Indiabix - Equipment and Plant Design Flashcards
Fresh water carrying pipelines in chemical industries are
coloured with __________ color.
A. sea green
B. brown
C. yellow
D. red
A. sea green
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. Rimmed Still
The ratio of shear stress to shear strain is called
A. bulk modulus
B. shear modulus
C. modulus of rigidity
D. modulus of elasticity
B. shear modulus
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. height is 75% of the I.D. of the shell.
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
C. 45
Le/D for fully open globe value may be around
A. 10
B. 25
C. 75
D. 300
D. 300
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).
D. all (a), (b) and (c).
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.
C. Maintenance cost for valve and seive trays are comparatively more than bubble cap tray due to their relatively complicated construction features.
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. increases
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
B. 2.5 to 5
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
B. 5-11
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
C. elastic limit
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.
C. shortest centre to centre distance between
adjacent tubes.
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.
B. Reflux is not a saturated liquid.
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).
D. all (a), (b) and (c).
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. 10
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
D. 8
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
D. (1.2)5/3
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)
C. both (a) & (b)
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. At the inner surface.
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
C. 0.80
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
D. none of these
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).
C. permits the use of more tubes in a given shell
diameter
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. thick walled vertical
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
D. none of these
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
B. inside diameter
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
C. 7500
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).
D. both (b) and (c).
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
B. 20
In chemical process equipments, the conical bottom
heads used, usually has an apex angle of
A. 20°
B. 40°
C. 60°
D. 80°
C. 60°
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
C. 75
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
C. less
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.
B. ultimate stress to working stress.
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
B. 20-40
__________ tray arrangement is recommended for
distillation column having diameter upto 4 ft.
A. Radial flow
B. Cross flow
C. Split flow
D. Cascade
B. Cross flow
What is the value of ‘q’ for saturated liquid feed to a
distillation column ?
A. 0
B. <1
C. 1
D. >1
C. 1
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).
D. all (a), (b) and (c).
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.
C. facilitate handling of large flow rate of liquid.
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. 50-150
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
D. Ellipsoidal
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. Di, opt = 3 Q0.36 μ 0.18
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.
B. Packed towers are generally preferred over
plate towers, if the liquids have a foaming
tendency.
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
B. less
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. It is used for high viscosity liquor having large
rate of scaling.
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.
D. none of these.
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. 0.1 to 2
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.
B. prevention of fluid leakage around moving
parts.
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
C. Δp = G2
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.
D. dished bottom vessel has very high power
consumption.
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. very large diameter pipes.
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.
D. all a, b & c.
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. Safety valves are provided in heat exchangers
for removal of non-conden-sables.
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
B. decreases
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. central dished section and corner torus
section.
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).
C. both (a) & (b).
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.
C. Allowable vapour velocity.
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’.
D. all ‘a’, ‘b’ & ‘c’.
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.
B. smaller reactor should come first.
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’
C. both ‘a’ & ‘b’
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. Sorel-Lewis method.
Saddle supports are used for supporting __________
vessels.
A. horizontal cylindrical
B. tall vertical
C. thick walled vertical
D. thick spherical
A. horizontal cylindrical
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
B. 15 to 30
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
B. 5-8
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.
C. total cost consideration (fixed cost of the
column plus the cooling water & steam cost).
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. (BTU/hr.ft2 . °F)-1
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. 0.2 D
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. 0.5” -1.25”.
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.
C. back up condensate and cause water hammer
in steam line.
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
B. -q/(1-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
B. 20 to 100
__________ strain is measured using a ‘strain rosetter’.
A. Volumetric
B. Shear
C. Linear
D. none of these
C. Linear
Thin spherical shells subjected to internal pressure,
develop __________ stresses.
A. radial
B.circumferential
C. both (a) & (b)
D. neither (a) nor (b)
A. radial
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. fixed charges initially
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
B. ∞
Vertical vessels are not supported by
A. brackets
B. skirts
C. columns
D. saddles
D. saddles
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. increase
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. withstand higher pressure for a given metallic
shell thickness.
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.
B. allow for thermal expansion and facilitate
installation.
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.
B. ideal trays required to the number of real trays
required.
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.
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.
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
C. 30
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. 0.1 to 0.25
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
B. chain
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.
D. The value of crushing load is more than that
of buckling load for long columns.
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)
D. all (a), (b) and (c)
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.
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.
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. pd/2t
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).
D. both (b) and (c).
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.
B. multipass shell and tube heat exchanger.
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.
B. cases where temperature difference between
the shell and the tubes is more (>50°C).
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.
B. 6” dia cap with 4” dia riser.
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. nozzle or rim
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).
D. all (a), (b) and (c).
In a distillation column, the minimum residence time for
liquid in the downspout is about __________ seconds.
A. 1
B. 8
C. 80
D. 180
B. 8
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)
C. more
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).
D. All (a), (b) and (c).
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
B. 1.25 to 3.125
Rivets are generally specified by the
A. head diameter
B. shank diameter
C. overall length
D. none of these
B. shank diameter
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
B. 4 to 10
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
B. 19
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
B. 600
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).
D. both(b) & (c)
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.
D. none of these.
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
B. 1
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 vapor phase reactor.
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.
B. density of the gas and inversely as viscosity
of the gas.
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)
C. all multipass
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).
D. all (a), (b) and (c).
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. decreases upwards
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
B. 0.8
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
B. damaging
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
C. 3 to 12.5
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
B. 15-20
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. d1/(d1+d2)
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. liquid gradient on the tray.
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
B. 5
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.
B. D/5 or minimum 2” to 5D.
Brass valves are usually made for pipe sizes __________
inches.
A. ≤1
B. ≤2
C. >2.5
D. >3.5
B. ≤2
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
C. remains same
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. results in higher shell side pressure drop
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.
D. Higher pressure fluid stream should be routed
through the shell side.
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).
D. all (a); (b) and (c).
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
B. (1/n)th
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.
C. Flat head covers are most suitable for larger
vessels operating at very high pressure.
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.
D. Liquor flows inside the tube, while the steam
is outside submerging the tube.
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).
D. all (a), (b) and (c).
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.
B. high latent heat.
__________ shapedroof is the most commonly used roof
for cylinderical storage tanks.
A. Conical
B. Flat
C. Dome
D. Umbrella
A. Conical
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 .
D. Horton sphere is used for the storage of liquid
at sub-zero temperature at very high pressure
upto 200 kg/cm2
Value of Peclet number = ∞, is the representative of
A. laminar flow.
B. complete back mixing,
C. plug flow.
D. eddy diffusivity = 0.
C. plug flow.
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).
D. both (b) and (c).
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
B. 1.25-1.50 times
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. 1.3 to 2
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).
D. all (a), (b) and (c).
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
B. faulty operating procedures.
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
D. bubble cap
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
C. (ph - dt)/ph
__________ 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. Permissible slot velocity
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.
D. Flash distillation, differential distillation &
steam distillation are all continuous
distillation processes
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
C. 650
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
C. Copper
Normal screwed fittings are used for pipes upto a
diameter of __________ inches.
A. 1.5
B. 3
C. 5
D. 7
B. 3
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. not less than one-fourth of the tube diameter
or 3/16”.
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.
B. upper limit of the vapour velocity.
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. decreases.
Maximum acceptable total liquid gradient over a tray is
about __________ mm.
A. 5.5
B. 12.5
C. 30.5
D. 45.5
B. 12.5