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Petroleum Refinery Engineering

Petroleum Refinery Engineering
With increase in the molecular weight of aromatic present in kerosene, its smoking tendency

Decreases
Increases
Remains same
Is unpredictable

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Petroleum Refinery Engineering
Name the endothermic reaction out of the following:

Catalytic cracking
Catalytic polymerisation
Dehydrogeneration of naphthene to produce aromatic
Hydrocracking

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Petroleum Refinery Engineering
Iso-octane is used as a reference substance in the definition of octane number and it is assigned an octane number value of 100. Iso-octance is chemically known as

α-methyl naphthalene
2-2-4 tri methyl pentane
Tetra methyl ethylene
1, 3 butadiene

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Petroleum Refinery Engineering
Octane number of n-heptane is assumed to be

∞
0
100
70

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Petroleum Refinery Engineering
Though increased pressure has a retarding effect on cracking reaction, yet in actual process, a positive pressure of 10-15 kgf/cm² is maintained during cracking mainly to

Increase the yield of light distillates
Enhance the octane number of gasoline
Suppress coke formation
Reduce gum content in gasoline

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

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

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