I'm currently trying to simulate Carbon Engineering's direct air capture process. I'm using this paper as reference.
Right now, I'm trying to react 2KOH + CO2 -> K2CO3 + H2O using the absorber. In the literature, they state that 63.5 % of CO2 in the incoming flue gas flow is absorbed by the aqueous KOH solution with an absorption column.
My results are way off from expected values and I'm not sure exactly where I can fix it. The model converges.
I'm currently trying to simulate Carbon Engineering's direct air capture process. I'm using this paper as reference.
Right now, I'm trying to react 2KOH + CO2 -> K2CO3 + H2O using the absorber. In the literature, they state that 63.5 % of CO2 in the incoming flue gas flow is absorbed by the aqueous KOH solution with an absorption column.
My results are way off from expected values and I'm not sure exactly where I can fix it. The model converges.
I'm sorry, but the absorption column doesn't support reactive absorption.
Regards,
Daniel
Are there any alternatives within DWSIM to simulate my process?
you could try a chemsep column, but I don't know if it supports KOH and K2CO3.
Hello Daniel, even for MEA solution?