Process Equipment Design Flashcards
Section 1-8
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
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
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
4
Q
- 25 per cent cut segmental baffle means that the baffle
A
a. height is 75% of the I.D. of the shell.
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
6
Q
- Le/D for fully open globe value may be around
a. 10
b. 25
c. 75
d. 300
A
d. 300
7
Q
- Lug 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).
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.
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
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
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
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
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 center to center distance between adjacent tubes.
d. none of these.
A
c. shortest center to center distance between adjacent tubes.
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.
15
Q
- Overall distillation column efficiency for most of the refinery columns can be given by (for μ = 0.07 - 1.4 cp and relative volatility < 4) (where η = overall column efficiency, % μ = molal average viscosity of feed at average column temperature and pressure, cp Δp = pressure drop per tray, psi)
a. η = 17 - 61.1 log μ
b. η = 24.6 ( delta rho/ μ)
c. η = 1.66 - 0.25 log μ
d. η = 0.25 log μ - 1.67
A
a. η = 17 - 61.1 log μ
16
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).
17
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
18
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
19
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
20
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)
21
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.
22
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. 0.5
A
c. 0.80
23
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
24
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.
25
Q
- Bracket supports are the most suitable for supporting vessels.
a. thick walled vertical
b. horizontal
c. thin spherical (e.g. Horton sphere)
d. none of these
A
a. thick walled vertical
26
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
27
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
a. inside diameter
28
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
29
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).
30
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
31
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°
32
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
33
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
34
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.
35
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
36
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
37
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
38
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).
39
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.
40
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
41
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
42
Q
- For laminar flow (NRe < 2100) in steel pipe, the optimum inside pipe diameter is given by
a. Di, opt = 3 Q0.36 ρ0.18
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 ρ0.18
43
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.
44
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
45
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 down-take.
d. Down-take 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.
46
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.
47
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
48
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.
49
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 = G^0.5
c. Δp = G^2
d. Δp= 1/ G^0.6
A
c. Δp = G^2
50
Q
- Pick out the wrong statement. 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.
51
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.
52
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.
53
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.
54
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
55
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.
56
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).
57
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.
58
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’.
59
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.
60
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’
61
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.
62
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
63
Q
- The diameter of a propeller agitator used in agitation tank ranges from ______ percent of the tank diameter and its peripheral speed is normally 300 to 500 meters/minute.
a. 5 to 10
b. 15 to 30
c. 40 to 50
d. 55 to 75
A
b. 15 to 30
64
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
65
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).
66
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
67
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
68
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”.
69
Q
- An under-designed 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.
70
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)
71
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
72
Q
- ______strain is measured using a ‘strain rosetter’
a. Volumetric
b. Shear
c. Linear
d. none of these
A
c. Linear
73
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
74
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
75
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. ∞
76
Q
- Vertical vessels are not supported by
a. brackets
b. skirts
c. columns
d. saddles
A
d. saddles
77
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
78
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.
79
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.
80
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.
81
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.
82
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
83
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
84
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
85
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.
86
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)
87
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.
88
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
89
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).
90
Q
- LMTD correction factor is used in heat exchanger design for
a. double pipe heat exchanger.
b. multi-pass shell and tube heat exchanger.
c. fouling fluids.
d. counter flow of hot and cold fluids.
A
b. multi-pass shell and tube heat
91
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).
92
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.
93
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
94
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).
95
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
96
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
97
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)
98
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
99
Q
- Rivets are generally specified by the
a. head diameter
b. shank diameter
c. overall length
d. none of these
A
b. shank diameter
100
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
101
Q
- Tube wall thickness depends on the cor-rosiveness of the fluids and their operating pressure & temperature and is specified by Birmingham wire gauge (B.W.G)-a number which varies from 8 to 18 with the numbers 14 and 16 being more commonly used. Outside diameter of tubes varies from about 15 to 50 mm; however a tube of less than mm outside diameter is generally not recommended for fouling fluids.
a. 16
b. 19
c. 28
d. 38
A
b. 19
102
Q
- Angled baffles are preferred in the agitation tank to control the swirling action; if the viscosity of the liquid to be mixed is about 200 poise. However, the baffle may be completely eliminated for mixing liquids having viscoisty above poise.
a. 300
b. 600
c. 1000
d. 1500
A
b. 600
103
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).
104
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.
105
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
106
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.
107
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.
108
Q
- The LMTD correction factor (FT) is applied in _____ heat exchangers.
a. co-current
b. double pipe
c. all multi-pass
d. all (involving liquid/liquid heat transfer)
A
c. all multi-pass
109
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).
110
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.
111
Q
- In the design of a paddle agitator, the ratio PADDLE DIA/ TANK DIA is normally taken as:
a. 0.1
b. 0.8
c. 0.25
d. 0.5
A
b. 0.8
112
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
113
Q
- Hole diameter of the seive trays in the distillation column ranges from mm.
a. l to 3
b. 4 to 8
c. 3 to 12.5
d. 12.5 to 18.5
A
c. 3 to 12.5
114
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
115
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)
116
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 down-comer liquid seal.
A
a. liquid gradient on the tray.
