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Total Questions : 1628 | Page 9 of 163 pages
Question 81. In a rotary drier, the average retention time of solid is(where Z = length of the drier, metres ρ = apparent solid density, kg/m³ L = flow rate of dry solids, kg/see. m² drier cross-section H = hold up of solid.)
  1.    Z.H.ρ/L
  2.    L/Z.H.ρ
  3.    H.ρ/L
  4.    Z.H/L.ρ
 Discuss Question
Answer: Option A. -> Z.H.ρ/L
Question 82. The most common standard size of bubble caps used in industrial operation is
  1.    1" dia cap with 0.5" dia riser
  2.    6" dia cap with 4" dia riser
  3.    8" dia cap with 1" dia riser
  4.    4" dia cap with 8" dia riser
 Discuss Question
Answer: Option B. -> 6" dia cap with 4" dia riser
Question 83. The circumferential (hoop) stress in a thin walled cylinderical vessel under internal pressure is
  1.    pd/2t
  2.    pd/4t
  3.    pd/t
  4.    pd/3t
 Discuss Question
Answer: Option A. -> pd/2t
Question 84. The longitudinal stress induced in a thin walled cylinderical vessel under internal pressure is
  1.    pd/2t
  2.    pd/4t
  3.    pd/t
  4.    pd/8t
 Discuss Question
Answer: Option B. -> pd/4t
Question 85. In case of design of a shell and tube heat exchanger,
  1.    Minimum cleaning lane of 6.5 mm is provided, when tubes are on a square pitch
  2.    Minimum tube sheet thickness (in which tubes are fixed) is equal to the O.D. of the tube upto 15 mm tube diameter; and for > 15 mm tube diameter, tube sheet thickness is smaller than tube diameter
  3.    O.D. of the tube is 6 to 40 mm while the tube lengths used are 0.5, 2.5, 3.0, 4.0, 5.0, 6 metres
  4.    All of the above
 Discuss Question
Answer: Option D. -> All of the above
Question 86. Pick out the wrong statement about routing of fluids in a shell and tube heat exchanger.
  1.    The corrosive and fouling fluid should be preferably routed through the tubes
  2.    The viscous fluid should be routed through the shell side
  3.    Lower flow rate fluid should be routed through the shell side
  4.    Higher pressure fluid stream should be routed through the shell side
 Discuss Question
Answer: Option D. -> Higher pressure fluid stream should be routed through the shell side
Question 87. Pick out the wrong statement pertaining to a shell and tube heat exchanger.
  1.    The minimum value of baffle spacing is 50 mm
  2.    The maximum value of baffle spacing is equal to the I.D. of the shell
  3.    The maximum unsupported tube span is generally about 75 times tube diameter, but is reduced to about 60 times for aluminium, copper & alloys of these
  4.    Disk and doughnut baffle is the most commonly used baffle
 Discuss Question
Answer: Option D. -> Disk and doughnut baffle is the most commonly used baffle
Question 88. Pick out the wrong statement pertaining to shell and tube heat exchanger.
  1.    Clearance between shell & baffles and between tube & baffles should be minimum to avoid by-passing of the fluid, but it should be enough to permit the removal of tube bundle
  2.    Baffles are supported independently of the tubes by tie rods and positioned by spacers
  3.    Tie rods are fixed at one end in the tube sheet by making blind holes and the minimum number of tie rods is 4 with at least 10 mm diameter
  4.    Bracket supports are used for horizontal shell, while saddle support is used for vertical shell
 Discuss Question
Answer: Option D. -> Bracket supports are used for horizontal shell, while saddle support is used for vertical shell
Question 89. In case of a shell and tube heat exchanger, the effect of L/D on inside film heat transfer co-efficient (hi) vanishes after a Reynold number of
  1.    1000
  2.    3000
  3.    5000
  4.    10000
 Discuss Question
Answer: Option D. -> 10000
Question 90. In a multipass shell and tube heat exchanger, the baffles on shell side is primarily provided for
  1.    Reducing scale deposition
  2.    Increasing pressure drop
  3.    Fixing the tubes
  4.    Creating turbulence
 Discuss Question
Answer: Option D. -> Creating turbulence

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