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Asia Pacific J Clin Nutr (1993) 2, 155-163

The trans fatty acid and positional (sn-2) fatty acid composition of some Australian margarines, dairy blends and animal fats

M.P. Mansour* and A.J. Sinclair**

*School of Nutrition and Public Health, Deakin University, Geelong, Australia; **Department of Applied Biology and Biotechnology, Royal Melbourne Institute of Technology, Melbourne, Australia.

We have analysed the fatty acid (FA) composition including the trans fatty acid by GLC and Fourier Transform Infra-Red (FTIR) Spectrophotometry of 13 margarines, five butter/dairy blends and two animal fats (lard and dripping). The samples were purchased from supermarkets in three separate locations across Victoria: Gladstone Park (near Melbourne), Waurn Ponds (near Geelong) and Geelong city. From the FA composition, the P/S, P/(S+trans monoenoic FA), P/M(S+trans monoenoic FA) and w6/w3 ratios were calculated. The FA composition and trans FA content were compared with the last published analysis of Australian margarines in Sydney in 1982. The FA composition of the sn-2 position was obtained by pancreatic lipase deacylation of the whole triglycerides (TG) . From this data, we estimated the per cent interesterified fat which was present in the margarines. The trans FA content of the margarines which was determined by FTIR ranged from 9.2% to 16.3% (mean of 13.1% of total FAME) (7.6 g-13.0 g trans FA/100 g sample, mean of 10.4 g/100 g sample) and from 3.2% to 4.1% (mean of 3.8%) for butter and dairy blends. Lard contained 0.4% trans FA while dripping consisted of 3.6% trans FA. The trans FA content in the margarines was similar to the values published in 1982 with the exception of four brands. The w6/w3 ranged from 2.5 to 363 and the P/S ranged from 1.4 to 3.3 compared with the 1982 figures where the w6/w3 ranged from 3 to 49 and the P/S ranged from 0.1 to 3.7. The estimated per cent interesterified fat in the margarines ranged from 25% to 100%. We estimated the total trans FA intake in the Australian diet to be between 2.7 g/head/day and 4.8 g/head/day. We also estimated that table margarines account for between 36% and 64% of the total trans FA intake in the Australian diet.


Introduction

Trans FAs are formed during the partial hydrogenation of vegetable oils1-4 which are used for the manufacture of margarines and processed foods. Trans FA also occurs in milk fat, butter and ruminant fats such as tallow and dripping (lamb and beef fat, respectively)1,2,4. Trans FA may also be present in fat from non-ruminant animals that consume diets containing trans FA1. In recent times there has been growing concern as to the possible detrimental effects of consumption of trans FA on human health2-9.

Dietary trans FAs have been shown to increase plasma LDL cholesterol 10-14 while decreasing plasma HDL cholesterol levels10-15. Plasma lipoprotein (a) which is thought to be an indicator of atherogenic risk has also been shown to rise with increasing intake of trans FA16,17. As a result of these observations trans monoenoic FAs, which are the major trans FA isomers found in margarines are now being considered at least as harmful as saturated fatty acids12,14,18.

Trans FAs accumulate in a variety of tissues in different amounts with adipose tissue containing the highest level19. Trans FA isomers have also been detected in human breast milk and it has been suggested that these levels may be affected by the mother's diet20,21. Recent reports have shown that trans FA isomers of 18:3 may be metabolized to trans docosahexaenoic acid which can be detected in the brain lipids of rats fed trans 18:322.

The amount of trans FA in margarines depends on the extent of hydrogenation and whether or not the partially hydrogenated vegetable oil is blended with interesterified, animal or dairy fat. The main determinants in the above processes are the availability and cost of the seed oils, animal and dairy fats, in addition to the desired consistency of a particular product.

Several workers have indicated that, irrespective of fatty acid composition, the distribution of FA in the triglyceride structure effects cholesterolaemia. Thus there have been suggestions that linoleic acid is more hypocholesterolaemic23 and stearic acid more hypercholesterolaemic24 when present at the sn-2 position, than when esterified in positions sn-1 or sn-3. The fact that stearic acid is normally esterified at position 1 and rarely at position 2 may partly explain the apparent 'neutral' effect of stearic acid on blood cholesterol.

