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Petroleum Refinery Engineering

Petroleum Refinery Engineering
In sweetening process, solutizer agent used with caustic alkali is

Methanol
Sodium plumbite
Potassium isobutyrate
Phenol

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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.

5
60
15
40

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Petroleum Refinery Engineering
Pour point and freezing point is equal for

Petrol
Water
Crude petroleum
Diesel

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Petroleum Refinery Engineering
Which of the following theories of origin of petroleum does not explain the presence of nitrogen & sulphur compounds in crude oil?

Carbide theory
Engler theory
Modern theory
All of these

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Petroleum Refinery Engineering
Straight run naphtha is converted into high octane number petrol (gasoline) by catalytic

Cracking
Polymerisation
Reforming
Isomerisation

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Petroleum Refinery Engineering
Hydrogen content in petroleum products varies from 12 to 15% (by weight). As a result the difference between gross and net heating value of petroleum fuels varies in the range of __________ kcal/kg.

2000-2500
600-750
1000-1500
250-350

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