Modelling reactive absorption of CO2 in packed columns for post-combustion carbon capture applications

2011 ◽  
Vol 89 (9) ◽  
pp. 1600-1608 ◽  
Author(s):  
F.M. Khan ◽  
V. Krishnamoorthi ◽  
T. Mahmud
2009 ◽  
Vol 146 (3) ◽  
pp. 362-369 ◽  
Author(s):  
Jan F. Maćkowiak ◽  
Andrzej Górak ◽  
Eugeny Y. Kenig

2017 ◽  
Vol 62 ◽  
pp. 100-112 ◽  
Author(s):  
Mathias Leimbrink ◽  
Stephen Tlatlik ◽  
Sonja Salmon ◽  
Anna-Katharina Kunze ◽  
Timo Limberg ◽  
...  

2020 ◽  
Vol 1000 ◽  
pp. 318-323
Author(s):  
Muharam Yuswan ◽  
Hamzah ◽  
Ramadhany Muhammad Audry

Carbon capture storage provides an alternative to reducing global warming. In order to reduce the cost of carbon capture storage, high mass transfer packings for CO2 absorption from flue gas is an alternative. The study modeled and numerically simulated CO2 absorption by monoethanolamine solution with super mini ring contactor. The model considered the effect of the mass and momentum transfers, as well the chemical reaction. The simulation results show that the driving force of the reactive absorption is higher than the ordinary absorption in term of the low concentration of CO2 in the liquid phase. The CO2 concentration in the bulk gas is approximately 7.56 mol/m3. It decreases to around 5.75 mol/m3 after crossing the concentration boundary layer.


2021 ◽  
Author(s):  
Dan Vasiliu ◽  
Elmar Kessler ◽  
Erik von Harbou ◽  
Hans Hasse

A new short-cut method (NoVa) for assessing solvents for gas cleaning by reactive absorption is presented. It considers the absorption / desorption cycle using the assumption of infinite number of stages in both columns. For a given feed and removal rate, the method yields an estimate for the specific regeneration energy q as a function of the solvent circulation rate L/G. The sole solvent-dependent input consists of two correlations describing the gas solubility at absorber and desorber conditions and estimates of caloric properties. Furthermore, a simple equation (SolSOFT) for correlating the gas solubility as a function of the gas loading of the solvent is presented. A theoretical analysis of the process reveals general properties of the dependency of q on L/G. The NoVa method is described and tested using amine-based solvents for post combustion carbon capture as examples.


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