A Belgian research group reported that butter was less hypercholesterolaemic if the triglyceride FA were randomized by the technique of interesterification25. Butter contains a high proportion of 14:0 and 16:0 FA in the sn-2 position and the interesterification process would reduce the proportion in the 2-position, since interesterification evenly distributes the FA in each of the sn-positions in the TG. Kritchevsky et al.26 have shown that the atherogenic effects of peanut oil for rats could be reduced if the peanut oil was interesterified.

While the mechanisms of these effects are still obscure, nevertheless the results highlight the importance of the positional distribution of FA in the TG. It has been suggested by Redgrave et al.27 that saturated FA in the sn-2 position reduced chylomicron remnant metabolism, a process which has been implicated in atherosclerosis. Ahikari et al.28 have been able to use two FA ratios, namely, the ratio of palmitic acid in the sn-2 position to that found in the whole triglyceride and similarly the amount of total saturated fatty acids in the sn-2 position to that found in the whole triglyceride (R1 and R2, respectively) to estimate the amount of interesterified fat added to a hydrogenated fat. Carpenter et al.29 have been able to show that trans monoenoic FAs are concentrated in the sn-2 positions in some margarines. This observation has been attributed to polyunsaturated FAs being preferentially located in the sn-2 position of the original vegetable oil which are partly converted to trans monoenoic FA during hydrogenation.

Several analyses of Australian margarines (197682)30-33 have reported values of trans FA which were lower (less than 15%) than those from other western countries notably America (10-30% in 1984)34, Canada (10-35% in 1985)35, Britain (4-42% in 1984)36 and up to 50% in northern Europe where partially hydrogenated marine oils were used in the formulation of some cheaper margarines37.

The last analysis of trans FA in Australian margarines was carried out in 198233. Owing to the potential variability in margarine formulations and an upsurge in the interest in trans FA there was a need to analyse the currently produced margarines in the Australian marketplace, determine the trans FA content and sn-2 FA composition and estimate the extent to which interesterified fats were added to partially hydrogenated vegetable oils.

Methods

(All standards and reagents were of 99.9% purity and analytical grade, respectively, unless otherwise stated).

Validation for selection of number of tubs to be analysed

Margarines from three different locations were sampled and initially two tubs were purchased from each location. Duplicate determinations of trans FA content were performed on each tub. We found that the average per cent trans FA content of the first tubs collected from the three locations (10.32 ± 0.28% for six determinations) was very similar to the average per cent trans FA content of the first and second tubs collected from the three locations (10.10 ± 0.40% for twelve determinations). From these results it was concluded that sampling three tubs, one from each location (six determinations) was sufficient.

Sample collections

After collecting one tub from each location, they were coded, dated and stored in a refrigerator at 4°C until required for analysis. Three tubs of an olive oil-based margarine manufactured in Greece (Brio brand) obtained as a gift from Unilever Australia Ltd were also analysed.

Subsampling for analysis

The top 1 cm surface layer was discarded and a core sample of approximately 2 g was taken from two locations in the tub at least 3 cm apart and placed in a 15 mL test tube with a teflon-lined screw cap.

Extraction of lipid

The sample was extracted into petroleum ether (PE) (1 x 10mL then 2x5 mL) with shaking/vortex mixing and centrifugation each time. Effectively all the lipid was extracted by this method as a further chloroform/ methanol (2/1, v/v) re-extraction of the residue yielded no detectable lipid. The extract was transferred and made up to volume in a 25 mL standard flask.

Gravimetric determination of per cent lipid

Aliquots of 1 mL were taken from the 25 mL stock and delivered into pre-weighed glass vials. The PE was evaporated in a stream of nitrogen. The dry extract was stored overnight in a dessicator over silica gel and reweighed the following day.

