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THIXOTROPY OF ORANGE CONCENTRATE AND
QUINCE PUREE
A.M. RAMOS
Departamento de Tecnologia de Alimentos
Vniversidade Federal de Vicosa
6570.000 Vicosa, Brazil
AND
A . IBARZ'
Departament de Tecnologia d 'Aliments
Vniversitat de Lleida
Av. Rovira Roure, 177
251 98 Lleida, Spain
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(Manuscript received 1997; in final form March 16. 1998)
ABSTRACT
Orange juice with pulp and pectins is thixotropic at soluble solids
concentrations of 55 and 60 "Brix in the range of temperatures from 0 to 20C
and shear ratefrom 7.2 to 57.6 s-'. Quince pure'e is thixotropic at soluble solids
concentrations of 12.3 to 28 "Brix in the range of temperatures between 0 to
20C and shear rate from 7.2 to 57.6 s-'. The thixotropic behaviour of orange
juice and quince pure'e increases with increasing concentration and decreasing
temperature and they can be described by the kinetic model proposed by Figoni
and Shoemaker (1983):
u = ae+( uoi- ue)exp(-kt)
The thixotropic structure of orangejuice was destroyed by applying a shear
rate of 57.6 s-'for 5 min, and for quince pure'e for 10 min. Quince puree shows
a greater thixotropic character than orange juice, because it has a higher
content of fiber, pulp and pectins and also because it shows a microscopic
structure consisting of long particles and heterogeneous fibers.
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INTRODUCTION
Various authors agree that fruit concentrate and puree are thixotropic and
that this is related to the percentage of total pectins and fibers (Mizrahi and Berk
'
To whom correspondence should be addressed
Journal of Texture Studies 29 (1998) 313-324. All Righrs Reserved.
"Copyright 1998 by Food & Nutrition Press, Inc., Trumbull, Connecticut
313
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3 14
A . M . RAMOS and A. IBARZ
1970; Crandall et al. 1990; Ibarz and Lozano 1992) and also with pulp content
(Mizrahi and Firstenberg 1975). The time dependence is related to the structural
change due to shear. If the shear ceases, the viscosity returns to its initial value
due to the structural recovery of the material. This process is reversible; it could
pass from a state of gel to sol and from sol to gel.
The structural factors that contribute to dependence of the time to the flow
of a material are similar to those that contribute to pseudoplastic characteristic
(Rha 1978). Therefore, thixotropy is the result of structural reorganisation, with
a decrease in the resistance to flow (Barbosa-Cinovas et al. 1993). An example
is the degree of torque required to stir the viscous liquids in a mixer with
constant speed (Mohsenin 1996). The usual method to characterise thixotropy
is to apply a constant shear rate and study the variation of shear stress with
time, and fit the experimental data to models that describe that variation (Tung
et al. 1970; Ibarz 1993).
This work has the goals of determining the thixotropic behaviour of quince
purke and orange juice at several concentrations, and study the effects of
temperature and shear rate on this thixotropic behaviour and the influence of
structure of these derived fruits on the thixotropy.
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MATERIAL AND METHODS
Raw materials were supplied by industries in the region of Lleida in Spain.
The samples used are orange juice concentrate with soluble solids of 60 "Brix
and quince purke at concentration of 12.3 "Brix. The samples of quince puree
and orange juice were characterised by soluble solids concentration, pH, water
activity and fiber (AOAC 1990); acidity and formol index (MAPA 1993); pectin
(IFFJP 1984); pulp content ( D u r h and Jimknez 1980) and sugars (Garza er al.
1996). All of which were carried out five times.
Samples of quince puree were obtained with several soluble solid
concentrations through the process of vacuum evaporation (Rotavapor Resona
Technics Lab0 Rota) at 50C. Orange juice concentrate was diluted with distilled
water to obtain several concentrations of soluble solids.
