Follow
Andreas Richter
Title
Cited by
Cited by
Year
Drag forces and heat transfer coefficients for spherical, cuboidal and ellipsoidal particles in cross flow at sub-critical Reynolds numbers
A Richter, PA Nikrityuk
International Journal of Heat and Mass Transfer 55 (4), 1343-1354, 2012
1952012
New correlations for heat and fluid flow past ellipsoidal and cubic particles at different angles of attack
A Richter, PA Nikrityuk
Powder technology 249, 463-474, 2013
872013
Heat and mass transfer within thermogravimetric analyser: From simulation to improved estimation of kinetic data for char gasification
S Schulze, P Nikrityuk, Z Abosteif, S Guhl, A Richter, B Meyer
Fuel 187, 338-348, 2017
562017
Three-dimensional calculation of a chemically reacting porous particle moving in a hot O2/CO2 atmosphere
A Richter, PA Nikrityuk, B Meyer
International Journal of Heat and Mass Transfer 83, 244-258, 2015
532015
Novel intrinsic-based submodel for char particle gasification in entrained-flow gasifiers: Model development, validation and illustration
S Schulze, A Richter, M Vascellari, A Gupta, B Meyer, PA Nikrityuk
Applied Energy 164, 805-814, 2016
512016
Numerical Investigation of a Chemically Reacting Carbon Particle Moving in a Hot O2/CO2 Atmosphere
A Richter, PA Nikrityuk, M Kestel
Industrial & Engineering Chemistry Research 52 (16), 5815-5824, 2013
412013
Numerical study on entrained-flow gasification performance using combined slag model and experimental characterization of slag properties
D Safronov, T Förster, D Schwitalla, P Nikrityuk, S Guhl, A Richter, ...
Fuel Processing Technology 161, 62-75, 2017
382017
Detailed analysis of reacting particles in an entrained-flow gasifier
A Richter, M Vascellari, PA Nikrityuk, C Hasse
Fuel Processing Technology 144, 95-108, 2016
382016
Drag coefficient and Nusselt number for porous particles under laminar flow conditions
K Wittig, P Nikrityuk, A Richter
International Journal of Heat and Mass Transfer 112, 1005-1016, 2017
332017
Numerical and experimental study of heavy oil gasification in an entrained-flow reactor and the impact of the burner concept
A Bader, M Hartwich, A Richter, B Meyer
Fuel Processing Technology 169, 58-70, 2018
292018
A fixed-grid model to track the interface and porosity of a chemically reacting moving char particle
F Dierich, A Richter, P Nikrityuk
Chemical Engineering Science 175, 296-305, 2018
262018
A large-scale benchmark for the CFD modeling of non-catalytic reforming of natural gas based on the Freiberg test plant HP POX
A Richter, P Seifert, F Compart, P Tischer, B Meyer
Fuel 152, 110-121, 2015
262015
Particle-resolved numerical study of char conversion processes in packed beds
S Schulze, P Nikrityuk, F Compart, A Richter, B Meyer
Fuel 207, 655-662, 2017
252017
Performance of different optimization concepts for reactive flow systems based on combined CFD and response surface methods
P Rößger, A Richter
Computers & Chemical Engineering 108, 232-239, 2018
242018
CFD-based multi-objective optimization of a quench reactor design
K Uebel, P Rößger, U Prüfert, A Richter, B Meyer
Fuel Processing Technology 149, 290-304, 2016
232016
Three‐dimensional modeling of porosity development during the gasification of a char particle
K Wittig, PA Nikrityuk, S Schulze, A Richter
AIChE Journal 63 (5), 1638-1647, 2017
202017
In-situ investigation of single particle gasification in a defined gas flow applying TGA with optical measurements
F Küster, P Nikrityuk, M Junghanns, S Nolte, A Tünnermann, ...
Fuel 194, 544-556, 2017
202017
Stabilized discontinuous Galerkin methods for flow–sound interaction
A Richter, J Stiller, R Grundmann
Journal of Computational Acoustics 15 (01), 123-143, 2007
172007
LES simulation of char particle gasification at Reynolds numbers up to 1000
S Kriebitzsch, A Richter
Combustion and Flame 211, 185-194, 2020
162020
3D numerical study of the performance of different burner concepts for the high-pressure non-catalytic natural gas reforming based on the Freiberg semi-industrial test facility …
T Förster, Y Voloshchuk, A Richter, B Meyer
Fuel 203, 954-963, 2017
162017
The system can't perform the operation now. Try again later.
Articles 1–20