Sabtu, 01 Agustus 2009

Termodinamika

Disusun Ulang Oleh:

Arip Nurahman

Pendidikan Fisika, FPMIPA. Universitas Pendidikan Indonesia

&

Follower Open Course Ware at MIT-Harvard University. Cambridge. USA.


Materi kuliah termodinamika ini disusun dari hasil perkuliahan di departemen fisika FPMIPA Universitas Pendidikan Indonesia dengan Dosen:

1. Bpk. Drs. Saeful Karim, M.Si.

2. Bpk. Insan Arif Hidayat, S.Pd., M.Si.

Dan dengan sumber bahan bacaan lebih lanjut dari :

Massachusetts Institute of Technology, Thermodynamics

Professor Z. S. Spakovszk, Ph.D.

Office: 31-265

Phone: 617-253-2196

Email: zolti@mit.edu

Aero-Astro Web: http://mit.edu/aeroastro/people/spakovszky

Gas Turbine Laboratory: home

2.5 Control volume form of the conservation laws

[VWB&S, 6.1, 6.2]

The thermodynamic laws (as well as Newton's laws) are for a system, a specific quantity of matter. More often, in propulsion and power problems, we are interested in what happens in a fixed volume, for example a rocket motor or a jet engine through which mass is flowing at a certain rate. We may also be interested in the rates of heat and work into and out of a system. For this reason, the control volume form of the system laws is of great importance. A schematic of the difference is shown in Figure 2.8. Rather than focus on a particle of mass which moves through the engine, it is more convenient to focus on the volume occupied by the engine. This requires us to use the control volume form of the thermodynamic laws, developed below.

Figure 2.8: Control volume and system for flow through a propulsion device
Image fig0ControlVolume_web

2.5.1 Conservation of mass

For the control volume shown, the rate of change of mass inside the volume is given by the difference between the mass flow rate in and the mass flow rate out. For a single flow coming in and a single flow coming out this is

$\displaystyle \frac{dm_{\textrm{cv}}}{dt} = \dot{m}_{\textrm{in}} - \dot{m}_{\textrm{out}}$

If the mass inside the control volume changes with time it is because some mass is added or some is taken out. In the special case of a steady flow, $ d/dt =0$ , therefore
$\displaystyle \dot{m}_{\textrm{in}} =\dot{m}_{\textrm{out}} = \dot{m}.$

Figure 2.9: A control volume used to track mass flows
Image fig5CtrlVolume_web

2.5.2 Conservation of energy

The first law of thermodynamics can be written as a rate equation:

$\displaystyle \frac{dE}{dt}=\dot{Q}-\dot{W},$

where
$\displaystyle \dot{Q}$ $\displaystyle = \lim_{dt\rightarrow 0}\left(\frac{\delta Q}{dt}\right)\qquad \textrm{rate of total heat transfer to the system}$
$\displaystyle \dot{W}$ $\displaystyle = \lim_{dt\rightarrow 0}\left(\frac{\delta W}{dt}\right)\qquad \textrm{rate of total work done by the system}.$

To derive the first law as a rate equation for a control volume we proceed as with the mass conservation equation. The physical idea is that any rate of change of energy in the control volume must be caused by the rates of energy flow into or out of the volume. The heat transfer and the work are already included and the only other contribution must be associated with the mass flow in and out, which carries energy with it. Figure 2.10 shows two schematics of this idea. The desired form of the equation will be

$\displaystyle \left(\textrm{rate of change of }\textrm{energy in cv}\right)$ $\displaystyle = \left(\textrm{rate of heat }\textrm{added to C.V.}\right) -\lef... ...o C.V.}\right) -\left(\textrm{rate of energy flow }\textrm{out of C.V.}\right).$

Figure 2.10: Schematic diagrams illustrating terms in the energy equation for a simple and a more general control volume
[Simple] Image fig5CtrlVolumeCandleAndShaft_web [More General] Image fig0ControlVolumeComplicatedSFEE_web

