lec17_sunway.pdf
TRANSCRIPT
TRC2200: Thermo Fluids & Power Systems
LECTURE 17
Mass and Energy Analysis of Open Systems (Control Volumes)
Lecturer: Alpha Agape Gopalai
• Conservation of mass
• Flow work and the energy of a flowing fluid
• Energy analysis of steady-flow systems
• Some steady-flow engineering devices
Lecture Outline
• Conservation of mass: Mass, like energy, is a conserved property, and it cannot be created or destroyed during a process.
• Closed systems: The mass of the system remain constant during a process.
• Control volumes: Mass can cross the boundaries, and so we must keep track of the amount of mass entering and leaving the control volume.
Mass is conserved even in chemical reactions
Conservation of Mass
9
Flow work and the energy of a flowing fluid
Schematic for flow work.
Flow work, or flow energy: The work
(or energy) required to push the mass into
or out of the control volume. This work is
necessary for maintaining a continuous
flow through a control volume.
11
• Nozzles and Diffusers
• Turbines and Compressors
•Throttling valve
• Mixing chambers
• Heat exchangers
• Pipe and duct flow
Case studies
12
Nozzle and Diffuser
A nozzle is a device that increases the velocity of
a fluid at the expense of pressure.
A diffuser is a device that increases the pressure
of a fluid by slowing it down.
Nozzles and diffusers are commonly utilized in jet
engines, rockets, spacecraft, and even garden hoses.
14
Compressor
Compressors, as well as pumps and fans, are devices used to increase the
pressure of a fluid. Work is supplied to these devices from an external source
through a rotating shaft.
Energy balance for the compressor in
this figure:
15
Turbine
A turbine is a rotary engine that extracts energy from a fluid flow and converts it into useful work.
16
Throttling valves
Throttling valves are any kind of flow-restricting devices that cause a significant
pressure drop in the fluid.
What is the difference between a turbine and a throttling valve?
The pressure drop in the fluid is often accompanied by a large drop in temperature,
and for that reason throttling devices are commonly used in refrigeration and air-
conditioning applications.
17
Throttling valves
The temperature of an ideal gas does not
change during a throttling (h =
constant) process since h = h(T).
Energy balance
18
Mixing chambers
In engineering applications, the section where the mixing process takes place is commonly referred to as a mixing chamber.
Energy balance for the adiabatic
mixing chamber in the figure is:
19
Heat exchangers
Heat exchangers are devices where two moving fluid streams exchange heat without mixing. Heat exchangers are widely used in various industries, and they come in various designs.
A heat exchanger can be as simple
as two concentric pipes.
20
Pipe and duct flow
The transport of liquids or gases in pipes and
ducts is of great importance in many
engineering applications. Flow through a pipe
or a duct usually satisfies
the steady-flow conditions.
Heat losses from a hot fluid flowing through an uninsulated
pipe or duct to the cooler environment may be very significant.
Pipe or duct flow may involve more than
one form of work at the same time.
Example
21
Air enters the compressor of a gas-turbine plant at 100 kPa and 25°C with a low velocity and exits at 1 MPa and 347°C with a velocity of 90 m/s. The power input to the compressor is 250 kW and it is cooled at 1500 kJ/min. (a) Determine the mass flow rate of air through the compressor. Take the molecular mass of air as 29 kg/kmol and allow for variation in specific heat of air as a function of temperature (in Kelvin) as given by the equation:C pa = 28.11 + 0.1967 x 10-2T +0.4802 x 10-5T2 -1.966 x 10-9T3 kJ/kmol.K
Example:
You may begin by considering the general energy equation given below:
outoutinin WQgZ
ChmWQgZ
Chm 2
2
221
2
11
22
P1=100kPaT1=25oC
C1=0
P2=1MPaT2=347oC
C2=90m/s
1500 kJ/min
250 kWGiven:
Molecular mass of air 29 kg/kmol
Compressor power input Win = 250 kW
Heat rejection Qout = 1500 kJ/min
22
P1=100kPaT1=25oC
C1=0
P2=1MPaT2=347oC
C2=90m/s
250 kW
1500 kJ/min
The potential energy change, input heat, inlet velocity and output mechanical work are negligible in the case of the compressor
Determine:
a) Mass flow rate of air
2
2
2121
2Q
CmWTCTCm papa
C pa = 28.11 + 0.1967 x 10-2+0.4802 x 10-5T2 -1.966 x 10-9T3 kJ/kmol.K
At T1 = 298K Cpa = 29.07 kJ/kmol K
= 29.07/29 kJ/kgK
= 1.004 kJ/kgK
h=CpT
Example
23
At T2 = 620K Cpa = 30.71kJ/kmol K
= 30.71/29 kJ/kgK
= 1.0588 kJ/kgK
2
2
2121
2Q
CmWTCTCm papa
skgm
xmxxm
/62.0
60
1500
10002
902506200588.1298004.1
2
P1=100kPaT1=25oC
C1=0
P2=1MPaT2=347oC
C2=90m/s
1500 kJ/min
250 kW
Example
• Conservation of mass
• Mass and volume flow rates
• Mass balance for a steady-flow process
• Mass balance for incompressible flow
• Flow work and the energy of a flowing fluid
• Energy transport by mass
• Energy analysis of steady-flow systems
• Some steady-flow engineering devices
• Nozzles and Diffusers
• Turbines and Compressors
• Throttling valves
• Mixing chambers and Heat exchangers
• Pipe and Duct flow
Lecture Summary