CA2209765C - Food microemulsion formulations - Google Patents
Food microemulsion formulations Download PDFInfo
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- CA2209765C CA2209765C CA002209765A CA2209765A CA2209765C CA 2209765 C CA2209765 C CA 2209765C CA 002209765 A CA002209765 A CA 002209765A CA 2209765 A CA2209765 A CA 2209765A CA 2209765 C CA2209765 C CA 2209765C
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- fat
- hydrolyzed
- emulsion
- preconcentrate
- oil
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Classifications
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- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23L—FOODS, FOODSTUFFS, OR NON-ALCOHOLIC BEVERAGES, NOT COVERED BY SUBCLASSES A21D OR A23B-A23J; THEIR PREPARATION OR TREATMENT, e.g. COOKING, MODIFICATION OF NUTRITIVE QUALITIES, PHYSICAL TREATMENT; PRESERVATION OF FOODS OR FOODSTUFFS, IN GENERAL
- A23L27/00—Spices; Flavouring agents or condiments; Artificial sweetening agents; Table salts; Dietetic salt substitutes; Preparation or treatment thereof
- A23L27/80—Emulsions
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- A—HUMAN NECESSITIES
- A21—BAKING; EDIBLE DOUGHS
- A21D—TREATMENT, e.g. PRESERVATION, OF FLOUR OR DOUGH, e.g. BY ADDITION OF MATERIALS; BAKING; BAKERY PRODUCTS; PRESERVATION THEREOF
- A21D13/00—Finished or partly finished bakery products
- A21D13/40—Products characterised by the type, form or use
- A21D13/41—Pizzas
-
- A—HUMAN NECESSITIES
- A21—BAKING; EDIBLE DOUGHS
- A21D—TREATMENT, e.g. PRESERVATION, OF FLOUR OR DOUGH, e.g. BY ADDITION OF MATERIALS; BAKING; BAKERY PRODUCTS; PRESERVATION THEREOF
- A21D2/00—Treatment of flour or dough by adding materials thereto before or during baking
- A21D2/08—Treatment of flour or dough by adding materials thereto before or during baking by adding organic substances
- A21D2/14—Organic oxygen compounds
- A21D2/16—Fatty acid esters
-
- A—HUMAN NECESSITIES
- A21—BAKING; EDIBLE DOUGHS
- A21D—TREATMENT, e.g. PRESERVATION, OF FLOUR OR DOUGH, e.g. BY ADDITION OF MATERIALS; BAKING; BAKERY PRODUCTS; PRESERVATION THEREOF
- A21D6/00—Other treatment of flour or dough before baking, e.g. cooling, irradiating, heating
- A21D6/001—Cooling
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23D—EDIBLE OILS OR FATS, e.g. MARGARINES, SHORTENINGS, COOKING OILS
- A23D7/00—Edible oil or fat compositions containing an aqueous phase, e.g. margarines
- A23D7/005—Edible oil or fat compositions containing an aqueous phase, e.g. margarines characterised by ingredients other than fatty acid triglycerides
- A23D7/0053—Compositions other than spreads
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23L—FOODS, FOODSTUFFS, OR NON-ALCOHOLIC BEVERAGES, NOT COVERED BY SUBCLASSES A21D OR A23B-A23J; THEIR PREPARATION OR TREATMENT, e.g. COOKING, MODIFICATION OF NUTRITIVE QUALITIES, PHYSICAL TREATMENT; PRESERVATION OF FOODS OR FOODSTUFFS, IN GENERAL
- A23L2/00—Non-alcoholic beverages; Dry compositions or concentrates therefor; Their preparation
- A23L2/52—Adding ingredients
- A23L2/56—Flavouring or bittering agents
-
- C—CHEMISTRY; METALLURGY
- C11—ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
- C11C—FATTY ACIDS FROM FATS, OILS OR WAXES; CANDLES; FATS, OILS OR FATTY ACIDS BY CHEMICAL MODIFICATION OF FATS, OILS, OR FATTY ACIDS OBTAINED THEREFROM
- C11C1/00—Preparation of fatty acids from fats, fatty oils, or waxes; Refining the fatty acids
- C11C1/02—Preparation of fatty acids from fats, fatty oils, or waxes; Refining the fatty acids from fats or fatty oils
- C11C1/04—Preparation of fatty acids from fats, fatty oils, or waxes; Refining the fatty acids from fats or fatty oils by hydrolysis
-
- C—CHEMISTRY; METALLURGY
- C11—ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
- C11C—FATTY ACIDS FROM FATS, OILS OR WAXES; CANDLES; FATS, OILS OR FATTY ACIDS BY CHEMICAL MODIFICATION OF FATS, OILS, OR FATTY ACIDS OBTAINED THEREFROM
- C11C1/00—Preparation of fatty acids from fats, fatty oils, or waxes; Refining the fatty acids
- C11C1/02—Preparation of fatty acids from fats, fatty oils, or waxes; Refining the fatty acids from fats or fatty oils
- C11C1/04—Preparation of fatty acids from fats, fatty oils, or waxes; Refining the fatty acids from fats or fatty oils by hydrolysis
