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RESEARCH ARTICLE
In situ LIF temperature measurements in aqueous ammoniumchloride solution during uni-directional solidification
M. Behshad Shafii • Chee L. Lum •
Manoochehr M. Koochesfahani
Received: 12 June 2009 / Revised: 16 September 2009 / Accepted: 24 September 2009 / Published online: 14 October 2009
� Springer-Verlag 2009
Abstract We present in situ whole-field measurements of
the temperature field using laser-induced fluorescence in a
study of bottom-chilled uni-directional solidification of
aqueous ammonium chloride. We utilize a two-color, two-
dye, ratiometric approach to address the significant spatial
and temporal variations of laser sheet intensity field due to
refractive index variations caused by the evolving con-
centration and temperature fields. In our work we take
advantage of two temperature sensitive fluorescent dyes
with opposite temperature sensitivities in order to increase
the overall sensitivity and temperature resolution of the
measurements. The resulting temperature sensitivity (about
4% K-1) is more than a factor of two higher than the
original work of Sakakibara and Adrian (Exp Fluids 26:7–
15, 1999) with a sensitivity 1.7% K-1. In situ measure-
ments of the temperature field during solidification are
presented, along with temperature characteristics of some
of the complex flow features, such as plumes and fingers.
1 Introduction
A wide variety of products are now made of metal alloys
such as automobile engine blocks and the compressor and
turbine section of an aircraft engine. The major issues for
these alloys are melt-related defects and inhomogeneities
such as segregation defects and freckles formed during the
solidification process. The solidification process of a binary
melt is influenced by fluid motion in the liquid, whose
flow pattern strongly depends on both thermal and solutal
buoyancy forces. Studies of these multiphase transport
phenomena include stability and numerical analyses of the
coupled nonlinear governing equations based on simplifying
assumptions, exemplified by works such as Heinrich et al.
(1989), Worster (1991), Neilson and Incropera (1991),
Worster (1992), Schneider and Beckermann (1995), Schulze
and Worster (1998) and Feltham and Worster (1999).
An experimental approach to studying the solidification
of metallic alloys has been the use of transparent analogs of
metallic alloys. A popular analog is the binary aqueous
ammonium chloride (NH4Cl-H2O) system which has pro-
ven to be useful for flow visualization and morphological
studies and has been utilized by many researchers because
of its convenient solidification temperature and similar
behavior to metallic alloys (e.g., Chen and Chen 1991;
Magirl and Incropera 1993; Beckerman and Wang 1996;
Liu and Hellawell 1999). Previous studies indicate that
convective phenomena associated with solidification of
aqueous ammonium chloride solution cover a large range
of length scales that evolve dynamically. These features
include the vertical growth of a solid/liquid interface along
with the development of numerous fine structures of salt
fingers, followed by the appearance of a number of plumes
ejecting water-rich fluid jets from channels in the mushy
zone of the growing dendritic crystal mass.
M. B. Shafii � C. L. Lum � M. M. Koochesfahani (&)
Department of Mechanical Engineering,
Michigan State University, East Lansing,
MI 48824, USA
e-mail: [email protected]
Present Address:M. B. Shafii
Mechanical Engineering Department,
Sharif University of Technology,
Azadi St., 14588-89694 Tehran, Iran
Present Address:C. L. Lum
BD Medical, Franklin Lakes,
NJ 07417, USA
123
Exp Fluids (2010) 48:651–662
DOI 10.1007/s00348-009-0758-7
The general features described above are illustrated in
Fig. 1 for the specific geometry that is the subject of the
current study. This figure depicts a shadowgraph visuali-
zation of the solidification process in a hypereutectic (26%
by weight; 26% w) ammonium chloride (NH4Cl) solution
within a rectangular container at room temperature whose
base plate is cooled to -14�C to impose a vertical tem-
perature gradient and initiate uni-directional solidification
(Lum et al. 2001; Lum 2001). The details of the experi-
mental setup will be provided later in this paper. The
cooling of the base plate starts at time zero and small-scale
features, termed ‘‘fingers’’, begin to form at about 4 min.
As the cooling of fluid continues, more ascending water-
rich fingers develop due to a need to reject more solute
during the crystallization process. This is accompanied by a
stronger convection and the fingers are discernible all the
way to the top of the test section (see image at 10 min).
The large Lewis number of aqueous ammonium chloride
helps in maintaining the identity of the water-rich fingers
(Lewis number is defined by Le = a/D, where a and D are
thermal and mass diffusivity, respectively). During the
initial stages of cooling, rapid formation of ammonium
chloride crystals occurs which settle to form the mushy
layer. As time progresses, well-defined chimney-like
structures begin to form which provide outlets from the
mush for rejecting lighter fluid into the surroundings
through ascending water-rich plumes. The small fingers in
the earlier stages die down as more plumes develop.
