Solid-liquid fractionation process of oil composition

Food or edible material: processes – compositions – and products – Inhibiting chemical or physical change of food by contact... – Treating liquid material

Reexamination Certificate

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C426S417000, C426S489000, C426S495000, C426S604000, C554S030000, C196S139000

Reexamination Certificate

active

06630189

ABSTRACT:

BACKGROUND OF THE INVENTION
1. Field of the Invention
The present invention relates to a process for separating and preparing a solid oil or fat (hereafter referred to as “oil” merely) composition and a liquid oil composition from an oil composition containing at least 50% by weight of partial glycerides.
2. Description of the Background Art
From the healthy inclination in recent years, a high attention is paid to prevention of increase in body weight to prevent obesity. However, it is being clarified from the results of researches in recent years that not only the prevention of increase in body weight, but also decrease in body fat, particularly, visceral fat is effective to prevent and improve various diseases such as hypofunction of heart, hypertension and arteriosclerosis. It was found that diglycerides having a saturated or unsaturated acyl group having 12 to 22 carbon atoms as a constitutive acyl group are useful as agent for preventing and treating fatty liver (Japanese Patent Application Laid-Open Nos. 300828/1992).
Such diglycerides and monoglycerides (hereinafter referred to as partial glycerides) can be prepared by an ester exchange reaction of oil and fat (hereafter referred to as “oil” merely) such as soybean oil or rapeseed oil with glycerol, an esterification reaction of a fatty acid derived from such an oil and obtained by hydrolysis thereof with glycerol, or the like and purification treatments such as molecular distillation and deodorization.
An oil composition containing partial glycerides prepared by such a process is a mixture of glycerol fatty acid esters having acyl groups of various chain lengths. In order to achieve the inhibitory effect of the diglycerides on accumulation of body fat by daily eating habits, it is necessary replace oil (triglyceride) usually ate by the diglyceride. In order to do so, there are 2 methods. One is to use the diglyceride as a cooking oil in place of usual cooking oil (salad oil). The other is to eat processed food such as mayonnaise, margarine or fry making use of the diglyceride in place of the oil.
Oils different in melting point have been used in these foods from the viewpoints of the place used, flavor and mouth feel, shelf stability and the like, and low-boiling oil and high-boiling oil have been used properly.
For example, salad oil undergoes no crystallization of oil even in a refrigerator or under low-temperature conditions in winter. However, diglyceride is higher in melting point than triglyceride from the viewpoint of structure, and so it crystallizes at a low temperature. Therefore, the glyceride fails to take out of a bottle, or has a disadvantage from the viewpoint of appearance. In addition, when the diglyceride is used as an oil material for mayonnaise or dressing, which may be stored in a refrigerator, as it is, the diglyceride crystallizes, and so the emulsion is solidified, or oil-off (separation of the oil material) occurs. The diglyceride is generally prepared from a general-purpose animal or vegetable oil. Even when rapeseed oil or the like, which contains saturated fatty acids only in a small amount, is used as a raw material for the purpose of lowering the melting point of the resulting diglyceride, the glyceride crystallizes in a refrigerator (at 5° C.) to solidify. The melting point of rapeseed oil is about −5° C., while the melting point of the diglyceride prepared by using the rapeseed oil as a raw material is about 15° C. Accordingly, it has been necessary to remove the high-melting portion of the diglyceride by fractionation to lower the melting point. The fractionated high-melting portion can be used as an oil for bread, fry, chocolate, etc., of which a high melting point is required, as it is.
The nutrition researches of such diglycerides have been made clear in recent years, and the low-melting portion and the high-melting portion thereof have been required to be fractionated. However, in the prior art, there are examples where diglycerides are concentrated or removed from a glyceride mixture by using a solvent (Japanese Patent Application Laid-Open Nos. 65212/1977, 122793/1988, 117845/1989 and 34990/1996, etc.), but there is no example where a high-melting diglyceride and a low-melting diglyceride are fractionated from high-concentration diglycerides. The reason for it is that high-purity diglycerides heretofore marketed from emulsifier makers are those having a melting point of at least 20° C., such as stearic acid diglyceride and oleic acid diglyceride, and they are used as lipophilic emulsifiers by incorporating them in a small amount into an oil and can be completely dissolved in the oil even when their melting points are high, and so no diglyceride having a melting point of 20° C. or lower is required.
Taking the fractionation process of the low-melting portion and the high-melting portion into consideration as described above, separation by chromatography and distillation are considered. However, such processes involve problems of low productivity, high cost, deterioration of quality, etc.
In order to fractionate partial glycerides into a solid portion and a liquid potion, it is necessary to cool the partial glycerides to crystallize a high-melting part thereof. There have been proposed a process in which a lipophilic polyglycerol fatty acid ester is added to an oil to fractionate it into a solid portion and a liquid potion (Japanese Patent Application Laid-Open Nos. 289897/1989 and 31397/1991), a process in which an emulsifier is added to fatty acids to remove a crystallized portion (Japanese Patent Application Laid-Open No. 106782/1999) and the like. However, diglycerides and monoglycerides are treated as impurities which inhibit the crystallization of oil (Yu Kagaku (Oil Chemistry), 28, 700-708 (1979); and Oil Palm News, 22, 10-18 (1997)), and the diglycerides are considered to be hard to be crystallized and, particularly, difficult to dry-fractionate them without using any solvent.
SUMMARY OF THE INVENTION
It is an object of the present invention to provide a process for fractionate an oil composition containing at least 50% by weight of partial glycerides into a solid portion and a liquid portion, by which these problems can be solved.
In fact, in fractionation of palm oil making use of a dry fractionation process, or wintering for preparation of salad oil, crystals deposited by simply cooling are firm, and a crystal slurry thereof is fluid and can be easily separated into a solid portion and a liquid portion by filtration or centrifugation, while a crystal slurry obtained by simply cooling high-concentration diglycerides is not fluid and cannot be separately into a solid portion and a liquid portion under conditions of ordinary filtration or centrifugation, resulting in a failure to provide a liquid portion. As described above, the oil and the partial glycerides are entirely different from each other in crystal properties, and fractionation becomes more difficult as the content of the partial glycerides increases. However, it has been found that in an oil composition containing at least 50% by weight of partial diglycerides, solid-liquid separation becomes feasible by cooling the oil composition to deposit crystals only in the case where an emulsifier is added thereto. It has been thereby found that the oil composition containing the partial glycerides can be separated into a solid portion and a liquid portion with low energy under mild conditions at low cost without using any solvent.
According to the present invention, there is thus provided a process for fractionating an oil composition containing at least 50% by weight of partial diglycerides into a solid portion and a liquid portion, which comprises dissolving an emulsifier in the oil composition, cooling the solution to deposit crystals and then conducting solid-liquid separation.
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS
The oil composition containing at least 50% by weight (hereafter indicated merely by “%”) of partial glycerides used in the present invention is prepared by causing an alkali catalyst or l

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