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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| 格式: | Thesis |
| 语言: | English |
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2003
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| 在线阅读: | http://eprints.usm.my/59461/1/24%20Pages%20from%2000001606663.pdf |
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