Environmental Engineering Reference
In-Depth Information
can adsorb at very low partial pressures. At present, two types of
processes are proposed:
Adsorption into highly alkaline solutions (see Box 11.3.3 ) [11.10]
Adsorption onto solids [11.11,11.12]
The design of fl ue gas capture processes requires capture of 90% of
the inlet CO 2 ; Direct Air Capture processes, however, are not subject to
Box 11.3. 3 Carbon capture with sodium hydroxide
In Chapter 5, we saw that adding a base to water will signifi cantly enhance the CO 2
solubility in the mixture because of the reaction of CO 2 with the hydroxide:
CO 2 +
NaOH
Na 2 CO 3
+
H 2 O
This is a very exothermic reaction that is effi cient in capturing very small concentra-
tions of CO 2 . The idea is to use this process to capture CO 2 directly from the air.
Similar to capturing CO 2 from fl ue gasses using absorption, we need to regenerate
the solvent and compress the CO 2 for, say, geological sequestration.
The regeneration of sodium carbonate into sodium hydroxide is called caus-
ticization and is a well-known industrial process. The process involves three steps.
First, Na 2 CO 3 is reacted with lime, Ca(OH) 2 , to form NaOH and lime mud (CaCO 3 ):
Na 2 CO 3
+
Ca(OH) 2
2NaOH
+
CaCO 3
H 100°C =
5.3 kJ/mol CO 2
The calcium carbonate precipitates in this reaction and is subsequently calcined
(heated with air) to recover the CO 2 :
CaCO 3
CaO(s)
+
CO 2
H 900°C
=
179 kJ/mol CO 2
The CaO is converted back to Ca(OH) 2 through quicklime hydration:
CaO(s)
+
H 2 O
Ca(OH) 2 ,
H 100°C =
−65 kJ/mol CO 2
The enthalpy of absorption of CO 2 from air into sodium hydroxide solution for a 1 M
solution at standard conditions is -109.4 kJ/mol CO 2 . Hence, the minimum energy
to recover the CO 2 is also 109.4 kJ/mol CO 2 . We see that the calcination step
already takes 179 kJ/mol CO 2 , which indicates that the required energy for conven-
tional causticization is far beyond the thermodynamic minimum. Therefore, this
process consumes a large amount of energy.
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