- C11C1/045—Preparation of fatty acids from fats, fatty oils, or waxes; Refining the fatty acids from fats or fatty oils by hydrolysis using enzymes or microorganisms, living or dead
-
- C—CHEMISTRY; METALLURGY
- C11—ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
- C11C—FATTY ACIDS FROM FATS, OILS OR WAXES; CANDLES; FATS, OILS OR FATTY ACIDS BY CHEMICAL MODIFICATION OF FATS, OILS, OR FATTY ACIDS OBTAINED THEREFROM
- C11C3/00—Fats, oils, or fatty acids by chemical modification of fats, oils, or fatty acids obtained therefrom
- C11C3/04—Fats, oils, or fatty acids by chemical modification of fats, oils, or fatty acids obtained therefrom by esterification of fats or fatty oils
- C11C3/10—Ester interchange
Abstract
An emulsion preconcentrate which contains a hydrolyzed fat, which contains at least 10 % by weight free fatty acids, and an aroma or flavour. The emulsion preconcentrate is included in frozen or chilled food products. Upon heating of the food product to above the melting point of the hydrolyzed fat, the emulsion preconcentrate spontaneously forms an emulsion having microemulsion characteristics with aqueous media in the food product to rapidly release the aroma or flavour.
Description
WO 96!23425 PCT/EP96/00367 F~~d lVlicroemulsion Formulations This invention relates to a formulation for use in food which, when mixed with an aqueous medium and heated, is capable of spontaneously forming an emulsion and releasing a functional substance. The invention also relates to a food product which contains the formulation.
It is often desirable to incorporate functional substances, such as flavourants, aromas, and the like, in foods. For example, consumer perception of a food product is often significantly improved if the product gives off pleasant aroma while cooking or on the table. However many convenience foods which need only be reheated by the consumer often give off reduced amounts of aroma;
if at all. The problem is particularly acute with foods heated in a microwave oven since heating times are not long enough and temperatures are not high enough for flavours and aromas to develop.
Unfortunately, incorporation of functional substances into foods is often problematic. In particular, it is difficult to provide a stable formulation which also readily releases the functional substance when desired. Either the formulation is not stable enough or it is too stable and does not release the functional substance when desired. These problems often become more acute if the functional substance is not soluble in the chosen carrier medium. Also, many functional substances are in the form of precursors which are soluble in one medium as precursors but are soluble in another medium in operative form.
Usually it is not possible to simply mix the various substances since the resulting formulations are not sufficiently stable. These stability problems become even more acute with volatile substances like aromas.
To deal with these problems and other problems, much emphasis has been placed in recent times on microemulsions since these formulations are thermodynamically stable. For example, the formulation of flavourants into microemulsions has been suggested in US patent 4,835,002. However the microemulsions described in this patent require the use of surfactants and alcohols in order for them to form. However the present trend is to reduce the use of these sorts of ingredients in foodstuffs; if at all possible.
Another microemulsion formulation is described in US patent 5,045,337.
Here the aqueous phase, which comprises up to 5% by weight of the emulsion, is formulated as the dispersed phase of a microemulsion. The surfactant which is used to form the microemulsion is a polyglycerol mono, diester of an unsaturated or branched chain fatty acid having from 12 to 24 carbon atoms, esterified with a polyglycerol consisting of up to 30% diglycerol, 30 to 50% triglycerol, 15 to 50%
tetraglycerol, and up to 10% mono and other polyglycerols. The main advantage of these microemulsions is much reduced surfactant content. Although these microemulsions provide an effective solution in some instances, surfactant still must be used.
Therefore there is still a need for a system for incorporating functional substances into food products which does not require the use of added surfactant.
