CATALYTIC SURFACE MODIFICATION OF ALUMINA MEMBRANE FOR OXYGEN SEPARATION

Authors

  • ‘Ainun Sailah Sihar Department of Oil and Gas Engineering, Faculty of Chemical Engineering, UiTM, 40450, Shah Alam, Selangor, Malaysia
  • Munawar Zaman Shahrudin Department of Oil and Gas Engineering, Faculty of Chemical Engineering, UiTM, 40450, Shah Alam, Selangor, Malaysia
  • Nur Hashimah Alias Department of Oil and Gas Engineering, Faculty of Chemical Engineering, UiTM, 40450, Shah Alam, Selangor, Malaysia
  • 'Azzah Nazihah Che Abdul Rahim Department of Oil and Gas Engineering, Faculty of Chemical Engineering, UiTM, 40450, Shah Alam, Selangor, Malaysia
  • Nur Hidayati Othman Department of Oil and Gas Engineering, Faculty of Chemical Engineering, UiTM, 40450, Shah Alam, Selangor, Malaysia
  • Mukhlis A. Rahman Advanced Membrane Technology Research Center (AMTEC), Faculty of Chemical and Energy Engineering, Universiti Teknologi Malaysia, 81310 UTM Johor Bahru, Johor, Malaysia

DOI:

https://doi.org/10.11113/jt.v79.10433

Keywords:

Surface modification, LSCF, Alumina hollow fibre membrane, Ceramic membrane, Sintering

Abstract

Two types of alumina ceramic membrane in hollow fibre shape was used in this study. Both alumina hollow fibres (AHF) were sintered at different temperatures; (a) 1350oC and (b) 1450oC. In order to improve the catalytic activity of the alumina membrane for oxygen separation purposes, surface modification of the membranes was carried out using La0.6Sr0.4Co0.2Fe0.8O3-δ (LSCF) perovskite catalyst. LSCF was synthesised using simple Pechini sol-gel method. The evaporation time and temperature of the LSCF-sol were varied to obtain various viscosity of catalytic sol. From XRD analysis, pure LSCF perovskite structure formed at temperature at 850oC. The morphological of unmodified and surface-modified alumina hollow fibre membranes (AHF) were studied using FESEM. The effect of LSCF catalytic sol viscosity was studied and it was found that as the viscosity of the sol increases, the amount of catalyst deposited on the alumina hollow fibre were increased.  Besides, the amount of catalyst deposited on 1350 AHF was found to be higher than 1450 AHF. This result is supported by the result of pore distribution data whereby 1350 AHF was observed to be more porous than 1450 AHF, with porosity percentage of 40.38% and 28.80%, respectively. Although higher viscosity of catalytic sol could lead to a high amount of catalyst deposited on the AHF substrate, there is a tendency for micro-cracks to develop. Thus, the viscosity of the catalytic sol is important to control in order to have higher oxygen permeation flux.   

References

Teraoka, Y., Zhang, H. M., Okamoto, K. and Yamazoe N. 1988. Mixed Ionic-electronic Conductivity Of La1-xSrxCo1-yFeyO3-δ Perovskite-Type Oxides. Mater. Res. Bull. 23(1): 51-58.

Leo, A., Smart, S., Liu, S. and Diniz da Costa, J. C. 2011. High Performance Perovskite Hollow Fibres For Oxygen Separation. J. Memb. Sci. 368(1-2): 64-68.

Teraoka, Y., Honbe, Y., Ishii, J., Furukawa, H. and Moriguchi, I. 2002. Catalytic Effects In Oxygen Permeation Through Mixed-Conductive LSCF Perovskite Membranes. Solid State Ionics. 152-153: 681-687.

Liu, J., Co, A. C., Paulson, S. and Birss, V. I. 2006. Oxygen Reduction At Sol-Gel Derived La0.8Sr0.2Co 0.8Fe0.2O3 Cathodes. Solid State Ionics. 177(3-4): 377-387.

Montgkolkachit, C. and Wanakitti, S. 2008. Characterization of (La,Sr)(Co,Fe)O3-δ Ferrite-Based Cathodes for Intermediate-Temperature SOFCs. Journal of Metals, Materials and Minerals., 18(2): 33-36.

Tan, T., Liu, N., Meng, B., Sunarso, J., Zhang, K. and Liu, S. 2012. Oxygen Permeation Behavior of La0.6Sr0.4Co0.8Fe0.2O3 Hollow Fibre Membranes With Highly Concentrated CO2 Exposure. J. Memb. Sci. 389: 216-222.

Kim, J. H., Park, Y. M. and Kim, H. 2011. Nano-Structured Cathodes Based on La0.6Sr0.4Co0.2Fe0.8O3−δ For Solid Oxide Fuel Cells. J. Power Sources. 196(7): 3544-3547.

Tan, X., Pang, Z., Gu, Z. and Liu, S. 2007. Catalytic Perovskite Hollow Fibre Membrane Reactors For Methane Oxidative Coupling. J. Memb. Sci. 302(1-2): 109-114.