Fatty acid analysis

Saponification and methylation

A 0.5 mL aliquot from the lipid stock solution and a 1.0 mL aliquot of triheptadecanoin internal standard (13.0 mg/mL) in chloroform were taken and delivered into test tubes with teflon lined screw caps. The solvent was evaporated in a stream of nitrogen and 2 mL of potassium hydroxide in methanol KOH/MeOH (58 mg/mL) was added. The contents of the tube were flushed with nitrogen, quickly capped and placed in a fan-forced oven set at 105°C. After 10 min, 2 mL of 20% boron trifluoride in methanol (BF3/MeOH) was added and the tube reheated for 10 min at 105°C. The fatty acid methyl esters (FAME) were then extracted into the PE. The FAME were then washed with distilled water and dried over anhydrous sodium sulphate. The FAME were chromatographed immediately or stored at -20°C until required for analysis.

Gas liquid chromatography (GLC)

The FAME were separated on a 50 m BPx70 (0.32 mm ID and 0.25 mm film thickness) bonded phase, fused silica capillary column (SGE Ringwood, Victoria, Australia), connected to a Shimadzu GC-9A chromatograph which was interfaced to a Shimadzu CR4A microprocessor integrator used for data storage and handling. The injector and FID detector temperatures were both 280°C and the linear carrier gas (Helium) flow was set to 20 cm/sec. The column oven was set at an initial temperature of 110°C for 3 min and was then increased at 1°C/min until a temperature of 170°C was reached. The rate was then increased to 5°C/min and the final temperature of 200°C was maintained for 30 min.

Total methylene interrupted trans fatty acids by FTIR

This method is based on an IUPAC official method38. The remaining 21.5 mL of the lipid stock was saponified by refluxing with 20 mL of KOH/MeOH (58 mg/mL) for 10 min. 20 mL of BF3/MeOH (20%) was then added and the mixture refluxed for a further 10 min. When the mixture had cooled 20 mL of PE and 20 mL of saturated sodium chloride solution were added, the flask stoppered and the mixture shaken to extract the FAME into the PE phase. After the layers had separated the FAME were siphoned into a 50 mL round-bottomed flask and concentrated on a rotary evaporator at 35°C.

The FAME were purified by eluting through a silica sep-pak (Millipore-Waters) with 10% diethylether (DE) in PE into a pre-weighed 10 mL volumetric flask. The solvent was evaporated in a stream of nitrogen and the flask re-weighed to calculate the mass of FAME. The FAME were diluted to the mark with carbon disulphide (CS2). A 2 mL aliquot was further diluted to 5 mL prior to measuring the IR absorbance.

A series of calibration standards made up of elaidic and stearic acid methyl esters were obtained by bulk methylation of the free fatty acids (Nu Chek Prep, Minnesota, USA) and purified by silica column chromatography using PE as the eluting solvent. The purity was rechecked by thin layer chromatography (TLC) before drying the FAME with nitrogen. The standard solutions were then used to construct a calibration curve. A CS2 filled sodium chloride cell of 1 mm path length was used as the background blank.

The IR absorbance peak area at 970 cm-1 was measured on a FTIR spectrophotometer (FTS-7) (Biorad Laboratories, Digilab Division, Hercules, CA, USA) using the quantitation software (Interquant). The concentration of the total methylene interrupted trans FAME was interpolated from the calibration curve.

Positional (sn-2 FA) analysis of triglycerides

The purification of the TG was achieved by preparative TLC of 400 m L of the lipid stock solution on two TLC plates (200 m L on each plate). The plates were then developed in a solvent system consisting of PE/DE/ glacial acetic acid (90/10/1 v/v/v). After the development the plate was sprayed with 2'7'-dichlorofluoroscein in MeOH and the TG band visualized and marked under a 360 nm UV lamp. The silica gel was then scraped off the plate and placed into a methylation tube and extracted with 10% DE in PE (3 x 5 mL). The extracts were combined and dried in a stream of nitrogen then reconstituted in 400 m L of PE.

