Hydrogen production from acetic acid steam reforming over nickel-based catalyst synthesized via MOF process

In our earlier work, we have reported that Ni supported on g-Al2O3-La2O3-CeO2 (ALC) catalyst prepared via metal organic framework (MOF) was more active for acetic acid steam reforming (AASR) [1]. Here we report detailed study on the performance of this catalyst for AASR. Effects of operating conditions such as temperatures (400-650 degrees C), steam to carbon molar ratio (S/C) and feed flow rate (1.5-5.5 mL/h) were evaluated and optimized. Results showed an excellent activity for AASR at the molar ratio S/C = 6.5, feed flow rate = 2.5 mL/h and, at 600 degrees C with almost total conversion and more than 90% of H-2 yield. The ordered porous structure of embedded nickel supported catalyst promotes excellent steam reforming activity and water gas shift reaction even at low temperatures, which leads to the good stable behaviour up to 36 h of TOS. The coke formation was also significantly suppressed by ALC support. Catalyst regenerated by passing oxygen at 500 degrees C and followed by reduction in hydrogen also show a good activity. Catalysts were characterized by DTTGA, XRD, TEM, H-2-TPR and N-2-adsorption-desorption to understand the micro structure and coke deposition behaviour. (c) 2020 Hydrogen Energy Publications LLC. Published by Elsevier Ltd. All rights reserved.