Indiabix - Equipment and Plant Design Flashcards

1
Q

Fresh water carrying pipelines in chemical industries are
coloured with __________ color.

A. sea green
B. brown
C. yellow
D. red

A

A. sea green

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2
Q

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

A. Rimmed still
B. Mild steel
C. Killed steel
D. Semi-killed steel

A

A. Rimmed Still

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3
Q

The ratio of shear stress to shear strain is called

A. bulk modulus
B. shear modulus
C. modulus of rigidity
D. modulus of elasticity

A

B. shear modulus

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4
Q

25 per cent cut segmental baffle means that the baffle

A. height is 75% of the I.D. of the shell.
B. height is 25% of the I.D. of the shell.
C. spacing is 75% of its height.
D. width is 25% of its height.

A

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

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5
Q

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

A. 20
B. 30
C. 45
D. 85

A

C. 45

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6
Q

Le/D for fully open globe value may be around

A. 10
B. 25
C. 75
D. 300

A

D. 300

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7
Q

Leg support is

A. the most suitable for thick vertical vessel.
B. same as bracket support.
C. provided usually for vessels of much smaller
height than skirt supported vessels.
D. all (a), (b) and (c).

A

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

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8
Q

Pick out the wrong statement pertaining to the use of
valve tray, seive tray and bubble cap trays in continuous
distillation column.

A. Bubble cap trays though most expensive are the best in situations, where low vapour rates is to be
handled and a positive liquid seal is essential at all flow rates.
B. Murphree efficiency of all the three trays are nearly equal, however the peak efficiency is generally higher for seive and valve trays than the
bubble cap.
C. Maintenance cost for valve and seive trays are comparatively more than bubble cap tray due to their relatively complicated construction features.
D. Valve trays have the highest turn down ratio (i.e. the ratio of the highest to the lowest vapour flow rates) and thus provides the maximum flexible
operating range.

A

C. Maintenance cost for valve and seive trays are comparatively more than bubble cap tray due to their relatively complicated construction features.

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9
Q

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

A. increases
B. decreases
C. remains same
D. remains same, only if the number of tube passes
does not change.

A

A. increases

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10
Q

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

A. 1.5 to 2
B. 2.5 to 5
C. 5 to 10
D. 10 to 15

A

B. 2.5 to 5

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11
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. 3-5
B. 5-11
C. 8-15
D. 12-18

A

B. 5-11

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12
Q

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

A. ultimate stress
B. yield stress
C. elastic limit
D. breaking stress

A

C. elastic limit

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13
Q

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

A. O.D. of the tube for square pitch.
B. shortest distance between two adjacent tube holes.
C. shortest centre to centre distance between adjacent tubes.
D. none of these.

A

C. shortest centre to centre distance between
adjacent tubes.

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14
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. Sensible heat changes for vapour & liquid are negligibly small.
B. Reflux is not a saturated liquid.
C. Molar latent heat of the two components are equal.
D. Heat of mixing of normal liquid is assumed to be zero.

A

B. Reflux is not a saturated liquid.

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15
Q

The value of fouling factor depends upon the

A. characteristic of process fluid.
B. velocity of process fluid containing suspended solids.
C. suspended solids in the fluid.
D. all (a), (b) and (c).

A

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

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16
Q

In case of bubble cap distillation column of diameter greater than 1.2 metres, the cap diameter is roughly about
__________ cms.
A. 10
B. 20
C. 30
D. 35

A

A. 10

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17
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. 2
B. 1/2
C. 4
D. 8

A

D. 8

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18
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)3/2
B. (1.2)3/5
C. (1.2)2/3
D. (1.2)5/3

A

D. (1.2)5/3

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19
Q

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

A. layout
B. pitch
C. both (a) & (b)
D. neither (a) nor (b)

A

C. both (a) & (b)

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20
Q

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

A. At the inner surface.
B. At the mid thickness of the cylindrical wall.
C. At the outer surface.
D. None of these.

A

A. At the inner surface.

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21
Q

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

A. 0.99
B. 0.95
C. 0.80
D. 0.55

A

C. 0.80

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22
Q

A rivetted joint does not fail by __________ of rivets.

A. tearing
B. shearing
C. tearing of the plate across a row
D. none of these

A

D. none of these

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23
Q

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

A. permits the use of less tubes in a given shell
diameter.
B. facilitates comparatively easier external cleaning
because of large clearance.
C. permits the use of more tubes in a given shell
diameter.
D. both (b) and (c).

A

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

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24
Q

Bracket supports are the most suitable for supporting
__________ vessels.

A. thick walled vertical
B. horizontal
C. thin shperical (e.g. Horton sphere)
D. none of these

A

A. thick walled vertical

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25
Q

In a multipass shell and tube heat exchanger, the shell
side cross flow area does not depend upon

A. baffle spacing
B. clearance
C. pitch
D. none of these

A

D. none of these

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26
Q

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

A. inside diameter
B. outside diameter
C. wall thickness
D. none of these

A

B. inside diameter

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27
Q

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

A. 1250
B. 2500
C. 7500
D. 15000

A

C. 7500

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28
Q

Pick out the wrong statement

A. For all the cylindrical process vessels operating
above atmospheric pressure, formed heads are
used for closing the vessel.
B. Fouling factor of river water is less than that of sea
water.
C. Risers provided in bubble cap trays in the
distillation column facilitate the flow of both liquid
and vapor.
D. both (b) and (c).

A

D. both (b) and (c).

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29
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.

A. 5
B. 20
C. 35
D. 55

A

B. 20

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30
Q

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

A. 20°
B. 40°
C. 60°
D. 80°

A

C. 60°

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31
Q

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.

A. 25
B. 50
C. 75
D. 150

A

C. 75

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32
Q

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

A. more
B. same
C. less
D. twice

A

C. less

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33
Q

Correct use of ‘factor of safety’ is very important in
equipment design. It is defined as the ratio of the
A. ultimate stress to breaking stress.
B. ultimate stress to working stress.
C. working stress to ultimate stress.
D. none of these.

A

B. ultimate stress to working stress.

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34
Q

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 metre height of
packing.

A. 1-5
B. 20-40
C. 100-150
D. 1000-1500

A

B. 20-40

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35
Q

__________ tray arrangement is recommended for
distillation column having diameter upto 4 ft.

A. Radial flow
B. Cross flow
C. Split flow
D. Cascade

A

B. Cross flow

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36
Q

What is the value of ‘q’ for saturated liquid feed to a
distillation column ?

A. 0
B. <1
C. 1
D. >1

A

C. 1

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37
Q

In perforated plate towers, the
A. hole sizes may be around 1/8” or 3/16”.

B. total hole area may be around 6 to 15% of tower
cross-sectional area.
C. pressure drop is less compared is similar bubble
cap towers.
D. all (a), (b) and (c).

A

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

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38
Q

The main purpose of providing stepping on the trays is to

A. increase the residence time.
B. decrease the pressure drop.
C. facilitate handling of large flow rate of liquid.
D. improve the flow condition.

A

C. facilitate handling of large flow rate of liquid.

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39
Q

The operating pressure drop range in a bag filter is about
__________ mm water gauge.

A. 50-150
B. 5-10
C. 500-1500
D. 1500-2500

A

A. 50-150

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40
Q

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.

A. Flat plate
B. Hemispherical
C. Torispherical
D. Ellipsoidal

A

D. Ellipsoidal

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41
Q

For laminar flow (NRe < 2100) in steel pipe, the optimum
inside pipe diameter is given by

A. Di, opt = 3 Q0.36 μ 0.18
B. Di, opt = 3.9 Q0.45 . ρ0.23
C. Di, opt = 7.6 Q0.36 . ρ0.9
D. Di, opt = 3 Q0.36 . ρ1.86 μ0.08

A

A. Di, opt = 3 Q0.36 μ 0.18

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42
Q

Pick out the correct statement.
A. When highly corrosive fluids are to be handled,
the plate towers prove to be cheaper and easier
to construct than packed tower.
B. Packed towers are generally preferred over
plate towers, if the liquids have a foaming
tendency.
C. The pressure drop through the packed towers is
generally more than the pressure drop through
plate towers designed for same duty.
D. none of these.

A

B. Packed towers are generally preferred over
plate towers, if the liquids have a foaming
tendency.

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43
Q

Wall thickness of schedule 40 pipe as compared to that of
schedule 80 pipe is
A. more
B. less
C. same
D. cither (a) or (b); depends upon the I.D. of the pipe

A

B. less

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44
Q

Pick out the wrong statement pertaining to the design of a
basket type evaporator.
A. It is used for high viscosity liquor having large
rate of scaling.
B. The tube bundle is suspended on bracket.
C. There is no central downtake.
D. Downtake is formed by the annular space
between the bundle and the shell.

A

A. It is used for high viscosity liquor having large
rate of scaling.

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45
Q

Pick out the wrong statement pertaining to the design of
the bubble cap tray of a distillation column to give stable
operation and even vapour distribution.

A. The pressure drop due to the caps & slots and the
static submergence should be as high as
practicable for reasonable operation.
B. Tendency towards stable operation is increased
by increasing the skirt clearance of the caps,
lowering the rate of liquid flow per unit plate width
or increasing the spacing between the caps.
C. The dimensionless ratio of liquid gradient to
pressure drop head caused by the bubble cap
assembly should be less than 0.4.
D. none of these.

A

D. none of these.

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46
Q

Speed of the drum of the rotary vacuum filter normally
ranges from __________ rpm.

A. 0.1 to 2
B. 5 to 7
C. 3 to 8
D. 8 to 15

A

A. 0.1 to 2

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47
Q

A stuffing box is used for

A. absorbing the contraction/expansion of pipeline
due to temperature changes.
B. prevention of fluid leakage around moving
parts.
C. facilitating smooth opening and closing of a valve.
D. reducing the resistance of fluid flow.

A

B. prevention of fluid leakage around moving
parts.

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48
Q

Pressure drop (Δp) and the superficial gas mass velocity
(G) in case of packed absorption tower operating in the
preloading range are related as

A. Δp = G
B. Δp = G0.5
C. Δp = G2
D. Δp = 1/G0.6

A

C. Δp = G2

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49
Q

In an agitated vertical cylinderical reaction vessel, the

A. ratio of liquid depth to tank diameter (i.e. the filling
ratio) recommended for most purposes is 1.
B. filling ratio for dispersing gas in a liquid is 2 for
sufficiently long contact period.
C. flat bottom and conical bottom vessels have low
agitation efficiency for agitation of heavy solids in
liquids.
D. dished bottom vessel has very high power
consumption.

