In this study, a Pd-Ag membrane reactor (MR) integrated with a lab-synthesized ruthenium catalyst supported on La2Ce2O7 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 N2 physisorption, X-ray diffraction (XRD), hydrogen temperature-programmed reduction (H2-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.

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

Napolitano E. S.;Italiano C.;Brunetti A.
;
Thomas M.;Vita A.
;
Barbieri G.
2025

Abstract

In this study, a Pd-Ag membrane reactor (MR) integrated with a lab-synthesized ruthenium catalyst supported on La2Ce2O7 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 N2 physisorption, X-ray diffraction (XRD), hydrogen temperature-programmed reduction (H2-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.
2025
Istituto di Tecnologie Avanzate per l'Energia - ITAE
Istituto per la Tecnologia delle Membrane - ITM
Hydrogen purification
Hydrogen carrier
Membrane
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Utilizza questo identificativo per citare o creare un link a questo documento: https://hdl.handle.net/20.500.14243/558552
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