
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.