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Analysis and formation of trans fatty acids in hydrogenated soybean oil during heating

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Hydrogenated oil has been widely used for production of shortenings or margarine, however, the presence of trans fatty acids may be detrimental to human health. The objectives of this study were to develop an improved method for analysis of trans fatty acids and evaluate their formation in both unhydrogenated and hydrogenated soybean oil during heating at 160, 180 and 200°C for varied length of time. Results showed that among the four columns tested, an Agilent HP-88 column (100×0.25mm I.D.,0.2-μm film thickness) could resolve eight trans fatty acids and nine cis fatty acids simultaneously within 31min with injector temperature 240°C, detector temperature 250°C, and column temperature 170°C in the beginning, maintained for 24min, increased to 220°C at 7.5°C/min, 230°C at 10°C/min, and maintained for 5min. The contents of both cis and trans fatty acids showed a decreased trend for the increase of heating time or temperature. No trans fatty acid formation was observed even after extensive heating of unhydrogenated and hydrogenated soybean oil for 24h. This phenomenon demonstrated that trans fatty acids can only be formed under severe conditions.
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Analytical, Nutritional and Clinical Methods
Analysis and formation of trans fatty acids in hydrogenated soybean
oil during heating
W.H. Liu, B. Stephen Inbaraj, B.H. Chen
*
Department of Nutrition and Food Science, Fu Jen University, Taipei 242, Taiwan
Received 4 January 2006; received in revised form 25 July 2006; accepted 27 October 2006
Abstract
Hydrogenated oil has been widely used for production of shortenings or margarine, however, the presence of trans fatty acids may be
detrimental to human health. The objectives of this study were to develop an improved method for analysis of trans fatty acids and eval-
uate their formation in both unhydrogenated and hydrogenated soybean oil during heating at 160, 180 and 200 °C for varied length of
time. Results showed that among the four columns tested, an Agilent HP-88 column (100 0.25 mm I.D., 0.2-lm film thickness) could
resolve eight trans fatty acids and nine cis fatty acids simultaneously within 31 min with injector temperature 240 °C, detector temper-
ature 250 °C, and column temperature 170 °C in the beginning, maintained for 24 min, increased to 220 °C at 7.5 °C/min, 230 °Cat
10 °C/min, and maintained for 5 min. The contents of both cis and trans fatty acids showed a decreased trend for the increase of heating
time or temperature. No trans fatty acid formation was observed even after extensive heating of unhydrogenated and hydrogenated soy-
bean oil for 24 h. This phenomenon demonstrated that trans fatty acids can only be formed under severe conditions.
Ó2006 Elsevier Ltd. All rights reserved.
Keywords: Trans fatty acid; Hydrogenated soybean oil; GC–MS; Heating
1. Introduction
Fats and oils are one of the major nutrients in the diet to
maintain human health by providing body energy and
essential fatty acids such as linoleic acid (Frankel, 1998).
Because of presence of two isolated double bonds, linoleic
acid is susceptible to oxidation or degradation during heat-
ing (Chen, Tai, Chen, & Chen, 2001). In an attempt to
enhance the stability of unsaturated fatty acids in edible
oils, the hydrogenation process has been often employed
for production of shortenings or margarine (Kris-Etherton,
1995). However, the isomerization of cis to trans fatty acids
can occur during hydrogenation and result in a wide distri-
bution of trans fatty acids in bakery and fried products
(Aro et al., 1998; Romero, Cuesta, & Sa
´nchez-Muniz,
2000). Although reported data on trans fatty acid contents
in food products can be varied from one country to
another, the food made with hydrogenated fats such as
cookies and other bakery products, have been shown to
be the main source of trans fatty acid in the diet (Vicario,
Griguol, & Leon-Camacho, 2003).
Epidemiological studies have revealed that the intake of
trans fatty acids in excess may raise the cholesterol level in
blood (Mensink & Katan, 1990, 1993), and the concentra-
tion of low density lipoprotein in the plasma could be ele-
vated following the consumption of hydrogenated fat
containing high levels of trans fatty acids (Han et al.,
2002). Several authors also reported that trans fatty acids
may adversely affect the inflammatory process in athero-
sclerosis by increasing the peripheral blood mononuclear
cell production of inflammatory cytokines (Libbey, Rid,
& Maseri, 2002; Taubes, 2002). More recently, Kummerow
et al. (2004) demonstrated that trans fats inhibit the meta-
bolic conversion of linoleic acid to arachidonic acid and to
other polyunsaturated fatty acids, a risk factor in the devel-
opment of coronary heart disease.
0308-8146/$ - see front matter Ó2006 Elsevier Ltd. All rights reserved.
doi:10.1016/j.foodchem.2006.10.069
*
Corresponding author. Tel.: +886 2 29053626; fax: +886 2 29021215.
E-mail address: nutr1007@mails.fju.edu.tw (B.H. Chen).
www.elsevier.com/locate/foodchem
Food Chemistry 104 (2007) 1740–1749
Food
Chemistry
In view of the impact of trans fatty acids on human health,
the quantitation of trans fatty acids in heated oil and food
products is extremely important. The analysis of trans fatty
acids has been previously achieved by high-performance
liquid chromatography (HPLC) (Adlof, 1994; Adlof, Copes,
& Emken, 1995; Christie & Breckenridge, 1989). However,
the resolution of trans fatty acids remains poor. Juane
´da
(2002) used two C-18 columns to separate trans isomers of
oleic acid in milk by HPLC, but this method fails to resolve
trans forms of linoleic acid and linolenic acid. To remedy the
problem, several authors have used gas chromatography
(GC) to analyze trans fatty acids instead (American Oil
Chemists’ Society, 1990; Juane
´da, 2002). Based on a GC
method developed by American Oil Chemists’ Society
(1990), a total of 21 fatty acids, including 15 cis fatty acids,
1trans oleic acid, 3 trans linoleic acids and 2 trans linolenic
acids were separated within 37 min by using a SP-2340 col-
umn (60 m 0.25 mm I.D., 0.2-lm film thickness) contain-
ing 100% polybiscyanopropyl siloxane as stationary phase.
Nevertheless, the resolution is inadequate since several peaks
of trans fatty acids are overlapped. Juane
´da (2002) devel-
oped a GC method to separate 18 fatty acids in milk, includ-
ing 10 trans fatty acids, and the major drawback is that the
separation time is lengthy (50 min) and only 4 trans fatty
acids are adequately resolved. Since many published reports
still encounter difficulties in separating cis and trans fatty
acids simultaneously, it is imperative to develop a precise
method to determine cis and trans fatty acids in food prod-
ucts. Moreover, starting January 1, 2006, the US Food and
Drug Administration issued a rule that the trans fatty acid
content should be declared in the nutrition label of conven-
tional foods and dietary supplements (Food & Drug Admin-
istration, 2003). The objectives of this study were to develop
a GC method for analysis of trans fatty acids in unhydroge-
nated and hydrogenated soybean oil during heating.
2. Materials and methods
2.1. Materials
All fatty acid standards, including lauric acid methyl
ester (C12:0), myristic acid methyl ester (C14:0), palmitic
acid methyl ester (C16:0), stearic acid methyl ester
(C18:0), arachidic acid methyl ester (C20:0), palmitoleic
acid methyl ester (C16:1, D9cis), oleic acid methyl ester
(C18:1, D9cis), linoleic acid methyl ester (C18:2, D9cis,
D12 cis), linolenic acid methyl ester (C18:3, D9cis,D12
cis,D15 cis), internal standard heptadecanoic acid methyl
ester (C17:0), 9-trans-hexadecenoic acid methyl ester
(C16:1, D9trans), 6-trans-octadecenoic acid methyl ester
(C18:1, D6trans), 9-trans-octadecenoic acid methyl
ester (C18:1, D9trans), 11-trans-octadecenoic acid methyl
ester (C18:1, D11 trans), 9-trans-12-trans-octadecadienoic
acid methyl ester (C18:2, D9trans,D12 trans), 9-cis-11-
trans-octadecadienoic acid methyl ester (C18:2, D9cis,
D11 trans) and 10-cis-12-trans-octadecadienoic acid methyl
ester (C18:2, D10 cis,D12 trans), were from Nu-Chek-Prep
Inc. (Elysian, MN, USA), and 9,12,15-trans-octadecatrie-
noic methyl ester (C18:3, D9trans,D12 trans,D15 trans)
was from Sigma (St. Louis, MO, USA).
The analytical-grade solvents such as n-hexane, metha-
nol and chloroform were from Merck Co. (Darmstadt,
Germany). Chemicals, including potassium hydroxide,
anhydrous sodium sulfate, sodium chloride and boron
fluoride (in methanol) were from Riedel-de Ha
¨en Co. (See-
lze, Germany). Deionized water was obtained using a Milli-
Q water purification system from Millipore Co. (Bedford,
MA, USA). Unhydrogenated soybean oil was from Chia-
Hsin Chemical Co. (Taichung, Taiwan), while hydroge-
nated soybean oil was from Nan-Chiao Chemical Co.
(Taoyuan, Taiwan).