Pancreatic lipase deacylation

All reagents used in this section were purchased from the Sigma Chemical Company (St Louis, MO, USA). This method is based on the procedure of Chacko et al.39 Approximately 10 m L of the purified TG (10 m L/400 m L) was dried with nitrogen in a methylation tube to which 100 m L of CaCl2 (22 mg/mL), 250 m L of bile salts (cholate/ deoxycholate, 0.5 mg/mL) and 1 mL of pancreatic lipase (porcine, type II, crude, Sigma, 21.23 mg/mL) in Trizma buffer (Tris base, pH8). The reaction mixture was incubated at 40°C for 0.5 min then the reaction was stopped with 0.5 mL of 6M HCl. The lipase reaction was repeated using 1.0 min and 1.5 min incubations.

After extracting into DE, washing and drying as previously achieved for the FAME, the reaction mixture was examined on TLC using a developing solvent system of PE/DE/glacial acetic acid (85/15/ v/v/v). The plate was then sprayed with 10% CuS04 in 8% H3PO4 (w/v) and charred at 140°C for 30 min.

An incubation time was selected to achieve a 50-60% hydrolysis which would provide a sufficient amount of monoglycerides (MG). If the lipase hydrolysis continues beyond the optimum time some migration of FA between sn-1, 2 and 3 positions may occur in the MG40,41. The optimum incubation time varied between 0.5 and 1.5 min for the various fats analysed.

Results

The measured per cent lipid of the margarines was at least what was stated on the tubs and ranged between 81% and 86% which was similar to the 1982 levels (79-84%). In the case of the dairy blends the per cent lipid ranged between 83% and 85% except for one low-fat brand. Lard and dripping each contained 100% lipid (see Table 1).

Table 1. The lipid content of margarines, butter/dairy blends and animal fats.

Sample Code %Lipid
Margarines
Gold'n Canola GC 85.5
Nuttlex NUT 84.7
Miracle M 82.9
Miracle Canola MCAN 83.1
Meadow Lea ML 81.1
Meadow Lea Canola MLCAN 81.9
ETA ETA 84.3
Flora Flora 82.4
Daffodil DAF 82.6
Becel BEC 85.7
Brio BRIO 81.0
Home Brand Margarine HBM 83.0
Mrs McGregor's MAC 82.6
Butter/Dairy Blends
Western Star Butter WSB 83.2
Western Star Country Gold WSCG 83.0
Devondale Dairy Soft DDS 83.1
Devondale Dairy Canola DDC 60.9
Prefer PRE 84.7
Animal Fat
Lard LAR 100
Dripping DRIP 100

Mean (n=6).

Figure 1 shows the typical chromatograms of a margarine and butter sample. It can be seen that the major trans FA and cis positional isomers are trans 18:1 positional isomers (tentatively identified as 9 trans, 10 trans and 11 trans, cis 18:1 positional isomers (tentatively identified as 9 cis, 10 cis and 11 cis), smaller amounts of trans 18:2 isomers and possibly trans 18:3 isomers. The amounts of these various isomers varied between the different brands of margarines. The FA composition of the margarines is shown in Table 2 and Table 3. The FA composition of the butter/dairy blends was more complex than that of the margarines in terms of having more short chain and branched FA as can be seen in Table 4. The FA composition of the animal fats was less complex than that of the dairy blends (see Table 4).

Figure 1a. A GLC trace of a margarine (MLCAN) showing the main trans 18:1 and cis 18:1 positional isomers (tentative identification) .

Figure 1b. GLC trace of a butter (WSB) showing differences in the amount and type of cis and trans 18:1 positional isomers.

Table 2. Fatty acid composition (% of total FA) in the sn-2 position of TG and of total margarinesa.

