Enzymatic Extraction and Modification, and Frying Stability of Moringa Oleifera Seed Oil.
Consumption of edible oils has grown with the increase in world population. The increasing health awareness and consciousness amongst consumers made the food industry more discriminating in the types of oil they use for food applications. Many circumstances have focused attention on high-oleic ve...
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Format: | Thesis |
Language: | English English |
Published: |
2006
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Online Access: | http://psasir.upm.edu.my/id/eprint/6707/1/FSTM_2005_1.pdf http://psasir.upm.edu.my/id/eprint/6707/ |
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Institution: | Universiti Putra Malaysia |
Language: | English English |
Summary: | Consumption of edible oils has grown with the increase in world population. The
increasing health awareness and consciousness amongst consumers made the food
industry more discriminating in the types of oil they use for food applications. Many
circumstances have focused attention on high-oleic vegetable oils, which have been
demonstrated to reduce the risk of coronary heart disease. The demand for high-oleic
oils is increasing but there are only a few known sources available. Moringa oleifera
seed oil, which is naturally high-oleic oil, therefore, presents a great opportunity for the
oil industry for meeting this ever-increasing demand.
The objectives of this study were to determine the properties of oil extracted from
Moringa oleifera seeds, evaluate the efficiency of enzymatic-extraction of the oil and
modification of the oil to enhance its oleic acid content and compare the oxidative
stability of the oil against several other oils during deep fat frying.The oil content of M. oleifera seeds in Malaysia ranged between 30.8% and 33.4%
depending on the variety, of which there were two. The physico-chemical properties of
the oil were determined following extraction with light petroleum ether. The dominant
fatty acid (FA) of the oil was indeed oleic acid, where Variety 1 contained 67.9% while
Variety 2 contained 74.4%. After refining, the oil from both varieties is light golden
color (O.1R + 1 .OY), and a viscosity, smoke point and refractive index (nD400C) of Cp
51.7, 206"C, and 1.4533, respectively. Using electronic nose analysis, the crude oil was
found to have an odor similar to that of peanut oil. It has a complete melting point of
18.9"C. The crude oil contains 95.6% triacylglycerols (TAG) and 1.9% 1,2- and 1,3-
diacylglycerols. The relative TAG content increased to 98.7% after refining. The oil
contains 36.7% trioleoyl glycerol (000) as the main TAG.
M. oleifera seed oil was extracted using four different types of enzymes namely;
Neutrase 0.8L (neutral protease), Termamyl 120L, type L (a-amylase), Pectinex Ultra
SP-L (pectinase) and Celluclast 1.5L FG (cellulase) all supplied by Novozymes
(Bagsvaerd Denmark). The enzymes were used either separately or in combination. The
efficiency of enzyme-extraction was compared to aqueous extraction without enzyme.
Enzymatic-extraction of M. oleifera seed oil showed that Neutrase alone at 2% vlw,
45°C and pH 6.8 was able to extract 71.9% oil relative to the amount obtained when the
oil was solvent-extracted. Neutrase was the most efficient among the enzymes used
followed by Termamyl, Celluclast and Pectinex with percent oil recoveries of 64.8%,
62.6% and 56.5%, respectively. Each extraction was carried out at the optimum pH and
temperature of the enzymes. A combination of the four enzymes at pH 7.5 increased the oil recovery to 74%. Percent oil recovery with all enzymes was significantly (P<0.05)
higher than the control (aqueous extraction without enzyme) (3 5.6%).
Solvent extracted M oleifera seed oil was transesterified using immobilized lipase
(Lipozyme IM 60) (Novozyrnes Bagsvaerd Denmark) in order to change its melting and
crystallizing behavior that will make it easier to fractionate. After transesterification, the
oil was fractionated with acetone at -18°C and without acetone at 10°C to obtain two
fractions, stearin and olein fractions. Incubation of the transesterified oil at 10°C for 24
h resulted in the formation of fat crystals, which settled at the bottom of the flask in
sample transesterified for 24 h, while the control (0 h) sample became rather viscous
with fat crystals in suspension. Transesterification affect the TAG profile of the oil,
which in turn affected the solid fat content (SFC) and thermal behavior. The SFC value
at 0°C after 24 h of reaction was 10.35% and significantly (P<0.05) higher than the
control (0 h) (7.94%). The oil remained liquid at 20°C for all reaction times. The end set
temperature (melting point) shifted from 18.9"C for the unreacted oil to 20S°C for oil
transesterified for 24 h. Transesterification of the oil resulted also in a significant
(P<0.05) increase in the crystallization temperature of the high melting glyceride from
the original value of 1.6"C to 12.9"C after transesterification for 24 h. There was a
significant increase in the oleic acid content in the olein fractions obtained following
fractionation of the transesterified oil with and without using acetone (75.2 and 70.5%,
respectively) compared to the unreacted oil (67.9%).The oxidative stability of refined M oleifera seed oil (MOO) in deep fat frying was
evaluated and compared with canola (CLO), soybean (SBO), and palm olein (PO). The
oils were used to fry potato chips for 6 h a day up to a maximum of 5 days. Changes in
fatty acid (FA) composition, free fatty acids (FFA), iodine value (IV) peroxide value
(PV), p-anisidine value (p-AV), specific extincti o;:1~n( 233 and 269 nm for conjugated
dienes and trienes), total polar compounds (TPC), color and viscosities were used to
evaluate the oils.
The frying process caused an increase in the FFA contents MOO, PO, CLO and SBO.
The FFA contents at the end of the frying period were 0.35%, 0.55%, 0.54% and 0.51%
for CLO, PO, SBO and MOO, respectively. The rate of increase in the PV (meqOz/kg)
for CLO (2.33 per day) was higher compared to those of MOO (0.80 per day), PO (1.00
per day), and SBO (0.70 per day). Conjugated dienes levels at the end of the frying
period were lowest in PO (4.27) followed by MOO (6.07) with high levels in CLO (9.28)
and SBO (10.64). The amount of TPC in MOO (20.78%) and PO (21.23%) were
significantly (P<0.05) lower than those in CLO (28.73%) and SBO (3 1.82%). Color and
viscosity of the oils increased with frying time. The rates of change of viscosity with the
frying days were similar for all the oils. Results of sensory analysis conducted on potato
chips fried in PO and MOO showed general acceptability of potato chips fried in both
oils with high scores for crispness (7.07 and 7.14), oiliness (6.86 and 7.09), and fried
food flavor (7.00 and 6.79) attributes, respectively. The overall acceptance of the French
fries fried in MOO was high (7.50) and not significantly (P>0.05) from that of PO
(7.58). |
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