Smaller sized packings are generally dumped to the packed columns, and the large ones of size greater than __________ mm are stacked individually, which provides better control over bed porosity and offers lower gas pressure drop.

Process Equipment and Plant Design
Smaller sized packings are generally dumped to the packed columns, and the large ones of size greater than __________ mm are stacked individually, which provides better control over bed porosity and offers lower gas pressure drop.

150

50

75

25

150

50

75

25

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

0.95

0.85

0.75

0.55

0.95

0.85

0.75

0.55

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Process Equipment and Plant Design
Height of the flights in the rotary drier is in the range of

0.02 to 0.05 d

0.5 to 0.6 d

0.08 to 0.12 d

0.2 to 0.5 d

0.02 to 0.05 d

0.5 to 0.6 d

0.08 to 0.12 d

0.2 to 0.5 d

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

Viscosity of filtrate

Both A & B

Filtering area & the pressure difference driving force

Cake & filter medium resistance

Viscosity of filtrate

Both A & B

Filtering area & the pressure difference driving force

Cake & filter medium resistance

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Process Equipment and Plant Design
The minimum tray spacing in distillation column of diameter less than 3 ft is normally __________ inches.

6

18

34

24

6

18

34

24

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Process Equipment and Plant Design
With increase in temperature drop (in a shell and tube heat exchanger), the LMTD correction factor, FT

Remains constant

Increases linearly

Increases very rapidly

Decreases very rapidly

Remains constant

Increases linearly

Increases very rapidly

Decreases very rapidly

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Process Equipment and Plant Design

Process Equipment and Plant Design Smaller sized packings are generally dumped to the packed columns, and the large ones of size greater than __________ mm are stacked individually, which provides better control over bed porosity and offers lower gas pressure drop.

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

Process Equipment and Plant Design Height of the flights in the rotary drier is in the range of

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

Process Equipment and Plant Design The minimum tray spacing in distillation column of diameter less than 3 ft is normally __________ inches.

Process Equipment and Plant Design With increase in temperature drop (in a shell and tube heat exchanger), the LMTD correction factor, FT

Process Equipment and Plant Design
Smaller sized packings are generally dumped to the packed columns, and the large ones of size greater than __________ mm are stacked individually, which provides better control over bed porosity and offers lower gas pressure drop.

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

Process Equipment and Plant Design
Height of the flights in the rotary drier is in the range of

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

Process Equipment and Plant Design
The minimum tray spacing in distillation column of diameter less than 3 ft is normally __________ inches.

Process Equipment and Plant Design
With increase in temperature drop (in a shell and tube heat exchanger), the LMTD correction factor, FT