FA BECEL ML MLCAN M MCAN BRIO
  Total FA sn-2 FA Total FA sn-2 FA Total FA sn-2 FA Total FA sn-2 FA Total FA sn-2 FA Total FA sn-2 FA
10:0 ndb 0.60 nd 021 nd 0,03 nd 0.39 nd 0.08 nd nd
12:0 nd 0.48 nd 0.17 nd 0.03 0.09 0.50 nd nd nd nd
14:0 0.08 1.77 0.23 0.80 0.18 0.46 0.35 1.07 0.08 0.52 nd nd
16:0 6.13 10.74 11.25 5.22 8.26 2.70 13.54 6.96 6.41 5.76 11.26 3.82
16:1 0.06 0.15 0.08 nd 0.16 nd 0.07 nd 0.14 0.31 0.48 nd
17:0 nd 0.86 nd 0.54 0.27 nd nd 0.34 nd 0.66 nd nd
17:1 nd nd nd nd nd nd nd nd nd nd nd nd
18:0 6.10 11.65 7.38 7.36 4.88 4.56 5.46 5.78 6.35 9.06 8.36 6.79
t-18:1c 7.51 5.67 13.20 11.77 8.83 11.18 12.11 12.84 13.22 9.74 12.78 14.14
18:1 31.00 31.33 24.59 24.33 48.32 49.06 25.18 29.84 51.47 42.34 61.19 64.90
t-18:2 0.97 1.93 0.54 0.37 0.42 0.70 0.66 0.89 1.08 1.14 nd nd
18:2 44.29 28.82 39.05 38.10 15.51 23.96 39.48 39.00 15.75 21.78 4.90 7.53
t-18:3 0.02 0.70 0.09 0.11 0.37 0.42 0.09 nd 0.22 0.52 nd nd
18:3 1.97 1.47 2.02 1.46 38.10 15.51 2.19 1.40 5.80 5.13 0.41 0.62
20:0 0.52 0.52 0.46 0.23 0.53 0.11 0.43 0.19 0.68 0.18 0.45 nd
t-20:1 nd 0.32 0.14 0.13 nd 0.12 0.01 nd nd nd nd nd
20:1 0.38 0.42 0.29 0.18 0.76 0.32 0.22 nd 0.78 0.32 0.17 nd
22:0 0.78 0.34 0.52 0.83 0.31 nd 0.55 0.20 0.33 0.20 nd nd
22:1 nd 2.03 0.02 7.90 0.14 nd nd 1.09 nd 2.26 nd nd
24:0 0.25 0.20 0.21 0.28 0.32 0.31 0.19 nd 0.18 nd nd nd
24:1 nd nd nd nd nd nd nd nd 0.12 nd nd nd

aMean (n=6)
b nd (not detected)
c t-18:1 = 9t-18:1 + 10t-18:1 + 11t-18:1.

Table 3. Fatty acid composition (% of total FA) in the sn-2 position of TG and of total margarinesa.

FA MAC HBA FLORA DAF ETA GC NUT
  Total Fa sn-2 FA Total FA sn-2 FA Total FA sn-2 FA Total FA sn-2 FA Total FA sn-2 FA Total FA sn-2 FA Total FA sn-2 FA
10:0 ndb nd 0.08 0.32 nd nd nd 0.59 nd nd nd nd nd nd
12:0 nd nd 0.10 0.29 0.03 nd 0.26 0.62 0.17 0.42 nd nd nd 0.23
14:0 0.64 1.30 0.22 1.47 0.29 0.51 0.29 1.62 0.24 1.20 0.21 0.51 0.28 0.98
16:0 20.73 11.00 10.81 10.45 12.34 6.17 12.73 10.43 10.44 7.23 9.09 2.24 13.14 6.83
16:1 0.31 0.32 0.08 0.29 0.07 nd 0.03 0.20 0.06 nd 0.21 0.16 nd 0.20
17:0 nd 0.46 nd 0.34 nd 0.24 nd 0.77 nd 0.34 nd 0.25 nd 0.79
17:1 nd nd nd nd nd nd nd nd nd nd nd nd nd nd
18:0 5.96 12.56 7.42 8.97 5.33 6.11 4.97 10.99 7.18 8.48 5.00 3.25 5.96 7.56
t-18:1c 13.51 10.74 9.66 8.10 13.24 14.49 11.62 10.40 13.59 12.09 7.73 9.09 10.98 11.14
18:1 19.30 25.75 24.33 27.08 23.89 29.40 22.16 27.95 25.81 28.86 54.58 48.38 27.29 33.23
t-18:2 0.70 0.58 1.36 0.50 0.44 0.32 0.50 0.99 0.73 0.65 nd 0.22 0.67 1.09
18:2 37:48 30.42 44.65 36.17 40.81 38.45 44.02 30.36 38.63 35.05 15.11 25.62 39.92 32.77
t-18:3 0.14 1.53 nd 0.23 0.06 0.69 nd 0.61 0.08 0.26 0.28 0.58 0.11 0.57
18:3 0.15 1.06 0.74 1.76 1.84 1.48 1.44 1.25 1.42 1.51 5.71 8.50 0.11 0.64
20:0 0.42 0.33 0.39 0.36 0.65 0.18 0.46 0.47 0.49 0.31 0.58 0.10 0.34 0.29
t-20:1 0.18 0.27 nd 0.37 0.07 nd nd 0.08 0.14 0.67 nd 0.13 nd nd
20:1 0.20 0.34 0.13 0.40 0.22 0.55 0.18 0.34 0.31 0.27 0.97 0.18 0.11 0.66
22:0 0.17 0.25 0.61 0.26 0.54 0.16 0.57 0.29 0.52 0.18 0.28 nd 0.54 0.25
22:1 nd 3.29 0.28 2.63 0.01 1.24 nd 2.03 nd 2.48 nd 0.81 nd 2.38
24:0 0.10 nd 0.20 nd 0.19 nd 0.20 nd 0.20 nd nd nd nd 0.13
24:1 nd nd nd nd nd nd nd nd nd nd nd nd nd 0.24

