Process Equipment and Plant Design MCQs

Welcome to our comprehensive collection of Multiple Choice Questions (MCQs) on Process Equipment and Plant Design, a fundamental topic in the field of Basic Chemical Engineering. Whether you're preparing for competitive exams, honing your problem-solving skills, or simply looking to enhance your abilities in this field, our Process Equipment and Plant Design MCQs are designed to help you grasp the core concepts and excel in solving problems.

In this section, you'll find a wide range of Process Equipment and Plant Design mcq questions that explore various aspects of Process Equipment and Plant Design problems. Each MCQ is crafted to challenge your understanding of Process Equipment and Plant Design principles, enabling you to refine your problem-solving techniques. Whether you're a student aiming to ace Basic Chemical Engineering tests, a job seeker preparing for interviews, or someone simply interested in sharpening their skills, our Process Equipment and Plant Design MCQs are your pathway to success in mastering this essential Basic Chemical Engineering topic.

Note: Each of the following question comes with multiple answer choices. Select the most appropriate option and test your understanding of Process Equipment and Plant Design. You can click on an option to test your knowledge before viewing the solution for a MCQ. Happy learning!

So, are you ready to put your Process Equipment and Plant Design knowledge to the test? Let's get started with our carefully curated MCQs!

Process Equipment and Plant Design MCQs | Page 1 of 50

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Q1.
Overall distillation column efficiency for most of the refinery columns can be given by (for ฮผ = 0.07 - 1.4 cp and relative volatility < 4) (where ฮท = overall column efficiency, % ฮผ = molal average viscosity of feed at average column temperature and pressure, cp ฮ”p = pressure drop per tray, psi)

a.

A

b.

B

c.

C

d.

D

Discuss
Answer: (a).A
Q2.
For laminar flow (Nส€โ‚‘ < 2100) in steel pipe, the optimum inside pipe diameter is given by

a.

A

b.

B

c.

C

d.

D

Discuss
Answer: (a).A
Q3.
For annular flow of a fluid, the ratio of the equivalent diameter for pressure drop calculation to the equivalent diameter for heat transfer calculation is

a.

A

b.

B

c.

C

d.

D

Discuss
Answer: (a).A
Q4.
Pressure drop due to pipe fittings can be estimated by the following equation, where, Lโ‚‘ = equivalent length of straight pipeline which will incur the same frictional loss as the fitting and D = diameter of the fitting. The value of Lโ‚‘/D (dimensionless) for 45° elbow and 180° close return bends would be respectively around
Discuss
Answer: (b).45 and 75
Q5.
In a rotary drier, the average retention time of solid is (where Z = length of the drier, metres ฯ = apparent solid density, kg/m³ L = flow rate of dry solids, kg/see. m² drier cross-section H = hold up of solid.)

a.

A

b.

B

c.

C

d.

D

Discuss
Answer: (a).A
Q6.
In a double pipe concentric heat exchanger, the equivalent diameter of annulus for heat transfer would be (where, Dโ‚ and Dโ‚‚ are I.D. of inner and outer pipes)

a.

A

b.

B

c.

C

d.

D

Discuss
Answer: (a).A
Q7.
For turbulent flow (Nส€e > 2100) of low viscosity fluid (ฮผ > 20cp) in steel pipes, the optimum inside pipe diameter is given by(where, Q = fluid flow rate, ft³/sec.ฯ = fluid density, lb/ft³ ฮผ = fluid viscosity, centipoise Dแตข = optimum inside pipe diameter, inches)

a.

A

b.

B

c.

C

d.

D

Discuss
Answer: (a).A
Q8.
The following ratio, is normally taken as
Discuss
Answer: (a).0.15-030
Q9.
Stress-strain diagram for low carbon steel/mild steel is shown below in the Figure. The point 'A' on the Figure represents the
Discuss
Answer: (c).elastic limit
Q10.
Equivalent diameter for heat transfer calculation for a duct of square cross-section having each side as 'd' will be

a.

A

b.

B

c.

C

d.

D

Discuss
Answer: (a).A