Mass of steam to be produced, m = 4.4 kg
Pressure of steam, p = 6 bar
Temperature of steam, tsup = 250°C
Temperature of water = 30°C
Specific heat of steam, cps = 2.2 kJ/kg
At 6 bar, 250°C : From steam tables,
ts = 158.8°C, hf = 670.4 kJ/kg, hfg = 2085 kJ/kg
Enthalpy of 1 kg superheated steam reckoned from 0°C,
hsup = hf + hfg + cps (Tsup – Ts )
= 670.4 + 2085 + 2.2(250 – 158.8)
= 2956 kJ
Amount of heat already with 1 kg of water
= 1 × 4.18 × (30 – 0) = 125.4 kJ
Net amount of heat required to be supplied per kg
= 2956 – 125.4 = 2830.6 kJ
Total amount of heat required
= 4.4 × 2830.6 = 12454.6 kJ.