Since the thermal buoyancy force is one of the main
forces that plays an essential role in uni-directional solid-
ification, it is important to characterize the in situ tem-
perature distribution during the solidification process.
Unfortunately, there exist very little non-intrusive quanti-
tative experimental data on the in situ temperature field
during the solidification process of ammonium chloride.
Previous measurements include thermocouple measure-
ments of temperature histories in the test container (Magirl
and Incropera 1993) and at the container side wall (Wirtz
et al. 1998). Non-intrusive measurements with thermo-
chromic liquid crystal paints (TLC) have also been repor-
ted on the surface of a Hele-Shaw test cell (Solomon and
Hartley 1998). Any inference on the temperature in the
interior was indirect and based on the assumption of rapid
diffusion of heat across the narrow gap of the test cell. The
use of encapsulated TLC particles (10–15 lm in diameter)
has been reported by Nishimura et al. (1992) and Ni-
shimura and Wakamatsu (2000) for generating qualitative
temperature maps based on the color change of TLC; the
quantitative temperature distributions were measured by
thermocouples, however. We also note that TLC tends to
give a high temperature resolution, but over a rather narrow
temperature range, e.g., 2.5�C range in Nishimura et al.
(1992).
Motivated by the discussion above, we present here in
situ whole-field measurements of the temperature field
using laser-induced fluorescence (LIF) in a study of bot-
tom-chilled uni-directional solidification process of aque-
ous ammonium chloride. This work was first reported
briefly by Shafii and Koochesfahani (2003) and extensive
details can be found in Shafii (2005). In our work we have
employed a two-color, two-dye, ratiometric approach to
address the significant spatial and temporal variations of
laser sheet intensity field due to refractive index variations
10 minutes
50 minutes
90 minutes 70 minutes
30 minutes
4 minutes
10 mm
nucleator base plate
Fig. 1 Shadowgraph visualization of the unidirectional cooling of
ammonium chloride at different times during the solidification
process (Lum 2001). The entire test section is shown. Cooling is
from the bottom and the growth of the solidification front is
highlighted by the increasing thickness of the (black) mushy zone
652 Exp Fluids (2010) 48:651–662
123
caused by the evolving concentration and temperature
fields. The traditional approach uses a temperature sensi-
tive dye along with another with little temperature sensi-
tivity (e.g., see Sakakibara and Adrian 1999). In our work,
however, we take advantage of two temperature sensitive
fluorescent dyes, with opposite temperature sensitivities
(Fluorescein and Kiton Red, at 514.5 nm excitation), in
order to increase the overall sensitivity and temperature
resolution of our measurements. An approach of this type
has also been recently reported by Sutton et al. (2008)
using other dye pairs for the 532-nm excitation of Nd-YAG
laser. Another distinction in our study is that we focus on a
‘‘cold’’ application of LIF with temperatures below ambi-
ent, whereas most previous studies have addressed heated
fluid measurements with temperatures above ambient.
In the following sections the LIF technique for mea-
suring temperature is briefly described, along with a dis-
cussion of our dye selection, calibration, and further details
of implementation. The experimental test facility and the
procedure for creating the uni-directional solidification of
ammonium chloride are given next. Finally, sample mea-
surement results are provided in terms of in situ quantita-
tive temperature maps at different times during the
solidification process, along with characterization of tem-
perature profiles at selected locations in the test section.
2 Temperature measurement using laser induced
fluorescence (LIF)
The use of LIF in fluid flows takes advantage of the fact that,
for dilute solutions and unsaturated laser excitation energies,
the fluorescence emission intensity I at a given point is given
by I ¼ AIiCeU; where A is a parameter representing the
detection collection efficiency, Ii the local incident laser
intensity, C the concentration of the dye, e the absorption
coefficient, and U the photoluminescence quantum effi-
ciency. For some molecules, the absorption coefficient e
and/or the quantum efficiency U are temperature dependant,
allowing the measurement of the emission intensity of tracer
molecules to be used to quantify the temperature field in
a fluid flow. The temperature sensitive fluorescent dye,
Rhodamine B, has been one of the most common tracers
used in various applications (see e.g., Sakakibara et al. 1993;
Sato et al. 1997; Coppeta and Rogers 1998; Sakakibara and
Adrian 1999, 2004; Lemoine et al. 1999; Coolen et al. 1999;
Kim and Kihm 2001; Lavieille et al. 2001; Saeki and Hart
2001; Kim et al. 2003). Comparative studies of commonly
used fluorescent dyes in liquids can be found in Coppeta and
Rogers (1998) and Saeki and Hart (2001).