For the thixotropic characterization a Rotovisco RV-12 Haake viscometer
was used. The sensors used were the NV (radii ratio Re/Ri= 1.02) and SV (radii
ratio Re/R, = 1.14), that consist of cups with two rotors that allow to obtain
different measuring ranges. A M500 torque measuring unit that could measure
a maximum torque of 4.90 N.cm was used. A thermostatic bath was used to
control the working temperature within the range 0 to 80C (f 0.2C). The
instrument can be operated at 16 different speeds from 1 to 512 rpm which are
changed stepwise with a selector switch (Haake 1983).
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ORANGE CONCENTRATE AND QUINCE PUREE
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315
The experimental data were controlled automatically through the DECIPHER PLUS version 1.1 program (Decipher 1992) installed in a computer PC,
connected to a DATA-TAKER 500 signals microprocessor (Datataker 1992)
which is directly connected to the Haake viscometer.
The thixotropy was characterised in samples of industrial quince puree at
concentrations of 12.3; 16; 20; 24; 28 "Brix; and in samples of orange juice at
concentrations of 45, 50, 55, 60 "Brix. For orange concentrate the sensor
system NV was used in all determinations.
In preliminary tests, the working temperatures of 0, 5, 10, 20C and shear
rates of 7.2; 14.4; 28.8; 57.6 s-' were chosen. The sample was placed in the
viscometer and excess sample is removed with a syringe or pipette. It is left for
one hour to allow relaxation and the equilibration of temperature (BarbosaCanovas and Peleg 1983). The concentration, the working temperature and the
shear rate of the sample are fixed, and the variation of the shear stress during
a period of 10 min studied. Results were reported as average of three thixograms obtained for each condition, with an error less than 2%. A covering of
low viscosity oil was applied at the edge of all samples, after loading, between
the two cylinders. The variation of the shear stress with the time at constant
shear rate was controlled automatically by means of a computer programmer that
samples the shear stress every second. Experimental data obtained was fitted by
Figoni and Shoemaker (1983) model through analysis of regression carried out
with the statistical package STATGRAPHICS v. 7.0.
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RESULTS AND DISCUSSION
Thixotropic Behaviour of Concentrated Orange
Orange juice at 55 and 60 "Brix showed time dependence while juice at 45
and 50 "Brix did not. The thixograms for orange juices (60 and 55 "Brix)
divided into two stages. The first, from 0 to 20 s, a rapid decrease in the shear
stress, while in the second stage the decrease is slow. This could be explained
by means of two mechanisms of structural break-down. The first mechanism
could be due to the disintegration of irregular pulps into smaller and more
homogeneous particles. The second mechanism is explained by the orientation
of particles caused by the shearing action. The behaviour obtained for the other
conditions were similar.
Experimental values were fitted to Weltman (1943) and Figoni and
Shoemaker models (1983). A better fit was obtained with the Figoni and
Shoemaker model in all cases, so only the values obtained by this fit are given.
Figoni and Shoemaker's model (1983) states that:
316
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A.M. RAMOS and A. IBARZ
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where a is the shear stress, a, is the shear stress equilibrium value which is
reached after a long enough shear time (Pa), a,, is the initial shear stress, (aoi a,) represents the quantity of break-down structure for shearing, k, is a kinetic
constant of structural destruction and 0 is the time of shearing.
Thixotropic parameters of Figoni and Shoemaker model, and the determination coefficients, are listed in Table 1. The fits and the estimates of the
parameters, a,,, a, (aoi - a,) and k,are significant with a probability level of
95%.
Effect of Shear Rate on the Thixotropy
The effect of shear rate on the thixotropic character of the juice is shown
in Table 1. For a shear rate of 57.6 s-' the quantity structure break-down (aoiae)during shearing was greater than for shear rate of 7.2 s-I. A shear rate of 7.2
s-I showed a smaller value for the equilibrium shear stress, a,, which implies
that it will show a smaller apparent final viscosity than the sample shearing at
the higher shear rate. Those behaviours have also been detected in juice
concentration at 60 "Brix. This could be explained by the fact that when
applying a high shear rate, the shear stress obtained is greater, which implies
higher differences between the initial stress and equilibrium stress. Chiralt ef al.
