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Process Equipment and Plant Design

Process Equipment and Plant Design
Welded joint efficiency in the design of chemical process equipment is taken as

0.85
0.55
0.95
0.75

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Process Equipment and Plant Design
for couplings and unions would be

200
60
350
Negligible

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Process Equipment and Plant Design
Compensation against openings in process vessels for giving inlet and outlet connections, for providing sight glasses and manholes etc. is provided for strength and rigidity. The most efficient type of compensation is of __________ type.

Nozzle or rim
Flared out
Ring plate
Fluid in

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Process Equipment and Plant Design
Steam economy is defined as the amount of evaporation per unit amount of steam used, while the capacity is the total evaporation obtained per hour. Use of multiple effect in evaporation

Increases economy
Does not affect the capacity
Increases capacity
Both B & C

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Process Equipment and Plant Design
Multiple blade paddle agitator is used for mixing high viscosity liquids/paste in which the paddle diameter is commonly 0.8 times the tank diameter. However, the width of the blade is in the range of __________ times the paddle diameter.

0.3 to 0.5
0.65 to 0.80
0.5 to 0.6
0.1 to 0.25

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Process Equipment and Plant Design
Shortest distance between two tubes is

Called tube clearance
None of these
More in case of triangular pitch as compared to square pitch of tube layout
Called tube pitch

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