A

D. dished bottom vessel has very high power
consumption.

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50
Q

Needle valves are generally not used for

A. very large diameter pipes.
B. high pressure throttling service.
C. very accurate flow control.
D. smaller sizes of pipe.

A

A. very large diameter pipes.

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51
Q

Height equivalent to a theoretical plate (HETP) is the
height of packing that will give the same separation as one
theoretical plate in gas-liquid mass transfer operations
like distillation, absorption/stripping and humidification/dehumidification. HETP which is
experimentally determined, depends upon the

A. flow rates of each fluid.
B. type and size of packing.
C. concentration of each fluid.
D. all a, b & c.

A

D. all a, b & c.

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52
Q

Pick out the wrong statement.

A. Safety valves are provided in heat exchangers
for removal of non-conden-sables.
B. Liquid metals and dowtherm are used for very
high temperature heating.
C. In a shell and tube heat exchanger, high pressure
fluid is generally routed through the tube.
D. A loop seal or U-seal is provided in a vertical
condenser sub-cooler to prevent quick draining of
the condensate.

A

A. Safety valves are provided in heat exchangers
for removal of non-conden-sables.

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53
Q

With increase in gas flow rate to fabric surface area ratio
(Nm3/hr/m2 fabric surface area), the size & the cost of a
bag filter

A. increases
B. decreases
C. remain unaffected
D. none of these

A

B. decreases

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54
Q

A head comprises of straight flange section, corner torus,
section and central dished section. Crown radius and
knuckle radius in a head is related respectively to the

A. central dished section and corner torus
section.
B. corner torus section and central dished section.
C. central dished section and straight flange section.
D. straight flange section and corner torus section.

A

A. central dished section and corner torus
section.

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55
Q

Number of evaporators which can be used in service in a
multiple effect evaporation system is limited by the

A. practical limit reached, due to low heat transfer
rate because of inadequate temperature
difference.
B. economic limit reached, when the plant cost
exceeds the saving of steam.
C. both (a) & (b).
D. neither (a) nor (b).

A

C. both (a) & (b).

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56
Q

Which of the following is used to set the diameter of the
distillation column ?

A. Number of theorectical plates.
B. Static submergence.
C. Allowable vapour velocity.
D. Length of straight rectangular weir on cross-flow
tray.

A

C. Allowable vapour velocity.

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57
Q

Ponchon Savarit method is based on the use of enthalpy
concentration diagram, which contains the bubble point
curve (saturated liquid curve), dew point curve (saturated
vapour curve) and equilibrium tie lines. As compared to
McCabe-Thiele’s method, this method

A. is more accurate in finding the number of
equilibrium stages.
B. accounts for the enthalpy changes in the process.
C. facilitates direct calculation of heat load on
reboiler & condenser from, the diagram used in
this method.
D. all ‘a’, ‘b’ & ‘c’.

A

D. all ‘a’, ‘b’ & ‘c’.

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58
Q

The optimum size ratio for two mixed reactors in series
depends on the kinetics of the reaction and the conversion
level. For reaction orders more than one, the

A. equal sized reactors are the best.
B. smaller reactor should come first.
C. larger reactor should come first.
D. none of these.

A

B. smaller reactor should come first.

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59
Q

In a shell and tube heat exchanger, tube side __________
of the mass velocity.

A. heat transfer co-efficient is proportional to 0.8th
power
B. pressure drop is proportional to the square
C. both ‘a’ & ‘b’
D. neither ‘a’ nor ‘b’

A

C. both ‘a’ & ‘b’

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60
Q

Which of the following is not a graphical method (but is an
analytical method) for the calculation of theoretical
number of stages in case of continuous binary distillation?

A. Sorel-Lewis method.
B. McCabe-Thiele’s method.
C. Ponchon-Savarit method.
D. none of these.

A

A. Sorel-Lewis method.

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61
Q

Saddle supports are used for supporting __________
vessels.

A. horizontal cylindrical
B. tall vertical
C. thick walled vertical
D. thick spherical

A

A. horizontal cylindrical

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62
Q

The diameter of a propeller agitator used in agitation tank
ranges from __________ percent of the tank diameter
and its peripherial speed is normally 300 to 500
metres/minute.
A. 5 to 10
B. 15 to 30
C. 40 to 50
D. 55 to 75

A

B. 15 to 30

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63
Q

In packed towers provided with saddle packing, liquid
redistributors are positioned at every __________ times
column diameter or 6 metres whichever is less.

A. 2-3
B. 5-8
C. 10-15
D. 20-25

A

B. 5-8

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64
Q

Optimum reflux ratio in a continuous distillation column is
determined by the

A. maximum permissible vapour velocity.
B. flooding limit of the column.
C. total cost consideration (fixed cost of the
column plus the cooling water & steam cost).
D. none of these.

A

C. total cost consideration (fixed cost of the
column plus the cooling water & steam cost).

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65
Q

Cooling water fouling factors vary in the range of 0.001 to
0.003

A. (BTU/hr.ft2 . °F)-1
B. (kcal/hr.m2 .°C)-1
C. (W/m2.°K)-1
D. (kcal/hr. m. °C)-1

A

A. (BTU/hr.ft2 . °F)-1

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66
Q

Minimum recommended baffle spacing in a shell and tube
heat exchanger is about (where, D = shell diameter )

A. 0.2 D
B. 0.5 D
C. 0.66 D
D. 0.80 D

A

A. 0.2 D

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67
Q

The maximum liquid gradient over a tray must not exceed

A. 0.5” -1.25”.
B. 2”-3.5”.
C. 5”.
D. half the tray spacing.

A

A. 0.5” -1.25”.

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68
Q

An underdesigned steam trap will

A. waste steam.
B. destroy itself of acceleration wear due to rapid
recycling.
C. back up condensate and cause water hammer
in steam line.
D. none of these.

A

C. back up condensate and cause water hammer
in steam line.

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69
Q

The slope of the feed line in distillation opeartion is given
by (where, q = fraction of the feed stream that is liquid.)

A. -q
B. -q/(1-q)
C. -q/(q-1)
D. none of these

A

B. -q/(1-q)

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70
Q

Speed of industrial paddle agitator ranges from
__________ rpm.

A. 1 to 5
B. 20 to 100
C. 500 to 750
D. 1000 to 2000

A

B. 20 to 100

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71
Q

__________ strain is measured using a ‘strain rosetter’.

A. Volumetric
B. Shear
C. Linear
D. none of these

A

C. Linear

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72
Q

Thin spherical shells subjected to internal pressure,
develop __________ stresses.

A. radial
B.circumferential
C. both (a) & (b)
D. neither (a) nor (b)

A

A. radial

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73
Q

With increase in the reflux ratio for a fixed production from
a continuous binary distillation column, the __________
decreases.

A. fixed charges initially
B. running cost of cooling water for condenser
C. vapour & liquid load both
D. running cost of steam for reboiler

A

A. fixed charges initially

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74
Q

The slope of operating line in the rectifying section of a
distillation column is unity, if the reflux ratio is

A. 0
B. ∞
C. 1
D. minimum

A

B. ∞

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75
Q

Vertical vessels are not supported by

A. brackets
B. skirts
C. columns
D. saddles

A

D. saddles

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76
Q

With increase in pressure drop (for a given particle size),
the dust collection efficiency of a cyclone separator will

A. increase
B. decrease
C. remain unaffected
D. increase or decrease depending on the nature of
the dust.

A

A. increase

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77
Q

Spherical shaped pressure vessel is considered to be the
most ideal, because it can

A. withstand higher pressure for a given metallic
shell thickness.
B. be fabricated very easily.
C. be designed without wind load considerations.
D. be supported very easily.

A

A. withstand higher pressure for a given metallic
shell thickness.

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78
Q

An adequate clearance between the tray and the shell
wall of a distillation column is provided to

A. drain the liquid from the tray when the unit is not
in operation.
B. allow for thermal expansion and facilitate
installation.
C. avoid back-trapping.
D. none of these.

A

B. allow for thermal expansion and facilitate
installation.

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79
Q

Overall tray efficiency of a distillation column is the ratio
of the number of

A. overall gas transfer units to the number of ideal
trays required.
B. ideal trays required to the number of real trays
required.
C. real trays required to the number of ideal trays
required.
D. none of these.

A

B. ideal trays required to the number of real trays
required.

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80
Q

Pick out the wrong statement about the design of a sieve
plate column.

A. An increased weir height improves the tray
efficiency at the cost of high plate pressure drop;
optimum wear height being 40-90 mm for column
pressure above atmospheric and 6-12 mm for
vacuum columns.
B. For segmental downcomers, the chord length is
60-80% of the column diameter. An initial value of
downcomer area of 12% is taken in the design.
C. Width of the calming section provided at the inlet
and outlet sides of the plate is 75 mm for column
diameter below 1.5 metres and 100 mm for larger
diameter columns.
D. Minimum recommended downcomer
residence time for the disengagement of
entrained vapour is the same for both foaming
and non-foaming liquids, which is about 20
seconds.

A

D. Minimum recommended downcomer
residence time for the disengagement of
entrained vapour is the same for both foaming
and non-foaming liquids, which is about 20
seconds.

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81
Q

Generally, no corrosion allowance in wall thickness of a
part is required, if the thickness is more than __________
mm.
A. 10
B. 20
C. 30
D. 5

A

C. 30

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82
Q

Multiple blade paddle agitator is used for mixing high
viscosity liquids/paste in which the paddle diameter is
commonly 0.8 times the tank diameter. However, the
width of the blade is in the range of __________ times the
paddle diameter.

A. 0.1 to 0.25
B. 0.3 to 0.5
C. 0.5 to 0.6
D. 0.65 to 0.80

A

A. 0.1 to 0.25

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83
Q

In a __________ rivetted joint, the rivets in the various
rows are opposite to each other.

A. zig-zag
B. chain
C. diamond
D. none of these

A

B. chain

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84
Q

Pick out the wrong statement:

A. The tensile strength of a brittle material is less
than its compressive strength.
B. The compressive strength of a ductile materia] is
less than its tensile strength.
C. In a thick cylindrical shell, the hoop stress is
maximum at the inner radius.
D. The value of crushing load is more than that
of buckling load for long columns.

