In actual operation of a bubble cap distillation tower, the __________ at the bottom of the tower is more than that at the top of the tower. Molal flow rate of vapour All of these Pressure and temperature Vapour molecular weight TRUE ANSWER : ? YOUR ANSWER : ?
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. 100-150 1000-1500 20-40 43835 TRUE ANSWER : ? YOUR ANSWER : ?
Hoop (circumferential) stress induced in a thin walled 'Horton Sphere' used for the storage of liquid ammonia under pressure is pD/6t pD/2t pD/4t pD/3t TRUE ANSWER : ? YOUR ANSWER : ?
__________ head is the most economical for cylindrical vessels designed for operating at high pressure (> 15 atm.). Ellipsoidal Conical Hemispherical Dished TRUE ANSWER : ? YOUR ANSWER : ?
In hydrostatic testing of welded pipe (for leakage, strength etc.) the ratio of minimum hydrostatic test pressure to internal design pressure is around 2.5 0.5 3.5 1.5 TRUE ANSWER : ? YOUR ANSWER : ?
The raio, (properller agitator dia/tank dia) is normally taken as 0.5-0.65 0.60-0.90 0.75-0.85 0.15-030 TRUE ANSWER : ? YOUR ANSWER : ?
Pick out the wrong statement pertaining to the design of the distillation column. The purpose of the slot is to disperse the gas into the liquid in the form of small bubbles If sufficient slot area is not provided, the gas may pass through the skirt clearance Generally, a skirt clerance of 0.5" to 1.5' is recommended to prevent plugging of the slots by residue build up None of these TRUE ANSWER : ? YOUR ANSWER : ?
In a distillation column, minimum clearance to be maintained betweeen the overflow weir and the last row of the bubble caps is __________ cms. 20 7.5 2.5 15 TRUE ANSWER : ? YOUR ANSWER : ?
Tube side pressure drop in a 1-2 heat exchanger (for turbulent flow of fluids through the tubes) is about __________ times, that in a 1-1 heat exchanger having the same size & number of tubes and operated at the same liquid flow rate. 1/2 2 4 8 TRUE ANSWER : ? YOUR ANSWER : ?
With increase in temperature drop (in a shell and tube heat exchanger), the LMTD correction factor, FT Remains constant Increases linearly Decreases very rapidly Increases very rapidly TRUE ANSWER : ? YOUR ANSWER : ?