The fluid that enters or leaves has an amount of energy per unit mass given by

$\displaystyle e=u+c^2/2+gz,$

where $ c$ is the fluid velocity relative to some coordinate system, and we have neglected chemical energy. In addition, whenever fluid enters or leaves a control volume there is a work term associated with the entry or exit. We saw this in Section 2.3, example 1, and the present derivation is essentially an application of the ideas presented there. Flow exiting at station ``e'' must push back the surrounding fluid, doing work on it. Flow entering the volume at station ``i'' is pushed on by, and receives work from the surrounding air. The rate of flow work at exit is given by the product of the pressure times the exit area times the rate at which the external flow is ``pushed back.'' The latter, however, is equal to the volume per unit mass times the rate of mass flow. Put another way, in a time $ dt$ , the work done on the surroundings by the flow at the exit station is

$\displaystyle dW_{\textrm{flow}}=p v dm_e.$

The net rate of flow work is

$\displaystyle \dot{W}_{\textrm{flow}} = p_e v_e \dot{m}_e - p_i v_i \dot{m}_i.$

Including all possible energy flows (heat, shaft work, shear work, piston work, etc.), the first law can then be written as:

$\displaystyle \frac{d}{dt}\sum{E_{\textrm{cv}}}=\sum\dot{Q}_{\textrm{cv}}+\sum\... ...iston}}+ \sum\dot{W}_{\textrm{flow}}+\sum\dot{m}\left(u+\frac{c^2}{2}+gz\right)$

where $ \sum$ includes the sign associated with the energy flow. If heat is added or work is done on the system then the sign is positive, if work or heat are extracted from the system then the sign is negative. NOTE: this is consistent with $ \Delta E = Q-W$ , where $ W$ is the work done by the system on the environment, thus work is flowing out of the system.

We can then combine the specific internal energy term, $ u$ , in $ e$ and the specific flow work term, $ pv$ , to make the enthalpy appear:

\begin{multline*} \textrm{Total energy associated with mass flow:} e + pv = u + c^2/2 + gz + pv = h + c^2 /2 + gz. \end{multline*}

Thus, the first law can be written as:

$\displaystyle \frac{d}{dt}\sum{E_{\textrm{cv}}}=\sum\dot{Q}_{\textrm{cv}}+\sum\... ...ar}}+\sum\dot{W}_{\textrm{piston}}+ \sum\dot{m}\left(h+\frac{c^2}{2}+gz\right).$

For most of the applications in this course, there will be no shear work and no piston work. Hence, the first law for a control volume will be most often used as:

$\displaystyle \frac{dE_{\textrm{cv}}}{dt}=\dot{Q}_{\textrm{cv}}-\dot{W}_{\textr... ..._i+\frac{c_i^2}{2}+gz_i\right)- \dot{m}_e\left(h_e+\frac{c_e^2}{2}+gz_e\right).$ (2..10)

Note how our use of enthalpy has simplified the rate of work term. In writing the control volume form of the equation we have assumed only one entering and one leaving stream, but this could be generalized to any number of inlet and exit streams.

In the special case of a steady-state flow,

$\displaystyle \frac{d}{dt} =0 \qquad \textrm{and} \qquad \dot{m}_i=\dot{m}_e = \dot{m}.$

Applying this to Equation 2.10 produces a form of the ``Steady Flow Energy Equation'' (SFEE),
$\displaystyle \dot{Q}_{\textrm{cv}} - \dot{W}_{\textrm{cv}} = \dot{m}\left[\left(h_e+\frac{c_e^2}{2}+gz_e\right)-\left(h_i+\frac{c_i^2}{2}+gz_i\right)\right],$ (2..11)

which has units of Joules per second. We could also divide by the mass flow to produce
$\displaystyle q_{\textrm{cv}} - w_{\textrm{cv}} = \left(h_e+\frac{c_e^2}{2}+gz_e\right)-\left(h_i+\frac{c_i^2}{2}+gz_i\right),$

which has units of Joules per second per kilogram. For problems of interest in aerospace applications the velocities are high and the term that is associated with changes in the elevation is small. From now on, we will neglect the $ gz$ terms unless explicitly stated.





Muddy Points

What is shaft work? (MP 2.5)

What distinguishes shaft work from other works? (MP 2.6)

Definition of a control volume (MP 2.7)


2.5.3 Stagnation Temperature and Stagnation Enthalpy

Suppose that our steady flow control volume is a set of streamlines describing the flow up to the nose of a blunt object, as in Figure 2.11.

