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TRANSCRIPT
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Paper: ASAT-13-PP-12
13th
International Conference on
AEROSPACE SCIENCES & AVIATION TECHNOLOGY,
ASAT- 13, May 26 28, 2009, E-Mail: [email protected]
Military Technical College, Kobry Elkobbah, Cairo, Egypt
Tel : +(202) 24025292 24036138, Fax: +(202) 22621908
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An Investigation on the Internal Flow in Simulated Solid RocketMotor Chamber/Nozzle Configuration
M. Nasr*, A. M. Hegab
**, W. A. El-Askary
*, K. A. Yousif
*
Abstract: This paper describes numerical, analytical and experimental investigation of
acoustic wave propagation in a simulated Solid Rocket Motor (SRM) chamber. The
experimental study is carried out on a square-cylinder cross-sectional channel with two
equally permeable sidewalls. An endwall disturbance is imparted using a moving piston
located at the head end while the exit end of the channel is opened to the atmosphere.
Moreover a convergent and convergent-divergent nozzle is changeable fixed at the exit end of
the channel to study the behavior of the complex wave interactions mechanism at different
nozzle areas. The unsteady, compressible, two dimensional Navier-Stokes equations in a
laminar regime are numerically solved by predictor-corrector MacCormack scheme. Axial
acoustic velocity field generated by the end wall disturbances interacts with steady sidewall
injection to generate rotational flow field through the channel. As a result, a steady vorticity is
generated at the sidewall and then is convected toward the centerline by the transverse
component of the total velocity. Furthermore the time-independent, compressible Navier-
Stokes equations with laminar effects are solved. An analytical solution for pure acoustic flowis derived from the reduced form of the full Navier-Stokes equations. The numerical and
analytical solutions are compared with the experimental data. The comparisons show
reasonable agreement between these three approaches. Moreover, the results show that, the
geometry of the variable area parts has significant effect on the generated complex wave
pattern inside the chamber.
Keywords: Solid Rocket Motor chamber, Permeable sidewalls injection, Internal cavity,
Solid rocket nozzle.
Nomenclaturebn wave number
C'o speed of sound, m/s
Cp specific heat at constant pressure
Cv specific heat at constant volume
Et total energy
H dimensionless channel half-heightH' channel half-height, cm
K thermal conductivity
L dimensionless channel length
*Mechanical Power Engineering Department, Faculty of Engineering, Menoufiya University,
Shebin El-Kom, EGYPT**Mechanical Power Engineering Department, Faculty of Engineering, Menoufiya
University, Shebin El-Kom, EGYPT, Corresponding author: [email protected], Tel.
012-7858517
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L' channel length, cm
M Mach number
n wave number index
P static pressure
Patm atmospheric pressure
P'o stagnation pressure, paP% dimensionless pressure perturbation
Pr Prandtl number
Re Reynolds Number
T temperature
T'o stagnation temperature, K
t time
t'a acoustic time, L'/ C'o
u axial speed
U'o reference axial speed, m/s
v transverse speed
V'inj reference injection speed, m/s
x axial coordinateX' dimension axial coordinate
y transverse coordinate
Greek symbols
ratio of specific heat
aspect ratio
transient axial velocity amplitude
' dynamic viscosity, pa.s
density
'o stagnation density, Kg/m3
frequency
Subscripts
' dimension quantities
o stagnation value
inj injection
1. IntroductionThe current work is devoted to examine the time-dependent flow field in a porous channel
with endwall disturbance to describe the effect of adding convergent and convergent-
divergent area parts at the open end on the complex wave pattern inside the chamber. The
presence of sidewall injection with traveling acoustic waves inside long slender square cross-
sectional channel can lead to a rotational flowfield that are decreed by the system geometry.
These waves can, in turn, interact with the solid boundaries to generate acoustic and vortical
wave resulting in complex flow patterns.
In the hope of elucidating the nature of the resulting flowfield, an experimental investigation
was conducted by Brown et al. [1]. They used nitrogen gas injection through uniformly
sintered bronze plates inside a cylinder chamber. In their facility, acoustic waves are
generated from an external rotary valve that controlled the flow exiting the chamber. Their
results verified the accuracy of the analytical model suggested by Culick [2] for the mean
flowfield and also provided substantial data for the resulting acoustic field. Independently of
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the work given in [1], a novel investigation facility was built by Ma [3] to simulate similar
flow conditions in a rectangular chamber. That experiment employed the sublimation of
carbon dioxide, a process that resembled the combustion of propellant, in generating the CO2
gas to mimic the chamber's transpiring wall. Unfortunately, the work by Ma [3] had
experimental difficulties in measuring acoustic pressure and velocity. The results indicated
that the wave generator produced many non-harmonics waves with many higher fundamentalsthat make the interpretation of the complex mechanism is difficult. Moreover, in that
experiment, Ma [3] didnt verify the occurrence of generating turbulence. Barron et al. [4]
introduced an improvement to Ma's experiment by utilizing a Scotch-yoke mechanism to
replace the slider-crank mechanism. The new mechanism led to higher pressure amplitudes,
pure sinusoidal motion and resulted in acceptable validation between numerical and
experimental results.
