10 kg of fluid per minute goes through a reversible steady flow process. The
properties of fluid at the inlet are : p1 = 1.5 bar, ρ1 = 26 kg/m3, C1 = 110 m/s and u1 = 910 kJ/kg and
at the exit are p2 = 5.5 bar, ρ2 = 5.5 kg/m3, C2 = 190 m/s and u2 = 710 kJ/kg. During the passage,
the fluid rejects 55 kJ/s and rises through 55 metres. Determine :
(i) The change in enthalpy (∆ h) ;
(ii) Work done during the process (W).
Flow of fluid = 10 kg/min
Properties of fluid at the inlet :
Pressure "p_1= 1.5 \\;bar = 1.5 \\times 10^5 \\;N\/m^2"
Density "\u03c1_1 = 26 \\;kg\/m^3"
Velosity "C_1= 110 \\;m\/s"
Internal energy "u_1=910 \\;kJ\/kg"
Properties of the fluid at the exit :
Pressure "p_2= 5.5 \\;bar = 5.5 \\times 10^5 \\;N\/m^2"
Density "\u03c1_2 = 5.5 \\;kg\/m^3"
Velocity "C_2= 190 \\;m\/s"
Internal energy "u_2=710 \\;kJ\/kg"
Heat rejected by the fluid, "Q= 55 \\;kJ\/s"
Rise is elevation of fluid = 55 m
(i) The change in enthalpy,
"\u0394h=\u0394u +\u0394(pv) \\;\\;\\;\\;(i)\\\\\n\n\u0394(pv) = \\frac{p_2v_2 -p_1v_1}{1} \\\\\n\n= \\frac{p_2}{\u03c1_2} -\\frac{p_1}{\u03c1_1} \\\\\n\n= 1 \\times 10^5 -0.0577 \\times 10^5 \\\\\n\n= 10^5 \\times 0.9423 \\;Nm \\\\\n\n= 94.23 \\;kJ \\\\\n\n\u0394u =u_2 -u_1 = 710 -910 = -200 \\;kJ\/kg"
Substituting the value in eqn. (i), we get
"\u0394h = -200 + 94.23 = -105.77 \\;kJ\/kg"
(ii) The steady flow equation for unit mass flow can be written as
"Q=\u0394KE + \u0394PE +\u0394h +W"
where Q is the heat transfer per kg of fluid
"Q= 55 \\;kJ\/s = \\frac{55 \\;kJ\/s}{\\frac{10}{60} \\;kg\/s} = 55 \\times 6 = 330 \\;kJ\/kg \\\\\n\n\u0394KE = \\frac{C^2_2 -C^2_1}{2}= \\frac{190^2 -110^2}{2} \\;Nm = 12000 \\;J = 12 \\;kJ \\\\\n\n\u0394PE=(Z_2 -Z_1) \\;g = (55- 0) \\times 9.81 \\;Nm = 539.5 \\;J = 0.54 \\;kJ"
Substituting the value in steady flow equation,
"-330 = 12 +0.54 -105.77 +W \\\\\n\nW= -236.77 \\;kJ\/kg"
Work done per second "= -236.77 \\times \\frac{10}{60} = -39.46 \\;kJ\/s = -39.46 \\;kW"
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