Food or edible material: processes – compositions – and products – Products per se – or processes of preparing or treating... – Fat or oil is basic ingredient other than butter in emulsion...
Reexamination Certificate
2001-06-13
2002-11-05
Paden, Carolyn (Department: 1761)
Food or edible material: processes, compositions, and products
Products per se, or processes of preparing or treating...
Fat or oil is basic ingredient other than butter in emulsion...
C426S606000, C426S607000, C554S211000
Reexamination Certificate
active
06475548
ABSTRACT:
BACKGROUND OF THE INVENTION
The present invention refers to a process for the preparation of a blend of triglycerides and to food products containing such blends.
Vegetable oils are the major constituents for the manufacture of margarine and similar fat continuous emulsion spreads. However, natural vegetable oils either do not have the triglyceride composition for imparting a proper plastic consistency to the final product or the obtained spreads show various product defects and/or nutritional drawbacks. Additional processing is necessary for a vegetable fat to become a suitable fat phase for spread manufacture. Usually a relative large amount of unprocessed liquid oil is blended with a relatively small amount of fat which is selected because of its liquid oil structuring ability. Such fat usually is a solid fat which has been subjected to one or more processing treatments. Current developments in food production aim at reducing artificial treatments of food in general and of fat in particular. Particularly, chemical processing such as hydrogenation is expected to be largely abandoned.
When developing new margarine fats one of the aims is to find and grow plants which produce fat which after harvesting and purification is suited for margarine manufacture without additional fat processing. Present margarine fats have a high nutritional value because of a high unsaturated fatty acids acid content, but lack the relatively high stearic acid content and particularly the SUS triglycerides which are needed for structuring the liquid part of the fat blend. On the other side too much stearic acid has to be avoided for nutritional reasons. Breeding novel sunflower plants is a promising route for obtaining improved oils.
Some successes have been reported already with obtaining oils which not only have a high content of oleic acid but also an increased stearic acid content, the so called HSHOSF oils. WO 95/20313 discloses mutants seeds of sunflower plants from which a HSHOSF oil can be harvested with a stearic acid content amounting up to 54 wt. %.
The oleic acid content amounts up to 85 wt. % and the linoleic acid content of up to 2 wt. % is desirably low.
The oils can qualify as natural because being obtained not by genetical modification but by classical breeding techniques. They have been developed in an attempt to obtain a margarine fat which does not need further processing. They would enable the manufacture of a margarine prepared with only natural fat. In principle the high amount (>20 wt. %) of native SOS triglycerides in those novel oils of WO 95/20313 promise good structuring of the margarine fat blend. Such oils were expected to perform as margarine fat without the usual addition of a separate hardstock fat. The high monounsaturates (oleic acid) content is advantageous for nutritional value and for oxidation stability.
However, margarine produced with those fats have shown serious product defects because of the fat's poor crystallization kinetics and an unacceptably high margarine hardness at refrigerator temperature.
Moreover the amount of saturated fatty acids in the final product exceeds the level which is still acceptable for a fat which can meet standards for healthy nutrition.
According to WO 95/20313 the novel oils may be used in a margarine fat composition after dilution with a common liquid oil. Such liquid oils generally contain >90 wt. % of U3+SU2 triglycerides (U: unsaturated fatty acid with 18 or more C-atoms, S: saturated fatty acids with 16 or more C-atoms). Although by dilution said product defects become less pronounced, they do not disappear and the level of saturated fatty acids in the products is still too high. Dilution increasingly reduces the amount of structuring triglycerides to such low level that no proper structuring of the fat phase is possible.
WO 97/35987 discloses another high stearic sunflower seed oil containing 30-65 wt. % of stearic acid. However, this oil has a high palmitic acid content of at least 15 wt. % of palmitic acid. This means that it will be considered as a controversial tropical oil because in a number of countries it is believed to be not acceptable for food production. Additionally, for controlling blood cholesterol level stearic acid is clearly preferred above palmitic acid. For the first hardly an effect on cardiovascular health has been found, while the latter is related to adverse health effects.
The sunflower seed oil disclosed in WO 96/39804 also contains a high amount of palmitic acid and therefore has the same disadvantages as the oils disclosed in WO 97/35987.
The present invention is based on the finding that generally with HSHOSF oils, exemplified by the fat of WO 95/20313, nevertheless a high quality margarine fat can be prepared provided that not the whole HSHOSF fat is used but only its stearin fraction which subsequently is blended with a common cheap vegetable oil.
In comparison with a reference spread product made with the untreated oil of WO 95/20313, the margarine obtained according to the invention exhibits fine product properties, such as good spreadability at temperatures close to refrigerator temperature, excellent melting behaviour in the mouth and stability against oil exudation at high ambient temperatures. The performance of the fat blend equals the performance of known high quality fat compositions, but which often comprise a non-natural component such as hydrogenated fat.
For producing the margarine fat blend of the present invention no chemical means are used, so it may be qualified as a natural margarine fat.
Since long stearin fractions of fats are known to be used as part of a fat phase in order to solve other problems with spread manufacture. Good spreads (melanges) could be prepared with a fat phase consisting of at least 70% of natural butter fat and the remainder vegetable oil. In U.S. Pat. No. 4,438,149 the problem was addressed that when spreads were prepared with a fat phase containing less than 70% butter fat the product possessed a too soft consistency at room temperature. It was found that when the stearinfraction of the butter fat was used, less expensive butter fat was needed for melange production while the spreadability of the product was improved.
SUMMARY OF THE INVENTION
The present invention comprises the preparation of a triglyceride fat suited for structuring a liquid vegetable oil, characterized in that a high stearic high oleic sunflower oil (HSHOSF), such oil containing at least 12 wt. % of stearic acid residues and at least 40 wt. % of oleic acid residues, is subjected to either a wet fractionation or a dry fractionation and a stearin fraction is collected.
The stearin fraction of the fat blend can be obtained by exposing the starting HSHOSF oil to standard conditions for fractionation, either wet or dry fractionation. The fraction containing >30 wt.% of SUS and <40 wt. % of SUU triglycerides is collected.
Suitably, fractionation is stopped when the first 25 wt. % of solid fat has crystallised.
DETAILED DESCRIPTION OF THE INVENTION
Wet fractionation uses a solvent selected from the group consisting of acetone, hexane or petroleum ether. A solvent to oil ratio of 4-6 l solvent per kg oil is applied. For crystallization the oil is cooled to 0-5° C.
Dry fractionation, which is the preferred mode, proceeds according to the following steps:
1. heating the HSHOSF to at least 65° C.,
2. cooling the liquefied oil at a speed of approximately 1° C./minute under continuous agitation to 35° C.;
3. further cooling at an increased rate of approximately 1.5° C/minute to 20° C.,
4. slow cooling to and stabilization at 5-20° C., in particular at 15° C.
The stearin is separated from the resulting slurry in a filter press applying a pressure of about 20 bar. Typically the amount of produced stearin shall be not higher than twice the amount of SUS triglycerides present in the original oil. Typically from an oil containing 20 wt. % of SUS triglycerides not more than 40 wt. % of stearin should be separated. Usually the stearin consists of 50 wt. % of solid material and 5
Bons Johannes Robert
Floeter Eckhard
Stellema Cornelis Sjouke
Honig Milton L.
Lipton division of Conopco, Inc.
Paden Carolyn
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