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Simulation of CO2 and H2S Removal Using Methanol in Hollow Fiber Membrane Gas Absorber (HFMGA)

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Figure

Table 1. Specifications of the membrane gas absorber.
Figure 2. Comparison between experimental [20] and simu- lated CO2 removal efficiency
Figure 4. CO2 concentration distribution in computational do main for VL = 0.1 m/s, VG = 3 m/s and T = 298 K
Figure 6. CO2 and H2S radial tube side concentration profiles along fiber length for z/L = 0.1, 0.5, 0.9, VL = 0.1 m/s, VG = 3 m/s and T = 298 K
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