Figure 2.11: Streamlines and a stagnation region; a control volume can be drawn between the dashed streamlines and points 1 and 2
Image fig5StagLine_web

The streamlines are stationary in space, so there is no external work done on the fluid as it flows. If there is also no heat transferred to the flow (adiabatic), then the steady flow energy equation becomes

$\displaystyle c_pT_2 + \frac{c_2^2}{2} = c_pT_1 + \frac{c_1^2}{2}.$

The quantity that is conserved is defined as the stagnation temperature,

$\displaystyle T_t$ $\displaystyle \equiv T + \frac{c^2}{2c_p}$

or


$\displaystyle \frac{T_t}{T}$ $\displaystyle = 1+ \frac{\gamma-1}{2}M^2 \qquad \textrm{using } a= \sqrt{\gamma RT},$

where $ M = c / a$ is the Mach number2.5. The stagnation temperature is the temperature that the fluid would reach if it were brought to zero speed by a steady adiabatic process with no external work. Note that for any steady, adiabatic flow with no external work, the stagnation temperature is constant.

It is also convenient to define the stagnation enthalpy,

$\displaystyle h_t = c_pT + \frac{c^2}{2}$

which allows us to write the Steady Flow Energy Equation in a simpler form as
$\displaystyle q_{\textrm{1-2}}-w_{\textrm{s,1-2}}=h_{t2}-h_{t1}.$

Note that for a quasi-static adiabatic process
$\displaystyle \frac{T_1}{T_2} =\left(\frac{p_1}{p_2}\right)^{\frac{\gamma-1}{\gamma}}$

so we can write
$\displaystyle \frac{T_t}{T} = \left(\frac{p_t}{p}\right)^{\frac{\gamma-1}{\gamma}}$

and define the relationship between stagnation pressure and static pressure as
$\displaystyle \frac{p_t}{p} \equiv \left(1 + \frac{\gamma-1}{2}M^2\right)^{\frac{\gamma}{\gamma-1}},$

where, the stagnation pressure is the pressure that the fluid would reach if it were brought to zero speed, via a steady, adiabatic, quasi-static process with no external work.

2.5.3.1 Frame dependence of stagnation quantities

An area of common confusion is the frame dependence of stagnation quantities. The stagnation temperature and stagnation pressure are the conditions the fluid would reach if it were brought to zero speed relative to some reference frame, via a steady adiabatic process with no external work (for stagnation temperature) or a steady, adiabatic, reversible process with no external work (for stagnation pressure). Depending on the speed of the reference frame the stagnation quantities will take on different values.

For example, consider a high speed reentry vehicle traveling through the still atmosphere, which is at temperature, $ T$ . Let's place our reference frame on the vehicle and stagnate a fluid particle on the nose of the vehicle (carrying it along with the vehicle and thus essentially giving it kinetic energy). The stagnation temperature of the air in the vehicle frame is

$\displaystyle T_t = T + \frac{c^2}{2 c_p}$

where $ c$ is the vehicle speed. The temperature the skin reaches (to first approximation) is the stagnation temperature and depends on the speed of the vehicle. Since re-entry vehicles travel fast, the skin temperature is much hotter than the atmospheric temperature. The atmospheric temperature, $ T$ , is not frame dependent, but the stagnation temperature, $ T_t$ , is.

The confusion comes about because $ T$ is usually referred to as the static temperature. In common language this has a similar meaning as ``stagnation,'' but in fluid mechanics and thermodynamics static is used to label the thermodynamic properties of the gas ($ p$ , $ T$ , etc.), and these are not frame dependent.

Thus in our re-entry vehicle example, looking at the still atmosphere from the vehicle frame we see a stagnation temperature hotter than the atmospheric (static) temperature. If we look at the same still atmosphere from a stationary frame, the stagnation temperature is the same as the static temperature.

2.5.3.2 Example

For the case shown below, a jet engine is sitting motionless on the ground prior to take-off. Air is entrained into the engine by the compressor. The inlet can be assumed to be frictionless and adiabatic.

