
This scientic publication in digital format is a continuation of the Printed Review: Legal Deposit pp 196802ZU42, ISSN 0378-7818.
Carrasquero et al. Rev. Fac. Agron. (LUZ). 2025, 42(2): e254224
3-6 |
added to 1 L of distilled water. Subsequently, the dierent turbidity
values tested (13, 75, and 200 NTU) were obtained through successive
dilutions, with the following true color levels of 9, 19, and 32 UC Pt-
Co, respectively.
Coagulant solution
C. lanatus seeds were collected from residues from producing
fruit juices and salads in Maracaibo, Zulia state, Venezuela. It should
be noted that the endosperm was used; so, the seeds were washed,
then manually peeled and dried in an oven (Hamilton Beach, Mod.
31105, USA) at a temperature of 60 ± 5 °C for 2 h, then processed in a
manual mill (Corona Nacional, Venezuela) until obtain a our, which
was sieved through a 60 sieve (0.250 mm pore diameter) and stored in
amber jars for subsequent characterization, defatting and use.
The our obtained was defatted using the Soxhlet method. Twenty-
ve grams (25 g) were weighed and placed in an extraction cartridge,
and 150 mL of hexane (Merck, Purity 98.5 %) was added to the
ask; the extraction was performed for 8 h at a temperature of 45 °C.
Once the seeds were defatted, they were dried in an oven (Hamilton
Beach, Mod. 31105, USA) for 4 h at 50 °C (Association of Ocial
Analytical Chemists [AOAC], 2005). Then, they were characterized
by the following parameters: Humidity (Venezuelan Commission of
Industrial Standards [COVENIN], 1980), ash content (COVENIN,
1981a), and extractable oils and fats (COVENIN, 1981b).
The coagulant was prepared with 5 g of the seed previously
ground, sieved, and defatted, in a volume of 1 L of distilled water.
Subsequently, the evaluated doses were obtained by dilution: 50, 70,
90, 100, 150, 200, 250, 300, 400, and 500 mg.L
-1
as recommended
by Carrasquero et al. (2019). Coagulation-occulation tests were
performed using the Jar test in variable agitation equipment (Phipps and
Brid Inc., Mod. 300, USA), treating synthetic waters of low, medium,
and high turbidity, i.e., 13, 75, and 200 NTU, simulating drought and
rainfall conditions that can cause turbidity variations in natural water
bodies (Bina et al., 2009).
Eciency of the natural coagulant in the clarication process
Five hundred (500 mL) of STW were poured into the beakers, then
the dierent quantities of coagulant were dosed, and rapid mixing was
initiated, which corresponded to coagulation, at 100 rpm for 2 min,
followed by occulation with a slow mixture at 30 rpm for 20 min,
and, nally, sedimentation was carried out for 30 min. At the end of
this time, a sample of treated water was extracted, and ltered in a
vacuum pump using Whatman paper with a pore size of 25 μm, for the
determination of the physicochemical parameters: true color (platinum-
cobalt method), turbidity (nephelometric method), total alkalinity
(volumetric method), pH (standard potentiometric method), total
dissolved solids (gravimetric method), and total solids (gravimetric
method), following the Standard Methods for the Examination of
Water and Wastewater (Lipps et al., 2022).
To determine the eect of coagulation time in the rapid mixing
phase, Jar tests were performed by applying the doses that generated
the lowest values of turbidity and true color obtained in the previous
section under dierent times (1, 2, 4, and 5 min).
Experimental design
The results of the physicochemical parameters measured in seed
characterization were expressed using descriptive statistics, indicating
the values of central tendency (mean) and dispersion (standard
deviation). The results of the removal of physicochemical parameters
were studied using an analysis of variance and comparison of means
through Tukey’s test, using the statistical program IBM SPSS
Statistics. Before performing the ANOVAs, both the homogeneity
of the variances (Bartlett’s test) and the normal distribution of the
residuals (Kolmogorov-Smirnov Test) were checked, complying with
these precepts without requiring mathematical transformation.
In the rst stage, the eectiveness of the coagulant solution in
removing turbidity and true color for dierent initial turbidity levels
was evaluated, using a completely randomized design with a total of 9
assays (3 turbidity levels × 3 repetitions). For this statistical analysis,
a one-way ANOVA was applied, complemented with Tukey’s mean
separation test. In the second stage, the eect of mixing time on
coagulant eectiveness was studied, applying a 3×4 factorial design
(three turbidity levels by four stirring times), with a total of 12
treatments. In this case, a two-way ANOVA was used, followed by
Tukey’s test for the comparison of means.
Results and discussion
Physicochemical characteristics of C. lanatus seed
The preliminary characterization of the seed was carried out by
determining moisture, oils and fats, and ashes, as physicochemical
parameters (table 2).
Table 2. Physicochemical characteristics of C. lanatus seed.
Parameter ( % ) Arithmetic mean value ± standard deviation
Removable oils and fats 25.40 ± 1.76
Moisture 5.43 ± 0.42
Ash content 4.07 ± 0.15
n:3. N: Number of repetitions.
The average percentage of oils and fats was 25.40 %, a value
higher than that reported for other seeds used in the clarication
process, such as Mangifera indica L. (15.00 %), and Tamarindus
indica (7.63 %) (Carrasquero et al., 2019), which conrms the need
to defat the seed before performing clarication tests because the
natural coagulant could incorporate dissolved particles, fats and oils
from the seed (Carrasquero et al., 2015). Regarding the percentage
of moisture, an average value of 5.43 % was found, which is positive,
because a higher water content would accelerate the appearance of
decomposition reactions, which would cause the deterioration of the
seed.
Eectiveness of C. lanatus seeds by applying various doses
in the treatment of synthetic waters with three levels of initial
turbidity
At the end of the treatments, a decrease in turbidity was obtained
compared to the initial values. However, the increase in coagulant dose
was associated with slight increases in measured residual turbidity,
although they always remained below the original levels, evidencing
the eectiveness of the seed in turbidity removal (gure 1).
The results obtained showed a turbidity elimination range of
46.6 to 96.8 % during the analysis of all synthetic turbid waters.
For an initial turbidity of 13 NTU, values were obtained after the
coagulation-occulation process, ranging from 0.82 to 7.43 NTU,
applying doses between 50 and 500 mg.L
-1
. The highest percentages
of turbidity reduction, 91.8 and 92.5 %, were obtained using doses
of 50 and 70 mg.L
-1
, respectively, presenting statistical dierences
(p≤0.05) with the rest of the doses applied.