Process Equipment and Plant Design (Set 2) Flashcards

Concepts and heuristics necessary for design of equipment, processes, and process systems.

1
Q

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.

A

19

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2
Q

Angled baffles are preferred in the agitation tank to control the swirling action; if the viscosity of the liquid to be mixed is about 200 poise. However, the baffle may be completely eliminated for mixing liquids having viscoisty above ____ poise.

A

600

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3
Q

Ratio of tube length to shell diameter for a shell and tube heat exchanger is
a. 8 : 1 to 12 : 1 for both liquid-liquid and gas-gas heat exchangers.
b. 4 : 1 to 8 : 1 for liquid-liquid exchanger.
c. < 4 : 1 for gas-gas exchangers.

A

both(b) & (c).

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4
Q

The dust collection efficiency of a cyclone separator
a. decreases with increase in gas flow rate.
b. is inversely proportional to the mass of the dust particle.
c. and is directly proportional to the radius of the dust particle path.
d. none of these.

A

none of these.

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5
Q

In a shell and tube heat exchanger, the overall heat transfer co-efficient is proportional to the tube side (volumetric flow rate)0.8. This is valid, only when the ratio of the tube side film resistance to the total resistance is almost equal to

A

1

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6
Q

Which of the following types of reactors is the safest from operation point of view?

A

A vapor phase reactor.

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7
Q

In a bag filter, the pressure drop increases directly as the

A

density of the gas and inversely as viscosity of the gas.

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8
Q

The LMTD correction factor (FT) is applied in ____ heat exchangers.

A

all multipass

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9
Q

Movement of pipeline caused by thermal expansion is taken care by providing

A

all (a), (b) and (c).

expansion joint, changes in its direction, change in the shape of pipeline

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10
Q

For a cylindrical shell, (subject to the thickness of uppermost course being more than the minimum for diaofthe tank in question), the thickness of the courses of shell

A

decreases upwards.

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11
Q

In the design of a paddle agitator, the ratio paddle dia/tank dia is normally taken as

A

0.8

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12
Q

The design stress, which is more than the damaging stress, is the least unit stress that will render a member unfit for service before the end of its normal life. The design stress factor or factor of safety indicates the margin between design stress and the ____ stress.

A

damaging

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13
Q

Hole diameter of the seive trays in the distillation column ranges from ____ mm.

A

3 to 12.5

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14
Q

Factor of safety (i.e., overdesign factor) in heat transfer equipments is about ____ percent more than the actual/theoretical design factor.

A

15-20

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15
Q

For annular flow of a fluid, the ratio of the equivalent diameter for pressure drop calculation to the equivalent diameter for heat transfer calculation is

A

d1/(d1+d2)

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16
Q

In actual operation of distillation column, the vapour is not distributed uniformly among the bubble caps, primarily because of the

A

liquid gradient on the tray.

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17
Q

The minimum shell thickness for tank ≤ 15 metres diameter is limited to ____ mm, for reasons of elastic stability.

A

5

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18
Q

If ‘D’ is the inside diameter of the shell of a shell and tube heat exchanger, then the baffle spacing is usually in the range of

A

D/5 or minimum 2” to 5D.

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19
Q

Brass valves are usually made for pipe sizes ____ inches.

A

≤2

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20
Q

At the following point for a given packing and set of fluids, the pressure drop per metre of packed height, with variation in fluid rates and operating pressure

A

remains same

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21
Q

In a shell and tube heat exchanger, triangular pitch arrangement as compared to square pitch arrangement

A

results in higher shell side pressure drop.

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22
Q

Pick out the wrong statement about routing of fluids in a shell and tube heat exchanger.

A

Higher pressure fluid stream should be routed through the shell side.

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23
Q

The necessary wall thickness for a metallic storage vessel is a function of the
a. ultimate tensile strength (or yield point) of the material and operating temperature.
b. operating pressure and welding/joint efficiency.
c. diameter of the vessel.

A

all (a); (b) and (c).

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24
Q

In a multiple effect evaporator system having ‘n’ effects, the amount of water evaporated per unit surface area in approximately equal to ____ times that in a single effect.

A

(1/n)th

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25
Q

Pick out the wrong statement.

a. In a flanged and standard dished head, the crown radius is ≤ shell outside diameter.
b. In a flanged and shallow dished head, the crown radius is > shell outside diameter.
c. Flat head covers are most suitable for larger vessels operating at very high pressure.
d. Flanged only head is a type of flat head in which gradual change in the shape at the centre results in reduced local stresses.

A

Flat head covers are most suitable for larger vessels operating at very high pressure.

