Answer:
(a) T₂ = 126°C , T₂s = 106°C
(b) 64%
Step-by-step explanation:
we will begin with a step by step process;
using the expression
Wт = m(ex)Cp(T₁ - T₂)
where
Wт = turbine power output
m(ex) = mass of the exhaust gas
Cp = specific heat at constant pressure
T₁ = exhaust gas temperature at the turbine inlet
T₂ = exhaust gas temperature at the turbine exit
using from the gas table, the specific heat of exhaust gas at avg temperature of 425°C as 1.075kJ/kg.K
making substitutions we have;
T₁ = 450°C, T₂ = 400°C, m(ex) = 0.02kg/s, Cp = 1.075kJ/kg.K
Substituting values into formula gives;
Wт = m(ex)Cp(T₁ - T₂)
Wт = [(0.02kg/s)(1.075kJ/kg.K)(450+273)K-(400+273)K]
Wт = 1.075 kW
The relationship of mechanical efficiency between turbine and compressor is given as;
Лм = Wc/Wт............................. (1)
where Wт = turbine output
Wc = compressor output
Лм = mechanical efficiency
Wc = Лм × Wт
Wc = 0.95 × 1.075(kW)
Wc = 1.021 kW
compressor power:
Wc = m(air)Cp(T₂ - T₁)
where m(air) = mass of air
T₁ = air temp at the compressor inlet
T₂ = air temp at the compressor exit
Cp = specific heat at constant pressure
T₂ = T₁ + Wc/m(air)Cp .................. (2)
the specific heat of air at the expected average temperature of 100°C is 1.011 kJ/kg.K
substituting T₁ = 70°C, Wc = 1.021 kW, m(air) = 0.018 kg/sm Cp = 1.011 kJ/kg.K
T₂ = 70 °C + (1.021)kW/ (0.018kg/s)(1.011 kJ/kg.K)
T₂ = 126 °C
Considering an isentropic process, the air temperature at the compressor exit;
T₂s = T₁ (P²/P¹)∧(k-1)/(k)
where T₁ = 70°C, P₁= 95kPa, P₂ = 135kPa, k = 1.397
T₂s = (70+273)K (135/95 kPa) ∧ (1.397-1)/(1.397)
T₂s = 379 K = 106 °C
(b). the isentropic efficiency of the compressor
Лc = (T₂s - T₁ / T₂ - T₁)
Лc = (106°C - 70°C) / (126°C - 70°C)
Лc = 0.642 = 64%
the isentropic efficiency of the compressor is 64%
cheers i hope this helps