| Parameter | Units | Value |
| Vapour density | kg∙m−3 | 9.52 |
| Liquid density at 2880 K | kg∙m−3 | 924.8 |
| Specific heat of gas | kj∙kg−1∙K−1 | 3.3 |
| Specific heat of liquid | kj∙kg−1∙K−1 | 2.67 |
| Heat of vaporization | kj∙kg−1 | 156 |
| Temperature of vapourization | K | 698 |
| -gas oil to gasoline | kj | −2970 |
| -gas oil to light hydrocarbon gases | kj | −9240 |
| -gas oil to coke | kj | 23,820 |
| -gasoline to light hydrocarbon | kj | −6030 |
| -gasoline to coke gases | kj | 22,606 |
| Catalyst |
|
|
| Bulk density | kg∙m−3 | 975 |
| Particle size | m | 95 × 10−6 |
| Specific heat capacity | kj∙kg−1∙K−1 | 1.12 |
| Mass flow rate of catalyst from the reactor to regenerate | kg/hr | 1,729,750 |