In one aspect, this invention provides an emulsion preconcentrate comprising a hydrolyzed fat which contains at least 10% by weight free fatty acids, and a functional substance captured in the hydrolyzed fat, the emulsion preconcentrate spontaneously forming an emulsion including droplets of dispersed phase of size less than 200 nm upon admixture with water at a temperature higher than the melting point of the hydrolyzed fat.
Surprisingly fats, once hydrolyzed are able, at least partially, to spontaneously form emulsions, in the presence of water and at temperatures above the melting point of the fat, which have characteristics of a microemulsion.
However, unlike prior microemulsions, added surfactant is not required. This is a substantial advantage. For the avoidance of doubt, a microemulsion is a thermodynamically stable, clear liquid which forms spontaneously upon addition of its components and which contains a lipid phase and an aqueous phase.
Further the droplets of the dispersed phase have a droplet size less than 200 nm;
and preferably less than l OQ nm. A microemulsion is different from a normal emulsion in that normal emulsions have droplet sizes in the micron range, are not clear, are not thermodynamically stable, and do not form spontaneously.
Further, in a microemulsion, because the droplets of the dispersed phase are very small, the surface area of the dispersed phase, and hence the surface area for functional substance release, is very large. Thus, upon dissolution in water at a temperature above the melting point of the hydrolyzed fat, the preconcentrate releases a burst of the functional substance; a very significant advantage.
Further, without wishing to be bound by theory, in a microemulsion it is believed that the droplets of the dispersed phase constantly form and reform.
This further permits rapid release of the functional substance. However, prior to the formation of the microemulsion, the functional substance is captured in the preconcentrate in a stable manner.
It is often desirable to incorporate functional substances, such as flavourants, aromas, and the like, in foods. For example, consumer perception of a food product is often significantly improved if the product gives off pleasant aroma while cooking or on the table. However many convenience foods which need only be reheated by the consumer often give off reduced amounts of aroma;
if at all. The problem is particularly acute with foods heated in a microwave oven since heating times are not long enough and temperatures are not high enough for flavours and aromas to develop.
Unfortunately, incorporation of functional substances into foods is often problematic. In particular, it is difficult to provide a stable formulation which also readily releases the functional substance when desired. Either the formulation is not stable enough or it is too stable and does not release the functional substance when desired. These problems often become more acute if the functional substance is not soluble in the chosen carrier medium. Also, many functional substances are in the form of precursors which are soluble in one medium as precursors but are soluble in another medium in operative form.
Usually it is not possible to simply mix the various substances since the resulting formulations are not sufficiently stable. These stability problems become even more acute with volatile substances like aromas.
To deal with these problems and other problems, much emphasis has been placed in recent times on microemulsions since these formulations are thermodynamically stable. For example, the formulation of flavourants into microemulsions has been suggested in US patent 4,835,002. However the microemulsions described in this patent require the use of surfactants and alcohols in order for them to form. However the present trend is to reduce the use of these sorts of ingredients in foodstuffs; if at all possible.
Another microemulsion formulation is described in US patent 5,045,337.
Here the aqueous phase, which comprises up to 5% by weight of the emulsion, is formulated as the dispersed phase of a microemulsion. The surfactant which is used to form the microemulsion is a polyglycerol mono, diester of an unsaturated or branched chain fatty acid having from 12 to 24 carbon atoms, esterified with a polyglycerol consisting of up to 30% diglycerol, 30 to 50% triglycerol, 15 to 50%
tetraglycerol, and up to 10% mono and other polyglycerols. The main advantage of these microemulsions is much reduced surfactant content. Although these microemulsions provide an effective solution in some instances, surfactant still must be used.
Therefore there is still a need for a system for incorporating functional substances into food products which does not require the use of added surfactant.
In one aspect, this invention provides an emulsion preconcentrate comprising a hydrolyzed fat which contains at least 10% by weight free fatty acids, and a functional substance captured in the hydrolyzed fat, the emulsion preconcentrate spontaneously forming an emulsion including droplets of dispersed phase of size less than 200 nm upon admixture with water at a temperature higher than the melting point of the hydrolyzed fat.
Surprisingly fats, once hydrolyzed are able, at least partially, to spontaneously form emulsions, in the presence of water and at temperatures above the melting point of the fat, which have characteristics of a microemulsion.
However, unlike prior microemulsions, added surfactant is not required. This is a substantial advantage. For the avoidance of doubt, a microemulsion is a thermodynamically stable, clear liquid which forms spontaneously upon addition of its components and which contains a lipid phase and an aqueous phase.
