Process Equipment and Plant Design Questions
Practice Process Equipment and Plant Design MCQs with answers and explanations. Page 2 of 20.
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Chemical Engineering
Topic
Process Equipment and Plant Design
Page
2 / 20
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Practice
Questions
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Hopper/heads geometry in process vessels: the included apex angle commonly used for CONICAL BOTTOM HEADS on chemical process equipment is approximately
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Pipe schedules and dimensions: two steel pipes of the SAME nominal size but DIFFERENT schedule numbers will have the same _____ by definition of standard pipe sizes.
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Comparing pipe schedules: relative to Schedule 80 of the same nominal size, the wall thickness of Schedule 40 pipe is
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Feed thermal condition in distillation: what is the value of the “q” line slope parameter for a SATURATED LIQUID feed entering a distillation column?
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Heat exchanger geometry: in a shell-and-tube exchanger, the “TUBE PITCH” is defined as the _____ between adjacent tubes on the same pattern.
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LMTD correction in multi–shell-pass exchangers
In a shell-and-tube heat exchanger, how does the LMTD correction factor FT change when the number of shell passes is increased (for the same terminal temperatures and number of tube passes)?
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Materials for pressure vessels – identify the one seldom used
Among the listed steels, which is seldom used for pressure vessel construction due to quality and through-thickness property concerns?
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Siting of petroleum storage tanks – underground vs. aboveground
At petrol pumps and similar facilities, storage tanks are normally installed underground when the required capacity is less than how many kilolitres (kL)?
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Packed towers vs. plate (tray) towers – choose the correct statement
Considering corrosion, foaming tendency, and pressure drop, which of the following statements is correct?
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Tube layout choice – triangular vs. square pitch in shell-and-tube exchangers
Compared with a square pitch, a triangular pitch tube layout in a given shell diameter:
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Supports for vertical vessels – understanding lug supports
Which statement best characterizes lug supports for vertical vessels in comparison to skirt supports?
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Pressure drop comparison – 1–2 versus 1–1 heat exchanger (tube side)
For turbulent flow in the tubes, the tube-side pressure drop in a 1–2 exchanger is approximately how many times that in a 1–1 exchanger of the same size and tube count at the same liquid flow rate?
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Bag filter operation – typical pressure drop range
What is the normal operating pressure drop range across an industrial baghouse (fabric filter), expressed as mm water gauge?
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Rotary vacuum drum filters – typical drum speed
What is the normal rotational speed range of the drum in a rotary vacuum drum filter (RVDF), expressed in revolutions per minute (rpm)?
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Stuffing box – primary function in fluid-handling equipment
In pumps and valves, a stuffing box is primarily used for which purpose?
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Agitated vertical cylindrical vessel design:
Pick the single WRONG statement about geometry and agitation performance.
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Packed absorption tower design data:
Operating velocity is typically 40–50% of flooding. What pressure drop is normally used for design per metre of packing (mm H2O per m)?
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Basket-type natural-circulation evaporator:
Pick the WRONG statement about configuration and typical service.
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Thick-walled cylinder under internal pressure:
Where is the maximum tensile (hoop) stress located?
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Strength terminology in materials:
The stress beyond which a material shows permanent set is the yield stress; the highest stress that can be applied without any permanent set is called the __________.
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