. A quantity of steam at 10 bar and 0.85 dryness occupies 0.15 m3. Determine the heat supplied to raise the temperature of the steam to 300°C at constant pressure and
percentage of this heat which appears as external work.
Take specific heat of superheated steam as 2.2 kJ/kg K.
Solution;
Given ;
Pressure of steam ,"P_1=P_2=10" bar
Dryness fraction,"x_1=0.85"
Volume of steam; "v_1=0.15m^3"
Final temperature of steam,"t_{p_2}=300\u00b0c"
Specific heat of superheated steam,"C_{ps}=2.2kJ\/kgK"
From steam tables;
At 10 bar;
"\\nu_g=0.194m^3\/kg"
"t_s=179.9\u00b0c"
"h_{fg}=2013.6kJ\/kg"
Mass of steam will be given as;
"m_s=\\frac{V_1}{x_1\\nu_g}=" "\\frac{0.15}{0.84\u00d70.194}" =0.909kg
Heat supplied per kg of steam is;
="(1-x_1)h_{fg}+c_p(t_{p_2}-t_s)"
=(1-0.85)×2013.6+2.2×(300-179.9)
=566.26kJ/kg
Total heat supplied;
=566.26×0.909=514.7kJ
External work done during the process;
W="p(\\nu_{sp_2}-x\\nu_g)"
W="p[(\\nu_g\u00d7\\frac{t_{p_2}}{t_{p_1}})-x_1\\nu_g]"
"W=10\u00d710^5[(0.194\u00d7\\frac{300+273}{179.9+273})-(0.85\u00d70.194)]\u00d710^{-3}"
"W=80kJ\/kg"
Percentage of total heat supplied per kg is;
="\\frac{80}{566.26}=0.141" ="14.1" %
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