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Process Equipment and Plant Design

Process Equipment and Plant Design
Steam side heat transfer co-efficient for design consideration under ordinary condition can be assumed to be about __________ kcal/hr.m².°C.

2500
15000
7500
1250

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Process Equipment and Plant Design
In case of a 'thin' pressure vessel, the ratio of its diameter to wall thickness is

30
> 20
< 10
> 10

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Process Equipment and Plant Design
In the allocated cap area, bubble caps are generally arranged on equilateral triangular pitch. Number of caps fixed on a plate is with a

Either A or B
Neither A nor B
Cap pitch of 1.3-2 times the cap diameter
Clearance of 25-75 mm

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Process Equipment and Plant Design
Tube height in a calendria type evaporator is normally less than __________ metres.

2
1
5.5
3.5

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Process Equipment and Plant Design
In a distillation column, minimum clearance to be maintained betweeen the overflow weir and the last row of the bubble caps is __________ cms.

15
20
7.5
2.5

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Process Equipment and Plant Design
__________ tower is the most suitable gas-liquid contacting device involving highly corrosive fluids.

None of these
Sieve plate
Bubble cap plate
Packed

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