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Petroleum Refinery Engineering

Petroleum Refinery Engineering
Molecular weight of crude petroleum may be around

1500
5000
50
250

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Petroleum Refinery Engineering
Flash point of motor gasoline may be around __________ °C.

10
45
100
150

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Petroleum Refinery Engineering
Which of the following reactions is undesirable in the production of catalytically reformed gasoline?

Dehydrocyclisation of higher paraffins
Isomerisation of paraffins
Dehydrogenation of naphthene
Dehydrogenation of lower paraffins

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Petroleum Refinery Engineering
__________ converts n-paraffins to i-paraffins.

Alkylation
Polymerisation
None of these
Isomerisation

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Petroleum Refinery Engineering
Hydrogen percentage (by weight) in crude petroleum may be about

25
15
35
5

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Petroleum Refinery Engineering
Which of the following processes in oil refinery does not employ 'cracking'?

Visbreaking
Pyrolysis
None of these
Coking

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