Can you please draw the TS Diagram of the problem below. I already have a solution but I badly need the TS Diagram. Problem: A 25,000 kW turbo-generator is supplied with 128,000 kg/h of steam at 2.50 MP and 400°C when developing it rated load. There are actually extracted 10,400 kg/h at 0.3 MPa and 8300 kg/h at 0.06 MPa. The condenser pressure is 0.007 MPa and actual feedwater temperature is 127°C. Again, please only draw the TS Diagram. Thanks! Please refer to the image below.

Elements Of Electromagnetics
7th Edition
ISBN:9780190698614
Author:Sadiku, Matthew N. O.
Publisher:Sadiku, Matthew N. O.
ChapterMA: Math Assessment
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Can you please draw the TS Diagram of the problem below. I already have a solution but I badly need the TS Diagram.

Problem:

A 25,000 kW turbo-generator is supplied with 128,000 kg/h of steam at 2.50 MP and 400°C when developing it rated load. There are actually extracted 10,400 kg/h at 0.3 MPa and 8300 kg/h at 0.06 MPa. The condenser pressure is 0.007 MPa and actual feedwater temperature is 127°C. 

Again, please only draw the TS Diagram. Thanks!

Please refer to the image below.

Reference solution for making the TS Diagram
@ Point 1 (Superheated)
@ Point 5 (Saturated Liquid)
P₁ = 2.5 MPa > T₁ = 400
h₁ = 32 39.3 kJ /kg
P5 = P4 = 0.007 MPa
hshes = 163.40 kJ/kg
V₁ = Vf5 = 0.0010074 m³/kg
S₁ = 7.0148 kJ/kg
@ Point 2
S₂
P₂ = 0.3 MPa
Sg
S, 7.0148 kJ/kg
= 6.99 19 kJ /kg k < 5₂ (su
S
h
6.9726
7.0148
7.0263
Sig
Sf = 0.5592
Sfg=
7.7167
27 39.4
h₂ = 2734.710056 kJ/kg
h₁ = 163.40
hfg = 2409.1
@ Point 3 (Wet)
S3 S17.0148 kJ/kgk
P3 = 0.00 MPa
Sg= 7.5320 S3 (wet)
S = 11453
= 6.3867
2717.5
h₂
x = 0.9190192118
h3 = 359.86 + x(2293.6)
h3 =
2467.722464 kJ/kg
Wpi= has hs
0.0533922
hf 359.86
hfg = 2293.6
=
has 163.40
has 163.4533922 kJ/kg
@ Point 4 (Wet)
SA S₁ = 7.048 kJ/kgk
P4 = 0.007 MPa
S4= 5 + XSpg
7.0148 0.5592 + X(7.7167)
h4 = hf + xhfg
X= 0.83657522
163.40+ x(24091)
2178.793362
@ Point B, (Subcooled)
WP₁ = V₂ (Po-Ps)
-0.001 0074 (60-7)
= 0.0533922 kJ/kg
@ Point 6 (Saturated Liquid)
P6 = P3 = 0.06 MPa
ho hr6 = 359.86 kJ/kg
V6 Vf6. 0.0010 331 m²/kg
@ Point B (Subcooled)
WP2 V6 (PP)
-0.00160331 (300- 60)
= 0.247944
Wp₂= hp 359.86
he6 = 360. 107944
@ Point 7 (Saturated Liquid)
P7= P₂ = 0.3 MPa
hz = hf7 561.47 kJ/kg
V7 V7 = 0.0010732 m³/kg
@ Point B, (Subcooled)
V7(P₁-P+)
WP3
= 0.0010732( 2500-300)
=
2.36 104
hez-ha
Wp3
2. 36104 = hs7 -561.47
h87 563. 83104
Transcribed Image Text:Reference solution for making the TS Diagram @ Point 1 (Superheated) @ Point 5 (Saturated Liquid) P₁ = 2.5 MPa > T₁ = 400 h₁ = 32 39.3 kJ /kg P5 = P4 = 0.007 MPa hshes = 163.40 kJ/kg V₁ = Vf5 = 0.0010074 m³/kg S₁ = 7.0148 kJ/kg @ Point 2 S₂ P₂ = 0.3 MPa Sg S, 7.0148 kJ/kg = 6.99 19 kJ /kg k < 5₂ (su S h 6.9726 7.0148 7.0263 Sig Sf = 0.5592 Sfg= 7.7167 27 39.4 h₂ = 2734.710056 kJ/kg h₁ = 163.40 hfg = 2409.1 @ Point 3 (Wet) S3 S17.0148 kJ/kgk P3 = 0.00 MPa Sg= 7.5320 S3 (wet) S = 11453 = 6.3867 2717.5 h₂ x = 0.9190192118 h3 = 359.86 + x(2293.6) h3 = 2467.722464 kJ/kg Wpi= has hs 0.0533922 hf 359.86 hfg = 2293.6 = has 163.40 has 163.4533922 kJ/kg @ Point 4 (Wet) SA S₁ = 7.048 kJ/kgk P4 = 0.007 MPa S4= 5 + XSpg 7.0148 0.5592 + X(7.7167) h4 = hf + xhfg X= 0.83657522 163.40+ x(24091) 2178.793362 @ Point B, (Subcooled) WP₁ = V₂ (Po-Ps) -0.001 0074 (60-7) = 0.0533922 kJ/kg @ Point 6 (Saturated Liquid) P6 = P3 = 0.06 MPa ho hr6 = 359.86 kJ/kg V6 Vf6. 0.0010 331 m²/kg @ Point B (Subcooled) WP2 V6 (PP) -0.00160331 (300- 60) = 0.247944 Wp₂= hp 359.86 he6 = 360. 107944 @ Point 7 (Saturated Liquid) P7= P₂ = 0.3 MPa hz = hf7 561.47 kJ/kg V7 V7 = 0.0010732 m³/kg @ Point B, (Subcooled) V7(P₁-P+) WP3 = 0.0010732( 2500-300) = 2.36 104 hez-ha Wp3 2. 36104 = hs7 -561.47 h87 563. 83104
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