Environmental Engineering Reference
In-Depth Information
Table 9.3.3 Distribution of energy requirements of methanol production.
H 2 production: equivalent thermal
CCS: equivalent thermal energy requirement
energy requirement for 3 moles of H 2
for 1 mole of CO 2
Method
kJ
method
kJ
Cu-Cl cycle
1759
Na 2 CO 3 -based
353.0
1759
K 2 CO 3 -based
363.8
1759
CaO-based
440.4
1759
MEA-based
412.0
Water electrolysis
2147
Na 2 CO 3 -based
353.0
2147
K 2 CO 3 -based
363.8
2147
CaO-based
440.4
2147
MEA-based
412.0
Figure 9.3.1 Percentage of CO 2 capture energy in the synthesis of methanol production.
by hydrogen preparation accounts for the majority of energy cost in the methanol
production process.
As Reaction 9.3.4 can be self-sustained and the solar reactors for hydrogen pro-
duction have been presented in the hydrogen production section of the chapter, this
section will focus on the reactors for CO 2 capture, particularly the extraction of solid
carbonates from the aqueous solution and the release of CO 2 from the carbonates or
sorbents. As the carbonation and calcination operations are very mature in industry,
 
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