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Process Equipment and Plant Design

Process Equipment and Plant Design
In a multiple effect evaporator system having 'n' effects, the amount of water evaporated per unit surface area in approximately equal to __________ times that in a single effect.

0.5 nth
nth
1.5 nth
(1/n)th

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Process Equipment and Plant Design
The necessary wall thickness for a metallic storage vessel is a function of the

All of these
Diameter of the vessel
Operating pressure and welding/joint efficiency
Ultimate tensile strength (or yield point) of the material and operating temperature

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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.

1250
7500
2500
15000

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Process Equipment and Plant Design
Tube wall thickness depends on the cor-rosiveness of the fluids and their operating pressure & temperature and is specified by Birmingham wire gauge (B.W.G)-a number which varies from 8 to 18 with the numbers 14 and 16 being more commonly used. Outside diameter of tubes varies from about 15 to 50 mm; however a tube of less than __________ mm outside diameter is generally not recommended for fouling fluids.

38
16
28
19

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Process Equipment and Plant Design
Which of the following is used to set the diameter of the distillation column?

Number of theorectical plates
Length of straight rectangular weir on cross-flow tray
Allowable vapour velocity
Static submergence

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Process Equipment and Plant Design
Accidents in chemical plants are mostly due to

Improper layout of the equipments
Failure of equipments
Faulty operating procedures
Inadequate equipment design

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