ArticlePDF Available

Optimization of the Extrusion Process Temperature and Moisture Content on the Functional Properties and in vitro Digestibility of Bovine Cattle Feed Made out of Waste Bean Flour

Authors:

Abstract and Figures

The main purpose of this research was to evaluate and optimize the effect of the extrusion temperature and moisture content on the functional properties of a bovine cattle feed made out of waste bean flour. In order to do so the methodology of response surface with a central composed design with star points was used, in which the independent variables were the temperature of extrusion and the moisture content; the response variables evaluated were the expansion index, bulk density, hardness, water absorption index, water solubility index and In Vitro digestibility. The diets were extruded on a simple screw extruder. On the statistical analysis of the most important response variables that influence the ruminal digestibility of the elaborated feed are water absorption index (WAI) and water solubility index (WSI), they presented a non-significant quadratic model and a significant model (0.5428 and 0.0202, respectively). In these models, it was observed that the linear term of the extrusion temperature was not significant in both cases, while for the WSI, the moisture content on its linear term did show a significant effect on the whole model on this response variable. In the WSI case, it was observed that the quadratic term of the temperature and its interaction with the moisture content presented a statistically significant effect. Under the experimental design evaluated it is concluded that it is possible to elaborate an extruded feed for bovine cattle with high values of solubility.Temperature and moisture content showed significative effect (p < 0.05) on WAI, WSI and BD.
Content may be subject to copyright.
Online version is available on: www.grjournals.com
Journal of Animal science advances
Optimization of the Extrusion Process Temperature and
Moisture Content on the Functional Properties and in vitro
Digestibility of Bovine Cattle Feed Made out of Waste Bean
Flour
Reyes-Jáquez D., Vargas-Rodríguez J., Delgado-Licon E., Rodríguez-Miranda J., Araiza-
Rosales E. E., Andrade-González I., Solís-Soto A. and Medrano-Roldan H.
J Anim Sci Adv 2011, 1(2): 100-110
REYES-JAQUEZ ET AL.
100
Optimization of the Extrusion Process Temperature
and Moisture Content on the Functional Properties
and in vitro Digestibility of Bovine Cattle Feed Made
out of Waste Bean Flour
1
Reyes-Jáquez D.,
1
Vargas-Rodríguez J.,
*1
Delgado-Licon E., Rodríguez-Miranda J.,
Araiza-Rosales E. E., Andrade-González I., Solís-Soto A. and Medrano-Roldan H.
1
Graduate School of Biochemical Engineering, Postgraduate, Research and Development Unit, Technological Institute of Durango.
Blvd. Felipe Pescador 1830 Ote., Col. Nueva Vizcaya, C.P. 34080, Durango, Durango, México
2
Technological Institute of Tlajomulco, Km. 10 Carr. San Miguel Cuyutlán, Apartado postal No. 12, C.P. 45640, Tlajomulco de
Zúñiga, Jalisco, México
Abstract
The main purpose of this research was to evaluate and optimize the effect of the extrusion temperature and
moisture content on the functional properties of a bovine cattle feed made out of waste bean flour. In order to do
so the methodology of response surface with a central composed design with star points was used, in which the
independent variables were the temperature of extrusion and the moisture content; the response variables
evaluated were the expansion index, bulk density, hardness, water absorption index, water solubility index and
In Vitro digestibility. The diets were extruded on a simple screw extruder. On the statistical analysis of the most
important response variables that influence the ruminal digestibility of the elaborated feed are water absorption
index (WAI) and water solubility index (WSI), they presented a non-significant quadratic model and a
significant model (0.5428 and 0.0202, respectively). In these models, it was observed that the linear term of the
extrusion temperature was not significant in both cases, while for the WSI, the moisture content on its linear
term did show a significant effect on the whole model on this response variable. In the WSI case, it was
observed that the quadratic term of the temperature and its interaction with the moisture content presented a
statistically significant effect. Under the experimental design evaluated it is concluded that it is possible to
elaborate an extruded feed for bovine cattle with high values of solubility.Temperature and moisture content
showed significative effect (p < 0.05) on WAI, WSI and BD.
Key words: Bovine cattle feed, digestibility, extruded
*
Corresponding author: edelgad@itdposgrado-bioquimica.com.mx, Tel: +52-618-8186936, Ex. 105. Fax: +52-618-8186936, Ext. 107. E-
Received on: 11 Nov 2011
Revised on: 18 Nov 2011
Accepted on: 21 Nov 2011
Online Published on: 1 Dec 2011
Original Article
ISSN: 2251-7219
OPTIMIZATION OF THE EXTRUSION PROCESS TEMPRATURE AND MOISTURE CONTENT …
101
J. Anim. Sci. Adv., 2011, 1(2):100-110
Introduction
In Mexico, the scarcity of good-quality sources
of forage during the dry season affects many
livestock-growing regions (El Excelsior, 1996; La
Jornada, 2002). In some regions there is an
overproduction of crop residues including those of
maize, sugar cane, sorghum, wheat, bean and oats.
These residues could be used as animal feed,
especially for ruminants, which are the only animals
that can digest these high fiber materials. Due to
their poor nutritional quality, crop residues have
only been used to prevent weight loss in animals or
at least to maintain them alive during critical times.
To enhance their poor nutritional characteristics,
crop residues can also be mixed with low-cost-by-
products (Valadez, 2008).
On the other hand, crop residues are naturally
low-density materials and, therefore, the application
of a form of densification would increase their
utility. The densification process is able to convert
residues into a compressed form with advantages in
transportation, handling and storage and hence can
help address the problem of local overabundance
(Bhattacharya et al., 1987). The process has
historically been applied to produce either fuel or
animal feed, any form of high pressure densification
can reduce costs in long-distance transportation,
improve feed control and the addition of medicines
without risk of inexact measurement, create a
homogeneous mixture preventing the avoidance of
some ingredients by the cattle, reduce feed waste,
improve the efficiency of feed delivery, eliminate
harmful bacteria and, by means of a suitable diet
preparation, improve its digestibility (Payne et al.,
1994). The aim of this study was to evaluate the
effect of extrusion temperature and moisture content
on the functional properties and In vitro digestibility
of a balanced feed for bovine cattle based on bean
flour.
Materials and Methods
Experimental diets formulation
Two diets were elaborated with 10 % of bean
flour (DB) and 10 % of alfalfa (DA) (Table 1). The
ingredients used were: waste bean (Phaseolus
vulgaris L., known as “granza”), Pinto Saltillo
variety, alfalfa (Medicago sativa L.), white corn
flour (Zea maiz L.), cafime variety, cane molasses
(Mine-Gan, dry powder), soymeal (47.7 protein %)
and limestone (38%). All of them were donated by
the Local Livestock Durango Association C. A., and
milled to have less than 2 mm diameter.
Tabel 1: Formulation of diets
Ingredients
Diets (% DM)
DA
DB
Bean flour
0
10
Alfalfa flour
10
0
Corn flour
55
55
Cottonseed meal
23
23
Cane molasses
5
5
Soy meal
5
5
Limestone
2
2
DA = Diet with alfalfa, DB = Diet with bean flour, DM=
Dry matter
Chemical composition
Proximate chemical composition of the
ingredients and extrudates, as well as two
commercial diets were determined in triplicate
following standard AOAC (2005) methods:
moisture (925.10), ash (923.03), protein (920.87)
and fat (920.39). Crude fiber was determined by
acid-alkaline digestion (Tejeda, 1992).