Dunlap et al. [5] presented an experimental verification for the cold flow simulation of rocket
chamber flow field based on Culick's analysis [2] of steady state flow. The results of Dunlap
et al. [5] revealed that the inviscid flow field solution gives accurate results as long as the
Reynolds number is sufficiently large to ensure that viscous effects are small compared with
pressure gradients.
Flandro [6] provided an early assessment of the importance of vorticity in acoustic boundary
layer. He studied the impact of a small axial pressure gradient, varying harmonically in time,
on the viscous process occurring adjacent to a surface from which a steady spatially uniform
injection occurs. A linear equation for axial velocity contains a balance of convection,
pressure gradient forces and viscous diffusion. The solution described a shear wave
convecting away from the wall, with amplitude that is damped by viscous effects. Flandro [6]
observed intense, transient vorticity in the boundary layer compared to the weaker steady
vorticity associated with the inviscid, rotational Culick's solution [2].
A mathematical model formulatedby Zhao et al. [7] is used to describe the initiation and
evolution of intense unsteady vorticity in a low Mach number, weakly viscous internal flowsustained by mass addition through the side wall of a long narrow cylinder. The intense
vorticity is formed at walls and is convected into the entire chamber by the steady radial
velocity. The amplitude and the distribution of the vorticity are impacted by weak viscous and
nonlinear effects. It was also demonstrated that there are parameter ranges of Mach number,
Reynolds number and driving frequency for which vorticity is really confined to weakly
viscous acoustic boundary layer, thin compared to the radius of the cylinder but larger than
that obtained by Flandro [6].
Erickson et al. [8] presented analytical study concerning forced gas-dynamic oscillations in
closed, constant diameter cylindrical ducts and ducts whose cross-section area varies axially.
The objective of that work was to determine the effect of duct shape on resulting oscillations
amplitude, wave form, harmonic content, and identify duct shapes that produce largeamplitude oscillations for a given energy content. The results showed that the higher
amplitude pressure oscillations can be forced in horn like shaped ducts as opposed to
cylindrical ducts. Shocks like waveforms existed in constant diameter ducts are caused by the
generation of higher harmonics through efficient non-linear coupling with the fundamental
mode. In contrast, the non-linear coupling between the fundamental mode and its harmonic
was weak in ducts whose cross sectional area varies axially (horn-like ducts). This induces
much lower relative energy content in higher harmonics in that duct and hence decreases the
excitation of harmonics.
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The structure of turbulence in a channel flow with a fully transpired wall has been
investigated experimentally by Deng et al. [9]. The aim of that experiment was to study the
effect of the porous surface boundary conditions on the core flow development and flow
structure in the channel. Air is sucked into the channel through the top honeycomb by high
pressure direct drive blower. It was found that the boundary conditions on the porous surface
are very important to the internal core flow evolution and flow pattern. For a course poroussurface (1/4'' honeycomb), the mean flow differs significantly from classical Culick's solution
[2] and computational results. However, with small pore size (1/8'' honeycomb), the mean
velocity profiles are very close to laminar solution for a considerable downstream length and
that profiles agree well with Culick [2], even though large turbulence intensity was observed.
Hegab [10]presented numerical study that describes the transient flow dynamics generated in
a SRM's chamber model with time-dependent mass injection. The main goal was to
understand the heat transfer and temperature dynamics that accompany the co-existing
acoustic and rotational velocity disturbances. Also the effect of adding variable duct to the
open end on the internal flow-field was considered. The results showed that surprisingly large
transient temperature gradient is presented at the sidewalls and the interior of the channel.
Large gradients at the sidewall imply that there is an unexpectedly heat transfer which mayinfluence the combustion zone above the burning propellant even though the fluid injection is
isothermal. It is observed that the unsteady vorticity across the chamber is sensitive to small
changes in flow dynamics and the maximum amplitude of the vorticity increases as the throat
height is decreased. Also, the time history of pressure amplitude increases as throat height
decreases.
The influence of adding variable area portions to the open end of a circular constant-area tube
on finite amplitude wave deformation and radiation, under resonant conditions was studied
experimentally by Sileem and Nasr [11]. They concluded that, the radiated part of energy
delivered by the piston to the atmosphere depends on the tube end configuration. The noticed
difference between results of the open-end tube and that when variable area portions are
added presumably attributed to the deviation of the natural frequency of the variable areacases from that of the open end tube case.
The internal flow-field forming in the combustion chamber of SRM was analytically studied
by Majdalani et al. [12]. A combined geometric configuration is considered in which a
straight cylinder is connected to a tapered cone and the gases are injected perpendicularly to
the surface. The selection of the injection velocity was followed from the experimental work
of Brown et al. [1]. They concluded that the taper effect is more pronounced as the gases
move away from the head end due to the increasing cross-sectional area. The mean flow
approaches its asymptotic limit in sufficiently long cylinders. It may be worth mentioning that
accurate matching of both numerical and analytical solutions requires that the motor
parameters be chosen within specified limits and the corresponding criteria was shown to be
practical. Similar experimental investigation to that of[12]used for studying the influence ofsolid propellant inclination angle through small-scale cold flow simulation was presented by
Nguyen et al. [13]. The experiments were conducted on a cold gas experimental setup. They
concluded that the sidewall injection angle has significant effect on the internal flow field and
vortex shedding in SRM. For small inclination angles the whole interactions between shear
layer and vortex shedding were decreased and hence decreased the wall vorticity, weaken
pressure wave intensity and oscillation levels. On the contrary, the larger angles enhanced the
influence of wall vortex shedding at the rear end of the chamber, which lead to the increase of
pressure fluctuation levels.
