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Petroleum Refinery Engineering

Petroleum Refinery Engineering
The yield of straight run LPG from crude oil is about __________ weight percent.

1-1.5
20-25
0.1-0.2
44119

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

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

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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
Performance number of a liquid fuel is related to its

Knocking tendency
Spontaneous ignition temperature
Wax content
Sulphur content

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Petroleum Refinery Engineering
Carbon/hydrogen ratio (by weight) is maximum (out of following) for

Light gas oil
Kerosene
Heavy fuel oil
Gasoline

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Petroleum Refinery Engineering
Ethyl mercaptan is a/an __________ compound.

None of these
Oxygen
Sulphur
Nitrogen

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