Extrusion Processing
To elaborate the diets, a Brabender laboratory
simple-screw extruder (Model 20DN/8-235-00, C.,
W Disburg, Germany) was used with the following
characteristics: three heating zones, screw
compression force 1:1, longitude/diameter relation
(L/D) 20:1, and internal diameter of the exit die of 6
mm. Before extrusion, a mixture of formulate was
performed as well as the adjustment of the humidity
content of 18 to 22 % according to the experiment
design. The samples extruded were dried at 75 ºC
for 3 h at 6 % humidity, they stored in sealed
polyurethane bags at 4 ºC for later analysis.
Experimental design and data analysis
A central composite design with three
independent variables was performed using
commercial software (Design-Expert 8.0.2, Statease
Inc., Minneapolis, MN, U.S.A.). The independent
variables considered were temperature at the exit of
the die (X
1
) and moisture content (X
2
) (Table 2).
The response variables were expansion index
(EI), bulk density (BD), water absorption index
REYES-JAQUEZ ET AL.
102
(WAI), water solubility index (WSI), hardness (H)
and In vitro digestibility (IVD).
Table 2: Factors and variation levels of experimental
design for two factors
Factor
Levels of variation
-α
-1
0
+1
+ α
Temperature
(ºC)
113.79
120
135
150
156.21
Moisture
(%)
17.17
18
20
22
22.83
(α =1.1414)
Surface response methodology was applied to
the experimental data using the commercial statistic
software previously mentioned. Results were
analyzed by multiple lineal regressions (Equation
1). Experimental data was adjusted to the selected
models and the obtained regression coefficients.
Regression terms statistical significance was
examined by a variance analyzes (ANOVA) for
each response.
=
0
+
1
1
+
2
2
+
11
1
2
+
22
2
2
+
12
1
2
(1)
Process optimization
Numerical optimization was performed through
different response (EI, BD, WAI, WSI, H and IVD)
surface superposition for each of the diets.
Commercial diets were obtained intervals EI (0.88
to 1.11), BD (1027-1052 kg/m
3
), WAI (2.9 to 5.5
g/g), WSI (2.1 to 3%), H (29.4 to 49.4 N) and IVD
(91.9 to 93.9 %) and settled in the program as
optimal values, which must contain the extruded
products.
Determinations
Expansion Index (EI) and Bulk Density (BD)
EI is measured according to the Gujska and
Khan (1990) method, dividing the diameter of the
extrusion by the diameter of the socket opening in
the extrusion exit. The BD was determined
according to the technique reported by Wang et al,
(1993). The diameter (d) and the longitude (l) were
measured from 10 randomly selected samples.
Three diameter measurements were taken from each
sample and the average value was calculated. Later,
each extrude was weighed (Pm), to determine
density using the equation (the results were
expressed in Kg/m
3
):
Density =
Pm
π
d
2
2
l
(2)
Water Absorption Index (WAI) and Water
Solubility Index (WSI)
The water absorption index (WAI) and water
solubility index (WSI) were determined as outlined
by Anderson et al. (1969). One gram of ground
product was sieved at 0.420 mm and dispersed in 10
mL of water at room temperature (25±1 °C). The
resulting suspension was gently stirred for 30 min
and then the samples were centrifuged at 3000 x g
for 15 min (Hettich Zentrifugen EBA 12 D-78532,
Germany). The supernatant was decanted into a
tared evaporating dish. The WAI was calculated as
the weight of sediment or gel obtained after removal
of the supernatant per unit weight of original solids
as dry basis. The WSI was the weight of dry solids
in the supernatant expressed as a percentage of the
original weight of sample on dry basis.
Hardness (H)
This is a textural variable evaluated using a
texture profile analysis with the TAXT2 (Texture
Technologies Corp., Scarsdale, NY/Stable
MicroSystems, Haslemere, Surrey, UK). In each
trial fifteen samples were sheared using the Warner
Brazler blade probe with a sensitivity of 1 kg/force
and 5 cm min
-1
for the evaluation of breaking
strength.
In Vitro Digestibility (IVD)
IVD was calculated using DAYSYII
(ANKOM, 2000) procedure. A 250 mg (DM)
sample (triplicated) was placed in polyester
multilayer filter bags (F57; 5 x 5.5 cm
2
, ANKOM
Technology Corp., Macedon, NY) that were
previously washed with ketone and dried in an air
forced stove at 60°C for 2 h. The bags were sealed
and placed in digestion jars (25 bags per jar,
DaisyII, ANKOM Technology Corp. system,
Macedon, NY). The jars were placed in an
incubation chamber. A 49 inoculum was prepared
diluting ruminal liquid obtained from a rumen
fistulated cow, and a buffer solution with a 1:4 (v/v)
OPTIMIZATION OF THE EXTRUSION PROCESS TEMPRATURE AND MOISTURE CONTENT …
103
J. Anim. Sci. Adv., 2011, 1(2):100-110
proportion according with the manufacturer
specifications. The inoculum was incorporated to
the jars, which were CO
2
purged. After a 48 h at
39°C incubation period, the jars were withdrawn
from the incubation chamber and the bags were
washed with distilled water. The bags were then
treated with a neutral detergent solution for 75 min.
Then the bags were rinsed ketone and hot water,
and were later dried at 55°C. IVD was calculated as
the difference between incubated DM and the
residue after neutral detergent solution treatment.
Results and Discussion
Raw material chemical composition
Table 3 shows raw material proximal chemical
analysis. Highest protein content was found in soy
flour (55g/ 100g), followed by cottonseed meal
(44g/ 100g), whilst waste bean flour and alfalfa
flour presented the same content (19g/ 100g).
Highest lipid content was found in soy flour (3.7g/
100g), followed by alfalfa flour (2.6g/ 100g) and
maize flour (2.1g/ 100g). Waste bean flour was
found a 1.5g/ 100g lipid content. Highest ashes
content was found in calcium carbonate (39.76g/
100g), followed by molasses (7.16g/ 100g). Alfalfa
flour presented higher ashes content than waste
bean flour, 5.25 and 2.95g/ 100g, respectively.
Highest raw fiber content was found in the alfalfa
flour (26g/ 100g), followed by cottonseed meal
(14.1g/ 100g) and waste bean flour (7.5g/ 100g).
Raw material NFE highest content was found in the
maize flour (87.5g/ 100g); followed by molasses
(86.84g/ 100g), waste bean flour (73.15g/ 100g) and
alfalfa flour (76.55g/ 100g).
Raw material protein content used in ruminant
cattle feed it’s very important, due to different
protein fraction interaction, it offers soluble protein,
slowly degradable protein and a high protein
percentage (Chamorro et al., 1999). High protein
and energy content allow a better volatile fat acids
balance, protein fraction presents low to medium
ruminal degradability, which increases small
intestine protein flow and improves the absorbed
nutrients energy-protein balance. Likewise, with
micronutrients secondary metabolites addition
increase bacterial growth logarithmic phase and
ruminal bacterial and fungus enzymatic activity
closely related to the selected diet structural
carbohydrates degradability increase (Beltrán, 1992,
Cortés & Gutiérrez, 1997, Navas et al., 1992, Díaz
et al., 1993).
