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...
محفوظ في:
المؤلف الرئيسي: | Ahmed Alsobaai, Ahmed Mubarak |
---|---|
التنسيق: | أطروحة |
اللغة: | English |
منشور في: |
2003
|
الموضوعات: | |
الوصول للمادة أونلاين: | http://eprints.usm.my/59461/1/24%20Pages%20from%2000001606663.pdf |
الوسوم: |
إضافة وسم
لا توجد وسوم, كن أول من يضع وسما على هذه التسجيلة!
|
مواد مشابهة
-
Transesterification Of Virgin And Waste Cooking Palm Oil Using Calcium Oxide Catalyst Supported On Activated Carbon.
بواسطة: Kamis, Wan Zuraida Wan
منشور في: (2010) -
Development Of Niw-Zeolite-Based Catalysts For Hydrocracking Of Gas Oil: Synthesis, Characterization,
Activity And Kinetics Studies
بواسطة: Ahmed Alsobaai, Ahmed Mubarak
منشور في: (2007) -
Synthesis Of Carbon Nanotubes Via Decomposition Of Methane Using Carbon Supported Catalysts
بواسطة: Murugaiyan, Sivakumar Vaiyazhipalayam
منشور في: (2011) -
Development Of Silica-Based And Activated
Carbon-Based Catalysts For Glycerol
Acetylation, Transesterification And
Acetalization Processes For The Production Of
Oxygenated Fuel Additives
بواسطة: Khayoon, Muataz Shakir
منشور في: (2013) -
Silica Supported Indium
Heterogeneous Catalyst In
Benzylation And Benzoylation Of
Toluene
بواسطة: Sek, Kei Lin
منشور في: (2013)