A

D. The value of crushing load is more than that
of buckling load for long columns.

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85
Q

Generally, elliptical dished heads

A. are manufactured on 2:1 ratio of major to minor
axis and is recommended to be used for pressure
vessels operating above a pressure of 1.5 MN/m2
B. resist half the pressure rating compared to hemi
spherical head provided on the cylindrical shell of
the same thickness and diameter.
C. are approximately as strong as seamless
cylindrical shell having the corresponding I.D and
O.D.
D. all (a), (b) and (c)

A

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

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86
Q

Pick out the wrong statement pertaining to the
comparative evaluation of performance of the packed
tower and the plate tower.

A. Plate tower is perferred, if interstage cooling is
required to remove heats of reaction or solution.
B. Plate tower is preferred over packed tower, if the
operation involves liquids containing dispersed
solids.
C. The total weight of a dry plate tower is usually
much more than that of a dry packed tower
designed for the same duty.
D. In operations involving large temperature
changes. (e.g. distillation), plate towers are
preferred over packed towers as the packing may
be crushed due to large temperature changes.

A

C. The total weight of a dry plate tower is usually
much more than that of a dry packed tower
designed for the same duty.

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87
Q

The circumferential (hoop) stress in a thin walled
cylinderical vessel under internal pressure is
A. pd/2t
B. pd/4t
C. pd/t
D. pd/3t

A

A. pd/2t

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88
Q

Le/D For fully open gate valves would be

A. much more than that for fully open globe valves.
B. much less (say 2% than that for fully open globe
valves).
C. around 7.
D. both (b) and (c).

A

D. both (b) and (c).

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89
Q

LMTD correction factor is used in heat exchanger design
for
A. double pipe heat exchanger.
B. multipass shell and tube heat exchanger.
C. fouling fluids.
D. counter flow of hot and cold fluids.

A

B. multipass shell and tube heat exchanger.

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90
Q

Floating head heat exchangers are used for the

A. heat transfer between corrosive fluids.
B. cases where temperature difference between
the shell and the tubes is more (>50°C).
C. co-current heat transfer systems.
D. counter-current heat transfer systems.

A

B. cases where temperature difference between
the shell and the tubes is more (>50°C).

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91
Q

The most common standard size of bubble caps used in
industrial operation is

A. 1” dia cap with 0.5” dia riser.
B. 6” dia cap with 4” dia riser.
C. 8” dia cap with 1” dia riser.
D. 4” dia cap with 8” dia riser.

A

B. 6” dia cap with 4” dia riser.

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92
Q

Compensation against openings in process vessels for
giving inlet and outlet connections, for providing sight
glasses and manholes etc. is provided for strength and
rigidity. The most efficient type of compensation is of
__________ type.
A. nozzle or rim
B. flared out
C. fluid in
D. ring plate

A

A. nozzle or rim

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93
Q

In case of a continuous distillation column, increase in
reflux ratio may result in the

A. lower fixed charges for the column.
B. greater cost for the reboiler heat supply.
C. greater cost for the condenser coolant.
D. all (a), (b) and (c).

A

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

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94
Q

In a distillation column, the minimum residence time for
liquid in the downspout is about __________ seconds.
A. 1
B. 8
C. 80
D. 180

A

B. 8

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95
Q

Thickness of the frame of a plate and frame filter as
compared to that of plates is
A. less
B. same
C. more
D. either (a) or (b)

A

C. more

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96
Q

Which of the following factors affect the pressure drop in
a co-current gas-liquid absorption packed tower ?

A. Size, shape, orientation and surface of the
packing particles.
B. Density and viscosity of fluids.
C. Fluid flow rates.
D. All (a), (b) and (c).

A

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

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97
Q

The thickness of heat transfer plates used in the plate type
heat exchanger ranges from __________ mm, pressed in
a single piece provided with grooves & corrugations.

A. 0.3 to 0.8
B. 1.25 to 3.125
C. 3.5 to 7.0
D. 8-12

A

B. 1.25 to 3.125

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98
Q

Rivets are generally specified by the

A. head diameter
B. shank diameter
C. overall length
D. none of these

A

B. shank diameter

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99
Q

Length to diameter ratio of most rotary driers is in the
range of

A. 1 to 2
B. 4 to 10
C. 10 to 20
D. 20 to 30

A

B. 4 to 10

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100
Q

Tube wall thickness depends on the corrosiveness 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. 16
B. 19
C. 28
D. 38

A

B. 19

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101
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 viscosity
above __________ poise.

A. 300
B. 600
C. 1000
D. 1500

A

B. 600

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102
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.
D. both(b) & (c).

A

D. both(b) & (c)

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103
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. is directly proportional to the radius of the dust
particle path.
D. none of these.

A

D. none of these.

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104
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. ∞
B. 1
C. 20.8
D. 2

A

B. 1

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105
Q

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

A. A vapor phase reactor.
B. Pot type reactor.
C. A liquid phase reactor.
D. A liquid phase catalytic reactor.

A

A. A vapor phase reactor.

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106
Q

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

A. density of the gas, but is independent of the
viscosity of the gas.
B. density of the gas and inversely as viscosity
of the gas.
C. viscosity of the gas and inversely as density of the
gas.
D. none of these.

A

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

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107
Q

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

A. 1-1 cocurrent
B. double pipe
C. all multipass
D. all (involving liquid/liquid heat transfer)

A

C. all multipass

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108
Q

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

A. expansion joint.
B. changes in its direction.
C. change in the shape of pipeline.
D. all (a), (b) and (c).

A

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

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109
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.
B. increases upwards.
C. remains same throughout.
D. may decrease or increase upwards depending
upon whether vacuum or positive pressure would
be maintained inside the shell.

A

A. decreases upwards

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110
Q

In the design of a paddle agitator, the ratio of paddle
diameter over tank diameter is normally taken as
A. 0.1
B. 0.8
C. 0.25
D. 0.5

A

B. 0.8

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111
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. working
B. damaging
C. allowable
D. none of these

A

B. damaging

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112
Q

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

A. l to3
B. 4 to 8
C. 3 to 12.5
D. 12.5 to 18.5

A

C. 3 to 12.5

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113
Q

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

A. 5-10
B. 15-20
C. 30-35
D. 35-40

A

B. 15-20

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114
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)
B. d2(d1+d2)
C. (d2+d1)/d1
D. (d2+d1)/d2

A

A. d1/(d1+d2)

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115
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.
B. lower skirt clearance.
C. lower static submergence.
D. small downcomer liquid seal.

A

A. liquid gradient on the tray.

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116
Q

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

A. 2
B. 5
C. 10
D. 15

A

B. 5

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117
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/2 or minimum 2” to 5D.
B. D/5 or minimum 2” to 5D.
C. D/5 or minimum 2” to D.
D. none of these.

A

B. D/5 or minimum 2” to 5D.

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118
Q

Brass valves are usually made for pipe sizes __________
inches.

A. ≤1
B. ≤2
C. >2.5
D. >3.5

A

B. ≤2

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119
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. increases
B. decreases
C. remains same
D. may increase or decrease depending upon the
solubility of the gas in the liquid

A

C. remains same

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120
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.
B. can accommodate less number of tubes for a given
shell diameter.
C. facilitates easier shell side cleaning; hence is more suitable for handling high dirt factor shell
side fluid.
D. creates relatively lower turbulence on the shell side resulting in lower shell side heat transfer co-
efficient.

A

A. results in higher shell side pressure drop

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121
Q

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

A. The corrosive and fouling fluid should be
preferably routed through the tubes.
B. The viscous fluid should be routed through the
shell side.
C. Lower flow rate fluid should be routed through the
shell side.
D. Higher pressure fluid stream should be routed
through the shell side.

A

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

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122
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.
D. all (a); (b) and (c).

A

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

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123
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. ‘n’th
B. (1/n)th
C. 0.5 nth
D. 1.5 nth

A

B. (1/n)th

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124
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

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

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125
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

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

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126
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.
D. all (a), (b) and (c).

A

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

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127
Q

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

A. low cost.
B. high latent heat.
C. non-corrosive condensate.
D. high film co-efficient.

A

B. high latent heat.

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128
Q

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

A. Conical
B. Flat
C. Dome
D. Umbrella

A

A. Conical

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129
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

D. 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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130
Q

Value of Peclet number = ∞, is the representative of
A. laminar flow.
B. complete back mixing,
C. plug flow.
D. eddy diffusivity = 0.

A

C. plug flow.

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131
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.
D. both (b) and (c).

A

D. both (b) and (c).

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132
Q

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

A. less than
B. 1.25-1.50 times
C. 2.5 times
D. one-fourth of

A

B. 1.25-1.50 times

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133
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
B. 1.6 to 2
C. 2.5
D. 1.5 to 3

A

A. 1.3 to 2

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134
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.
D. all (a), (b) and (c).

A

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

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135
Q

Accidents in chemical plants are mostly due to
A. inadequate equipment design.
B. faulty operating procedures.
C. improper layout of the equipment
D. failure of equipment

A

B. faulty operating procedures.

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136
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

D. bubble cap

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137
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 - dh)/ph
B. (ph - dh . dt/2)/ph
C. (ph - dt)/ph
D. (ph - dh)/dh

A

C. (ph - dt)/ph

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138
Q

__________ is the determining factor for the number of
bubble caps to be used per tray.
A. Permissible slot velocity
B. Tray diameter
C. Liquid load
D. Vapor load

A

A. Permissible slot velocity

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139
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

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

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140
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. 250
B. 450
C. 650
D. 750

A

C. 650

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141
Q

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

A. Aluminium
B. Stainless steel
C. Copper
D. Carbon steel

A

C. Copper

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142
Q

Normal screwed fittings are used for pipes upto a
diameter of __________ inches.
A. 1.5
B. 3
C. 5
D. 7

A

B. 3

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143
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”.
B. more than the tube diameter.
C. equal to the tube diameter.
D. more in case of triangular pitch as compared to
the square pitch tube layout.

A

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

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144
Q

Diameter of the seive tray column is determined by the

A. lower limit of vapour velocity.
B. upper limit of the vapour velocity.
C. hole diameter of the seive tray.
D. height of the plate spacing.

A

B. upper limit of the vapour velocity.

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145
Q

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

A. decreases.
B. increases.
C. remains unaffected.
D. may increase or decreaes depending upon
whether the fluid is Newtonian or non-Newtonion.

