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Process simulation and integration of IGCC systems with novel mixed ionic and electronic conducting membrane-based water gas shift membrane reactors for CO2 capture
Affiliation:1. Key Laboratory of Advanced Energy and Power, Institute of Engineering Thermophysics, Chinese Academy of Sciences, Beijing 100190, China;2. Dalian National Laboratory for Clean Energy, Chinese Academy of Sciences, Dalian 116023, China;3. University of Chinese Academy of Sciences, Beijing 100049, China;4. State Key Laboratory of Catalysis, Dalian Institute of Chemical Physics, Chinese Academy of Sciences, Dalian 116023, China;5. School of Mechanical Electronic & Information Engineering, China University of Mining & Technology – Beijing, Beijing 100083, China;1. School of Chemistry and Chemical Engineering, Guangxi University, Nanning, 530004, China;2. The Key Laboratory of Advanced Materials, School of Materials Science and Engineering, Collaborative Innovation Center of Advanced Nuclear Energy Technology, Tsinghua University, Beijing, 100084, China;3. CAS Key Laboratory of Marine Environmental Corrosion and Bio-fouling, Institute of Oceanology, Chinese Academy of Sciences, No.7 Nanhai Road, Qingdao, 266071, China;1. CAS Key Laboratory of Experimental Marine Biology, Center for Ocean Mega-Science, Institute of Oceanology, Chinese Academy of Sciences, Qingdao, Shandong, 266071, China;2. Laboratory for Marine Biology and Biotechnology, Qingdao National Laboratory for Marine Science and Technology, Qingdao, Shandong, 266237, China;3. Institute of Basic Biological Problems RAS, Pushchino, Moscow Region, 142290, Russia;1. University of Belgrade, Vinča Institute of Nuclear Sciences, Mike Petrovića Alasa 12-14, 11001, Vinča, Serbia;2. Institute of General and Physical Chemistry, Studentski trg 12/V, 11158, Belgrade, 118, Serbia;3. University of Belgrade - Faculty of Physical Chemistry, Studentski trg 12-16, 11158, Belgrad, 118, Serbia;4. Department of Materials Science and Engineering, School of Industrial Engineering and Management, KTH - Royal Institute of Technology, Brinellvägen 23, 100 44, Stockholm, Sweden;5. Environ llc, Cukaricka 9, 11000, Belgrade, Serbia
Abstract:A mixed ionic and electronic conducting (MIEC) membrane provides an alternative to the palladium alloy membrane for water gas shift membrane reactor. It exhibits much better sulfur resistance performance than the palladium alloy membrane. In this paper, the thermodynamic performance of the integrated gasification combined cycle (IGCC) system with MIEC membrane reactor is predicted for the first time. The effects of reactor operation parameters on system flowsheet and performance are investigated and illustrated by sensitive analysis. When the reactor operation temperature is 900 °C and the H2O decomposition ratio is 0.5, the system net efficiency is about 38.90%, which is 2.6% points higher than that of the IGCC with Selexol. The system net efficiency increases with the decrease of operation temperature. With the net efficiency of the conventional system as the reference, the minimum H2O decomposition ratios at different operating temperatures are provided.
Keywords:Water gas shift membrane reactor  Mixed ionic and electronic conducting membrane  Integrated gasification combined cycle
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