Membranes could be an integral part of the post-combustion capture of CO
2 from the effluent gas stream of coal-fired power plants. The objective of this work is to design polymeric membranes that have very high CO
2 permeability and high selectivity toward CO
2 (i.e. very low H
2 and N
2 permeability). It is our hypothesis that the favorable thermodynamic interactions that enable certain polymers to dissolve in dense CO
2 at extremely high pressure will also allow membranes composed of these polymers to exhibit high CO
2 permeability and CO
2 selectivity at low pressure. (These polymeric membranes have recently been assessed for the pre-combustion capture of CO
2 from a CO
2- and H
2-rich shifted gasifier stream).
The crosslinked polymeric membranes used in this study of post-combustion capture of CO2 from a N2-rich stream have been previously assessed and shown promise for the pre-combustion separation of CO2 from a H2-rich shifted fuel gas stream. Candidates include either (a) CO2-philic polymers with linear repeat units such as poly(ethylene glycol) (PEG), polytrimethylene ether glycol (i.e. linear polypropyleneglycol), and polytetramethylene glycol ether (i.e. linear polybutylene glycol), or (b) CO2-philic polymers with branched repeat units such as polypropyleneglycol and polybutylene glycol. Results of mixed gas permeability and selectivity values for CO2/N2 gas pairs will be discussed, and the performance of membranes with linear and branched repeat units will be contrasted.