Deposition of Pd-Ag thin film membranes on ceramic supports for hydrogen purification/separation

• Tipo: Artigo em Revista Científica Internacional
• Data: 2015

Autores

S. C. Rodrigues (Autor) FEUP; A. Mendes (Autor) FEUP; L. M. Madeira (Autor) FEUP; A. I. Pereira (Autor) Outra; P. Pérez (Autor) Outra; C. J. Tavares (Autor) Outra

Revista

Título: Materials Research Bulletin

Vol. 61

Páginas: 528-533

ISSN: 0025-5408

Editora: Elsevier

Indexação

ISI Web of Knowledge - 9 Citações

ISI Web of Science

Scopus - 14 Citações

INSPEC

Classificação Científica

FOS: Ciências da engenharia e tecnologias > Engenharia química

CORDIS: Ciências Tecnológicas > Engenharia > Engenharia química

Projetos Associados

PTDC/EQU-ERQ/098730/2008 - Integração de Reactores de Membrana com Processos Adsorptivos usando-se Catalisadores Suportados em Monolitos para a Produção de Hidrogénio de Elevada Pureza

Outras Informações

ID Authenticus: P-009-Z7G

DOI: 10.1016/j.materresbull.2014.10.055

Abstract (EN): Pd-Ag based membranes supported on porous alpha-Al2O3 (doped with yttria-stabilized zirconia) were studied for hydrogen selective separation. Magnetron sputtering technique was employed for the synthesis of thin film membranes. The hydrogen permeation flux is affected by the membrane columnar structure, which is formed during deposition. From scanning electron microscopy analysis, it was observed that different sputtering deposition pressures lead to distinct columnar structure growth. X-ray diffraction patterns provided evidence of a Pd-Ag solid solution with an average crystallite domain size of 21 nm, whose preferential growth can be altered by the deposition pressure. The gas-permeation results have shown that the Pd-Ag membrane supported on porous alpha-Al2O3 is selective toward H-2. For optimized membrane synthesis conditions, the permeance toward N-2 is 0.076 x 10(-6) moi m(-2) s(-1) pa(-1) at room temperature, whereas for a pressure difference of 300 kPa the H-2-flux is of the order of ca. 0.21 mol m(-2) s(-1), which corresponds to a permeance of 0.71 x 10(-6) mol m(-2) s(-1) Pa-1, yielding a selectivity of alpha (H-2/N-2) = 10. These findings suggest that the membrane has a reasonable capacity to selectively permeate this gas. (C) 2014 Elsevier Ltd. All rights reserved.

Idioma: Inglês

Tipo (Avaliação Docente): Científica

Notas: Publicação abrangida pelo Journal Citation Reports 2015

Nº de páginas: 6