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Petroleum Refinery Engineering

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

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

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Petroleum Refinery Engineering
Crude topping column operates at __________ pressure.

10 atm
Atmospheric
3 atm
Vacuum

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Petroleum Refinery Engineering
Ethyl mercaptan is added to the Doctor negative LPG for facilitating the detection of its leakage (by bad odour) to the extent of about __________ ppm.

10000
1
50
5000

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Petroleum Refinery Engineering
Which of the following is a non-regenerative fixed bed catalytic reforming process?

Platforming
Thermofer catalytic reforming
Hydroforming
Hyperforming

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Petroleum Refinery Engineering
Dearomatisation of kerosene (by liquid sulphur dioxide extraction) is done to

Improve its oxidation stability
Increase its smoke point
None of these
Decrease the breathing loss

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Petroleum Refinery Engineering
Smoke point of a test sample of kerosene is found to be 15 mm. On removal of __________ from it, the smoke point rises to 25 mm.

None of these
Olefins
Aromatics
N-paraffins

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