Enhanced ammonia decomposition using a Pd-Ag membrane reactor for high-purity hydrogen production

In this study, a Pd-Ag membrane reactor (MR) integrated with a lab-synthesized ruthenium catalyst supported on La 2 Ce 2 O 7 was used for the efficient production and recovery of highly-pure hydrogen from ammonia decomposition. The catalyst was synthesized using solution combustion techniques, and its structure–activity relationship was thoroughly investigated through a range of advanced characterization methods, including N 2 physisorption, X-ray diffraction (XRD), hydrogen temperature-programmed reduction (H 2 -TPR), and transmission electron microscopy (TEM). The performance of the membrane reactor was evaluated by varying the feed pressure and flow rate, using either single ammonia or a simulated outlet stream from a conventional reactor with ammonia conversions ranging from 20 % to 50 %. This configuration was designed to assess the MR ability to mitigate or prevent hydrogen back-permeation, as well as optimize membrane performance. The MR achieved ammonia conversions of up to 85 %, surpassing the thermodynamic limits typical of traditional reactors (TR). Hydrogen recovery rates reached 97 %, with purity consistently exceeding 90 %. Notably, the MR demonstrated up to 3.6 times higher ammonia conversion compared to conventional TR, highlighting its significant advantages for ammonia decomposition applications. • Pd-Ag membrane reactor packed with Ru/La₂Ce₂O₇ catalyst to produce highly pure hydrogen. • Novel reactor operation mitigates H 2 back-permeation, enhancing the membrane utilization. • NH₃ conversion up to 85 % exceeding the traditional reactor equilibrium conversion. • H₂ recovery to 97 % and purity above 90 %. • NH 3 conversion achieved in MR 3.6 times greater than TR one.

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Publication Details

Journal
Fuel Processing Technology
Published
2025-03-13
DOI
https://doi.org/10.1016/j.fuproc.2025.108203
Citations
6
Primary Topic
Ammonia Synthesis and Nitrogen Reduction
Type
article
Field-Weighted Citation Impact
2.33
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article

Enhanced ammonia decomposition using a Pd-Ag membrane reactor for high-purity hydrogen production

Emilio Napolitano, Adele Brunetti, Minju Thomas, Giuseppe Barbieri et al.
6 citations
Fuel Processing Technology
Ammonia Synthesis and Nitrogen Reduction
2.33
article

Enhanced ammonia decomposition using a Pd-Ag membrane reactor for high-purity hydrogen production

Emilio Napolitano, Adele Brunetti, Minju Thomas, Giuseppe Barbieri, Cristina Italiano, Antonio Vita
article en
6 citations

Abstract

In this study, a Pd-Ag membrane reactor (MR) integrated with a lab-synthesized ruthenium catalyst supported on La 2 Ce 2 O 7 was used for the efficient production and recovery of highly-pure hydrogen from ammonia decomposition. The catalyst was synthesized using solution combustion techniques, and its structure–activity relationship was thoroughly investigated through a range of advanced characterization methods, including N 2 physisorption, X-ray diffraction (XRD), hydrogen temperature-programmed reduction (H 2 -TPR), and transmission electron microscopy (TEM). The performance of the membrane reactor was evaluated by varying the feed pressure and flow rate, using either single ammonia or a simulated outlet stream from a conventional reactor with ammonia conversions ranging from 20 % to 50 %. This configuration was designed to assess the MR ability to mitigate or prevent hydrogen back-permeation, as well as optimize membrane performance. The MR achieved ammonia conversions of up to 85 %, surpassing the thermodynamic limits typical of traditional reactors (TR). Hydrogen recovery rates reached 97 %, with purity consistently exceeding 90 %. Notably, the MR demonstrated up to 3.6 times higher ammonia conversion compared to conventional TR, highlighting its significant advantages for ammonia decomposition applications. • Pd-Ag membrane reactor packed with Ru/La₂Ce₂O₇ catalyst to produce highly pure hydrogen. • Novel reactor operation mitigates H 2 back-permeation, enhancing the membrane utilization. • NH₃ conversion up to 85 % exceeding the traditional reactor equilibrium conversion. • H₂ recovery to 97 % and purity above 90 %. • NH 3 conversion achieved in MR 3.6 times greater than TR one.

Fuel Processing TechnologyVol. 272
Institute for Advanced Energy Technologies (IT), Institute on Membrane Technology (IT)
Openalex Percentile: Top 12%
Ammonia Synthesis and Nitrogen Reduction
2.33
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