations .................................................................................. xviii 1. Introduction and Aim ....................................................................................... 1 2. General Overview of Slag ............................................................................... 2 2.1 Viscosity ...................................................................................................... 2 2.1.1 Viscosity Introduction ........................................................................... 2 2.1.2 Flow behavior of fluids ......................................................................... 3 2.2 Slag Definition and Phase Diagrams ........................................................... 4 2.3 Solid Slag Structure .................................................................................... 5 2.4 Liquid Slag Structure ................................................................................. 10 2.5 Basicity and B/A-ratio ................................................................................ 11 2.6 Slag Components...................................................................................... 13 2.6.1 Silicon dioxide .................................................................................... 13 2.6.2 Aluminum oxide ................................................................................. 13 2.6.3 Calcium oxide .................................................................................... 15 2.6.4 Iron oxide ........................................................................................... 16 2.6.5 Magnesium Oxide .............................................................................. 18 2.6.6 Potassium Oxide ................................................................................ 19 2.6.7 Sodium Oxide .................................................................................... 20 2.6.8 Titanium Oxide ................................................................................... 21 2.6.9 Phosphorous ...................................................................................... 22 2.6.10 Sulfur .............................................................................................. 22 2.7 Summary of Last Chapters ........................................................................ 23 3. Slag Viscosity Toolbox .................................................................................. 25 3.1 Slag Viscosity Predictor............................................................................. 25 3.2 Slag Viscosity Database............................................................................ 26 3.3 Prediction Quality of Viscosity Models ....................................................... 27 4. Classic Slag Viscosity Modelling ................................................................... 30 4.1 Selected Classic Viscosity Models ............................................................ 31 4.1.1 S2 ....................................................................................................... 32 4.1.2 Watt-Fereday ..................................................................................... 32 4.1.3 Bomkamp ........................................................................................... 32 4.1.4 Shaw .................................................................................................. 32 4.1.5 Lakatos .............................................................................................. 33 4.1.6 Urbain ................................................................................................ 33 4.1.7 Riboud ............................................................................................... 33 4.1.8 Streeter .............................................................................................. 34 4.1.9 Kalmanovitch-Frank ........................................................................... 34 4.1.10 BBHLW .......................................................................................... 34 4.1.11 Duchesne ....................................................................................... 34 4.1.12 ANNliq ............................................................................................ 35 4.2 Need of Improvement in Viscosity Literature ............................................. 35 4.3 Summary of Last Chapters ........................................................................ 36 5. Advanced Slag Viscosity Modelling .............................................................. 37 5.1 Crystallization ............................................................................................ 37 5.1.1 Nucleation .......................................................................................... 38 5.1.2 Crystallization Rate ............................................................................ 39 5.1.3 Crystallization Measurement Methods ............................................... 39 5.2 Slag Properties Changes During Crystallization ........................................ 40 5.2.1 Slag Density ....................................................................................... 40 5.2.2 Solid Volume Fraction ........................................................................ 46 5.2.3 Estimation of Slag Composition During Cooling ................................. 46 5.3 Viscosity Depending on Particles and Shear Rate..................................... 47 5.3.1 Einstein-Roscoe Equation .................................................................. 48 5.3.2 Improved Modelling Approach by Modified Einstein-Roscoe .............. 49 5.4 Summary of Last Chapters ........................................................................ 50 6. Experimental Procedures ............................................................................. 52 6.1 Viscosity Measurements ........................................................................... 52 6.1.1 Estimating Parameter Ranges of Viscosity Measurements ................ 53 6.1.2 Viscosity Measurement Procedure ..................................................... 54 6.2 Thermal Analysis of Slags ......................................................................... 55 6.2.1 Experimental Conditions of DTA ........................................................ 55 6.3 Phase Determination ................................................................................. 55 6.3.1 Quench Experiment Processing ......................................................... 56 6.3.2 Phase Determination on XRD Results ............................................... 56 6.4 Summary of Last Chapters ........................................................................ 57 7. Results and Discussion ................................................................................ 58 7.1 Selected Slag Samples ............................................................................. 58 7.1.1 Slag Sample Composition Before Viscosity Measurements ............... 58 7.1.2 Slag Sample Composition After Viscosity Measurements .................. 