2.2. Heating of oil
A 5-l unhydrogenated or hydrogenated soybean oil was
poured into an oil tank separately, which was preheated to
160, 180 and 200 °C, and the heating time started to count
for 4, 8, 12, 16, 20 and 24 h. The temperature-controlled oil
tank (model B503) was from I-Seng Scientific Co. (Taipei,
Taiwan). After the desired heating time was reached, the oil
tank was cooled immediately to room temperature and a
10-ml oil sample was collected and poured into a 40-ml
brown vial for storage at 20 °C. Both fresh unhydroge-
nated and hydrogenated soybean oil were used as control
samples to compare with heated samples. Duplicate exper-
iments were carried out for each temperature and heating
time, and a total of 42 treatments were used.
2.3. Preparation of fatty acid methyl esters
A modified method based on Vicario et al. (2003) was
used. A 0.5-g oil sample was mixed with 10-ml methanolic
potassium hydroxide solution (0.5 N), and the mixture was
saponified at 90 °C in a water bath for 10 min. After cool-
ing to room temperature, a 8-ml BF
3
-CH
3
OH solution was
added and the mixture was standing in a water bath at
90 °C for 5 min to promote formation of methyl ester.
Again, the mixture was cooled to room temperature, then
8-ml hexane was added and the solution was heated in a
water bath at 90 °C for 3 min to allow complete esterifica-
tion of fatty acids. After cooling to room temperature, the
saturated saline solution was added to terminate the reac-
tion. The solution was allowed to settle until two layers
were formed, and the supernatant was collected, followed
by addition of 0.2-g anhydrous sodium sulfate to remove
excessive moisture and evaporation of the solution to dry-
ness. The residue was dissolved in 10-ml hexane and 1-ll
was injected into GC.
2.4. GC analysis of fatty acid methyl esters
Initially, four GC capillary columns were compared with
respect to the separation efficiency of standards of five sat-
urated fatty acid methyl esters, four unsaturated fatty acid
W.H. Liu et al. / Food Chemistry 104 (2007) 1740–1749 1741
methyl esters, eight trans fatty acid methyl esters and inter-
nal standard (C17:0). In addition, the various injector, col-
umn and detector temperatures, as well as flow rate and
split ratio were also evaluated. The GC instrument (model
6890) equipped with flame ionization detector (FID) and
mass spectrophotometer (model 5973) was from Agilent
Technologies (Palo Alto, CA, USA). All the standards were
dissolved in hexane to a concentration of 100 lg/ml each
and stored at 20 °C until use. The characteristics of each
GC column are listed below: (1) the DB-1 column
(60 m 0.32 mm I.D., 0.25-lm film thickness, coated with
100% dimethylpolysiloxane) was from J & W Scientific
Co. (Folsom, CA, USA); (2) the INNOWAX column
(30 m 0.32mm I.D., 0.25-lm film thickness, coated with
100% polyethylene glycol) was from Agilent Technologies
(Palo Alto, CA, USA); (3) the INNOWAX column (60 m
0.32 mm I.D., 0.25-lm film thickness, coated with 100%
polyethylene glycol); (4) the HP-88 column (100 m
0.25 mm I.D., 0.2-lm film thickness, coated with 88%
cyanopropyl-methylaryl polysiloxane) was also from Agi-
lent Technologies.
The various cis and trans fatty acids in the oil were iden-
tified by comparing retention time and mass spectra of
unknown peaks with reference standards and cochroma-
tography with added standards. For GC–MS, the interface
temperature was 270 °C with an electron multipler voltage
70 eV and ion voltage 1360 V, and detection was per-
formed by total ion mode with a scanning range of 35–
500 and rate at 2.94 scans/s. Eight concentrations of each
fatty acid standard (0.5, 0.8, 1.2, 1.5, 2.0, 3.0, 4.0 and
5.0 ppm) was prepared in hexane and the detection limit
was calculated based on S/NP3, whereas the quantitation
limit was based on S/NP10. For quantitation, eight con-
centrations (5, 10, 20, 40, 60, 100, 150 and 250 ppm) of
oleic acid methyl ester (C18:1, D9cis) and linoleic acid
methyl ester (C18:2, D9cis,D12 cis) were prepared and
mixed with internal standard (C17:0) for a final concentra-
tion of 91 ppm. Likewise, eight concentrations of the other
fatty acid standards (5, 10, 20, 40, 60, 80, 100 and 150 ppm)
were prepared and mixed with internal standard for a con-
centration of 91 ppm. Then the standard curves were
obtained by plotting concentration ratio against area ratio,
and the correlation coefficient (r
2
) was calculated with the
linear equations used for quantitation. The amount of each
fatty acid in the oil was calculated based on the following
formula:
W¼
A=RRF
Ai
Wi
Ws
recovery
where relative response factor (RRF) = (A/Ai)(W
i
/W);
Wis the concentration (mg/g) of each fatty acid in the oil
sample; Ais the peak area of each fatty acid standard; A
i
is
the peak area of internal standard; W
i
is the concentration
of internal standard; and W
s
is the weight of the sample.
The recovery was accomplished by adding two concen-
trations (10,000 and 20,000 ppm) of 1-ml of each fatty acid
standard to 0.5 g oil for extraction, with the exception of
C12:0, C18:2 (D9cis,D12 trans) and C18:2 (D9cis,D11
trans), because these three fatty acids were found not pres-
ent in heated oil. The recovery of each fatty acid was calcu-
lated based on the ratio of the amount of each standard
obtained after and before GC.
2.5. Statistical analysis
All the experiments were performed in duplicate and the
data were subjected to analysis of variance using ANOVA
and Duncan’s multiple range test for comparison of signif-
icant difference (P< 0.05) using SAS (2003).
3. Results and discussion
3.1. GC analysis of cis and trans fatty acid standards
Initially, the official method published by the American
Oil Chemists’ Society (American Oil Chemists’ Society,
1990) was adopted for separation of cis and trans fatty
acid standards. However, the resolution of trans fatty
acids remains poor, and thus a modified method was
developed. Four GC capillary columns differing in length
and polarity of stationary phase as described in Section 2
were evaluated, and the various GC separation conditions
were also compared. After numerous studies, an Agilent
HP-88 column was found to be the most appropriate
for simultaneous separation of trans and cis fatty acids.
For the other three columns, only 9 cis fatty acid stan-
dards, including C12:0, C14:0, C16:1 (D9c), C16:0,
C18:2 (D9cD12c), C18:3 (D9cD12cD15c), C18:1 (D9c),
C18:0 and C20:0 were separated by using a DB-1 column.
Likewise, a total of 15 fatty acids, including 6 more trans
fatty acids were separated using an INNOWAX column
(30 or 60 m). The difference is that a 60-m INNOWAX
column resulted in a much longer retention time than a
30-m INNOWAX column, and several trans fatty acids
were overlapped for both columns. The GC chromato-
gram of fatty acid methyl ester standards using a HP-88
column is shown in Fig. 1. A total of 18 peaks, including
5cis saturated fatty acids, 4 cis unsaturated fatty acids, 8
trans fatty acids and internal standard (C17:0) were
resolved within 31 min, with helium as carrier gas and
flow rate at 3 ml/min, injector temperature at 240 °C
and detector temperature at 250 °C. The split ratio was
10:1 and the column temperature was programmed as fol-
lows: 170 °C in the beginning, maintained for 24 min,
raised to 220 °C at 7.5 °C/min, 230 °Cat10°C/min and
maintained for 5 min. With the exception of trans isomers
of oleic acid (peaks 7, 8 and 9), all the other fatty acids
were adequately resolved. We have to point out here that
the partial overlap of trans oleic acid should not affect
quantitation because, for food labeling, these three iso-
mers can be regarded as those representing the total
amount of trans oleic acid. Nevertheless, when compared
to some other previous reports (American Oil Chemists’
Society, 1990; Juane
´da, 2002), this method is much better
1742 W.H. Liu et al. / Food Chemistry 104 (2007) 1740–1749
in terms of retention time and separation number of trans
fatty acids.
Table 1 shows the quality control data of 14 fatty acid
standards. Three fatty acid standards, namely, C12:0,
C18:2 (D9cis,D12 trans) and C18:2 (D9cis,D11 trans) were
excluded because they were not detected in heated soybean
oil. Both intra- and inter-day tests are routinely used for
evaluation of precision of the developed analytical method,
which are often carried out by comparing the concentra-
tion difference of multiple analyses within one day and
between days, and the concentration difference should be
as minimal as possible to attain a high reproducibility for
this method (International Conference on Harmonization,
1996). The coefficient of variation (CV) (%) of the intra-day
variability based on the mean concentration of five injec-
tions within one day ranged from 0.2% to 2.7% while the
CV of the inter-day variability based on the mean concen-
tration of five injections every week for a total of 5 weeks
ranged from 1.0% to 3.6%. This result clearly indicated a
high reproducibility was achieved by this method. Table
2shows the detection limit (DL) and quantitation limit
(QL) of 14 fatty acid standards. The DL based on S/
NP3 ranged from 0.8 to 1.2 ppm, whereas the QL based
on S/NP10 ranged from 2.6 to 3.9 ppm. These values
were lower than a report by Ruiz-Jimenez, Priego-Capote,
and Luque de Castro (2004), who determined the amount
of trans fatty acids in bread and found the DL ranged from
0.98 to 3.93 ppm and the QL ranged from 3.23 to
12.98 ppm. The r
2
of all the linear regression equations of
14 standard curves were higher than 0.99. Table 3 shows
the recovery data of each fatty acid standard added to
heated soybean oil. A high recovery of 94.4–102.7% was
attained for all the 14 fatty acid standards, which was
higher than a previous study by Indarti, Majid, Hashim,
and Chong (2005), who analyzed the fatty acid content in
fish oil and reported the recovery to be approximately
80%. This difference may be due to variation in extraction
min
5 10 15 20 25 30
pA
10
12
14
16
18
20
22
24
solvent
1
2
345IS
6
7
8910
11
12
13
14
15
16
17
Fig. 1. GC chromatogram of FAMEs standards using a HP-88 column.
