Problem Statement Submit at least one entry to the Rankine Cup Contest which meets all of the constraints given below. Use the link below to access the Rankine Cycle Simulator. Constraints 1. Minimum allowable quality at turbine exits is 90%. 2. Maximum allowable turbine efficiency is 90%. 3. Maximum allowable pump efficiency is 90%. 4. Minimum allowable net power output 600 MW. 5. The maximum allowable temperature anywhere in the cycle is 500°C. 6. The maximum allowable pressure anywhere in the cycle is 240 bar. 7. All limitations inherent to the Rankine Cycle Simulator are in effect. Links • Rankine Cup Link Rankine Cycle Simulator Operating Parameters Pressure [kPa] Steam Generator: 10000 Reheat 1: 5000.0 500.0 3000.0 1000.0 10.0 Reheat 2: OFWH: CFWH: Condenser: Temperature [C] SG Exit: 312.0 Reheat 1: 0.0 Reheat 2: 0.0 Mass Flow Rate [kg/s] SG Exit: 1.0 Percent Extraction [%] OFWH: CFWH: 0.0 0.0 Condenser Trap CFWH to: OFWH Subcooling [C] CFWH Exit: 0.0 Efficiency [%] Turbine: Pump: Reset State Points 1 Turbine inlet 2s Turbine ideal exit 100.0 100.0 Submit Contest Entry P T h S X [kPa] [C] [kJ/kg] [KJ/(kg K)] [-] 10,000 312.0 2,732.5 5.6279 SHV 10 45.8 1,779.8 5.6279 0.664 10 45.8 1,779.8 5.6279 0.664 10 45.8 191.8 10,000 46.1 201.9 10,000 46.1 201.9 0.6491 0.000 0.6492 SCL 0.6492 SCL 2 Turbine real exit Condenser exit 3 4s Pump ideal exit 4 Pump real exit SCL Subcooled liquid = SHV Superheated vapour Operating Conditions Work Transfer Pump work Turbine work Net work Heat Transfer Steam generator heat added Condenser heat rejected -10.09 kW 952.70 kW 942.61 kW 2,530.65 kW -1,588.04 kW
Problem Statement Submit at least one entry to the Rankine Cup Contest which meets all of the constraints given below. Use the link below to access the Rankine Cycle Simulator. Constraints 1. Minimum allowable quality at turbine exits is 90%. 2. Maximum allowable turbine efficiency is 90%. 3. Maximum allowable pump efficiency is 90%. 4. Minimum allowable net power output 600 MW. 5. The maximum allowable temperature anywhere in the cycle is 500°C. 6. The maximum allowable pressure anywhere in the cycle is 240 bar. 7. All limitations inherent to the Rankine Cycle Simulator are in effect. Links • Rankine Cup Link Rankine Cycle Simulator Operating Parameters Pressure [kPa] Steam Generator: 10000 Reheat 1: 5000.0 500.0 3000.0 1000.0 10.0 Reheat 2: OFWH: CFWH: Condenser: Temperature [C] SG Exit: 312.0 Reheat 1: 0.0 Reheat 2: 0.0 Mass Flow Rate [kg/s] SG Exit: 1.0 Percent Extraction [%] OFWH: CFWH: 0.0 0.0 Condenser Trap CFWH to: OFWH Subcooling [C] CFWH Exit: 0.0 Efficiency [%] Turbine: Pump: Reset State Points 1 Turbine inlet 2s Turbine ideal exit 100.0 100.0 Submit Contest Entry P T h S X [kPa] [C] [kJ/kg] [KJ/(kg K)] [-] 10,000 312.0 2,732.5 5.6279 SHV 10 45.8 1,779.8 5.6279 0.664 10 45.8 1,779.8 5.6279 0.664 10 45.8 191.8 10,000 46.1 201.9 10,000 46.1 201.9 0.6491 0.000 0.6492 SCL 0.6492 SCL 2 Turbine real exit Condenser exit 3 4s Pump ideal exit 4 Pump real exit SCL Subcooled liquid = SHV Superheated vapour Operating Conditions Work Transfer Pump work Turbine work Net work Heat Transfer Steam generator heat added Condenser heat rejected -10.09 kW 952.70 kW 942.61 kW 2,530.65 kW -1,588.04 kW
Elements Of Electromagnetics
7th Edition
ISBN:9780190698614
Author:Sadiku, Matthew N. O.