In its simplest form of implementation, the emission
from a single fluorescent dye, over a single spectral band,
can be used to measure the temperature field (e.g., Lemoine
et al. 1999). The difficulty in this case is that any spatial
and temporal variations in the local incident laser intensity
need to be separately accounted for, something that is
impossible to do if the variations are caused by the flow
itself. A good example is the solidification process which is
the focus of our investigation. This flow is characterized by
variable temperature and concentration fields that cause a
variable index of refraction field within the flow, causing
the incident laser intensity field within the flow to vary in
time and space. Figure 2 illustrates the recorded fluores-
cence intensity, before and during solidification, from a
region in the test section that is illuminated by a laser sheet.
The smoothly varying intensity field before the start of
solidification, which is characteristic of the spatial intensity
distribution of the laser sheet, develops significant
‘‘streaks’’ after the start of the solidification process. The
strengths and positions of these streaks change with time.
A common method to eliminate the effect of in situ
variations of incident laser intensity is to use a ratiometric
approach. In the two-color, single-dye, approach, emission
from two different spectral bands with different temperature
sensitivities are utilized (see Lavieille et al. 2001). A three-
color approach, using emission from three different spectral
Fig. 2 Fluorescence intensity over an imaged area, a before solidification and b during solidification
Exp Fluids (2010) 48:651–662 653
123
bands, has also been reported for measurements with large
optical paths (Lavieille et al. 2004). The most popular
method, however, has been the two-color, two-dye, approach
where two dyes with different temperature sensitivities are
employed (e.g., Coppeta and Rogers 1998; Sakakibara and
Adrian 1999, 2004; Kim and Kihm 2001; Kim et al. 2003).
The details of this approach are given in the cited references
and will not be repeated here. Briefly, however, for fixed
concentrations of a mixture of two fluorescent dyes the
fluorescence intensity ratio R of the two dyes is cast in the
form R � I1=I2 ¼ K � FðTÞ: In this expression, I1 and I2 are
the fluorescence intensities emitted by the two dyes, K is a
constant that contains information about the specific exper-
imental setup (i.e., dye concentrations and optical detection
parameters), and F(T) represents the overall temperature
response function that is connected to the temperature
dependence of the absorption coefficients and quantum
efficiencies of the two dyes. An experimental calibration is
used to establish the fluorescence intensity ratio referenced
to its value at a reference temperature To, i.e., R(T)/R(To), as
the primary calibration curve that is used to measure the fluid
temperature. The following section provides details on the
selection of the fluorescent dyes used in this study and the
calibration of the temperature response curve.
2.1 Dye selection and calibration
The most common fluorescent dyes used in the two-color,
two-dye, ratiometric method are the temperature sensitive
Rhodamine B and the nearly temperature insensitive
Rhodamine 110. The overall temperature sensitivity of this
dye pair is 1.6–1.7% K-1 (Sakakibara and Adrian 1999). In
our investigation, the vertical temperature variation in the
liquid melt is about 20�C, but the transverse temperature
variation across fingers and plumes is expected to be much
smaller and on the order 2�C. It is, therefore, desirable to
improve the temperature sensitivity of the fluorescent dye
pair. To accomplish this, we take advantage of two tem-
perature sensitive dyes, one with positive and the other
with negative temperature sensitivities. Most fluorescent
molecules, however, have a negative temperature sensi-
tivity, i.e., fluorescence intensity decreases with increasing
temperature. Fluorescein (disodium fluorescein), on the
other hand, has a positive temperature sensitivity when
excited at 514.5 nm (green line of argon-ion laser) due to
the increase with temperature of its absorption at this
wavelength (Coppeta and Rogers 1998). The second dye
was selected to be Kiton Red because its absorption and
emission spectra are red-shifted in comparison with Rho-
damine B and this reduces the spectral conflicts in the two-
dye approach.
The relative absorption and emission spectra of Fluo-
rescein and Kiton Red are depicted in Fig. 3. To minimize
spectral conflicts during detection, appropriate spectral
bands were selected using two optical filters (Edmond
Optics). Fluorescein’s fluorescence was captured over
the wavelength range 535–545 nm (optical filter with full-
width half-maximum FWHM of 10, 540 nm center wave-
length), with minimal influence from Kiton Red’s emission.