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Hegab and Nasr [14] studied experimentally and numerically the propagation of acoustic
waves (which is generated by oscillating piston) in a long, narrow chamber with endwall
disturbance. Their study includes also, an analytical solution to the two following cases. The
first case is in which straight duct with endwall disturbance at the head end and without
sidewall mass injection. The second case, duct contributes steady sidewall mass injection
from permeable walls and endwall disturbance. They illustrated a reasonable comparisonbetween the experimental, analytical, and the computational results using the two-four
explicit predictor-corrector MaCcormack scheme.
From the mentioned review it is noticed that, the effect of exit geometry on the acoustic
flowfield generated in SRM cavity with/without sidewall mass injection did not take the
sufficient attention. Therefore, the present work focuses on experimental and theoretical
studies for the unsteady flow in a simulated SRM interior cavity. The cavity is represented by
square-cylinder chamber with permeable sidewalls. Moreover, convergent and convergent-
divergent nozzles are changeable installed at the exit end of the channel. The numerical
solution of the laminar, two dimensional, compressible and steady/unsteady Navier-Stokes
equations for the same geometry are considered to validate the experimental work. Also the
analytical solution of the reduced form of Navier-Stokes equations is considered.
2. Experimental SetupThe cavity of SRM is represented by square-cylinder chamber of axial length 44 cm and cross
section height of 2.5 cm. The general arrangement of the experimental set-up layout is shown
in Fig.1. It consists of the following parts: an oscillating piston [2.5 cm diameter and 1.9 cm
stroke] driven by an electric AC motor of YC90S-2 type, 2900 rpm, 1 HP, single phase
electrical input and suitable for variable speed through a pulley-belt system. The number of
revolution of AC motor can be changed (from 3610 rpm to 4774 rpm) by voltage regulator.
The variable speed piston oscillates to generate the acoustic disturbance at one end of the
channel and the other end is open to atmosphere. The square cross-sectional area channel has
permeable sidewalls to inject a guided-steady state flow into the channel. The injected airflows through two similar hoses which connected to two similar injection ducted guided-blade
ducts to obtain uniform injection steady velocity at both sides of the channel. Convergent and
convergent-divergent nozzles are changeably added to the open end of the square cross-
sectional area channel. The detailed dimensions of those parts are given in Table (1). Wall
pressure time histories are recorded at two locations along the channel, where the lower one is
5.5 cm apart from the Top Dead Center (TDC) and the upper one is at 19.5 cm apart from
square cross-sectional area channel end. These pressure histories are measured using
Capacitance Pressure Transducer [model SA, Data Instrument, Action MA01720, USA 0-100
psi, accuracy 1%] connected to Data Acquisition System (DAS) and desktop computer
through a Labview software. The data are recorded in files and plotted as will be shown later.
The uncertainties of the measured pressure shown here are estimated according to the
procedures given by Coleman et al. [15] found to be within 2.5% for a confidence interval of
95.45 %. The reading error of U-tube manometer which is used to measure the injected flow
rate by an orifice meter is 0.25 mm and the total uncertainty of the measured flow rate is
equal to 61.412 10 .
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(16)
(17)
(15)
(13)
(8)
cL
L
2 H
c dL
2 exH 2 thH
10-Distribution board
11- Pressure measuring holes connected
by capacitance pressure transducer
12 To DAS
13- Desktop computer
14- Oscillating piston
15- Pulley-belt system16- AC motor
17- Voltage regulator
18- U-tube manometer
1- Air from atmosphere
2- Reciprocating compressor
3- Air reservoir (volume 500 lit.)
4- Orifice meter
5-Two perforated plates
6- Injection air flow through duct with
guide blades7- Square channel (test duct)
8- Electrical power supply
9- Controlled voltage circuit and
constant voltage power supply device
Fig.1 The experimental test-rig components
Table (1) Detailed dimensions of straight, convergent, and convergent-divergent area
channels.
Part type
Length
(cm)
Exit height,
2H'ex (cm)
Throat height,
2H'th (cm)
Square Duct Constant area 44 2.5 -----------
Convergent Variable area 5 0.65,0.95,1.27 -----------
Convergent- Variable area 14 3,5.78,8.725 0.65,0.95,1.27
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3. Mathematical ModelThe mathematical model is based on solving the unsteady, two dimensional parabolized
Navier-Stokes equations describing both dynamics and acoustic in a perfect gas within a
square-cylinder channel. The gas is initially stationary with a reference-state defined byoP
(the total pressure),o
(the total stagnation density) ando
T (the total temperature). The
associated sound speed is found to be ( / )o o o
C P = , where prime quantities refer to
dimensional values. The characteristic length scales for the axial and transverse variables are
chosen to be the axial length of the channel L and the half-height of the cross section H , respectively. Time is nondimensionalized with respect to the axial acoustic time
a ot L C /= .
