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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Main Authors: Abdulrahim Saad, Sukritthira Ratanawilai, Chakrit Tongurai
Format: Article
Language:English
Published: North Carolina State University 2015-04-01
Series:BioResources
Subjects:
Online Access:http://ojs.cnr.ncsu.edu/index.php/BioRes/article/view/BioRes_10_2_3224_Saad_Catalytic_Cracking_Pyrolysis_Oil
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spelling 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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AT sukritthiraratanawilai catalyticcrackingofpyrolysisoilderivedfromrubberwoodtoproducegreengasolinecomponents
AT chakrittongurai catalyticcrackingofpyrolysisoilderivedfromrubberwoodtoproducegreengasolinecomponents
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