A total of 1500 kg/hr of steam at 300°C and 5 bar is decompressed to 150°C and 1 bar. If there is no work in this process, determine the heat transfer. Explain what the positive or negative sign on the calculated heat transfer means.
A total of 1500 kg/hr of steam at 300°C and 5 bar is decompressed to 150°C and...
1. (42 points) A piston-cylinder device contains 6 kg of steam at 100°C with a quality of 50 percent. This steam undergoes two processes as follows: 1-2 Heat is transferred to the steam in a reversible manner while the temperature is held constant until the steam exists as a saturated vapor. 2-3 The steam expands in an adiabatic, reversible process until the pressure is 15 kPa. (a) (24 points) Fill in the table using the given and determined properties. You...
100 kg of steam is enclosed in a piston-cylinder device initially at 300°C and 5 bar It expands and cools to 200°C and 1 bar. What is the change in entropy?
3. Steam at 20 bar and 640 °C is available at one location in an industrial plant. At another location, steam at 15 bar and 360 °C is required for use in a certain process. An engineer suggests that steam at this condition can be provided by allowing the higher-pressure steam to expand through a valve to 15 bar and then cool to 360 °C through a heat exchanger with heat transfer to the surroundings, which are at 25 °GC...
Propane gas enters a continuous adiabatic heat exchanger 240°C. Superheated steam at 300 C and 5 bar enters the exchanger flowing countercurrently to the propane and exits as a saturated liquid at the same pressure at 40 C and 250 kPa and exits at Taking flow chart. Include both mass and volumes on your inlet and outlet streams. b. Calculate the specific enthalpy values for the inlet and outlet streams. c. Use an energy balance to calculate the required mass...
A turbine discharges 216.3 kg/h saturated steam at 10.0 bar. It is desired to generate steam at 250°C and 10.0 bar by mixing the turbine discharge with a second stream of superheated steam of 300°C and 10.0 bar. For 393.2 kg/h of the product stream to be generated , how much heat must be added to the mixer in kW? Report positive umber.
Soru (2 points) Five kg of steam undergo an expansion in a piston cylinder assembly from state 1 to state 2. The amount of heat transfer from the heat source to the steam and the amount of work transfer from the paddle wheel to the steam are shown in the figure. The specific internal energy change of the steam during this process is also illustrated. Determine the amount of energy transfer by work from the steam to the piston during...
In a cogeneration plant, 10% kg/h of steam at 80 bar, 480 °C expands in the h.p. turbine to 10 bar. From the exhaust 4 x 10 kgh of steam is extracted for process heating. The remaining steam expands in the l.p. turbine to 0.08 bar. Saturated liquid at 0.08 bar leaving the condenser is pumped to 9.5 bar where it mixes with the condensate from the process heater leaving at 9.5 bar, 120°C. The entire flow is then pumped...
In a cogeneration plant, 10^6 kg/h of steam at 80 bar, 480 °C expands in the h.p. turbine to 10 bar. From the exhaust 4 x 10 kgh of steam is extracted for process heating. The remaining steam expands in the l.p. turbine to 0.08 bar. Saturated liquid at 0.08 bar leaving the condenser is pumped to 9.5 bar where it mixes with the condensate from the process heater leaving at 9.5 bar, 120°C. The entire flow is then pumped...
5. A steam turbine operates with an inlet condition of 30 bar, 400 °C, 160 m/s and an outlet state of a saturated vapour at 0.7 bar with a velocity of 100 m/s. The mass flow rate is 1200 kg/min and the power output is 10800 kW. Present the process on the T-v diagram. Determine the magnitude and direction of the heat-transfer rate in kJ/min if the potential energy change in negligible.
In a cogeneration plant, 10^6 kg/h of steam at 80 bar, 480 °C expands in the h.p. turbine to 10 bar. From the exhaust 4 x 10 kgh of steam is extracted for process heating. The remaining steam expands in the l.p. turbine to 0.08 bar. Saturated liquid at 0.08 bar leaving the condenser is pumped to 9.5 bar where it mixes with the condensate from the process heater leaving at 9.5 bar, 120°C. The entire flow is then pumped...