59 7.2 General Results of Viscosity Measurements ............................................. 60 7.2.1 Viscosity under Air Atmosphere ......................................................... 63 7.2.2 Viscosity under Reducing Atmospheres ............................................. 65 7.2.3 Viscosity under Constant Partial Oxygen Pressure ............................ 66 7.2.4 Summary of Last Chapter .................................................................. 68 7.3 Mineral Formation ..................................................................................... 69 7.3.1 General Results on Primarily Mineral Formation ................................ 69 7.3.2 Influences on Primarily Mineral Formation ......................................... 70 7.3.3 Mineral Formation over Wide Temperature Ranges ........................... 71 7.3.4 Summary of Last Chapter .................................................................. 77 7.4 Results Obtained by DTA .......................................................................... 78 7.4.1 Comparing Results obtained by DTA and Quenching ........................ 80 7.4.2 Summary of Last Chapter .................................................................. 82 7.5 Shear Rate Influence on Slag Viscosity ..................................................... 82 7.5.1 Shear Rate Influence under Oxidizing Atmospheres .......................... 83 7.5.2 Shear Rate Influence under Reducing Atmospheres .......................... 87 7.5.3 Shear Rate Influence under Constant Atmospheres .......................... 91 7.5.4 Summary of chapter ........................................................................... 92 7.6 Atmospheric Influence on Viscosity ........................................................... 93 7.6.1 Summary of Last Chapter .................................................................. 95 7.7 Cooling Rate Influence on Slag Viscosity .................................................. 95 7.7.1 Summary of Last Chapter .................................................................. 97 8. Advanced Viscosity Modelling Approach ...................................................... 99 8.1 Prediction Quality of Classical Viscosity Models ........................................ 99 8.1.1 Selecting the Best Viscosity Model for Newtonian Flow ..................... 99 8.1.2 Summary of Last Chapter ................................................................ 103 8.2 Predicting Liquidus Temperature ............................................................. 103 8.2.1 Comparing Liquidus Calculations and Quenching Experiments ....... 103 8.2.2 Comparing DTA Results and Liquidus Calculations ......................... 105 8.2.3 Summary of Last Chapter ................................................................ 107 8.3 Predicting Liquid Slag Composition ......................................................... 108 8.3.1 Results of Slag Composition Calculations at Oxidizing Conditions ... 108 8.3.2 Results of Slag Composition Calculations at Reducing Conditions ... 110 8.3.3 Summary of Last Chapter ................................................................ 111 8.4 Modelling Approach ................................................................................ 112 8.4.1 Development of Datasets for Advanced Viscosity Modeling ............. 113 8.4.2 Summary of Last Chapter ................................................................ 116 8.5 Results of Advanced Slag Viscosity Modelling Approach ........................ 116 8.5.1 Summary of Last Chapter ................................................................ 121 9. Summary .................................................................................................... 123 10. Appendix: Information on Classic Viscosity Modelling ................................. 126 10.1 Backgrounds of Applied Viscosity Models............................................ 126 10.2 Viscosity Model of the BCURA (S2) ..................................................... 129 10.3 Watt-Fereday ....................................................................................... 130 10.4 Bomkamp ............................................................................................ 130 10.5 Shaw ................................................................................................... 131 10.6 Lakatos Model ..................................................................................... 132 10.7 Urbain Model ....................................................................................... 133 10.8 Riboud Model ...................................................................................... 134 10.9 Streeter Model ..................................................................................... 136 10.10 Kalmanovitch-Frank Model .................................................................. 137 10.11 BBHLW Model ..................................................................................... 137 10.12 Duchesne Model .................................................................................. 139 10.13 ANNliq Model ...................................................................................... 141 11. Appendix: Settings of Equilibrium Calculations ........................................... 143 12. Appendix: Parameters of Einstein-Roscoe Equation ................................... 153 13. Appendix: Ash and Slag Sample Preparation ............................................. 155 14. Appendix: Experimental Procedures: Viscometer ....................................... 159 14.1 General Viscometer Description .......................................................... 159 14.2 Temperature Calibration ...................................................................... 160 14.3 Viscometer Calibration ......................................................................... 160 14.4 Accuracy and Reproducibility of HT-Viscosity Measurements .............. 161 14.5 Influence of Inductive Heating .............................................................. 163 14.6 Influence of Measurement System Materials ....................................... 164 15. Appendix: Experimental Procedures: Quenching Furnace .......................... 167 16. Appendix: Slag Sample Parameters and Composition ................................ 168 17. Appendix: Slag Viscosity Measurements Results ....................................... 175 18. Appendix: Viscosities at Different Cooling Rates ........................................ 182 19. Appendix: Slag Viscosity Modelling: AALE Calculations ............................. 187 20. Appendix: Advanced Viscosity Modelling: a-factors .................................... 193 21. Appendix: Slag Mineral Phase Investigations and Modelling ...................... 197 22. Appendix: Results of DTA Measurements on Slags .................................... 207 23. Appendix: Advanced Slag Viscosity Modelling Approach ............................ 211 References ........................................................................................................... 228