Green solvent extraction and quality characteristics of passion fruit seed oil (Passiflora edulis Sims var. edulis)

ISSN 2588-1299  
VJAS 2019; 2(4): 469-474  
Vietnam Journal  
of Agricultural  
Sciences  
Green Solvent Extraction and Quality  
Characteristics of Passion Fruit Seed Oil  
(Passiflora edulis Sims var. edulis)  
Nguyen Thi Thu Nga, Nguyen Xuan Bac & Lai Thi Ngoc Ha  
Faculty of Food Science and Technology, Vietnam National University of Agriculture,  
Hanoi 131000, Vietnam.  
Abstract  
The extraction of oil from passion fruit seeds with acetone, ethanol,  
ethyl acetate, isopropanol, and hexane was studied. The effects of the  
variables, namely type of solvent, material to solvent ratio,  
temperature, and extraction time, were investigated. The highest  
extraction yield was 78.52%, which was obtained using ethyl acetate  
with a material to solvent ratio of 1/10 at room temperature (28oC)  
for 4h using a shaker. This yield was similar to that obtained when  
using hexane as a solvent. Our results indicate that ethyl acetate can  
replace the conventional hexane solvent in the extraction of oil from  
passion fruit seeds. The high content of polyunsaturated fatty acids in  
passion fruit seed oil suggests that this product has good potential for  
use in the human food, cosmetic, and pharmaceutical industries.  
Keywords  
Oil extraction, Passiflora edulis Sims var. edulis, passion fruit seed  
oil, polyunsaturated fatty acids  
Introduction  
The purple passion fruit (Passiflora edulis Sims var. edulis) and  
the yellow passion fruit (Passiflora edulis Sims var. flavicarpa) are  
two subvarieties of P. eduliks, which is the significant commercial  
value variety of the family Passifloraceae (Rehm & Espig, 1984). The  
purple passion fruit is mainly grown for fresh fruits and concentrated  
juice processing in Vietnam. The industrial processing of passion  
fruit juices produces large amounts of by-products, including seeds  
and peels, that account for up to 60% of the total fruit weight (Silva  
et al., 2015). While discarding passion fruit seeds may lead to an  
increasing environmental problem, their high lipid content, around  
30% (Oliveira et al., 2014; Silva et al., 2015), could be employed in  
the food and cosmetic industries (Oliveira et al., 2013).  
Received: June 9, 2019  
Accepted: December 25, 2019  
Correspondence to  
ORCID  
Lai Thi Ngoc Ha  
3752  
In general, the extraction of oil from the seeds can be done easily  
and efficiently using organic solvents, and the efficiency mainly depend  
469  
Green Solvent Extraction and Quality Characteristics of Passion Fruit Seed Oil (Passiflora edulis Sims var. edulis)  
on the choice of solvents (Cowan, 1999). Hexane  
is the most popular solvent for oil extraction due  
to its low cost and the high solubility of oils in  
hexane. However, hexane is not allowed to be  
used as a solvent “for all uses” in the food  
industry because of environmental and public  
health concerns. There are a number of solvents  
that are friendly to the environment, like acetone,  
ethanol, ethyl acetate, and isopropanol, because  
they generate less waste than other solvents  
(Oliveira et al., 2013) and can be used in the food  
industry (Directive 2009/32/EC of the European  
Parliament and of the Council). Besides solvents,  
the material to solvent ratio as well as the  
extraction temperature and time are generally  
known as factors affecting oil extraction from  
plant materials.  
collected and transported to the laboratory on the  
day of processing at the factory. The seeds were  
first washed with tap water to remove the aril  
around the seeds, rinsed in distilled water three  
times, and then dried under sunlight to 10%  
moisture content. Before extraction, the dried  
seed samples were ground into a fine powder  
form (from 0.5 to 1mm in diameter) with a  
laboratory grinder (HR2115, Philips) and kept in  
a sealed container (dark, dry, and at 4oC).  
