Process Equipment and Plant Design Flashcards

1
Q

Which of the following material is seldom used for pressure vessel construction?

A

Rimmed Steel

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2
Q

The ratio of shear stress to shear strain is called

A

shear modulus

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3
Q

25 percent cut segmental baffle means that the baffle

A

height is 75% of the I.D. of the shell.

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4
Q

Liquid/petroleum fuel storage tanks are built underground (as in case of petrol pumps), when the storage capacity is less than __________ kilolitres.

A

45

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5
Q

Le/D for fully open globe value may be around

A

300

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6
Q

With increase in the number of shell passes, the value of FT

A

increases

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7
Q

Holes of a sieve tray are arranged in triangular pitch of __________ times the hole diameter.

A

2.5 to 5

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8
Q

In case of a shell and tube heat exchanger, the minimum shell thickness for carbon steel (inclusive of corrosion allowance) depends on shell diameter and is in the range of __________ mm.

A

5-11

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9
Q

The stress developed in a material without any permanent set is called the

A

elastic limit

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10
Q

In a shell and tube heat exchanger, the ‘tube pitch’ is defined as the

A

shortest centre to centre distance between adjacent tubes.

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11
Q

Which of the following is not a valid assumption in continuous binary distillation for calculating the number of equilibrium stages by Mc-Cabe-Thiele’s method?

A

Reflux is not a saturated liquid

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12
Q

Overall distillation column efficiency for most of the refinery columns can be given by (for μ = 0.07 - 1.4 cp and relative volatility < 4) (where η = overall column efficiency, % μ = molal average viscosity of feed at average column temperature and pressure, cp Δp = pressure drop per tray, psi)

A

η = 17 - 61.1 log μ

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13
Q

In case of bubble cap distillation column of diameter greater than 1.2 metres, the cap diameter is roughly about __________ cm.

A

10

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14
Q

Tube side pressure drop in a 1-2 heat exchanger (for turbulent flow of fluids through the tubes) is about __________ times, that in a 1-1 heat exchanger having the same size & number of tubes and operated at the same liquid flow rate

A

8

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15
Q

To keep the power input constant for a stirred vessel operating under fully developed turbulent flow conditions (constant power number), if the impeller diameter is increased by 20%, the impeller speed should be decreased by a factor of

A

(1.2)^(5/3)

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16
Q

In a heat exchanger, shell side fluid velocity can be changed by changing the tube

A

layout and pitch

17
Q

Where does the maximum tensile strength occur in a thick cylindrical vessel subjected to internal pressure?

A

At the inner surface.

18
Q

It is not desirable to design a heat exchanger for LMTD correction factor, FT, of less than

19
Q

Triangular pitch tube layout as compared to square pitch in a shell and tube heat exchanger

A

permits the use of more tubes in a given shell diameter.

20
Q

Bracket supports are the most suitable for supporting __________ vessels.

A

thin-walled vertical

21
Q

Two iron pipes of the same nominal diameter but different schedule numbers will have the same

A

inside diameter (should be OD)

22
Q

Steam side heat transfer co-efficient for design consideration under ordinary condition can be assumed to be about __________ kcal/hr.m2.°C.

23
Q

Lessing ring is formed by the addition of a partition across the centre of a raschig ring, which results in an area increase of about __________ percent.

24
Q

In chemical process equipment, the conical bottom heads used, usually has an apex angle of

25
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.
75
26
Shell side heat transfer co-efficient in case of square pitch as compared to the triangular pitch under similar condition of fluid flow and tube size is
less
27
Correct use of 'factor of safety' is very important in equipment design. It is defined as the ratio of the
ultimate stress to working stress.
28
The operating velocity in the absorption tower is usually 40-50% of the flooding velocity. Packed absorption towers are normally designed for a pressure drop of about __________ mm of water column per meter height of packing.
20-40
29
__________ tray arrangement is recommended for distillation column having diameter up to 4 ft.
Cross-flow
30
What is the value of 'q' for saturated liquid feed to a distillation column?
1
31
The main purpose of providing stepping on the trays is to
facilitate handling of large flow rate of liquid.
32
The operating pressure drop range in a bag filter is about __________ mm water gauge.
50-150
33
The ends of a cylinderical vessel can be closed by a head, which can be one of the four shapes. For the same thickness, choose the one which can withstand the highest pressure.
Ellipsoidal
34
For laminar flow (NRe < 2100) in steel pipe, the optimum inside pipe diameter is given by
Di,opt = 3 Q^(0.36) ρ^(0.18)
35
Wall thickness of schedule 40 pipe as compared to that of schedule 80 pipe is
less
36
Speed of the drum of the rotary vacuum filter normally ranges from __________ rpm.
0.1 to 2
37
A stuffing box is used for
prevention of fluid leakage around moving parts.
38
Pressure drop (Δp) and the superficial gas mass velocity (G) in case of packed absorption tower operating in the preloading range are related as
Δp = G^2