Practice Test: Question Set - 02
1. Stress-strain diagram for low carbon steel/mild steel is shown below in the Fig. The point 'A' on the Fig. represents the
- (A) Breaking stress
- (B) Ultimate stress
- (C) Elastic limit
- (D) Yield point
2. Power required for agitation depends upon the
- (A) Height & properties of the liquid
- (B) Agitator type & speed of agitation
- (C) Size of agitator & the tank
- (D) All (a), (b) and (c)
3. High pressure fluid in a shell and tube heat exchanger should preferably be routed through the
- (A) Tubes to avoid the expansion of high pressure shell construction
- (B) Shell side for smaller total pressure drop
- (C) Shell side, if the flow is counter-current and
tube side if the flow is co-current
- (D) Shell side for large overall heat transfer co-efficient
4. Stage efficiency for packed tower varies with the
- (A) Type & size of packing
- (B) Fluid rates and fluid properties
- (C) Operating pressure and column diameter
- (D) All (a), (b) and (c)
5. What is the slope of the feed line, if the feed to a distillation column is a saturated liquid?
- (A) 0
- (B) ∞
- (C) > 1
- (D) < 1
6. Tube wall thickness depends on the corrosiveness of the fluids and their operating pressure & temperature and is specified by Birmingham wire gauge (B.W.G)-a number which varies from 8 to 18 with the numbers 14 and 16 being more commonly used. Outside diameter of tubes varies from about 15 to 50 mm; however a tube of less than _________ mm outside diameter is generally not recommended for fouling fluids.
- (A) 16
- (B) 19
- (C) 28
- (D) 38
7. _________ tower is the most suitable gas-liquid contacting device involving highly corrosive fluids.
- (A) Sieve plate
- (B) Packed
- (C) Bubble cap plate
- (D) None of these
8. In hydrostatic testing of welded pipe (for leakage, strength etc.) the ratio of minimum hydrostatic test pressure to internal design pressure is around
- (A) 0.5
- (B) 1.5
- (C) 2.5
- (D) 3.5
9. For a cylindrical shell, (subject to the thickness of uppermost course being more than the minimum for dia of the tank in question), the thickness of the courses of shell
- (A) Decreases upwards
- (B) Increases upwards
- (C) Remains same throughout
- (D) May decrease or increase upwards depending upon whether vacuum or
positive pressure would be maintained inside the shell
10. In a shell and tube heat exchanger, the shortest center to center distance between the adjacent tubes is
- (A) Called tube pitch
- (B) Called tube clearance
- (C) Always less than the diameter of the tube
- (D) None of these
11. Pick out the wrong statement.
- (A) If sufficient residence time (around 8 seconds)
is not provided to the downcoming liquid in the downcomer, it may entrain some
vapor
- (B) The liquid head in the downcomer should not be
greater than one half the plate spacing to avoid flooding
- (C) The discharge end of the downcomer must project far enough into the
tray liquid so that no gas bubbles can enter the open end and by pass the
bubble caps
- (D) None of these
12. 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
- (A) D/2 or minimum 2" to 5D
- (B) D/5 or minimum 2" to 5Dv
- (C) D/5 or minimum 2" to D
- (D) None of these
13. For turbulent flow (NRe > 2100) of low viscosity fluid (μ > 20cp) in steel pipes, the optimum inside pipe diameter is given by(where, Q = fluid flow rate, ft3/sec, ρ = fluid density, lb/ft3 μ = fluid viscosity, centipoise Di = optimum inside pipe diameter, inches)
- (A) Di, opt = 3.9 Q0.45 ρ0.13
- (B) Di, opt = 3.9 Q0.45.
μ0.95
- (C) Di, opt = 4.7 Q0.36.
μ3.2ρ0.13
- (D) Di, opt = 3 Q0.36.
μ0.88
14. Scale up problem in design based on the similarity concept takes into account _________ similarity.
- (A) Geometrical
- (B) Kinematic
- (C) Dynamic
- (D) All (a), (b) and (c)
15. Weep holes provided in the plates of a distillation column
- (A) Facilitate draining out liquid from a tray when the unit is not in
operation
- (B) Are normally located near the overflow weir so that any delivery of
liquid during operation follows approximately the same path as the overflow
fluid
- (C) Must be large enough (usually 1/4" to 5/8" dia) to prevent
plugging but should not deliver excessive amount of fluid during operation
- (D) All (a), (b) and (c)
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