Sample extraction  
The dried passion fruit seed powder (5g) was  
mixed with different solvents (acetone, ethanol,  
ethyl acetate, isopropanol, or hexane) in  
Erlenmeyer flasks with rubber tops. The solvents  
were added at different sets of seed to solvent  
ratios of 1/4, 1/6, 1/8, 1/10, and 1/12. The  
Erlenmeyer flasks then were placed in an orbital  
incubator shaker Gyromax 727 (Amerex  
Instruments, Inc., USA) with a shaking speed of  
150 rounds/min. The extraction times were 0.5,  
1, 2, 3, 4, 5, and 6 hours at varying temperatures  
(room temperature, 40, 50, 60, and 70oC).  
Afterwards, the crude extracts were transferred  
to 50mL falcon conical centrifuge tubes and  
centrifuged at 6,000rpm for 20 minutes with a  
Hermle Z400 (Hermle, Germany) tabletop  
centrifuge. The supernatants were concentrated  
using a rotary evaporator R-210 Rotavapor  
(Buchi, Switzerland) at the boiling point of the  
solvent under vacuum pressure. The seed powder  
was extracted in triplicate for each extraction  
treatment.  
The objectives of this work were: (i) to  
investigate the effects of process variables on the  
oil extraction from passion fruit seeds using a  
shaker with green solvents (acetone, ethanol,  
ethyl acetate, and isopropanol) in comparison  
with using the conventional solvent (hexane);  
and (ii) to determine the chemical and quality  
characteristics of the oil obtained from the seeds  
of a purple passion fruit variety commonly  
grown in Vietnam. This study was the first step  
in investigating the exploitation of passion seeds  
as an additional dietary source of an essential  
polyunsaturated fatty acid (PUFA).  
Materials and Methods  
Sample preparation  
Purple passion fruit seeds (Passiflora edulis  
Sims var. edulis) were obtained from the  
Nafoods Group (Nghe An, Vietnam) in  
November 2017. They were by-products of the  
production of passion fruit concentrated juice.  
Approximately 20kg of fresh seeds were  
A single factor experiment was used to  
determine the suitable extraction conditions for  
passion fruit seeds. The influence of the  
extraction parameters, namely the type of  
solvent, material to solvent ratio, extraction  
temperature, and time, on oil extraction yield  
Table 1. Independent parameters involved in the extraction of oil from passion fruit seeds  
Factor names  
Type of solvent  
Factor levels  
Acetone, ethanol, ethyl acetate, isopropanol, and hexane  
1/4, 1/6, 1/8, 1/10, and 1/12 (w/v)  
Material to solvent ratio  
Extraction temperature  
Extraction time  
Room temperature, 40, 50, 60, and 70 (oC)  
0.5, 1, 2, 3, 4, 5, and 6 (hours)  
Vietnam Journal of Agricultural Sciences  
470  
Nguyen Thi Thu Nga et al. (2019)  
Table 2. Experimental design studying the effects of different extraction parameters on the oil yield of passion fruit seeds  
Experiment  
Type of solvent  
Extraction parameters  
Fixed parameter  
1/8 g mL-1, 50oC, 3h  
Acetone, ethanol, ethyl acetate,  
isopropanol, and n-hexane  
Material to solvent ratio  
Extraction temperature  
1/4, 1/6, 1/8, 1/10, and 1/12 (w/v)  
Selected solvent, 50oC, 3h  
Room temperature (28oC), 40, 50, 60,  
and 70 (oC)  
Selected solvent, material to solvent ratio, 3h  
Extraction time  
1, 2, 3, 4, and 5 (hours)  
Selected solvent, material to solvent ratio, and  
extraction temperature  
from passion fruit seeds were studied (Tables 1  
and 2). The oil extraction yield was calculated  
using the equation:  
experiments, the significant differences (P  
<0.05) among means were subjected to one-way  
analysis of variance (ANOVA) with Duncan’s  
test using the statistical software SAS 9.3.  
Oil extraction yield = 100.Oe/Os  
where Oe is the oil content that was obtained  
in the extraction and Os is the oil content in the  
seeds.  
Results and Discussion  
Effects of the process variables on oil  
extraction from passion fruit seeds using a  
shaker  
Methods  
The oil content of passion fruit seeds  
(g/100g) was determined by measuring weight  
loss after a 6-cycle extraction with hexane in a  
Soxhlet apparatus. The acidity index of the  
extracted seed oil was determined by titration  
using a solution of KOH 0.1N according to  
EEC/TCVN 6127:2010. The peroxide value of  
the extracted seed oil was obtained by titration  
using a 0.01N solution of sodium thiosulfate  
according to AOCS Cd8b-90. The fatty acid  
profile of the extracted seed oil was determined  
by gas chromatography (GC-FID) at the National  
Institute for Food Control.  
