Catalytic Cracking of Iraqi Vacuum Gasoil Using Large and Medium Pore Size of Zeolite Catalysts

The catalytic cracking conversion of Iraqi vacuum gas oil was studied on large and medium pore size (HY, HX, ZSM-22 and ZSM-11) of zeolite catalysts. These catalysts were prepared locally and used in the present work. The catalytic conversion performed on a continuous fixed-bed laboratory reaction u...

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Autores principales:	Ameel Mohammed Rahman, Mohanned H. Salman, Khalid Waleed Hammed
Formato:	article
Lenguaje:	EN
Publicado:	Al-Khwarizmi College of Engineering – University of Baghdad 2015
Materias:	Chemical engineering TP155-156 Engineering (General). Civil engineering (General) TA1-2040
Acceso en línea:	https://doaj.org/article/f1d1170f60134cb9a314e3a427b158c6
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spelling	oai:doaj.org-article:f1d1170f60134cb9a314e3a427b158c62021-12-02T06:41:03ZCatalytic Cracking of Iraqi Vacuum Gasoil Using Large and Medium Pore Size of Zeolite Catalysts 1818-1171https://doaj.org/article/f1d1170f60134cb9a314e3a427b158c62015-03-01T00:00:00Zhttp://www.iasj.net/iasj?func=fulltext&aId=99184https://doaj.org/toc/1818-1171The catalytic cracking conversion of Iraqi vacuum gas oil was studied on large and medium pore size (HY, HX, ZSM-22 and ZSM-11) of zeolite catalysts. These catalysts were prepared locally and used in the present work. The catalytic conversion performed on a continuous fixed-bed laboratory reaction unit. Experiments were performed in the temperature range of 673 to 823K, pressure range of 3 to 15bar, and LHSV range of 0.5-3h-1. The results show that the catalytic conversion of vacuum gas oil increases with increase in reaction temperature and decreases with increase in LHSV. The catalytic activity for the proposed catalysts arranged in the following order: HY>HX>ZSM-11>ZSM-22 The product distribution depends greatly on the temperature and on the catalyst type. A higher hydrocarbon yields was obtained for HY zeolite catalyst. The selectivity towards high octane number compounds for the proposed catalysts are arranged in the following order: HY>HX>ZSM-11>ZSM-22 The cracking conversion is improved by increasing reaction pressure up to 15 bar. The simulated experiments of the catalytic cracking process show that the higher conversion and more desired products can be achieved to conventional feeds.Ameel Mohammed RahmanMohanned H. Salman Khalid Waleed HammedAl-Khwarizmi College of Engineering – University of BaghdadarticleChemical engineeringTP155-156Engineering (General). Civil engineering (General)TA1-2040ENAl-Khawarizmi Engineering Journal, Vol 11, Iss 1, Pp 73-83 (2015)
institution	DOAJ
collection	DOAJ
language	EN
topic	Chemical engineering TP155-156 Engineering (General). Civil engineering (General) TA1-2040
spellingShingle	Chemical engineering TP155-156 Engineering (General). Civil engineering (General) TA1-2040 Ameel Mohammed Rahman Mohanned H. Salman Khalid Waleed Hammed Catalytic Cracking of Iraqi Vacuum Gasoil Using Large and Medium Pore Size of Zeolite Catalysts
description	The catalytic cracking conversion of Iraqi vacuum gas oil was studied on large and medium pore size (HY, HX, ZSM-22 and ZSM-11) of zeolite catalysts. These catalysts were prepared locally and used in the present work. The catalytic conversion performed on a continuous fixed-bed laboratory reaction unit. Experiments were performed in the temperature range of 673 to 823K, pressure range of 3 to 15bar, and LHSV range of 0.5-3h-1. The results show that the catalytic conversion of vacuum gas oil increases with increase in reaction temperature and decreases with increase in LHSV. The catalytic activity for the proposed catalysts arranged in the following order: HY>HX>ZSM-11>ZSM-22 The product distribution depends greatly on the temperature and on the catalyst type. A higher hydrocarbon yields was obtained for HY zeolite catalyst. The selectivity towards high octane number compounds for the proposed catalysts are arranged in the following order: HY>HX>ZSM-11>ZSM-22 The cracking conversion is improved by increasing reaction pressure up to 15 bar. The simulated experiments of the catalytic cracking process show that the higher conversion and more desired products can be achieved to conventional feeds.
format	article
author	Ameel Mohammed Rahman Mohanned H. Salman Khalid Waleed Hammed
author_facet	Ameel Mohammed Rahman Mohanned H. Salman Khalid Waleed Hammed
author_sort	Ameel Mohammed Rahman
title	Catalytic Cracking of Iraqi Vacuum Gasoil Using Large and Medium Pore Size of Zeolite Catalysts
title_short	Catalytic Cracking of Iraqi Vacuum Gasoil Using Large and Medium Pore Size of Zeolite Catalysts
title_full	Catalytic Cracking of Iraqi Vacuum Gasoil Using Large and Medium Pore Size of Zeolite Catalysts
title_fullStr	Catalytic Cracking of Iraqi Vacuum Gasoil Using Large and Medium Pore Size of Zeolite Catalysts
title_full_unstemmed	Catalytic Cracking of Iraqi Vacuum Gasoil Using Large and Medium Pore Size of Zeolite Catalysts
title_sort	catalytic cracking of iraqi vacuum gasoil using large and medium pore size of zeolite catalysts
publisher	Al-Khwarizmi College of Engineering – University of Baghdad
publishDate	2015
url	https://doaj.org/article/f1d1170f60134cb9a314e3a427b158c6
work_keys_str_mv	AT ameelmohammedrahman catalyticcrackingofiraqivacuumgasoilusinglargeandmediumporesizeofzeolitecatalysts AT mohannedhsalman catalyticcrackingofiraqivacuumgasoilusinglargeandmediumporesizeofzeolitecatalysts AT khalidwaleedhammed catalyticcrackingofiraqivacuumgasoilusinglargeandmediumporesizeofzeolitecatalysts
_version_	1718399788725043200

Catalytic Cracking of Iraqi Vacuum Gasoil Using Large and Medium Pore Size of Zeolite Catalysts

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