In case of a shell and tube heat exchanger, the effect of L/D on inside film heat transfer co-efficient (hi) vanishes after a Reynold number of 10000 3000 5000 1000 TRUE ANSWER : ? YOUR ANSWER : ?
Liquid gradient over a tray can be minimised by Providing a higher skirt clearance or a higher weir All of these Decreasing the number of rows of caps through which the liquid flows or by decreasing the velocity of liquid flow past the caps or by reducing the distance along the tray through which the liquid must Using split flow, radial flow or cascade flow for column diameter large than 4 ft TRUE ANSWER : ? YOUR ANSWER : ?
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. 44055 0.3 to 0.8 1.25 to 3.125 3.5 to 7.0 TRUE ANSWER : ? YOUR ANSWER : ?
Thickness of the frame of a plate and frame filter as compared to that of plates is More Less Either A or B Same TRUE ANSWER : ? YOUR ANSWER : ?
The stress developed in a material without any permanent set is called the Yield stress Elastic limit Ultimate stress Breaking stress TRUE ANSWER : ? YOUR ANSWER : ?
Which of the following types of reactors is the safest from operation point of view? A liquid phase catalytic reactor A vapor phase reactor A liquid phase reactor Pot type reactor TRUE ANSWER : ? YOUR ANSWER : ?
Bracket supports are the most suitable for supporting __________ vessels. Horizontal Thin shperical (e.g. Horton sphere) Thick walled vertical None of these TRUE ANSWER : ? YOUR ANSWER : ?
In the downcomer of a distillation column, the minimum recommended residence time is about __________ seconds. 2.5 5 12.5 17.5 TRUE ANSWER : ? YOUR ANSWER : ?
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. 28 16 38 19 TRUE ANSWER : ? YOUR ANSWER : ?
In a shell and tube heat exchanger for a given heat transfer surface area, smaller diameter tubes are favoured as compared to larger diameter ones ; because the smaller diameter tubes Are easier to clean None of these Are less prone to fouling Can be fitted into a smaller shell diameter hence the cost of the heat exchanger would be less TRUE ANSWER : ? YOUR ANSWER : ?