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Petroleum Refinery Engineering

Petroleum Refinery Engineering
Octane number (unleaded) of gasoline produced by isomerisation of butane may be about

55
45
70
90

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Petroleum Refinery Engineering
Catalytic cracking compared to thermal cracking of residue of vacuum distillation of crude oil

Higher sulphur content in the product
Lower octane number of petrol
Gives higher yield of petrol
Higher gum forming material in petrol

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Petroleum Refinery Engineering
Solvent used for dewaxing of petroleum products are

Both B & C
Furfural
Propane
Methyl ethyl ketone (MEK)

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Petroleum Refinery Engineering
Operating condition in the electrical dehydrators for crude oil is about

6.5 kgf/Cm² & 95°C
1 atm. & 110 °C
20 kgf/cm² & 110°C
50 atm. and 150°C

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Petroleum Refinery Engineering
Higher boiling fractions like atmospheric residue is distilled under vacuum at low temperature because at high temperature, there is a tendency of the predominance of

Discoloration
Thermal cracking
Coking
Gum formation

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Petroleum Refinery Engineering
Viscosity index of a lubricating oil

Should be low
None of these
Is the measure of variation of viscosity with temperature
Is the measure of its flash point

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