A

A. decreases.

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146
Q

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

A. 5.5
B. 12.5
C. 30.5
D. 45.5

A

B. 12.5

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147
Q

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

A. < 10
B. > 10
C. > 20
D. 30

A

B. > 10

148
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.
B. shell side for smaller total pressure drop.
C. shell side, if the flow is counter-current and tube
side if the flow is co-current.

D. shell side for large overall heat transfer co-
efficient.

A

A. tubes to avoid the expansion of high pressure
shell construction

149
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.
A. of its flexibility and nearly constant efficiency
under varying conditions of operation.
B. it incurs less pressure drop as compared to any
other try designed for the same duty.
C. it eliminates the foaming and entrain-ment
tendency during operation.
D. none of these.

A

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

150
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
B. 1.2 Aa = 1.2 Sa
C. Sa = 1.5 Aa
D. Aa = 1.5 Sa

A

A. Aa = Sa

151
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 = 1.004G0.37
B. 1.004G0.8
C. hG = 0.0176G0.37
D. 0.0176G1.37

A

A. hG = 1.004G0.37

152
Q

In the agitators, the power required will be changed with
the increase of diameter of agitator (D) as
A. D2
B. D5
C. D
D. D9

A

B. D5

153
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.
D. both (a) and (b)

A

D. both (a) and (b)

154
Q

Tube side heat transfer co-efficient for turbulent flow of
liquid through tubes is proportional to
A. G^0.2
B. G^0.5
C. G^0.8
D. G^1.5

A

C. G^0.8

155
Q

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

A. half
B. equal to
C. twice
D. eight times

A

C. twice

156
Q

The dust collection efficiency of electrostatic precipitator
increases with increase in the
A. gas flow rate.
B. electrode area.
C. both (a) & (b).
D. neither (a) nor (b).

A

B. electrode area.

157
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
B. 2.5 to 3.5
C. 4 to 5
D. 6 to 8

A

A. 1 to 1.5

158
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.
D. All (a), (b) and (c).

A

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

159
Q

The absorption factor is defined as (where, S1 = slope of
the equilibrium curve, S2 = slope of the operating line)
A. S1/S2
B. S1.S2
C. S2/S1
D. 1/S1.S2

A

A. S1/S2

160
Q

In shell and tube heat exchangers, straight tie rods are
used to
A. hold baffle in space.
B. fix the tubes in position.
C. account for thermal strain.
D. none of these.

A

A. hold baffle in space

161
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.
D. all (a), (b) & (c).

A

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

162
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
B. σh = σL
C. σh = σL/2
D. no relation exists

A

A. σh = 2 σL

163
Q

Excessive liquid gradient on a tray may result in the
A. maldistribution of gas.
B. back trapping.
C. gas blowing beneath cap skit.
D. all (a), (b) and (c).

A

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

164
Q

The ratio of tube length to shell diameter in case of liquid
shell and tube heat exchanger ranges from
A. 2 to 3
B. 3 to 5
C. 4 to 8
D. 6 to 12

A

C. 4 to 8

165
Q

What is the slope of the operating line in the stripping
section of a distillation column ?
A. 0
B. ∞
C. > 1
D. < 1

A

C. > 1

166
Q

__________ shaped roof is most commonly used for
cylindrical tanks.
A. Cone
B. Dome
C. Umbrella
D. Flat

A

A. Cone

167
Q

In a thin cylindrical shell, the hoop stress is __________
stress.
A. radial
B.circumferential tensile
C. compressive

A

B.circumferential tensile

168
Q

Commercial packed scrubbers are normally designed for
a pressure drop range of __________ mm water coloumn
per metre of packed height.
A. 4-8
B. 17-34
C. 52-68
D. 88-105

A

B. 17-34

169
Q

The retention time of material in a rotary dryer depends
upon its
A. rpm
B. slope & length
C. flights arrangement
D. all (a), (b) and (c)

A

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

170
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
D. all (a), (b) and (c)

A

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

171
Q

Rotary driers are most economically designed for the
number of heat transfer units (HTU) from
A. 0.01 to 1
B. 1.5 to 2.5
C. 5 to 10
D. 10 to 20

A

B. 1.5 to 2.5

172
Q

The difficulty of liquid distribution in packed towers is
accentuated, when the ratio of tower diameter to packing
diameter is
A. < 30
B. < 7
C. > 7 < 15
D. > 20 < 50

A

B. < 7

173
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.
D. both (b) & (c).

A

D. both (b) & (c).

174
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.
D. all (a), (b) and (c).

A

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

175
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
D. all (a), (b) & (c)

A

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

176
Q

With increase in temperature drop (in a shell and tube
heat exchanger), the LMTD correction factor, FT
A. decreases very rapidly
B. increases very rapidly
C. remains constant
D. increases linearly

A

A. decreases very rapidly

177
Q

The normal range of velocity of steam in pipes is
__________ m/sec.
A. 0.1-0.5
B. 1-5
C. 10-20
D. 80-100

A

D. 80-100

178
Q

__________ dished head is the strongest of all.
A. Hemispherical
B. Elliptical
C. Torispherical
D. none of these

A

A. Hemispherical

179
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

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

180
Q

“A clamming section” before the liquid flows into the
downcomer is provided to
A. permit release of entrained vapour in the
liquid.
B. reduce the discharge fluctuation.
C. ensure better vapour-liquid contact.
D. cool the liquid before it flows down.

A

A. permit release of entrained vapour in the
liquid.

181
Q

The units of Young’s modulus of elasticity and
__________ are the same.
A. strain
B. stress
C. modular ratio
D. none of these

A

B. stress

182
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.
D. all (a), (b) & (c).

A

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

183
Q

Vertical condenser is advantageous to the horizontal
condenser from operation point of view, when
A. hydrostatic head is required for refluxing the
condensate.
B. only the function of condensation is to be carried
out.
C. sub cooling of condensate is desired.
D. both the functions of condensation & sub
cooling are carried out in a single unit.

A

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

184
Q

Hazards associated with the relief valve leakage for
extremely hazardous material storage can be taken care
of by providing
A. rupture diaphragm
B. dikes
C. surge chamber
D. none of these

A

A. rupture diaphragm

185
Q

Minimum baffle spacing recommended in a shell and tube
heat exchanger is equal to
A. 5 cms
B. 40% of the I.D. of the shell
C. 25 cms
D. I.D. of the shell

A

A. 5 cms

186
Q

__________ liquor is best handled in a long tube vertical
evaporator.
A. Foamy
B. Scaling
C. Viscous
D. Salting

A

A. Foamy

187
Q

Theoretically calculated diameter of the stripping section
of the continuous rectification column is __________ that
of the enriching section.
A. less than
B. more than
C. same as
D. either more or less (depending upon relative
volatility)

A

B. more than

188
Q

Hold up of material in an operating rotary drier is in the
range of
A. 0.05 to 0.15
B. 0.25 to 0.50
C. 0.5 to 0.8
D. 0.8 to 0.9

A

A. 0.05 to 0.15

189
Q

A binary liquid azeotropic mixture has boiling point higher
than either of the components, when it shows
__________ deviation from Raoult’s Law.
A. positive
B. negative
C. no
D. none of these

A

B. negative

190
Q

Flanges are connected to pipes by
A. screwing
B. welding
C. brazing
D. all (a), (b) and (c)

A

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

191
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
B. 1 to 1.5
C. 1.5 to 2
D. 2 to 2.5

A

A. 0.5 to 1

192
Q

Shortest distance between two tubes is
A. called tube pitch.
B. called tube clearance.
C. more in case of triangular pitch as compared to
square pitch of tube layout.
D. none of these.

A

B. called tube clearance.

193
Q

__________ tower is the most suitable gas-liquid
contacting device involving highly corrosive fluids.
A. Sieve plate
B. Packed
C. Bubble cap plate
D. None of these

A

B. Packed

194
Q

At equal mass velocities, the values of film coefficients for
gases as compared to that for liquids are generally.
A. higher
B. lower
C. same
D. unpredictable

A

B. lower

195
Q

The ratio of the largest load in a test to the original cross-
sectional area of the test specimen is called the

__________ stress.
A. yield point
B. breaking
C. ultimate
D. none of these

A

C. ultimate

196
Q

Baffle spacing is generally __________ the I.D. of the
shell.
A. more than
B. not greater than
C. not less than one fifth of
D. both (b) and (c)

A

D. both (b) and (c)

197
Q

The wall thickness of thin cylindrical shell with
hemispherical ends is __________ that of the spherical
ends.
A. equal to
B. more than
C. less than
D. either (b) or (c); depends on maximum
permissible internal pressure

A

B. more than

198
Q

A ‘rupture disc’ is provided in chemical equipments as an
accessory meant for

A. relieving excess pressure.
B. creating turbulence.
C. enhancing mixing rate.
D. avoiding vortex formation.

A

A. relieving excess pressure

199
Q

In a vertical short tube evaporator (Calendria type), the
A. tube dia of 2.5-7.5 cms, tube length of 75-200 cms
and cylinderical drum dia of 1-6 metres are
normally used.
B. area of central downtake is equal to 40 to 100%
of total cross-sectional area of the surrounding
tube.
C. liquor is inside the tube while the steam is outside
the tube.
D. all (a), (b) & (c).

A

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

200
Q

In a multipass shell and tube heat exchanger, the problem
of differential expansion between the shell and tube
passes is taken care of by using a
A. U-bend
B. floating head tube sheet
C. either (a) or (b)
D. neither (a) nor (b)

A

C. either (a) or (b)

201
Q

In a shell and tube heat exchanger, the shortest centre to
centre distance between the adjacent tubes is
A. called tube pitch.
B. called tube clearance.
In a shell and tube heat exchanger, the shortest centre to
centre distance between the adjacent tubes is
A. called tube pitch.
B. called tube clearance.
C. always less than the diameter of the tube.
D. none of these.

A

A. called tube pitch.

202
Q

Any shell opening greater than 5 cms for a storage tank
must be reinforced for reason of
A. preventing the local overstressing of the shell
around the opening.
B. reduction of discontinuity in shape at the junction.
C. making the joint leak proof.
D. none of these.

