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Hydrogen‐rich syngas production from chemical looping steam reforming of bio‐oil model compound: Effect of bimetal on LaNi 0.8 M 0.2 O 3 (M = Fe, Co, Cu, and Mn)
Author(s) -
Liu Chen long,
Chen Dong,
Wang Wenju
Publication year - 2019
Publication title -
international journal of energy research
Language(s) - English
Resource type - Journals
SCImago Journal Rank - 0.808
H-Index - 95
eISSN - 1099-114X
pISSN - 0363-907X
DOI - 10.1002/er.4581
Subject(s) - syngas , space velocity , catalysis , steam reforming , chemistry , inorganic chemistry , acetic acid , hydrogen , hydrogen production , perovskite (structure) , adsorption , nuclear chemistry , organic chemistry , selectivity
Summary Chemical looping steam reforming (CLSR) of acetic acid as bio‐oil model compound is a suitable way to produce hydrogen‐rich syngas. The LaNiO 3 and LaNi 0.8 M 0.2 O 3 (M = Fe, Co, Mn, and Cu) perovskites were prepared via the sol‐gel method. The perovskites were characterized by X‐ray diffraction (XRD), thermogravimetry (TG), and test activity of hydrogen‐rich syngas in a fixed bed. XRD and TG results showed that the coke generation on LaNi 0.8 Fe 0.2 O 3 needs a lower decomposition temperature, and a stable structure was appeared after reaction. The activity order of hydrogen‐rich syngas on five types of perovskite is LaNi 0.8 Fe 0.2 O 3 > LaNi 0.8 Co 0.2 O 3 > LaNiO 3 > LaNi 0.8 Mn 0.2 O 3 > LaNi 0.8 Cu 0.2 O 3 at 650°C, mole ratio of steam/carbon (2:1), and sample mixture flow (GHSV = 34 736 g of feed/(g catalyst h)). The CLSR of acetic acid with LaNi 0.8 Fe 0.2 O 3 at GHSV = 43 992 g of feed/(g catalyst h) showed good stability. Correlated to experimental results, the adsorption energy of steam and acetic acid on five types of perovskite were calculated using density functional theory (DFT). The adsorption energy of steam (−0.61 eV) and acetic acid (−0.93 eV) of LaNi 0.8 Fe 0.2 O 3 is maximum. This value of DFT calculation is well explained in the experimental results.