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

被引:0
|
作者
Napolitano, Erasmo Salvatore [1 ]
Italiano, Cristina [2 ]
Brunetti, Adele [1 ]
Thomas, Minju [2 ]
Vita, Antonio [1 ]
Barbieri, Giuseppe [2 ]
机构
[1] Inst Membrane Technol Natl Res Council Italy CNR I, Via P Bucci 17C, I-87036 Arcavacata Di Rende, CS, Italy
[2] Adv Energy Technol Inst Natl Res Council Italy CNR, Salita Santa Lucia Sopra Contesse 5, I-98126 Messina, ME, Italy
关键词
Hydrogen purification; Hydrogen carrier; Membrane; CATALYTIC-ACTIVITY; FUEL; TEMPERATURE; COMBUSTION; STORAGE;
D O I
10.1016/j.fuproc.2025.108203
中图分类号
O69 [应用化学];
学科分类号
081704 ;
摘要
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.
引用
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页数:9
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