Moisture and extrusion temperature effect on
expansion index (EI) and bulk density (BD)
EI it’s one of the most important parameters,
it’s related to bulk density (Conway & Anderson,
1973). Table 5 shows IE´s diets regression results. It
was founded that moisture content in its lineal term
(p < 0.05), had effect (p < 0.05) on all of EI’s diets,
however, DA studied variables didn´t present
significative effect (p > 0.05). D2´s moisture
positive regression coefficient (Table 5) indicates
that increasing moisture from 18 to 22%, EI
increased (Figure 2), this was also observed with
bean extrudates (Gujska & Khan, 1991). High
starch content extrudates, like DB, with higher
moisture, higher expansion index. These results
agree with Owusu-Ansah et al. (1984) results, in
which high starch content in extrudates, require
higher moisture quantity to obtain high EI. Usually,
functional properties changes in extrudates such as
EI and BD are related to structural starch
transformations (Camire et al., 1990; Balandrán-
Quintana, 1998; Zazueta-Morales et al., 2002;
Pérez-Navarrete, 2006).
Extruded diets bulk density it’s directly related
to the expansion that is produced during extrusion
(Colonna et al., 1989). Table 5 presents BD
regression analysis. Extrusion temperature in its
lineal term has effect (p < 0.05) on DA. Extrusion
moisture in its lineal term, presented a significative
effect (p < 0.05) on both diets.
Temperature on D1 negative lineal coefficients
regression (Table 5) indicate that increasing
temperature from 120 to 150°C BD decreases, this
could be due that during the extrusion process, with
high temperatures, starch suffers a greater
degradation and can reach a dextrinization reducing
expansion radius, especially with low starch content
mixtures (Chiang & Johnson 1977; Colonna et al.,
1984; Davidson et al., 1984; Chinnaswamy &
Hanna 1987; Sacchetti et al., 2005), and with this
affecting final product expansion. Moisture on DA
and DB negative lineal coefficients regression
(Table 5) indicate that increasing moisture from 18
to 22% BD decreases, having a greater decrease on
REYES-JAQUEZ ET AL.
104
DB due that these diets present a higher starch content (greater expansion, less density).
Table 3: Raw material chemical composition
Ingredient
Component (g/ 100g)
Protein
lipids
Ash
Crude Fiber
NFE
Alfalfa flour
19.0 ± 0.64
2.6 ± 0.08
5.25 ± 0.52
26.0 ± 2.23
73.15 ± 3.28
Waste bean flour
19.0 ± 0.77
1.5 ± 0.04
2.95 ± 0.12
7.5 ± 1.09
76.55 ± 2.48
Cottonseed meal
44.0 ± 0.05
1.3 ± 0.16
5.35 ± 0.47
14.1 ± 2.84
49.35 ± 3.61
Corn flour
9.2 ± 0.14
2.1 ± 0.36
1.2 ± 0.09
7.1 ± 0.74
87.5 ± 3.75
Dry molasses
5.8 ± 0.60
0.1 ± 0.02
7.16 ± 0.78
0.5 ± 0.05
86.94 ± 3.96
Soy flour
55.1 ± 0.89
3.7 ± 0.41
1.0 ± 0.04
4.27 ± 0.61
40.2 ± 3.12
Calcium carbonate
0.09 ± 0.02
0.0 ± 0.00
39.76 ± 1.86
0.0 ± 0.00
60.15 ± 2.97
DM= Dry matter, NFE= Nitrogen free extract
Table 4: Commercial meals and waste bean and alfalfa extrudates proximal chemical composition
Sample
Component (g/ 100g DB)
Fat
Protein
Crude fiber
Ash
NFE
DA
1.05 ± 0.05
c
20.09 ± 0.07
b
6.83 ± 1.03
a
9.47 ± 0.16
b
62.07 ± 0.98
c
DB
1.47 ± 0.09
a
21.57 ± 0.06
a
4.49 ± 0.08
bc
10.63 ± 0.59
a
61.84 ± 0.64
c
CD-1
1.28 ± 0.00
b
11.3 ± 0.41
d
3.51 ± 0.00
c
4.91 ± 0.41
d
79.00 ± 0.50
a
CD-2
1.56 ± 0.00
a
15.40 ± 0.28
c
5.21 ± 0.00
b
6.46 ± 0.35
c
71.39 ± 0.63
b
DM= Dry matter, NFE= Nitrogen free extract, DA = Diet with alfalfa, DB = Diet with bean flour, CD=
Commercial diets 1 and 2.
a-d;
different letters in the same column indicate significative difference
(p<0.05)
Table 5: Regression coefficients of the response surface models
Responses
Coefficients
R
2
Interception
Lineal
Quadratics
Interaction
b
0
X
1
X
2
X
1
2
X
2
2
X
1
X
2
IE-DA
0.995
0.000
0.007
-0.003
-0.004
-0.002
0.12
IE-DB
0.998
0.009
-0.001
-0.004
0.004
0.005
0.69
BD-DA
1143.006
-57.904
-28.982
-20.812
-15.062
-22.147
0.55
BD-DB
1078.220
-9.873
-38.702
-0.069
8.335
-14.969
0.85
WAI-DA
4.107
0.160
-0.371
-0.035
-0.014
0.123
0.74
WAI-DB
3.671
-0.068
-0.023
0.021
-0.032
-0.112
0.47
WSI-DA
2.082
-0.002
0.053
0.012
-0.056
0.007
0.54
WSI-DB
2.118
0.010
0.012
-0.006
-0.017
-0.015
0.86
H-DA
82.767
-8.719
-13.535
-1.954
5.481
15.110
0.74
H-DB
76.745
-1.037
-3.382
-1.686
-4.544
-5.026
0.46
IVD-DA
91.522
-0.532
0.313
0.520
0.249
0.915
0.71
IVD-DB
93.144
0.774
-0.585
-1.679
-1.233
-0.218
0.70
X
1
= Temperature; X
2
= Moisture. *Bold parameters are significant (p < 0.05). EI= Expansion index, BD= Bulk density, H=
Hardness, WAI= Water absorption index, WSI= Water solubility index, IVD= In Vitro digestibility. DA = Diet with
alfalfa, DB = Diet with bean flour
OPTIMIZATION OF THE EXTRUSION PROCESS TEMPRATURE AND MOISTURE CONTENT …
105
J. Anim. Sci. Adv., 2011, 1(2):100-110
Moisture and extrusion temperature effect on
water absorption index (WAI), water solubility
index (WSI) and hardness (H)
WAI is firstly related to the amount of
absorbed water by the starch granules after swallow
in water excess and can be used as a gelatinization
grade index (Van den Einde et al., 2003; Chevanan
et al., 2007; Rodríguez-Miranda et al., 2011), and
secondly to the proteins hydrophilic balance in the
mixture, which changes according to the
denaturalization grade of the aforementioned, where
the extrusion process changes the solubility profiles
(Singh et al., 2007).
Table 5 presents WAI regression analysis.
Temperature and moisture in their lineal terms have
effect (p < 0.05) on DA and don´t have effect on
DB. DA’s moisture lineal negative regression
coefficient (Table 5) indicates that increasing
moisture from 18 to 22%, WAI decreases and DA’s
temperature lineal positive regression coefficient
indicates that increasing temperature from 120 to
150 °C, WAI increases (Figure 3).
