scholarly journals Mathematical modeling and validation of CO2 mass transfer in a membrane contactor using ionic liquids for pre-combustion CO2 capture

2017 ◽  
Vol 123 ◽  
pp. 377-387 ◽  
Author(s):  
Muhammad Usman ◽  
Zhongde Dai ◽  
Magne Hillestad ◽  
Liyuan Deng
2020 ◽  
Vol 99 ◽  
pp. 103076 ◽  
Author(s):  
Qazi Sohaib ◽  
Jose Manuel Vadillo ◽  
Lucía Gómez-Coma ◽  
Jonathan Albo ◽  
Stéphanie Druon-Bocquet ◽  
...  

Membranes ◽  
2021 ◽  
Vol 11 (4) ◽  
pp. 271
Author(s):  
Akrivi Asimakopoulou ◽  
Dimitrios Koutsonikolas ◽  
Georgia Kastrinaki ◽  
George Skevis

CO2 mineralization is an alternative to conventional geological storage and results in permanent carbon storage as a solid, with no need for long-term monitoring and no requirements for significant energy input. Novel technologies for carbon dioxide capture and mineralization involve the use of gas-liquid membrane contactors for post-combustion capture. The scope of the present study is to investigate the application of hollow fiber membrane contactor technology for combined CO2 capture from energy-intensive industry flue gases and CO2 mineralization, in a single-step multiphase process. The process is also a key enabler of the circular economy for the cement industry, a major contributor in global industrial CO2 emissions, as CaCO3 particles, obtained through the mineralization process, can be directed back into the cement production as fillers for partially substituting cement in high-performance concrete. High CO2 capture efficiency is achieved, as well as CaCO3 particles of controlled size and crystallinity are synthesized, in every set of operating parameters employed. The intensified gas-liquid membrane process is assessed by calculating an overall process mass transfer coefficient accounting for all relevant mass transfer resistances and the enhanced mass transfer due to reactive conditions on the shell side. The obtained nanocomposite particles have been extensively characterized by DLS, XRD, TGA, SEM, TEM, and FTIR studies, revealing structured aggregates (1–2 μm average aggregate size) consisting of cubic calcite when the contactor mode is employed.


2020 ◽  
Vol 223 ◽  
pp. 115719 ◽  
Author(s):  
Qazi Sohaib ◽  
Jose Manuel Vadillo ◽  
Lucía Gómez-Coma ◽  
Jonathan Albo ◽  
Stéphanie Druon-Bocquet ◽  
...  

2019 ◽  
Vol 95 (7) ◽  
pp. 1844-1857 ◽  
Author(s):  
Sohaib Qazi ◽  
Lucía Gómez‐Coma ◽  
Jonathan Albo ◽  
Stéphanie Druon‐Bocquet ◽  
Angel Irabien ◽  
...  

2012 ◽  
Vol 44 ◽  
pp. 557-558 ◽  
Author(s):  
L.A. Neves ◽  
C.A.M. Afonso ◽  
I.M. Coelhoso ◽  
J.G. Crespo

2021 ◽  
Vol 294 ◽  
pp. 06004
Author(s):  
Yichen Liu

This study investigates the removal efficiency of carbon dioxide by aqueous absorbents containing monoethanolamine (MEA), piperazine(PZ), diethylenetriamine(DETA) and ionic liquids in a rotating packed bed. The performance of an absorbent was assessed in terms of an overall volumetric mass transfer coefficient and regeneration heat duty. The CO2 removal efficiency in a rotating packed bed was observed to be more suitable than that in a packed column, suggesting a potential of a rotating packed bed can replace a traditional packed column to the usage of reduction of the greenhouse gas CO2 from the exhausted gas. The mixture containing PZ and DETA exhibited a high CO2 removal efficiency among these absorbents. Besides, DETA has a lower regeneration heat duty than MEA, which means the finest mixture for industrial CO2 capture system will be the combination of PZ, DETA, and ionic liquids, instead of traditional alkanolamines, MEA.


2014 ◽  
Vol 63 ◽  
pp. 773-780 ◽  
Author(s):  
Nan Yang ◽  
Hai Yu ◽  
Dong–yao Xu ◽  
William Conway ◽  
Marcel Maeder ◽  
...  

Sign in / Sign up

Export Citation Format

Share Document