Process Equipment and Plant Design Flashcards
Fresh water carrying pipelines in chemical industries are coloured with __________ color.
sea green
Which of the following material is seldom used for pressure vessel construction ?
Rimmed steel
The ratio of shear stress to shear strain is called
shear modulus
25 per cent cut segmental baffle means that the baffle
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.
45
Le/D for fully open globe value may be around
300
Pick out the wrong statement pertaining to the use of valve tray, seive tray and bubble cap trays in continuous distillation column.
Maintenance cost for valve and sieve 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
increases
Holes of a sieve tray are arranged in triangular pitch of __________ times the hole diameter.
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.
5-11
The stress developed in a material without any permanent set is called the
elastic limit
In a shell and tube heat exchanger, the ‘tube pitch’ is defined as the
shortest center to center 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 ?
Reflux is not a saturated liquid.
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)
η = 17 - 61.1 log μ
In case of bubble cap distillation column of diameter greater than 1.2 metres, the cap diameter is roughly about __________ cms.
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.
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
(1.2)^5/3
Where does the maximum tensile strength occur in a thick cylindrical vessel subjected to internal pressure ?
At the inner surface.
It is not desirable to design a heat exchanger for LMTD correction factor, FT, of less than
0.80
Triangular pitch tube layout as compared to square pitch in a shell and tube heat exchanger
permits the use of more tubes in a given shell diameter.
Bracket supports are the most suitable for supporting __________ vessels.
thick walled vertical
Two iron pipes of the same nominal diameter but different schedule numbers will have the same
inside diameter
Steam side heat transfer co-efficient for design consideration under ordinary condition can be assumed to be about __________ kcal/hr.m2.°C.
7500
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.
20
In chemical process equipments, the conical bottom heads used, usually has an apex angle of
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.
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
less
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.
20-40
Correct use of ‘factor of safety’ is very important in equipment design. It is defined as the ratio of the
ultimate stress to working stress.
What is the value of ‘q’ for saturated liquid feed to a distillation column ?
1
__________ tray arrangement is recommended for distillation column having diameter up to 4 ft.
Cross flow
The main purpose of providing stepping on the trays is to
facilitate handling of large flow rate of liquid.
The operating pressure drop range in a bag filter is about __________ mm water gauge.
50-150
The ends of a cylindrical vessel can be closed by a head, which can be one of the four shapes. For the same thickness, choose the one which can withstand the highest pressure.
Ellipsoidal
For laminar flow (NRe < 2100) in steel pipe, the optimum inside pipe diameter is given by
Di, opt = 3 Q^0.36 ρ^0.18
Pick out the correct statement.
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
LESS
Pick out the wrong statement pertaining to the design of a basket type evaporator.
It is used for high viscosity liquor having large rate of scaling.
Speed of the drum of the rotary vacuum filter normally ranges from __________ rpm.
0.1 to 2
A stuffing box is used for
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
Δp = G2
Pick out the wrong statement.
dished bottom vessel has very high power consumption.
Pick out the wrong statement.
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
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
central dished section and corner torus section.
Which of the following is used to set the diameter of the distillation column ?
Allowable vapor velocity.
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
smaller reactor should come first.
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?
Sorel-Lewis method.
Saddle supports are used for supporting __________ vessels.
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.
15 to 30
In packed towers provided with saddle packing, liquid redistributors are positioned at every __________ times column diameter or 6 meters whichever is less.
5-8
Optimum reflux ratio in a continuous distillation column is determined by the
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
(BTU/hr.ft2 . °F)-1
Minimum recommended baffle spacing in a shell and tube heat exchanger is about (where, D = shell diameter )
0.2 D
The maximum liquid gradient over a tray must not exceed
0.5” -1.25”.
An under designed steam trap will
back up condensate and cause water hammer in steam line.
Speed of industrial paddle agitator ranges from __________ rpm.
20-100
__________ strain is measured using a ‘strain rosetter’.
Linear
With increase in the reflux ratio for a fixed production from a continuous binary distillation column, the __________ decreases.
fixed charges initially
The slope of operating line in the rectifying section of a distillation column is unity, if the reflux ratio is
∞
Vertical vessels are not supported by
saddles
Spherical shaped pressure vessel is considered to be the most ideal, because it can
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
allow for thermal expansion and facilitate installation.