A

A. preventing the local overstressing of the shell
around the opening.

203
Q

Minimum tube pitch recommended for shell and tube heat
exchangers is about __________ times the outside
diameter of the tube.
A. 1.25
B. 1.75
C. 2.5
D. 3.5

A

A. 1.25

204
Q

Liquid redistribution should be done in a packed tower
packed with raschig rings every 6 metres or __________
times the column diameter, whichever is lower.
A. 2.5-3.0
B. 5-7.5
C. 10-12.5
D. 15-20

A

A. 2.5-3.0

205
Q

Slope of countercurrent flow rotary drier is in the range of
__________ meter/metre.
A. 0 to 0.08
B. 0 to 0.8
C. 0 to 1.5
D. 0 to 2.2

A

A. 0 to 0.08

206
Q

In case of saddle packing (e.g., berl and intralox saddles),
the maximum size of the packing should not exceed
__________ of the column diameter.
A. l/5th
B. l/15th
C. l/30th
D. l/50th

A

B. l/15th

207
Q

Seamless pipe is made

A. from rolled strips formed into cylinders and seam-
welded.

B. by extrusion & casting into static and centrifugal
molds.
C. by forging a solid round, piercing it by
simultaneously rotating & forcing it over a piercer
point and further reducing it by rolling gas
drawing.
D. both (b) and (c).

A

D. both (b) and (c).

208
Q

The thermal stress in a metallic bar does not depend upon
the
A. changes in temperature.
B. cross-sectional area.
C. both (a) and (b).
D. neither (a) nor (b).

A

B. cross-sectional area.

209
Q

The minimum baffle height should be
A. equal to the impeller diameter.
B. twice the impeller diameter.
C. twice the tank diameter.
D. 3/4 of the tank height.

A

B. twice the impeller diameter

210
Q

For turbulent flow (NRe > 2100) of low viscosity fluid (μ >
20cp) in steel pipes, the optimum inside pipe diameter is
given by(where, Q = fluid flow rate, ft3/sec.ρ = fluid
density, lb/ft3 μ = fluid viscosity, centipoise Di = optimum
inside pipe diameter, inches)
A. Di, opt = 3.9 Q0.45 ρ0.13
B. Di, opt = 3.9 Q0.45 . μ0.95
C. Di, opt = 4.7 Q0.36 . μ3.2ρ0.13
D. Di, opt = 3 Q0.36 . μ0.88

A

A. Di, opt = 3.9 Q0.45 ρ0.13

211
Q

To avoid the tearing off the plate of an edge, the margin
(i.e., the minimum distance from the centre of the rivet
hole to the nearest edge of the plate) should be equal to
A. 0.5 d
B. d
C. 1.5 d
D. 2.5 d

A

C. 1.5 d

212
Q

The normal range of velocity of water in pipes is
__________ m/sec.
A. 0.1-0.5
B. 1-2
C. 10-50
D. 15-30

A

B. 1-2

213
Q

Baffles are provided in a shell and tube heat exchanger to
increase the turbulence and velocity of the shell side fluid.
Which of the following shaped baffles does not fall in the
category of transverse baffle ?
A. Segmental baffle
B. Flat plate extending across the wall
C. Disk type baffle
D. Helical type baffle

A

B. Flat plate extending across the wall

214
Q

A certain pressure vessel manufacturer avoids doing
reinforcements calculations for openings by always
providing a reinforcing pad extending upto double the
diameter of the opening and of the same material and
thickness as that of the shell wall. If area compensation is
accepted as a code guideline, his approach leads to safe
design
A. only if the opening is on spherical vessel.
B. only if the opening is on a vertical cylinderical
vessel.
C. only if the opening is on a horizontal cylinderical
vessel.
D. irrespective of the shape of the vessel.

A

D. irrespective of the shape of the vessel.

215
Q

In a __________ rivetted joint, the number of rivets
decreases from the innermost row to the outermost row.
A. chain
B. diamond
C. zig-zag
D. none of these

A

B. diamond

216
Q

Large process vessels operating under extreme
temperature and pressure conditions are normally clad/
lined with materials like stainless steel, aluminium, nickel
& its alloys, copper & its alloys and titanium. The cladding
thickness is generally about __________ percent of the
total thickness.
A. 1 to 5
B. 10 to 20
C. 30 to 40
D. 40 to 50

A

B. 10 to 20

217
Q

Heat transfer co-efficient for a horizontal condenser as
compared to a vertical condenser operating under similar
conditions is
A. same
B. less
C. about 3 times
D. about 0.33 times

A

C. about 3 times

218
Q

Pick out the wrong statement pertaining to the design of
the distillation column.
A. Generally, a skirt clerance of 0.5” to 1.5’ is
recommended to prevent plugging of the slots by
residue build up.
B. The purpose of the slot is to disperse the gas into
the liquid in the form of small bubbles.
C. If sufficient slot area is not provided, the gas may
pass through the skirt clearance.
D. none of these.

A

D. none of these.

219
Q

In distillation columns, bubble caps are held in place over
trays by
A. rivets
B. a hold down bar
C. bolts
D. both (b) and (c)

A

D. both (b) and (c)

220
Q

The buckling tendency of compression members is
always in the direction of the
A. least radius of gyration.
B. axis of the load.
C. perpendicular to the axis of the load.
D. none of these.

A

A. least radius of gyration.

221
Q

In case of plain carbon steel, butt welded joints are used
for shell plate thickness ≤ __________ cms.
A. 1.2
B. 0.5
C. 3.8
D. 6.8

A

C. 3.8

222
Q

The average velocity in the tubes of a 1-4 heat exchanger
is __________ times that in 1-1 heat exchanger having
the same size & number of tubes and operated at same
liquid flow rate.
A. 2
B. 1/2
C. 4
D. 1/4

A

C. 4

223
Q

When one of the fluids is highly corrosive and has fouling
tendency, it should

A. preferably flow inside the tube for its easier
internal cleaning.
B. perferably flow outside the tube.
C. flow at a very slow velocity.
D. flow outside the tube, when the flow is counter-
current and inside the tube when the flow is co-
current.

A

A. preferably flow inside the tube for its easier
internal cleaning.

224
Q

A/an __________ is used for changing the direction of a
pipeline.
A. elbow
B. union
C. flange
D. disc compensator

A

A. elbow

225
Q

Maximum plate efficiency is achieved in case of
__________ flow.
A. split
B. cross
C. cascade
D. reverse

A

B. cross

226
Q

The LMTD correction factor (FT) is defined as the
A. ratio of true temperature difference to the
LMTD.
B. ratio of LMTD to the true temperature difference.
C. differenced of true temperature difference and the
LMTD.
D. geometric mean of the true temperature
difference and the LMTD.

A

A. ratio of true temperature difference to the
LMTD.

227
Q

The clearance between two tubes in a shell and tube heat
exchanger is known as ‘ligament’, whose minimum value
is __________ the outside diameter of the tube, but in no
case it should be less than 4.5 mm.
A. equal to
B. half
C. one fourth
D. three fourth

A

C. one fourth

228
Q

The ratio for the rate of washing to the final rate of filtration
in a washing type of plate and frame filter is
A. 0.25
B. 0.50
C. 0.75
D. 1.25

A

A. 0.25

229
Q

Normally, the length to diameter ratio of rotary dryers
varies form 4 to 10 and for its economic operation, the
number of transfer units (NTU) for such dryers varies from
A. 1.5-2.5
B. 3.5-5.5
C. 7.5-10.0
D. 10-15

A

A. 1.5-2.5

230
Q

Value of Peclet number = 0, is the representative of
A. laminar flow.
B. complete back mixing.
C. plug flow.
D. eddy diffusivity = 0.

A

B. complete back mixing.

231
Q

Poisson’s ratio of a material is the ratio of unit lateral strain
to the unit axial elongation within its elastic limit. The value
of Poisson’s ratio for structural and pressure vessel steel
may be taken as
A. 0.01
B. 0.3
C. 0.75
D. 0.95

A

B. 0.3

232
Q

Removable connection of tubes to tube sheet is called
A. ferrule
B. socket
C. nipple
D. saddle

A

A. ferrule

233
Q

Typical static submergence for bubble cap plate column
operating at atmospheric pressure may be around
A. 2.5”
B. 0.5”
C. 5”
D. 50% of the plate spacing

A

B. 0.5”

234
Q

In the allocated cap area, bubble caps are generally
arranged on equilateral triangular pitch. Number of caps
fixed on a plate is with a
A. clearance of 25-75 mm.
B. cap pitch of 1.3-2 times the cap diameter.
C. either ‘a’ or ‘b’.
D. neither ‘a’ nor ‘b’.

A

C. either ‘a’ or ‘b’

235
Q

The length of straight rectangular weir used on cross-flow
trays is generally __________ the column diameter.
A. 0.6-0.8 times
B. equal to
C. twice
D. 2 ft irrespective of (for column > 3 ft diameter)

A

A. 0.6-0.8 times

236
Q

Le/D for couplings and unions would be
A. 60
B. 200
C. 350
D. negligible

A

D. negligible

237
Q

What is the slope of the operating line in the rectifying
section of a distillation coloumn ?
A. 0
B. ∞
C. > 1
D. <1

A

D. <1

238
Q

Stage efficiency for packed tower varies with the
A. type & size of packing.
B. fluid rates and fluid properties.
C. operating pressure and column diameter.
D. all (a), (b) and (c).

A

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

239
Q

The minimum plate spacing in most of the pertroleum
refinery distillation columns (of dia > 3 ft) is normally
__________ inches.
A. 6
B. 12
C. 18
D. 34

A

C. 18

240
Q

Joint efficiency (J) for a seamless pipe is
A. 1
B. 0.85
C. 1.2
D. < 0.5

A

A. 1

241
Q

For a given design of bubble cap, the number of bubble
caps to be used per tray is set by the
A. allowable gas velocity through the slots.
B. plate spacing.
C. diameter of the column.
D. all (a), (b) and (c).

A

A. allowable gas velocity through the slots

242
Q

The shell side pressure drop in a shell and tube heat
exchanger is maximum for __________ baffle.
A. disk and ring
B. segmental
C. orifice
D. independent of the type of

A

C. orifice

243
Q

The function of manholes provided in the shell of a
distillation column is to
A. keep a check on the liquid gradient over the plate
by direct visual observation.
B. give access to the individual trays for
cleaning, maintenance and installation.
C. guard against foaming & entrainment by dumping
antifoaming agent through it.
D. all (a), (b) and (c).

