| 1 |
The implications of choice between sour and sweet shift on process design and operation of an IGCC power plant integrated with a dual-stage selexol unit
Zhang YX, Ahn H
Energy, 173, 1273, 2019 |
| 2 |
Evaluation of a dense skin hollow fiber gas-liquid membrane contactor for high pressure removal of CO2 from syngas using Selexol as the absorbent
Belaissaoui B, Favre E
Chemical Engineering Science, 184, 186, 2018 |
| 3 |
Ejector integration for the cost effective design of the Selexol (TM) process
Ashrafi O, Bashiri H, Esmaeili A, Sapoundjiev H, Navarri P
Energy, 162, 380, 2018 |
| 4 |
Removal of carbon dioxide from pressurized landfill gas by physical absorbents using a hollow fiber membrane contactor
Li YF, Wang L, Jin PR, Song X, Zhan XY
Chemical Engineering and Processing, 121, 149, 2017 |
| 5 |
The quantitative evaluation of two-stage pre-combustion CO2 capture processes using the physical solvents with various design parameters
Park SH, Lee SJ, Lee JW, Chun SN, Bin Lee J
Energy, 81, 47, 2015 |
| 6 |
Carbon dioxide capture by single droplet using Selexol, Rectisol and water as absorbents: A theoretical approach
Chen WH, Chen SM, Hung CI
Applied Energy, 111, 731, 2013 |
