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Petroleum Refinery Engineering

Petroleum Refinery Engineering
Molecular weight of crude oil is in the range of

100-120
600-850
450-550
230-250

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Petroleum Refinery Engineering
Natural gasoline is produced

From oil wells
None of these
In oil refineries
By natural gas stripping

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Petroleum Refinery Engineering
Paraffins are desirable in lubricating oil, as it has got high

Pour point
Viscosity index
Smoke point
Viscosity

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

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

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Petroleum Refinery Engineering
1 centistoke is equal to __________ Redwood I seconds.

4.08
0.408
40.8
1

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Petroleum Refinery Engineering
Sulphur content in lighter and heavier petroleum products is generally determined respectively by

Bomb method and quartz tube method
Lamp method and bomb method
Quartz tube method and lamp method
Bomb method and lamp method

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