| 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 |
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 |
| 3 |
Predicting flows from the Dynamic Ergun Equation
Tupper GB, Govender I, Mainza AN
Minerals Engineering, 103, 11, 2017 |
| 4 |
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 |
| 5 |
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 |
| 6 |
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 |
| 7 |
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 |
| 8 |
Methods for in-situ porosity determination of moving porous columns and application to horizontal slug flow pneumatic conveying
Lecreps I, Orozovic O, Eisenmenger M, Jones MG, Sommer K
Powder Technology, 253, 710, 2014 |
| 9 |
Non-Darcy Flow of Water Through a Packed Column Test
Sedghi-Asl M, Rahimi H, Salehi R
Transport in Porous Media, 101(2), 215, 2014 |
| 10 |
Investigation on interface resistance between alternating layers in the upper of blast furnace
Liu JZ, Xue QG, She XF, Wang JS
Powder Technology, 246, 73, 2013 |
