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Process Equipment and Plant Design

Process Equipment and Plant Design
Baffles may be eliminated for

Large diameter tanks
None of these
High viscosity liquids (> 600 poise)
Low viscosity liquids (< 200 poise)

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Process Equipment and Plant Design
Rivets are generally specified by the

None of these
Shank diameter
Head diameter
Overall length

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Process Equipment and Plant Design
Cooling water fouling factors vary in the range of 0.001 to 0.003

(BTU/hr.ft² . °F)⁻¹
(kcal/hr.m² .°C)⁻¹
(W/m².°K)⁻¹
(kcal/hr. m. °C)⁻¹

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Process Equipment and Plant Design
The ratio of the largest load in a test to the original cross-sectional area of the test specimen is called the __________ stress.

Breaking
Yield point
None of these
Ultimate

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Process Equipment and Plant Design
For storing hazardous chemicals in large storage tanks, the minimum safe distance between the two tanks should range between __________ times the tank diameter.

4 to 5
6 to 8
1 to 1.5
2.5 to 3.5

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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.

80
60
45
95

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