High purity, self-sustained, pressurized hydrogen production from ammonia in a catalytic membrane reactor
AuthorsCerrillo, Jose L.
Morlanes, Natalia Sanchez
Kulkarni, Shekhar Rajabhau
Katikaneni, Sai P.
Paglieri, Stephen N.
KAUST DepartmentKAUST Catalysis Center (KCC), King Abdullah University of Science and Technology (KAUST), Thuwal 23955-6900, Saudi Arabia
KAUST Catalysis Center (KCC)
Chemical Engineering Program
Physical Science and Engineering (PSE) Division
Clean Combustion Research Center
Online Publication Date2021-12-24
Print Publication Date2021-12
Permanent link to this recordhttp://hdl.handle.net/10754/675133
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AbstractThe combination of catalytic decomposition of ammonia and in situ separation of hydrogen holds great promise for the use of ammonia as a clean energy carrier. However, finding the optimal catalyst – membrane pair and operation conditions have proved challenging. Here, we demonstrate that cobalt-based catalysts for ammonia decomposition can be efficiently used together with a Pd-Au based membrane to produce high purity hydrogen at elevated pressure. Compared to a conventional packed bed reactor, the membrane reactor offers several operational advantages that result in energetic and economic benefits. The robustness and durability of the combined system has been demonstrated for>1000 h on stream, yielding a very pure hydrogen stream (>99.97 % H2) and recovery (>90 %). When considering the required hydrogen compression for storage/utilization and environmental issues, the combined system offers the additional advantage of production of hydrogen at moderate pressures along with full ammonia conversion. Altogether, our results demonstrate the possibility of deploying high pressure (350 bar) hydrogen generators from ammonia with H2 efficiencies of circa 75% without any external energy input and/or derived CO2 emissions.
CitationCerrillo, J. L., Morlanés, N., Kulkarni, S. R., Realpe, N., Ramírez, A., Katikaneni, S. P., … Gascon, J. (2021). High purity, self-sustained, pressurized hydrogen production from ammonia in a catalytic membrane reactor. Chemical Engineering Journal, 134310. doi:10.1016/j.cej.2021.134310
SponsorsThe authors gratefully acknowledge the financial support provided by Saudi Aramco, and the resources and facilities provided by the King Abdullah University of Science and Technology. N.M. and J.G. conceived this work. J.L.C and N.M. designed, characterized and conducted synthesis and catalytic experiments. N.R. and S.R.K. performed control regime studies. A.R. performed the technology simulation comparison and provided experimental support. J.G. P.C. and S.M.S. provided revision suggestions. J.L.C and N.M. wrote the original draft of the manuscript. All authors have given the approval to the final version of the manuscript.
JournalChemical Engineering Journal
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