Publisher:Sadiku, Matthew N. O.
ChapterMA: Math Assessment
Section: Chapter Questions
Problem 1.1MA
Related questions
Question
Transcribed Image Text:Problem Statement
Submit at least one entry to the Rankine Cup Contest which meets all of the constraints
given below.
Use the link below to access the Rankine Cycle Simulator.
Constraints
1. Minimum allowable quality at turbine exits is 90%.
2. Maximum allowable turbine efficiency is 90%.
3. Maximum allowable pump efficiency is 90%.
4. Minimum allowable net power output 600 MW.
5. The maximum allowable temperature anywhere in the cycle is 500°C.
6. The maximum allowable pressure anywhere in the cycle is 240 bar.
7. All limitations inherent to the Rankine Cycle Simulator are in effect.
Links
•
Rankine Cup Link
![Rankine Cycle Simulator
Operating Parameters
Pressure [kPa]
Steam Generator:
10000
Reheat 1:
5000.0
500.0
3000.0
1000.0
10.0
Reheat 2:
OFWH:
CFWH:
Condenser:
Temperature [C]
SG Exit:
312.0
Reheat 1:
0.0
Reheat 2:
0.0
Mass Flow Rate [kg/s]
SG Exit:
1.0
Percent Extraction [%]
OFWH:
CFWH:
0.0
0.0
Condenser
Trap CFWH to:
OFWH
Subcooling [C]
CFWH Exit:
0.0
Efficiency [%]
Turbine:
Pump:
Reset
State Points
1
Turbine inlet
2s Turbine ideal exit
100.0
100.0
Submit Contest Entry
P
T
h
S
X
[kPa] [C] [kJ/kg] [KJ/(kg K)]
[-]
10,000 312.0 2,732.5
5.6279 SHV
10 45.8 1,779.8
5.6279 0.664
10 45.8 1,779.8
5.6279 0.664
10 45.8 191.8
10,000 46.1 201.9
10,000 46.1 201.9
0.6491 0.000
0.6492 SCL
0.6492 SCL
2 Turbine real exit
Condenser exit
3
4s Pump ideal exit
4 Pump real exit
SCL Subcooled liquid
=
SHV Superheated vapour
Operating Conditions
Work Transfer
Pump work
Turbine work
Net work
Heat Transfer
Steam generator heat added
Condenser heat rejected
-10.09 kW
952.70 kW
942.61 kW
2,530.65 kW
-1,588.04 kW](/v2/_next/image?url=https%3A%2F%2Fcontent.bartleby.com%2Fqna-images%2Fquestion%2F5227ed1d-0d6f-4397-9f94-b482003ba8b2%2Ffbb33b5f-8f57-4bd5-b7cc-ffecf65caa93%2Fmltnis5_processed.jpeg&w=3840&q=75)
Transcribed Image Text:Rankine Cycle Simulator
Operating Parameters
Pressure [kPa]
Steam Generator:
10000
Reheat 1:
5000.0
500.0
3000.0
1000.0
10.0
Reheat 2:
OFWH:
CFWH:
Condenser:
Temperature [C]
SG Exit:
312.0
Reheat 1:
0.0
Reheat 2:
0.0
Mass Flow Rate [kg/s]
SG Exit:
1.0
Percent Extraction [%]
OFWH:
CFWH:
0.0
0.0
Condenser
Trap CFWH to:
OFWH
Subcooling [C]
CFWH Exit:
0.0
Efficiency [%]
Turbine:
Pump:
Reset
State Points
1
Turbine inlet
2s Turbine ideal exit
100.0
100.0
Submit Contest Entry
P
T
h
S
X
[kPa] [C] [kJ/kg] [KJ/(kg K)]
[-]
10,000 312.0 2,732.5
5.6279 SHV
10 45.8 1,779.8
5.6279 0.664
10 45.8 1,779.8
5.6279 0.664
10 45.8 191.8
10,000 46.1 201.9
10,000 46.1 201.9
0.6491 0.000
0.6492 SCL
0.6492 SCL
2 Turbine real exit
Condenser exit
3
4s Pump ideal exit
4 Pump real exit
SCL Subcooled liquid
=
SHV Superheated vapour
Operating Conditions
Work Transfer
Pump work
Turbine work
Net work
Heat Transfer
Steam generator heat added
Condenser heat rejected
-10.09 kW
952.70 kW
942.61 kW
2,530.65 kW
-1,588.04 kW
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