Further the droplets of the dispersed phase have a droplet size less than 200 nm;
and preferably less than l OQ nm. A microemulsion is different from a normal emulsion in that normal emulsions have droplet sizes in the micron range, are not clear, are not thermodynamically stable, and do not form spontaneously.
Further, in a microemulsion, because the droplets of the dispersed phase are very small, the surface area of the dispersed phase, and hence the surface area for functional substance release, is very large. Thus, upon dissolution in water at a temperature above the melting point of the hydrolyzed fat, the preconcentrate releases a burst of the functional substance; a very significant advantage.
Further, without wishing to be bound by theory, in a microemulsion it is believed that the droplets of the dispersed phase constantly form and reform.
This further permits rapid release of the functional substance. However, prior to the formation of the microemulsion, the functional substance is captured in the preconcentrate in a stable manner.
The fat which is hydrolyzed may be a natural or fractionated natural fat, or such a fat which has been subjected to selected and directed interesterification.
Preferably the hydrolyzed fat contains at least 20% by weight free fatty acids. For example, the content of free fatty acids in the hydrolyzed fat may be in the range of about 50% to 90% by weight; preferably 70% to 85% by weight.
The free fatty acids preferably include at least 70% by weight of fatty acids having at least 14 carbon atoms. More preferably, the fatty acids having at least 14 carbon atoms provide at least 80% by weight of the total amount of free fatty acids; for example more than 90% by weight.
It is also preferred for the hydrolyzed fat to have a melting point above about 15°C; for example about 30 to 40°C. With a melting point at these temperatures, the hydrolyzed fat is solid at room temperature leading to better entrapment of the functional substance in the emulsion preconcentrate. However for frozen or chilled applications, hydrolyzed fats having lower melting points are acceptable.
The emulsion preconcentrate may further comprise up to 10% by weight of an aqueous medium. This is particularly advantageous when the functional substance is water soluble and not oil soluble. Preferably, however, the preconcentrate contains less than 2% by weight of the aqueous medium.
Preferably the functional substance comprises less than 10% by weight of the preconcentrate; more preferably from 0.01% to 2% by weight.
The function substance may be selected from an aroma, a flavourant, a precursor of ar~aroma or flavourant, or mixtures thereof. Other functional substances such as vitamins, salts, minerals, antioxidants, and the like may also be included. Conveniently, the functional substance is a volatile aroma or precursor thereof, which is released upon the formation of a microemulsion.
In another aspect, this invention provides a food product incorporating an emulsion preconcentrate as defined above. If necessary, the food product may contain additional aqueous phase sufficient to form an emulsion upon heating of the product to a temperature above the melting point of the hydrolyzed fat.
Preferably, the food product is frozen or chilled.
The microemulsion preconcentrate preferably comprises from 0.05 % to ~%
by weight of the food product; more preferably 0.1 to 2% by weight. For example, the microemulsion preconcentrate may comprise 0.2 to 0.6 % by weight of the food product.
Preferably the hydrolyzed fat contains at least 20% by weight free fatty acids. For example, the content of free fatty acids in the hydrolyzed fat may be in the range of about 50% to 90% by weight; preferably 70% to 85% by weight.
The free fatty acids preferably include at least 70% by weight of fatty acids having at least 14 carbon atoms. More preferably, the fatty acids having at least 14 carbon atoms provide at least 80% by weight of the total amount of free fatty acids; for example more than 90% by weight.
It is also preferred for the hydrolyzed fat to have a melting point above about 15°C; for example about 30 to 40°C. With a melting point at these temperatures, the hydrolyzed fat is solid at room temperature leading to better entrapment of the functional substance in the emulsion preconcentrate. However for frozen or chilled applications, hydrolyzed fats having lower melting points are acceptable.
The emulsion preconcentrate may further comprise up to 10% by weight of an aqueous medium. This is particularly advantageous when the functional substance is water soluble and not oil soluble. Preferably, however, the preconcentrate contains less than 2% by weight of the aqueous medium.
Preferably the functional substance comprises less than 10% by weight of the preconcentrate; more preferably from 0.01% to 2% by weight.
The function substance may be selected from an aroma, a flavourant, a precursor of ar~aroma or flavourant, or mixtures thereof. Other functional substances such as vitamins, salts, minerals, antioxidants, and the like may also be included. Conveniently, the functional substance is a volatile aroma or precursor thereof, which is released upon the formation of a microemulsion.