Othman, N. H., Wu, Z. and Li, K. 2014. A Micro-Structured La0.6Sr0.4Co0.2Fe0.8O3-δ Hollow Fibre Membrane Reactor For Oxidative Coupling of Methane. Journal of Membrane Science. 468: 31-41.

Zydorczak, B., Wu, Z. and Li, K. 2009. Fabrication Of Ultrathin La0.6Sr0.4Co0.2Fe0.8O3-δ Hollow Fibre Membranes For Oxygen Permeation. Chem. Eng. Sci. 64(21): 4383-4388.

Middelkoop, V., Chen, H., Michielsen, B., Jacobs, M., Syvertsen-Wiig, G., Mertens, M., Buekenhoudt, A. and Snijkers, F. 2014. Development And Characterisation Of Dense Lanthanum-Based Perovskite Oxygen-Separation Capillary Membranes For High-Temperature Applications. J. Memb. Sci. 468: 250-258.

Wang, Z., Liu, H., Tan, X., Jin, Y. and Liu, S. 2009. Improvement of The Oxygen Permeation Through Perovskite Hollow Fibre Membranes By Surface Acid-Modification. J. Memb. Sci. 345(1-2): 65-73.

Yacou, C., Sunarso, J., Lin, C. X. C., Smart, S., Liu, S. and Diniz da Costa, J. C. 2011. Palladium Surface Modified La0.6Sr0.4Co0.2Fe0.8O3-δ Hollow Fibres For Oxygen Separation. Journal of Membrane Science. 380(1-2): 223-23.

Tan, X., Wang, Z., Liu, H. and Liu, S. 2008. Enhancement Of Oxygen Permeation Through La0.6Sr0.4Co0.2Fe0.8O3-δ Hollow Fibre Membranes By Surface Modifications. J. Memb. Sci. 324(1-2): 128-135.

Han, N., Zhang, S., Meng, X., Yang, N., Meng, B., Tan, X. and Liu, S. 2016. Effect Of Enhanced Oxygen Reduction Activity On Oxygen Permeation Of La0.6Sr0.4Co0.2Fe0.8O3-δ Membrane Decorated By K2NiF4-Type Oxide. J. Alloys Compd. 654: 280-289.

Han, D., Wu, J., Yan, Z., Zhang, K., Liu, J. and Liu, S. 2014. La0.6Sr0.4Co0.2Fe0.8O3-δ Hollow Fibre Membrane Performance Improvement By Coating of Ba0.5Sr0.5Co0.9Nb0.1O3−δ Porous Layer. RSC Advances. 4(38): 19999.

Kingsbury, B. F. K. and Li, K. 2009. A Morphological Study Of Ceramic Hollow Fibre Membranes. J. Memb. Sci. 328(1-2): 134-140.

Abdullah, N., Rahman, M. A., Othman, M. H. D., Ismail, A. F., Jaafar, J. and Aziz, A. A. 2016. Preparation And Characterization of Self-Cleaning Alumina Hollow Fiber Membrane Using The Phase Inversion And Sintering Technique. Ceram. Int. 42(10): 12312-12322.

Agrafiotis, C. and Tsetsekou, A. 2002. Deposition Of Meso-Porous γ-Alumina Coatings On Ceramic Honeycombs By Sol-Gel Methods. J. Eur. Ceram. Soc. 22(4): 423-434.

Ritchie, J. T., Richardson, J. T. and Luss, D. 2011. Ceramic Membrane Reactor For Synthesis Gas Production. Aiche J., 47(9): 2092-2101.

Gbenedio, E., Wu, Z., Hatim, I., Kingsbury, B. F. K. and Li, K. 2010. A Multifunctional Pd/Alumina Hollow Fibre Membrane Reactor For Propane Dehydrogenation. Catal. Today. 156(3-4): 93-98.

Stephane, H., Michel, B., Jamal, A. and Barbara, E. 2008. Thin Palladium Layer Deposited On Ceramic Materials: Application In Hydrogen Transport And Catalytic Membrane Process. Int. J. Surf. Sci. Eng. 2: 202-221.

Othman, N. H., Shahruddin, M. Z., Sihar, A. S., Wu, Z. and Li, K. 2016. In-Situ Catalytic Surface Modification of Micro-Structured Vacuum-Assisted Technique. MATEC Web of Conferences 6. 05002: 1-6.

Jin, W., Li, S., Huang, P., Xu, N. and Shi, J. 2000. Fabrication of La0.2Sr0.8Co0.8Fe0.2O3-δ Mesoporous Membranes On Porous Supports From Polymeric Precursors. J. Memb. Sci. 170(1): 9-17.

Wang, Z., Yang, N. and Meng, B. 2008. Preparation And Oxygen Permeation Properties of Highly Asymmetric La0. 6Sr0. 4Co0. 2Fe0. 8O3−δ Perovskite Hollow-Fiber Membranes. Ind. Eng. Chem. Res. 510-516.

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Published

2017-01-31

How to Cite

CATALYTIC SURFACE MODIFICATION OF ALUMINA MEMBRANE FOR OXYGEN SEPARATION. (2017). Jurnal Teknologi (Sciences & Engineering), 79(1-2). https://doi.org/10.11113/jt.v79.10433