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Petroleum Refinery Engineering

Petroleum Refinery Engineering
In catalytic cracking process, olefins crack __________ times faster than in thermal cracking process.

1000-10000
200-300
10
100

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Petroleum Refinery Engineering
Reforming

Uses naphtha as feedstock
All of these
Does not much affect the molecular weight of the feed
Improves the quality & yield of gasoline

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Petroleum Refinery Engineering
The main purpose of recycling the byproduct hydrogen gas in the reformer reactor is to

Maintain the reaction temperature
Hydrogenate the feed stock
Sustain the reactor pressure
Obviate catalyst poisoning

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Petroleum Refinery Engineering
The proper arrangement of the petroleum fractions in order of their boiling points is

Lubricating oil > diesel > petrol > LPG
Petrol > diesel > LPG > lubricating oil
Petrol > lubricating oil > diesel > LPG
Lubricating oil > petrol > diesel > LPG

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Petroleum Refinery Engineering
Solvent used in duo-sol extraction for lube oil upgradation is a mixture of

Methyl ethyl ketone & glycol
Propane & liquid sulphur dioxide
Phenol & furfural
Propane & phenol-cresol mixture

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Petroleum Refinery Engineering
In hydrofining catalytic desulphurisation process for sweetening of petroleum products, use of hydrogen

Minimises coke formation
Both A & B
Neither A nor B
Enhances the desulphurisation process

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