Catalytic cracking of bio-oil to organic liquid product (OLP)

The main objective of this paper is to find the optimum operating condition to upgrade the EFB-derived pyrolysis oil (bio-oil) to liquid fuel, mainly gasoline using Taguchi Method. From the analysis that has been done, it is found that the optimum operating condition for heterogeneous catalytic crac...

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Main Authors: Hew, K. L., Tamidi, A. M., Yusup, Suzana, Ahmad, Murni M
Format: Article
Language:English
Published: Elsevier 2010
Subjects:
Online Access:http://scholars.utp.edu.my/id/eprint/2949/
http://scholars.utp.edu.my/id/eprint/2949/1/catalytic_cracking_of_bio_oil_to_organic_liquid_product_%28OLP%29.PDF
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author Hew, K. L.
Tamidi, A. M.
Yusup, Suzana
Ahmad, Murni M
author_facet Hew, K. L.
Tamidi, A. M.
Yusup, Suzana
Ahmad, Murni M
author_sort Hew, K. L.
building UTP Institutional Repository
collection Online Access
description The main objective of this paper is to find the optimum operating condition to upgrade the EFB-derived pyrolysis oil (bio-oil) to liquid fuel, mainly gasoline using Taguchi Method. From the analysis that has been done, it is found that the optimum operating condition for heterogeneous catalytic cracking process is at 400 °C, 15 min of reaction time using 30 g of catalyst weight where operating at this condition produced the highest yield of gasoline fraction which is 91.67 wt.%. This observation proves that EFB-derived pyrolysis oil could be upgraded via heterogeneous catalytic cracking to produce gasoline.
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spelling oai:scholars.utp.edu.my:29492017-01-19T08:23:54Z http://scholars.utp.edu.my/id/eprint/2949/ Catalytic cracking of bio-oil to organic liquid product (OLP) Hew, K. L. Tamidi, A. M. Yusup, Suzana Ahmad, Murni M TP Chemical technology The main objective of this paper is to find the optimum operating condition to upgrade the EFB-derived pyrolysis oil (bio-oil) to liquid fuel, mainly gasoline using Taguchi Method. From the analysis that has been done, it is found that the optimum operating condition for heterogeneous catalytic cracking process is at 400 °C, 15 min of reaction time using 30 g of catalyst weight where operating at this condition produced the highest yield of gasoline fraction which is 91.67 wt.%. This observation proves that EFB-derived pyrolysis oil could be upgraded via heterogeneous catalytic cracking to produce gasoline. Elsevier 2010-07-10 Article PeerReviewed application/pdf en http://scholars.utp.edu.my/id/eprint/2949/1/catalytic_cracking_of_bio_oil_to_organic_liquid_product_%28OLP%29.PDF Hew, K. L. and Tamidi, A. M. and Yusup, Suzana and Ahmad, Murni M (2010) Catalytic cracking of bio-oil to organic liquid product (OLP). Bioresource Technology, 101 (22). pp. 8855-8858. ISSN 0960-8524 http://www.sciencedirect.com/science/article/B6V24-50H1HBP-1/2/075c4403a68610b174cd3bc0adff77ee DOI: 10.1016/j.biortech.2010.05.036 DOI: 10.1016/j.biortech.2010.05.036
spellingShingle TP Chemical technology
Hew, K. L.
Tamidi, A. M.
Yusup, Suzana
Ahmad, Murni M
Catalytic cracking of bio-oil to organic liquid product (OLP)
title Catalytic cracking of bio-oil to organic liquid product (OLP)
title_full Catalytic cracking of bio-oil to organic liquid product (OLP)
title_fullStr Catalytic cracking of bio-oil to organic liquid product (OLP)
title_full_unstemmed Catalytic cracking of bio-oil to organic liquid product (OLP)
title_short Catalytic cracking of bio-oil to organic liquid product (OLP)
title_sort catalytic cracking of bio-oil to organic liquid product (olp)
topic TP Chemical technology
url http://scholars.utp.edu.my/id/eprint/2949/
http://scholars.utp.edu.my/id/eprint/2949/
http://scholars.utp.edu.my/id/eprint/2949/
http://scholars.utp.edu.my/id/eprint/2949/1/catalytic_cracking_of_bio_oil_to_organic_liquid_product_%28OLP%29.PDF