Hydrodynamics and Mass-Transfer Studies in a Pilot-Plant Airlift Reactor:  Non-Newtonian Systems

1998 ◽  
Vol 37 (1) ◽  
pp. 41-48 ◽  
Author(s):  
W. A. Al-Masry ◽  
A. R. Dukkan
2005 ◽  
Vol 192 (1) ◽  
pp. 108-124 ◽  
Author(s):  
Khosrow Rostami ◽  
Wenge Fu ◽  
Murray Moo-Young

Clean Energy ◽  
2019 ◽  
Vol 3 (4) ◽  
pp. 263-277
Author(s):  
James Coker ◽  
Daniel Boafo Afari ◽  
Jessica Narku-Tetteh ◽  
Raphael Idem

Abstract Mass-transfer studies of catalyst-aided CO2 absorption and desorption were performed in a full-cycle, bench-scale pilot plant to improve CO2 absorption using 5M MEA, 5M MEA-2M MDEA and 2M BEA-2M AMP. A solid-base catalyst, K/MgO, and an acid catalyst, HZSM-5, were used to facilitate absorption and desorption, respectively. Absorption and desorption mass-transfer performance was presented in terms of the overall mass-transfer coefficient of the gas side (KGav) and liquid side (KLav), respectively. For non-catalytic runs, the highest KGaV and KLaV were 0.086 Kmolm3.kPa.hr  and 0.785 1hr for 2M BEA-2M AMP solvent. The results showed 38.7% KGav and 23.6% KLav increase for 2M BEA-2M AMP with only HZSM-5 catalyst in desorber and a 95% KGaV and 45% KLaV increase for both K/MgO catalyst and HZSM-5 catalyst. This was attributed to the role of K/MgO in bonding loosely with CO2 and making it available for the amine reaction.


2015 ◽  
Vol 103 ◽  
pp. 1-11 ◽  
Author(s):  
A.A. Harraz ◽  
I.A. El Gheriany ◽  
M.H. Abdel-Aziz ◽  
T.M. Zewail ◽  
A.H. Konsowa ◽  
...  

1994 ◽  
Vol 33 (3) ◽  
pp. 647-656 ◽  
Author(s):  
M. Henriques de Brito ◽  
U. von Stockar ◽  
A. Menendez Bangerter ◽  
P. Bomio ◽  
M. Laso

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