Section 4 Flashcards
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
1.2 Aa = 1.2 Sa
Sa = 1.5 Aa
Aa = 1.5 Sa
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 = 1.004 G^0.37
1.004 G^0.8
hG = 0.0176 G^0.37
0.0176 G^1.37
hG = 1.004 G^0.37
In the agitators, the power required will be changed with the increase of diameter of agitator (D) as
D^2
D^5
D
D^9
D^5
Apex angle of conical heads used in the bottom heads of chemical process equipments is usually
30°
45°
60°
75
60°
Pressure drop due to pipe fittings can be estimated by the equation,
, 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 (dimensionless) for 45° elbow and 180° close return bends would be respectively around
5 and 10
45 and 75
180 and 300
300 and 500
45 and 75
A pressure vessel is said to be made of ‘thick’ shell, if the ratio of its diameter to wall thickness is
10
10
20
20
10
Rate of filtrate delivery is inversely proportional to the
filtering area & the pressure difference driving force.
viscosity of filtrate.
cake & filter medium resistance.
both (a) and (b)
both (a) and (b)
Tube side heat transfer co-efficient for turbulent flow of liquid through tubes is proportional to
G^0.2
G^0.5
G^0.8
G^1.5
G^0.8
Circumferential (hoop) stress in a thin cylindrical vessel under internal pressure is __________ the longitudinal stress.
half
equal to
twice
eight times
twice
The dust collection efficiency of electrostatic precipitator increases with increase in the
gas flow rate.
electrode area.
both (a) & (b).
neither (a) nor (b).
electrode area.
For storing hazardous chemicals in large storage tanks, the minimum safe distance between the two tanks should range between __________ times the tank diameter.
1 to 1.5
2.5 to 3.5
4 to 5
6 to 8
1 to 1.5
Which of the following factors determine the amount of entrainment in a distillation column ?
Plate spacing.
Depth of liquid above the bubble cap slots.
Vapour velocity in the volume between the plates.
All (a), (b) and (c).
All (a), (b) and (c).
The absorption factor is defined as (where, S1 = slope of the equilibrium curve, S2 = slope of the operating line)
S1/S2
S1.S2
S2/S1
1/S1.S2
S1/S2
In shell and tube heat exchangers, straight tie rods are used to
hold baffle in space.
fix the tubes in position.
account for thermal strain.
none of these.
hold baffle in space.
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.)
(Z H ρ ) / L
In case of design of a shell and tube heat exchanger,
minimum cleaning lane of 6.5 mm is provided, when tubes are on a square pitch.
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.
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.
all (a), (b) & (c).
all (a), (b) & (c).
In a cylinderical vessel subjected to internal pressure, the longitudinal stress σL and the circumferential stress, σn are related by
σh = 2 σL
σh = σL
σh = σL/2
no relation exists
σh = 2 σL
Nominal size of a pipe is an indication of its __________ diameter.
inner
outer
approximate
none of these
approximate
Excessive liquid gradient on a tray may result in the
maldistribution of gas.
back trapping.
gas blowing beneath cap skit.
all (a), (b) and (c).
all (a), (b) and (c).
The ratio of tube length to shell diameter in case of liquid shell and tube heat exchanger ranges from
2 to 3
3 to 5
4 to 8
6 to 12
4 to 8