chemical engineering Mcqs
3702. Liquid gradient over the tray results due to the___________________?
comments icon0

A. Large plate spacing

B. Resistance offered to flow of liquids by caps & risers and the flow of gas

C. Large reflux ratio

D. Low gas velocity

3703. 1.2 to 3.8 cms is the value of the ______________________?
comments icon0

A. Skirt clearance for bubble caps

B. All A., B. and C.

C. Static submergence in case of a bubble cap tray for column operating under pressure (? 1 atm)

D. Downcomer liquid seal in case of a balanced tray design

3704. Generally, as the length of the liquid path on a tray is increased beyond 5 ft, the overall column efficiency___________________?
comments icon0

A. May increase or decrease depending upon the plate spacing

B. Remain same

C. Increases

D. Decreases

3706. Pick out the wrong statement pertaining to the design of a long tube vertical evaporator ?
comments icon0

A. Steam is fed to the shell, whereas the liquor is filled inside the tube

B. Tube dia is 3-6 cms, while tube length in 3-6 metres

C. None of these

D. Liquor level is maintained at 1/3rd to 1/2 of the height of the tube

3708. A rupture disc is provided in chemical equipments as an accessory meant for ___________________?
comments icon0

A. Creating turbulence

B. Avoiding vortex formation

C. Enhancing mixing rate

D. Relieving excess pressure
3709. In the case of a shell and tube heat exchanger, the logarithmic mean temperature difference ______________________?
comments icon0

A. Is always more than arithmetic mean value and the geometric mean value

B. ther the flow of stream is co-current or counter-current

C. Is always less than arithmetic average value

D. May be either more or less than geometric mean and arithmetic mean value depending upon

E. Is always less than arithmetic mean value, but more than geometric mean value

3715. Of the pressure vessels, with same thickness but different diameters, which one withstands higher pressure ?
comments icon0

A. Larger dia vessel

B. Strength of the vessel is same irrespective of the diameter

C. Larger dia long vessel

D. Smaller dia vessel
3718. Which of the following material is seldom used for pressure vessel construction ?
comments icon0

A. Killed steel

B. Semi-killed steel

C. Rimmed still

D. Mild steel

3720. Flanges are connected to pipes by _______________________?
comments icon0
A. All A., B. and C.

B. Screwing

C. Brazing

D. Welding

3725. ______________ of water makes it a widely used coolant in heat exchangers?
comments icon0

A. Low viscosity

B. High specific heat

C. Low corrosiveness

D. Low dirt factor

3726. Normally, the plate thickness of the bottoms and roofs of vertically cylindrical storage vessels as compared to that of the cylindrical shell is____________?
comments icon0
A. Less

B. More

C. More or less depending upon the pressure & temperature inside the vessel and the nature of

D. fluid contained therein

E. Same

3727. In a multipass shell and tube heat exchanger, the baffles on shell side is primarily provided for______________?
comments icon0

A. Reducing scale deposition

B. Increasing pressure drop

C. Creating turbulence

D. Fixing the tubes

3729. In case of a continuous distillation column, increase in reflux ratio may result in the______________?
comments icon0
A. All A., B. and C.

B. Lower fixed charges for the column

C. Greater cost for the condenser coolant

D. Greater cost for the reboiler heat supply

3732. (Le/D) for fully open gate valves would be __________________?
comments icon0

A. Much more than that for fully open globe valves

B. Much less (say 2% than that for fully open globe valves)

C. Around 7

D. Both B. and C.
3736. Reflux ratio variation in a distillation column is between___________________?
comments icon0

A. Zero and infinity

B. Zero and one

C. None of these

D. Minimum and infinity
3737. With increase in the reflux ratio for a fixed production from a continuous binary distillation column, the ______________________ decreases?
comments icon0
A. Fixed charges initially

B. Running cost of cooling water for condenser

C. Vapour & liquid load both

D. Running cost of steam for reboiler

3739. Value of Peclet number = ?, is the representative of___________________?
comments icon0
A. Plug flow

B. Eddy diffusivity = 0

C. Complete back mixing

D. Laminar flow

3741. Pick out the wrong statement about the design of sieve plate column and the bubble cap column ?
comments icon0
A. Weir height for a bubble cap plate column is the same as that for a sieve plate column

B. ve plate

C. te and bubble cap columns

D. The downcomer design and the residence time in the downcomer is almost same for sieve

E. Weir height in case of a bubble cap plate ranges from 50 to 150 mm and is higher than the

F. Weir length for a bubble cap plate is the same as that for the sieve plate

3743. Which of the following is the most common type of baffle used in industrial shell and tube heat exchanger ?
comments icon0
A. 25% cut segmental baffle

B. Disk and doughnut baffle

C. Orifice baffle

D. 75% cut segmental baffle

3746. Which of the following factors determine the amount of entrainment in a distillation column ?
comments icon0

A. Plate spacing

B. Depth of liquid above the bubble cap slots

C. All A., B. and C.

D. Vapour velocity in the volume between the plates

3748. In the design of a shell and tube heat exchanger, the corrosion allowance ____________________?
comments icon0

A. Need not be provided for non-pressure parts like tie rods, spacers, baffles, supports etc.

B. For carbon steel and cast iron pressure parts is 1.5 mm (except for tubes) and for severe

C. ditions it is 3 mm

D. For internal cover and tube sheet is provided on both the sides

E. All A., B. & C.
3749. Pick out the wrong statement pertaining to the comparative evaluation of performance of the packed tower and the plate tower ?
comments icon0

A. In operations involving large temperature changes. (e.g. distillation), plate towers are

B. ferred over packed towers as the packing may be crushed due to large temperature changes

C. ution

D. Plate tower is preferred over packed tower, if the operation involves liquids containing

E. Plate tower is preferred, if interstage cooling is required to remove heats of reaction or

F. The total weight of a dry plate tower is usually much more than that of a dry packed tower