(199 1) observed similar behaviours, working with Jijona turrbn.
Effect of Temperature on the Thixotropy
As temperature rises, thixotropy is reduced (Pascual 1974; Alvarez et al.
1989). In orange juice at concentration of 60 "Brix, structural break-down of
samples decreases when the temperature increases, being less with decreasing
shear stress.
The effect the temperature is seen in Table 1. With the increase of
temperature, equilibrium shear stress decreases, this indicates that it will show
less apparent viscosity with the increase of temperature.
Effect of Concentration on the Thixotropy
The evolution of shear stress with time at shear rate of 28.8 s-' for orange
juice at temperature of 1OC and concentrations of 55 "Brix and 60 "Brix was
also studied. The difference from the variation of shear stress-time exists,
especially in the initial times, where the structural destruction of sample to
concentration of 55 "Brix was slightly more rapid.
ORANGE CONCENTRATE AND QUINCE PUREE
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317
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TABLE 1 .
FIGONI AND SHOEMAKER MODEL PARAMETERS FOR ORANGE
C
("Bnx)
Y
T
(s.')
('C)
% - 0,
011,
~
55
(Pa)
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72
10
3 7 8 ~ 0 7 26 1 t 0. I
1 I 7 f 0.6
0 I70 f 0,013
0.864
144
10
642k09
46.5 f 0. I
17 7f0.9
0 223 f 0,014
0.898
0 1065t07
92.2 f 0.1
14.2 f 0.6
0.101 f 0 . 0 0 7
0.891
5
951k11
74.7 f 0.1
20 7 f 1.0
0.182 f 0.0 12
0.889
10
994rt 1 9
60.6 t 0.1
38.9 f 1.8
0.600 t 0 030
0.943
20
665k19
43.7 f 0.1
21.8 k 1.8
0.580 f 0 050
0.832
576
10 1 0 7 6 k 0 9
83.9 2 0.1
23.7 k 0.8
0.225 f 0 010
0.944
7.2
0 102 2 k 0 . 6
80.9 f 0.1
21.3 f 0.5
0.083 k 0.003
0.962
5 6 8 9 2 1.1
49.1 t 0. I
19.8k 1.1
0.250t0017
0.883
_-
_-
--
_-
20 66.0 k 1.3
39.4 f 0. I
26.6 f I 2
0.205 f 0.013
0.903
0 117.32 1.5
94.9 f 0.1
23.4 f 1.4
0.195 f0.016
0.839
288
50
60
RL
(Pa)
10
14.4
28.8
57.6
--
5
85.3 t 1.3
65.6 f 0.1
1 9 . 7 t 1.2
0.161 f0.013
0.838
10
71.5 k 0 . 6
60.6 f 0.2
10.9 f 0.3
0.030 f 0.002
0.904
20
77.0 k 0 . 7
61.2 f 0. I
15.8f0.6
0.124f0.007
0.915
0 155.22 1.3 132.0 f 0.2
23.3 ? 1.2
0.134 f 0.009
0.874
5 130.82 1.4
103 4 f 0.2
27.4 k 1.3
0.144 zk 0.009
0.893
10 110.2 k 0 . 5
882fO I
0.1 10 f 0.003
0.972
20 1 0 7 . 0 t 1.6
*
22.1 f 0.5
75 7 0.1
31.3f 1.5
0.311 f 0 . 0 1 8
0.913
0 181.9 22.3
136.3 f 0.2
45.6 t 2.1
0.251 f 0.015
0.907
5 145.2 k 1.6
1 16.8 f 0.1
28.4 f 1.5
0.202 f 0.014
0.875
10 115.7f 1 . 1
98.3 f 0.2
17.3 t 1.0
0.073 f0.006
0.828
20 107.3 f 1.3
84.5 f 0.1
22.8 f 1.2
0.201 f 0.005
0.879
318
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A.M. RAMOS and A. IBARZ
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The difference, a, - uer represents the quantity of juice structure that is
degraded during the shearing. The values obtained for 55 "Brix juice at i. =
28.8s.' (14.2 to 38.9 Pa, Table 1) and for 60 "Brix juice at i. = 28.8s.' (22.1
to 31.3 Pa, Table 1) indicate an appreciable magnitude of thixotropy.
