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Petroleum Refinery Engineering

Petroleum Refinery Engineering
Maximum use of petroleum coke is in

Adsorption refining operation
Fuel gas manufacture
Carbon electrode manufacture
Iron ore reduction

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Petroleum Refinery Engineering
Dearomatisation of kerosene (by liquid sulphur dioxide extraction) is done to

Increase its smoke point
Decrease the breathing loss
Improve its oxidation stability
None of these

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Petroleum Refinery Engineering
Reid vapour pressure of gasoline is the measure of its

Cloud point
Pour point
Carbon residue
Vapour locking tendency

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Petroleum Refinery Engineering
Visbreaking

Produces fuel oil of lower viscosity
Is carried out at atmospheric pressure
Uses natural gas as feed
Produces gasoline only

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Petroleum Refinery Engineering
Higher viscosity of lubricating oil usually signifies

Higher flash point and fire point
Higher acid number
Lower Reid vapour pressure
Lower flash point and fire point

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Petroleum Refinery Engineering
Operating temperature and pressure in catalytic reforming is about

50 - 75 kgf/cm² & 600 - 800°C
1-5 Kgf/cm² & 200°C
15-45 Kgf/cm² & 450-550°C
5-10 kgf/cm² & 150 - 250°C

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