S3 Flashcards
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 viscoisty above ________ poise.
600
The dust collection efficiency of a cyclone separator
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
1
Which of the following types of reactors is the safest from operation point of view?
A vapor phase reactor.
In a bag filter, the pressure drop increases directly as the
density of the gas and inversely as viscosity of the gas.
The LMTD correction factor (FT) is applied in ________ heat exchangers.
all multipass
Movement of pipeline caused by thermal expansion is taken care by providing
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
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 seive trays in the distillation column ranges from ________ mm.
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.
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.
≤1
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
remains same