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Modularization strategy for syngas generation in chemical looping methane reforming systems with CO 2 as feedstock
Author(s) -
Kathe Mandar,
Fryer Charles,
Sandvik Peter,
Kong Fanhe,
Zhang Yitao,
Empfield Abbey,
Fan LiangShih
Publication year - 2017
Publication title -
aiche journal
Language(s) - English
Resource type - Journals
SCImago Journal Rank - 0.958
H-Index - 167
eISSN - 1547-5905
pISSN - 0001-1541
DOI - 10.1002/aic.15692
Subject(s) - syngas , chemical looping combustion , modular programming , methane , process engineering , raw material , natural gas , oxide , chemistry , nuclear engineering , chemical engineering , waste management , oxygen , catalysis , computer science , engineering , organic chemistry , programming language
This study considers a CO 2 feedstock in conventional methane reforming processes and metal oxide lattice oxygen based chemical looping reforming. Lattice oxygen from iron‐titanium composite metal oxide provides the most efficient co‐utilization of CO 2 with CH 4 . A modularization chemical looping strategy is developed to further improve process efficiencies using a thermodynamic rationale. Modularization leverages the ability of two or more reactors operating in parallel to produce a higher quality syngas than a single reactor operating alone while offering a direct solution to scale up of multiple parallel reactor processes. Experiments conducted validate the thermodynamic simulation results. Simulation and experimental results ascertain that a cocurrent moving bed in a modularization system can operate under CO 2 neutral or negative conditions. The results for a modularization process system for 7950 m 3 per day (50,000 barrels per day) of liquid fuel indicate a ∼23% reduction of natural gas usage over baseline‐case. © 2017 American Institute of Chemical Engineers AIChE J , 63: 3343–3360, 2017