Abstract:
The effects of coexistent gaseous components and fine particles on the CO
2 separation performance by polydimethylsiloxane/polysulfon (PDMS-PSF) flat sheet composite membranes were investigated in a simulated test-bed. It can be found that O
2 slightly inhibits the CO
2 separation performance, while the effect of SO
2 is negligible during the test time due to its low concentration in the flue gas. Water vapor promotes the CO
2 separation performance of PDMS-PSF composite membranes. The fly ash fine particles significantly deteriorate the CO
2 separation performance of PDMS-PSF membranes. Moreover, the CO
2 separation experiments by PDMS-PSF membranes with an actual flue gas from a desulfurization system of the coal-fired hot testing facility were conducted for 50 h. At the beginning, the CO
2 separation performance is slightly improved due to the combined effect of water vapor, O
2 and SO
2. With the extension of the test time, the impact of the fine particles deposited on the membrane surface increases, which gradually deteriorates the CO
2 separation performance of PDMS-PSF membrane. The CO
2/N
2 selectivity and the CO
2 permeation rate are decreased by 17.91% and 28.21%, respectively.