Helium was used as carrier gas. The oven temperature was programmed as
follows: 170 °C in the beginning, maintained for 24 min, increased to
220 °C at 7.5 °C/min, to 230 °Cat10°C/min, maintained for 5 min.
Peaks: (1) lauric acid methyl ester, (2) myristic acid methyl ester, (3)
palmitic acid methyl ester, (4) 9-trans-hexadecenoic acid methyl ester, (5)
palmitoleic acid methyl ester, (6) stearic acid methyl ester, (7) 6-trans-
octadecenoic acid methyl ester, (8) 9-trans-octadecenoic acid methyl ester,
(9) 11-trans-octadecenoic acid methyl ester, (10) oleic acid methyl ester,
(11) 9-trans-12-trans-octadecadienoic acid methyl ester, (12) linoleic acid
methyl ester, (13) 9,12,15-trans octadecatrienoic acid methyl ester, (14)
arachidic acid methyl ester, (15) linolenic acid methyl ester, (16) 9-cis, 11-
trans-octadecadienoic acid methyl ester, (17) 10-cis, 12-trans-octadecadi-
enoic acid methyl ester. IS = internal standard.
Table 1
Quality control data of 14 fatty acid methyl esters standards analyzed by
GC
Fatty acid methyl ester standard Intra-day
a
variability
Inter-day
b
variability
CV (%) CV (%)
Myristic acid methyl ester (C14:0) 1.7 2.4
Palmitic acid methyl ester (C16:0) 0.2 1.0
9-trans-Hexadecenoic acid methyl ester
(C16:1,9t)
2.1 3.2
Palmitoleic acid methyl ester (C16:1,9c) 2.7 3.6
Stearic acid methyl ester (C18:0) 0.2 1.8
6-trans-Octadecenoic acid methyl ester
(C18:1,6t)
0.5 2.3
9-trans-Octadecenoic acid methyl ester
(C18:1,9t)
0.7 1.7
11-trans-Octadecenoic acid methyl ester
(C18:1,11t)
0.8 1.8
Oleic acid methyl ester (C18:1,9c) 0.7 1.4
9-trans-12-trans-Octadecadienoic acid
methyl ester (C18:2,9t12t)
1.6 2.0
Linoleic acid methyl ester (C18:2,9c12c) 1.5 2.2
9,12,15-trans-Octadecatrienoic acid
methyl ester (C18:3,9t12t15t)
0.4 2.0
Arachidic acid methyl ester (C20:0) 0.7 2.5
Linolenic acid methyl ester
(C18:3,9c12c15c)
0.7 1.6
a
Mean concentration of five injections within one day.
b
Mean concentration of five injections every week for a total of five
weeks.
Table 2
Detection and quantitation limits of 14 fatty acid methyl esters standards
analyzed by GC
Fatty acid methyl ester standard DL
(ppm)
a
QL
(ppm)
b
Myristic acid methyl ester (C14:0) 0.8 2.6
Palmitic acid methyl ester (C16:0) 0.8 2.6
9-trans-Hexadecenoic acid methyl ester (C16:1,9t) 1.2 3.9
Palmitoleic acid methyl ester (C16:1,9c) 0.8 2.6
Stearic acid methyl ester (C18:0) 0.8 2.6
6-trans-Octadecenoic acid methyl ester (C18:1,6t) 0.8 2.6
9-trans-Octadecenoic acid methyl ester (C18:1,9t) 0.8 2.6
11-trans-Octadecenoic acid methyl ester (C18:1,11t) 0.8 2.6
Oleic acid methyl ester (C18:1,9c) 0.8 2.6
9-trans-12-trans-Octadecadienoic acid methyl ester
(C18:2,9t12t)
0.8 2.6
Linoleic acid methyl ester (C18:2,9c12c) 1.2 3.9
9,12,15-trans Octadecatrienoic acid methyl ester
(C18:3,9t12t15t)
1.2 3.9
Arachidic acid methyl ester (C20:0) 1.2 3.9
Linolenic acid methyl ester (C18:3,9c12c15c) 1.2 3.9
a
DL: limit of detection based on S/N=3.
b
QL: limit of quantitation based on S/N=10.
W.H. Liu et al. / Food Chemistry 104 (2007) 1740–1749 1743
procedure. It is also possible that the methyl esterification
method (the boron-trifluoride method) used in our experi-
ment may enhance the recovery substantially. Lee, Wang,
and Ming (1990) compared the effect of four methyl ester-
ification methods on the recovery of fatty acids in salad oil
and depicted that a high recovery (>96%) could be
achieved by either boron-trifluoride, sulfuric acid-reflux
or tetramethyl-ammonium-salt method. Conversely, a low
recovery (85.7%) was yielded by the sodium methoxide
method, probably because of moisture absorption and
decomposition into sodium hydroxide, resulting in an
incomplete esterification.
3.2. Fatty acid composition change in soybean oil during
heating
Tables 4–9 show the fatty acid composition in unhydro-
genated and hydrogenated soybean oil. Fresh unhydroge-
nated soybean oil was found to contain three saturated
fatty acids (C16:0, C18:0 and C20:0), 3 cis unsaturated
fatty acids (C18:1, C18:2 and C18:3), of which linoleic acid
constituted the largest portion (407.8 mg/g), followed by
oleic acid (198.9 mg/g). However, in fresh hydrogenated
soybean oil, three saturated fatty acids (C16:0, C18:0 and
C20:0), 2 cis unsaturated fatty acids (C18:1 and C18:2)
and four trans fatty acids (C18:1, D6t; C18:1, D9t;
C18:1, D11tand C18:2, D9tD12t) were present, with cis
oleic acid (199.5 mg/g) dominating, followed by trans oleic
acid (194.7 mg/g). No linolenic acid (C18:3) was detected,
mainly because of conversion into linoleic acid (C18:2) or
oleic acid (C18:1) or stearic acid (C18:0) during hydrogena-
tion. By comparing the various trans forms of fatty acids,
oleic acid was the most susceptible to formation in hydro-
genated soybean oil. Karabulut, Kayahan, and Yaprak
(2003) and Schmidt (2000) studied the formation of trans
fatty acids during oil hydrogenation and the contents of
trans forms of both oleic acid and linoleic acid followed
an increased trend for the increase of reaction time.
3.2.1. Unhydrogenated soybean oil
Table 4 shows the fatty acid composition change of
unhydrogenated soybean oil during heating at 160 °C
for 4, 8, 12, 16, 20 and 24 h. Compared to fresh soybean
oil, the levels of five fatty acids, namely, C16:0, C18:0,
C18:1 (D9c), C18:2 (D9cD12c) and C18:3 (D9cD12cD15c)
decreased along with increasing heating time, probably
because of degradation during extensive heating. After
prolonged heating for 24 h, a sharp decline by 20.2
(22.2%), 6.9 (22.9%), 46.6 (23.4%), 83.6 (25.5%) and
7.3 mg/g (20.4%) occurred for C16:0, C18:0, C18:1
(D9c), C18:2 (D9cD12c) and C18:3(D9cD12cD15c), respec-
tively. However, no trans fatty acid was formed under this
heating condition. The total amounts of fatty acids for
24 h samples were not the same as control samples, which
could be accounted for by the instability of cis fatty acid
under drastic condition for the former (Chen et al., 2001).
