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Petroleum Refinery Engineering

Petroleum Refinery Engineering
Pressure & temperature maintained in catalytic cracking is about

10atm & 500°C
50atm. & 750°C
30atm & 200°C
2atm & 500°C

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Petroleum Refinery Engineering
95% (by volume) of LPG at 760 mm Hg pressure will evaporate at __________ °C.

-40
55
2
30

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Petroleum Refinery Engineering
Which of the following is used as a catalyst in fluidised bed catalytic cracking?

Silica-magnesia
Silica-alumina
Bentonite clays
All of these

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Petroleum Refinery Engineering
Carbon/hydrogen ratio (by weight) is maximum (out of following) for

Heavy fuel oil
Gasoline
Light gas oil
Kerosene

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Petroleum Refinery Engineering
An upper limit of oil content is limited to about __________ percent for achieving efficient and satisfactory level of wax sweating.

60
5
40
15

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Petroleum Refinery Engineering
Presence of aromatics in

All of these
Kerosene increases its smoke point
Diesel increases its cetane number
Petrol increases its octane number

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