The fluorescence emission of Kiton Red was captured by a
long pass filter over wavelengths greater than 600 nm, little
affected by fluorescein’s emission. The negligible leakage
through the filters was confirmed by preparing the Fluo-
rescein solution and measuring its emission by the fluo-
rescein camera, followed by introducing the Kiton Red dye
into the solution and measuring the emission intensity
again. The results showed the intensity change was about
0.1%, indicating there was negligible leakage through the
fluorescein filter. The same experiment was carried out by
preparing the solution with Kiton Red and then adding
Fluorescein into the solution, resulting in the same con-
clusion as before, i.e., leakage through the kiton red filter
was negligible. Note, in Fig. 3, that the Fluorescein emis-
sion over the selected spectral band is partially absorbed by
Kiton red, a spectral conflict that is difficult to avoid in the
two-color, two-dye approach. To reduce this conflict, the
molar concentrations of Fluorescein and Kiton red were
minimized at 5 9 10-7 M. The practical implication of this
spectral conflict, and possible additional self-absorption, is
that the detected emission intensity can become dependent
on the optical path length L within the liquid (i.e., the dis-
tance between laser sheet illumination and the viewed
test section wall). This influence is negligible in our study,
as will be quantified later through calibration experiments.
An important issue that needs consideration is the pH of
the solution. The working fluid in our study, Aqueous
Filter 2
Filter 1
0
0.2
0.4
0.6
0.8
1.0
1.2
1.4
400 450 500 550 600 650 700
Kiton Red, EmissionKiton Red, AbsorptionFluorescein, EmissionFluorescein, Absorption
Wavelength (nm)
Rel
ativ
e In
ten
sity
, I
Fig. 3 Absorption and emission spectra of Fluorescein and Kiton
Red. Green arrow designates argon-ion laser excitation at 514.5 nm.
The spectral bands of the optical filters used for detection are noted by
areas in shaded gray
654 Exp Fluids (2010) 48:651–662
123
ammonium chloride solution, is acidic and its pH is mea-
sured to be as low as 4.3 for a 26% w solution (Shafii
2005). There is also a slight variation of solution pH with
temperature (about 6% change over about 10�C; see Shafii
2005). It is known that fluorescence of Fluorescein is pH
dependent, increases significantly over the pH range 3–7
and becomes insensitive to it above pH of about 7. On the
other hand, Kiton Red does not exhibit a pH dependent
fluorescence over the pH range 3–10 (Coppeta and Rogers
1998). In order to operate in the pH-insensitive range of
Fluorescein, the pH of ammonium chloride solution was
always raised to about 7.8 by adding Sodium Hydroxide
(NaOH).
The calibration of the overall temperature response of
the two-color, Fluorescein-Kiton Red, system was carried
out in the same test section, and with the same optical and
detection configuration as the actual solidification experi-
ments; see Fig. 4. The test section was filled with the
aqueous solution (Ammonium Chloride 19% wt., 5 9 10-7
M Fluorescein, and 5 9 10-7 M Kiton Red) at room
temperature. This particular concentration of NH4Cl was
selected based on the phase diagram of ammonium chlo-
ride (Shafii 2005) to avoid solidification of the liquid
solution down to -15�C. The calibration was carried
out over the (4–20�C) range, however, because previous
experimental results of Wirtz et al. (1998) suggested that
the temperature of mush/melt interface was always above
4�C. The temperature of the fluid was lowered by lowering
the temperature of the base plate, whose temperature was
controlled by a recirculating constant-temperature bath (see
Section 3 for further details). The solution was stirred
continuously to ensure a uniform temperature over the
imaged area in the test section. The temperature of the
solution was independently monitored with a thermocou-
ple. The fluid was illuminated with a laser sheet (argon-ion
laser at 514.5 nm) and fluorescence images of Fluorescein
and Kiton Red were recorded by two aligned 8-bit,
640 9 480 pixel Pulnix cameras (TM-9701) at 30 fra-
mes s-1. Each camera was fitted with appropriate optical
filter (see earlier description) to capture the emission from
one dye. Calibration intensity data were averaged over 30
images and over a 32 9 32 pixel region of the image.
