Modeling of a bubble column for CO2 removal by absorption with NaOH

被引:3
|
作者
Michelson, Johan [1 ]
Maki-Arvela, Paivi [1 ]
Rajala, Pasi [2 ]
Hallapuro, Markus [2 ]
Schmid, Daniel [1 ]
Karlstrom, Oskar [1 ,3 ]
Warna, Johan [1 ]
Murzin, Dmitry Yu [1 ]
机构
[1] Abo Akad Univ, Johan Gadolin Proc Chem Ctr, Turku 20500, Finland
[2] TM Syst Finland Oy, Turku, Finland
[3] Univ Turku, Dept Mech & Mat Engn, Ind Engn & Management, Turku, Finland
关键词
CO2; removal; NaOH; absorption isotherm; pH dependence; modelling; bubble column; CARBON-DIOXIDE CAPTURE; MASS-TRANSFER; CHEMISORPTION;
D O I
10.1080/00986445.2023.2261105
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
CO2 capture experiments were carried out in a small-scale bubble column reactor using alkaline solutions of sodium hydroxide. The results of the experiments show that a higher NaOH content in the liquid phase and elevated CO2 concentrations in the gas mixture led to a higher CO2 removal efficiency. A mathematical model was developed to describe the CO2 absorption as a function of CO2 gas inlet and OH- concentrations at low CO2 and OH- concentrations. The CO2 uptake at high OH- concentrations (high pH) was accurately predicted by the model, whereas the CO2 uptake at lower OH- concentrations could not be predicted with the same accuracy.
引用
收藏
页码:571 / 581
页数:11
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