In another aspect, this invention provides a food product incorporating an emulsion preconcentrate as defined above. If necessary, the food product may contain additional aqueous phase sufficient to form an emulsion upon heating of the product to a temperature above the melting point of the hydrolyzed fat.
Preferably, the food product is frozen or chilled.
The microemulsion preconcentrate preferably comprises from 0.05 % to ~%
by weight of the food product; more preferably 0.1 to 2% by weight. For example, the microemulsion preconcentrate may comprise 0.2 to 0.6 % by weight of the food product.
The food product has the significant advantage that, upon heating (for example in a microwave oven) to a temperature above the melting point of the fat, the preconcentrate combines with any aqueous medium in the food to spontaneously form an emulsion which contains droplets of dispersed phase in the microemulsion range. A rapid release of flavour or aroma then results.
Embodiments of the invention are now described, by way of example only.
In this specification, an "emulsion preconcentrate" is a lipid medium which, when added to an aqueous medium at a temperature sufficiently high for the lipid medium to be liquid, is capable of self emulsifying to spontaneously form an emulsion; either water-in-oil or oil-in-water, which includes droplets of dispersed phase in the microemulsion range. It is possible that minor amounts of the dispersed phase may, for various reasons, form larger droplets than would fall within the definition of a microemulsion but these droplets are relatively stable;
at least at neutral pH. If the lipid medium is the dispersed phase, it may contain minor amounts of an aqueousphasedi~ersed in it.
The microemulsion preconcentrate is produced by first hydrolyzing a fat.
The source and the exact composition of the fat used is not critical;
primarily the fat will be selected for desired taste characteristics, compatibility, or for stability.
For example, the fat may be a natural oil or fat of vegetable, animal, or marine origin. Specific examples of suitable fats include sunflower oil, soybean oil, maize oil, safflower oil, rapeseed oil, cottonseed oil, peanut oil, olive oil, cocoa butter, butter fat, fish oils, chicken fat, pork fat, tallow, beef fat, shortening, mixtures thereof, and the like. Alternatively the fat may be a fraction obtained from these natural oils and fats by conventional fractionation techniques; or may be a natural or fractionated fat which has been subjected to selected and directed interesterification. Suitable synthetic fats may also be used but they will usually be too expensive.
The oil may be hydrolyzed by any suitable hydrolysis procedure. However the procedure is ideally such that the formation of large amounts of low molcular weight fatty acids (for example fatty acids having 4 carbon atoms) is avoided since these acids can impart rancid flavours. In one suitable procedure, the oil may be subjected to alkaline hydrolysis in a manner similar to conventional saponification processes for fats and oils. The alkaline used in the procedure may be any suitable alkaline but alkaline based upon alkali and alkali earth metal hydroxides are preferred since the residues of these acids are often acceptable in foods. The alkali metal hydroxides NaOH and KOH are particularly preferred.
WO 96!23425 PCT/EP96/00367 The hydrolysis may be terminated in a conventional manner; for example by adding an acid. Again the acid used is best selected from acids of which the residues are food grade. For example, HCl may be used. This procedure gives particularly good results with high conversion of the oil into free fatty acids; for example up to about 80%.
Alternatively, the oil may be subjected to steam stripping at temperatures in the range of about 90°C to about 210°C. Such a process may be carried out in a high pressure reactor using direct injection of steam at high pressure. This procedure has the advantage that trace elements are not added to the oil during hydrolysis but the extent of hydrolysis may be lower; for example around 20 to 25%.
Another procedure for hydrolyzing the oil is to react the oil with between 5 to 20% by weight water in a sealed reactor. Reaction temperatures in the range of about 175°C to 260°C may be used. Reaction times of about 30 minutes to 2 hours are suitable. Particularly good results are obtained with about 10 % by weight water reacted at 245°C for 1 hour. Usually the hydrolysis is terminated by allowing the reaction mixture to cool. This procedure also has the advantage that trace elements are not added to the oil. However, the procedure has the further advantage that high levels of free fatty acids are readily obtainable; for example up to 80%.