Figure 5 shows the measured intensity variation of both
dyes with temperature for two different optical path lengths
L. Measurements are also included for water solution (i.e.,
without NH4Cl) to assess the influence ammonium chloride
on the temperature response of these dyes. Intensity data of
each dye are normalized by their respective intensity at
reference temperature of 20�C. As expected for 514.5 nm
excitation, the fluorescence intensity of Fluorescein
decreases with decreasing temperature, whereas the emis-
sion of Kiton Red increases, instead. The normalized
intensity ratio, R(T)/R(20�C), was calculated from the data
in Fig. 5 and the results are illustrated in Fig. 6. Several
observations are noteworthy in this figure. First, the pres-
ence of ammonium chloride has a very minor affect on the
temperature response (i.e., calibration curve) compared to
that for the native aqueous solution. Second, the effect of
spectral conflict is small, but observable when we compare
the calibration curve for the two optical path lengths
L = 1 cm and 7 cm. Our studies of solidification typically
used optical path lengths in the range 1–3 cm (Shafii 2005)
and the results reported here are for L & 1 cm. Generally
speaking, before each experiment the appropriate calibra-
tion curve corresponding to its optical path length was first
determined. The final observation from Fig. 6 is that the
temperature sensitivity of the two-color, Fluorescein-Kiton
Red, system is about 4% per �C, significantly higher than
the 1.7% for the original Rhodamine B-Rhodamine 110
pair (Sakakibara and Adrian 1999). As mentioned earlier,
the approach of using two dyes with positive and negative
Argon-Ion Laser Mirror
Mirror
Spherical lens
Cylindrical lens
CCD Camera
CCD Camera
Green Filter for Fluorescein
Red Filter for Kiton Red
Beam Splitter
Test Section
Fig. 4 Schematic of optical setup for calibration and actual
experiments
0.7
0.8
0.9
1.0
1.1
1.2
1.3
1.4
1.5
1.6
5.0 7.5 10.0 12.5 15.0 17.5 20.0
Fluorescein (without NH4Cl; L = 1 cm)
Fluorescein (with NH4Cl; L = 1 cm)
Fluorescein (with NH4Cl; L = 7 cm)
Kiton Red (without NH4Cl; L = 1 cm)
Kiton Red (with NH4Cl; L = 1 cm)
Kiton Red (with NH4Cl; L = 7 cm)
Temperature, T (oC)
No
rmal
ized
Inte
nsi
ty,
I / I 20
OC
Fig. 5 Fluorescence intensity variation with temperature for Kiton
Red and Fluorescein (514.5 nm excitation; pH & 7.8; both dye
concentrations are 5 9 10-7 M; L represents the optical path length)
Exp Fluids (2010) 48:651–662 655
123
temperature sensitivities has also been recently reported by
Sutton et al. (2008) using other dye pairs with the 532-nm
excitation of Nd-YAG laser.
Figure 7 depicts the results from a preliminary test to
assess the effectiveness of the radiometric approach,
described above, for in situ mapping of the temperature
field in the uni-directional solidification problem under
investigation. Shown are the inferred temperature fields if
each dye (Fluorescein or Kiton Red) is used by itself using
its own single-dye calibration curve. The non-uniform
illumination field and ‘‘streaking’’ due to the index of
refraction variations render the results unreliable. The
temperature map using the ratiometric method does not
suffer from the artifacts caused by the streaks and the
nonuniform laser intensity field. The remaining oblique
streak on the upper portion of the image was a consequence
of the very low intensities of less than 20 counts in that
region (see the laser sheet intensity distribution in Fig. 2),
which make it difficult for the ratiometric approach to
remove the high intensity gradients in the streak. The
temperature field illustrated in Fig. 7 shows evidence of a
spanwise set of cold fingers protruding into the ambient
ammonium chloride solution. Section 4 provides more
specific examples of the evolution of the temperature field.
3 Experimental setup
The solidification system utilized is similar to the one
described in Magirl and Incropera (1993). The schematic of
the test section is shown in Fig. 8 and is identical to the one
described in Wirtz et al. (1998), Lum (2001, and Lum et al.
1.0
1.2
1.4
1.6
1.8
5 10 15 20
Exponential FitWith NH
4Cl; L = 1 cm
Without NH4Cl; L = 1 cm
With NH4Cl; L = 7 cm
Temperature, T (oC)
R(T
) / R
(20o
C)
Fig. 6 Variation with temperature of fluorescence intensity ratio, R,
of Kiton Red and Fluorescein (514.5 nm excitation; pH & 7.8; both
dye concentrations are 5 9 10-7 M; L represents the optical path
length)
Fluorescein Kiton Red
T (oC)
Ratiometric
Fig. 7 Sample temperature
map during solidification
experiment, arrived at using
only Fluorescein, only Kiton
Red, and ratiometric approach
Coolant inlet
Coolant outlet
Quartz container
Nucleators
Shrinkage compensator
11.17 mm 11.11 mm
89 mm
Row 1
Row 2
Row 3
11.71m
m14.29
mm
52mm
Fig. 8 Schematic of test section, stainless steel base plate, and
location of nucleators
656 Exp Fluids (2010) 48:651–662
123
(2001). An enclosure made of 1/400 quartz glass measuring
52 mm 9 89 mm 9 100 mm was placed over a stainless
steel base plate and sealed with high vacuum grease and
gaskets to form the test section. The base plate served as a
heat exchanger with a cooling chamber underneath whose
temperature was maintained by a constant-temperature bath
(Neslab RTE-140) that recirculated through the cooling
chamber a coolant mixture of 50:50 water and automotive
anti-freeze solution. A Plexiglas lid was placed above the
quartz enclosure and was fitted with shrinkage compensa-
tors to allow additional fluid to be supplied during the
course of the experiment to compensate for solidification
shrinkage. This ensured that the amount of fluid within the
test section at any time was kept constant. Eleven nucleators
of size 1.59 mm 9 1.59 mm 9 3.18 mm were embedded
in the base plate on a regular pattern to induce finite dis-
turbances and create convective plumes in geometrically
regular locations. The fluid used in these studies was a 26%
wt aqueous solution of ammonium chloride (i.e., a hyper-
eutectic ammonium chloride solution according to its phase
diagram) mixed with 5 9 10-7 M Fluorescein, and
5 9 10-7 M Kiton Red. The fluid in the test was initially at
room temperature (about 23�C) and the solidification pro-
cess was initiated by lowering the temperature of the base
plate to -14�C. The two-color, two-dye, approach requires
the dye concentrations in the solution to remain fixed.