Low WAI values obtained at low temperatures
indicate restricted water availability for the starch
granule, due to a more compact structure. However,
when temperature increases, amylose and
amylopectin chains form an expandable matrix that
translates into a higher water retention capacity
(Colonna et al., 1989; Kokini et al., 1992). If
temperature increases beyond a limit, WAI reaches
a maximum and then decreases as a starch
dextrinization result according to Anderson et al.,
(1969a, b; Anderson, 1982). This effect was also
observed by Gujska and Khan (1990), whom found
that WAI was higher by increasing the initial
moisture content in pinto bean extrudates, which
increased from 3 (110 °C) to 4 (132 °C).
WSI it´s directly related to the starch
degradation level that’s happening inside the
extruder (Harper, 1981). Table 5 presents WSI
regression analysis. Moisture, in its lineal term, has
effect (p < 0.05), on DB, also in its quadratic term
and the moisture-temperature interaction. The
studied variables didn’t present a significative effect
(p < 0.05) on DA. DA’s moisture lineal positive
regression coefficient (Table 5) indicates that
increasing moisture from 18 to 22% WSI increased.
WSI increases as temperature increases (Figure 4),
due to the starch and other macromolecules retro
polimerization present in the mixture, which leads
to amylose and amylopectin chains reduction
(Anderson et al., 1982). This probably happens due
that during the extrusion process, high moisture
content increases gelatinized starch percentage,
obtaining higher WSI values (Chang et al., 1998;
Colonna et al., 1989; Hernández-Díaz et al., 2007),
because of the lower shearing forces produced by
the mixture’s viscosity decrease. Proteins can
interact with the starch through the crossed bonds
formation (Goel et al., 1999; Fernández-Gutiérrez et
al., 2004).
Hardness it’s an extrudate product physical
chemical property that is strongly related to raw
materials extrusion temperature and moisture
content as its starch content (De Pilli et al., 2008).
Table 5 presents H regression analysis. Moisture in
its lineal term, presented a significative effect (p <
0.05) on both diets. DB’s moisture in its quadratic
term has effect (p < 0.05); also, temperature-
moisture interaction has effect (p < 0.05). Moisture
negative lineal coefficients regression on both diets
(Table 5) indicate that increasing moisture from 18
to 22% H decreases, having a greater effect (p <
0.05) on DA, in which greater H values were
obtained. H presents a correlation to EI and BD
indicating with it that diets with high EI and low
densities present low H values.
Moisture and extrusion temperature effect on
extrudates In vitro digestibility (IVD)
Cattle feed nutritional value knowledge it’s
fundamental, since chemical analysis are not
enough, digestion processes such as absorption and
animal metabolism have to be considered (Bondi,
1989). Digestibility tests allow to estimate the
present nutrients proportion in a ration that can be
absorbed by the digestive apparatus (Church &
Pond, 1994) left available for the animal (Bondi,
1989). Table 5 presents IVD regression analysis.
Temperature in its quadratic term has effect (p <
0.05) on DB. The studied variables didn’t present a
significant effect (p < 0.05) on DA. DB’s
temperature lineal negative regression coefficient
(Table 5) indicates that increasing temperature from
120 to 150°C, IVD increases (Figure 1).
Figures 1A and 1B show moisture and
extrusion temperature effect on IVD, diets response
surfaces (DA and DB) present that DA’s highest
REYES-JAQUEZ ET AL.
106
IVD are obtained at high temperature and high
moisture content, however, also at low moisture
content (16-17%) and at low temperatures (110-
120°C). DB’s response surfaces present IVD
highest values at intermediate moisture content (19-
21%) and at intermediate temperatures (120-
135°C), representing an energy savings in their
elaboration.
Extrusion it’s a high temperature-short time
(HT-ST) treatment that promotes starch
gelatinization, which makes amorphous and
crystalline starches more digestible (Camire et al.,
1990). It also leads to protein partial
denaturalization that diminishes rumen’s protein
degradability (Chapoutot & Sauvant, 1997;
Prestløkken, 1999). However, few researches have
investigated the thermic treatment effect on non-
degraded proteins intestinal degradability and the
few results are controverted in function on the kind
and intensity of the treatments (Dakowski et al.,
1996; Prestløkken, 1999). Besides, due the
extrusion, some positive results have presented on
meat production, especially on young animals
(Serrano et al., 1998; Solanas et al., 2004). This
effect could be related to the different physical-
chemical modifications that extrusion produce in
nutrients affecting carbohydrates and proteins
digestion (Solanas et al., 2007). Prestløkken (1999)
and Solanas et al. (2005) demonstrated a decrease
in In Situ protein degradability for different feeding
sources, especially on protein supplements, without
an adverse effect on post non-degraded protein
ruminal digestion. A higher rumen’s energy
availability due starch gelatinization could lead to a
higher microbial growth and duodenum’s bacterial
protein flow increase. However, Russell (1998)
suggests that rumen’s quick energy availability it’s
related to the easily fermented carbohydrates
presence, little ammoniac and amino acids
availability due proteins degradation, which gives
room to a lower microbial protein synthesis
efficiency.
Diets chemical composition
Table 4 shows commercial meals, DA and DB
proximal chemical analysis results. Ruminants’
owners’ main concern focus on energy
(carbohydrates), protein, minerals, vitamins and
water. Energy it’s responsible of growth functions,
animal maintaining and heat generation. Protein
makes tissue grow and performs other vital
functions. Other nutrients and minerals like
Vitamins A and E, calcium, phosphorus and
selenium can be feed at “free election” as a mineral
supplement (Lee Rinehart, 2008).
Optimization
Numerical optimization was performed through
the superposition of the different surface responses
(EI, BD, WAI, WSI, H and IVD), for each one of
the diets, basing on the obtained results from the
commercial products, establishing as optimum
values that must contain the elaborated extrudates
with the finality of finding the values inside this
range for each one of the evaluated diets. DA’s best
conditions were at 145°C and a 22.3% moisture
content with an EI of 1, BD of 845.4 Kg/m
3
, WAI
of 3.7 g/g, WSI of 2.1, H of 73.9 N and an IVD of
92.7%. DB’s best conditions were at 120°C with a
22% moisture content, with an EI of 1, BD of
1145.8 Kg/m
3
, WAI of 3.5 g/g, WSI of 2.1%, H of
72 N and an IVD of 92%, with this diet, a less
moisture content and less temperature are required,
demonstrating that at higher starch content in the
extruder, less energy is required to obtain an
optimum gelatinization (Camire et al., 1990;
Balandrán-Quintana, 1998; Zazueta-Morales et al.,
2002; Pérez-Navarrete, 2006). While DA require a
higher temperature and moisture content to obtain
diets that are in the commercial diets physical
characteristics range. Hence the use of waste bean
flour represents energetics savings.
Conclusions
Table 4 demonstrates that DA and DB are
nutritionally much more superior than commercial
meals, adding the fact that waste bean flour is used,
resulting in a cheaper product. Also the fact that DA
and DB have a high IVD, makes an overall
excellent alternative for cattle feed. Bean can be a
viable option for cattle feed, not only in raw
material availability terms, but also in extrudates
production costs, as it possible to use low
temperatures and moisture contents. This research
development was made in tight relation with the
private sector, assuring that the obtained results
OPTIMIZATION OF THE EXTRUSION PROCESS TEMPRATURE AND MOISTURE CONTENT …
107
J. Anim. Sci. Adv., 2011, 1(2):100-110
have a direct industry application and hence its
commercialization.
