| 1 |
Gaseous flow through coarse granular beds: The role of specific surface area
Buchwald T, Schmandra G, Schutzenmeister L, Fraszczak T, Mutze T, Peuker U
Powder Technology, 366, 821, 2020 |
| 2 |
Fluid flow through 3D-printed particle beds: a new technique for understanding, validating, and improving predictability of permeability from empirical equations
Gjengedal S, Brotan V, Buset OT, Larsen E, Berg OA, Torsaeter O, Ramstad RK, Hilmo BO, Frengstad BS
Transport in Porous Media, 134(1), 1, 2020 |
| 3 |
Estimating pressure drop and Ergun/Forchheimer parameters of flow through packed bed of spheres with large particle diameters
Amiri L, Ghoreishi-Madiseh SA, Hassani FP, Sasmito AP
Powder Technology, 356, 310, 2019 |
| 4 |
An Equivalent Spherical Particle System to Describe Characteristics of Flow in a Dense Packing of Non-spherical Particles
Guo PJ, Stolle D, Guo SX
Transport in Porous Media, 129(1), 253, 2019 |
| 5 |
Predicting flows from the Dynamic Ergun Equation
Tupper GB, Govender I, Mainza AN
Minerals Engineering, 103, 11, 2017 |
| 6 |
Determination of pressure drop for air flow through sintered metal porous media using a modified Ergun equation
Zhong W, Xu K, Li X, Liao YX, Tao GL, Kagawa T
Advanced Powder Technology, 27(4), 1134, 2016 |
| 7 |
Dry pressure drop in spiral wound wire mesh pads at low and elevated pressures
Setekleiv AE, Svendsen HF
Chemical Engineering Research & Design, 109, 141, 2016 |
| 8 |
Assessment of porosity and biofilm thickness in packed beds using porous media models
Dumont E, Woudberg S, Van Jaarsveld J
Powder Technology, 303, 76, 2016 |
| 9 |
Validation of a novel open-source work-flow for the simulation of packed-bed reactors
Boccardo G, Augier F, Haroun Y, Ferre D, Marchisio DL
Chemical Engineering Journal, 279, 809, 2015 |
| 10 |
Effect of material type and particle size distribution on pressure drop in packed beds of large particles: Extending the Ergun equation
Koekemoer A, Luckos A
Fuel, 158, 232, 2015 |
