FUND OF ENG THERMODYN(LLF)+WILEYPLUS
9th Edition
ISBN: 9781119391777
Author: MORAN
Publisher: WILEY
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The Figure shows a simple vapor power plant operating at steady state with water
circulating through the components.
Relevant data at key locations are given on the figure. The mass flow rate of the
water is 90 kg/s. Kinetic and potential energy effects are negligible as are all stray
heat transfers. Determine
a. The heat added in boiler to the water
b. If the combustion efficiency is 85%, find the mass of diesel fuel combustion
rate in kg/day if CVDiesel =52 MJ/kg.
c. The output turbine power in kW.
6.110 Figure P6.110 shows a simple vapor power plant operating
at steady state with water as the working fluid. Data at key locations
are given on the figure. The mass flow rate of the water circulating
through the components is 109 kg/s. Stray heat transfer and kinetic
and potential energy effects can be ignored. Determine
a. the net power developed, in MW.
b. the thermal efficiency.
c. the isentropic turbine efficiency.
t2
d. the isentropic pump efficiency.
e. the mass flow rate of the cooling water, in kg/s.
f. the rates of entropy production, each in kW/K, for the turbine,
condenser, and pump.
P = 100 bar
T = 520°C
%3D
Power out
Turbine
P2 = 0.08 bar
2 = 90%
%3D
Steam
Cooling
water in at 20°C
generator
Condenser
Pa= 100 bar
T= 43°C
Cooling
water out at 35°C
4.
Pump
3 P3 0.08 bar
Saturated liquid
Power
in
FIGURE P6.110
2.
www
Figure below shows a simple vapor power plant operating at steady state with water
as the working fluid. Data at key locations are given on the figure. The mass flow
rate of the water circulating through the components is 109 kg/s and isentropic
turbine efficiency is 80%. Stray heat transfer and kinetic and potential energy effects
can be ignored. Determine
(a) the net power developed, in MW.
(b) the thermal efficiency.
(c) the isentropic pump efficiency.
(d) the mass flow rate of the cooling water, in kg/s.
(e) the rates of entropy production, each in kW/K, for the turbine, condenser, and
pump.
P-100 bar
Ty-$60°C
Power out
Turbine
Py-0.08 bar
-80%
Steam
Cooling
water in at 20°C
generator
Condenser
P-100 bar
T-60°C
Cooling
water out at 40°C
4.
Pump
3 P= 0.08 bar
Saturaied liquid
Power
in
ww
Knowledge Booster
Similar questions
- Problem 5.060 SI The figure shows the schematic of a vapor power plant in which 100 kg/s of water circulates through the four components operating at steady state. The water flows through the boiler and condenser at constant pressure and through the turbine and pump adiabatically. Kinetic and potential energy effects can be ignored. Process data follow: Process 4-1: constant-pressure at 4000 kPa from saturated liquid to saturated vapor. Process 2-3: constant-pressure at 20 kPa from x2 = 88% to x3 = 18%. m = 100 kg/s Boiler X2 = 88% X3 = 18% Water Pump Turbine Condenser 2 Determine thermal efficiency. Determine ởrvle, in kW/K. Determine if the cycle is internally reversible, irreversible, or impossible. v Step 1 Determine the cycle thermal efficiency. % the tolerance is +/-2% Click if you would like to Show Work for this question: Open Show Work By accessing this Question Assistance, you will learn while you earn points based on the Point Potential Policy set by your instructor.…arrow_forwardHandwritten answer needed.arrow_forwardFigure 5.15 in the text gives a schematic of a Carnot cycle operating with a H2O liquid/vapor with a steady flow (constant mass flow rate) through each component. From the properties given below your cycle may or may not be a Carnot cycle. Kinetic energy and potential energy changes can be ignored in this problem. The cycle conditions are as follows: Process 4 – 1: constant pressure at 300 kPa from saturated liquid to saturated vapor Process 2 – 3: constant pressure at 30 kPa from x2 = 87.9% to x3 = 10.9% a) Determine the thermal efficiency using steam table data b) Compare the result of part a) with the Carnot efficiency using the boiler and condenser temperatures. c) State if the cycle is internally reversible, irreversible or impossiblearrow_forward