A
B
Fig. 1: Temperature and moisture content effect on A= DA = Diet with alfalfa, B= DB = Diet with bean flour on In vitro
digestibility
A
B
Fig. 2: Temperature and moisture content effect on A: alfalfa diets = D1, B: waste bean diets = D2 on expansion index
A
B
Fig. 3: Temperature and moisture content effect on A: alfalfa diets = D1, B: waste bean diets = D2 on water absorption
index
REYES-JAQUEZ ET AL.
108
A
B
Fig. 4: Temperature and moisture content effect on A: alfalfa diets = D1, B: waste bean diets = D2 on water solubility
index
References
Anderson, R. A., Conway, H. F., Pfeifer, V. F., & Griffin, E.
L. 1969a. Gelatinization of corn grits by roll and extrusion
cooking. Cereal Science Today, 14, 4-12.
Anderson, R.A., 1982. Water absorption and solubility and
amylograph characteristics on roll-cooked small grain
products. Cereal Chemistry, 59: 265-269.
Anderson, R. A., Conway, H. F., Pfeifer, V. F., & Griffin, E.
L. 1969b. Roll and extrusion-cooking of grain sorghum
grits. Cereal Science Today, 14: 372- 381.
ANKOM, 2000. In vitro true digestibility using the DAISYII
incubator. Ankom Inc. Macedon, NY, USA.
Association of Official Analytical Chemistry (AOAC). 2005.
International. Official Methods of Analysis., 15th ed. The
Association of Official Analytical Chemists: Arlington,
Va, 2005:Vol. II.
Balandrán-Quintana, R.R., Barbosa-Cánovas, G.V., Zazueta-
Morales, J.J., Anzaldúa- Morales, A., Quintero-Ramos, A.,
1998. Functional and nutritional properties of extruded
whole pinto bean meal (Phaseolus vulgaris L.). J. Food
Sci. 63, 113-116.
Beltrán Juan Carlos. 1992. Efecto de la suplementación con
orejero (Enterolobium Cyclocarpum) sobre el
funcionamiento ruminal, tesis Corporación Universitaria
de ciencias Agropecuarias, facultad de medicina
veterinaria. 151-247.
Bhattacharya, M., Hanna, M.A., 1987. Influence of process
and product variables and extrusion energy and pressure
requirements. J. Food Eng. 6, 153-163.
Bondi, A. A. 1989. Nutrición Animal. Editorial Acribia, S. A.
Zaragoza, España. 546.
Camire, M.E., 1990. Chemical and nutritional changes in food
during extrusion. Crit. Rev. Food Sci. Nutr. 29 (1), 35-57.
Chamorro, Diego. Gallo, Jorge. Arcos, Juan. y Vanegas,
Miguel. 1998. Gramíneas y Leguminosas, consideraciones
agrozootécnicas para ganaderías del trópico Bajo. Boletín
de investigación. CORPOICA. Regional 6. Doc. 18405.
Capítulo 6.
Chang, Y.K., Wang, S.S. 1998. Advances in Extrusion
Technology (Aquaculture/Animal feeds and foods).
Lancaster, PA, USA: Technomic.
Chapoutot, P. and Sauvant, D. 1997: Nutritive value of raw
and extruded pea-rapeseeds blends for ruminants. Animal
Feed Science and Technology. 65, 5977.
Chevanan, N., Rosentrater, K.A., Muthukumarappan, K.,
2007. Twin screw extrusion processing of feed blends
containing distiller’s dried grains with solubles (DDGS).
Cereal Chem. 84(5), 428-436.
Chiang, B.Y., Johnson, J.A., 1977. Measurement of total and
gelatinized starch by glucoamylase and o-toluidine
reagent. Cereal Chem. 54(3), 429-435.
Chinnaswamy, R., Hanna, M.A., 1987. Optimum extrusion
cooking conditions for maximum expansion of corn starch.
J. Food Sci. 53 (3), 834-836
Church, D. C. y Pond. W. G. 1994. Fundamentos de nutrición
y alimentación de animales. Editorial Limusa, S. A. de C.
V. Grupo Noriega Editores. México. 438.
Colonna, P., Doublier, J.L., Melcion, J.P., De Monredon, F.,
Mercier, C., 1984. Extrusion cooking and drum drying of
wheat starch. I. Physical and macromolecular
modifications. Cereal Chem. 61, 538-543.
Colonna, P., Tayeb, J., Mercier, C., 1989. Extrusion cooking
of starch and starchy products, in Extrusion Cooking, C.
Mercier, P. Linko and J.M. Harper (Ed.), p. 247- 319. Am.
Assoc. Cereal Chem., Inc., St. Paul, MN.
Conway, H.F., Anderson, R.A., 1973. Protein fortified
extruded food products. Cereal Sci. Today 18, 94.
Cortes Javier Eduardo y Gutiérrez Eduardo Alberto. 1997.
Efecto de la reducción de protozoarios ciliados sobre el
funcionamiento ruminal de ovinos alimentados con tamo
de trigo. Tesis, Universidad de la Salle Facultad de
zootecnia, 69-122.
Dakowski, P., Weisbjerg, M. R. and Hvelplund, T.1996: The
effect of temperature during processing of rape seed meal
on amino acid degradation in the rumen and digestion in
OPTIMIZATION OF THE EXTRUSION PROCESS TEMPRATURE AND MOISTURE CONTENT …
109
J. Anim. Sci. Adv., 2011, 1(2):100-110
the intestine. Animal Feed Science and Technology. 58,
213226.
Davidson, V.J., Paton, D., Diosady, L.L., Larocque, G., 1984.
Degradation of wheat starch in a single-screw extruder:
characteristics of extruded starch starch polymers. J. Food
Sc. 49, 453-458.
De Pilli, T., Carbone, B.F., Derossi, A., Fiore, A.G., and
Severini, C. 2008. Effects of operating conditions on oil
loss and structure of almond snacks. J. Food Sc. 43, 430-
439.
Diaz, A., Avendano, M. and Escobar, A. 1993. Evaluation of
Sapindus saponaria as a defaunating agent and its effects
on different ruminal digestion parameters. Livestock
Research for Rural Development, 5: 2-4.
El Excelsior (1996). En peligro, 2 millones de cabezas de
ganado por la sequía. México D.F. Disponible en: /http://
excelsior.com.mx/960513/nac11.htmlS.
Fernández-Gutiérrez, J.A., Martin-Martínez, E.S., Martínez-
Bustos, F., & Cruz-Orea, A. 2004. Physicochemical
properties of caseinstarch interaction obtained by
extrusion process. Starch/Stärke, 56, 190198.
Goel, P.K., Singhal, R.S. & Kulkarni, P.R., 1999. Studies on
interactions of corn starch with casein and casein
hydrolysates. Food Chemistry, 64, 383389.
Gujska, E., Khan, K., 1990. Effect of temperature on
properties of extrudates from high starch fractions of navy,
pinto and garbanzo beans. J. Food Sci. 55. 466-469.
Gujska, E., Khan, K., 1991. Feed moister effects on functional
properties, trypsin inhibitor and hemaglutinating activities
of extruded bean high starch fractions. J. Food Sci. 56,
443-447.
Harper, J. M. 1981. Extrusion of Foods. Vols. I and 2. CRC
Press: Boca Raton, Fl.
Hernández-Díaz, J. R.; Quintero-Ramos, A.; Barnard, J., &
Balandrán-Quintana, R.R. 2007. Functional properties of
extrudates prepared with blends of wheat flour/pinto bean
meal with added wheat bran. Food Science and
Technology International, 13(4), 301-308.