It will be appreciated that the hydrolyzed fats produced by these processes are unlikely to be completely hydrolyzed in that amounts of mono-, di- and/or triglycerides will be present in the product hydrolyzed oil. If desired these glycerides may be removed by conventional separation techniques but this is not necessary. Therefore it is to be understood that in this specification, the term "hydrolyzed fat" includes a fat which has been partially hydrolyzed and thus contains amounts of mono-, di- and/or triglycerides; for example from about 5%
to about 90% by weight mono-, di- and/or triglycerides. The hydrolyzed oils so produced usually have a melting point above about 30°C and therefore they are solid at room temperature. This has the advantage of better entrapment of the functional substance in the hydrolyzed oil; providing some improvement in functional substance retention during storage.
Once the oil has been hydrolyzed, the functional substance must be incorporated into it to form the preconcentrate. Any desired functional substance may be incorporated. If it is oil soluble or miscible, the functional substance may be simply mixed with the hydrolyzed oil; for example in a ribbon blender.
WO 96/23425 PCT/EP96l00367 Heating of the hydrolyzed oil to its melting point may be required. Or the functional substance may be mixed in a suitable carrier oil and the carrier oil mixed with the hydrolyzed oil. The carrier oil may be of the same source as the hydrolyzed oil, but being unhydrolyzed. Alternatively, for water soluble substances, the function substance may be dissolved in a small amount of water and the water mixed with the hydrolyzed oil as a dispersed phase.
Alternatively, the functional substance may be absorbed into the hydrolyzed oil; this procedure being particularly suitable for gaseous aromas.
Conveniently the functional substance is a flavour or aroma, or a precursor of a flavour or aroma, or mixtures thereof. Any suitable aromas and flavours, be they natural or synthetic, may be used as desired. Examples are fruit flavours and aromas, herb flavours and aromas, meat or animal fat flavours aromas, and the like. Further functional substances such as nutrients; for example vitamins, trace minerals and the like, salts, sugars, preservatives, and the like may also be incorporated.
Then the emulsion preconcentrate is applied to a food product. The food product may be any suitable food product as.desired and the emulsion preconcentrate may be mixed in using any suitable procedure. The emulsion preconcentrates, however, are particularly useful in frozen or chilled convenience foods. For example, the preconcentrates may be added to frozen dinners or may be used in frozen pizzas, frozen sweet and sour dishes, breads, frozen French fries, frozen deserts and pies, and the like. The preconcentrate may be sprayed on the food product, may be mixed in the food product, mixed in.~sauces forming part of the food product, and the like. If the food product does not naturally contain sufficient aqueous phase to form an emulsion, water may be added to the food product. Particularly if the food product is frozen, the small amounts of additional water should not caused any significant problem.
In use, the user merely heats the food product; for example in a microwave oven or a convection oven. Once heated, the hydrolyzed fat in the emulsion preconcentrate melts and spontaneously forms an emulsion with aqueous phase present in the food product; the droplets of the dispersed phase including droplets of size below about 200nm. These very fine droplets are stable but not visible to the eye. The functional ingredient in these droplets is released rapidly because of the very large surface area of the dispersed phase and as the droplets constantly reform. Then, for example, if the functional ingredient is an aroma, the user perceives a burst of aroma.
_7_ -.
That this can be achieved in a microwave oven is particularly surprising.
Usually foods reheated or cooked in a microwave oven are not subjected to high . s. .~ ~;;" :> ..,; ~.. ~ ~.. " ~..: ~~--_"~<. ..
enough temperatures and long enough cooking times for flavours and aroma to develop. Consequently most frozen foods heated in a microwave oven give off no substantial amounts of aromas. However food heated or cooked in a microwave is likely to be heated to a temperature at least above the melting point of the hydrolyzed fat. Hence if the food contains the emulsion preconcentrate, aromas and flavours will be released rapidly in a burst.
To further illustrate the invention, the following examples are given:
Exa a 1 Pressure and Temperatures Hydrolysis of Butter fat and Chicken fat Two reaction mixtures are made up; one of a sample of butter fat (Land O'Lake butter obtained from a local supermarket) and the other of a sample of chicken fat (again obtained from a local supermarket). Water is added to each reaction mixture to make up 90% by weight of the mixture. Each mixture is degassed under vacuum and placed in a Pan bomb and the bomb heated to 246°C
for 60 minutes. Each bomb is placed in an ice bath to terminate hydrolysis.
Each bomb is allowed to depressurize and is opened. Once the oil has solidified, the aqueous phase is discarded. In each case, the hydrolyzed oil has a melting point in the range of 30 to 40°C.
