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Petroleum Refinery Engineering

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

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

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Petroleum Refinery Engineering
Pour point of a petrofuel is

None of these
Multiple of 5°F
5°C below the temperature at which oil ceases to flow
Multiple of 3°F

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

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

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Petroleum Refinery Engineering
Phenols are added in gasoline to

Act as an antioxidant
Increase its pour point
Reduce its viscosity
Improve the octane number

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Petroleum Refinery Engineering
Higher pressure in the reforming reactor

Increases the rate of reaction
Produces high octane number gasoline
Increases coke formation
None of these

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

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

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