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Petroleum Refinery Engineering

Petroleum Refinery Engineering
Feedstock for polymerisation is

None of these
Cracked gases rich in C₂ & C₄ olefins
Naphtha
Low boiling aromatics

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Petroleum Refinery Engineering
Higher pressure in the reforming reactor

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

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Petroleum Refinery Engineering
Which of the following is a non-regenerative fixed bed catalytic reforming process?

Hyperforming
Thermofer catalytic reforming
Platforming
Hydroforming

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

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

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Petroleum Refinery Engineering
The main aim of cracking is to produce

Gasoline
Lube oil
Coke
Petrolatum

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Petroleum Refinery Engineering
Pour point of a petrofuel is

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

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