A

B. give access to the individual trays for
cleaning, maintenance and installation

244
Q

Back-trapping in a distillation column results due to

A. low gas velocity.
B. high gas velocity.
C. excessive liquid gradient over the tray.
D. low reflux ratio.

A

C. excessive liquid gradient over the tray.

245
Q

For a cylinderical vessel of moderate height, the weld joint
efficiency for joints parallel to the cylinderical axis is given
as 1.0, while for joints along the girth (circumference) it is given as 0.8. In calculating the shell wall thickness using
code formula for an internally pressurised cylinderical
vessel, what value of weld joint efficiency should be used
?
A. 0.8
B. 0.9
C. 1.0
D. (0.8)0.5

A

A. 0.8

246
Q

Diameter of bubble caps used in high pressure columns
is __________ as compared to that used in identical
vacuum columns.
A. less
B. more
C. same
D. either (a) or (b); no generalisation can be made

A

B. more

247
Q

The ideal size of round bubble caps to be used in
industrial distillation column having a diameter of 3-6
metres is __________ cms.
A. 5
B. 15
C. 7.5
D. 50

A

B. 15

248
Q

Lap joints are preferred for plates having thickness
__________ mm.

A. < 12.5
B. > 3
C. > 5
D. 5-10

A

B. > 3

249
Q

In a distillation column, minimum clearance to be
maintained betweeen the overflow weir and the last row
of the bubble caps is __________ cms.
A. 2.5
B. 7.5
C. 15
D. 20

A

B. 7.5

250
Q

Which of the following lengths of heat exchanger tubes
are normally not used in practice?
A. 2.5 metres
B. 6 metres
C. 10 metres
D. 0.5 metre

A

C. 10 metres

251
Q

A pipe is generally made of circular cross-section,
because a circular cross-section has the
A. higher structural strength.
B. lowest surface area requirement for a given
volume.
C. both (a) & (b).
D. none of these.

A

C. both (a) & (b).

252
Q

In case of a shell and tube heat exchanger, the effect of
L/D on inside film heat transfer co-efficient (hi) vanishes
after a Reynold number of
A. 1000
B. 3000
C. 5000
D. 10000

A

D. 10000

253
Q

Equivalent diameter for heat transfer calculation for a duct
of square cross-section having each side as ‘d’ will be
A. d
B. d0.5
C. 2πd
D. 2d

A

A. d

254
Q

A cylindrical storage tank can have a self-supported
conical roof,
A. if its diameter is less than 15-20metres.
B. if its diameter is more than 50 meters.
C. if the thickness of the roof is more than that of the
cylindrical shell.
D. irrespective of its diameter.

A

A. if its diameter is less than 15-20metres.

255
Q

For high pressure process equipments/vessels, the
connected nozzle should be
A. welded
B. screwed
C. flanged
D. brazed

A

C. flanged

256
Q

Smoker’s equation for the calculation of number of
equilibrium stages in a continuous binary distillation
column is used, when the
A. relative volatility is close to one (e.g.,
separation of close boiling isomers).
B. feed is not at its bubble point.
C. number of equilibrium stages in only stripping
section is to be calculated.
D. number of equilibrium stages required is likely to
be very small.

A

A. relative volatility is close to one (e.g.,
separation of close boiling isomers).

257
Q

Column support for the roof of cylindrical storage tank
must be provided for
A. small diameter tanks.
B. large diameter tanks.
C. small diameter tall tanks.
D. all tanks irrespective of their heights and
diameters.

A

B. large diameter tanks.

258
Q

For a cylinderical internally pressurised vessel, which of
the following closure types would withstand highest
pressure, if each closure is of the same material and
thickness?
A. hemispherical
B. ellipsoidal (2 : 1)
C. conical
D. flat plate

A

B. ellipsoidal (2 : 1)

259
Q

In inclined long tube vertical evaporators, the tubes are
inclined at an angle of

A. 15°
B. 90°
C. 45°
D. 60°

A

C. 45°

260
Q

In a continuous distillation column, the optimum reflux
ratio ranges from __________ times the minimum reflux
ratio.
A. 1.1 to 1.5
B. 1.6 to 2
C. 2.2 to 2.6
D. 2.7 to 3

A

A. 1.1 to 1.5

261
Q

The wall thickness for a large high pressure pipeline is
determined by the consideration of the
A. axial tensile stress in the pipe.
B. forces exerted by static and dynamic action at
bends.
C.circumferential pipewall tension.
D. temperature stresses.

A

C.circumferential pipewall tension

262
Q

In the case of a shell and tube heat exchanger, the
logarithmic mean temperature difference

A. is always less than arithmetic average value.
B. is always more than arithmetic mean value and
the geometric mean value.
C. is always less than arithmetic mean value, but
more than geometric mean value.
D. may be either more or less than geometric mean
and arithmetic mean value depending upon
whether the flow of stream is co-current or
counter-current.

A

A. is always less than arithmetic average value.

263
Q

Skirt support is the most suitable for supporting
__________ vessels.
A. small horizontal
B. large horizontal
C. tall vertical
D. thick walled

A

C. tall vertical

264
Q

Baffles may be eliminated for
A. low viscosity liquids (< 200 poise).
B. high viscosity liquids (> 600 poise).
C. large diameter tanks.
D. none of these.

A

B. high viscosity liquids (> 600 poise)

265
Q

Generally, as the length of the liquid path on a tray is
increased beyond 5 ft, the overall column efficiency
A. increases
B. decreases
C. remains same
D. may increase or decrease depending upon the
plate spacing

A

A. increases

266
Q

In packed absorption tower, onset of flooding usually
occurs at a pressure drop of about __________ mm of
water column per metre height of packing.
A. 25-50
B. 50-75
C. 200-250
D. 750-1000

A

B. 50-75

267
Q

For pipe flows, head is proportional to __________ at
constant capacity (where D = pipe diameter ).
A. 1/D
B. 1/D2
C. 1/D5
D. D2

A

C. 1/D5

268
Q

The minimum tray spacing in distillation column of
diameter less than 3 ft is normally __________ inches.
A. 6
B. 18
C. 24
D. 34

A

A. 6

269
Q

Oxygen carrying pipelines in chemical industries are
coloured with __________ colour.
A. yellow
B. black
C. blue
D. red

A

C. blue

270
Q

Normally, the ratio of the total riser area to the tower cross
sectional area (for bubble cap towers of diameter more
than 3 ft) is around
A. 0.4-0.6
B. 0.35-0.75
C. 0.1-0.2
D. 0.55-0.85

A

C. 0.1-0.2

271
Q

Pick out the wrong statement about the design of seive
plate column and the bubble cap column.
A. The downcomer design and the residence time in
the downcomer is almost same for seive plate and
bubble cap columns.
B. Weir length for a bubble cap plate is the same as
that for the seive plate.
C. Weir height for a bubble cap plate column is
the same as that for a seive plate column.
D. Weir height in case of a bubble cap plate ranges
from 50 to 150 mm and is higher than the seive
plate.

A

C. Weir height for a bubble cap plate column is
the same as that for a seive plate column.

272
Q

Maximum size of the raschig rings used in a packed tower
is about __________ of the coloumn diameter.
A. 1/10th
B. 1/20th
C. 1/30th
D. 1/50th

A

C. 1/30th

273
Q

The type of stress developed in a metallic bar on
subjecting it to a change in temperature without allowing
it to be deformed is __________ stress.
A. shear
B. tensile
C. compressive
D. thermal

A

D. thermal

274
Q

The safe distance of habitation from a hazardous
chemical plant (TLV of its product < 1000 ppm) should be
about __________ kms.
A. 1
B. 5
C. 15
D. 25

A

D. 25

275
Q

Pick out the wrong statement pertaining to a shell and
tube heat exchanger.
A. The minimum value of baffle spacing is 50 mm.
B. The maximum value of baffle spacing is equal to
the I.D. of the shell.
C. The maximum unsupported tube span is
generally about 75 times tube diameter, but is
reduced to about 60 times for aluminium, copper
& alloys of these.
D. Disk and doughnut baffle is the most
commonly used baffle.

A

D. Disk and doughnut baffle is the most
commonly used baffle.

276
Q

Corrosion allowance in the design of pressure
vessel/chemical equipment is not necessary, if
A. plain carbon steel and cast iron parts are used.
B. wall thickness is > 30 mm.
C. material of construction is high alloy steel.
D. both(b) & (c).

A

D. both(b) & (c).

277
Q

Maximum allowable vapour velocity in a bubble cap tower
is determined by the
A. entrainment considerations.
B. vapour density.
C. diameter of the column.
D. none of these.

A

A. entrainment considerations.

278
Q

Normally, the plate thickness of the bottoms and roofs of
vertically cylindrical storage vessels as compared to that
of the cylindrical shell is
A. more
B. less
C. same
D. more or less depending upon the pressure &
temperature inside the vessel and the nature of
the fluid contained therein.

A

B. less

279
Q

The practical representative values of HETP for a number
of commercial operations lies within a range of
__________ metre.
A. 0.1-0.2
B. 0.2-0.5
C. 0.4-0.9
D. 1.2-1.5

A

C. 0.4-0.9

280
Q

Of the pressure vessels, with same thickness but different
diameters, which one withstands higher pressure ?
A. Larger dia vessel.
B. Smaller dia vessel.
C. Larger dia long vessel.
D. Strength of the vessel is same irrespective of the
diameter.

A

B. Smaller dia vessel.

281
Q

Reflux ratio variation in a distillation column is between
A. zero and infinity
B. zero and one
C. minimum and infinity
D. none of these

A

C. minimum and infinity

282
Q

In condenser, the cooling water is passed in the tube side
in a pass arrangement, because
A. it reduces heat transfer area.
B. more thinner tubes can be used.
C. pressure drop is reduced.
D. it makes condenser compact.

