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Petroleum Refinery Engineering

Petroleum Refinery Engineering
Octane number of gasoline produced by two stage fluidised catalytic cracking process is

97
87
80
92

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Petroleum Refinery Engineering
95% (by volume) of LPG at 760 mm Hg pressure will evaporate at __________ °C.

30
-40
2
55

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Petroleum Refinery Engineering
Methyl tertiary butyl ether (MTBE), a high octane (octane no. = 115) gasoline blending component is produced by the simple additive reaction of isobutylene with

Ethane
Methane
Ethyl alcohol
Methyl alcohol

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Petroleum Refinery Engineering
Straight run naphtha is converted into high octane number petrol (gasoline) by catalytic

Polymerisation
Isomerisation
Reforming
Cracking

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Petroleum Refinery Engineering
Petroleum liquid fuels having flash point greater than 66°C is considered as safe during storage and handling. Which of the following has flash point > 66°C ?

Naphtha
Heavy fuel oil
Kerosene
Petrol

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Petroleum Refinery Engineering
Preheating temperature of medium viscosity furnace oil for better atomisation through burner is about __________ °C.

90
50
140
70

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