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Petroleum Refinery Engineering

Petroleum Refinery Engineering
Smoke volatility index is equal to smoke point plus

0.42 x(% distilled at 204°C)
0.84 x (% distilled at 204°C)
5 mm
10 mm. approximately

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Petroleum Refinery Engineering
H/C ratio (by weight) for the same number of carbon atoms is the highest in case of

Olefins
Aromatics
Naphthenes
Paraffins

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Petroleum Refinery Engineering
The main use of heavy gas oil produced by the vacuum distillation unit is as a

None of these
Blending component for kerosene
Feedstock for fluid catalytic cracking unit
Blending component for petrol

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Petroleum Refinery Engineering
Reforming converts

Naphthenes into olefins
Olefins into paraffins
Naphthenes into aromatics
Naphthenes into paraffin

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Petroleum Refinery Engineering
Catalyst used in the catalytic cracking is

Silica gel
Nickel
Vanadium pentoxide
Silica-alumina

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

55
-40
30
2

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