Name | Density at 20˚C, kg/m3 | Viscosity at 50˚C, mm2/s | Temperature of, ˚C: | Coking, % | Yield in % by weight of asphaltenes, with the method: | |||||
Freezing | Flash | Proposed | Existing | |||||||
Before | After | Before | After | |||||||
The extraction | The extraction | |||||||||
Oil | Initial | 865.9 | 7.11 | −10 | 5 | 1.91 | - |
| - |
|
The same, after deasphalting | 859.0 | 6.33 | −10 | 5 | 0.88 | 1.50 | 1.07 | 0.87 | 0.58 | |
Masut*) | Initial | 909.5 | 43.22 | +8 | 146 | 3.51 | - | - | - |
|
The same, diluted in n-heptane | 783.0 | 1.82 | - | - | - | - |
| - |
| |
The same, after deasphalting | 907.4 | 42.0 | +6 | 148 | 3.30 | 3.10 | 2.57 | 1.0 | 0.79 | |
Tar*) | Initial | 947.3 | 181.1**) | 49 | 280 | 4.67 | - |
| - |
|
The same, diluted in n-heptane | 787.0 | 4.19 | - | - | - | - |
| - |
| |
The same, after deasphalting | 940.3 | 105.6**) | 48 | 280 | 4.10 | 4.50 | 3.96 | 1.46 | 0.89 |