Table 3 shows the results obtained from the  
shaker extraction of oil from Passiflora edulis  
var. edulis seeds.  
Solvent type had a strong effect on the oil  
extraction yield. The results showed that ethanol,  
hexane, and isopropanol gradually increased the  
oil extraction yield from 71.1 to 72.47% but they  
were not significantly different at a significance  
level of 5%. The remaining solvents, acetone and  
ethyl acetate, gave the highest oil extraction  
efficiencies and performed equally well as  
isopropanol and hexane. The only statistically  
significant difference in the extraction yield of  
passion fruit seeds was that ethanol was  
significantly lower than both ethyl acetate and  
acetone (P <0.05).  
Statistical analysis  
All experimental results in this study were  
expressed as mean values ± standard errors (SE)  
of nine measurements (n = 9). In the single factor  
With different polarities (hexane is a non-polar  
Table 3. Effects of the process variables on oil extraction yield from passion fruit seeds  
Yield  
(%)  
Material/  
solvent ratio  
Yield  
(%)  
Yield  
(%)  
Extraction  
time  
Yield  
(%)  
Solvent  
Acetone  
Extraction temperature  
72.98a  
71.1b  
1/4  
1/6  
63.10c  
72.88b  
74.51b  
78.01a  
79.17a  
Room temperature  
75.66b  
76.60ab  
77.00ab  
77.46a  
77.74a  
1h  
2h  
3h  
4h  
5h  
71.41c  
71.62c  
75.26b  
78.52a  
79.49a  
Ethanol  
40oC  
50oC  
60oC  
70oC  
Ethyl acetate  
Isopropanol  
Hexane  
73.67a  
72.47ab  
72.07ab  
1/8  
1/10  
1/12  
Note: Values in the same column that do not share a common superscript are significantly different (P <0.05).  
471  
Green Solvent Extraction and Quality Characteristics of Passion Fruit Seed Oil (Passiflora edulis Sims var. edulis)  
solvent, ethanol and isopropanol are polar  
solvents, and ethyl acetate and acetone are  
aprotic polar solvents), different solvents  
resulted in different extraction efficiencies. The  
data indicated that the aprotic polar solvents were  
more suitable for the extraction of oil from purple  
passion fruit seeds since ethyl acetate and  
acetone had better oil extraction capacities than  
ethanol. Oliveira et al. (2014) also found the  
same result in that acetone was the best solvent  
compared to ethanol and isopropanol in  
extracting oil from passion fruit seeds.  
extracting solvent was used in the extraction of  
oil from passion fruit seeds and thus, this ratio  
was chosen for the determination of the  
extraction temperature and extraction time.  
Regarding the extraction temperature, the  
results indicated a significant increase in the oil  
extraction yield when the temperature increased  
from room temperature (28oC) to 60oC (P <0.05)  
but the oil extraction efficiency did not  
significantly differ between the temperatures of  
60 and 70oC (P >0.05).  
When performing extractions at low and  
mediate temperatures, from room temperature to  
50oC, the flexibility of the fatty constituents in  
the materials was not strongly promoted; hence,  
the extraction efficiency was around 76%. When  
the temperature was raised to 60oC, the thermal  
conductivity increased, which made the diffusion  
coefficient of the solutes increase, consequently  
increasing their solubility (Al-Farsi & Chang,  
2007) and thus, accelerating the whole extraction  
up to 78%. Although increasing the temperature  
to 60oC resulted in a 2% increase in the oil  
extraction yield, 60oC is not only closer to the  
boiling point of ethyl acetate (77oC), which  
might cause significant losses in the solvent,  
energy consumption, and economic efficiency,  
but small constituents of materials are also easily  
dissolved at this temperature, leading to  
difficulties in oil recovery. Therefore, room  
temperature (28oC) was selected for the  
extraction of oil from passion fruit seeds in the  
subsequent step.  