a Mean (n=6)
b nd (not detected)
c t-18:1 = 9t-18:1 + l0t-18:1 + 11t-18:1.

Table 4. Fatty acid composition (% of total FA) in the sn-2 position of TG and of total butter/dairy blends and animal fatsa.

FA WSB WSCG DDS DDC PRE LAR DRIP
  Total FA sn-2 FA Total FA sn-2 FA Total FA sn-2 FA Total FA sn-2 FA Total FA sn-2 FA Total FA sn-2 FA Total FA sn-2 FA
8:0 0.69 0.54 0.68 ndb 0.75 nd 0.45 nd 0.71 0.69 nd nd nd nd
10:0 2.38 0.52 2.26 0.51 2.26 0.11 1.67 0.23 2.13 0.19 nd 0.19 nd 0.22
10:0 0.21 0.13 0.16 nd 0.16 nd nd nd 0.17 nd nd nd nd nd
12:0 3.11 2.84 2.95 1.55 2.67 1.54 2.12 1.59 2.60 0.90 0.08 0.33 0.15 0.22
13:0 0.07 0.12 nd nd 0.07 0.15 nd nd nd nd nd nd nd nd
14:0 11.45 17.07 9.47 8.64 8.60 9.26 7.55 9.39 9.11 28.37 1.62 2.20 4.14 2.72
14:1 0.83 0.63 0.65 0.26 0.54 0.32 0.43 0.22 0.65 0.20 nd 0.16 0.77 nd
15.0 1.10 1.47 0.88 0.74 0.79 0.80 0.66 0.80 0.90 0.80 0.13 0.29 0.58 0.28
16:0 28.84 37.33 22.56 23.00 21.39 23.42 19.17 24.97 23.81 24.17 27.48 47.70 26.52 12.55
16:1 1.23 1.70 0.89 0.83 0.81 0.88 0.82 0.90 0.99 0.96 2.02 0.87 3.12 3.27
17:0 nd 0.78 nd 0.75 nd 0.56 nd 0.77 nd 0.60 nd 1.12 nd 0.58
17:1 0.26 0.36 0.19 nd 0.17 0.20 0.21 nd 0.16 0.36 0.46 0.19 0.66 0.63
18:0 11.29 7.30 11.21 11.47 11.39 9.42 9.85 10.09 11.95 8.66 16.48 10.23 18.02 11.33
t-18:1c 3.35 2.60 3.09 2.88 3.36 3.34 2.34 2.39 2.71 4.23 0.34 2.24 3.10 1.64
18:1 19.58 16.84 22.69 25.78 22.70 22.98 38.46 29.20 23.67 22.46 39.20 18.66 36.92 47.18
t-18:2 0.38 1.04 0.87 0.26 0.90 1.01