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Highly efficient methane reforming over a low‐loading Ru/γ‐Al 2 O 3 catalyst in a Pd‐Ag membrane reactor
Author(s) -
Simakov David S. A.,
RománLeshkov Yuriy
Publication year - 2018
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.16094
Subject(s) - syngas , methane , catalysis , steam reforming , membrane reactor , chemistry , hydrogen , bar (unit) , catalytic reforming , methane reformer , carbon fibers , chemical engineering , nuclear chemistry , hydrogen production , materials science , organic chemistry , physics , meteorology , composite number , engineering , composite material
Natural gas can be reformed to syngas (CH 4 + H 2 O = CO + 3H 2 ), at temperatures above 850°C. Membrane catalytic reformers can provide high CH 4 conversions at temperatures below 650°C, by separating H 2 from the reactive mixture. Traditional Ni‐based catalysts suffer from low activity at low temperatures and deactivate rapidly by coking, particularly at low steam/carbon ratios. In this study, an ultralow loading (0.15 wt %) Ru/γ‐Al 2 O 3 catalyst was implemented in a lab‐scale membrane reformer, using a supported 5μm Pd‐Ag film membrane. Methane conversions above 90% were achieved at 650°C, 8 bar, and H 2 O/CH 4 = 2, 3 with contact times of ca. 10 s. The system generated up to 3.5 mol of ultrapure H 2 per mol of CH 4 fed, with a maximum power density of 0.9 kW/L. No significant deactivation was observed after 200 h time on stream, even when using low H 2 O:CH 4 ratios. © 2018 American Institute of Chemical Engineers AIChE J , 64: 3101–3108, 2018