Base area of the boiler, A = 0.15 m2
Thickness of the boiler, l = 1.0 cm = 0.01 m
Boiling rate of water, R = 6.0 kg/min
Mass, m = 6 kg
Time, t = 1 min = 60 s
Thermal conductivity of brass, K = 109 J s –1 m–1 K–1
Heat of vaporisation, L = 2256 × 103 J kg–1
The amount of heat flowing into water through the brass base of the boiler is given by:
θ = \(\frac{KA(T_1-T_2)t}{I}\) .........(i)
Where,
T1 = Temperature of the flame in contact with the boiler
T2 = Boiling point of water = 100°C
Heat required for boiling the water:
θ = mL ....... (ii)
Equating equations (i) and (ii), we get:
∴ mL = \(\frac{KA(T_1-T_2)t}{I}\)
T1-T2 = \(\frac{mLl}{KAt}\)
= \(\frac{6 \times 2256 \times 10^3 \times 0.01}{10^9 \times 0.15 \times 60}\)
= 137.98°C
Therefore, the temperature of the part of the flame in contact with the boiler is 237.98°C.
List-I (Molecule / Species) | List-II (Property / Shape) |
---|---|
(A) \(SO_2Cl_2\) | (I) Paramagnetic |
(B) NO | (II) Diamagnetic |
(C) \(NO^{-}_{2}\) | (III) Tetrahedral |
(D) \(I^{-}_{3}\) | (IV) Linear |
Figures 9.20(a) and (b) refer to the steady flow of a (non-viscous) liquid. Which of the two figures is incorrect ? Why ?
It is defined as the movement of heat across the border of the system due to a difference in temperature between system and its surroundings.
Heat can travel from one place to another in several ways. The different modes of heat transfer include: