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Chemical Engineering :: Heat Transfer

  1. The Nusselt number for fully developed (both thermally and hydrodynamically) laminar flow through a circular pipe whose surface temperature remains constant is

  2. A.
    1.66
    B.
    88.66
    C.
    3.66
    D.
    dependent on NRe only

  3. Sensible heat of hot industrial flue gases can not be recovered by a/an

  4. A.
    economiser
    B.
    regenerator
    C.
    ceramic recuperator
    D.
    none of these

  5. The critical radius of insulation for a spherical shell is (where, K = thermal conductivity of insulating material h0 = heat transfer coefficient at the outer surface)

  6. A.
    K/h0
    B.
    2K/h0
    C.
    h0/K
    D.
    h0/2K

  7. Radiator of an automobile engine is a __________ type of heat exchanger.

  8. A.
    co-current
    B.
    cross-current
    C.
    counter-current
    D.
    direct contact

  9. In pipe flow, heat is transferred from hot wall to the liquid by

  10. A.
    conduction only.
    B.
    forced convection only.
    C.
    forced convection and conduction.
    D.
    free and forced convection.

  11. The value of Stefan-Boltazman constant in SI unit is

  12. A.
    5.6697 x 10-8W/m2.°K4
    B.
    0.1714 x 10-8W/m2.°K4
    C.
    5.6697 x 10-8kcal/m2 . °K4
    D.
    0.1714 x 10-8kcal/m2. °K4

  13. The unit of heat transfer co-efficient is

  14. A.
    BTU/hr. ft2°F
    B.
    BTU/hr. °F. ft.
    C.
    BTU/hr. °F
    D.
    BTU/hr. ft

  15. For turbulent flow in a tube, the heat transfer co-efficient is obtained from the Dittus-Boelter correlation. If the tube diameter is halved and the flow rate is doubled, then the heat transfer co-efficient will change by a factor of

  16. A.
    1
    B.
    1.74
    C.
    6.1
    D.
    37

  17. The inner wall of a furnace is at a temperature of 700°C. The composite wall is made of two substances, 10 and 20 cm thick with thermal conductivities of 0.05 and 0.1 W.m-1.°C-1 respectively. The ambient air is at 30°C and the heat transfer co-efficient between the outer surface of wall and air is 20 W.m-2.°C-1. The rate of heat loss from the outer surface in W.m-2is

  18. A.
    165.4
    B.
    167.5
    C.
    172.5
    D.
    175

  19. Value of Nusselt number [Nu = (hD/k)] for the heat transfer by conduction from a droplet or a spherical particle to a surrounding stagnant film is

  20. A.
    0.5
    B.
    2
    C.
    10
    D.
    100