According to the phase diagram of the hypereutectic
ammonium chloride solution used here, cooling of the fluid
results in the phase change (crystallization) of ammonium
chloride; the water itself does not freeze. As a result, we do
not expect variations of dye concentration to develop. This
was confirmed by comparing the temperature measured by
LIF against that from a thermocouple at specific locations in
the solution. The results agreed to better than 0.2�C.
The optical arrangement was discussed previously; see
Fig. 4. The beam of an argon-ion laser, operating at single
line (514.5 nm) and 1.5 W, was manipulated into a laser
sheet (thickness about 0.3 mm) using appropriate optics.
Images were obtained with two CCD cameras (Pulnix
TM9701, 8-bit, 640 9 480 pixel, 30 frames s-1), each fit-
ted with the appropriate optical filter (see Sect. 2.1). The
cameras viewed the same field of view through a cube
beamsplitter and were aligned to one pixel accuracy. The
framing rate of the camera used here is much faster than
needed. The convective flow generated in this uni-direc-
tional solidification problem is very slow (Lum 2001; Lum
et al. 2001) and it can be considered ‘‘frozen’’ over several
consecutive images. For example, the plumes shown in
Fig. 1 ascend at about 2 mm s-1. Therefore, temporal
averaging of data over consecutive frames could be used for
reducing the random error in the instantaneous tempera-
ture measurements. These issues will be discussed more
fully when measurements of temperature distributions are
presented in Sect. 4. In the early stages of the solidification
process (approximately the first 8 min) the flow convection
is exceedingly small in the liquid melt and possible
photobleaching of the fluorescent dyes needs to be consid-
ered. It was observed that the intensity of fluorescein would
drop about 1% upon two-seconds of continuous exposure to
laser. Therefore, a shutter was used to limit the exposure of
the solution to the laser to 0.5 s at a time. The bleaching rate
of Kiton Red was measured to be about one tenth of Fluo-
rescein’s and was not a factor. The effect of dye bleaching
in the worst case (i.e., roughly the initial 8 min of the
solidification process) would correspond to a temperature
error of about 0.06�C, based on the temperature sensitivity
of current approach.
The estimation of temperature requires calculation of
the intensity ratio at the same spatial location. To accom-
plish this, a reference target (1 mm grid pattern) placed in
the image plane was used to establish the relative dis-
placement between the pixels of one camera relative to
those of the other. This was done to sub-pixel accuracy
(better than 0.1 pixel) using the spatial correlation proce-
dure described by Gendrich and Koochesfahani (1996).
The resulting displacement field was used to define a third
order two-dimensional polynomial mapping function by a
least-squares procedure. A bi-linear interpolation scheme
was used to estimate intensities at sub-pixel locations.
4 Results and discussion
Before carrying out quantitative temperature measure-
ments, it would be prudent to establish that the presence of
fluorescent dyes in the liquid melt did not influence the
solidification process. Experiments were carried out with
and without the addition of fluorescent dyes at four times
the nominal concentration and shadowgraph image time
series, similar to Fig. 1, were analyzed. It was noted that
the timing of various events (e.g., fingers, plumes), the
wavelength of plumes and the rise speed of plumes all
remained unchanged. The growth of the mushy zone, cal-
culated from the shadowgraph images and shown in Fig. 9,
also confirmed that the low concentration of the dyes used
here did not influence the solidification process under
investigation.
We now discuss representative temperature measure-
ments. The imaged area selected was 25 9 19 mm2 in size
and was chosen to be located on the first row nucleators
approximately 2.25 cm above the cooling base plate. See
Fig. 10 for a schematic of the imaged region. The spatial
resolution of the measurement in the imaged plane was
about 40 lm per pixel. The measured temperature maps at
different times during the solidification process are shown
Fig. 11. The approximate location of the imaged area
Exp Fluids (2010) 48:651–662 657
123
relative to the mushy zone is indicated by the red box on
the shadowgraph images that are included in the figure.
