Hydrocracking And Hydrodesulphurization Activities Of Nimo Catalyst Supported On Alumina And Activated Carbons For Petroleum

This study aims to improve petroleum residual oil quality by converting it into lighter products over different types of catalysts. The process was conducted in a batch mode under various operating conditions, temperature in range 250-350 °C, reaction time 90- 230 min and catalyst ratio 0.3-1.30...

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Main Author: Ahmed Alsobaai, Ahmed Mubarak
Format: Thesis
Language:English
Published: 2003
Subjects:
Online Access:http://eprints.usm.my/59461/
http://eprints.usm.my/59461/1/24%20Pages%20from%2000001606663.pdf
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author Ahmed Alsobaai, Ahmed Mubarak
author_facet Ahmed Alsobaai, Ahmed Mubarak
author_sort Ahmed Alsobaai, Ahmed Mubarak
building USM Institutional Repository
collection Online Access
description This study aims to improve petroleum residual oil quality by converting it into lighter products over different types of catalysts. The process was conducted in a batch mode under various operating conditions, temperature in range 250-350 °C, reaction time 90- 230 min and catalyst ratio 0.3-1.30 using a high-pressure stirred reactor in the presence of hydrogen and catalyst. At first commercial NiMo/Ah03 catalyst was used to find the range of operation conditions for catalytic hydrocracking of petroleum residual oi). Statistical design of experiment, (DOE), was used to obtain the range of operating conditions. It was found that the range of operating conditions for catalytic hydrocracking of petroleum residual oil over commercial NiMo/Ah03 sulphided catalyst are: temperature of 330°C, time of 200 min and catalyst ratio of 1.1.
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institution Universiti Sains Malaysia
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language English
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publishDate 2003
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spelling usm-594612023-10-10T07:07:44Z http://eprints.usm.my/59461/ Hydrocracking And Hydrodesulphurization Activities Of Nimo Catalyst Supported On Alumina And Activated Carbons For Petroleum Ahmed Alsobaai, Ahmed Mubarak TP1-1185 Chemical technology This study aims to improve petroleum residual oil quality by converting it into lighter products over different types of catalysts. The process was conducted in a batch mode under various operating conditions, temperature in range 250-350 °C, reaction time 90- 230 min and catalyst ratio 0.3-1.30 using a high-pressure stirred reactor in the presence of hydrogen and catalyst. At first commercial NiMo/Ah03 catalyst was used to find the range of operation conditions for catalytic hydrocracking of petroleum residual oi). Statistical design of experiment, (DOE), was used to obtain the range of operating conditions. It was found that the range of operating conditions for catalytic hydrocracking of petroleum residual oil over commercial NiMo/Ah03 sulphided catalyst are: temperature of 330°C, time of 200 min and catalyst ratio of 1.1. 2003-09 Thesis NonPeerReviewed application/pdf en http://eprints.usm.my/59461/1/24%20Pages%20from%2000001606663.pdf Ahmed Alsobaai, Ahmed Mubarak (2003) Hydrocracking And Hydrodesulphurization Activities Of Nimo Catalyst Supported On Alumina And Activated Carbons For Petroleum. Masters thesis, Perpustakaan Hamzah Sendut.
spellingShingle TP1-1185 Chemical technology
Ahmed Alsobaai, Ahmed Mubarak
Hydrocracking And Hydrodesulphurization Activities Of Nimo Catalyst Supported On Alumina And Activated Carbons For Petroleum
title Hydrocracking And Hydrodesulphurization Activities Of Nimo Catalyst Supported On Alumina And Activated Carbons For Petroleum
title_full Hydrocracking And Hydrodesulphurization Activities Of Nimo Catalyst Supported On Alumina And Activated Carbons For Petroleum
title_fullStr Hydrocracking And Hydrodesulphurization Activities Of Nimo Catalyst Supported On Alumina And Activated Carbons For Petroleum
title_full_unstemmed Hydrocracking And Hydrodesulphurization Activities Of Nimo Catalyst Supported On Alumina And Activated Carbons For Petroleum
title_short Hydrocracking And Hydrodesulphurization Activities Of Nimo Catalyst Supported On Alumina And Activated Carbons For Petroleum
title_sort hydrocracking and hydrodesulphurization activities of nimo catalyst supported on alumina and activated carbons for petroleum
topic TP1-1185 Chemical technology
url http://eprints.usm.my/59461/
http://eprints.usm.my/59461/1/24%20Pages%20from%2000001606663.pdf