In a study dealing with oxidative stability of methyl lino-
leate, methyl oleate and methyl stearate during heating,
Chen et al. (2001) reported that the degradation could
proceed faster than the peroxide formation at elevated
temperature (200 °C). Table 5 shows the fatty acid com-
position change in unhydrogenated soybean oil during
heating at 180 °C. Likewise, the contents of all the fatty
acids exhibited a decreased tendency for the increase in
heating time. After 24-h heating, a marked decline of
21.8 (24.0%), 10.6 (35.2%), 51.9 (26.1%), 11.7 (27.4%),
3.8 (35.0%) and 13.8 mg/g (38.7%) was observed for
C16:0, C18:0, C18:1 (D9c), C18:2 (D9cD12c), C20:0 and
C18:3 (D9cD12cD15c), respectively. Also, no trans fatty
acid was formed in soybean oil heated at 180 °C. Simi-
larly, the levels of all the fatty acids dropped pro-
nouncedly during heating of soybean oil at 200 °C
(Table 6), and a greater loss by 24.3 (26.7%), 12.0
(39.9%), 85.2 (42.8%), 144.1 (35.3%), 4.3 (39.8%) and
19.7 mg/g (55.2%) occurred for C16:0, C18:0, C18:1
(D9c), C18:2 (D9cD12c), C20:0 and C18:3 (D9cD12cD15c),
respectively,after extensive heating for 24 h. Again, no
Table 3
Recovery data of fatty acid methyl esters standards when added to heated soybean oil
Fatty acids Recovery (%) Total average
5000 ppm 10,000 ppm
First Second Average First Second Average
C14:0 100.1 102.9 101.5 103.1 104.4 103.8 102.7 ± 1.6
C16:0 96.1 97.0 96.6 97.2 98.3 97.8 97.2 ± 0.9
C16:1,9t94.0 96.2 95.1 95.2 97.6 96.4 95.8 ± 0.9
C16:1,9c96.1 97.4 96.8 97.1 98.0 97.6 97.2 ± 0.6
C18:0 97.2 98.5 97.9 97.7 99.1 98.4 98.2 ± 0.4
C18:1,6t94.8 96.3 95.5 96.3 98.3 97.3 96.4 ± 1.3
C18:1,9t95.5 94.3 94.9 94.8 96.8 95.8 95.4 ± 0.7
C18:1,11t93.2 94.6 93.9 95.7 97.2 96.5 95.2 ± 1.8
C18:1,9c96.1 97.5 96.8 96.7 98.6 97.7 97.2 ± 0.6
C18:2,9t12t94.9 96.8 95.8 96.0 98.4 97.2 96.5 ± 1.0
C18:2,9c12c93.7 95.8 94.7 96.3 97.1 96.7 95.7 ± 1.4
C18:3,9t12t15t95.4 93.3 94.3 95.2 96.4 95.8 95.0 ± 1.0
C20:0 92.3 93.1 92.7 96.5 95.7 96.1 94.4 ± 2.4
C18:3,9c12c15c95.9 97.1 96.5 96.4 98.4 97.4 96.9 ± 0.6
1744 W.H. Liu et al. / Food Chemistry 104 (2007) 1740–1749
trans fatty acid was formed in heated soybean oil at
200 °C. This result demonstrated that the higher the tem-
perature, the faster the degradation of cis fatty acids
(Frankel, 1998). Moreover, a drastic heating condition
(>200 °C and >24 h) should be required to generate trans
fatty acid formation in the oil. Theoretically, cis fatty acid
should be more susceptible to heat loss than trans fatty
acid (Frankel, 1998). Our result did prove that cis fatty
Table 4
Fatty acid composition change during heating of soybean oil at 160 °C for varied length of time
Fatty acid (mg/g)
C
Heating (h)
Control
A
4 8 12 16 20 24
C14:0 ND
B
ND ND ND ND ND ND
C16:0 91.0 ± 1.9
a
77.9 ± 1.1
bc
75.7 ± 1.4
cd
74.1 ± 1.0
de
73.2 ± 1.5
de
71.8 ± 1.0
e
70.8 ± 1.5
e
C16:1,9tND ND ND ND ND ND ND
C16:1,9cND ND ND ND ND ND ND
C18:0 30.1 ± 1.5
a
27.0 ± 0.8
bc
26.2 ± 0.8
bcd
25.6 ± 1.2
cde
24.9 ± 0.2
cde
24.1 ± 0.4
de
23.2 ± 1.1
e
C18:1,6tND ND ND ND ND ND ND
C18:1,9tND ND ND ND ND ND ND
C18:1,11tND ND ND ND ND ND ND
C18:1,9c198.9 ± 2.0
a
173.5 ± 1.6
b
170.6 ± 1.3
b
164.6 ± 1.6
c
160.6 ± 1.3
cd
157.4 ± 1.1
d
152.3 ± 3.1
e
C18:2,9t12tND ND ND ND ND ND ND
C18:2,9c12c407.8 ± 1.8
a
357.1 ± 3.1
b
352.5 ± 1.6
b
345.0 ± 1.7
c
340.6 ± 1.8
cd
336.9 ± 1.8
d
324.2 ± 2.0
e
C18:3,9t12t15tND ND ND ND ND ND ND
C20:0 10.8 ± 0.9
a
10.1 ± 1.5
ab
9.6 ± 0.7
ab
9.1 ± 0.7
ab
8.7 ± 0.4
ab
8.6 ± 0.1
b
8.1 ± 1.0
b
C18:3,9c12c15c35.7 ± 1.0
a
33.3 ± 0.6
bc
32.1 ± 0.9
bc
31.1 ± 1.2
cd
29.3 ± 0.8
de
28.4 ± 0.6
e
28.4 ± 1.2
e
Others 17.4 13.9 13.5 13.1 12.6 12.2 11.3
Subtotal (trans)NDNDND ND ND NDND
Subtotal (cis) 642.4 563.8 555.1 540.7 530.4 522.7 504.8
Subtotal (sat)
D
131.9 115.0 111.5 108.8 106.7 104.5 102.1
trans/cis nil nil nil nil nil nil nil
A
Control: fresh unhydrogenated soybean oil.
B
ND: not detected.
C
Means of duplicate analyses ± standard deviation.
D
Sat: saturated fatty acid.
a–e
Symbols bearing different letters in the same row are significantly different (P< 0.05).
Table 5
Fatty acid composition change during heating of soybean oil at 180 °C for varied length of time
Fatty acid (mg/g)
C
Heating (h)
Control
A
4 8 12 16 20 24
C14:0 ND
B
ND ND ND ND ND ND
C16:0 91.0 ± 1.9
a
73.2 ± 2.9
b
71.4 ± 2.8
b
71.5 ± 1.6
b
71.3 ± 1.1
b
70.5 ± 1.6
b
69.2 ± 1.3
b
C16:1,9tND ND ND ND ND ND ND
C16:1,9cND ND ND ND ND ND ND
C18:0 30.1 ± 1.5
a
23.4 ± 1.4
b
22.0 ± 1.1
bc
23.1 ± 1.5
b
21.5 ± 0.8
bc
21.0 ± 1.7
bc
19.5 ± 1.3
bc
C18:1,6tND ND ND ND ND ND ND
C18:1,9tND ND ND ND ND ND ND
C18:1,11tND ND ND ND ND ND ND
C18:1,9c198.9 ± 2.0
a
169.8 ± 1.7
b
167.9 ± 2.3
bc
163.5 ± 2.0
cd
159.2 ± 3.3
d
151.7 ± 1.0
e
147.0 ± 2.3
e
C18:2,9t12tND ND ND ND ND ND ND
C18:2,9c12c407.8 ± 1.8
a
342.7 ± 3.6
b
340.2 ± 2.2
bc
334.6 ± 2.0
c
324.8 ± 4.9
d
305.8 ± 4.0
e
296.1 ± 2.2
f
C18:3,9t12t15tND ND ND ND ND ND ND
C20:0 10.8 ± 0.9
a
8.3 ± 1.3
b
9.3 ± 1.3
ab
8.4 ± 1.5
ab
7.6 ± 0.2
b
7.5 ± 1.1
b
7.0 ± 0.8
b
C18:3,9c12c15c35.7 ± 1.0
a
29.0 ± 2.1
b
27.4 ± 1.3
bc
24.9 ± 1.3
cd
23.3 ± 1.1
d
22.6 ± 1.3
d
21.9 ± 2.2
d
Others 17.4 13.2 12.9 12.4 11.3 10.3 9.5
Subtotal (trans)NDNDND ND NDNDND
Subtotal (cis) 642.4 541.5 535.5 523.0 507.3 480.0 464.9
Subtotal (sat)
D
131.9 105.0 102.7 102.9 100.5 99.0 95.6
trans/cis nil nil nil nil nil nil nil
A
Control: fresh unhydrogenated soybean oil.
B
ND: not detected.
C
Means of duplicate analyses ± standard deviation.
D
Sat: saturated fatty acid.
a–f
Symbols bearing different letters in the same row are significantly different (P< 0.05).
W.H. Liu et al. / Food Chemistry 104 (2007) 1740–1749 1745
acid could undergo degradation under severe heating con-
ditions, and the degraded products could be aldehyde,
alcohol, ketone or hydrocarbon compounds, depending
on heating temperature and time (Frankel, 1998). In a
similar study dealing with heating of sunflower oil at
220, 240 and 270 °C for 5 h alone, Kamel and Kakuda
(1994) reported no trans fatty acid formation at 220 °C.