The aspect ratio is defined as the ratio of the channel length to the half-height of the
channel, /L H = .The characteristic axial velocity oU is related to the characteristic side-
wall injection velocity of the fluidinj
V through the global mass conservation. The
characteristic axial flow Mach number, Prandtl number and flow Reynolds number are
defined respectively, as follows:
Pro o poM U C C k = / , / = , Re o oU L /=
The governing flow equation can be written in its dimensionless form as follows;
Q F
t x y
+ + = 0 (1)
Where Q, E and F are column vectors given by [16]
t
uQ
v
=
( 1)t
u
pu
uv
u up
+
=
+
, ,
/ Re
= /( )
[ ( 1) ]
Re.Pr
y
yt
M v
uv u
F v p
v p
+
+
The dimensionless form of the equation of state for a perfect gas is;
p T= (2)
The non dimensional form of the total energy is represented by
[ ( ) ] ( 1)2
t v
v
uC + = + (3)
Where, Cv and are the specific heat at constant volume and the specific heat ratio,
respectively.
The velocity and temperature gradients read;
yu
uy
=
, yT
y
=
(4)
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In general >>1, M>1 and Pr=O(1)
In the present work, two solution techniques including numerical as well as analytical
methods are used. They will be discussed in the following subsection.
3.1. Numerical Method
An accurate flow-field time history in SRM chamber can be obtained using finite-differencescheme which shows the evolution of the flow variables in the axial and transverse directions
after many acoustic wave cycles. The present study employs higher-order accuracy difference
equations to minimize the impact of numerical diffusion which was found to affect the results
obtained from the second order explicit MacCormack code, see Hegab [17]. Near the
boundaries, the second order explicit predictor-corrector scheme, developed by MacCormack
[18] is used to descretize the two-dimensional, unsteady, compressible, Navier-Stokes
equations. At the interior points, the Navier-Stokes equations are descretized using the Two-
Four explicit, predictor corrector scheme, developed by Gottlieb and Turkel [19], which is a
fourth-order variant of the fully explicit MacCormack scheme. This method, applied by
Kirkkopru et al. [20], is highly-phase accurate and therefore suitable for describing many
wave cycles and wave interaction problems. Hegab [21] used the same numerical method in
similar problems with good numerical predictions.
3.1.a Boundary ConditionsThere are three kinds of boundary conditions used in this study. The first, case (1) in which
the air is injected uniformly across the sidewalls of the channel and the head end is closed
while the other free end is open to atmosphere. Also, variable area nozzles are changeably
added at the open end. At the head end, x=0 the no slip boundary conditions are applied, u=
v=0. While, at the duct exit, the pressure is taken as an atmospheric pressure and the other
parameters are extrapolated using zero gradient at exit. At the sidewalls, the no slip condition
is applied for the streamwise component of velocity, but the crosswise velocity is taken to be
the injection velocity V'inj. The second, case (2) of the boundary conditions is concerned with
studying the internal flow field when only acoustic waves are generated at the closed end
while the other free end is open to atmosphere. Also variable area nozzles are added to thechannel free end. The same boundary conditions for the case (1) are applied except that; the
no slip condition is applied also to the velocity components at sidewalls, i.e. u=v=0. At the
head end, x=0, the streamwise velocity is considered in the form u= sin (t). In the third,
case (3) of boundary conditions the air is injected uniformly across the sidewall of the
chamber and acoustic waves are generated at the head end while the other free end is open to
atmosphere. The variable area nozzles are also included at the free end. The same boundary
conditions for the case (1) are applied except that; at the head end (x=0), u= sin (t). At the
sidewalls, v'(X', 0) =V'inj and v'(X', 2H') =-V'inj, (v=v'/V'inj, V'inj=0.1273 m/s)
3.2. Analytical Solution
3.2.a Analytical Solution for Case (1)
In this case a steady uniform injection from the sidewalls of square-cylinder channel is
considered. Culick [2] and Hegab [10] showed that the axial velocity distribution is
independent of viscosity when Reynolds number is sufficiently large. Culick [2] derived the
following equations for axial, transverse velocities and static pressure:
o
u ycos[( ) (1 )]
U 2 H
= (5-a)
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inj
v ysin[( ) (1 )]
V 2 H
= (5-b)
2( / )o
o atm
P PL
P P
=
(5-c)
Where Uo is the center line dimensionless velocity at the channel exit, and Po is thedimensionless stagnation pressure at the channel head end.
