(Q)₁= 5052.482 kW • Heat rejection (Q)R T3=1400 K (turbine inlet temperature) Ta turbine exit temperature = (6) 1400 (10) T₁

Elements Of Electromagnetics
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Author:Sadiku, Matthew N. O.
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A,B and C were answered, proceed to D,E and F. Air enters the compressor of an ideal air standard brayton cycle at 100 kPa, 300 K, with a volumetric flow rate of 5 cu.m/s. The compressor pressure ratio is 10. The turbine inlet temperature is 1400 K. Compute the (a) P, V, and T at each point of the cycle; (b) QA, QR in kW; (c) WC, WT in kW; (d) rp, TBW; (e) e; (f) mep.
Hence the heat adan
|(Q)A = 5052.482 kW
• Heat rejection (QR
T3-1400 K (turbine inlet temprerature)
T₁ turbine exit temperature
2=(6)
1400 (10)
T₁
T4=725, 126 K
(QR=mx C₂ x (T4-T₁)
(Q)R 6. 125 x 1.005 x (725. 126-300)
(QR-2616.916 kW
Hence the heat rejection
(Q)R= 2616.916 kW
Step 3
(c). Calculation of work consumed by the
compressor (Wc) and work done by the
turbine (WT):
• The work consumed by the
compressor (WC)
T₂=579.209 K
T₁=300 K
m=6. 125 kg/s
Cp=1.005 kJ/kg K
(Wc)=mx cp x (T₂-T₁)
(We) 6. 125 x 1.005 × (579.209 300)
(We) 1718.706 kW
Hence the work consumed by the
compressor (We) = 1718.706 kW
• The work done by the turbine (WT)
(WT) turbine work
T₁ turbine inlet temperature
T4 turbine exit temperature
T;=1400 K
T₁=725. 126 K
m=6.125 kg/s
Cp=1.005 kJ/kg K
(WT)=mx c₂ x (T3-T4)
(WT)=6. 125 x 1.005 x (1400-725. 126)
(WT)=4154.271 kW
Hence the work done by the turbine
(WT) = 4154.271 kW
Step 4
Results:
For the given problem the following results
are obtained,
The heat addtion |(Q), = 5052.482 kW
The heat rejection (Q) = 2616.916 kW
The work consumed by the compressor
(We) = 1718. 706 kW
The work done by the turbine
(WT) = 4154.271 kW
Transcribed Image Text:Hence the heat adan |(Q)A = 5052.482 kW • Heat rejection (QR T3-1400 K (turbine inlet temprerature) T₁ turbine exit temperature 2=(6) 1400 (10) T₁ T4=725, 126 K (QR=mx C₂ x (T4-T₁) (Q)R 6. 125 x 1.005 x (725. 126-300) (QR-2616.916 kW Hence the heat rejection (Q)R= 2616.916 kW Step 3 (c). Calculation of work consumed by the compressor (Wc) and work done by the turbine (WT): • The work consumed by the compressor (WC) T₂=579.209 K T₁=300 K m=6. 125 kg/s Cp=1.005 kJ/kg K (Wc)=mx cp x (T₂-T₁) (We) 6. 125 x 1.005 × (579.209 300) (We) 1718.706 kW Hence the work consumed by the compressor (We) = 1718.706 kW • The work done by the turbine (WT) (WT) turbine work T₁ turbine inlet temperature T4 turbine exit temperature T;=1400 K T₁=725. 126 K m=6.125 kg/s Cp=1.005 kJ/kg K (WT)=mx c₂ x (T3-T4) (WT)=6. 125 x 1.005 x (1400-725. 126) (WT)=4154.271 kW Hence the work done by the turbine (WT) = 4154.271 kW Step 4 Results: For the given problem the following results are obtained, The heat addtion |(Q), = 5052.482 kW The heat rejection (Q) = 2616.916 kW The work consumed by the compressor (We) = 1718. 706 kW The work done by the turbine (WT) = 4154.271 kW
Step 2
(a). Pressure (P)-volume (V) and
temperature (T)-entropy (S) diagram of air
standard Brayton cycle:
The following P-V and T-S diagram for each
process of the Brayton cycle,
V₂
T
P-P,
S₁-S₂
Volume →→→→
Figa: Pressure-Volume diagram of
Brayton cycle.
P₁-P₁
(10)
T₂=579.209 K
T3=1400 K
V=5 m³/s
S-S
V₁
Entropy
Fig b Temperature-entropy diagram of
Brayton cycle.
4
(b). Calculation of heat addition (Q) and
heat rejection (Q)K:
• Heat addition (Q)A
T₂=temperature after compression
T₁=300 K (temperature before compress
r=10 (compression ratio)
y=1.4 (adiabatic indx)
p=1.225 kg/m³ (air density)
m=p x v
Hence the heat addition
(Q)A = 5052.482 kW
m=1.225 x 5
m=6. 125 kg/s
Cp=1.005 kJ/kg K (specific heat)
(Q)₁=mx C₂ x (T3-T₂)
(Q)₁ 6. 125 x 1.005 x (1400 - 579. 209)
(Q)₁=5052.482 kW
Transcribed Image Text:Step 2 (a). Pressure (P)-volume (V) and temperature (T)-entropy (S) diagram of air standard Brayton cycle: The following P-V and T-S diagram for each process of the Brayton cycle, V₂ T P-P, S₁-S₂ Volume →→→→ Figa: Pressure-Volume diagram of Brayton cycle. P₁-P₁ (10) T₂=579.209 K T3=1400 K V=5 m³/s S-S V₁ Entropy Fig b Temperature-entropy diagram of Brayton cycle. 4 (b). Calculation of heat addition (Q) and heat rejection (Q)K: • Heat addition (Q)A T₂=temperature after compression T₁=300 K (temperature before compress r=10 (compression ratio) y=1.4 (adiabatic indx) p=1.225 kg/m³ (air density) m=p x v Hence the heat addition (Q)A = 5052.482 kW m=1.225 x 5 m=6. 125 kg/s Cp=1.005 kJ/kg K (specific heat) (Q)₁=mx C₂ x (T3-T₂) (Q)₁ 6. 125 x 1.005 x (1400 - 579. 209) (Q)₁=5052.482 kW
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