In accordance with Directive 2009/32/EC of  
the European Union on April 23, 2009, both ethyl  
acetate and acetone are allowed to be used as  
solvents in the food industry because they  
generate less waste than other solvents. Because  
the boiling point of ethyl acetate is 77oC, higher  
than that of acetone (56oC), ethyl acetate was  
selected for the next experiment due to less  
solvent loss during oil recovery.  
The oil content in the extracts strongly  
depended on the material to solvent ratio. There  
was an increase of the passion fruit seed oil yield  
with an increase of the material to solvent ratio  
(w/v). The material to solvent ratio of 1:12 (w/v)  
showed the highest amount of oil but was not  
significantly different from the ratio of 1:10 (w/v)  
(P >0.05). The opposite behavior is reported by  
Oliveira et al. (2014) who found that the ratio 1:4  
of passion fruit seeds to solvent was the best ratio  
to extract oil from these seeds. Maybe  
differences between yellow and purple passion  
fruit seeds led to the differences in findings  
between the results of Oliveira et al. (2014) and  
our study.  
The evaluation of the extraction time  
showed that the extraction capacity of passion  
fruit seeds increased sharply when the  
extraction time was increased to 4h, but at  
longer extraction times, the efficiency did not  
increase significantly (P >0.05). This finding  
is in agreement with the report of Oliveira et  
al. (2014) who reported that the highest oil  
extraction capacity value from passion fruit  
seeds was obtained after 4h of extraction.  
These phenomena could be explained by Fick’s  
second law of diffusion, predicting that a final  
equilibrium between the solute concentration  
in the plant matrix and in the solvent might be  
reached after a certain time.  
A high material to solvent ratio could  
promote an increased concentration gradient,  
producing a higher chance of oil coming into  
contact with the extraction solvent, resulting in  
an increased diffusion rate that allows for greater  
extraction of materials by the solvent (Cacace &  
Mazza, 2003). These results were consistent with  
the mass transfer principle. However, the active  
component yields would not continue to increase  
once equilibrium had been reached (Herodež et  
al., 2003). An equilibrium constant trend was  
observed at the material to solvent ratio of 1:10  
(w/v) that indicated a sufficient amount of  
Vietnam Journal of Agricultural Sciences  
472  
Nguyen Thi Thu Nga et al. (2019)  
used as an indicator of lipid oxidation. High  
peroxide values of extracted oil indicate that the  
oil was exposed to oxidative processes during the  
preparation of the raw material, extraction, or oil  
storage. In our study, the peroxide value of the  
seed oil from P. edulis var. edulis was 2.5 times  
lower than peroxide value of the seed oil from P.  
edulis var. flavicarpa found by Silva et al. (2015)  
of 1.54 ± 0.14 meqO2kg-1 and far lower than the  
value that the Codex Alimentarius Commission  
established for refined and crude oils in 2008 at  
15 meqO2kg-1.  
Chemical and quality characteristics of  
Passiflora edulis var. edulis seed oil  
According to the chemical characteristics of  
passion fruit seed oil (Table 4), the oil content of  
Passiflora edulis var. edulis seeds was 27.28% on  
a dry basis indicating that these seeds were a good  
oil source when compared to soybean seeds,  
which contain about 25% on a dry basis (Hammad  
et al., 2012). The oil content reported in this study  
was higher than the values of 18.5% for P. edulis  
var. edulis seeds and 20.6% for P. edulis var.  
flavicarpa seeds in Uganda found by Nyanzi et al.  
(2005), and lower than the figures of 30.39% and  
30.22% for yellow passion fruit seeds in Brazil  
found by Malacrida & Jorge (2012) and Silva et  
al. (2015), respectively. Differences in the oil  
contents of P. edulis could be due to genetic,  
climate, and geographical attributes.  
The GC analysis of the fatty acids of the P.  
edulis var. edulis seed oil showed a high content  
of unsaturated fatty acids such as linoleic and  
oleic (Table 5). Linoleic acid (C18:2n6), an  
essential polyunsaturated omega-6 fatty acid for  
humans, was the most dominant fatty acid  
making up 75.7% of the total fatty acids and was  
followed by oleic acid (C18:1n9) at 9%. These  
data were in agreement with the results reported  
by Nyanzi et al. (2005) in that linoleic and oleic  
acids made up the majority of the fatty acids  
found in the extracted oil of P. edulis var. edulis  
seeds with the values of 74.3% for linoleic acid  
and 13.6% for oleic acid.  