A sample of 20 ~.g of each hydrolyzed oil is dissolved in 20 ~,l of a 2:1 chloroform:hexane mixture and then applied on a HPTLC plate (silica gel 60 F
254 obtained from Merck GmbH, Darmstadt, Germany) using capillaries. The plates are then subjected to HPTLC analysis using the two-stage development technique described in Jork et al; 1989; Dunns hicht-Chromato -~raphie, Band 1 a, Merck, VCH, Weinheim, Germany, pages 327 to 330. The composition of the neutral lipids is then determined by titration or gas chromatography. The free fatty acid content is about 80%. At least 95% by weight of the fatty acids contain 14 or more carbon atoms.
100 ml of water at pH 7 is held at a temperature of about 60°C. 20 mg of the hydrolyzed oil is added to the water. A slightly turbid emulsion spontaneously forms. The emulsion is subjected to droplet size analysis and the mean droplet size is determined to be about 290 nm; including droplets of size less than 200 nm (for example about 50 nm). Small amounts of very fine droplets of oil are detected on the surface of the water. The emulsion is inspected _$_ a week later and is found to be stable. These results indicate the presence of a microemulsion; along with stable droplets having a size outside of the microemulsion range.
le 2 Alkaline Hydrolysis of butter fat and chicken fat The butter fat and chicken fat of example 1 are used. A 600 ml sample of each fat is placed in a reaction vessel in a water bath at 70°C. An aliquot of 200 ml of 2 N KOH is added to each sample and the mixture incubated for 2 hours at 70°C. The reaction is stopped by adding 70 ml of 6N HCI.
Upon addition of the HC1, the mixture separates into an aqueous phase and an oil phase, the latter solidifying with cooling. Upon solidification of the oil phase, the aqueous phase is discarded leaving the hydrolyzed oils. The melting point of each hydrolyzed oil is determined to be in the range of 40 to 55°C. The free fatty acid content of each hydrolyzed oil is determined as described in example 1. The hydrolyzed fats contain about 80 to 85% by weight of free fatty acids. At least 95% by weight of the fatty acids contain 14 or more carbon atoms.
Each hydrolyzed oil is added to hot water as described in example 1 and subjected to droplet size analysis. The emulsion includes droplets of size less than 200 nm. Small amounts of very fine droplets of oil are detected on the surface of the water. The emulsion is inspected a week later and is found to be stable. These results indicate the presence of a microemulsion; along with stable droplets having a size outside of the microemulsion range.
Example Steam Hydrolysis of butter fat and chicken fat 500 g of each of the butter fat and chicken fat of example 1 is loaded into a separate 1.5 litre high pressure bomb (Pressure Products Industries, Inc., Warminster, Pennsylvania, USA). Steam at 2070 kPa (300 psi) is directly injected into each pressure bomb to provide a reaction temperature of 204°C
(400°F). The contents are held at the reaction temperature for about 1 minute.
Then the pressure is released and the hydrolyzed oil removed. The hydrolyzed oil has a melting point of about 40°C and a free fatty acid content of about 25%. , At least 95% by weight of the fatty acids contain 14 or more carbon atoms.
Each hydrolyzed oil is added to hot water as described in example l and subjected to droplet size analysis. The emulsion includes droplets of size less than 200 nm. Small amounts of very fine droplets of oil are detected on the surface of the water. The elrtitlsion is insp~~t~d a Vveek later and is found to be stable. These results indicate the presence of a microemulsion; along with stable droplets having a size outside of the microemulsion range.
Ex~le 4 Hydrolysis of Butter fat and Chicken shortening Crisco Chicken shortening and O'Dells butter fat are obtained commercially and hydrolyzed as described in example 1. Each hydrolyzed oil is added to hot water as described in example 1 and subjected to droplet size analysis. The emulsion includes droplets of size less than 200 nm. Small amounts of very fine droplets of oil are detected on the surface of the water. The emulsion is inspected a week later and is found to be stable. These results indicate the presence of a microemulsion; along with stable droplets having a size outside of the microemulsion range.
A chicken aroma is mixed into the hydrolyzed chicken shortening. The mixture is comminuted and added to a Lean Cuisine sweet and sour frozen chicken dinner. The dinner is placed in a microwave oven and heated as directed on the package. The chicken dinner has a strong chicken aroma.
A garlic aroma/flavour is mixed into the hydrolyzed butter fat. The mixture is comminuted and placed into french bread. Butter is also added. The bread is frozen and then reheated in a microwave oven. The bread has a strong garlic flavour.