Temperature maps in Fig. 11 are shown in three dif-
ferent ways corresponding to different temperature accu-
racy levels. The data in the left column represent the
instantaneous map, calculated from a single image pair of
the two CCD detectors corresponding to a temporal aver-
aging time of 30 ms. The noise characteristics of the CCD
cameras, measured using a highly stable light source,
corresponded to a rms intensity fluctuation of about 2.5%
of the mean intensity for the conditions of these experi-
ments (Shafii 2005). Assuming the noise of the two
detectors are uncorrelated, the temperature sensitivity of
current two-dye approach would suggest a temperature
measurement rms uncertainty of 0.8�C based on a single
image pair. This accuracy is comparable to the 1.4 K 95%
confidence level reported in Sakakibara and Adrian (1999).
As mentioned earlier, the convective flow generated in our
uni-directional solidification problem is very slow (Lum
2001; Lum et al. 2001) and it can be considered ‘‘frozen’’
over several consecutive images. Therefore, we take
advantage of temporal averaging over 10 consecutive
frames (i.e., 300 ms temporal averaging) in order to reduce
the random error in the temperature measurement to about
0.25�C. These results are shown in the temperature maps in
the middle column of Fig. 11. Comparison of temperature
maps in the left and middle columns clearly show the
justification of ‘‘frozen’’ flow state over the 300 ms inte-
gration period and the resulting reduction of the tempera-
ture measurement noise. The temperature maps in the right
column represent a further spatial filtering (8 9 8 pixel
area), using the Wiener method in Matlab, in order to
reduce the remaining striations in the spatial maps and a
further improvement in temperature accuracy by a factor of
eight, estimated at 0.03�C. As can be seen in Fig. 11,
because of the high resolution of the original images the
corresponding degradation of spatial resolution by spatial
filtering does not impact the ability to clearly resolve the
essential thermal features in this problem.
The temperature maps of Fig. 11 reveal the presence of
four fingers in the imaged area at time t = 17 min and one
of them has a lower temperature than the rest (i.e., the third
finger from the left located at X = 1.5 cm). This finger is
right above a nucleator and later becomes a plume, while
the adjacent fingers weaken and decline in number. We
note that the number of fingers visible in the temperature
map is significantly less that those in the shadowgraph
images. This is because the shadowgraph technique shows
a field of view that is integrated across the depth of the test
section, whereas the LIF temperature maps are obtained
over a single plane illuminated by a thin laser sheet.
Generally speaking, at each time the temperatures are
cooler at the bottom of the image than the top, as expected
from the mean vertical temperature gradient that is
imposed. Also, as time progresses the temperature field
over the imaged plane becomes cooler over the entire plane
as the mush zone grows and gets close to the bottom of the
images area. We note that at t = 40 min three of the four
fingers subside and only one finger survives as a plume. At
this time, the mushy zone height is about 1.8 cm, 0.45 cm
below the imaged area. The missing portion of the plume
0
5
10
15
20
25
30
0 20 40 60 80 100 120
With Fluorescein and Kiton RedTrial #2 (without fluorescent dyes)Trial #1 (without fluorescent dyes)
Time (min)
Hei
gh
t o
f M
ush
y R
egio
n (
mm
)
Fig. 9 Growth of the mushy region with time. Kiton Red and
Fluorescein concentrations are 2 9 10-6 M; pH & 7.8
Imaged Area 25 x 19 mm
2
2.25 cm
10 cm
8.9 cm
Imaged area
Fig. 10 Location and size of the imaged area for the temperature
maps in Fig. 11
658 Exp Fluids (2010) 48:651–662
123
on the top of the temperature map is likely due to the
helical motion of the plume, causing the center of plume to
move out of the illuminated laser sheet. At time
t = 60 min, the mushy zone has reached the bottom of the
imaged area and one distinct plume is clearly observed.
The feature on the right side of the plume is speculated to
be a finger that is about to form. At this time the mush
interface has a temperature of 8.4�C, whereas the temper-
ature of the plume at the exit of the mush is cooler and is
about 7.8�C.
Temperature profiles along a horizontal line at selected
times are extracted from the temperature maps of Fig. 11 in
T (oC)
X (cm)X (cm)X (cm)
Y (c
m)
t = 17min
T (oC)
X (cm)X (cm)X (cm)
Y (c
m)
t = 30min
T (oC)
Y (c
m)
X (cm)X (cm)X (cm)
t = 40min
T (oC)
Y (c
m)
X (cm)X (cm)X (cm)
t = 60min
Fig. 11 Temperature maps at different times during the solidification
process over the region indicated in Fig. 10. Left column represents
the instantaneous map, middle column is average of ten consecutive
images (i.e., 300 ms temporal average), and right column represents
further spatial filtering over 8 9 8 pixel area. The approximate
location of the imaged area relative to the mushy zone is indicated by
the red box on the shadowgraph images
Exp Fluids (2010) 48:651–662 659
123
order to quantify the temperature profiles across the finger
and plumes. Results are shown in Fig. 12 across a line at
Y & 0.3 cm in the temperature maps (about 2.6 cm above
the cooling plate). Data are shown for both 300 ms tem-
poral averaging and those after 8 9 8 pixel spatial filtering.
