Process Equipment and Plant Design (Set 2) Flashcards
Concepts and heuristics necessary for design of equipment, processes, and process systems.
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
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.
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. and is directly proportional to the radius of the dust particle path.
d. none of these.
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).
expansion joint, changes in its direction, change in the shape of pipeline
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.
≤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
remains same
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.
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.
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.
(1/n)th