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Process Equipment and Plant Design

Process Equipment and Plant Design
For high pressure process equipments/vessels, the connected nozzle should be

Brazed
Screwed
Welded
Flanged

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Process Equipment and Plant Design
Maximum acceptable total liquid gradient over a tray is about __________ mm.

30.5
5.5
45.5
12.5

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Process Equipment and Plant Design
Ratio of tube length to shell diameter for a shell and tube heat exchanger is

4 : 1 to 8 : 1 for liquid-liquid exchanger
Both B & C
8 : 1 to 12 : 1 for both liquid-liquid and gas-gas heat exchangers
< 4 : 1 for gas-gas exchangers

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Process Equipment and Plant Design
Rate of filtrate delivery is inversely proportional to the

Both A & B
Filtering area & the pressure difference driving force
Viscosity of filtrate
Cake & filter medium resistance

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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
1 to 1.5
2.5 to 3.5
6 to 8

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Process Equipment and Plant Design
The raio, (properller agitator dia/tank dia) is normally taken as

0.60-0.90
0.5-0.65
0.15-030
0.75-0.85

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