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26
Q

Pick out the wrong statement pertaining to the design of a horizontal tube evaporator.

a. It is unsuitable for concentrating those liquids, which form a scale or deposit salt.
b. It is suitable for process, in which the final product is a liquor instead of solid.
c. Its usual dimensions are: tube dia = 2-3 cms; evaporator body dia = 1-4 metres and evaporator height = 2.5-4 metres.
d. Liquor flows inside the tube, while the steam is outside submerging the tube.

A

Liquor flows inside the tube, while the steam is outside submerging the tube.

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27
Q

Weep holes provided in the plates of a distillation column

a. facilitate draining out liquid from a tray when the unit is not in operation.
b. are normally located near the overflow weir so that any delivery of liquid during operation follows approximately the same path as the overflow fluid.
c. must be large enough (usually 1/4” to 5/8” dia) to prevent plugging but should not deliver excessive amount of fluid during operation.

A

all (a), (b) and (c).

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28
Q

Steam is preferred to be used as a heating medium in heat exchangers, because of its

A

high latent heat.

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29
Q

____ shapedroof is the most commonly used roof for cylinderical storage tanks.

A

Conical

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30
Q

Pick out the wrong statement pertaining to ‘Horton sphere’ used for the storage of liquid ammonia.

a. Diameter of Horton sphere is normally 6 to 25 metres and it is supported by 6 to 12 nos. tubular or rolled section column.
b. Thickness of spherical shell is half that of the cylinderical vessel under same operating pressure condition. Besides, the ratio of surface area to volume is less for sphere than any other shape ; hence insulation required is less.
c. Horton sphere is used for the storage of gases and volatile liquid at a moderate pressure of 1 to 10 kg/cm2.
d. Horton sphere is used for the storage of liquid at sub-zero temperature at very high pressure upto 200 kg/cm2 .

A

Horton sphere is used for the storage of liquid at sub-zero temperature at very high pressure upto 200 kg/cm2 .

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31
Q

Value of Peclet number = ∞, is the representative of

A

plug flow.

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32
Q

Le/D for a Tee (used as elbow, entering branch) would be
a. less than that for Tee (used as elbow, entering run).
b. more than that for Tee (used as elbow, entering run).
c. around 90.

A

both (b) and (c).

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33
Q

In most of the shell and tube heat exchangers, the tube pitch is generally ____ the tube diameter.

A

1.25-1.50 times

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34
Q

In a distillation column, bubble caps are located on trays with a pitch of ____ times the outside diameter of the caps.

A

1.3 to 2

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35
Q

1.2 to 3.8 cms is the value of the

a. downcomer liquid seal in case of a balanced tray design.
b. static submergence in case of a bubble cap tray for column operating under pressure (≥ 1 atm.).
c. skirt clearance for bubble caps.

A

all (a), (b) and (c).

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36
Q

Accidents in chemical plants are mostly due to

A

faulty operating procedures.

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37
Q

For identical operating conditions, the pressure drop over ____ tray is the highest out of the following.
a. sieve
b. valve
c. counterflow
d. bubble cap

A

bubble cap

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38
Q

A perforated plate has holes of diameter dn arranged in a pitch ph. Each hole has a tube of I.D. dt passing through it. The ligament efficiency is given by

A

(ph - dt)/ph

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39
Q

____ is the determining factor for the number of bubble caps to be used per tray.

A

Permissible slot velocity

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40
Q

Pick out the wrong statement about distillation operation

a. Distillation under vacuum is a substitute for steam distillation.
b. In differential (simple) distillation, the vapour is removed as soon as it is formed without appreciable condensation.
c. In flash (equilibrium) distillation, a definite fraction of liquid is vaporised in such a way that the evolved vapour & residual liquids are in equilibrium with each other.
d. Flash distillation, differential distillation & steam distillation are all continuous distillation processes.

A

Flash distillation, differential distillation & steam distillation are all continuous distillation processes.

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41
Q

Low pressure steam (with saturation temperature between 105 to 120°C) is usually used in the vacuum evaporators, which normally employ a vacuum of about ____ mm Hg (referred to a 760 mm mercury barometer).

A

650

42
Q

Which of the following is the best tube material from thermal conductivity point of view alone?

A

Copper

43
Q

Normal screwed fittings are used for pipes upto a diameter of ____ inches.

A

3

44
Q

In a shell and tube heat exchanger, the clearance of the tube is generally

A

not less than one-fourth of the tube diameter or 3/16”.

45
Q

Diameter of the seive tray column is determined by the

A

upper limit of the vapour velocity.