3.2.b Analytical Solution for Case (2)
In the case (2), endwall disturbance is fitted at the duct head end while the other end is open
to atmosphere. The analytical approach is based on the reduced form of the Navier-Stokes
equations using asymptotic techniques [9, 14 and 20]. The final solution for pressure and
velocity is as follows:
The non resonance acoustic solution for axial velocity is:
2 2 20
( , ) sin 2 ( sin sin )sinn nn
n n
u x t t t b t b xb b
== + %
forbn* (6)
Where bn is the wave number, ( 1/ 2)nb n = + with n as the wave number index, is theforced frequency and bn* is the wave number at resonance conditions. The perturbation
pressure ( , )p x t% can be obtained using the following equation [20]:
( , ) 1 ( , )u x t p x t
t x
=
%%(7)
The boundary condition at the duct head end, x=1 reads p=1. Integrating equation (7) yieldsthe pressure perturbation in the form [20]:
20
2( , ) ( 1)cos (cos cos )cos
n nn
n
p t x x t t b t b xb
== % (8)
The solution for resonance case can be also found in [20] as:
* * *
*
1( , ) sin { sin( ) cos( )}sin( )n n n
n
u x t t b t t b t b xb
= +%
( )** * *( , ) cos( ) ( 1) 2 cos sin cosnn n np x t t x b t b t b t b x = % (9)
Where *nb = and represents the wave amplitude
4. Results and DiscussionsThe present results are classified into three categories. The first category of the results (case
(1)) deals with the steady state internal flow generated by a steady mass addition from the two
sidewalls of the square-cylinder channel (nozzless duct). Moreover, the effect of adding
convergent and convergent-divergent area nozzles to the end of the duct is considered. The
second category of the results (case (2)) considers the same channel with endwall disturbance
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at the head end, while variable area nozzles are added changeably at the channel exit. The last
category (case (3)) deals with the channel as in the second category with the presence of
uniform injected air from permeable sidewalls.
The axial pressure distribution along the chamber wall is shown Fig. 2 for experimental,
numerical and analytical solutions as in case (1). In such case, air is injected uniformly acrossthe sidewalls of the square chamber with 0.1273 /inj
V m s = and the head end is closed while
the other free end is open to atmosphere (nozzless duct). It is noticed that, the static pressure
reaches its maximum value at the closed duct head end at ( / 0X L = ) and graduallydecreases toward the channel exit. The comparison between the numerical and analytical
approaches with the experimental data shows reasonable agreement. In Fig. 3, the axial
velocity distribution across the channel height from the present numerical code, the analytical
solution and the results obtained using the commercial code Fluent [22] at different axial
locations is shown. The development of the velocity profiles is attributed to the mass addition
from the walls as axial distance increases. It is noted that the velocity profiles are found to be
very close to the laminar velocity profiles and symmetrical about the centerline. Consistent
results for Fig. 3 have been shown also in [10]. Figure 4 shows transverse velocity at different
axial locations for the same conditions given in Fig. 3. The numerical and analytical resultsare almost coincides in the all domain, while small deviation occurs near the duct inlet and
exit. This deviation is attributed to the increase in the axial velocity due to the mass
accumulation at aft end and in turn makes the flow to be convected towards downstream as
soon as it is injected from the walls. However, the analytical solution is proved to be the best
choice to simulate such flowfield case when the air is injected uniformly along the sidewall,
like the gasification of propellant in SRMs.
Experimental data
0 0.2 0.4 0.6 0.8 10.1 0.3 0.5 0.7 0.9X' / L'
1.00000
1.00010
1.00020
1.00030
1.00040
1.00050
1.00005
1.00015
1.00025
1.00035
1.00045
P'/P'atm
Numerical 1
Analytical
Fig. 2 Static Pressure distribution along the duct wall for nozzless duct
without acoustic (case (1)).[1-persent code]
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Numerical 2Analytical
0.0
0.2
0.4
0.6
0.8
1.0
0.1
0.3
0.5
0.7
0.9
Y
'/2H'
Numerical 1
0 2 4 61 3 5 7
U' (m/s)
Fig. 3 Transverse axial velocity distribution at different axial locations for
nozzless duct without acoustic (case (1)).[1-persent code, 2-Fluent code]
X=0.25
X=0.5
X=0.75
0.0
0.2
0.4
0.6
0.8
1.0
0.1
0.3
0.5
0.7
0.9
Y'/2H
'
0.0
Analytical
-0.1 0.1-0.15 -0.05 0.05 0.15
v'(m/s)
X=0.95
Fig. 4 Transverse velocity distribution for nozzless channel without acoustic
(case (1)).
The effect of adding convergent area nozzle on the static pressure distribution along the wall
of the channel for case (1) is shown in Fig. 5. The convergent area nozzle has total height at
exit of 2 0.65exH cm = and its converging length about 5 cm. It is appeared that the static
pressure decreases slowly through the channel and then it decreases with strong gradient
through the nozzle due to the flow acceleration in the nozzle. The over-prediction of the
experimental results with numerical may be related to uncertainty of the experimental data.
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L' L'c
H'ex
H'
0.0 0.4 0.80.2 0.6 1.0
X'/L'
1.000
1.001
1.002
1.003
1.004
1.005
P'/P'atm
Experimental
Numerical 1
1.1136
Fig. 5 Static Pressure distribution along the wall of duct ended by convergent
nozzle, 2H'in=2.5 cm, 2H'ex=0.65 cm, L'c=5 cm and V'inj=0.1273 m/s,
(case (1)).
