(491a) Biomass – Flare Gas Synergistic Co-Processing over Fe / Ni / Pd Doped Mo2c Supported on Graphene Nanosheets: Experimental and DFT Integrated Approach to Hydrogen Production | AIChE

(491a) Biomass – Flare Gas Synergistic Co-Processing over Fe / Ni / Pd Doped Mo2c Supported on Graphene Nanosheets: Experimental and DFT Integrated Approach to Hydrogen Production

Authors 

Lalsare, A. - Presenter, West Virginia University
Khan, T. S., Indian Institute of Technology Delhi
Leonard, B., West Virginia University
Vukmanovich, R., West Virginia University
Tavazohi, P., West Virginia University
Li, L., West Virginia University
Hu, J., West Virginia University
Biomass – flare gas synergistic co-processing is a novel energy generation and conversion technology that aims at harnessing abundant renewable energy source: biomass and reduce greenhouse gas emissions from flaring in stranded shale plays. In this study p-cresol is used as a model biomass-lignin molecule for methane assisted reforming studies, then scaled-up to model alkali lignin and eventually hardwood biomass in a detail bottom-up approach to gain the molecular level understanding of the reaction mechanism and ascertain the role of active sites. Novel in-situ catalyst synthesis using biomass precursor was achieved through pyrolysis to yield graphene nanosheets (GNS) supported transition metal and Mo2C nanoparticles. Initially, experimental work and DFT modelling calculations were performed for methane assisted p-cresol reforming using Fe, Ni, Mo2C, Fe-Mo2C, Ni-Mo2C, Pd-Mo2C supported on GNS. Detailed mechanistic investigation of methane – p-cresol synergistic reaction experimentally and through molecular simulations helped ascertain the unique reaction pathway occurring on dual active sites on a transition metal doped β-Mo2C-GNS catalyst. Transition metal doped Mo2C viz.: Fe-Mo2C-GNS and Ni-Mo2C-GNS are equally effective as Mo2C-GNS for methane dissociation and p-cresol HDO but present significantly lower barrier for H2 (1.15, 1.13 eV vs. 1.70 eV) and CO (2.87, 2.80 eV vs. 3.67 eV) gas-phase desorption. Dual active sites are required for hydrogen rich syngas production through methane assisted p-cresol reforming as validated by experiments, DFT calculations, and micro-kinetic modelling (MKM). Lignin and hardwood biomass both having higher O:C weight ratio compared to p-cresol (0.46, 1.09 vs. 0.19) were co-processed with methane over FeMo-GNS, NiMo-GNS, and MoPd-GNS catalysts. Transition metal doped Mo2C was found to be highly active for simultaneous CH4 activation and extensive hydrodeoxygenation of p-cresol, lignin, and hardwood biomass. Up to 99% hydrogen present in lignin could be valorized as syngas with a concentration of > 65%.