46
Q

For a given fluid, as the pipe diameter increases, the pumping cost

A

decreases.

47
Q

Maximum acceptable total liquid gradient over a tray is about ____ mm.

A

12.5

48
Q

In case of a ‘thin’ pressure vessel, the ratio of its diameter to wall thickness is

A

> 10

49
Q

High pressure fluid in a shell and tube heat exchanger should preferably be routed through the

A

tubes to avoid the expansion of high pressure shell construction.

50
Q

Bubble cap tray is the most commonly used tray in large distillation column, because

A

of its flexibility and nearly constant efficiency under varying conditions of operation.

51
Q

In common bubble cap distillation column design practice, riser area is approximately equal to (where, Aa = Annular passage area, and Sa = Slot area)

A

Aa = Sa

52
Q

Heat transfer co-efficient, hG(Kcal/hr.m2 .°C) and mass velocity of air, G (kg/hr.m2 ) for air flow parallel to the surface in case of constant drying rate in batch drying is related as hG = 0.0176G0.8. But when the flow of air perpendicular to the surface is encountered, this equation changes to

A

hG = 1.004G^0.37

53
Q

In the agitators, the power required will be changed with the increase of diameter of agitator (D) as

A

D^5

54
Q

Apex angle of conical heads used in the bottom heads of chemical process equipments is usually

A

60°

55
Q

Pressure drop due to pipe fittings can be estimated by the equation, https://www.indiabix.com/_files/images/chemical-engineering/process-equipment-and-plant-design/561-40-1.png
, where, Le = equivalent length of straight pipeline which will incur the same frictional loss as the fitting and D = diameter of the fitting. The value of Le/D (dimensionless) for 45° elbow and 180° close return bends would be respectively around

A

45 and 75

56
Q

A pressure vessel is said to be made of ‘thick’ shell, if the ratio of its diameter to wall thickness is

A

10

57
Q

Rate of filtrate delivery is inversely proportional to the
a. filtering area & the pressure difference driving force.
b. viscosity of filtrate.
c. cake & filter medium resistance.

A

both (a) and (b)

58
Q

Tube side heat transfer co-efficient for turbulent flow of liquid through tubes is proportional to

A

G^0.8

59
Q

Circumferential (hoop) stress in a thin cylindrical vessel under internal pressure is ____ the longitudinal stress.

A

twice

60
Q

The dust collection efficiency of electrostatic precipitator increases with increase in the

A

electrode area.

61
Q

For storing hazardous chemicals in large storage tanks, the minimum safe distance between the two tanks should range between ____ times the tank diameter.

A

1 to 1.5

62
Q

Which of the following factors determine the amount of entrainment in a distillation column?
a. Plate spacing.
b. Depth of liquid above the bubble cap slots.
c. Vapour velocity in the volume between the plates.

A

All (a), (b) and (c).

63
Q

The absorption factor is defined as (where, S1 = slope of the equilibrium curve, S2 = slope of the operating line)

A

S1/S2

64
Q

In shell and tube heat exchangers, straight tie rods are used to

A

hold baffle in space.

65
Q

In a rotary drier, the average retention time of solid is(where Z = length of the drier, metres ρ = apparent solid density, kg/m3 L = flow rate of dry solids, kg/see. m2 drier cross-section H = hold up of solid.)

A

Z.H.p/L

66
Q

In case of design of a shell and tube heat exchanger,

a. minimum cleaning lane of 6.5 mm is provided, when tubes are on a square pitch.

b. minimum tube sheet thickness (in which tubes are fixed) is equal to the O.D. of the tube upto 15 mm tube diameter; and for > 15 mm tube diameter, tube sheet thickness is smaller than tube diameter.

c. O.D. of the tube is 6 to 40 mm while the tube lengths used are 0.5, 2.5, 3.0, 4.0, 5.0, 6 metres.

A

all (a), (b) & (c).

67
Q

In a cylinderical vessel subjected to internal pressure, the longitudinal stress σL and the circumferential stress, σn are related by

A

σh = 2 σL

68
Q

Nominal size of a pipe is an indication of its ____ diameter.

A

approximate

69
Q

Excessive liquid gradient on a tray may result in the

a. maldistribution of gas.
b. back trapping.
c. gas blowing beneath cap skit.

A

all (a), (b) and (c).

70
Q

The ratio of tube length to shell diameter in case of liquid shell and tube heat exchanger ranges from

A

4 to 8

71
Q

In a double pipe concentric heat exchanger, the equivalent diameter of annulus for heat transfer would be (where, D1 and D2 are I.D. of inner and outer pipes)

A

https://www.indiabix.com/_files/images/chemical-engineering/process-equipment-and-plant-design/566-92-1.png

72
Q

What is the slope of the operating line in the stripping section of a distillation column?