Figure 2.12: A stationary gas turbine drawing air in from the atmosphere
Image fig5GasTurb_web

Considering the state of the gas within the inlet, prior to passage into the compressor, as state (1), and working in the reference frame of the motionless airplane:

  1. Is $ T_{t1}$ greater than, less than, or equal to $ T_{\textrm{atm}}$ ?

    The stagnation temperature of the atmosphere, $ T_{\textrm{t,atm}}$ , is equal to $ T_{\textrm{atm}}$ since it is moving the same speed as the reference frame (the motionless airplane). The steady flow energy equation tells us that if there is no heat or shaft work (the case for our adiabatic inlet) the stagnation enthalpy (and thus stagnation temperature for constant $ C_p$ ) remains unchanged. Thus $ T_{\textrm{t1}}= T_{\textrm{t,atm}} = T_{\textrm{atm}}$

  2. Is $ T_1$ greater than, less than, or equal to $ T_{\textrm{atm}}$ ?

    If $ T_{\textrm{t1}}= T_{\textrm{atm}}$ then $ p_{\textrm{atm}}$ ?

    Equal, by the same argument as 1.

  3. Is $ p_1$ greater than, less than, or equal to $ p_{\textrm{atm}}$ ?

    Less than, by the same argument as 2.

2.5.3.3 Steady Flow Energy Equation in terms of Stagnation Enthalpy

The form of the ``Steady Flow Energy Equation'' (SFEE) that we will most commonly use is Equation 2.11 written in terms of stagnation quantities, and neglecting chemical and potential energies,

$\displaystyle \textrm{Steady Flow Energy Equation: }\qquad\dot{Q}_{\textrm{cv}} - \dot{W}_{\textrm{shaft}}= \dot{m}(h_{te} - h_{ti}).$

The steady flow energy equation finds much use in the analysis of power and propulsion devices and other fluid machinery. Note the prominent role of enthalpy.





Muddy Points

What is the difference between enthalpy and stagnation enthalpy? (MP 2.8)

2.5.4 Example Applications of the First Law of Thermodynamics

[VW, S& B: 6.4]


2.5.4.1 Tank Filling

Using what we have just learned we can attack the tank filling problem solved in Section 2.3.3 from an alternate point of view using the control volume form of the first law. In this problem the shaft work is zero, and the heat transfer, kinetic energy changes, and potential energy changes are neglected. In addition there is no exit mass flow.

Figure 2.13: A control volume approach to the tank filling problem
Image fig0ControlVolumeTankFilling_web

The control volume form of the first law is therefore

$\displaystyle \frac{dU}{dt}=\dot{m}_i h_i.$

The equation of mass conservation is

$\displaystyle \frac{dm}{dt}=\dot{m}_i.$

Combining we have

$\displaystyle \frac{dU}{dt}=\frac{dm}{dt}h_i.$

Integrating from the initial time to the final time (the incoming enthalpy is constant) and using $ U=mu$ gives the result $ u_{\textrm{final}} = h_i = h_0$ as before.

2.5.4.2 Flow through a rocket nozzle

A liquid bi-propellant rocket consists of a thrust chamber and nozzle and some means for forcing the liquid propellants into the chamber where they react, converting chemical energy to thermal energy.

Figure 2.14: Flow through a rocket nozzle
Image fig5Rocket_web

Once the rocket is operating we can assume that all of the flow processes are steady, so it is appropriate to use the steady flow energy equation. Also, for now we will assume that the gas behaves as a perfect gas with constant specific heats, though in general this is a poor approximation. There is no external work, and we assume that the flow is adiabatic. We define our control volume as going between location $ c$ , in the chamber, and location $ e$ , at the exit, and then write the First Law as

$\displaystyle q_{\textrm{c-e}}-w_{\textrm{s,c-e}}=h_{te}-h_{tc} \qquad \textrm{which becomes} \qquad h_{te} = h_{tc}$

or
$\displaystyle c_p T_c+ \frac{c_c^2}{2} = c_p T_e + \frac{c_e^2}{2},$

Therefore
$\displaystyle c_e= \sqrt{2 c_p (T_c-T_e)}.$

If we assume quasi-static, adiabatic expansion then
$\displaystyle \frac{T_e}{T_c} = \left(\frac{p_e}{p_c}\right)^{\frac{\gamma-1}{\gamma}}$

so
$\displaystyle c_e = \sqrt{2 c_p T_c \left[1 - \left(\frac{p_e}{p_c}\right)^{\frac{\gamma-1}{\gamma}}\right]}.$

$ T_c$ and $ p_c$ , the conditions in the combustion chamber, are set by propellants, and $ p_e$ is the external static pressure.

