Dealuminated ZSM-5 zeolite catalyst for ethylene oligomerization to liquid fuels

Ethylene oligomerization using ZSM-5 zeolite was investigated to study the role of Bronsted acid sites in the formation of higher hydrocarbons. The oligomerization of olefins, dependent on the acidity of ZSM-5 zeolite, is an important step in the conversion of natural gas to liquid fuels. The framew...

Full description

Bibliographic Details
Main Authors: Saidina Amin, Nor Aishah, Anggoro, Didi Dwi
Format: Article
Language:English
Published: Science Press 2002
Subjects:
Online Access:http://eprints.utm.my/4662/
http://eprints.utm.my/4662/1/NoorAishahSaidinaAmin2002_DealuminatedZSM-5ZeoliteCatalyst.pdf
_version_ 1848890859073830912
author Saidina Amin, Nor Aishah
Anggoro, Didi Dwi
author_facet Saidina Amin, Nor Aishah
Anggoro, Didi Dwi
author_sort Saidina Amin, Nor Aishah
building UTeM Institutional Repository
collection Online Access
description Ethylene oligomerization using ZSM-5 zeolite was investigated to study the role of Bronsted acid sites in the formation of higher hydrocarbons. The oligomerization of olefins, dependent on the acidity of ZSM-5 zeolite, is an important step in the conversion of natural gas to liquid fuels. The framework Si/Al ratio reflects the number of potential acid sites and the acid strength of the ZSM-5 catalyst. ZSM-5 with the mole ratio SiO2/Al2O3 equal to 30 was dealuminated for different periods of time according to the acidic ion-exchange method to produce ZSM-5 with various Si/Al ratios. The FT-IR analysis revealed that the integrated framework aluminum band, non-framework aluminum band, and silanol groups areas of the ZSM-5 zeolites decreased after being dealuminated. The performance of dealuminated zeolite was tested for ethylene oligomerization. The result demonstrated that the dealumination of ZSM-5 led to higher ethylene conversion, but the gasoline selectivity was reduced compared to the performance of a ZSM-5 zeolite. The characterization results revealed that the amount of aluminum in the zeolitic framework, the crystallinity of the ZSM-5 zeolite and the Si/Al ratio affected the formation of Bronsted acid sites. The number of the Bronsted acid sites on the catalyst active sites is important in the olefin conversion to liquid hydrocarbons.
first_indexed 2025-11-15T20:48:46Z
format Article
id utm-4662
institution Universiti Teknologi Malaysia
institution_category Local University
language English
last_indexed 2025-11-15T20:48:46Z
publishDate 2002
publisher Science Press
recordtype eprints
repository_type Digital Repository
spelling utm-46622017-05-08T08:04:08Z http://eprints.utm.my/4662/ Dealuminated ZSM-5 zeolite catalyst for ethylene oligomerization to liquid fuels Saidina Amin, Nor Aishah Anggoro, Didi Dwi T Technology (General) Ethylene oligomerization using ZSM-5 zeolite was investigated to study the role of Bronsted acid sites in the formation of higher hydrocarbons. The oligomerization of olefins, dependent on the acidity of ZSM-5 zeolite, is an important step in the conversion of natural gas to liquid fuels. The framework Si/Al ratio reflects the number of potential acid sites and the acid strength of the ZSM-5 catalyst. ZSM-5 with the mole ratio SiO2/Al2O3 equal to 30 was dealuminated for different periods of time according to the acidic ion-exchange method to produce ZSM-5 with various Si/Al ratios. The FT-IR analysis revealed that the integrated framework aluminum band, non-framework aluminum band, and silanol groups areas of the ZSM-5 zeolites decreased after being dealuminated. The performance of dealuminated zeolite was tested for ethylene oligomerization. The result demonstrated that the dealumination of ZSM-5 led to higher ethylene conversion, but the gasoline selectivity was reduced compared to the performance of a ZSM-5 zeolite. The characterization results revealed that the amount of aluminum in the zeolitic framework, the crystallinity of the ZSM-5 zeolite and the Si/Al ratio affected the formation of Bronsted acid sites. The number of the Bronsted acid sites on the catalyst active sites is important in the olefin conversion to liquid hydrocarbons. Science Press 2002 Article PeerReviewed application/pdf en http://eprints.utm.my/4662/1/NoorAishahSaidinaAmin2002_DealuminatedZSM-5ZeoliteCatalyst.pdf Saidina Amin, Nor Aishah and Anggoro, Didi Dwi (2002) Dealuminated ZSM-5 zeolite catalyst for ethylene oligomerization to liquid fuels. Journal of Natural Gas Chemistry , 11 (1-2). pp. 79-86. ISSN 1003-9953 http://www.jenergchem.org/EN/Y2002/V11 /I1/79
spellingShingle T Technology (General)
Saidina Amin, Nor Aishah
Anggoro, Didi Dwi
Dealuminated ZSM-5 zeolite catalyst for ethylene oligomerization to liquid fuels
title Dealuminated ZSM-5 zeolite catalyst for ethylene oligomerization to liquid fuels
title_full Dealuminated ZSM-5 zeolite catalyst for ethylene oligomerization to liquid fuels
title_fullStr Dealuminated ZSM-5 zeolite catalyst for ethylene oligomerization to liquid fuels
title_full_unstemmed Dealuminated ZSM-5 zeolite catalyst for ethylene oligomerization to liquid fuels
title_short Dealuminated ZSM-5 zeolite catalyst for ethylene oligomerization to liquid fuels
title_sort dealuminated zsm-5 zeolite catalyst for ethylene oligomerization to liquid fuels
topic T Technology (General)
url http://eprints.utm.my/4662/
http://eprints.utm.my/4662/
http://eprints.utm.my/4662/1/NoorAishahSaidinaAmin2002_DealuminatedZSM-5ZeoliteCatalyst.pdf