Various conditions under which the hollow fiber membrane separation system would be the optimal selection are investigated in terms of cost effectiveness. Numerical simulation is carried out to examine the effects of different configurations such as single-stage, two-stage and three-stage CO2 separation processes. In particular, the hollow fiber membrane processes for CO2 separation with vacuum pumps, heat exchangers, coolers and compressors to provide
pressurized feed streams are analyzed. Operating costs are evaluated and compared numerically for the processes with and without recycle streams to compare feasibility for commercial implementation while maintaining the purity and recovery ratio as high as possible.
Choi SH, Kim JH, Kim BS, Lee SB, Lee YT, Theories and Applications of Chem. Eng., 14(1), 298, 2008
Park HB, Jung CH, Lee YM, Hill AJ, Pas SJ, Mudie ST, Wagner EV, Freeman BD, Cookson DJ, Science., 318, 254, 2007
Choi SH, Kim JH, Kim BS, Lee SB, Membr. J., 15, 310, 2005
Hendriks CA, Wildenborg AFB, Blok K, Floris F, van Wees JD, In paper presented at the 5th International Conference on Greenhouse Gas Control Technologies (GHGT-5), 2000
van der Sluijs JP, Hendriks CA, Blok K, Energy Convers.Manage., 33, 429, 1992