Monday, June 11, 2018
Grand Ballroom (Hilton Lexington)
Membrane gas contactors are a promising alternative to conventional post combustion carbon capture technologies. However, residuals of other acid gas compounds can exist in the flue gas streams emitted from industrial facilities that might have a notable impact on the absorption performance of the membrane system. Simultaneous removal of CO2 and SO2 from a simulated flue gas stream was carried out in a polytetrafluoroethylene (PTFE) hollow fiber gas-liquid membrane contacting (GLMC) system using different scrubbing solutions. A series of experiments was conducted to study the effects of operating conditions such as gas and liquid cross flow velocity, concentration of feed gas, absorbent nature and concentration, and long-term performance of the GLMC system on the removal efficiencies and mass transfer rates of CO2 and SO2. Experimental results indicated that simultaneous absorption of CO2 and SO2 enhanced with increasing the liquid-phase cross flow velocity, decreasing gas-phase cross flow velocity, and using chemical stripping absorbents. Moreover, sodium hydroxide is a more superior absorbents in compared with alkanolamine solutions for the co-capture of CO2 and SO2 gases. It was observed that low concentrations of SO2 in the feed gas had a minimal impact on the decarbonization of GLMC system. The durability of the membrane system was also evaluated by running the simultaneous gas removal experiments over a 24-hour period. Consistency of the absorption efficiency results confirmed the potential of using PTFE membrane system for the simultaneous absorption of CO2 and SO2 gases.
See more of this Session: Poster Session on Membranes
See more of this Group/Topical: 2018 North American Membrane Society Meeting: Poster Submissions
See more of this Group/Topical: 2018 North American Membrane Society Meeting: Poster Submissions