However, at 240 and 270 °C, the levels of trans fatty acids
Table 6
Fatty acid composition change during heating of soybean oil at 200 °C for varied length of time
Fatty acid (mg/g)
C
Heating (h)
Control
A
4 8 12 16 20 24
C14:0 ND
B
ND ND ND ND ND ND
C16:0 91.0 ± 1.9
a
70.0 ± 1.2
b
70.2 ± 0.5
b
69.4 ± 1.6
bc
68.3 ± 0.1
bc
67.4 ± 0.8
bc
66.7 ± 0.6
c
C16:1,9tND ND ND ND ND ND ND
C16:1,9cND ND ND ND ND ND ND
C18:0 30.1 ± 1.5
a
21.2 ± 1.6
b
21.7 ± 0.7
b
20.0 ± 1.3
bc
20.3 ± 1.1
bc
19.4 ± 1.3
bc
18.1 ± 0.8
c
C18:1,6tND ND ND ND ND ND ND
C18:1,9tND ND ND ND ND ND ND
C18:1,11tND ND ND ND ND ND ND
C18:1,9c198.9 ± 2.0
a
167.4 ± 3.5
b
158.7 ± 2.8
c
150.0 ± 2.4
d
139.1 ± 1.8
e
126.0 ± 2.0
f
113.7 ± 2.1
g
C18:2,9t12tND ND ND ND ND ND ND
C18:2,9c12c407.8 ± 1.8
a
340.4 ± 3.3
b
329.2 ± 0.3
c
315.9 ± 2.3
d
299.5 ± 2.7
e
280.5 ± 2.6
f
263.7 ± 2.3
g
C18:3,9t12t15tND ND ND ND ND ND ND
C20:0 10.8 ± 0.9
a
7.6 ± 1.0
bc
7.9 ± 0.5
bc
7.7 ± 0.6
bc
7.4 ± 0.4
bc
7.0 ± 0.4
c
6.5 ± 0.5
c
C18:3,9c12c15c35.7 ± 1.0
a
27.5 ± 2.1
b
26.8 ± 0.0
b
23.3 ± 1.1
c
21.1 ± 1.9
cd
18.4 ± 1.1
de
16.0 ± 1.0
e
Others 17.4 12.9 11.8 10.2 9.3 8.1 7.2
Subtotal (trans)NDNDNDNDNDNDND
Subtotal (cis) 642.4 535.2 514.6 489.2 459.6 424.9 393.4
Subtotal (sat)
D
131.9 98.8 99.8 97.1 96.1 93.7 91.3
trans/cis nil nil nil nil nil nil nil
A
Control: fresh unhydrogenated soybean oil.
B
ND: not detected.
C
Means of duplicate analyses ± standard deviation.
D
Sat: saturated fatty acid.
a–g
Symbols bearing different letters in the same row are significantly different (P< 0.05).
Table 7
Fatty acid composition change during heating of hydrogenated soybean oil at 160 °C for varied length of time
Fatty acid (mg/g)
C
Heating (h)
Control
A
4 8 12 16 20 24
C14:0 ND
B
ND ND ND ND ND ND
C16:0 106.0 ± 0.8
a
97.8 ± 0.8
b
95.3 ± 0.8
c
94.2 ± 0.8
cd
93.7 ± 0.6
cd
92.7 ± 0.6
de
91.0 ± 0.9
e
C16:1,9tND ND ND ND ND ND ND
C16:1,9cND ND ND ND ND ND ND
C18:0 81.0 ± 0.8
a
77.2 ± 1.0
b
74.6 ± 1.1
c
73.7 ± 1.0
cd
72.6 ± 0.8
cde
71.6 ± 1.0
de
70.9 ± 0.8
e
C18:1,6t50.5 ± 1.0
a
48.0 ± 1.1
ab
46.7 ± 1.4
b
46.0 ± 1.2
bc
45.7 ± 0.8
bc
43.5 ± 1.3
cd
42.1 ± 1.0
d
C18:1,9t70.4 ± 1.1
a
66.5 ± 1.0
b
65.0 ± 1.0
bc
63.2 ± 0.6
cd
61.5 ± 1.0
d
58.9 ± 1.1
e
56.1 ± 1.2
f
C18:1,11t73.8 ± 0.9
a
68.4 ± 0.7
bc
66.7 ± 1.0
c
64.2 ± 0.9
d
62.7 ± 1.1
de
60.4 ± 1.1
e
57.4 ± 1.3
f
C18:1,9c199.5 ± 1.1
a
186.5 ± 1.1
b
182.9 ± 0.8
c
180.0 ± 1.6
c
174.9 ± 1.1
d
166.8 ± 1.4
e
158.6 ± 1.1
f
C18:2,9t12t9.5 ± 0.5
a
9.1 ± 0.5
ab
8.8 ± 0.4
abc
8.7 ± 0.4
abc
8.3 ± 0.4
bc
8.2± 0.4
bc
7.8 ± 0.6
c
C18:2,9c12c8.0 ± 0.5
a
8.0 ± 0.4
a
7.6 ± 0.6
ab
7.3 ± 0.6
ab
6.4 ± 0.6
bc
6.0 ± 0.4
c
5.6 ± 0.5
c
C18:3,9t12t15tND ND ND ND ND ND ND
C20:0 6.2 ± 0.3
a
6.1 ± 0.3
a
6.1 ± 0.4
a
5.9 ± 0.6
a
6.0 ± 0.4
a
6.1 ± 0.6
a
5.9 ± 0.4
a
C18:3,9c12c15cND ND ND ND ND ND ND
Others 80.7 72.3 70.1 68.9 67.8 66.1 64.4
Subtotal (trans) 204.2 192.0 187.2 182.0 178.1 171.0 163.4
Subtotal (cis) 207.5 194.4 190.5 187.3 181.3 172.8 164.2
Subtotal (sat)
D
193.3 181.1 175.9 173.8 172.3 170.4 167.7
trans/cis 1.0 1.0 1.0 1.0 1.0 1.0 1.0
A
Control: fresh unhydrogenated soybean oil.
B
ND: not detected.
C
Means of duplicate analyses ± standard deviation.
D
Sat: saturated fatty acid.
a–f
Symbols bearing different letters in the same row are significantly different (P< 0.05).
1746 W.H. Liu et al. / Food Chemistry 104 (2007) 1740–1749
rose by 3% and 11%, respectively. Also, no trans fatty
acid formation was observed in several vegetable oils
when heated at 170 and 350 °C for 30 min or 200 and
220 °C for 16 h, and thus Mo
¨llenken (1998) concluded
that trans fatty acids would be difficult to form unless a
severe cooking condition was used. This phenomenon fur-
ther proved that the heating conditions in our experiment
are inadequate to induce formation of trans fatty acids.
Table 8
Fatty acid composition change during heating of hydrogenated soybean oil at 180 °C for varied length of time
Fatty acid (mg/g)
C
Heating (h)
Control
A
4 8 12 16 20 24
C14:0 ND
B
ND ND ND ND ND ND
C16:0 106.0 ± 0.8
a
95.5 ± 1.1
b
94.4 ± 1.1
b
93.2 ± 1.1
bc
91.7 ± 0.8
cd
89.9 ± 0.6
de
87.7 ± 0.8
e
C16:1,9tND ND ND ND ND ND ND
C16:1,9cND ND ND ND ND ND ND
C18:0 81.0 ± 0.8
a
74.9 ± 1.1
bc
73.6 ± 0.9
cd
73.1 ± 1.0
cd
71.7 ± 0.8
de
70.1 ± 1.0
ef
68.9 ± 1.1
f
C18:1,6t50.5 ± 1.0
a
46.7 ± 1.3
b
46.2 ± 1.3
bc
45.3 ± 1.2
bc
43.3 ± 1.6
cd
41.5 ± 1.5
de
38.7 ± 1.6
e
C18:1,9t70.4 ± 1.1
a
63.7 ± 1.3
bc
62.2 ± 1.3
c
61.3 ± 1.2
c
58.6 ± 1.2
d
55.4 ± 1.0
e
50.7 ± 0.6
f
C18:1,11t73.8 ± 0.9
a
65.2 ± 1.6
bc
63.7 ± 1.6
c
63.7 ± 1.6
c
60.4 ± 1.1
d
57.4 ± 1.0
e
51.5 ± 0.8
f
C18:1,9c199.5 ± 1.1
a
183.3 ± 1.3
bc
181.6 ± 1.1
c
177.7 ± 1.1
d
169.3 ± 1.2
e
159.1 ± 1.8
f
144.0 ± 2.4
g
C18:2,9t12t9.5 ± 0.5
a
8.9 ± 0.5
ab
8.9 ± 0.5
ab
8.8 ± 0.4
ab
8.6 ± 0.5
abc
7.8 ± 0.6
bc
7.5 ± 0.4
c
C18:2,9c12c8.0 ± 0.5
a
7.8 ± 0.5
ab
7.4 ± 0.5
ab
7.1 ± 0.6
ab
6.6 ± 0.5
bc
5.7 ± 0.4
c
5.5 ± 0.6
c
C18:3,9t12t15tND ND ND ND ND ND ND
C20:0 6.2 ± 0.3
a
5.9 ± 0.6
a
5.9 ± 0.5
a
6.1 ± 0.4
a
6.0 ± 0.4
a
5.8 ± 0.1
a
5.8 ± 0.5
a
C18:3,9c12c15cND ND ND ND ND ND ND
Others 80.7 70.1 69.1 67.5 65.2 63.0 60.4
Subtotal (trans) 204.2 184.5 180.9 179.0 170.8 162.1 148.2
Subtotal (cis) 207.5 191.0 189.0 184.7 175.8 164.7 149.5
Subtotal (sat)
D
193.3 176.2 173.8 172.4 169.4 165.7 162.4
trans/cis 1.0 1.0 1.0 1.0 1.0 1.0 1.0
A
Control: fresh unhydrogenated soybean oil.
B
ND: not detected.
C
Means of duplicate analyses ± standard deviation.
D
Sat: saturated fatty acid.
a–g
Symbols bearing different letters in the same row are significantly different (P< 0.05).