At 5C and shear rate at 28.8 s-' (Table l), the equilibrium stress, u,,
decreases with concentration, and the sample with more elevated concentration
will show a greater apparent final viscosity. For the break-down structure
parameter, a, - a,, this quantity is greater in the sample of orange juice at 60
"Brix, than the one which indicates that a higher quantity of structure has been
destroyed during the shearing, k, values of sample at 55 "Brix are higher; these
values imply that the speed of structural destruction of the sample is higher than
the sample at 60 "Brix.
Thixotropic Behaviour of Quince PurCe
The shear stress obtained on quince puree at 28 "Brix at a shear rate of
57.6 s-' was extremely sensitive to the time of shearing, especially in the first
100 s. All the samples showed thixotropic characteristic. The shear stress, as
well as the apparent viscosity reaches a constant value after the 300 s of
shearing. For the puree at 12.3; 16; 24 and 28 "Brix similar thixograms were
also observed; however, values of initial shear stress were directly influenced
by shear rate. Similar behaviour has been obtained by Costell and D u r h (1978)
and Costell et al. (1982) in apricot puree; Chiralt et al. (1991) in "Jijona
turron"; Ibarz and Lozano (1992) in peach puree and Alonso et al. (1995) in
fruit-based baby foods.
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Effect of Shear Rate on the Thixotropy
Table 2 shows the influence of shear rate applied on the degree of
thixotropy for quince puree at different concentrations at 1OC. The behaviour is
similar to orange juice (Table 1) and agrees with results obtained by Chiralt el
al. (1991).
Effect of Temperature on the Thixotropy
An increase of temperature reduces the thixotropy of quince puree samples.
This is similar to orange juice at 55 and 60 "Brix (this work) and condensed
milk (Alvarez ef al. 1989). In quince puree, structural degradation of the
samples decreases when the temperature increases.
The thixogram for the quince puree (28 "Brix, 57.6 s-I) also has two
different stages, as that obtained for orange juice (this work) and "Jijona turron"
(Chiralt et af. 1991). The first stage, which is characterised as a rapid decrease
in the shear stress, is more extended and it is in an interval from 0 to 100 s.
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ORANGE CONCENTRATE AND QUINCE PUREE
319
This difference shows the greater thixotropy of puree.
Effect of Concentration on the Thixotropy
A greater thixotropic behaviour can be seen at higher concentrations of the
puree, while for the concentrations of 16 and 12.3 "Brix the time dependence
is small and the thixotropy structure in these concentrations is weak.
The effect of concentration has also been studied for the shear rates 7.2,
12.4 and 57.6 s.' at 1OC. Similar thixograms were obtained. However, values
of initial shear stress are directly influenced by the shear rate applied and an
initial shear stress increase with the shear rate, which implies a higher stress
equilibrium.
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TABLE 2.
FIGONI AND SHOEMAKER MODEL PARAMETERS FOR QUINCE PUREE AT
TEMPERATURES OF 1OC AT DIFFERENT SHEAR RATES AND
CONCENTRATIONS SOLUBLE SOLIDS
7
c
(S-')
("Brix)
7.2
12.3
16
20
24
28
444f02
I08 f 1 0
307 t 3 0
608f6O
837 f 9 0
14.4
12 3
16
20
24
28
28.8
57.6
(JOl
(Je
(Pa)
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(Pa)
(JO,
- (Je
(Pa)
kl
R:
(S.')
