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Master Thesis at Division of Energy Technology Department of Energy and Environment Chalmers University of Technology CFD-modelling of the 400 kWth test kiln at LKAB/MEFOS Supervisor: Robert Johansson; +46317725249, [email protected] Examiner: Klas Andersson; +46317725242, [email protected] The production of iron ore pellets involves sintering of the pellets in order for the pellets to obtain a higher mechanical strength. The sintering is carried out by heating the pellets to a high temperature, around 1250˚C, and in the grate-kiln process this is done in a rotary kiln. The kilns of today are fired with coal and this part of the pelletizing process therefore causes considerable fuel costs and emissions of CO2. There is accordingly a large need for improvements of the energy efficiency of the process, i.e. its fuel consumption, but also an interest in the use of alternative fuels with a lower relative emission of CO2. Any modifications of the process must, however consider the product quality of the pellets. For the sintering this means that any changes of the kiln or the combustion in it must be made with consideration of the heat transfer from the flame to the pellets. Tests of process modifications in a full scale process are extremely costly and most R&D is therefore carried out on smaller scale test rigs and/or with modelling. Computational Fluid Dynamics (CFD) is here regarded as one of the key tools to understand the combustion and heat transfer in the kiln. This master thesis is an initial study of the use of CFD modelling as a tool to investigate how the combustion in the kiln is affected by co-combustion of biomass and coal, fuel properties, air flow, air temperature etc. Focus will be put on heat transfer effects and especially the radiative heat transfer which is of most importance for the high temperatures in the kiln. The task involves modelling of pulverized biomass and coal combustion in the 400 kWth test kiln at LKAB/MEFOS for which there exist significant experimental data. The whole combustion process, including drying, devolatilisation and char burnout will be modelled. The aim is to identify suitable submodels and areas where there is a need for further developments of modelling strategies. The modelling will be carried out with ANSYS/FLUENT and is suitable for one or two students who have interest and/or experience of this tool. a) b) Figure 1: a) The burner side of the test kiln, b) inside the kiln looking towards the burner.