Malaysian
Journal of Analytical Sciences Vol 20 No 2 (2016): 303 - 308
HYDROGEN PRODUCTION FROM GASIFICATION OF PALM KERNEL
SHELL IN THE PRESENCE OF Fe/CeO2 CATALYSTS
(Penghasilan
Hidrogen daripada Pengegasan Isirung Kelapa Sawit dengan Kehadiran Mangkin Fe/CeO2)
Anita
Ramli1*, Mas Fatiha Mohamad2, Suzana Yusup2,
Taufiq Yap Yun Hin3
1Department of Fundamental
and Applied Sciences
2Department of
Chemical Engineering
Universiti Teknologi PETRONAS, 32600 Bandar Seri
Iskandar, Perak, Malaysia.
3Department of
Chemistry,
Universiti
Putra Malaysia, 43400 UPM Serdang, Selangor, Malaysia
*Corresponding author: anita_ramli@petronas.com.my
Received: 24
February 2015; Accepted: 27 October 2015
Abstract
Biohydrogen is a renewable source of clean fuel and energy which can be
derived from biomass. One of the suitable candidate as a source of biomass is
palm kernel shell (PKS). Our initial work shows that biohydrogen may be
produced from PKS in the presence of zeolite supported catalysts. The potential
of using cerium oxide (CeO2) supported catalysts for the production
of biohydrogen from PKS is explored in this work using 2.5 – 10 % Fe loading.
The catalysts were prepared by incipient wetness impregnation method and calcined
at 500 oC for 16 h. The physicochemical properties of these
catalysts were characterized using BET and XRD. The catalysts were tested
in dry and steam gasification of PKS at
700 oC using PKS feeding rate of 2 g h-1 under N2
atmosphere with biomass to catalyst ratio of 3:1 (wt/wt). Steam to biomass ratio of 3.5:1 (wt/wt)
was used in steam gasification
reaction. The gaseous products were analyzed using an on-line gas
chromatography equipped with thermal conductivity detectors (TCD) and fitted
with Molsieve 5A and Hayesep Q columns. Result shows that 2.5 % Fe/CeO2
gave the highest hydrogen production in both the dry and steam gasification of
PKS.
Keywords: biohydrogen, palm kernel shell, ceria
supported catalysts, gasification
Abstrak
Biohidrogen adalah sumber bahan api yang
boleh diperbaharui daripada sumber biomas. Isirung kelapa sawit (PKS) merupakan
salah satu sumber biomas yang sesuai digunakan umtuk tujuan ini. Kajian awal
menunjukkan biohidrogen boleh dihasilkan daripada PKS dengan menggunakan
mangkin berpenyokong zeolite. Dalam kajian ini, muatan mangkin 2.5 – 10 % logam
Fe berpenyokong cerium oksida (CeO2) digunakan untuk meningkatkan
penghasilan biohydrogen daripada PKS. Pemangkin disediakan menggunakan kaedah
pengisitepuan pembasahan permulaan dan dikalsinkan pada suhu 500 oC
selama 16 jam. Sifat fizikal kimia pemangkin ini dianalisa menggunakan teknik
BET dan XRD. Kereaktifan mangkin untuk penghasilan biohidrogen diuji dalam
pengegasan kering dan berstim pada suhu 700 oC dengan PKS
diperkenalkan pada kadar 2g h-1 dan nisbah PKS kepada pemangkin
adalah 3:1 (wt/wt). Nisbah stim kepada PKS 3.5: 1 (wt/wt) telah ditetapkan
dalam eksperimen pengegasan berstim. Gas yang telah dihasilkan telah dianalisa
menggunakan kromatograf gas yang dilengkapi pengesan konduktiviti termal (TCD)
serta tiub Molsieve 5A dan Hayesep Q. Keputusan kajian menunjukkan penghasilan
hidrogen yang maksimum dicapai dengan kehadiran mangkin 2.5 % Fe / CeO2.
Kata
kunci: biohidrogen,
tempurung kelapa sawit, mangkin berpenyokong CeO2, pengegasan
References
1.
Balat, M., Kirtay, E. and Balat. H. (2009). Main routes for the
thermo-conversion of biomass into fuels and
chemicals. Part 2: Gasification systems Energy
Conversion and Management, 50: 3158 – 3168.
2.
Nordgreen, T., Liliedahl, T. and Sjöström. K. (2006). Metallic iron as a tar
breakdown catalyst related to atmospheric fluidized bed gasification of
biomass, Fuel, 85: 689 – 694.
3.
Ramli, A., Misi, S. E. E., Mohamad, M. F. and Yusup. S. (2013). H2 Production from steam gasification of Palm Kernel Shell
in the presence of 5% Ni/BEA and 5% Fe/BEA catalysts, Advanced Science Letters, 19: 950 – 954.
4.
Kaspar, J., Fornasiero, P. and Graziani.
M. (1999). Metallic iron as
a tar breakdown
catalyst related to atmospheric, fluidised bed gasification of
biomass, Catalysis Today, 50: 285 – 298.
5.
Tomishige, K., Asadullah, M. and Kunimori. K. (2003). Novel catalysts
for gasification of biomass with high conversion
efficiency, Catalysis Surveys from Asia, 7: 219
–223.
6.
Pecchi, G., Reyes, P. and Villasenor. J. (2003). Fe supported catalysts
prepared by the sol-gel method. Characterization and evaluation
in phenol abatement, Journal of Sol-Gel Science and Technology, 26: 865 – 867.
7.
Reddy, A. S., Chen, C., Chien, S., Lin, C., Lin, K. and Chang.
S. (2010). Synthesis
and characterization of Fe/CeO2 catalysts: epoxidation of
cyclohexene, Journal of Molecular Catalysis A, 318: 60 – 67.
8.
Rao, G. R. and Mishra.
B. G. (2003). Structural, redox and catalytic chemistry of ceria
based materials, Bulletin of the Catalysis Society of
India, 2: 122 – 134.
9.
Perez-Alonso, F. J.,
Lopez Granados,
M., Ojeda, M., Terreros, P., Rojas, S., Herranz, T., Fierro, J. L. G., Gracia, M. and Gancedo, J. R.
(2005). Chemical
structures of co-precipitated Fe-Ce mixed oxides, Chemistry of Materials, 17: 2329 – 2339.
10.
Tang, L., Yamaguchi, D., Burke, N., Trimm, D. and Chiang, K .(2010). Methane decomposition over ceria modified iron
catalysts, Catalysis Communications, 11: 1215 –1219.
11.
Li, K. Z., Wang,
H., Wei, Y. And Yan, D. X.(2009). Selective oxidation of carbon using
iron-modified cerium oxide, Journal of
Physical Chemistry C, 113: 15288
– 15297.