Petroleum Refinery Engineering
Operating temperature and pressure in catalytic reforming is about

15-45 Kgf/cm² & 450-550°C
50 - 75 kgf/cm² & 600 - 800°C
5-10 kgf/cm² & 150 - 250°C
1-5 Kgf/cm² & 200°C

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Petroleum Refinery Engineering
Pick out the correct statement pertaining to catalytic cracking.

All of these
With increase in the reactor pressure, octane number of gasoline decreases
With increase in the reactor temperature, gasoline yield decreases for a given conversion
Percentage conversion increases with increase in the catalyst to oil ratio

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