TY - JOUR
T1 - Metallic Supported Pd-Ag Membranes for Simultaneous Ammonia Decomposition and H2 Separation in a Membrane Reactor
T2 - Experimental Proof of Concept
AU - Cechetto, Valentina
AU - Agnolin, Serena
AU - Di Felice, Luca
AU - Pacheco Tanaka, Alfredo
AU - Llosa Tanco, Margot
AU - Gallucci, Fausto
N1 - Publisher Copyright:
© 2023 by the authors.
PY - 2023/6
Y1 - 2023/6
N2 - The use of ammonia as a hydrogen carrier requires efficient cracking technology. A promising solution is the use of a membrane reactor (MR), which enables both ammonia decomposition and hydrogen separation to take place within the same device, providing advantages in terms of efficiency and compactness compared to conventional systems. The literature reports that ceramic-supported double-skinned Pd-Ag membranes show outstanding performance for hydrogen separation as well as good stability of the separation layer during ammonia decomposition. However, their sealing in the reactor may result in leakage increase, while their mechanical stability remains an unresolved issue. To circumvent these limitations, the use of metallic supported Pd-based membranes is recommended, due to their higher mechanical stability and ease of sealing and integration in the reactor. In this work, we propose the development of robust metallic supported hydrogen-selective membranes for integration in membrane reactors for ammonia cracking. A conventional Pd-Ag membrane was prepared on a low-cost porous Hastelloy X tubular filter, modified with α-Al2O3/γ-Al2O3 to reach the desired surface quality. The membrane was then tested for ammonia decomposition in a MR configuration, showing the ability to reach >99% NH3 conversion above 475 °C with H2 feed recovery >60%. The results achieved pave the way towards a possible substitute for the ceramic-supported alternatives.
AB - The use of ammonia as a hydrogen carrier requires efficient cracking technology. A promising solution is the use of a membrane reactor (MR), which enables both ammonia decomposition and hydrogen separation to take place within the same device, providing advantages in terms of efficiency and compactness compared to conventional systems. The literature reports that ceramic-supported double-skinned Pd-Ag membranes show outstanding performance for hydrogen separation as well as good stability of the separation layer during ammonia decomposition. However, their sealing in the reactor may result in leakage increase, while their mechanical stability remains an unresolved issue. To circumvent these limitations, the use of metallic supported Pd-based membranes is recommended, due to their higher mechanical stability and ease of sealing and integration in the reactor. In this work, we propose the development of robust metallic supported hydrogen-selective membranes for integration in membrane reactors for ammonia cracking. A conventional Pd-Ag membrane was prepared on a low-cost porous Hastelloy X tubular filter, modified with α-Al2O3/γ-Al2O3 to reach the desired surface quality. The membrane was then tested for ammonia decomposition in a MR configuration, showing the ability to reach >99% NH3 conversion above 475 °C with H2 feed recovery >60%. The results achieved pave the way towards a possible substitute for the ceramic-supported alternatives.
KW - Pd membranes
KW - ammonia decomposition
KW - hydrogen production
KW - metallic supports
UR - https://www.scopus.com/pages/publications/85163825047
U2 - 10.3390/catal13060920
DO - 10.3390/catal13060920
M3 - Article
AN - SCOPUS:85163825047
SN - 2073-4344
VL - 13
JO - Catalysts
JF - Catalysts
IS - 6
M1 - 920
ER -