Table 9
Fatty acid composition change during heating of hydrogenated soybean oil at 200 °C for varied length of time
Fatty acid (mg/g)
C
Heating (h)
Control
A
4 8 12 16 20 24
C14:0 ND
B
ND ND ND ND ND ND
C16:0 106.0 ± 0.8
3a
93.8 ± 0.5
b
93.0 ± 1.3
bc
91.6 ± 0.9
bc
90.9 ± 1.3
c
87.8 ± 1.0
d
84.1 ± 1.2
e
C16:1,9tND ND ND ND ND ND ND
C16:1,9cND ND ND ND ND ND ND
C18:0 81.0 ± 0.8
a
72.6 ± 0.7
bc
71.6 ± 1.1
cd
73.1 ± 0.9
bc
69.7 ± 0.8
de
68.0 ± 0.8
ef
66.1 ± 1.1
f
C18:1,6t50.5 ± 1.0
a
43.7 ± 1.7
b
44.6 ± 1.4
b
44.8 ± 1.0
b
40.4 ± 1.1
c
37.2 ± 1.5
d
35.2 ± 1.3
d
C18:1,9t70.4 ± 1.1
a
61.7 ± 1.2
bc
59.0 ± 1.9
cd
59.0 ± 1.9
cd
56.3 ± 2.1
d
52.2 ± 1.6
e
45.8 ± 1.4
f
C18:1,11t73.8 ± 0.9
a
63.3 ± 1.1
b
63.0 ± 1.2
b
61.2 ± 1.5
b
56.9 ± 1.3
c
52.7 ± 0.8
d
46.8 ± 1.3
e
C18:1,9c199.5 ± 1.1
a
181.4 ± 1.1
bc
179.3 ± 1.3
c
172.4 ± 1.6
d
154.7 ± 1.2
e
143.9 ± 1.7
f
130.7 ± 1.6
g
C18:2,9t12t9.5 ± 0.5
a
8.7 ± 0.1
abc
8.6 ± 0.4
abc
8.5 ± 0.6
abc
8.2 ± 0.6
bcd
7.6 ± 0.5
cd
7.2 ± 0.5
d
C18:2,9c12c8.0 ± 0.5
a
7.2 ± 0.6
ab
6.7 ± 0.6
abc
6.4 ± 0.4
bc
6.2 ± 0.8
bc
5.6 ± 0.4
c
5.2 ± 0.4
c
C18:3,9t12t15tND ND ND ND ND ND ND
C20:0 6.2 ± 0.3
a
5.9 ±0.5
a
5.9 ± 0.3
a
5.9 ± 0.3
a
5.7 ± 0.6
a
5.5 ± 0.4
a
5.7 ± 0.2
a
C18:3,9c12c15cND ND ND ND ND ND ND
Others 80.7 67.8 67.5 65.0 64.3 60.2 55.6
Subtotal (trans) 204.2 177.4 175.2 173.6 161.8 149.6 134.9
Subtotal (cis) 207.5 188.6 186.0 178.8 160.8 149.5 135.9
Subtotal (sat)
D
193.3 172.2 170.4 170.5 166.3 161.3 155.8
trans/cis 1.0 0.9 0.9 1.0 1.0 1.0 1.0
A
Control: fresh unhydrogenated soybean oil.
B
ND: not detected.
C
Means of duplicate analyses ± standard deviation.
D
Sat: saturated fatty acid.
a–g
Symbols bearing different letters in the same row are significantly different (P< 0.05).
W.H. Liu et al. / Food Chemistry 104 (2007) 1740–1749 1747
3.2.2. Hydrogenated soybean oil
Table 7 shows the fatty acid composition change in
hydrogenated soybean oil during heating at 160 °C for 4,
8, 12, 16, 20 and 24 h. A loss of 8.2, 3.8, 3.9, 5.4 and
13.0 mg/g was reached 4 h after heating for C16:0, C18:0,
C18:1 (D9t), C18:1 (D11t) and C18:1 (D9c), respectively.
In comparison with fresh hydrogenated soybean oil, a dis-
tinct decrease by 15.0 (14.2%), 10.1 (12.5%), 8.4 (16.6%),
14.3 (20.3%), 16.4 (22.2%), 40.9 (20.5%), 1.7 (17.9%) and
2.4 mg/g (30.0%) was shown for C16:0, C18:0, C18:1
(D6t), C18:1 (D9t), C18:1 (D11t), C18:1 (D9c), C18:2
(D9tD12t) and C18:2 (D9cD12c), respectively, after 24-h
heating. Likewise, both cis and trans fatty acids can
undergo degradation simultaneously after extensive heat-
ing. Nevertheless, no trans fatty acid was formed under this
condition. A similar trend was observed for the fatty acid
composition change during heating of hydrogenated soy-
bean oil at 180 °C(Table 8). A large decline by 18.3
(17.3%), 12.1 (15.0%), 11.8 (23.4%), 19.7 (28.0%), 22.3
(30.2%), 55.5 (27.8%), 2.0 (21.1%) and 2.5 mg/g (31.3%)
was attained 24 h after heating for C16:0, C18:0, C18:1
(D6t), C18:1 (D9t), C18:1 (D11t), C18:1 (D9c), C18:2
(D9tD12t) and C18:2 (D9cD12c), respectively. Also, no
trans fatty acid was formed. The same tendency also
applied to hydrogenated soybean oil when heated alone
at 200 °C for 24 h (Table 9), i.e., the contents of C16:0,
C18:0, C18:1 (D6t), C18:1 (D9t), C18:1 (D11t), C18:1
(D9c), C18:2 (D9tD12t) and C18:2 (D9cD12c) showed a
greater decrease by 21.9 (20.7%), 14.9 (18.4%), 15.3
(30.3%), 24.6 (34.9%), 27.0 (36.6%), 68.8 (34.5%), 2.3
(24.2%) and 2.8 mg/g (35.0%), respectively, while no trans
fatty acid formation was observed.
By comparison of the results shown above, it may be
concluded that an Agilent HP-88 column could provide
effective separation of eight trans fatty acids and nine
cis fatty acids within 31 min. Both the degradation of
cis and trans fatty acids could proceed fast at elevated
temperature. No trans fatty acid was formed in unhydro-
genated and hydrogenated soybean oil during heating at
160, 180 or 200 °C for 24 h, implying that trans fatty acid
can only be formed under drastic heating condition. The
technique developed in this study may be adopted as a
reference method for routine analysis of trans fatty acids
in commercial food products. As mentioned before, the
nutrition labeling of trans fatty acids has become an
urgent issue to solve, and application of this method
can provide valuable information to assist consumers in
maintaining healthy dietary practices. Further research is
necessary to study the formation of trans fatty acids in
bakery and fried products with hydrogenated oil as heat-
ing medium.
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... In addition, thermal treatment of cooking oils can alter their physicochemical properties and potentially generate TFA from cis-unsaturated fatty acids during cooking procedures (e.g., deep-, pan-, or stir-frying) [10][11][12]. While some previous studies have reported increases in TFA content of edible oils during cooking, others demonstrate little or no change [13][14][15]. Furthermore, amongst studies that report increases in TFA content of oil during cooking, the magnitude of the reported increase is variable. ...
... Of the 234 studies identified by our search, 33 were included in this review ( Figure 1 and Supplementary Table S1). Collectively, the studies analysed 21 different cooking oils, with corn [11,13,[16][17][18][19][20][21][22][23], soybean [15,20,21,[23][24][25][26][27][28][29], sunflower [11,16,20,21,[30][31][32][33][34], and hydrogenated vegetable fat [15,24,27,29,31,[35][36][37] being the most commonly assessed; fewer studies investigated other oils including Aleppo pine seed [38], blend [16,17,23,33,39,40], canola [17,41], coconut [42], cottonseed [35], groundnut [24], linseed [20], olive [11,12,16,20,24,32,34], palm [33,36,39,42,43], peanut [20,28,36], peony seed [20], rapeseed [20,24,44], rice bran [17,20,40], safflower [17,23], and sesame [17,20] oil; or solid fats such as ghee [24] and lard [16]. The relatively high baseline (preheating) levels of TFA in hydrogenated vegetable fats compared to the two most commonly studied cooking oils (corn and soybean) are shown in Supplementary Table S2. ...
... Of the 234 studies identified by our search, 33 were included in this review ( Figure 1 and Supplementary Table S1). Collectively, the studies analysed 21 different cooking oils, with corn [11,13,[16][17][18][19][20][21][22][23], soybean [15,20,21,[23][24][25][26][27][28][29], sunflower [11,16,20,21,[30][31][32][33][34], and hydrogenated vegetable fat [15,24,27,29,31,[35][36][37] being the most commonly assessed; fewer studies investigated other oils including Aleppo pine seed [38], blend [16,17,23,33,39,40], canola [17,41], coconut [42], cottonseed [35], groundnut [24], linseed [20], olive [11,12,16,20,24,32,34], palm [33,36,39,42,43], peanut [20,28,36], peony seed [20], rapeseed [20,24,44], rice bran [17,20,40], safflower [17,23], and sesame [17,20] oil; or solid fats such as ghee [24] and lard [16]. The relatively high baseline (preheating) levels of TFA in hydrogenated vegetable fats compared to the two most commonly studied cooking oils (corn and soybean) are shown in Supplementary Table S2. ...
