Hydrogen Separation Using Pt-Alumina Impregnated Membrane

Mohammed N. Kajama; Ngozi C. Nwogu; Edidiong O. Okon; Habiba Shehu; Ify Orakwe; Edward Gobina

doi:10.4236/epe.2015.79039

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EPE> Vol.7 No.9, August 2015

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Hydrogen Separation Using Pt-Alumina Impregnated Membrane ()

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DOI: 10.4236/epe.2015.79039 2,200 Downloads 2,584 Views Citations

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Mohammed N. Kajama, Ngozi C. Nwogu, Edidiong O. Okon, Habiba Shehu, Ify Orakwe, Edward Gobina

Affiliation(s)

Centre for Process Integration and Membrane Technology, (CPIMT), School of Engineering, The Robert Gordon University, Aberdeen, UK.

ABSTRACT

A tubular commercial mesoporous support was used to prepare a Pt impregnated membrane using the reservoir method and tested for moderate temperature (300°C) gas transport of hydrogen (H₂), helium (He) and nitrogen (N₂) gas molecules. H₂ and N₂ gas permeation of 6.1 and 4.5 l/min at 1.0 barg feed pressure and 25°C respectively was obtained from the support. On the other hand, H₂ and N₂ gas permeation of 4.6 and 1.7 l/min at 1.0 barg feed pressure and 25°C respectively was also obtained from the Pt membrane. Selectivity of H₂ over He of 1.96 at 300°C and 1.6 barg for the Pt membrane was obtained and found to be higher than that of the theoretical Knudsen selectivity. Also, a selectivity of H₂ over N₂ of 2.72 at 25°C and 1.0 barg was obtained and found to be close to that of the theoretical Knudsen selectivity. The gas permeation and the selectivity performance of the membrane were evaluated.

KEYWORDS

Tubular Support, Pt Membrane, Hydrogen Selectivity, Permeation Temperature

Cite this paper

Kajama, M. , Nwogu, N. , Okon, E. , Shehu, H. , Orakwe, I. and Gobina, E. (2015) Hydrogen Separation Using Pt-Alumina Impregnated Membrane. Energy and Power Engineering, 7, 412-417. doi: 10.4236/epe.2015.79039.

Conflicts of Interest

The authors declare no conflicts of interest.

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