Comparative study for catalytic cracking of model bio-oil and palm kernel shell derived bio-oil
This work investigates the comparison between upgraded product from model bio-oil and bio-oil from PKS. The process is carried out in the presence of HZSM-5 at temperature of 500°C, 3bar pressure and oil/catalyst ratio of 15. It is observed that the properties such as pH, density, calorific value a...
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my.utp.eprints.327192022-03-30T01:04:54Z Comparative study for catalytic cracking of model bio-oil and palm kernel shell derived bio-oil Jamil, F. Ahmad, M.M. Yusup, S. This work investigates the comparison between upgraded product from model bio-oil and bio-oil from PKS. The process is carried out in the presence of HZSM-5 at temperature of 500°C, 3bar pressure and oil/catalyst ratio of 15. It is observed that the properties such as pH, density, calorific value and elemental value of products are improved. The calorific value for upgraded bio-oil is 31.65 MJ/kg while for model bio-oil the value is 30.32 MJ/kg at same operating conditions. The degree of deoxygenation of the upgraded bio-oil and upgraded model bio-oil is 43.74 and 45.56 respectively. The study showed that the model bio-oil can be used to represent the bio-oil. © (2013)Trans Tech Publications,Switzerland. 2013 Article NonPeerReviewed https://www.scopus.com/inward/record.uri?eid=2-s2.0-84886266198&doi=10.4028%2fwww.scientific.net%2fAMR.781-784.2476&partnerID=40&md5=df193b4eb6e3b0a98e6bcdf30687b3f3 Jamil, F. and Ahmad, M.M. and Yusup, S. (2013) Comparative study for catalytic cracking of model bio-oil and palm kernel shell derived bio-oil. Advanced Materials Research, 781-78 . pp. 2476-2479. http://eprints.utp.edu.my/32719/ |
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This work investigates the comparison between upgraded product from model bio-oil and bio-oil from PKS. The process is carried out in the presence of HZSM-5 at temperature of 500°C, 3bar pressure and oil/catalyst ratio of 15. It is observed that the properties such as pH, density, calorific value and elemental value of products are improved. The calorific value for upgraded bio-oil is 31.65 MJ/kg while for model bio-oil the value is 30.32 MJ/kg at same operating conditions. The degree of deoxygenation of the upgraded bio-oil and upgraded model bio-oil is 43.74 and 45.56 respectively. The study showed that the model bio-oil can be used to represent the bio-oil. © (2013)Trans Tech Publications,Switzerland. |
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Article |
author |
Jamil, F. Ahmad, M.M. Yusup, S. |
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Jamil, F. Ahmad, M.M. Yusup, S. Comparative study for catalytic cracking of model bio-oil and palm kernel shell derived bio-oil |
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Jamil, F. Ahmad, M.M. Yusup, S. |
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Jamil, F. |
title |
Comparative study for catalytic cracking of model bio-oil and palm kernel shell derived bio-oil |
title_short |
Comparative study for catalytic cracking of model bio-oil and palm kernel shell derived bio-oil |
title_full |
Comparative study for catalytic cracking of model bio-oil and palm kernel shell derived bio-oil |
title_fullStr |
Comparative study for catalytic cracking of model bio-oil and palm kernel shell derived bio-oil |
title_full_unstemmed |
Comparative study for catalytic cracking of model bio-oil and palm kernel shell derived bio-oil |
title_sort |
comparative study for catalytic cracking of model bio-oil and palm kernel shell derived bio-oil |
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2013 |
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https://www.scopus.com/inward/record.uri?eid=2-s2.0-84886266198&doi=10.4028%2fwww.scientific.net%2fAMR.781-784.2476&partnerID=40&md5=df193b4eb6e3b0a98e6bcdf30687b3f3 http://eprints.utp.edu.my/32719/ |
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