Article
Full-text available
Consumption of trans fatty acids (TFA) is associated with adverse health outcomes and is a considerable burden on morbidity and mortality globally. TFA may be generated by common cooking practices and hence contribute to daily dietary intake. We performed a systematic review and meta- analysis to investigate the relationship between heating edible oils and change in their TFA content. A systematic search of experimental studies investigating the effect of various methods of heating on TFA content of edible oils was conducted in Medline and Embase since their inception up to 1 October 2020 without language restrictions. Comparable data were analysed using mixed multilevel linear models taking into account individual study variation. Thirty-three studies encompassing twenty-one different oils were included in this review. Overall, heating to temperatures <200 ◦C had no appreciable impact on different TFA levels. Between 200 and 240 ◦C, levels of C18:2 t (0.05% increase per 10 ◦C rise in temperature, 95% CI: 0.02 to 0.05%), C18:3t (0.18%, 95% CI: 0.14 to 0.21%), and total TFA (0.38%, 95% CI: 0.20 to 0.55%) increased with temperature. A further increase in total TFA was observed with prolonged heating between 200 and 240 ◦C. Our findings suggest that heating edible oils to common cooking temperatures (≤200 ◦C) has minimal effect on TFA generation whereas heating to higher temperatures can increase TFA level. This provides further evidence in favour of public health advice that heating oils to very high temperatures and prolonged heating of oils should be avoided.
... Трансжирні кислоти (ТЖК) -це ненасичені жирні кислоти, які містять хоча б один подвійний зв'язок у транс-конфігурації, які є твердими або напівтвердими при кімнатній температурі (Guo, et al., 2023). Останні утворюються під час промислової часткової гідрогенізації рослинної олії, процесу широко комерціалізованого для виробництва Вісник Сумського національного аграрного університету Серія «Ветеринарна медицина», випуск 1 (64), 2024 твердих жирів (Meijer, Weststrate, 1997;Liu, et al., 2007). Переробна харчова промисловість відіграє важливу роль у зниженні вмісту ТЖК у готових продуктах харчування шляхом альтернативних джерел жиру з нульовим їх вмістом (Ghafoorunissa, 2008). ...
... Нагрівання рослинної олії до температури 250 °С і вище або багаторазове нагрівання приготовлених продуктів чи повторне використання олії багато разів призводить до утворення трансжирів. Якщо смажити на натуральній олії за температури до 200 °С, то ТЖК не утворюються (Liu, et al., 2007). ...
Article
Метою здійснення огляду було проаналізувати сучасні світові тенденції щодо контролю харчових продуктів на наявність трансжирів та визначити їх вплив на здоров'я населення для захисту споживача. Нещодавно (2023 рік) ВООЗ оцінила ризик ТЖК та зазначила, що надмірне їх споживання (> 1% від загального споживання енергії) спричинило понад 500000 смертей від ішемічної хвороби (ІХС) і збільшило на 21% ризик серцевих захворювань, смертність – на 28% у всьому світі щорічно. На думку медиків, пальмова олія, в який в процесі рафінування, очищення і фракціонування за температури 200 °С і вище виникають шкідливі для здоров'я населення сполуки з канцерогенною дією (трансжири), широко застосовується останнім часом, та системно знижує рівень корисного холестерину високої щільності у крові і збільшує рівень холестерину низької щільності. Останній у вигляді ліпопротеїдів низької щільності осідає на стінках артерій і призводить до стенокардії, серцевої недостатності, ішемічної хвороби серця. інфаркту та інсульту. Дослідження довели прямий зв'язок, що вони можуть спричиняти онкологічні захворювання (рак молочної залози та прямої кишки), діабет, ожиріння, жирову дистрофію печінки, атеросклероз, безпліддя, скорочення терміну вагітності, алергію, розлади нервової системи та зору у немовлят, послаблення імунітету, зниження працездатності і провокують хворобу Альцгеймера, чоловічу фертильність. Однією з пріоритетних цілей ВООЗ у вирішенні питання контролю та профілактики неінфекційних хвороб є виключення промислововироблених ТЖК із харчових продуктів. Вирішення цього питання на державному рівні вимагає заборони наявності трансжирів в харчових продуктах, а переробна харчова промисловість повинна застосовувати альтернативні джерела жиру з нульовим їх вмістом, адже мова не лише про їх небезпечність, але й про здоров'я нації. Провідну роль у захисті споживача відіграє Держпродспоживслужба, яка має налагодити чітку систему контролю за ТЖК у готових виробах та забезпечити недопущення їх до реалізації. Для ефективного моніторингу і контролю за вмістом трансжирів у харчових продуктах необхідно посилити спроможності лабораторної мережі, проводити інформаційну роботу щодо здорового харчування серед населення.
... The formation of TFAs during frying was influenced by many parameters such as frying conditions, frying materials and even the techniques used for the measurements of TFAs. Although it can be formed by used frying materials and released into the frying oil (Bansal et al., 2009;Liu et al., 2007;Chen et al., 2001). Oil undergoes deterioration during frying through hydrogenation process and as a result increases the amount of TFAs and decreases the level of UFAs (Guallar-Castillón et al., 2012;Fillion and Henry, 1998). ...
... Attenuated total reflection Fourier transformed (ATR-FTIR) spectroscopy is a rapid and fast method to analyse TFAs content (<1%) in edible/vegetable oils and fats (Priego-Capote et al., 2004). However, GC and FTIR spectroscopy isa common technique used for the determination of the TFAs in the edible oils and fats (Cho et al., 2011;Priego-Capote et al., 2007;Liu et al., 2007). The quantitative determination of isolated TFAs using FTIR spectroscopy is based on the measurement of trans peak area in the specific region (991-945/cm), which represents (CH) out-of-plane deformation absorption. ...
... The formation of TFAs during frying was influenced by many parameters such as frying conditions, frying materials and even the techniques used for the measurements of TFAs. Although it can be formed by used frying materials and released into the frying oil (Bansal et al., 2009;Liu et al., 2007;Chen et al., 2001). Oil undergoes deterioration during frying through hydrogenation process and as a result increases the amount of TFAs and decreases the level of UFAs (Guallar-Castillón et al., 2012;Fillion and Henry, 1998). ...
... Attenuated total reflection Fourier transformed (ATR-FTIR) spectroscopy is a rapid and fast method to analyse TFAs content (<1%) in edible/vegetable oils and fats (Priego-Capote et al., 2004). However, GC and FTIR spectroscopy isa common technique used for the determination of the TFAs in the edible oils and fats (Cho et al., 2011;Priego-Capote et al., 2007;Liu et al., 2007). The quantitative determination of isolated TFAs using FTIR spectroscopy is based on the measurement of trans peak area in the specific region (991-945/cm), which represents (CH) out-of-plane deformation absorption. ...
Article
Full-text available
Trans Fats are the worst fat that human being consumed in a diet. It has been produced during the hydrogenation process of edible oil/fats. Basically it has an adverse effect on human health by raising bad cholesterol (LDL) and decreasing the percentage level of good cholesterol (HDL). This ultimately increases the chance of heart stroke due to high build-up of bad cholesterol in blood arteries. Now days, the growing interest related to the consumption of foods products comprising trans fatty acids (TFAs) has been increased due to their risky effects on health. The permissible consumption limit of trans fat in foods should be less than 1%. It is therefore necessary to focuses on the process that generate TFAs in different food products. Hydrogenation is main source for TFAs production, the part of industrial hydrogenation is mainly affected to raise the level of trans fat (10-50%) comparative to thermal process (1-3%).
... A modified method based on the literature was used [52]. First, 200 mg of lipid sample was placed in a 10 mL glass tube with 2 mL of KOH-CH 3 OH (0.5 mol/L); the mixture was then shaken at 60 • C for 30 min. ...
Article
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Improved methods for the extraction of eicosapentaenoic acid (EPA), an essential and economically important polyunsaturated fatty acid, are urgently required. However, lipid extraction rates using food-grade solvents such as ethanol are usually low. To improve the ethanol-based extraction rate, and to elucidate the relevant mechanisms, we used cellulase and laccase to treat powdered Nannochloropsis, one of the most promising microalgal sources of EPA. Cellulase and laccase synergistically increased lipid yields by 69.31% and lipid EPA content by 42.63%, by degrading the amorphous hemicellulose and cellulose, improving crystallinity, and promoting the release and extraction of lysodiacylglyceryltrimethylhomoserine. Scanning electron microscopy showed that cell morphology was substantially altered, with cell-wall rupture, loss of cell boundaries, and the release of intracellular substances. In conclusion, Nannochloropsis lipid yields may be directly linked to cell-wall hemicellulose structure, and enzymatic treatment to alter this may improve lipid yields.
... Apart from fat blending, interesterification is another technique that can be effectively used to produce CBE. Interesterification rearranges the fatty acids (FA) within or between the TAG molecules of fats so that their TAG compositions change without changing the FA profiles (Liu et al., 2007). Interesterification may be achieved by chemical or enzymatic processes. ...