- The adjacent figure provides steady-state operating data for a vapor power plant using water as the working fluid. The mass flow rate of water is 12 kg/s. The turbine and pump operate adiabatically but not reversibly. Determine a) the thermal efficiency. b) the rates of heat transfer QQ and QQ000000, each in kW. State 1 2 3 4 5 6 P 6 MPa 10 kPa 10 kPa 7.5 MPa 7 MPa 6 MPa T(°C) 500 Sat. 40 550 h (kJ/kg) 3422.2 1633.3 191.83 199.4 167.57 3545.3arrow_forwardAt steady state, Refrigerant 22 enters (1) the compressor at 40C, 5.5bar and is compressed to 60C, 13.8bar. R-22 exiting (2) the compressor enters a heat exchanger where energy transfer to air as a separate stream occurs and the refrigerant exits (3) as a liquid at 13.5bar, 32C. Air enters (4) the condenser at 27C, 1.0bar with a volumetric flow rate of 21.2m3/min and exits (5) at 43C. Assuming ideal gas behavior for the air and stray heat transfer and kinetic and potential energy effects are negligible, determine the compressor powerarrow_forwardSteam power plant shown in figure isoperating at steady state with water as the workingfluid. The mass flow rate of the water circulatingthrough the components is 50 kg/s. Determine: d) isentropic pump efficiencye) mass flow rate of the cooling water, in kg/s.f) rates of entropy production, each in kW/K, forthe turbine and steam generator.Include all the relevant governing equations andreferences to the tables you use. Be organizearrow_forward
- Figure shows a simple vapor power plant operating at steady state with water as the working fluid. Data at key locations are given on the figure. The mass flow rate of the water circulating through the components is 109 kg/s. Stray heat transfer and kinetic and potential energy effects can be ignored. Determine: (a) the mass flow rate of the cooling water, in kg/s. (b) the thermal efficiency. (c) the rates of entropy production, each in kW/K, for the turbine, condenser, and pump. (d) Using the results of part (c), place the components in rank order, beginning with the component contributing most to inefficient operation of the overall system. verlarrow_forwardAs shown in the figure, Refrigerant 22 enters the compressor of an air conditioning unit operating at steady state at 40oF, 80 lbf/in2 and is compressed to 160oF, 200 lbf/in2. The refrigerant exiting the compressor enters a condenser where energy transfer to air as a separate stream occurs, and the refrigerant exits as a liquid at 200 lbf/in2, 90oF. Air enters the condenser at 75oF, 14.7 lbf/in2 with a volumetric flow rate of 1500 ft3/min and exits at 110oF. Neglect stray heat transfer and kinetic and potential energy effects, and assume ideal gas behavior for the air.arrow_forwardAs shown in the figure, Refrigerant 22 enters the compressor of an air conditioning unit operating at steady state at 40oF, 80 lbf/in2 and is compressed to 160oF, 200 lbf/in2. The refrigerant exiting the compressor enters a condenser where energy transfer to air as a separate stream occurs, and the refrigerant exits as a liquid at 200 lbf/in2, 90oF. Air enters the condenser at 70oF, 14.7 lbf/in2 with a volumetric flow rate of 1500 ft3/min and exits at 110oF. Neglect stray heat transfer and kinetic and potential energy effects, and assume ideal gas behavior for the air.arrow_forward
- Air as an ideal gas flows through the compressor and heat exchanger shown in the figure. A separate liquid stream also flows through the heat exchanger. The data given are for operation at steady state. Stray heat transfer to the surroundings can be neglected, as can all kinetic and potential energy changes. Determine the compressor power, in kW, and the mass flow rate of the cooling water, in kg/s.arrow_forward6.107 Figure P6.107 provides the schematic of a heat pump using Refrigerant 134a as the working fluid, together with steady-state data at key points. The mass flow rate of the refrigerant is 7 kg/min, and the power input to the compressor is 5.17 kW. (a) Determine the co- efficient of performance for the heat pump. (b) If the valve were re- placed by a turbine, power could be produced, thereby reducing the power requirement of the heat pump system. Would you recommend this power-saving measure? Explain. She P2 = P3 = 9 bar Tz = 60°C Saturated liquid Condenser Expansion W = 5.17 kW Compressor valve Evaporator m= 7 kg/min P1 =P4 = 2.4 bar FIGURE P6.107arrow_forward6.111 Steam enters a two-stage turbine with reheat operating at steady state as shown in Fig. P6.111. The steam enters turbine 1 with a mass flow rate of 120,000 lb/h at 1000 lbf/in.², 800°F and expands to a pressure of 60 lbf/in. From there, the steam enters the reheater where it is heated at constant pressure to 350°C before entering tur- bine 2 and expanding to a final pressure of 1 lbf/in.? The turbines operate adiabatically with isentropic efficiencies of 88% and 85%, respectively. Kinetic and potential energy effects can be neglected. Determine the net power developed by the two turbines and the rate of heat transfer in the reheater, each in Btu/h. Qin P3 = 60 lbf/in.2 T = 350°C P2 = 60 lbf/in.2 Reheater W net Turbine 1 Turbine 2 Nu = 88% Ni2 = 85% P4 =1 lbf/in.2 P1 = 1000 Ibf/in.2 T = 800°F m = 120,000 lb/h FIGURE P6.111arrow_forward
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