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Petroleum Refinery Engineering

Petroleum Refinery Engineering
Pressure & temperature maintained in catalytic cracking is about

30atm & 200°C
10atm & 500°C
50atm. & 750°C
2atm & 500°C

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Petroleum Refinery Engineering
Catalyst used in alkylation process is

Nickel
Sulphuric acid
Alumina
Silica gel

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Petroleum Refinery Engineering
Extractor temperature is maintained at -20°C in Edeleanu process to reduce the __________ of kerosene.

Paraffins
Aromatics
Naphthenes
Smoke point

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Petroleum Refinery Engineering
The reservoir rock containing petroleum has

High permeability
Both B and C
Low porosity
High porosity

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Petroleum Refinery Engineering
The main reaction in reforming is the

Saturation of olefins
Dehydrogenation of naphthenes
Hydrocracking of paraffins
Hydrogenation of naphthenes

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Petroleum Refinery Engineering
Hydrogen content in petroleum products varies from 12 to 15% (by weight). As a result the difference between gross and net heating value of petroleum fuels varies in the range of __________ kcal/kg.

1000-1500
2000-2500
600-750
250-350

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