Article
Full-text available
Cocoa butter equivalent (CBE) was synthesised from blends of illipé butter stearin (IBS) and palm mid‐fraction (PMF) via enzymatic interesterification (EIE). IBS was blended with PMF in three wt ratios (70:30, 60:40 and 50:50) and the EIE reactions were performed at 50°C for 30 min using an sn‐1,3‐specific lipase from Rhizopus oryzae as a catalyst. The triacylglycerol (TAG) compositions, slip melting points (SMP), crystallisation and melting thermograms, solid fat content (SFC) curves, and crystal microstructure of the blends before and after EIE were studied and compared with cocoa butter (CB). After EIE, the contents of POP and StOSt decreased, whereas the POSt content increased in all blends. Blend EIE 60:40 exhibited the POP and StOSt contents that situated within the ranges of POP and StOSt contents of CB. It also showed SMP, melting peak and melting completion temperatures, melting enthalpy and crystal microstructure most similar to CB. Most importantly, its SFC curve completely matched that of CB. Consequently, EIE 60:40 was chosen for further investigation and it was found to be fully compatible with CB and crystallised into the same polymorphic form (β) as CB. Therefore, EIE 60:40 has a high potential for use as a commercial CBE.
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Nannochloropsis oceanica are marine microalgae that are rich in eicosapentaenoic acid (EPA); in the future, they may become one of the most effective sources of EPA. The cell walls of N. oceanica contain a three‐layered dense structure called algaenan, which hinders the extraction of intracellular lipids. Here, the main variables for the enzyme pretreatment of N. oceanica are optimized using response surface methodology. Under the optimal variables for enzyme pretreatment, the lipid yield and EPA content are increased to 26.9% and 20.7 g/100 g, respectively. Furthermore, lipidomics analysis is carried out utilizing ultra‐high performance liquid‐quadrupole‐time‐of‐flight mass spectrometry to identify the obtained lipids. After enzyme treatment, the betaine lipids (BL) content significantly increases, probably due to laccase and cellulase promoting the release of BL from membrane structure. In comparison, the hydrolysis of neutral lipids, glycolipids, and phospholipids during the enzyme treatment reduces their respective contents. The results of this study suggest that using compound enzymes to pretreat N. oceanica can effectively increase lipids extraction yields by ethanol and improve the EPA contents in lipids. Practical applications : This study indicates that enzyme pretreatment can promote the extraction of lipids, especially lipids with EPA, from N. oceanica or other marine microalgae.
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Book
Lipids are very important both as components of human nutrition and in applications such as the chemical, cosmetics and food industries. At present the world oil supply depends on conventional sources and changes in the political and economical map of the world may mean consumer demand will surpass supplies. In developed nations consumer preferences due to nutrition and health factors have also created a need to produce new types of oil. Many nations lack the power to purchase fats ,and oil due to shortages in hard currency. These nations have a vast number of plants that can be developed and used in extracting oil for home use and for sale as cash crops. Also, a vast amount of waste from food processing, such as tomatoes, peaches, plums and grapes, can be utilized to extract valuable amounts of usable oil. Biotechnology, genetic engineering, enzyme tech­ nologies and new processes are all being utilized in lipids research to develop new and modified types of oil for different applications; such developments include the high oleic acid, sunflower and rapeseed oils. The development of cocoa butter substitute is another example. This highly practical book reviews the methods of improving oil charac­ teristics from existing sources, and the technology and economics of developing under-utilized sources. It is written for lipid chemists, chemical engineers, food technologists, cosmetologists and nutritionists. Graduate and undergraduate students will find value in the data. B.S.K.
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This review critically evaluates the scientific data on trans fatty acids and coronary heart disease (CHD) risk. Trans fatty acids are present in a variety of foods but they contribute only 4-12% of total dietary fat intake (2-4% of total energy intake) in the United States. The physical properties of trans fatty acids are intermediate between cis and saturated fatty acids, but a trans double bond is chemically less reactive than a cis double bond. Biochemical data indicate that trans fatty acids are subject to the same metabolic control mechanisms that regulate the metabolism of saturated and cis-isomeric fatty acids. Equivocal results have been reported in observational studies of trans fatty acid intake and CHD because of numerous methodologic limitations, including the difficulties inherent in quantifying trans fatty acid intake. Studies in hamsters indicate that trans fatty acids have a neutral effect on low-density-lipoprotein (LDL)-receptor activity, LDL-cholesterol production rate, and plasma LDL-cholesterol concentration. Other animal studies show no differences in atherosclerosis incidence or severity between diets containing hydrogenated and native vegetable oils. In clinical studies partially hydrogenated oils lower total and LDL-cholesterol concentrations when substituted for animal or vegetable fats rich in saturates but raise total and LDL-cholesterol concentrations when substituted for the unhydrogenated native oil. The effects of trans fatty acids on high- density lipoprotein cholesterol and lipoprotein(a) concentrations are unclear because of limited and conflicting clinical data. Data supporting a relation between trans fatty acid intake and CHD risk are equivocal compared with extensive data from studies in animals and humans linking saturated fat intake to CHD. Additional research is needed to resolve questions about the independent effects of trans fatty acids on plasma lipoproteins and their mechanisms of action.
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Atherosclerosis, formerly considered a bland lipid storage disease, actually involves an ongoing inflammatory response. Recent advances in basic science have established a fundamental role for inflammation in mediating all stages of this disease from initiation through progression and, ultimately, the thrombotic complications of atherosclerosis. These new findings provide important links between risk factors and the mechanisms of atherogenesis. Clinical studies have shown that this emerging biology of inflammation in atherosclerosis applies directly to human patients. Elevation in markers of inflammation predicts outcomes of patients with acute coronary syndromes, independently of myocardial damage. In addition, low-grade chronic inflammation, as indicated by levels of the inflammatory marker C-reactive protein, prospectively defines risk of atherosclerotic complications, thus adding to prognostic information provided by traditional risk factors. Moreover, certain treatments that reduce coronary risk also limit inflammation. In the case of lipid lowering with statins, this anti-inflammatory effect does not appear to correlate with reduction in low-density lipoprotein levels. These new insights into inflammation in atherosclerosis not only increase our understanding of this disease, but also have practical clinical applications in risk stratification and targeting of therapy for this scourge of growing worldwide importance.
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Frying process has been considered to be a source of trans fatty acids. However, most trans fatty acids found in foods would come from the oil used and not from the process itself. To test this, the trans fatty acid production was measured frying in extra virgin olive oil (EVOO), high oleic sunflower oil (HOSO) and sunflower oil (SO) various frozen foods 20 times with frequent replenishment (FR) or without replenishment (NR) of the used oil with fresh oil during the frying. Further, the fat extracted from potatoes fried in the EVOO, HOSO and SO from the frying 8 and 20 was also analyzed by gas liquid chromatography to compare it trans fatty acid profile with that of the corresponding fryer oil. Trans fatty acids appear in lower amounts than 5 mg/g oil or fat in both FR and NR. Elaidic acid was the most abundant trans fatty acid in EVOO or in the fat extracted from EVOO fried potatoes while trans linoleic isomers were more abundant in SO. HOSO was in between. Present data suggest that frequent addition of fresh oil through the frying process minimizes the fatty acid changes contributing to obtain fried foods with less amount of trans fatty acids. The consumption of a large standard ratio (∼ 140 g) of these fried potatoes would implied the irrelevant amount of less than 0.13 g of trans fatty acids.
Article
In the TRANSFAIR study, foods contributing to 95% of total fat intake were collected in 14 European countries. In addition to edible fats, dairy, meat, and bakery products some specific food items with relatively high amounts oftransfatty acids were found. French fried potatoes, both those from fast-food restaurants and those from the supermarkets (including potato chips), contained mostly between 12 and 35%transfatty acid, but some products fried in animal fat or vegetable oil contained lower proportions between 0.5 and 7% total fatty acids. Deep-fried croquettes were also rich intransfatty acids. Microwave popcorn samples contained 27–34%transfatty acids. Ready-made popcorn was low intransfatty acids but generally contained even more saturated fatty acids. Dry soup and sauce mixes and cubes and high-fat, frosted breakfast cereals were other examples of foods that often contained >10%transfatty acids. It is concluded that any deep-fried product such as French fried potatoes may contain high proportions of isomerictransfatty acids. Processed foods with a long shelf life such as dry soup powders and cubes, savory snacks, and popcorn often contained relatively high proportions oftransfatty acids, although the contributions of these products to total fat intake are probably small. The foods and snacks with a high proportion oftransfatty acids usually contained less saturated fatty acids and morecis-unsaturated fatty acids than respective foods prepared with low-transsaturated vegetable fats or animal fats.
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The effects of methyl conjugated linoleate (MCLA) on the degradation and oxidative stability of model lipids, methyl linoleate (ML), methyl oleate (MO) and methyl stearate (MS), during heating at 100, 150 or 200°C for 3 h or illumination at 4000 lux for 14 days were studied. Results showed that under either temperature treatment or illumination, MCLA was the most susceptible to degradation, followed by ML, MO and MS. At 100°C, peroxide formation was the main reaction in each model lipid. However, at 150°C, peroxide formation was the main reaction in the initial period of heating, followed by degradation. At 200°C, the degradation was the major reaction. In contrast, peroxide formation was the main reaction for each model lipid during illumination. The addition of MCLA may slow degradation of each model lipid during heating. However, the oxidation stability of the whole system (model lipid plus MCLA) may also be decreased. Under light storage, the effect of MCLA was insignificant.