408tO 1
36?02
939206
140f04
244 0 f0 3 6 2 7 - 2 4
444 3 ? 0 7 l 6 3 9 f 1 2
241 + 8 0
596 0 2 1 2
0 104f0003
0118fOOO5
O125fO007
0117tOOO5
0 115t0006
0 887
0 952
0 923
0 944
0 936
486fO2
1293f09
363 f 4 0
654 f 8 0
919f I I 0
450tO 1
1134?0 1
274 6 If. 0 3
472 3 f0 8
663 I f 1 2
3.7 f 0.9
16.5 t 0 . 9
88 t 4 0
183 7.0
286 f 9.0
0. I09 k 0.009
0.183 f 0 . 0 1 3
0. I84 t 0.010
0.153 t 0.008
0.128 t 0.006
0 854
0 875
0 921
0 929
0 941
12.3
16
20
24
28
684fO4
1803tl 7
404 t 5 0
715 f 10 0
I082 f I3 0
61 4 f 0 1
1504fO I
318 2 2 0 5
520 9 f O 9
7536t12
7.0 f 0.4
29.9f 1.6
86 ? 4.0
195t9.0
328 ? 11.0
0.257 f 0.020
0.215 t 0 . 0 1 5
0.146 k 0.01 1
0 184fO.011
0.171 ?00.008
0 852
0 878
0 865
0 900
0 938
12.3
16
'0
24
28
I09 9 f 2 4
258f4O
439 f 5 0
789 ? I 1 0
l304+130
6 4 5 t O 1 45.3 f 2.3
70 f 3.0
I87 3 f 0 2
76 f 4.0
3627f06
5 8 0 9 f . 0 8 208 f 10.0
8 8 6 0 t l O 417f120
0.773 k 0.004
0.405 f 0.023
0. I I4 f 0.009
0.235 t 0.015
0239t0009
0 946
0 919
0 849
0 898
0960
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+
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320
A.M. RAMOS and A. IBARZ
The results were tested against two models (Weltman, and Figoni and
Shoemaker). A better fit was obtained with the Figoni and Shoemaker model in
all cases, so only the values obtained by this fit are given. Thixotropic
parameters of the Figoni and Shoemaker model, as also the determination
coefficients, are listed in Tables 2 and 3. The fits and the estimates of the
parameters, sol, a, (aol - a,) and k,are significant at the 95% probability level.
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TABLE 3.
FIGONI AND SHOEMAKER MODEL PARAMETERS FOR QUINCE PUREE AT
CONCENTRATION SOLUBLE SOLIDS OF 28 "BRIX AT SHEAR RATES
AND DIFFERENT TEMPERATURES
Y
T
601
(s-')
("C)
(Pa)
7.2
0
5
10
20
14.4
0
5
10
20
28.8
0
5
10
20
57.6
0
5
10
20
1042f
923f
837f
770f
(Je
001
(Pa)
9
7
9
8
731f1
657 f 1
596 f 1
536 f I
1153f 11
1024 k 1 I
920 f 1 1
843f 9
808 f 1
699 f 1
663 f I
620 f 1
I309 f 12
1224 k 14
I082 f 13
993 f 10
888f 1
826 f 1
754 1
694 f 1
1463 f 19
I439 k 19
I304 f 13
1123f12
1042 f 2
992 -+ 1
886 f 1
811fl
*
- (Je
kl
(Pa)
312f
267f
241 f
233f
7
6
8
7
*
0093 0.003
0.088 k 0.003
0.1 15 f 0.006
0.100 f 0.004
1
R?