Kokini, J. L., Lai, L., & Chedid, L. L. 1992. Effect of starch
structure on starch rheological properties. Food
technology. 46(6): 124-139.
La Jornada. (2002). La sequía en Sonora es aun manejable:
López Nogales. Disponible en:
/http://www.jornada.unam.mx/2002/05/22S.
Lee Rinehart. 2008. Nutrición para Rumiantes en Pastoreo.
Attra. Eds; Paul Driscoll. 1-20.
Navas Alberto, Laredo M. A, Cuesta Aurora, Anzola Hector
and Leon J. C 1992. Evaluation of Enterolobium
ciclocarpum as dietary alternative to eliminate protozoa
from the rumen. Livestock Research for Rural
Development, 4, (1).4.
Owusu-Ansah, J., van de Voort, F.R., Stanley, D.W., 1984.
Textural and microstructural changes in corn starch as a
function of extrusion variables. Canadian Institute of Food
Science and Technology Journal. 17, 65-70.
Payne J; Rattink W; Smith T; Winowiski T (1994). The
Pelleting Hand Book. Borregard Lignotech, England: 115-
119
Pérez-Navarrete, C., Gonzáles, R., Chel-Guerrero, L.,
Betancur-Ancona, D., 2006. Effect of extrusion on
nutritional quality of maize and Lima bean flour blends. J.
World Aquaculture. Soc. 86, 2477-2484.
Prestløkken, E. 1999. In situ ruminal degradation and
intestinal digestibility of dry matter and protein in
expanded feedstuffs. Animal Feed Science and
Technology. 77, 123.
Rodríguez-Miranda, J., Ruiz-López, I.I., Herman-Lara, E.,
Martínez-Sánchez, C.E., Delgado-Licon, E., & Vivar-
Vera, M.A., 2011. Development of extruded snacks using
taro (Colocasia esculenta) and nixtamalized maize (Zea
mays) flour blends, LWT-Food Science and Technology,
44; 673-680.
Russell, J. B., 1998: Strategies that ruminal bacteria use to
handle excess carbohydrate. Journal of Animal Science.
76, 19551963.
Sacchetti, G., Pittiam, P., Pinnavaia, G.G., 2005. The effect of
extrusion temperature and drying- tempering on both of
kinetics of hydration and the textural changes in extruded
ready-to-eat breakfast cereals during soaking in semi-
skimmed milk. Int. J. Food Sci. Technol. 40, 655-663.
Serrano, X.; Baucells, M. D.; Barroeta, A. C.; Puchal, F. 1998:
Effects of extruded diet on the productive performance of
weaning and post-weaned calves. Animal Feed Science
and Technology. 70, 275279.
Singh, S., Gamlath, S., & Wakeling, L. 2007. Nutritional
aspects of food extrusion: a review. International Journal
of Food Science and Technology, 42, 916929
Solanas, E.; Castrillo, C.; Serrano, X.; Guada, J. A. 2004: The
effect of cereal and/or protein supplement extrusion on diet
utilization and performance of intensively reared cattle. In:
ESVCN (ed.) Proceedings of the 8th International
Conference of European Society of Veterinary and
Comparative Nutrition. Budapest, Hungary, pp. 217.
Solanas E., Castrillo C., Balcells J. and Guada J. A. 2005. In
situ ruminal degradability and intestinal digestion of raw
and extruded legume seeds and soya bean meal protein.
Journal of Animal Physiology and Animal Nutrition. 89,
166171.
Solanas E., Castrillo C. and Calsamiglia S. 2007. Effect of
extruding the cereal and/or the legume protein supplement
of a compound feed on in vitro ruminal nutrient digestion
and nitrogen metabolism. Journal of Animal Physiology
and Animal Nutrition. 91: 269277.
Tejada, L. 1992. The thermal decomposition of carbohydrates.
Applied Science Publishers LTD. London.-
Valadez, M., Munoz-Hernandez, G., Sanchez-Lopez, R.
(2008), Design and evaluation of an extruder to convert
crop residues to animal feed, Biosystems Engineering 100:
66-78
Van den Einde, R. M., Van der Goot, A. J., & Boom, R. M.
2003. Understanding molecular weight reduction of starch
during heating-shearing process. Journal of Food Science,
68, 396-2904.
Wang, W.M., Klopfenstein, C.F., Ponte, J.G., 1993. Effects of
twin-screw extrusion on the physical properties of dietary
fiber and other components of whole wheat and wheat bran
REYES-JAQUEZ ET AL.
110
and on the baking quality of the wheat bran. Cereal Chem.
70, 707-711.
Zazueta-Morales, J., Martínez-Bustos, F., Jacobo-Valenzuela,
N., Ordorica-Falomir, C., Paredes-López, O., 2002. Effects
of calcium hydroxide and screw speed on physicochemical
characteristics of extruded blue maize, J. Food Sci. 67, (9),
3350-3357.
... The chemical content of all ingredients (Table 1) is comparable to other reports (Reyes-Jáquez et al., 2011), except for alfalfa's ash content, which is 2% above reported values, possibly due to a higher presence of fertilizers. Also, alfalfa's crude protein content was slightly higher than other reports (Coblentz and Hoffman, 2009). ...
... All regression coefficients of EI are low (Table 2), possibly because NFE (Table 1) is not high enough to expand, and, process conditions did not yield a significant pressure differential, thus influencing only shaping, not expansion. These results are similar to others (Reyes-Jáquez et al., 2011), where similar diets were extruded at the same T but with higher MC (18 -22%) and without oil. Oil adding in extrudates decreases starch gelatinization due to lower shear stress applied upon the mixture since it acts as a lubricant; it also promotes lipid-starch complexes' formation, restraining water-starch interaction, resulting in lower EI (Liu et al., 2006). ...
... which are acceptable values compared to other reports(Reyes-Jáquez et al., 2011). It can be concluded that OC and anti-nutritional factors presence did not have a significant difference in IVD nor ED since they were inactivated by high T and shear stress during processing. ...
Article
Full-text available
Preparation of extruded products with high oil content, presents a technological challenge, due oil decreases specific mechanic force but also acts as a lubricant, and forms starch-lipid complexes; thus, decreasing starch gelatinization. This research aimed to evaluate the effect of temperature, moisture, and sunflower oil content, on the extrusion process of bovine cattle feed. Two main ingredients were used for each diet: alfalfa (Medicago sativa L.), and bean (Phaseolus vulgaris L.). The obtained results showed that high temperature, moisture, and oil content, decreased bulk density, and hardness (P < 0.05). Oil content-temperature interaction increased both bulk density and hardness, while moisture-oil content interaction increased (P < 0.05) hardness. Optimization was performed based on the physicochemical characteristics of commercial feeds, showing that the best bean diets were obtained at 121ºC, 14% moisture content with 0% sunflower oil; 120ºC and 16% moisture content with 3.5% sunflower oil; and, 142ºC and 15% moisture content with 7% sunflower oil. Effective degradability ranged from 87.4 -90.4% for all extruded diets; and none of them showed significant differences between bean and alfalfa (P < 0.05), which opens a high potential opportunity of producing high concentrations of CLA from sunflower oil at a ruminal level.
