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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
1250
7500

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Process Equipment and Plant Design
The absorption factor is defined as (where, S₁ = slope of the equilibrium curve, S₂ = slope of the operating line)

S₁/S₂
1/S₁.S₂
S₂/S₁
S₁.S₂

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Process Equipment and Plant Design
Removable connection of tubes to tube sheet is called

Socket
Nipple
Saddle
Ferrule

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Process Equipment and Plant Design
The distance between the top of the slots and the liquid surface when the static liquid is just ready to flow over the overflow weir is called

Static submergence
None of these
Skirt clearance
Downcomer liquid seal

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Process Equipment and Plant Design
The ratio of volumes of the mixed reactor to the plug flow reactor (for identical feed composition, flow rate, conversion, and for all positive reaction orders) is always

>1
1
Equal to the order of reaction
< 1

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Process Equipment and Plant Design
In distillation columns, bubble caps are held in place over trays by

Bolts
Rivets
A hold down bar
Both B and C

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