0.966
0.970
0.936
0.952
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344f 9
326 f 10
286f 9
223f 8
0.122 f 0.005
0.124 f 0.005
0.128 f 0.006
0.1 12 f 0.006
0.958
0.95 1
0.941
0.933
422 2 1 1
399 f I3
3285 11
299 f 10
0.161 f 0.006
0.170 f 0.008
0.17 1 f 0.008
0.195 f 0.008
0.965
0.995
0.938
0.949
421 f 17
447f 18
417f 12
0.188f0.010
0.255 k0.013
0.239 f 0.009
0.199f0.010
0.925
0.931
0.960
0.935
312k11
For purCe at lOC, the equilibrium shear stress, a,, increases with the
increase at soluble solid concentration, such as with that of shear rate. For
samples shearing at shear rate of 7.2 s", the equilibrium shear stress increases
rapidly from 40.82 Pa, at 12.3 "Brix, to 596.0 Pa at 28 "Brix, while the
equilibrium stress increases to 886 Pa at shear rate of 57.6 s-'. This means that
the prolonged shear has different effects in accordance with the concentration of
quince puree. Similar behaviour were obtained for purees and derived fruits
(Chiralt et af. 1991; Lozano and Ibarz 1994).
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ORANGE CONCENTRATE AND QUINCE PUREE
32 1
For all concentrations of quince puree the parameter that measures the
structural break-down the shearing (a,,- a,) increases of progressively with
soluble solids content and with increasing shear rate. At a shear rate of 7.2 s-I,
the parameter u,, - u, increases from 3.55 Pa at 12.3 "Brix to 241 Pa at 28
"Brix, and to 417 Pa for the shear rate of 57.6 s-I. The values of parameter ao,u, indicate that thixotropy of quince puree has an important magnitude.
Table 2 shows that the constant k,, structural degradation rate, was almost
unchanged with concentration when the sample was shearing at 7.2 and 14.4 s-I;
while with higher shear rate, 28.8 and 57.6 s-', values k, decreases with the
increase of the concentration. Shear rate being 57.6 s-', ki value varies from
0.773 s.I for 12.3 "Brix to 0.239 s-' to 28 "Brix, which indicates that the speed
at which the structure for of the sample of 12.3 "Brix is destroyed is higher,
than for 28 "Brix. Similar behaviour is observed for orange juice at concentrations of 55 and 60 "Brix in this work and in peach puree by Lozano and Ibarz
( 1994).
Table 3 shows that a,, a,, - a,, have a similar behaviour to that obtained for
orange juice. Those parameters decrease with the increase of temperature, while
the constant k, increases with the increase of temperature. This behaviour was
also observed by Pascual (1974) and Alvarez et af. (1989).
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Comparison Between Quince Purke and Orange Concentrate
Structural Microscopic analysis. Quince puree shows a greater thixotropic
behaviour than orange concentrate. This could be caused by the higher level of
solid soluble, fibers, pulps and pectins in quince puree. Costell ef al. (1982),
Ibarz and Lozano (1992) obtained similar behaviour when studying texture and
thixotropy, respectively, in fruit purees.
For a more complete study of the thixotropic behaviour of the two samples,
microscopic observations of their structures were carried out (Fig. 1).
While orange pulp micrograph (Fig. la) showed a uniform and regular
distribution of particles, quince pulp (Fig. lb) had longer particles and a
heterogeneous fiber microscopic structure. As both orange and quince pulps
were manufactured in the same processing line, differences in the microscopic
structure could be attributed to inherent nature of cellular tissue for each fruit.
These studies confirm the greater degree of thixotropic behaviour of quince
puree. Lozano and Ibarz (1994) obtained similar behaviour studying thixotropy
in plum and peach purees.
ACKNOWLEDGMENT
The author A . M . Ramos is very grateful to CoordenaGiio de AperfeiGoamento de Pessoal de Nivel Superiorde Brasil -CAPES- and Federal University
322
A.M. RAMOS and A . IBARZ
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of ViCosa-UFV, Brazil for the financial support received while at University of
Lleida, Spain.
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FIG. I . MICROGRAPH OF CONCENTRATED ORANGE (a) A N D
QUINCE PUREE (b) PULPS
Marked bar is equivalent to 50 pm.
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ORANGE CONCENTRATE A N D QUINCE PUREE
323
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