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Process Equipment and Plant Design

Process Equipment and Plant Design
Holes of a sieve tray are arranged in triangular pitch of __________ times the hole diameter.

5 to 10
1.5 to 2
2.5 to 5
10 to 15

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Process Equipment and Plant Design
Cylinderical shell thickness of rotary drier is generally __________ mm.

44180
18-22
43864
43990

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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.

16
28
19
38

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Process Equipment and Plant Design
A high vapour velocity is required for high plate efficiency in a seive plate coloumn. The satisfactory value of operating vapor velocity for design purpose in seive plate column is about __________ percent of the flooding velocity.

60
45
80
95

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Process Equipment and Plant Design
The minimum baffle height should be

Twice the impeller diameter
Twice the tank diameter
Equal to the impeller diameter
3/4 of the tank height

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Process Equipment and Plant Design
Tube side heat transfer co-efficient for turbulent flow of liquid through tubes is proportional to

G0.5
G0.2
G0.8
G1.5

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