The acidity index of the extracted oil  
provides important information on the condition  
of oil conservation. A high acidity index  
indicates that the oil was partly oxidized or  
degraded. The value found in this study (1.61 ±  
0.05 mg KOHg-1) was equal with the value found  
by Silva et al. (2015) and 1.5 times lower than  
the quality parameter of 4.0 mg KOHg-1  
according to The Codex Alimentarius  
Commission (2008). This result indicates that the  
studied oil can be used for food purposes as it  
meets the required standard.  
In comparison to the fatty acid compositions  
of soybean oil and sunflower oil, two popular  
vegetable oils used in the food, cosmetic, and  
pharmaceutical industries (Rabasco & Gonzalez,  
2000), the percentage of saturated fatty acids in  
The determination of the peroxide value is  
Table 4. Chemical characteristics of P. edulis var. edulis seeds oil  
Component  
Oil content (%)  
Acidity index (mg KOH g-1)  
Peroxide value (meqO2 kg-1)  
Value*  
27.28 ± 0.54  
1.61 ± 0.05  
0.62 ± 0.03  
Note: * Each value is the mean ± SD of triplicate extractions and determinations.  
Table 5. Fatty acid composition of P. edulis var. edulis seed oil  
Fatty acids  
Composition (%)  
Oleic acid (C18:1n9c)  
Linoleic acid (C18:2n6)  
9
75.7  
0.94  
14  
Docosahexaenoic acid (C22:6n3)  
Saturated fatty acid (SFA)  
Unsaturated fatty acid (UFA)  
86  
473  
Green Solvent Extraction and Quality Characteristics of Passion Fruit Seed Oil (Passiflora edulis Sims var. edulis)  
passion fruit seed oil amounted to 14%, while  
the value obtained for soybean oil was slightly  
higher (15.1%) and the value for sunflower oil  
was a little lower (12.36%). Among the  
monounsaturated fatty acids, oleic acid was the  
main representative and its content was the  
lowest in passion fruit seed oil (9%) and  
highest in soybean oil (21.73%), while the  
level of oleic in sunflower oil was 15.93%  
(Zambiazi et al., 2007). Linoleic was the  
dominant fatty acid among the polyunsaturated  
fatty acids (PUFAs) and the linoleic acid  
amount in passion fruit seed oil was higher than  
the vales determined in sunflower oil and  
soybean oil, which were 71% and 56%,  
respectively. It can also be noted that  
sunflower oil’s high PUFA content makes this  
oil a good salad oil source (Sullivan, 1980),  
and with the primary constituents of oleic,  
linoleic, and linolenic acids, soybean oil and  
sunflower oil can be employed in cosmetic  
products and pharmaceutical formulations  
(Rabasco & Gonzalez, 2000). Hence, the high  
content of PUFAs of the studied oil indicates  
this product is a good source of essential  
PUFAs for human use.  
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Conclusions  
Oliveira R. C., Barros S. T. D. & Gimenes M. L. (2013).  
The extraction of passion fruit oil with green solvents.  
Journal of Food Engineering 117: 458-463.  
In this study, the effects of process variables  
on the solvent extraction of oil from passion fruit  
seeds were investigated using a shaker. The  
highest extraction yield was 78.52%, which was  
obtained using ethyl acetate at the ratio of 1:10  
material to solvent at room temperature (28oC)  
for 4h, and was similar to the results obtained  
with the conventional solvent hexane. Our results  
indicate that passion fruit seed oil extracted by  
ethyl acetate has a high content of PUFAs  
(around 77%) and thus, has good potential for use  
in the human food, cosmetic, and pharmaceutical  
industries.  
Oliveira R. C., Guedes T. A., Gimenes M. L. & Barros S.  
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Acknowledgements  
Sullivan F. E. (1980). Sunflower oil processing from crude  
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The authors would like to acknowledge  
Vietnam National University of Agriculture  
for providing financial support under the  
Research Grant Scheme (Grant agreement  
T2017-08-55).  
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Vietnam Journal of Agricultural Sciences  
474  
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