The second set of the results for case (2) discusses the internal flowfield due to endwall
disturbance using reciprocating piston at the head end of the channel along with and without a
convergent nozzle added at the end of the channel. The main purpose of this set is to describe
the effects of forced frequency, axial location and the nozzle geometry on the generated
acoustic field inside the interior cavity. In Figs. 6 and 7, a comparison between the
experimental and numerical results for nozzless duct at the same dimensional flow
characteristics as in Fig. 5 is presented. These Figures demonstrate the pressure time history at
two dimensionless distances from the head end or to be more precise from the top dead center
of the piston ( / 0.125X L = and 0.557 ) and constant dimensionless forced frequency=0.65. It is observed that, there is small deviation in the static pressure mean value and the
phase angle between the experimental and numerical results. Moreover, higher harmonic
oscillations are seen in the experimental data which represents the eigenfunction mode
contributions. The reasons behind these deficiencies may be related to the sudden change of
cross-sectional area from circular duct (in which the piton moves) at the TDC to the squarecross-sectional channel. Moreover, using slider-crank shaft mechanism cant produce a pure
sinusoidal piston motion. Since the piston movement is not purely sinusoidal, many
harmonics are introduced into the acoustic velocity and pressure fields as discussed by
Barron et. al [4]. Furthermore, it is found that, the amplitude of the measured static pressure
oscillation decreases as the axial distance increases downstream. That may be attributed to the
wave attenuation due to the boundary layer development on the duct sidewalls and acoustic
streaming.
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L
2HcL
cR
sinu t =
Numerical 1
0 20 40 60 80 100
t
0.992
0.996
1.000
1.004
1.008
P
'/P
'atm
Experimental
Fig. 6 Pressure-time history for nozzless channel fitted by forced
oscillation, =0.65, =0.045 and X'/L'=0.125 (case (2)).
0 20 40 60 80 100
t
0.992
0.996
1.000
1.004
1.008
P
'/P
'atm
Experimental
Numerical 1
Fig. 7 Pressure-time history for nozzless channel fitted by forced
oscillation, = 0.65, =0.045 and X'/L'=0.557 (case (2)).
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Figure 8 represents a comparison between analytical and numerical solutions for the pressure
time history at =1.1, =0.1, / 0.125X L = and =20. There are small deviations in bothphase and amplitude between the numerical and analytical results. This deviation may be
related to the assumption with the analytical solution that considers an incompressible,
inviscid flow and linear system. Similar trend was found by Hegab [10]. During one complete
cycle of the piston, the acoustic wave completes two round trips across the channel length asdiscussed by Sileem and Nasr [11]. A comparison of the analytical and numerical results near
resonance frequency for pressure time history is presented in Fig. 9 at =1.55, =0.1,
/ 0.557X L = and =20. For t10, the results show good agreement in amplitude and phase
Analytical
0 20 40 60 80 100
t
0.960
1.000
1.040
0.940
0.980
1.020
1.060
P'/P
'atm
Numerical 1
Fig. 8 Pressure-time history for nozzless channel fitted by forced
oscillation, =1.1, X'/L'=0.125, M=0.1 and =0.1 (case (2)).
0 10 20 30 40 50
t
0.6
0.8
1.0
1.2
1.4
0.5
0.7
0.9
1.1
1.3
1.5
P'/P'atm
AnalyticalNumerical 1
Fig. 9 Pressure-time history for nozzless channel fitted by forced
oscillation, =1.55, X'/L'=0.557, M=0.1 and =0.1 ((case (2)).
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between numerical and analytical approaches. While for t>10 the analytical solution shows
linear growth with time rather than beats with the numerical solution. Similar results were
previously noticed by Hegab [21], who discussed this phenomenon and gave interpretation to
this trend as the nonlinearity effect with the numerical solution.
The effect of forced frequency on the axial velocity time history is introduced in Figs. 10 and11. Data are recorded at / 0.125X L = and =0.52 and 0.65, respectively. It is observedthat, increasing the forced frequency leads to an increase of the axial velocity amplitude with
the same phase angle.
0 20 40 60 80 100
t
-0.2
0
0.2
-0.3
-0.1
0.1
0.3
u'/U
'o
AnalyticalNumerical 1
Fig. 10 Axial velocity time-history for nozzless channel fitted by forced
oscillation, =0.52, X'/L'=0.125 and =0.1 (case (2)).
0 20 40 60 80 100
t
-0.2
0
0.2
-0.3
-0.1
0.1
0.3
u'/U
'o
AnalyticalNumerical 1
Fig. 11 Axial velocity time-history for nozzless channel fitted by forced
oscillation, =0.65, X'/L'=0.125 and =0.1 (case (2)).
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Figures 12 and 13, show the acoustic axial velocity across the channel at x=0.25 and 0.5 for
=1.5, M=0.1 and =0.1 at four times t=10, 20, 40 and 78. One can observe the presence of
the acoustic boundary layer development at the same location with different boundary layer
thickness. Rotational flow is considered to be confined in that region. The explanation is
related to the interaction between the duct sidewalls and the acoustic wave motion. Baum [23]
noticed an overshoot of the axial velocity at the edge of acoustic boundary layer and showedthat, acoustic boundary layer thickness and axial velocity overshoot at its edge are strongly
influenced by mean flow Reynolds number and frequency of oscillations.
0.50
0.60
0.70
0.80
0.90
1.00
Y'/
2H
'
t=78
t=40
t=20
-1 0 1 2-0.5 0.5 1.5
u' / U'o
t=10
Fig. 12 Transverse axial velocity distribution for nozzless channel fitted by
forced oscillation, =1.5, X'/L'=0.25 and =0.1 and (case (2)).
