Catalytic Cracking of Pyrolysis Oil Derived from Rubberwood to Produce Green Gasoline Components
An attempt was made to generate gasoline-range aromatics from pyrolysis oil derived from rubberwood. Catalytic cracking of the pyrolysis oil was conducted using an HZSM-5 catalyst in a dual reactor. The effects of reaction temperature, catalyst weight, and nitrogen flow rate were investigated to det...
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North Carolina State University
2015-04-01
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doaj-4562a3e370404dc195eb296e300467712020-11-24T23:17:56ZengNorth Carolina State UniversityBioResources1930-21261930-21262015-04-011023224324110.15376/biores.10.2.3224-3241Catalytic Cracking of Pyrolysis Oil Derived from Rubberwood to Produce Green Gasoline ComponentsAbdulrahim Saad0Sukritthira Ratanawilai1Chakrit Tongurai2Prince of Songkla University; ThailandPrince of Songkla University; ThailandDepartment of Chemical Engineering, Faculty of Engineering, Prince of Songkla University, Had Yai, Songkhla, 90112, Thailand; ThailandAn attempt was made to generate gasoline-range aromatics from pyrolysis oil derived from rubberwood. Catalytic cracking of the pyrolysis oil was conducted using an HZSM-5 catalyst in a dual reactor. The effects of reaction temperature, catalyst weight, and nitrogen flow rate were investigated to determine the yield of organic liquid product (OLP) and the percentage of gasoline aromatics in the OLP. The results showed that the maximum OLP yield was about 13.6 wt%, which was achieved at 511 C, a catalyst weight of 3.2 g, and an N2 flow rate of 3 mL/min. The maximum percentage of gasoline aromatics was about 27 wt%, which was obtained at 595 C, a catalyst weight of 5 g, and an N2 flow rate of 3 mL/min. Although the yield of gasoline aromatics was low, the expected components were detected in the OLP, including benzene, toluene, ethyl benzene, and xylenes (BTEX). These findings demonstrated that green gasoline aromatics can be produced from rubberwood pyrolysis oil via zeolite cracking.http://ojs.cnr.ncsu.edu/index.php/BioRes/article/view/BioRes_10_2_3224_Saad_Catalytic_Cracking_Pyrolysis_OilPyrolysis oilZeolite crackingOrganic liquid product (OLP)Green gasoline-range aromatics |
collection |
DOAJ |
language |
English |
format |
Article |
sources |
DOAJ |
author |
Abdulrahim Saad Sukritthira Ratanawilai Chakrit Tongurai |
spellingShingle |
Abdulrahim Saad Sukritthira Ratanawilai Chakrit Tongurai Catalytic Cracking of Pyrolysis Oil Derived from Rubberwood to Produce Green Gasoline Components BioResources Pyrolysis oil Zeolite cracking Organic liquid product (OLP) Green gasoline-range aromatics |
author_facet |
Abdulrahim Saad Sukritthira Ratanawilai Chakrit Tongurai |
author_sort |
Abdulrahim Saad |
title |
Catalytic Cracking of Pyrolysis Oil Derived from Rubberwood to Produce Green Gasoline Components |
title_short |
Catalytic Cracking of Pyrolysis Oil Derived from Rubberwood to Produce Green Gasoline Components |
title_full |
Catalytic Cracking of Pyrolysis Oil Derived from Rubberwood to Produce Green Gasoline Components |
title_fullStr |
Catalytic Cracking of Pyrolysis Oil Derived from Rubberwood to Produce Green Gasoline Components |
title_full_unstemmed |
Catalytic Cracking of Pyrolysis Oil Derived from Rubberwood to Produce Green Gasoline Components |
title_sort |
catalytic cracking of pyrolysis oil derived from rubberwood to produce green gasoline components |
publisher |
North Carolina State University |
series |
BioResources |
issn |
1930-2126 1930-2126 |
publishDate |
2015-04-01 |
description |
An attempt was made to generate gasoline-range aromatics from pyrolysis oil derived from rubberwood. Catalytic cracking of the pyrolysis oil was conducted using an HZSM-5 catalyst in a dual reactor. The effects of reaction temperature, catalyst weight, and nitrogen flow rate were investigated to determine the yield of organic liquid product (OLP) and the percentage of gasoline aromatics in the OLP. The results showed that the maximum OLP yield was about 13.6 wt%, which was achieved at 511 C, a catalyst weight of 3.2 g, and an N2 flow rate of 3 mL/min. The maximum percentage of gasoline aromatics was about 27 wt%, which was obtained at 595 C, a catalyst weight of 5 g, and an N2 flow rate of 3 mL/min. Although the yield of gasoline aromatics was low, the expected components were detected in the OLP, including benzene, toluene, ethyl benzene, and xylenes (BTEX). These findings demonstrated that green gasoline aromatics can be produced from rubberwood pyrolysis oil via zeolite cracking. |
topic |
Pyrolysis oil Zeolite cracking Organic liquid product (OLP) Green gasoline-range aromatics |
url |
http://ojs.cnr.ncsu.edu/index.php/BioRes/article/view/BioRes_10_2_3224_Saad_Catalytic_Cracking_Pyrolysis_Oil |
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