2.5.4.3 Power to drive a gas turbine compressor

Consider for example the PW4084 pictured in Figure 2.15. The engine is designed to produce about 84,000 lbs of thrust at takeoff. The engine is a two-spool design. The fan and low pressure compressor are driven by the low pressure turbine. The high pressure compressor is driven by the high pressure turbine. We wish to find the total shaft work required to drive the compression system.

Figure 2.15: The Pratt and Whitney 4084 (drawing courtesy of Pratt and Whitney)
Image fig5PW4084_web

$\displaystyle \pi_f$ $\displaystyle = \textrm{total pressure ratio across the fan}$ $\displaystyle \approx 1.4$
$\displaystyle \pi_c$ $\displaystyle = \textrm{total pressure ratio across the fan + compressor}$ $\displaystyle \approx 45$
$\displaystyle \dot{m}_f$ $\displaystyle = 610\textrm{ kg/s}$
$\displaystyle \dot{m}_{\textrm{core}}$ $\displaystyle = 120\textrm{ kg/s}$
$\displaystyle T_{\textrm{inlet}}$ $\displaystyle = 300\textrm{ K}.$

We define our control volume to encompass the compression system, from the front of the fan to the back of the fan and high pressure compressor, with the shaft cutting through the back side of the control volume. Heat transfer from the gas streams is negligible, so we write the First Law (steady flow energy equation) as:
$\displaystyle \cancelto{0}{\dot{Q}}-\dot{W}_s = \dot{m}(h_{t2}-h_{t1}).$

For this problem we must consider two streams, the fan stream, $ f$ , and the core stream, $ c$ :
$\displaystyle -\dot{W}_s$ $\displaystyle = \dot{m}_f \Delta h_{t,f} + \dot{m}_c \Delta h_{t,c}$

$\displaystyle = \dot{m}_f c_p \Delta T_{t,f} + \dot{m}_c c_p \Delta T_{t,c}$

We obtain the temperature change by assuming that the compression process is quasi-static and adiabatic,
$\displaystyle \frac{T_2}{T_1} = \left(\frac{p_2}{p_1}\right)^{\frac{\gamma-1}{\gamma}}$

then
$\displaystyle \left(\frac{T_{t2}}{T_{t1}}\right)_{\textrm{fan}} = \pi_f^{\frac{\gamma-1}{\gamma}}=1.1 \Rightarrow \Delta T_{t,\textrm{fan}}=30\textrm{ K}$

$\displaystyle \left(\frac{T_{t2}}{T_{t1}}\right)_{\textrm{core}} = \pi_{\textrm... ...ac{\gamma-1}{\gamma}}=3.0 \Rightarrow \Delta T_{t,\textrm{core}}=600\textrm{ K}$

Substituting these values into the expression for the first law above, along with estimates of $ c_p$ , we obtain
$\displaystyle -\dot{W}_s$ $\displaystyle = 610\textrm{ kg/s} \times 30\textrm{ K}\times 1008\textrm{ J/kg-K} + 120\textrm{ kg/s}\times600\textrm{ K}\times 1008\textrm{ J/kg-K}$

$\displaystyle =-91\times 10^6 \textrm{ J/s}$

$\displaystyle =-91 \textrm{ Megawatts} \qquad \textrm{negative sign implies work done on the fluid}$

Note that $ 1\textrm{ Hp} = 745\textrm{ watts}$ . If a car engine has $ \approx 110\textrm{ Hp} = 8.2\times10^4\textrm{ watts}$ , then the power needed to drive compressor is equivalent to 1,110 automobile engines. All of this power is generated by the low pressure and high pressure turbines.


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Kepada Para Dosen di MIT dan Dosen Fisika FPMIPA Universitas Pendidikan Indonesia

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