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730 An expander operates adiabatically with nitrogen entering at Tl and PI with a molar flow rate A The exhaust pressure is P2, and the expander efficiency is q Estimate the power output of the expander and the temperature of the exhaust stream for one of the following sets of operating conditions (a) TI = 75315 K(480 C), P1= 6 bar, A = 02 kmol s-' , P2= 1 bar, q = 080 (b) TI = 67315 K(400 C), PI = 5 bar, A = 015 kmol s-', P2= 1 bar, q = 075 (c) Tl =77315 K(500 C), P1 =7bar, A =0175kmol s-', P2= I bar, q =078 (d) Tl = 72315 K(450 C), P1= 8 bar, i z = 01 kmol sf', P2= 2 bar, q = 085 (e) Tl = 75515 K(482"C), PI= 655 bar, A = 023 kmol s-', P2= 103 bar, q = 080 731 What is the ideal-work rate for the expansion process of Ex 76 What is the thermodynamic efficiency of the process What is the rate of entropy generation sG What is wLOs, Take T = 300 K , 732 Exhaust gas at 67315 K (400 C) and 1 bar from internal-combustion engines flows at the rate of 125 mol s-' into a waste-heat boiler where saturated steam is generated at a pressure of 1200 kPa Water enters the boiler at 29315 K (20 C) (T,), and the exhaust gases are cooled to within 10 K (10 C) of the steam temperature The heat capacity of the exhaust gases is Cp/ R = 334 112 x lop3TIK The steam flows into an adiabatic turbine and exhausts at a pressure of 25 kPa If the turbine efficiency q is 72%, (a) What is w,, the power output of the turbine (b) What is the thermodynamic efficiency of the boilerlturbine combination (c) Determine sG the boiler and for the turbine for (d) Express wl0,,(boiler) and %ost(turbine) as fractions of ( ~ i d , , lI, the ideal work of the process.

[root@fedora-serverA ~]# ls -R /export/home/ /export/home/: project5 /export/home/project5: a b c d e

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733 A small adiabatic air compressor is used to pump air into a 20-m3 insulated tank The tank initially contains air at 29815 K (25 C) and 10133 kPa, exactly the conditions at which air enters the compressor The pumping process continues until the pressure in the tank reaches 1000 kPa If the process is adiabatic and if compression is isentropic, what is the shaft work of the compressor Assume air to be an ideal gas for which C p = (7/2)R and Cv = (5/2)R 734 Saturated steam at 125 kPa is compressed adiabatically in a centrifugal compressor to 700 kPa at the rate of 25 kg s-' The compressor efficiency is 78% What is the power requirement of the compressor and what are the enthalpy and entropy of the steam in its final state 735 A compressor operates adiabatically with air entering at TI and P1 with a molar flow rate A The discharge pressure is P2 and the compressor efficiency is q Estimate the power requirement of the compressor and the temperature of the discharge stream for one of the following sets of operating conditions (a) Tl = 29815 K(25"C), PI = 10133kPa, ti ~ 0 kmol sC1, P2= 375kPa, q =075 1 (b) Tl = 35315 K(80 C), P1= 375kPa, A = 0 l kmol sf', P2= IOOOkPa, q =070 (c) Tl =30315K(30 C), P1= 100kPa, A =015 kmol s-', Pz =500kPa, q =080 (d) TI = 37315 K(lOO C), PI =5OOkPa, i z =005 kmol s-l, P2= 1300kPa, 77 = 075

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( e ) TI = 30015 K(27"C), PI = 101 bar, A =023 kmol s-l, P2 =38 bar, q =075 (f) TI = 33915 K(66"C), P1= 38 bar, A =023 kmol s-', P2= 93 bar, q = 070

[root@fedora-serverA ~]# chown -R project5project5 /export/home/project5/

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