Pick out the wrong statement pertaining to the use of valve tray, seive tray and bubble cap trays in continuous distillation column. Maintenance cost for valve and seive trays are comparatively more than bubble cap tray due to their relatively complicated construction features Murphree efficiency of all the three trays are nearly equal, however the peak efficiency is generally higher for seive and valve trays than the bubble cap Bubble cap trays though most expensive are the best in situations, where low vapour rates is to be handled and a positive liquid seal is essential at all flow rates Valve trays have the highest turn down ratio (i.e. the ratio of the highest to the lowest vapour flow rates) and thus provides the maximum flexible operating range TRUE ANSWER : ? YOUR ANSWER : ?
Needle valves are generally not used for Smaller sizes of pipe High pressure throttling service Very large diameter pipes Very accurate flow control TRUE ANSWER : ? YOUR ANSWER : ?
With increase in temperature drop (in a shell and tube heat exchanger), the LMTD correction factor, FT Increases very rapidly Decreases very rapidly Remains constant Increases linearly TRUE ANSWER : ? YOUR ANSWER : ?
Minimum tube pitch recommended for shell and tube heat exchangers is about __________ times the outside diameter of the tube. 3.5 1.75 2.5 1.25 TRUE ANSWER : ? YOUR ANSWER : ?
Holes of a sieve tray are arranged in triangular pitch of __________ times the hole diameter. 10 to 15 5 to 10 1.5 to 2 2.5 to 5 TRUE ANSWER : ? YOUR ANSWER : ?
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/2 or minimum 2" to 5D D/5 or minimum 2" to D None of these D/5 or minimum 2" to 5D TRUE ANSWER : ? YOUR ANSWER : ?
The average velocity in the tubes of a 1-4 heat exchanger is __________ times that in 1-1 heat exchanger having the same size & number of tubes and operated at same liquid flow rate. 43834 43832 4 2 TRUE ANSWER : ? YOUR ANSWER : ?
Larger depth of liquid on the trays of a distillation column Results in higher pressure drop per tray Neither A nor B Leads to high tray efficiency Both A & B TRUE ANSWER : ? YOUR ANSWER : ?
__________ closure is the weakest enclosure for cylindrical vessels. Torispherical Conical or flat plate Hemispherical Elliptical TRUE ANSWER : ? YOUR ANSWER : ?
Pressure drop due to pipe fittings can be estimated by the equation, ΔP/p = 4f.Le/D.V2/2gc, 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 Le/D (dimensionless) for 45° elbow and 180° close return bends would be respectively around 5 and 10 45 and 75 300 and 500 180 and 300 TRUE ANSWER : ? YOUR ANSWER : ?