| 1 |
Efficiency-based nonequilibrium modeling of industrial-scale multicomponent distillation columns
Poortalari H, Sabet JK, Varaminian F
Separation Science and Technology, 52(11), 1885, 2017 |
| 2 |
Comparison of equilibrium and non-equilibrium models of a tray column for post-combustion CO2 capture using DEA-promoted potassium carbonate solution
Borhani TNG, Akbari V, Afkhamipour M, Abd Hamid MK, Manan ZA
Chemical Engineering Science, 122, 291, 2015 |
| 3 |
Simple and rapid determination of effective Murphree component efficiencies for operating absorbers, strippers and distillation columns filled with any type of trays
Sadeghifar H
Separation and Purification Technology, 139, 104, 2015 |
| 4 |
Simulation and analysis of dehydration distillation column based on distillation mechanism integrated with neural network
Sun Q, Pan C, Yan X
Korean Journal of Chemical Engineering, 30(3), 518, 2013 |
| 5 |
Modeling of existing cooling towers in ASPEN PLUS using an equilibrium stage method
Queiroz JA, Rodrigues VMS, Matos HA, Martins FG
Energy Conversion and Management, 64, 473, 2012 |
| 6 |
Modeling of Mass Transfer in Nonideal Multicomponent Mixture with Maxwell-Stefan Approach
Song YM, Song JR, Gong M, Cao B, Yang YH, Ma XX
Chinese Journal of Chemical Engineering, 18(3), 362, 2010 |
| 7 |
Simulation of continuous physical refiners for edible oil deacidification
Ceriani R, Meirelles AJA
Journal of Food Engineering, 76(3), 261, 2006 |
| 8 |
The parastillation efficiency and hydrodynamic behaviour
Belincanta J, Ravagnani TMK, Pereira JAF
Canadian Journal of Chemical Engineering, 83(3), 582, 2005 |
| 9 |
Calculating distillation efficiencies of multicomponent i-butane/n-butane column
Ilme J, Klemola K, Aittamaa J, Nystrom L
Chemical Engineering Communications, 184, 1, 2001 |
| 10 |
회분식 증류탑을 이용한 아세톤-메탄올-2-프로판올계의 농도분포 및 Murphree 효율
김정근, 김석종, 주동표
HWAHAK KONGHAK, 36(4), 502, 1998 |