... Bulk density can be increased by decreasing moisture content, barrel temperature and screw speed. The expansion and texture of extrudates is more complex for products made with more than one component [17,[23][24][25]. The multiphase structure affects the elastic properties of extrudates. ...
... Expansion is reduced at concentrations of 50% of each component. It has been demonstrated that plant protein can be combined with corn flour protein as a complement to obtain highly valuable protein flour, and that extrusion is an alternative processing method for obtaining extruded products with high protein content for human or animal consumption [23][24][25]. Extruded snacks are quite popular [26]. An extruded snack made of cottonseed meal-corn flour may increase its nutritional value. ...
... Fat, protein, fiber, ash, and nitrogen free extract (NFE) of CSM, CSM/corn flour extrudate and commercial snacks are summarized in Table 2. Fat and protein content in CSM is higher than in legumes or corn used for extrusion by other authors [23,24], while the NFE is lower. Low NFE concentrations limit significantly the amount of CS-M used for extrusion. ...
Article
Full-text available
The results of the present study indicate that glandless cottonseed meal (CSM) can be incorporated in extruded corn flour snacks at a 10% content level, which increases snack protein content to 12.8% and reduce fat content to 6.2%. To improve snacks’ nutritional quality, CSM and corn flour were extruded using a simple screw extruder. An expansion index (EI) ranging of 1.2 - 4.7 was obtained. Penetration force (PF) was 7 - 9 times harder than other extruded products. High extrusion temperature and high CSM concentrations decreased (p < 0.05) EI, water activity, and water absorption index. Higher CSM concentrations can be incorporated into extrudates if snacks are processed at higher extrusion moistures. CSM increased (p < 0.05) extrudates’ PF giving them a unique crunchy texture. CSM decreased (p < 0.05) extrudates’ water solubility index. Extrusion conditions used showed a 68.5% starch gelatinization, and a starch avail-ability of more than 97%, which explains the high expansion index obtained.
... The use of densification processes such as extrusion and pelleting allows the inclusion in the diet of diverse ingredients that translate into nutritional improvements, transportation, handling and storage are also facilitated, costs are reduced and acceptability by animals is improved. Its use for the manufacture of supplements has resulted in improvements in fermentation and reduction of methane production in vitro (Reyes-Jáquez et al., 2011;Kang et al., 2016;Nguyen et al., 2020). ...
Article
Full-text available
Background: The use of non-conventional food sources is a key element in facing the current problems derived from climate change and food shortages that demand the establishment of new sustainable feeding systems for ruminants. Moreover, densification methods like pelleting constitute a way to improve the quality and acceptability as well as to facilitate the handling of supplements. The objective of this study was to evaluate Huizache leaves and agave bagasse incorporated into granulated and pelletized concentrates and their effects on methane production and in vitro fermentation patterns in ruminant diets. Methods: A protein concentrate granulated and pelletized containing Huizache leaves and agave bagasse were mixed with a high-quality forage (alfalfa hay) using a 23 factorial arrangement with a total of six treatments. In each treatment were determined crude protein, carbohydrates, in vitro digestibility, in vitro gas, methane, carbon dioxide, volatile fatty acids, ammoniacal nitrogen and microbial nitrogen. The variables were submitted to an analysis of variance using the procedure MIXED SAS and statistical differences were declared at P<0.05. Result: There was an interaction (P<0.01) between concentrate source (granulated vs pelleted) and relation (alfalfa hay + concentrate source) on maximum gas production "A" (P<0.05). Also, there was an interaction between concentrate source (granulated vs pelleted) and relation (alfalfa hay: concentrated) on microbial nitrogen production (P<0.05). The microbial nitrogen production increased in 55 % with pelleted concentrate in relation to granulated concentrate (P<0.05).
... Previous studies showed that plant proteins, such as pseudocereals and legumes, are excellent animal protein substitutes for food and feed products (Atienzo-Lazos et al., 2011;Delgado-Licon et al., 2008Gorinstein et al., 2001Gorinstein et al., , 2002Gorinstein et al., , 2003Reyes-Jáquez et al., 2011, 2014Rodriguez-Miranda et al., 2012;2014;2016). Plant protein changes the functional properties of the final food products, such as water absorption and solubility index, as well as expansion index of extruded aquaculture feed, compared to animal protein-based products. ...
Article
Full-text available
This investigation aimed to extract and characterize the GCSM proteins, determine their solubility potential at two different temperatures and different solvents, and explore their functional properties. During the extraction, no water‐ or ethanol‐soluble protein was found. Most of the protein was extracted with KOH solution. GCSM showed major protein bands between 13,273 and 56,564 Da with an isoelectric point of 5.1. The results showed that extraction temperature and solvent affected the amount of protein extracted from GCSM. The highest protein yield (63.4%) was obtained with KOH at 55 °C. Fat content negatively affected the protein solubility. The highest protein purity (99.9%) was obtained with 6% of fat content and the lowest one with 19% of fat content. GCSM has a high glutamic acid content, followed by arginine and aspartic acid compared to the other amino acids. The essential amino acids make up about 30.0% of the total amino acid concentration in KOH‐soluble fractions. The results showed a denaturation temperature of GCSM protein ranging from 61.4 to 63.6 °C. Scanning electron microscopy reveals a microglobular protein structure. GCSM protein isolate showed lower (P < 0.05) water‐holding and oil‐holding capacity but similar gelation properties as soy protein. GCSM protein shows a high foaming capacity at high pH values and high emulsion stability. Practical Application The results of this investigation have a direct impact on the plant protein processing industry. This paper presents a new source of plant protein with a high foaming capacity in alkaline conditions with potential applications for human consumption and feed for aquaculture and animals. The results of this research may impact the cotton producers who can increase their income, and the aquaculture industry will have a cheaper source of protein that can partially substitute the expensive fishmeal. Cottonseed protein can be used to develop high protein extruded snacks and other functional foods, such as plant protein‐based food products.
... Sin embargo, cuando la temperatura aumenta, las cadenas de amilosa y amilopectina forman una matriz expandible que se traduce en una mayor capacidad de retención de agua (Colonna et al., 1989;Kokini et al., 1992;Rodríguez-Miranda et al., 2011). Si la temperatura incrementa más allá de un límite, IAA alcanza un máximo y luego disminuye como resultado de la dextrinización del almidón, según lo reportado por (Gujska y Khan, 1990;Reyes-Jáquez et al., 2011). El ISA determina la cantidad de polisacáridos solubles liberados por los gránulos de almidón, después de la adición de agua en exceso, y es frecuentemente utilizado como un indicador de la degradación de componentes moleculares (Van den Einde et al., 2003). ...
Chapter
Full-text available
El objetivo de esta investigación fue desarrollar una dieta balanceada para ganado bovino de engorda a base de semillas de canola (Brassica napus) por extrusión. El proceso de extrusión se realizó en un extrusor de tornillo simple, con relación de compresión 1:1 y dado de salida cilíndrico de 6 mm de diámetro. Se utilizó un diseño experimental central compuesto rotable, con dos variables de proceso: temperatura de extrusión (120 -160 oC) y contenido de humedad (18 – 22%). El análisis estadístico de las variables de respuesta más importantes que influyen en la digestibilidad ruminal de los alimentos elaborados son el índice de absorción de agua (IAA) y el índice de solubilidad en agua (ISA), en los cuales solo el ISA presento un modelo cuadrático significativos (P< 0.05) y sí como el índice de expansión.