A

> 1

73
Q

____ shaped roof is most commonly used for cylindrical tanks.

A

Cone

74
Q

In a thin cylindrical shell, the hoop stress is ____ stress.

A

circumferential tensile

75
Q

Commercial packed scrubbers are normally designed for a pressure drop range of ____ mm water coloumn per metre of packed height.

A

17-34

76
Q

The retention time of material in a rotary dryer depends upon its

a. rpm
b. slope & length
c. flights arrangement

A

all (a), (b) and (c)

77
Q

In actual operation of a bubble cap distillation tower, the ____ at the bottom of the tower is more than that at the top of the tower.

a. molal flow rate of vapour
b. vapour molecular weight
c. pressure and temperature

A

all (a), (b) and (c)

78
Q

Rotary driers are most economically designed for the number of heat transfer units (HTU) from

A

1.5 to 2.5

79
Q

The difficulty of liquid distribution in packed towers is accentuated, when the ratio of tower diameter to packing diameter is

A

< 7

80
Q

A forced circulation long tube vertical evaporator as compared to the natural circulation evaporator

a. is economical in operation.
b. employs high velocity, high heat transfer rate and less heating surface requirement.
c. employs a centrifugal pump placed between external downtake from vapor drum and inlet to tube bundle.

A

both (b) & (c).

81
Q

An increase in the liquid resistance to interphase mass transfer and a resultant reduction in plate efficiency is caused by

a. an increase in liquid viscosity.
b. an increase in relatived volatility for rectification columns.
c. decrease in gas solubility for absorbers.

A

all (a), (b) and (c).

82
Q

In the design of a bag filter, the gas temperature is an important consideration, as it affects the
a. gas density
b. gas viscosity
c. fibre selection

A

all (a), (b) & (c)

83
Q

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

A

decreases very rapidly

84
Q

The normal range of velocity of steam in pipes is ____ m/sec.

A

80-100

85
Q

____ dished head is the strongest of all.

A

Hemispherical

86
Q

Pick out the correct statement.

a. It is preferred to use a vertical condenser for condensation of vapor from a distillation column without sub-cooling
b. Draining of residual liquid on tray during shut down of distillation column is facilitated by weep holes.
c. Random packing a packed tower offers the advantage of lower pressure drop and higher throughput of fluids as compared to regular/stacked packing.
d. Risers are generally not connected to the plate in a distillation coloumn by bolts, rivets or welding.

A

Risers are generally not connected to the plate in a distillation coloumn by bolts, rivets or welding.

87
Q

“A claming section” before the liquid flows into the downcomer is privided to

A

permit release of entrained vapour in the liquid.

88
Q

The units of Young’s modulus of elasticity and ____ are the same.

A

stress

89
Q

In the design of a shell and tube heat exchanger, the corrosion allowance

a. need not be provided for non-pressure parts like tie rods, spacers, baffles, supports etc.
b. for carbon steel and cast iron pressure parts is 1.5 mm (except for tubes) and for severe conditions it is 3 mm.
c. for internal cover and tube sheet is provided on both the sides.

A

all (a), (b) & (c).

90
Q

Vertical condenser is advantageous to the horizontal condenser from operation point of view, when

A

both the functions of condensation & sub cooling are carried out in a single unit.

91
Q

Hazards associated with the relief valve leakage for extremely hazardous material storage can be taken care of by providing

A

rupture diaphragm

92
Q

Minimum baffle spacing recommended in a shell and tube heat exchanger is equal to

A

5 cms

93
Q

____ liquor is best handled in a long tube vertical evaporator.

A

Foamy

94
Q

Theoretically calculated diameter of the stripping section of the continuous rectification column is ____ that of the enriching section.

A

more than

95
Q

Hold up of material in a operating rotary drier is in the range of

A

0.05 to 0.15

96
Q

A binary liquid azeotropic mixture has boiling point higher than either of the components, when it shows ____ deviation from Raoult’s Law.

A

negative

97
Q

The testing pressure of storage tanks and pressure vessels designed as per Indian standard codes should be about ____ times.the design pressure.

A

1.5 to 2

98
Q

Flanges are connected to pipes by
a. screwing
b. welding
c. brazing

A

all (a), (b) and (c)

99
Q

The ratio of down take area to cross-sectional area of the tube, for calendria type evaporator ranges from

A

0.5 to 1

100
Q

Shortest distance between two tubes is

A

called tube clearance.