Mass of water to be converted to steam, mw = 2 kg
Temperature of water, tw = 25°C
Pressure and dryness fraction of steam = 5 bar, 0.9 dry
At 5 bar : From steam tables
hf = 640.1 kJ/kg ; hfg = 2107.4 kJ/kg
Enthalpy of 1 kg of steam (above 0°C)
h = hf + xhfg
= 640.1 + 0.9 × 2107.4 = 2536.76 kJ/kg
Sensible heat associated with 1 kg of water
mw × cpw × (tw – 0)
= 1 × 4.18 × (25 – 0) = 104.5 kJ
Net quantity of heat to be supplied per kg of water
= 2536.76 – 104.5 = 2432.26 kJ
Total amount of heat to be supplied
= 2 × 2432.26 = 4864.52 kJ.