A

A. it reduces heat transfer area.

283
Q

In packed towers provided with pall rings liquid
redistributors are positioned at heights of every 6 metres
or 5-10 times the column diameter, whichever is less.
Maximum size of the pall rings should not exceed
__________ of the column diameter.
A. 1/10-1/15th
B. 1/5-1/10th
C. 1/20-1/30th
D. 1/2 to 1/4th

A

A. 1/10-1/15th

284
Q

Height of the flights in the rotary drier is in the range of
A. 0.08 to 0.12 d
B. 0.02 to 0.05 d
C. 0.2 to 0.5 d
D. 0.5 to 0.6 d

A

A. 0.08 to 0.12 d

285
Q

Vapor velocity in a distillation column for non-foaming
mixture is in the range of __________ times the flooding
velocity.
A. 0.1 to 0.3
B. 0.6 to 0.7
C. 0.85 to 0.95
D. 1.5 to 2

A

B. 0.6 to 0.7

286
Q

Cylindrical storage tanks used for the storage of volatile
liquids (e.g., naphtha) have __________ roofs.
A. conical
B. flat
C. floating
D. fixed

A

C. floating

287
Q

Larger depth of liquid on the trays of a distillation column
A. leads to high tray efficiency.
B. results in higher pressure drop per tray.
C. both (a) & (b).
D. neither (a) or (b).

A

C. both (a) & (b).

288
Q

Pick out the wrong statement.
A. Plate efficiency increases with increase in
superficial vapour velocity till entrainment limit.
B. Increase in depth of the liquid about the slots
increases the plate efficiency, particularly if the
liquid depth is < 1”.
C. Too small a plate spacing can cause a low
efficiency, if the vapour velocity is greater than the
allowable value.
D. none of these.

A

D. none of these.

289
Q

Pick out the wrong statement.
A. In practical operation, distillation towers having
diameter 3-6 metres equipped with bubble cap
(round) size of 15 cms are used.
B. Height of packing in a packed tower is about 3
times the column diameter for raschig rings and
about 5 to 10 times the column diameter for
saddle packing.
C. In a seive tray, the minimum hole diameter is
equal to the tray thickness.
D. In a stainless steel seive tray, the minimum
hole diameter is equal to 10 times the plate
thickness.

A

D. In a stainless steel seive tray, the minimum
hole diameter is equal to 10 times the plate
thickness

290
Q

In the downcomer of a distillation column, the minimum
recommended residence time is about __________
seconds.
A. 2.5
B. 5
C. 12.5
D. 17.5

A

B. 5

291
Q

For identical situation, condensing film coefficient in case
of a horizontal condenser is almost __________ the value
expected in case of vertical condenser.
A. half
B. twice
C. thrice
D. five times

A

C. thrice

292
Q

A binary liquid azeotropic mixture has boiling point lower
than either of the components, when it shows
__________ deviation from Raoult’s Law.
A. positive
B. negative
C. no
D. none of these

A

A. positive

293
Q

In which of the following evaporators, steam is fed inside
the tube while the liquor is outside the tube?
A. Long tube vertical evaporator
B. Short tube vertical evaporator
C. Horizontal tube evaporator
D. None of these

A

C. Horizontal tube evaporator

294
Q

A single pass air heater is connected to a two pass unit.
For the air flow rate and other conditions remaining the
same, the film heat transfer co-efficient for air will vary in
the ratio of

A. 2
B. 2^0.8
C. 2^0.2
D. none of these

A

B. 2^0.8

295
Q

In a multipass shell and tube heat exchanger, the baffles
on shell side is primarily provided for
A. reducing scale deposition.
B. increasing pressure drop.
C. fixing the tubes.
D. creating turbulence.

A

D. creating turbulence.

296
Q

For turbine agitator, the impeller diameter is about
A. 0.3 to 0.5 d
B. 0.1 to 0.2 d
C. 0.65 to 0.85 d
D. 0.95 d

A

A. 0.3 to 0.5 d

297
Q

If a single tube pass heat exchanger is converted to two
passes; for the same flow rate, the pressure drop per unit
length in tube side will __________ times.
A. increase by 1.8
B. decrease by 2^2
C. increase by 2^1.6
D. none of these

A

C. increase by 2^1.6

298
Q

Pick out the wrong statement pertaining to the design of a
long tube vertical evaporator.
A. Tube dia is 3-6 cms, while tube length in 3-6
metres.
B. Steam is fed to the shell, whereas the liquor is
filled inside the tube.
C. Liquor level is maintained at l/3rd to 1/2 of the
height of the tube.
D. none of these.

A

D. none of these.

299
Q

Which of the following is the most common type of baffle
used in industrial shell and tube heat exchanger ?
A. 75% cut segmental baffle.
B. 25% cut segmental baffle.
C. Orifice baffle.
D. Disk and doughnut baffle.

A

B. 25% cut segmental baffle

300
Q

What is the minimum recommended ligament for square
pitch arrangement in case of heat exchangers ?
A. 6.5 cms
B. 6.5 mm
C. Equal to tube I.D
D. Equal to tube O.D

A

A. 6.5 cms

301
Q

Pick out the correct statement
A. Centre to centre distance between two
consecutives rivets in a row is called the
pitch.
B. A rivetted joint made in overlapping plates is
called butt joint.
C. Hole size drilled in rivetted plates is less than the
actual size of the rivet.
D. none of these.

A

A. Centre to centre distance between two
consecutives rivets in a row is called the
pitch.

302
Q

Safety valves are provided in chemical equipments to
guard against excessive
A. temperature
B.pressure/pressure fluctuation
C. turbulence
D. noise

A

B.pressure/pressure fluctuation

303
Q

The equivalent diameter for pressure drop is __________
that for heat transfer.
A. smaller than
B. greater than
C. equal to
D. not related with

A

D. not related with

304
Q

Most of the storage vessels/tanks are made cylindrical,
because of the fact that a cylinder
A. has greater structural strength.
B. is easy to fabricate.
C. both (a) and (b).
D. neither (a) nor (b).

A

C. both (a) and (b)

305
Q

The distance between the top of the slots and the liquid
surface when the static liquid is just ready to flow over the
overflow weir is called
A. downcomer liquid seal
B. static submergence
C. skirt clearance
D. none of these

A

B. static submergence

306
Q

Liquid gradient over the tray results due to the
A. resistance offered to flow of liquids by caps &
risers and the flow of gas.
B. low gas velocity.
C. large plate spacing.
D. large reflux ratio.

A

A. resistance offered to flow of liquids by caps &
risers and the flow of gas.

307
Q

The centre to centre distance between two consecutive
baffles in a shell and tube heat exchanger is called the
baffle pitch or baffle spacing, which is more than 1/5th the
I.D. of the shell. Which of the following is not a function of
the baffles ?
A. To increase the residence time of shell side fluid.
B. To provide support to the tube bundle.
C. To reduce the induced vibration in the tubes.

D. To increase the tube side heat transfer co-
efficient by inducing turbulence.

A

D. To increase the tube side heat transfer co-
efficient by inducing turbulence.

308
Q

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.
A. 45
B. 60
C. 80
D. 95

A

C. 80

309
Q

The approximate liquid depth in an agitation tank is equal
to (where, d = tank diameter)
A. 0.5 d
B. 0.75 d
C. d
D. 2 d

A

C. d

310
Q

Baffle width is normally taken as __________ times the
tank diameter.
A. 0.1-0.12
B. 0.4-0.5
C. 0.45-0.6

A

A. 0.1-0.12

311
Q

Which of the following packing materials provides for
maximum mass transfer ?
A. Lessig rings.
B. Raschig rings.
C. Cross-partition rings.
D. All give the same value.

A

C. Cross-partition rings.

312
Q

__________ of water makes it a widely used coolant in
heat exchangers.
A. Low corrosiveness
B. Low dirt factor
C. High specific heat
D. Low viscosity

A

C. High specific heat

313
Q

Fouling factor must be included in the calculation of
overall design heat transfer coefficient, when the liquid
A. containing suspended solids flows at low
velocity.
B. containing suspended solids flows at high
velocity.
C. is highly viscous.
D. is of high specific gravity.

A

A. containing suspended solids flows at low
velocity.

314
Q

Overall mass transfer co-efficient in case of absorption of
__________ in water is based on the gas film co-efficient
only, as the mass transfer process is gas film (phase)
controlling.
A. CO2
B. SO2
C. NH3
D. none of these

A

C. NH3

314
Q

Lug support is meant for supporting __________ vessels.
A. large horizontal cylindrical
B. tall but empty
C. small
D. thick walled tall

A

C. small

315
Q

Which tube arrangement in a heat exchanger would
facilitate highest heat transfer rate?
A. Triangular pitch.
B. Square pitch.
C. Diagonal square pitch.
D. Heat transfer rate is independent of tube
arrangement.

A

A. Triangular pitch.

316
Q

In case of 1.5” heat exchanger tubes, the inside flow area
__________ with decrease in BWG.
A. increases
B. decreases
C. remains same
D. none of these

A

B. decreases

317
Q

Cylindrical pressure vessels in horizontal condition is
generally supported on a __________ support.

A. lug
B. skirt
C. saddle
D. guy wire

A

C. saddle

318
Q

Welded joint efficiency in the design of chemical process
equipment is taken as
A. 0.55
B. 0.75
C. 0.85
D. 0.95

A

C. 0.85

319
Q

The thickness of segmental baffles (25 -35% cut
truncated plates usually) is generally __________ the
tube wall thickness.
A. equal to
B. twice
C. four times
D. half

A

B. twice

320
Q

The safe height (h) to diameter (d) ratio (i.e., h/d) for
liquid/petro fuel storage tank of capacity more than 45
kilolitres is less than
A. 1
B. 2
C. 3
D. 3.5

A

A. 1

321
Q

For given number of passes, pitch & tube diameter, the
maximum number of tubes that can be accommodated in a shell of tripled inside diameter will be __________
times.
A. about 9
B. considerably more than 9
C. considerably less than 9
D. about 3

A

B. considerably more than 9

322
Q

The ratio of linear stress to linear strain is termed as the
A. modulus of elasticity
B. modulus of rigidity
C. bulk modulus
D. none of these

A

A. modulus of elasticity

323
Q

__________ head is the most economical for cylindrical
vessels designed for operating at high pressure (> 15
atm.).
A. Hemispherical
B. Dished
C. Ellipsoidal
D. Conical

A

C. Ellipsoidal

324
Q

Bubble cap plate column is
A. a finite stage contactor.
B. used only for distillation, not for absorption.
C. a differential stage contactor.
D. a continuous contactor.