Pick out the wrong statement about the design of a sieve plate column.
Minimum recommended down comer 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.
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.
0.1 to 0.25
In a __________ rivetted joint, the rivets in the various rows are opposite to each other.
chain
Pick out the wrong statement:
The value of crushing load is more than that of buckling load for long colmns.
Pick out the wrong statement pertaining to the comparative evaluation of performance of the packed tower and the plate tower.
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
pd/2t
LMTD correction factor is used in heat exchanger design for
multipass shell and tube heat exchanger.
Floating head heat exchangers are used for the
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
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.
nozzle or rim
In a distillation column, the minimum residence time for liquid in the downspout is about __________ seconds.
8
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.
1.25 to 3.125
Rivets are generally specified by the
shank diameter
Length to diameter ratio of most rotary driers is in the range of
4 to 10
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
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
600
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
1
Which of the following types of reactors is the safest from operation point of view ?
A vapor phase reactor.
The LMTD correction factor (FT) is applied in __________ heat exchangers.
all multipass
For a cylindrical shell, (subject to the thickness of uppermost course being more than the minimum for diameter of the tank in question), the thickness of the courses of shell
decreases upwards.
In the design of a paddle agitator, the ratio paddle dia / tank dia is normally taken as
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.
Damaging
Hole diameter of the sieve trays in the distillation column ranges from __________ mm.
3 to 12.5
Factor of safety (i.e., overdesign factor) in heat transfer equipment is about __________ percent more than the actual/theoretical design factor.
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
d1 / d1 + d2
In actual operation of distillation column, the vapour is not distributed uniformly among the bubble caps, primarily because of the
liquid gradient on the tray
The minimum shell thickness for tank ≤ 15 metres diameter is limited to __________ mm, for reasons of elastic stability.
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
D/5 or minimum 2” to 5D.
Brass valves are usually made for pipe sizes __________ inches.
≤ 2
In a shell and tube heat exchanger, triangular pitch arrangement as compared to square pitch arrangement
results in higher shell side pressure drop.
Pick out the wrong statement about routing of fluids in a shell and tube heat exchanger.
Higher pressure fluid stream should be routed through the shell side.
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.
(1/n)th
Pick out the wrong statement
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.
Liquor flows inside the tube, while the steam is outside submerging the tube.
Steam is preferred to be used as a heating medium in heat exchangers, because of its
high latent heat.
__________ shaped roof is the most commonly used roof for cylindrical storage tanks.
Conical
Pick out the wrong statement pertaining to ‘Horton sphere’ used for the storage of liquid ammonia.
Horton sphere is used for the storage of liquid at sub-zero temperature at very high pressure up to 200 kg/cm2 .
Value of Peclet number = ∞, is the representative of
plug flow.
In most of the shell and tube heat exchangers, the tube pitch is generally __________ the tube diameter.
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.
1.3 to 2
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
(ph - dt)/ph
Accidents in chemical plants are mostly due to
faulty operating procedures.
For identical operating conditions, the pressure drop over __________ tray is the highest out of the following.
bubble cap
Pick out the wrong statement about distillation operation
Flash distillation, differential distillation & steam distillation are all continuous distillation processes.
Normal screwed fittings are used for pipes upto a diameter of __________ inches.
3
Which of the following is the best tube material from thermal conductivity point of view alone?
Copper
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).
650
In a shell and tube heat exchanger, the clearance of the tube is generally
not less than one-fourth of the tube diameter or 3/16”.
High pressure fluid in a shell and tube heat exchanger should preferably be routed through the
tubes to avoid the expansion of high pressure shell construction.
In case of a ‘thin’ pressure vessel, the ratio of its diameter to wall thickness is
> 10
Bubble cap tray is the most commonly used tray in large distillation column, because
of its flexibility and nearly constant efficiency under varying conditions of operation.
Diameter of the sieve tray column is determined by the
upper limit of the vapour velocity.
Maximum acceptable total liquid gradient over a tray is about __________ mm.
12.5
In common bubble cap distillation column design practice, riser area is approximately equal to (where, Aa = Annular passage area, and Sa = Slot area)
Aa = Sa
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
hG = 1.004G0.37