0.50
0.60
0.70
0.80
0.90
1.00
Y
'/2H
'
t=78
t=40
t=20
-1 0 1 2-0.5 0.5 1.5u' / U'o
t=10
Fig. 13 Transverse axial velocity distribution for nozzless channel fitted by
forced oscillation, =1.5, X'/L'=0.5 and =0.1 (case (2)).
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The effect of installed convergent and convergent-divergent nozzles at the end of the channel
on the complex wave interaction mechanism inside the chamber is illustrated experimentally
in Figs. 14 and 15, respectively. The angular frequency is taken to be =0.52, and the
convergent nozzle length and total exit height are 5cL cm = , 2 0.65exH cm = , while the
convergent-divergent nozzle length, total throat and exit heights are
14cdL cm = , 2 0.65thH cm = and 2 3exH cm = , respectively. The exit height for the convergentarea nozzle is equal to the throat height of the convergent-divergent area nozzle with an equal
converging length. It is shown that, the static pressure amplitude for channel ended with
nozzles (at x=0.125) has higher amplitude with deviation in the mean value compared to
nozzless duct. It may be attributed to the decreasing of the flow area at the nozzle exit which
leads to a reduction in transmitted energy waves from nozzle exit and hence increases the
interactions between incident and reflected waves from boundaries which in turn increases the
pressure amplitude. The nozzle and nozzless results show higher harmonic oscillations as
discussed by Barron et. al [4].
0 20 40 60 80 100
t
0.992
0.996
1.000
1.004
1.008
P'/P'atm
Nozzless channel
Channel ended by convergent nozzle
Fig. 14 Pressure-time history for channel fitted by forced oscillation ended
by convergent nozzle,(2H'ex=0.65 cm) and nozzless channel
at =0.045, =0.52 and X'/L'=0.125 (case (2)).
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0 20 40 60 80 100
t
0.992
0.996
1.000
1.004
1.008
P'/P'atm
Nozzless channel
Channel ended by convergent-divergent nozzle
Fig. 15 Pressure-time history for channel fitted by forced oscillation endedby convergent-divergent, (2H'th=0.65 cm, 2H'ex=3 cm)and nozzles
channel at X'/L'=0.125, =0.52 and =0.045 (case (2)).
Moreover, the significant difference between the convergent and convergent-divergent nozzle
results is presumably related to the deviation of the natural frequency producing by adding
variable area portions at the end of the duct . Also, it is noticed that, the effect of adding
convergent-divergent nozzle results in higher amplitude in static pressure but still lower
amplitude compared with that of convergent nozzle. Sileem and Nasr [11] and Hegab [10]
have noticed similar trend in their results.
The effect of adding convergent and convergent-divergent nozzle at the open end of thechannel with sidewall mass addition is shown in Fig. 16 for case (3). The sidewall injection
velocity is 0.1273 /inj
V m s = and endwall disturbance at the head end with =0.65. It is
shown that, the steady sidewall injection reduces the pressure amplitude significantly.
(Compare Figs. 15 and 16). It may be explained that, the flow is injected through porous
surface on the duct sidewalls across two parallel perforated plates which act as jet velocity
through the generated flow field and hence attenuate the acoustic energy especially when that
energy is nearly small and the effect of exit from the nozzle doesnt play an explicit role in the
pressure amplitude.
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0 20 40 60 80 100
t
0.992
0.996
1.000
1.004
1.008
P'/P'atm
Channel ended by convergent nozzle
Nozzless channel
Channel ended by convergent-divergent nozzle
Fig. 16 Pressure-time history for nozzless channel, channel ended by convergent
nozzle and convergent-divergent at forced frequency
=0.65, =0.045 and X'/L'=0.125 (case (3)).
The effect of the exit height on the acoustic flowfield generated in the duct ended by
convergent nozzle (without air flow injection) is shown in Fig. 17 for case (2) at
/ ' 0.125X L = , = 0.52 and different exit heights; 2 1.27,0.95exH = and 0.65cm . It is
shown from this figure that, with deceasing the exit height of the convergent nozzle, the
pressure amplitude increases. It is clearly seen by decreasing the exit height causes an
increase in the amount of reflected acoustic energy which in turn interacts with the incident
waves from the piston and hence enhances the pressure amplitude. Figure 18 shows the effect
of throat height on the pressure time history for duct ended with convergent-divergent nozzle.
It is concluded that, at the same forced frequency and axial location, for no air flow injection;
decreasing the throat height increases the pressure amplitude but still smaller than the effect
of adding a convergent nozzle with the same throat heights.
The power spectrum density (PSD) is calculated from the experimental data for case (2) and
is shown in Fig. 19 for nozzless channel and without injection. It is shown that, the gas
oscillates at the same frequency of the piston (79.6 HZ). Higher harmonics of very small
energy content could be noticed before and after the main frequency.
The effect of adding convergent nozzle by different exit heights on the energy content in PSD
is shown in Fig. 20. It is concluded that, decreasing the exit height of the convergent nozzleincreases the amount of reflected waves which in turn increases the wave's interactions and
energy content. Moreover, higher harmonics increases as the exit height of the convergent
nozzle decreases. This is an indication of small wave deformation. This confirms the
aforementioned understanding of the mechanism of wave amplitude increasing, which is
mainly due to off-resonant situation caused by the exit area reduction.
