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Petroleum Refinery Engineering

Petroleum Refinery Engineering
In catalytic cracking process, olefins crack __________ times faster than in thermal cracking process.

100
10
1000-10000
200-300

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Petroleum Refinery Engineering
Flash point of an oil gives an idea of the

All of these
Amount of low boiling fraction present
Nature of boiling point diagram of the system
Explosion hazards

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Petroleum Refinery Engineering
The main reaction in reforming is the

Saturation of olefins
Dehydrogenation of naphthenes
Hydrocracking of paraffins
Hydrogenation of naphthenes

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Petroleum Refinery Engineering
Petroleum liquid fuels having flash point greater than 66°C is considered as safe during storage and handling. Which of the following has flash point > 66°C ?

Petrol
Naphtha
Heavy fuel oil
Kerosene

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

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

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Petroleum Refinery Engineering
Raw Kerosene has a smoke point of 15 mm. After it is subjected to dearomatisation by liquid SO₂ extraction (Edeleanu process), its smoke point may become __________ mm.

100
10
5
25

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