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Petroleum Refinery Engineering

Petroleum Refinery Engineering
Absolute vapor pressure of petrofuels is found by Reid bomb which is heated in water bath to 100°F. In Reid apparatus, the ratio of the volume of air chamber to that of the liquid fuel chamber is

3
2
1
4

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Petroleum Refinery Engineering
H/C ratio (by weight) for the same number of carbon atoms is the highest in case of

Aromatics
Paraffins
Naphthenes
Olefins

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

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

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Petroleum Refinery Engineering
In case of liquid petrofuels, momentary combustion is observed at its

Flash point
Flame temperature
Fire point
Preheating temperature corresponding to viscosity of 25 centistokes

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Petroleum Refinery Engineering
Tetraethyl lead is added to the petrol to increase its octane number, because its octane number is

Round about 100
Less than 25
More than 100
Between 50 and 100

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Petroleum Refinery Engineering
Illuminating characteristics of kerosene is expressed by its

Luminosity number
Aniline point
Smoke point
Aromatic content

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