Process Equipment and Plant Design Flashcards
Holes of a sieve tray are arranged in triangular pitch of __________ times the hole diameter.
2.5 to 5
The stress developed in a material without any permanent set is called the
elastic limit
A rivetted joint does not fail by __________ of rivets.
none of these
In a multipass shell and tube heat exchanger, the shell side cross flow area does not depend upon
none of these
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
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
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.
none of these
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.
In packed towers provided with saddle packing, liquid redistributors are positioned at every __________ times column diameter or 6 metres whichever is less.
5-8
Minimum recommended baffle spacing in a shell and tube heat exchanger is about (where, D = shell diameter )
0.2D
Speed of industrial paddle agitator ranges from __________ rpm.
20 to 100
The slope of operating line in the rectifying section of a distillation column is unity, if the reflux ratio is
infinity
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
Floating head heat exchangers are used for the
cases where temperature difference between the shell and the tubes is more (>50°C).