... The SA may also compete with the starch for the water available in the mixture since it is responsible for breakage of intrachain hydrogen bonds and formation of new interlinked hydrogen bridges, as well as starch chain association during gelatinization. However, the lower the available water content the lower the degree of starch gelatinization, which decreases expansion (Case et al., 1992; Reyes-Jáquez et al., 2011). High starch content materials require higher moisture content to reach high EI values (OwusuAnsah et al., 1984). ...
Article
Full-text available
Agglutinating compounds are commonly used to improve the physical quality of aquafeeds. An evaluation was done of the effect of the agglutinating compound sodium alginate on the functional properties of aquaculture fish feed produced by extrusion. Meals containing one of four sodium alginate concentrations (0, 0.5, 1.5 and 2%) were extruded in a simple-screw extruder at 120 °C, 20% moisture content and a 1:1 compression ratio, extruding each treatment in duplicate. Expansion index values ranged from 1.11 to 1.12 with no differences (P > 0.05) between the diets containing sodium alginate. In contrast, the different sodium alginate levels had positive (P < 0.05) effects on water absorption index values (2.24 to 2.79 g/g), water solubility index values (10 to 12.94%), sinking velocity (6 to 8.56 cm/s) and hardness (1.98 to 3.31 N). Maximum hardness (3.31 N) was produced in the 2% sodium alginate diet. The highest sodium alginate level tested (2%) had the most appropriate physical and functional properties for an extruded fish meal-based (62%) aquaculture fish feed.
... The SA may also compete with the starch for the water available in the mixture since it is responsible for breakage of intrachain hydrogen bonds and formation of new interlinked hydrogen bridges, as well as starch chain association during gelatinization. However, the lower the available water content the lower the degree of starch gelatinization, which decreases expansion (Case et al., 1992; Reyes-Jáquez et al., 2011). High starch content materials require higher moisture content to reach high EI values (OwusuAnsah et al., 1984). ...
Article
Full-text available
Agglutinating compounds are commonly used to improve the physical quality of aquafeeds. An evaluation was done of the effect of the agglutinating compound sodium alginate on the functional properties of aquaculture fish feed produced by extrusion. Meals containing one of four sodium alginate concentrations (0, 0.5, 1.5 and 2%) were extruded in a simple-screw extruder at 120 °C, 20% moisture content and a 1:1 compression ratio, extruding each treatment in duplicate. Expansion index values ranged from 1.11 to 1.12 with no differences (P > 0.05) between the diets containing sodium alginate. In contrast, the different sodium alginate levels had positive (P < 0.05) effects on water absorption index values (2.24 to 2.79 g/g), water solubility index values (10 to 12.94%), sinking velocity (6 to 8.56 cm/s) and hardness (1.98 to 3.31 N). Maximum hardness (3.31 N) was produced in the 2% sodium alginate diet. The highest sodium alginate level tested (2%) had the most appropriate physical and functional properties for an extruded fish meal-based (62%) aquaculture fish feed.
Article
There is a need to develop new food products with high protein quality and a high caloric value, high acceptability and low costs for low income families. The aim of this investigation was to evaluate in vivo an extruded bean-corn product, supplemented with Ca and Zn, as a potential nutritional snack. Extruded and nonextruded bean-corn flours were fed to rats. Antinutritional factors, rat weight and length, femur weight and heart weight and volume were determined. Microscopy pictures of rat liver were taken. The antinutritional factors present in the studied bean variety did not affect rat growth or internal organ characteristics. Bean-corn diets affected (p<0.05) rat weight and produced liver alterations, probably because of interference by bean protein with intestinal or systemic metabolism. Ca and Zn supplementation is not necessary in a bean-corn extruded snack for rats.
Article
Full-text available
Sweet sorghum (Sorghum bicolour (L.) moench) bagasse (SSB) a by-product obtained after juice extraction from the stalks of sweet sorghum was evaluated as potential roughage source for ruminants using in sacco degradability of dry matter and protein besides in vivo nutritive value. The crude protein (CP) and neutral detergent fibre (NDF) content of SSB were 3.94 and 74.76 per cent, respectively. The in sacco effective degradable dry matter (EDDM) and effective rumen degradable protein (ERDP) per cent of SSB were 40.60 and 55.30, respectively. The digestible crude protein (DCP) and total digestible nutrients (TDN) values of SSB were 1.58 and 51.59 per cent, respectively in graded Murrah buffalo bulls. The study inferred that the chemical composition and nutritive value of SSB are comparable to sorghum straw and may be used as an alternative roughage source four times more economical than sorghum straw in ruminant rations.
Article
The effect of extrusion variables (temperature, feed moisture and screw speed) on the expansion, breaking strength and microstructure of starch extrudates was studied using response surface methodology. For expansion the most significant variable was found to be feed moisture which bore an inverse relation to the expansion response. All the extrusion variables studied were significantly related to expansion and accounted for 95.7% of the total variation. Screw speed and feed moisture were the most significant variables for breaking strength, all three variables accounting for 89.7% of the total break strength variation. Microstructure of the extrudates could be related to the extrusion variables, the expansion and breaking strength responses. The porosity of the extrudates increased with decreasing moisture, with a concomitant increase in expansion and a decrease in breaking strength. Regression equations generated from composite rotatable response surface design experiments could be used to accurately predict the responses studied.
Article
Blends made of wheat flour and bean meal at various levels of moisture and bran content, were subjected to extrusion cooking by varying temperature and screw speed. Extrudates were analysed for expansion index, bulk density, apparent viscosity, water absorption index and water solubility index using a second-order rotatable central composite design. Excepting water absorption index, functional properties were significantly affected ( p<0.05) by levels of moisture, bran or extrusion conditions. Expansion index decreased with increasing levels of moisture in the blends; for bran the effect was the inverse. Response surface solution for apparent viscosity was maximum at 24% levels of moisture, 209r.p.m., 180°C and 10% bran. For water absorption index the response surface solution was a saddle point, with a minimum at 29% levels of moisture, 232r.p.m., 177°C and 25% bran. The higher apparent viscosity and lower absorption index reflected minor damage to starch and proteins, which was attributed to a protective role of the added fibre.
Article
Extrusion trials were conducted with varying levels of distillers dried grains with solubles (DDGS) along with soy flour, corn flour, fish meal, vitamin mix. mineral mix, and net protein content adjusted to 28% using a Wenger TX-52 twin-screw extruder. The properties of extrudates were studied in experiments conducted using a full-factorial design with three levels of DDGS content, two levels of moisture content, and two levels of screw speed. Increasing the DDGS content from 20 to 60% resulted in a 36.7% decrease in the radial expansion, leading to a 159 and 61.4% increase in the unit density and bulk density of the extrudates, respectively. Increasing the DDGS content resulted in a significant increase in the water absorption index (WAI) but a significant decrease in the water solubility index (WSI) of the extrudates. Changing the screw speed and moisture content had no significant effect on the radial expansion ratio but resulted in a significant difference in the bulk density of the extrudates, which may be due to the occurrence of longitudinal expansion. Even though changing the moisture content and screw speed had no significant effect on the WSI of the extrudates, significant differences in the WAI of the extrudates were observed. The ingredient components in the blend and moisture content had an influence on the color changes of the extrudates, as did the biochemical changes occurring inside the barrel during processing. Overall, it was determined that DDGS could be included at a rate of up to 60% using twin-screw extrusion, and that viable pelleted floating feeds can be produced.