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Cold Lake asphaltenes hydroconversion

The thermal hydroconversion of Cold Lake asphaltenes was studied initially to provide a basis for evaluation of catalytic effectiveness in subsequent work. Series of thermal runs were made at 335°C, 365°C and 400°C and the reaction products were separated as described previously. Several kinetic models were tried, but after examining the variability of our data, we decided on the simple first-order asphaltene decomposition model shown below ... [Pg.327]

Figure 1. Thermal hydroconversion of Cold Lake asphaltenes at 400°C and 6 MPa H2 asphaltenes ( A) maltenes (O) coke ) model (-). Figure 1. Thermal hydroconversion of Cold Lake asphaltenes at 400°C and 6 MPa H2 asphaltenes ( A) maltenes (O) coke ) model (-).
Figure 3. Arrhenius plot for hydroconversion of Cold Lake asphaltenes 200 ppm molybdenum (A) thermal (0). Figure 3. Arrhenius plot for hydroconversion of Cold Lake asphaltenes 200 ppm molybdenum (A) thermal (0).

See other pages where Cold Lake asphaltenes hydroconversion is mentioned: [Pg.324]    [Pg.325]    [Pg.342]   


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