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

被引：126

作者：

Hew, K. L. ^{[1
]}

Tamidi, A. M. ^{[1
]}

Yusup, S. ^{[1
]}

Lee, K. T. ^{[2
]}

Ahmad, M. M. ^{[1
]}

机构：

[1] Univ Teknol PETRONAS, Dept Chem Engn, Tronoh 31750, Perak, Malaysia

[2] Univ Sains Malaysia, Sch Chem Engn, Nibong Tebal 14300, Pulau Pinang, Malaysia

来源：

BIORESOURCE TECHNOLOGY | 2010年 / 101卷 / 22期

关键词：

Bio-oil; Empty fruit bunch; Gasoline; Catalytic cracking; Taguchi Method; HYDROCARBON FUELS; PYROLYSIS VAPORS; CONVERSION; HZSM-5;

D O I：

10.1016/j.biortech.2010.05.036

中图分类号：

S2 [农业工程];

学科分类号：

0828 ;

摘要：

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 degrees 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. (C) 2010 Elsevier Ltd. All rights reserved.

引用

页码：8855 / 8858

页数：4

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