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Home Chemical Engineering Process Equipment and Plant Design Comments

  • Question
  • Pressure drop per tray in the atmospheric distillation column is about __________ psi.


  • Options
  • A. 0.01 - 0.5
  • B. 0.07 - 0.12
  • C. 0.5 - 1.0
  • D. 1 - 3

  • Correct Answer
  • 0.07 - 0.12 


  • Process Equipment and Plant Design problems


    Search Results


    • 1. Larger depth of liquid on the trays of a distillation column

    • Options
    • A. leads to high tray efficiency.
    • B. results in higher pressure drop per tray.
    • C. both (a) & (b).
    • D. neither (a) or (b).
    • Discuss
    • 2. The equivalent diameter for fluid flow through a channel of constant non-circular cross section of area 'A' is given by (where, P = perimeter of the channel in contact with the fluid)

    • Options
    • A. 4 A/P
    • B. A/P
    • C. 4 P/A
    • D. A
    • Discuss
    • 3. Baffle width is normally taken as __________ times the tank diameter.

    • Options
    • A. 0.1-0.12
    • B. 0.4-0.5
    • C. 0.45-0.6
    • D. 0.2-0.45
    • Discuss
    • 4. A binary liquid azeotropic mixture has boiling point lower than either of the components, when it shows __________ deviation from Raoult's Law.

    • Options
    • A. positive
    • B. negative
    • C. no
    • D. none of these
    • Discuss
    • 5. For given number of passes, pitch & tube diameter, the maximum number of tubes that can be accommodated in a shell of tripled inside diameter will be __________ times.

    • Options
    • A. about 9
    • B. considerably more than 9
    • C. considerably less than 9
    • D. about 3
    • Discuss
    • 6. The centre to centre distance between two consecutive baffles in a shell and tube heat exchanger is called the baffle pitch or baffle spacing, which is more than 1/5th the I.D. of the shell. Which of the following is not a function of the baffles?

    • Options
    • A. To increase the residence time of shell side fluid.
    • B. To provide support to the tube bundle.
    • C. To reduce the induced vibration in the tubes.
    • D. To increase the tube side heat transfer co-efficient by inducing turbulence.
    • Discuss
    • 7. If a single tube pass heat exchanger is converted to two passes; for the same flow rate, the pressure drop per unit length in tube side will __________ times.

    • Options
    • A. increase by 1.8
    • B. decrease by 22
    • C. increase by 21.6
    • D. none of these
    • Discuss
    • 8. In the downcomer of a distillation column, the minimum recommended residence time is about __________ seconds.

    • Options
    • A. 2.5
    • B. 5
    • C. 12.5
    • D. 17.5
    • Discuss
    • 9. Bubble cap plate column is

    • Options
    • A. a finite stage contactor.
    • B. used only for distillation, not for absorption.
    • C. a differential stage contactor.
    • D. a continuous contactor.
    • Discuss
    • 10. In case of 1.5" heat exchanger tubes, the inside flow area __________ with decrease in BWG.

    • Options
    • A. increases
    • B. decreases
    • C. remains same
    • D. none of these
    • Discuss


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