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Chemical Engineering :: Process Equipment and Plant Design

  1. Speed of industrial paddle agitator ranges from __________ rpm.

  2. A.
    1 to 5
    B.
    20 to 100
    C.
    500 to 750
    D.
    1000 to 2000

  3. __________ strain is measured using a 'strain rosetter'.

  4. A.
    Volumetric
    B.
    Shear
    C.
    Linear
    D.
    none of these

  5. Thin spherical shells subjected to internal pressure, develop __________ stresses.

  6. A.
    radial
    B.
    circumferential
    C.
    both (a) & (b)
    D.
    neither (a) nor (b)

  7. With increase in the reflux ratio for a fixed production from a continuous binary distillation column, the __________ decreases.

  8. A.
    fixed charges initially
    B.
    running cost of cooling water for condenser
    C.
    vapour & liquid load both
    D.
    running cost of steam for reboiler

  9. Vertical vessels are not supported by

  10. A.
    brackets
    B.
    skirts
    C.
    columns
    D.
    saddles

  11. With increase in pressure drop (for a given particle size), the dust collection efficiency of a cyclone separator will

  12. A.
    increase
    B.
    decrease
    C.
    remain unaffected
    D.
    increase or decrease depending on the nature of the dust.

  13. Spherical shaped pressure vessel is considered to be the most ideal, because it can

  14. A.
    withstand higher pressure for a given metallic shell thickness.
    B.
    be fabricated very easily.
    C.
    be designed without wind load considerations.
    D.
    be supported very easily.

  15. An adequate clearance between the tray and the shell wall of a distillation column is provided to

  16. A.
    drain the liquid from the tray when the unit is not in operation.
    B.
    allow for thermal expansion and facilitate installation.
    C.
    avoid back-trapping.
    D.
    none of these.

  17. Overall tray efficiency of a distillation column is the ratio of the number of

  18. A.
    overall gas transfer units to the number of ideal trays required.
    B.
    ideal trays required to the number of real trays required.
    C.
    real trays required to the number of ideal trays required.
    D.
    none of these.

  19. Pick out the wrong statement about the design of a sieve plate column.

  20. A.
    An increased weir height improves the tray efficiency at the cost of high plate pressure drop; optimum wear height being 40-90 mm for column pressure above atmospheric and 6-12 mm for vacuum columns.
    B.
    For segmental downcomers, the chord length is 60-80% of the column diameter. An initial value of downcomer area of 12% is taken in the design.
    C.
    Width of the calming section provided at the inlet and outlet sides of the plate is 75 mm for column diameter below 1.5 metres and 100 mm for larger diameter columns.
    D.
    Minimum recommended downcomer residence time for the disengagement of entrained vapour is the same for both foaming and non-foaming liquids, which is about 20 seconds.