Effect of Steam and Catalyst on Palm Waste Thermal Decomposition for Hydrogen Production

The thermal decomposition of palm oil wastes in the form of palm shell and palm oil fronds in the presence of steam and catalyst was experimentally investigated using thermogravimetric analyzer-gas chromatography (TGA-GC). The hydrogen gas composition was observed for palm oil wastes thermal decompo...

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Main Authors: Khan, Zakir, Yusup, Suzana, Ahmad, Murni M, Ramli, Anita, Arpin, Mohamad Taufiq, Abdullah, S. S, Mohamad, Mas Fatiha, Misi, Siti Eda Eliana, Inayat, Abrar
Format: Conference or Workshop Item
Published: 2011
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Online Access:http://eprints.utp.edu.my/7050/1/Effect_of_Steam_and_catalyst_on_palm_oil_wastes_thermal_decomposition_for_hydrogen_production_%28ICCE_2011%29.pdf
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spelling my.utp.eprints.70502017-01-19T08:22:44Z Effect of Steam and Catalyst on Palm Waste Thermal Decomposition for Hydrogen Production Khan, Zakir Yusup, Suzana Ahmad, Murni M Ramli, Anita Arpin, Mohamad Taufiq Abdullah, S. S Mohamad, Mas Fatiha Misi, Siti Eda Eliana Inayat, Abrar TP Chemical technology The thermal decomposition of palm oil wastes in the form of palm shell and palm oil fronds in the presence of steam and catalyst was experimentally investigated using thermogravimetric analyzer-gas chromatography (TGA-GC). The hydrogen gas composition was observed for palm oil wastes thermal decomposition i) under inert atmosphere (no steam), ii) in steam gasification and iii) in catalytic steam gasification using a newly developed bi metallic catalyst. Detailed discussion has been made for product gas composition profiles at steam-to-biomass ratio of 1 and biomass-to-catalyst ratio of 3. Maximum H2 content up to 64 mol% and 50 mol% in product gas was observed for palm shell and palm oil fronds, respectively, in the catalytic steam gasification. The usage of steam has almost increased H2 content by 28% for both palm oil wastes. The catalyst usage in the steam gasification increased H2 content by 12.5% and 6% for palm shell and palm oil fronds, respectively. Moreover, CO2 concentration in the product gas was reduced in steam gasification where CO concentration was decreased in catalytic steam gasification. This decrease in CO concentration is due to the bi metallic catalyst activity on water gas shift reaction. 2011-05-29 Conference or Workshop Item PeerReviewed application/pdf http://eprints.utp.edu.my/7050/1/Effect_of_Steam_and_catalyst_on_palm_oil_wastes_thermal_decomposition_for_hydrogen_production_%28ICCE_2011%29.pdf http://www.chemenviron.net/ICCE/ Khan, Zakir and Yusup, Suzana and Ahmad, Murni M and Ramli, Anita and Arpin, Mohamad Taufiq and Abdullah, S. S and Mohamad, Mas Fatiha and Misi, Siti Eda Eliana and Inayat, Abrar (2011) Effect of Steam and Catalyst on Palm Waste Thermal Decomposition for Hydrogen Production. In: 5th International Congress of Chemistry and Environment (ICCE 2011), 27-29 May 2011, Port Dickson, Malaysia. http://eprints.utp.edu.my/7050/
institution Universiti Teknologi Petronas
building UTP Resource Centre
collection Institutional Repository
continent Asia
country Malaysia
content_provider Universiti Teknologi Petronas
content_source UTP Institutional Repository
url_provider http://eprints.utp.edu.my/
topic TP Chemical technology
spellingShingle TP Chemical technology
Khan, Zakir
Yusup, Suzana
Ahmad, Murni M
Ramli, Anita
Arpin, Mohamad Taufiq
Abdullah, S. S
Mohamad, Mas Fatiha
Misi, Siti Eda Eliana
Inayat, Abrar
Effect of Steam and Catalyst on Palm Waste Thermal Decomposition for Hydrogen Production
description The thermal decomposition of palm oil wastes in the form of palm shell and palm oil fronds in the presence of steam and catalyst was experimentally investigated using thermogravimetric analyzer-gas chromatography (TGA-GC). The hydrogen gas composition was observed for palm oil wastes thermal decomposition i) under inert atmosphere (no steam), ii) in steam gasification and iii) in catalytic steam gasification using a newly developed bi metallic catalyst. Detailed discussion has been made for product gas composition profiles at steam-to-biomass ratio of 1 and biomass-to-catalyst ratio of 3. Maximum H2 content up to 64 mol% and 50 mol% in product gas was observed for palm shell and palm oil fronds, respectively, in the catalytic steam gasification. The usage of steam has almost increased H2 content by 28% for both palm oil wastes. The catalyst usage in the steam gasification increased H2 content by 12.5% and 6% for palm shell and palm oil fronds, respectively. Moreover, CO2 concentration in the product gas was reduced in steam gasification where CO concentration was decreased in catalytic steam gasification. This decrease in CO concentration is due to the bi metallic catalyst activity on water gas shift reaction.
format Conference or Workshop Item
author Khan, Zakir
Yusup, Suzana
Ahmad, Murni M
Ramli, Anita
Arpin, Mohamad Taufiq
Abdullah, S. S
Mohamad, Mas Fatiha
Misi, Siti Eda Eliana
Inayat, Abrar
author_facet Khan, Zakir
Yusup, Suzana
Ahmad, Murni M
Ramli, Anita
Arpin, Mohamad Taufiq
Abdullah, S. S
Mohamad, Mas Fatiha
Misi, Siti Eda Eliana
Inayat, Abrar
author_sort Khan, Zakir
title Effect of Steam and Catalyst on Palm Waste Thermal Decomposition for Hydrogen Production
title_short Effect of Steam and Catalyst on Palm Waste Thermal Decomposition for Hydrogen Production
title_full Effect of Steam and Catalyst on Palm Waste Thermal Decomposition for Hydrogen Production
title_fullStr Effect of Steam and Catalyst on Palm Waste Thermal Decomposition for Hydrogen Production
title_full_unstemmed Effect of Steam and Catalyst on Palm Waste Thermal Decomposition for Hydrogen Production
title_sort effect of steam and catalyst on palm waste thermal decomposition for hydrogen production
publishDate 2011
url http://eprints.utp.edu.my/7050/1/Effect_of_Steam_and_catalyst_on_palm_oil_wastes_thermal_decomposition_for_hydrogen_production_%28ICCE_2011%29.pdf
http://www.chemenviron.net/ICCE/
http://eprints.utp.edu.my/7050/
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