All changes in kinetic and potential energy may be ignored. All pressure losses due to friction may be neglected. Ideal conditions must be assumed where necessary. Do the calculations needed to find the pressure at this point. Choose the closest value that will reduce the amount of interpolation needed. 1.1. Find the pressure (kPa) and temperature (K) at Points 1 to 7.. Assume ideal conditions where necessary. ASSUMPTIONS made at each point MUST be STATED clearly at the specific point. 1.2. Find the enthalpy at Points 8 to 15 (kJ/kg), Pump work must be included. Assume ideal conditions where necessary. ASSUMPTIONS made at each point MUST be STATED clearly at the specific point. 1.3. Calculate the mass flow rate of the steam at Point 10 in kg/min. ENERGY BALANCES must be SHOWN. 1.4. Calculate the nett work output available from the Rankine cycle in kJ/kg. ENERGY BALANCES must be SHOWN.

Solid Waste Engineering
3rd Edition
ISBN:9781305635203
Author:Worrell, William A.
Publisher:Worrell, William A.
Chapter7: Thermal Processes
Section: Chapter Questions
Problem 7.4P
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All changes in kinetic and potential energy may be ignored. All pressure losses due to friction may
be neglected. Ideal conditions must be assumed where necessary.
Do the calculations needed to find the pressure at this point. Choose the closest value that will reduce the amount of
interpolation needed.

1.1. Find the pressure (kPa) and temperature (K) at Points 1 to 7.. Assume ideal conditions where necessary. ASSUMPTIONS made
at each point MUST be STATED clearly at the specific point.
1.2. Find the enthalpy at Points 8 to 15 (kJ/kg), Pump work must be included. Assume ideal conditions where necessary. ASSUMPTIONS made at each point MUST be STATED clearly at the specific point.
1.3. Calculate the mass flow rate of the steam at Point 10 in kg/min. ENERGY BALANCES must be SHOWN.
1.4. Calculate the nett work output available from the Rankine cycle in kJ/kg. ENERGY BALANCES must be SHOWN.

8% of the incoming air is
removed for use in another
process
Combustor
RH
Mac=87%
CLP(R)
HP(g)
"- 89%
Нeat
Exchanger
10
(steam)
Condenser
|Closed Feed
Heater
FIGURE 1B
2 3 45 6 7| 8 9 10 11 | 12 13 14 15
Pressure (kPa)
95
839
97
10 6000
?
Temperature (°C)
17
850
87 40
700
m (metric tor
ton/nr)
Student number
P1
Transcribed Image Text:8% of the incoming air is removed for use in another process Combustor RH Mac=87% CLP(R) HP(g) "- 89% Нeat Exchanger 10 (steam) Condenser |Closed Feed Heater FIGURE 1B 2 3 45 6 7| 8 9 10 11 | 12 13 14 15 Pressure (kPa) 95 839 97 10 6000 ? Temperature (°C) 17 850 87 40 700 m (metric tor ton/nr) Student number P1
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9781305635203
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