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Process Equipment and Plant Design problems


  • 1. Factor of safety (i.e., overdesign factor) in heat transfer equipments is about __________ percent more than the actual/theoretical design factor.

  • Options
  • A. 5-10
  • B. 15-20
  • C. 30-35
  • D. 35-40
  • Discuss
  • 2. Pick out the wrong statement

  • Options
  • A. In a flanged and standard dished head, the crown radius is ? shell outside diameter.
  • B. In a flanged and shallow dished head, the crown radius is > shell outside diameter.
  • C. Flat head covers are most suitable for larger vessels operating at very high pressure.
  • D. Flanged only head is a type of flat head in which gradual change in the shape at the centre results in reduced local stresses.
  • Discuss
  • 3. In a bag filter, the pressure drop increases directly as the

  • Options
  • A. density of the gas, but is independent of the viscosity of the gas.
  • B. density of the gas and inversely as viscosity of the gas.
  • C. viscosity of the gas and inversely as density of the gas.
  • D. none of these.
  • Discuss
  • 4. In a distillation column, bubble caps are located on trays with a pitch of __________ times the outside diameter of the caps.

  • Options
  • A. 1.3 to 2
  • B. 1.6 to 2
  • C. 2.5
  • D. 1.5 to 3
  • Discuss
  • 5. In a shell and tube heat exchanger, triangular pitch arrangement as compared to square pitch arrangement

  • Options
  • A. results in higher shell side pressure drop.
  • B. can accomodate less number of tubes for a given shell diameter.
  • C. facilitates easier shell side cleaning; hence is more suitable for handling high dirt factor shell side fluid.
  • D. creates relatively lower turbulence on the shell side resulting in lower shell side heat transfer co-efficient.
  • Discuss
  • 6. Which of the following is the best tube material from thermal conductivity point of view alone?

  • Options
  • A. Aluminium
  • B. Stainless steel
  • C. Copper
  • D. Carbon steel
  • Discuss
  • 7. Ratio of tube length to shell diameter for a shell and tube heat exchanger is

  • Options
  • A. 8 : 1 to 12 : 1 for both liquid-liquid and gas-gas heat exchangers.
  • B. 4 : 1 to 8 : 1 for liquid-liquid exchanger.
  • C. < 4 : 1 for gas-gas exchangers.
  • D. both(b) & (c).
  • Discuss
  • 8. For a given fluid, as the pipe diameter increases, the pumping cost

  • Options
  • A. decreases.
  • B. increases.
  • C. remains unaffected.
  • D. may increase or decreaes depending upon whether the fluid is Newtonian or non-Newtonion.
  • Discuss
  • 9. Hole diameter of the seive trays in the distillation column ranges from __________ mm.

  • Options
  • A. lto3
  • B. 4 to 8
  • C. 3 to 12.5
  • D. 12.5 to 18.5
  • Discuss
  • 10. Value of Peclet number = ?, is the representative of

  • Options
  • A. laminar flow.
  • B. complete back mixing,
  • C. plug flow.
  • D. eddy diffusivity = 0.
  • Discuss

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