Catalytic steam methane reforming enhanced by CO2 capture on CaO based bi-functional compounds
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摘要:
Sorption enhanced steam methane reforming (SE-SMR) was performed to maximize hydrogen production and contemporary remove CO2 from the product stream using bi-functional sorbent-catalyst compounds.Samples were tested at two different scales:micro and laboratory.The CaO amount varied in the CaO-Ca12Al14O33 sorbent system synthesized by wet mixing (CaO content of 100 wt%,56 wt%,30 wt%,or 0 wt% and balance of Ca12Al14O33) which were upgraded to bi-functional compounds by impregnation of 3 wt% of Ni.Nitrogen adsorption (BET/BJH),X-Ray Diffraction (XRD),Temperature-Programmed Reduction (TPR) and Scanning and Transmission Electronic Microscopy (SEM and TEM,respectively) analyses were performed to characterize structural and textural properties and reducibility of the bi-functional materials and evaluate their catalytic behavior.A fixed sorbent composition CaO-Ca12Al14O33 (56 wt% of CaO and Ca12Al14O33 balance),was chosen to study the effect of different weight hourly space times (WHST) and CH4 stream compositions in SE-SMR activity.Impregnated mayenite at both micro and laboratory scales showed stable H2 content of almost 74%,with CH4 conversion of 72% similarly to the values reported by the sample containing 30 wt% of CaO in the post-breakthrough.Sample with 30 wt% of CaO showed promisingly behavior,enhancing H2 content up to almost 94.5%.When the sorption enhanced reaction is performed roughly 89% of CH4 conversion is achieved,and after the pre-breakthmugh,the catalyst worked at the thermodynamic level.During cycling sorption/regeneration experiments,even if CO2 removal efficiency slightly decreases,CH4 conversion and H2 yield remain stable.