117
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
118
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
c. D/5 or minimum 2” to D.
119
Q
- Brass valves are usually made for pipe sizes inches.
a. ≤1
b. ≤2
c. >2.5
d. >3.5
A
b. ≤2
120
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
121
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.
122
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.
123
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).
124
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
125
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 center results in reduced local stresses.
A
c. Flat head covers are most suitable for larger vessels operating at very high pressure.
126
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.
127
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).
128
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.
129
Q
- _____shaped-roof is the most commonly used roof for cylindrical storage tanks.
a. Conical
b. Flat
c. Dome
d. Umbrella
A
a. Conical
130
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 .
131
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.
132
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).
133
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
134
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
135
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)
136
Q
- Accidents in chemical plants are mostly due to
a. inadequate equipment design.
b. faulty operating procedures.
c. improper layout of the equipments.
d. failure of equipments.
A
b. faulty operating procedures.
137
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
138
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
39. is the determining
A
c. (ph - dt)/ph
139
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
140
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.
141
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
142
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
143
Q
- Normal screwed fittings are used for pipes up to a diameter of inches.
a. 1.5
b. 3
c. 5
d. 7
A
b. 3
144
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”.
145
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.
146
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.
147
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
148
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
149
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.
150
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.
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.
151
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
152
Q
- Heat transfer co-efficient, hG(Kcal/hr.m2 .°C) and mass velocity of air, G (kg/hr.m2 ) for air flow parallel to the surface in case of constant drying rate in batch drying is related as hG = 0.0176G0.8. But when the flow of air perpendicular to the surface is encountered, this equation changes to
a. hG = 1.004G^0.37
b. 1.004G^0.8
c. hG = 0.0176G^0.37
d. 0.0176G^1.37
A
a. hG = 1.004G^0.37
153
Q
- In the agitators, the power required will be changed with the increase of diameter of agitator (D) as
a. D^2
b. D^5
c. D
d. D^9
A
b. D^5
154
Q
- Apex angle of conical heads used in the bottom heads of chemical process equipments is usually
a. 30°
b. 45°
c. 60°
d. 75°
A
c. 60°
155
Q
- Pressure drop due to pipe fittings can be estimated by the equation, (chuchuchu) , where, Le = equivalent length of straight pipeline which will incur the same frictional loss as the fitting and D = diameter of the fitting. The value of LE/D (dimensionless) for 45° elbow and 180° close return bends would be respectively around
a. 5 and 10
b. 45 and 75
c. 180 and 300
d. 300 and 500
A
b. 45 and 75
156
Q
- A pressure vessel is said to be made of ‘thick’ shell, if the ratio of its diameter to wall thickness is
a. 10
b. 10
c. 20
d. 20
A
10
palakasan ng angel
157
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)
158
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
159
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
160
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.
161
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
162
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).
163
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
164
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.
165
Q
- In a rotary drier, the average retention time of solid is(where Z = length of the drier, metres ρ = apparent solid density, kg/m3 L = flow rate of dry solids, kg/see. m2 drier cross-section H = hold up of solid.)
A
(ZHp)/L
166
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).
167
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
168
Q
- Nominal size of a pipe is an indication of its diameter.
a. inner
b. outer
c. approximate
d. none of these
A
c. approximate
169
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).
170
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
171
Q
- In a double pipe concentric heat exchanger, the equivalent diameter of annulus for heat transfer would be (where, D1 and D2 are I.D. of inner and outer pipes)
A
(D2^2-D1^2)/D1^2
172
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
173
Q
- _______ shaped roof is most commonly used for cylindrical tanks.
a. Cone
b. Dome
c. Umbrella
d. Flat
A
a. Cone
174
Q
- In a thin cylindrical shell, the hoop stress is stress.
a. radial
b. circumferential tensile
c. compressive
d. longitudinal
A
b. circumferential tensile
175
Q
- Commercial packed scrubbers are normally designed for a pressure drop range of mm water column per metre of packed height.
a. 4-8
b. 17-34
c. 52-68
d. 88-105
A
b. 17-34
176
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)
177
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)
178
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
179
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
180
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).
181
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).
182
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)
183
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
184
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
185
Q
- __________dished head is the strongest of all.
a. Hemispherical
b. Elliptical
c. Torispherical
d. none of these
A
a. Hemispherical
186
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 column by bolts, rivets or welding.
187
Q
- “A claming section” before the liquid flows into the downcomer is privided 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.
188
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
189
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)
190
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.
191
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
192
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
193
Q
- liquor is best handled in a long tube vertical evaporator.
a. Foamy
b. Scaling
c. Viscous
d. Salting
A
a. Foamy
194
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
195
Q
- Hold up of material in a 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
196
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
197
Q
- The testing pressure of storage tanks and pressure vessels designed as per Indian standard codes should be about ________times the design pressure.
a. 1.5 to 2
b. 3 to 4
c. 4 to 5
d. >5
A
a. 1.5 to 2
198
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)
199
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
200
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.
201
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
202
Q
- At equal mass velocities, the values of film co-efficients for gases as compared to that for liquids are generally.
a. higher
b. lower
c. same
d. unpredictable
A
b. lower
203
Q
A