When compared with the spatially smoothed profiles, the
un-smoothed data indicate about 0.3�C rms fluctuation,
consistent with the previous estimate of temperature
accuracy for data with 300 ms temporal averaging. Tem-
perature profiles in Fig. 12 clearly show that the location of
the finger that later becomes the plume change very little
during the solidification process (minimum peak always
remains at X & 1.5 cm). We also note that the minimum
temperature in the center of the finger and the plume
illustrated in Fig. 12 is typically two degrees cooler than
the surroundings.
It is also instructive to examine the vertical variation of
temperature differential DT between the ambient and the
finger and plume. Figure 13 shows the measured difference
between the two indicated vertical lines at t = 17 min and
t = 60 min. The temperature difference right at the exit of
the mushy zone (Y = 0 cm and t = 60 min) is about
0.8�C. The maximum temperature difference reaches about
2.7�C and occurs when the plume is formed. 5 Conclusions
A two-color, two-dye, ratiometric laser induced fluores-
cence method was implemented for carrying out in situ
whole-field measurements of the temperature field in a
study of bottom-chilled uni-directional solidification of
aqueous ammonium chloride. The traditional approach
uses a temperature sensitive dye along with another with
little temperature sensitivity. In our work, however, we
took advantage of two temperature sensitive fluorescent
dyes, with opposite temperature sensitivities, in order to
increase the overall sensitivity and temperature resolution
of our measurements. The resulting temperature sensitivity
was more than a factor of two higher than the original work
of Sakakibara and Adrian (1999).
Initial measurements of the in situ temperature field
during solidification of ammonium chloride solution were
presented for the first time. Many interesting characteristics
of the process were quantified, including formation and
evolution of fingers and plumes and the temperature dis-
tributions within them. It was shown that as the plume
moves upward the maximum temperature difference
between the center of the plume and the surroundings
reaches about 2.7�C.
We note that even though the locations of the pixels of
one CCD camera relative to the pixels of the second
camera were determined with sub-pixel accuracy (better
than 0.1 pixel), some streaks and striations still remained
in the final temperature maps. The reasons for the
remaining streaks have been discussed by Sakakibara and
4
6
8
10
12
14
16
18
20
22
24
0 0.5 1.0 1.5 2.0 2.5
t = 60mint = 40mint = 30mint = 17min
X (cm)
Tem
per
atu
re, T
(oC
)
Y (
cm)
X (cm)
Fig. 12 Time variation of the horizontal temperature profile along
the indicated dashed line (Y & 0.3 cm). Symbols are data points
(every other 3 points shown) from the middle column of temperature
maps in Fig. 11 (i.e., 300 ms temporal average). Solid lines represent
the 8 9 8 pixel spatial average data (right column of temperature
maps in Fig. 11)
Y (
cm)
X (cm)
0
1
2
3
4
5
0.2 0.4 0.6 0.8 1.0 1.2 1.4 1.6
t = 60mint = 17min
Y (cm)
Tem
per
atu
re D
iffe
ren
ce,
∆T
(oC
)
Fig. 13 The vertical profile of temperature difference DT across the
indicated dashed lines at two times during the solidification process.
One of every five data points is shown
660 Exp Fluids (2010) 48:651–662
123
Adrian (2004) where they also suggest a blurring method
for improvement. Subsequent to the results we presented
here, improvements were achieved in terms of both
removing the streaks and also temperature accuracy by
using higher resolution CCD cameras with better dynamic
range (Cooke Corp. Pixelfly, 12-bit, 1,024 9 1,392 pixel).
Combination of better detection signal-to-noise ratio and
higher pixel density led to an increase in temperature
accuracy by a factor of four compared to those presented
here (see Shafii 2005). Sample of a temperature map
acquired with improved detection is shown in Fig. 14.
This figure illustrates the temperature map of ammonium
chloride solution at t = 9 min over an imaged area
30 9 22 mm2 located above the second nucleator on the
second row. The spatial resolution of the measurement in
the plane of illumination is about 21 lm per pixel, a
factor of two better than before. Temperature variations
within fingers are shown in great detail and clarity, with
little evidence of streaks.
Acknowledgments This work was supported by NASA, Grant No.
NAG8-1690. The assistance of Dr. Shahram Pouya in the preparation
of the manuscript is gratefully acknowledged.
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