Heat Transfer Miscellaneous


  1. A slender rod of length L, diameter d (L >> d) and thermal conductivity k1 i s joined with another rod of identical dimensions, but of thermal conductivity k 2, to form a composite cylindrical rod of length 2L. The heat transfer in radial direction and contact resistance are negligible. The effective thermal conductivity of the composite rod is









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    As per question, heat transfer in radial direction and contact resistance are negligible. In series connection,
    (Rth) eq = R1 + R2

    2L
    =
    L
    +
    L
    AkeqAK1AK2

    2
    =
    1
    +
    1
    KeqK1K2

    ⇒ Req =
    2K1K2
    K1 + K2

    Correct Option: A


    As per question, heat transfer in radial direction and contact resistance are negligible. In series connection,
    (Rth) eq = R1 + R2

    2L
    =
    L
    +
    L
    AkeqAK1AK2

    2
    =
    1
    +
    1
    KeqK1K2

    ⇒ Req =
    2K1K2
    K1 + K2


  1. The peak wavelength of radiation emitted by a black body at a temperature of 2000 K is 1.45 μm. If the peak wavelength of emitted radiation changes to 2.90 μm, then the temperature (in K) of the black body is









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    From wein’s displacement law λmax T = constant
    max)1 T1 = (λmax)2 T2
    1.45 × 2000 = 2.90 × T2

    T2 =
    1.45
    × 2000
    2.90

    T2 = 1000 K

    Correct Option: B

    From wein’s displacement law λmax T = constant
    max)1 T1 = (λmax)2 T2
    1.45 × 2000 = 2.90 × T2

    T2 =
    1.45
    × 2000
    2.90

    T2 = 1000 K



  1. A balanced counter flow heat exchanger has a surface area of 20 m2 and overall heat transfer coefficient of 20 W/m2K. Air (cp = 1000 J/kgK) entering at 0.4 kg/s and 280 K is to be preheated by the air leaving the system at 0.4 kg/s and 300 K. The temperature (in K) of the preheated air is









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    Counter flow heat exchanged
    Surface Area A = 20 m2, mass flow rate = 0.4 kg/s

    u =
    20W
    ;
    m2

    Temperature Tci = 280K
    Cp of air = 1000
    1
    kg K


    Since m is same for both flow = 0.4 kg/s
    Assume Cp is same = 100 J/kg.K
    Hence ∆T1 = Tci – Tco = ∆T2 = Th0 – Tci
    ∆T1 = 300 – Tco = Th0 – 280
    ∆Tm = ∆T1 = ∆T2
    uA∆Tm = mCp (Tco – Tci)
    20 × 20 × (300 – Tco) = 0.4 × 1000(Tco – 280)
    2Tco = 300 + 280
    Tco =
    580
    = 290 K
    2

    Correct Option: A

    Counter flow heat exchanged
    Surface Area A = 20 m2, mass flow rate = 0.4 kg/s

    u =
    20W
    ;
    m2

    Temperature Tci = 280K
    Cp of air = 1000
    1
    kg K


    Since m is same for both flow = 0.4 kg/s
    Assume Cp is same = 100 J/kg.K
    Hence ∆T1 = Tci – Tco = ∆T2 = Th0 – Tci
    ∆T1 = 300 – Tco = Th0 – 280
    ∆Tm = ∆T1 = ∆T2
    uA∆Tm = mCp (Tco – Tci)
    20 × 20 × (300 – Tco) = 0.4 × 1000(Tco – 280)
    2Tco = 300 + 280
    Tco =
    580
    = 290 K
    2


  1. Consider a parallel-flow heat exchanger with area Ap and a counter-flow heat exchanger with area Ac. In both the heat exchangers, the hot stream flowing at 1 kg/s cools from 80°C to 50°C. For the cold stream in both the heat exchangers, the flow rate and the inlet temperature are 2 kg/s and 10°C, respectively. The hot and cold streams in both the heat exchangers are of the same fluid. Also, both the heat exchangers have the same overall heat transfer coefficient. The ratio Ac /Ap is _____.









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    Correct Option: A



  1. In a counter-flow heat exchanger, water is heated at the rate of 1.5 kg/s from 40°C to 80°C by an oil entering at 120°C and leaving at 60°C. The specific heats of water and oil are 4.2 kJ/ kgK and 2 kJ/kgK, respectively. The overall heat transfer coefficient is 400 W/m2K. The required heat transfer surface area (in m2) is









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    Heat exchanger is a counterflow type.

    ∆Ti = 120 – 80 = 40°C (θ1)
    ∆Te = 60 – 40 = 20°C (θ2)

    LMTD =
    θ1 - θ2
    In
    θ1
    θ2

    =
    40 - 20
    = 28.86°C
    In
    40
    20

    Q = mc Cpc(Tce - Tci)
    = 1.5 × 4.2 × 103 (80 – 40) watt
    Q = 252000 W
    Q = UA∆Tm .
    A =
    Q
    =
    1.5 × 4.2 × 103 × 40
    U∆Tm400 × 28.86

    = 21.83 m2.

    Correct Option: D

    Heat exchanger is a counterflow type.

    ∆Ti = 120 – 80 = 40°C (θ1)
    ∆Te = 60 – 40 = 20°C (θ2)

    LMTD =
    θ1 - θ2
    In
    θ1
    θ2

    =
    40 - 20
    = 28.86°C
    In
    40
    20

    Q = mc Cpc(Tce - Tci)
    = 1.5 × 4.2 × 103 (80 – 40) watt
    Q = 252000 W
    Q = UA∆Tm .
    A =
    Q
    =
    1.5 × 4.2 × 103 × 40
    U∆Tm400 × 28.86

    = 21.83 m2.