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0 20 40 60 80 100
t
0.992
0.996
1.000
1.004
1.008
P'/P'atm
2H'ex=1.27 cm
2H'ex=0.95 cm
2H'ex=0.65 cm
Fig. 17 Pressure-time history for the channel ended by convergent nozzle at
different exit heights at forced frequency =0.52, =0.045 and
X'/L'=0.125 (case (2)).
0 20 40 60 80 100t
0.992
0.996
1.000
1.004
1.008
P'/P'atm
2H'th=1.27 cm
2H'th=0.65 cm
2H'th=0.95 cm
Fig. 18 Pressure-time history for the channel ended by convergent-divergent
nozzle at different throat heights at forced frequency =0.65, =0.045 and
X'/L'=0.125 (case (2)).
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0 40 80 120 160 200
0
4E-005
8E-005
0.00012
0.00016
0.0002
PSD
Fig. 19 Power spectrum density for nozzless channel at X'/L'=0.125 (case (2)).
0 40 80 120 160 200
0
4E-005
8E-005
0.00012
0.00016
0.0002
P
SD
2H'ex=1.27 cm
2H'ex=0.95 cm
2H'ex=0.65 cm
Fig. 20 Power spectrum density for channel ended by convergent
nozzle at X'/L'=0.125 (case (2)).
PSD for channel ended by convergent-divergent nozzle is shown in Fig. 21. It is obvious that,
installing convergent-divergent nozzle at the channel end increases the energy content of the
wave. Moreover, higher harmonics are clearly seen in this figure. It may be related to energy
dissipation and transfer from the fundamental mode to its higher harmonics. Also the
frequency deviation for the three throat heights may be result from the difference of the
natural frequency between the nozzless channel and channel ended with convergent-divergent
nozzle. Moreover, decreasing the throat height increases the PSD at the same frequency. The
maximum and minimum pressure amplitudes for nozzless channel, channel ended by
convergent nozzles and convergent-divergent nozzles are shown in tables (2), (3) and (4),
respectively.
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0
4E-005
8E-005
0.00012
0.00016
0.0002
PSD
2H'th=1.27 cm
0 40 80 120 160 200
2H'th=0.95 cm
2H'th=0.65 cm
Fig. 21 Power spectrum density for channel ended by convergent-divergent
nozzle at X'/L'=0.125 (case (2)).
Table (2) The maximum and minimum pressure amplitudes for nozzless channel.
Pmin Pmax
0.52 0.9955 1.0029
0.63 0.99515 1.003
0.65 0.99405 1.0032
Table (3) The maximum and minimum pressure amplitudes for channel ended by
convergent nozzle.
2H'ex=1.27 cm 2H'ex=0.95 cm 2H'ex=0.65 cm
Pmin Pmax Pmin Pmax Pmin Pmax
0.52 0.99732 1.0026 0.99612 1.0038 0.99512 1.00425
0.63 0.9953 1.00275 0.99525 1.0039 0.995 1.0049
0.65 0.99517 1.0028 0.99745 1.0033 0.99472 1.00527
Table (4) The maximum and minimum pressure amplitudes for channel ended by
convergent-divergent nozzle.
2H'th=0.65cm
and
2H'ex=3 cm
2H'th=0.95cm
and
2H'ex=5.78 cm
2H'th=1.27 cm
and
2H'ex=8.725 cm
Pmin Pmax Pmin Pmax Pmin Pmax
0.52 0.99599 1.00388 0.9951 1.00382 0.99737 1.0027
0.63 0.99633 1.00498 0.9952 1.0041 0.9955 1.0038
0.65 0.99521 1.0052 0.9956 1.0042 0.99618 1.00395
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5. ConclusionsThe effect of adding convergent and convergent-divergent nozzles at the end of square-
cylinder channel on the internal flow field is studied experimentally, analytically and
numerically. The flow field in the channel is generated by either steady mass addition from
sidewalls and/or endwall disturbance. The following statements could be drawn from the
current study:1. For the considered injection mass rate, the whole flow is found to be subsonic laminar.
2.The flow is highly rotational near walls and it then weakens until reaching the core region
as demonstrated in case (2).
3. The internal acoustic flowfield is highly affected by some parameters such as forced
frequency, boundary conditions treatment and exit area geometry.
4.Adding a convergent nozzle at the end of the channel leads to partially transmitted acoustic
waves at the duct exit and the remained are reflected from the solid walls. The latter increases
when the exit height decreases and hence increasing the wave amplitude.
Finally, the effect of convergent-divergent nozzle existence at the end of the channel shows
wave interaction mechanism, which is completely different than that with either nozzless or
convergent nozzle existence. Moreover, the flow injected through the porous sidewallattenuates the generated acoustic field throughout the channel. These acoustic waves interact
with the steady sidewall injection to generate vorticity across the chamber. The generated
rotational flow may impact the burning rate in the real solid rocket motor propellant.
6. AcknowledgmentThis work is supported by the Science and Technology Development Fund (STDF) through
the project ID-108.
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Paper: ASAT-13-PP-12
[9] Deng, Z., Addrian, R.J, and Tomkinson, C.D.," Structure of Turbulence in Channel
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