1 |
Impact of increased power plant cycling on the oxidation and corrosion of coal-fired superheater materials Abang R, Weiss S, Krautz HJ Fuel, 220, 521, 2018 |
2 |
Combustion measurements of type-1 pulverized coal flames operating under oxy-fired conditions da Silva RC, Krautz HJ Fuel Processing Technology, 171, 232, 2018 |
3 |
Quantitative and qualitative relationship between swirl burner operatingconditions and pulverized coal flame length Katzer C, Babul K, Klatt M, Krautz HJ Fuel Processing Technology, 156, 138, 2017 |
4 |
Flame pattern, temperatures and stability limits of pulverized oxy-coal combustion da Silva RC, Kangwanpongpan T, Krautz HJ Fuel, 115, 507, 2014 |
5 |
Heat-transfer from horizontal tube bundles into fluidized beds with Geldart A lignite particles Lechner S, Merzsch M, Krautz HJ Powder Technology, 253, 14, 2014 |
6 |
Heat-transfer from single horizontal tubes in fluidized beds: Influence of tube diameter, moisture and diameter-definition by Geldart C fines content Merzsch M, Lechner S, Krautz HJ Powder Technology, 235, 1038, 2013 |
7 |
A comparative study of different CFD-codes for numerical simulation of gas-solid fluidized bed hydrodynamics Herzog N, Schreiber M, Egbers C, Krautz HJ Computers & Chemical Engineering, 39, 41, 2012 |
8 |
Prediction of oxy-coal combustion through an optimized weighted sum of gray gases model Kangwanpongpan T, da Silva RC, Krautz HJ Energy, 41(1), 244, 2012 |
9 |
New correlations for the weighted-sum-of-gray-gases model in oxy-fuel conditions based on HITEMP 2010 database Kangwanpongpan T, Franca FHR, da Silva RC, Schneider PS, Krautz HJ International Journal of Heat and Mass Transfer, 55(25-26), 7419, 2012 |
10 |
Influence of two- and three-dimensional simulations on bubble behavior in gas-solid fluidized beds with and without immersed horizontal tubes Asegehegn TW, Schreiber M, Krautz HJ Powder Technology, 219, 9, 2012 |