The potential of hybrid membranes as a CO
2 capture technology for integrated gasification combined cycleapplications
was evaluated. Commercial
-alumina supports
were modified
with a variety of trichlorosilanesintended to enhance the surface adsorption of CO
2. The resulting hybrids
were characterized using X-rayphotoelectric spectroscopy and Fourier transform infrared spectroscopy and tested for performance in theseparation of He and CO
2. The silanization temperature
was determined to be important because membranesfabricated at 273 K had substantially different performance properties than those fabricated at room temperature.Specifically, the permeances of membranes modified
with alkyltrichlorosilanes at reduced temperatures
were1-2 orders of magnitude higher than those of membranes fabricated at room temperature, and the selectivitiesof these lo
w-temperature silanized membranes
were relatively similar to those expected from Knudsen diffusion.Supports modified
with silanes containing one of a variety of functionalities
were tested for CO
2/He selectivity.Membranes modified
with 2-acetoxyethyl, 2-carbomethoxyethyl, and 3-aminopropyl groups exhibited CO
2selectivity,
with the highest values approaching 7 for 2-carbomethoxyethyl-silated membranes at 50
C.Temperature dependences resulted in selectivity maxima for the 2-acetoxyethyl and 2-carbomethoxyethylmembranes. Mixed-gas selectivities
were slightly higher than pure-gas selectivities because of a decrease inHe permeance
with a relatively minor reduction in CO
2 permeance. Transport in the selective membranes isbelieved to occur by a combination of activated and solution diffusion for He and a combination of activatedand surface diffusion for CO
2.