A

A. a finite stage contactor.

325
Q

In seive plate column, holes are drilled or punched in sizes
ranging from 2.5 to 12 mm (5 mm being widely used). The
hole pitch is normally __________ times the hole
diameter to give the required hole area.
A. 0.5 to 1.5
B. 2.5 to 4.0
C. 5 to 10
D. 10 to 15

A

B. 2.5 to 4.0

326
Q

Pick out the wrong statement.
A. Rivetting provides a permanent fastening
method.
B. The joint made by overlapping of one plate
over the other, and then rivetting the two
plates together with two rows of rivets is
called ‘double rivetted butt joint’.
C. Shank diameter of the rivets should be less than
the size of the hole drilled in the plate for rivetting.
D. The efficiency of a rivetted joint is the ratio of the
strength of the rivetted joint to the strength of the
solid plate.

A

B. The joint made by overlapping of one plate
over the other, and then rivetting the two
plates together with two rows of rivets is
called ‘double rivetted butt joint’.

327
Q

The force due to wind load acting on a tall vessel depends
upon its
A. shape.
B. outside diameter.
C. height.
D. all (a), (b) & (c).

A

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

328
Q

Bubble cap diameter used for the distillation column
having diameter ranging from 1.5 to 4.5 metres is about
__________ mm.
A. 10
B. 50
C. 100
D. 150

A

C. 100

329
Q

Power required for agitation depends upon the
A. height & properties of the liquid.
B. agitator type & speed of agitation.
C. size of agitator & the tank.
D. all (a), (b) and (c).

A

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

330
Q

Tube height in a calendria type evaporator is normally less
than __________ metres.
A. 1
B. 2
C. 3.5
D. 5.5

A

B. 2

331
Q

Pick out the wrong statement.
A. Lug supports are less expensive than other type
of supports.
B. A pipe is differentiated from a tube by the fact that
a pipe has a greater wall thickness compared to
the tube.
C. A reducer is used to change the direction of a
pipe in a straight run.
D. The method of fixing tubes to a tube sheet by
expanding is called ‘tube rolling’.

A

C. A reducer is used to change the direction of a
pipe in a straight run.

332
Q

For a 25 mm hole drilled in plates to be rivetted, the shank
diameter of the rivet should be __________ mm.
A. 25
B. 23
C. 26
D. 27

A

B. 23

333
Q

Optimum economic pipe diameter for fluid flow is
determined by the
A. viscosity of the fluid.
B. density of the fluid.
C. total cost considerations (pumping cost plus
fixed cost of the pipe).
D. none of these.

A

C. total cost considerations (pumping cost plus

334
Q

Pressure differential maintained across a continuous
rotary vacuum filter is in the range of __________ mm Hg
column.
A. 50 to 100
B. 100 to 150
C. 250 to 500
D. 600 to 700

A

C. 250 to 500

335
Q

Vertical storage vessels are never supported by
__________ support.
A. bracket
B. saddle
C. skirt
D. lug

A

B. saddle

336
Q

In a double pipe (concentric) heat exchanger, the
hydraulic radius for heat transfer (for a fluid flowing
through the annulus) would be
A. same as that for fluid flow.
B. less than that for fluid flow.
C. more than that for fluid flow.
D. D2 - D1 (D1 and D2 are I.D. of inner and outer
pipes respectively).

A

C. more than that for fluid flow.

337
Q

Elastic failure of a material occurs, when the tensile stress
equals yield strength, yield point or the elastic limit. Also,
the elastic failure occurs according to maximum strain
theory, when the maximum tensile strain equals (where,
σ = yield strength and E = modulus of elasticity)

A. E
B. σ
C. σ/E
D. E/σ

A

C. σ/E

338
Q

In a pressure vessel containing multiple openings of
various dimensions at different parts, stress concentration
at the edges of the opening is maximum which becomes
negligibly small beyond the area covered by __________
times the hole diameter.
A. two
B. five
C. ten
D. twenty

A

A. two

339
Q

What is the slope of the feed line, if the feed to a distillation
column is a saturated liquid ?
A. 0
B. ∞
C. > 1
D. < 1

A

B. ∞

340
Q

Filtration rate is affected by the
A. pressure drop across the cake & filter medium.
B. cake & filter medium resistance.
C. area of filtering surface & the viscosity of filtrate.
D. all (a), (b) and (c).

A

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

341
Q

Liquid gradient over a tray can be minimised by

A. providing a higher skirt clearance or a higher weir.
B. decreasing the number of rows of caps through
which the liquid flows or by decreasing the
velocity of liquid flow past the caps or by reducing
the distance along the tray through which the
liquid must flow.
C. using split flow, radial flow or cascade flow for
column diameter large than 4 ft.
D. all (a), (b) and (c).

A

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

342
Q

In a shell and tube heat exchanger for a given heat
transfer surface area, smaller diameter tubes are
favoured as compared to larger diameter ones ; because
the smaller diameter tubes
A. are easier to clean.
B. are less prone to fouling.
C. can be fitted into a smaller shell diameter
hence the cost of the heat exchanger would
be less.
D. none of these.

A

C. can be fitted into a smaller shell diameter
hence the cost of the heat exchanger would
be less.

343
Q

Le/D for 90° elbow (medium radius) and 90°square elbow
would be respectively around
A. 25 and 60
B. 3 and 5
C. 100 and 250
D. 250 and 600

A

A. 25 and 60

344
Q

__________ heat exchanger is also known as ‘hair pin
type’ exchanger,
A. Double pipe
B. Finned
C. Plate type
D. Regenerative

A

A. Double pipe

345
Q

What is the value of ‘q’ for saturated vapor feed to a
distillation column ?(where q = fraction of the feed stream
that is liquid.)
A. 0
B. 1
C. <0
D. > 1

A

A. 0

346
Q

In hydrostatic testing of welded pipe (for leakage, strength
etc.) the ratio of minimum hydrostatic test pressure to
internal design pressure is around
A. 0.5
B. 1.5
C. 2.5
D. 3.5

A

B. 1.5

347
Q

Frame thickness in the plate and frame filter press is
normally in the range of __________ inches.
A. 0.25 to 4
B. 0.25 to 8
C. 1 to 5
D. 1 to 12

A

B. 0.25 to 8

348
Q

Cylinderical shell thickness of rotary drier is generally
__________ mm.
A. 2-3
B. 18-22
C. 6-8
D. 12-15

A

C. 6-8

349
Q

The ratio of lateral strain to linear strain is termed as the
A. Poisson’s ratio
B. bulk modulus
C. modulus of elasticity
D. shear modulus

A

A. Poisson’s ratio

350
Q

The distance between the centre of a rivet hole to the
nearest edge of the plate is called
A. pitch
B. margin
C. back pitch
D. none of these

A

B. margin

351
Q

Mc Cable Thiele method used for finding theoretical
stages in a distillation column assumes that the
A. sensible heat differences are small, because the
temperature changes from tray to tray is small.
B. Trouton’s rule is applicable.
C. liquid/vapor loading across the column remains
constant.
D. all (a), (b) and (c).

A

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

352
Q

A minimum clearance of about __________ mm is
maintained between the distillation column wall and the
bubble cap.
A. 19
B. 38
C. 76
D. 95

A

B. 38

353
Q

Pick out the wrong statement.
A. If sufficient residence time (around 8 seconds) is
not proivided to the downcoming liquid in the
downcomer, it may entrain some vapour.
B. The liquid head in the downcomer should not be
greater than one half the plate spacing to avoid
flooding.
C. The dischare end of the downcomer must project
far enough into the tray liquid so that no gas
bubbles can enter the open end and by pass the
bubble caps.
D. none of these.

A

D. none of these.

354
Q

Pick out the wrong statement pertaining to shell and tube
heat exchanger.
A. Clearance between shell & baffles and between

tube & baffles should be minimum to avoid by-
passing of the fluid, but it should be enough to

permit the removal of tube bundle.
B. Baffles are supported independently of the tubes
by tie rods and positioned by spacers.
C. Tie rods are fixed at one end in the tube sheet by
making blind holes and the minimum number of
tie rods is 4 with at least 10 mm diameter.
D. Bracket supports are used for horizontal
shell, while saddle support is used for vertical
shell.

A

D. Bracket supports are used for horizontal
shell, while saddle support is used for vertical
shell.

355
Q

Wind load consideration in the design of a support can be
neglected, when the vessel is
A. tall (say 30 metres), but is full of liquid.
B. tall but empty.
C. short (< 2 m) and housed indoor.
D. none of these.

A

C. short (< 2 m) and housed indoor.

356
Q

The ratio of volumes of the mixed reactor to the plug flow
reactor (for identical feed composition, flow rate,
conversion, and for all positive reaction orders) is always
A. 1
B. < 1
C. >1
D. equal to the order of reaction

A

C. >1

357
Q

Steam economy is defined as the amount of evaporation
per unit amount of steam used, while the capacity is the
total evaporation obtained per hour. Use of multiple effect
in evaporation
A. increases capacity.
B. increases economy.
C. does not affect the capacity.
D. both ‘b’ & ‘c’.

A

D. both ‘b’ & ‘c’.

358
Q

Le/D for a Tee (used as elbow, entering run) would be
around
A. 5
B. 60
C. 200
D. 350

A

B. 60

359
Q

Log mean temperature difference in case of multi-pass
shell and tube heat exchanger is always
A. less than arithmetic mean value.
B. more than arithmetic mean value.
C. more than geometric mean value.
D. both(b) & (c).

A

A. less than arithmetic mean value.

360
Q

Tubes are fixed to the tube sheet (a thick circular metallic

plate) by the method of tube rolling and brazing (non-
removable) or ferrule connection (removable). Thickness

of the tube, sheet is normally __________ the outside
diameter of the tube but in no case it should be less than
22 mm (7/8”).
A. half
B. three fourth
C. equal to
D. 1.5 times

A

C. equal to

361
Q

A shell may by termed as thin if its thickness to diameter
ratio is less than 0.1. The factor which can be neglected
in the calculation of membrane stresses is
A. bending
B. deformation
C. shear
D. elongation

A

A. bending

362
Q

Scale up problem in design based on the similarity
concept takes into account __________ similarity.
A. geometrical
B. kinematic
C. dynamic
D. all (a), (b) and (c)

A

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

363
Q

__________ closure is the weakest enclosure for
cylindrical vessels.
A. Hemispherical
B. Torispherical
C. Conical or flat plate
D. Elliptical

A

C. Conical or flat plate

364
Q

Which of the following efficiencies can be greater than
100% ?
A. Overall plate efficiency.
B. Murphree plate efficiency.
C. Point efficiency.
D. None of these.

A

B. Murphree plate efficiency.