E a Frozen Pizza product A frozen Lean Cuisine French bread pizza and a Stouffer French bread pizza is obtained from a local supermarket. A small amount of water is sprayed on each pizza and the pizzas returned to the freezer to freeze the water.
Hydrolyzed chicken fat produced as described in example 1 is heated to above its melting point. A cooked chicken aroma is mixed into the hydrolyzed chicken fat.
The hydrolyzed chicken fat is then sprayed on the pizzas. The pizzas are returned to the freezer. After 1 hour, the pizzas are placed in a microwave oven and heated as conventional. The pizzas have a strong chicken aroma.
For comparison, an untreated frozen pizza is heated in the microwave oven for the same time and under the same conditions. The cooked pizza has little aroma.
In the production of a frozen pizza, the microemulsion preconcentrate may also be sprayed onto the base prior to addition of the topping.
~ m le Frozen Chicken Dinners Several frozen chicken dinners (Stouffer's Lean Cuisine Chicken Fettucini, Glazed Chicken, Chicken in Peanut Sauce, Chicken Chow Mein, Chicken Sweet and Sour, Chicken Marsala, and Teriyaki Chicken) are obtained from a local supermarket. Hydrolyzed chicken fat produced as described in example 1 is heated to above its melting point. Cooked chicken aroma is mixed into the hydrolyzed chicken fat. The hydrolyzed chicken fat is then sprayed on each chicken dinner. The chicken dinner is returned to the freezer. After 1 hour, each chicken dinner is placed in a microwave oven and heated as directed on the package. The chicken aroma from each dinner is then evaluated by a test panel:
Dinner Aroma Intensity Chicken Fettucini ++
Glazed Chicken +
Chicken in Peanut +
Sauce Chicken Chow Mein +++
Chicken Sweet and +++
Sour Chicken Marsala +
Teriyaki Chicken +++
"-" indicates no aroma and "+++" indicates very intense aroma.
For comparison, an untreated Teriyaki Chicken dinner is heated in the microwave oven for the same time and under the same conditions. The cooked chicken dinner has almost no chicken aroma; equivalent to "-".
' In the production of a frozen dinner, the microemulsion preconcentrate may also be dispersed within the sauce.
Embodiments of the invention are now described, by way of example only.
In this specification, an "emulsion preconcentrate" is a lipid medium which, when added to an aqueous medium at a temperature sufficiently high for the lipid medium to be liquid, is capable of self emulsifying to spontaneously form an emulsion; either water-in-oil or oil-in-water, which includes droplets of dispersed phase in the microemulsion range. It is possible that minor amounts of the dispersed phase may, for various reasons, form larger droplets than would fall within the definition of a microemulsion but these droplets are relatively stable;
at least at neutral pH. If the lipid medium is the dispersed phase, it may contain minor amounts of an aqueousphasedi~ersed in it.
The microemulsion preconcentrate is produced by first hydrolyzing a fat.
The source and the exact composition of the fat used is not critical;
primarily the fat will be selected for desired taste characteristics, compatibility, or for stability.
For example, the fat may be a natural oil or fat of vegetable, animal, or marine origin. Specific examples of suitable fats include sunflower oil, soybean oil, maize oil, safflower oil, rapeseed oil, cottonseed oil, peanut oil, olive oil, cocoa butter, butter fat, fish oils, chicken fat, pork fat, tallow, beef fat, shortening, mixtures thereof, and the like. Alternatively the fat may be a fraction obtained from these natural oils and fats by conventional fractionation techniques; or may be a natural or fractionated fat which has been subjected to selected and directed interesterification. Suitable synthetic fats may also be used but they will usually be too expensive.
The oil may be hydrolyzed by any suitable hydrolysis procedure. However the procedure is ideally such that the formation of large amounts of low molcular weight fatty acids (for example fatty acids having 4 carbon atoms) is avoided since these acids can impart rancid flavours. In one suitable procedure, the oil may be subjected to alkaline hydrolysis in a manner similar to conventional saponification processes for fats and oils. The alkaline used in the procedure may be any suitable alkaline but alkaline based upon alkali and alkali earth metal hydroxides are preferred since the residues of these acids are often acceptable in foods. The alkali metal hydroxides NaOH and KOH are particularly preferred.
WO 96!23425 PCT/EP96/00367 The hydrolysis may be terminated in a conventional manner; for example by adding an acid. Again the acid used is best selected from acids of which the residues are food grade. For example, HCl may be used. This procedure gives particularly good results with high conversion of the oil into free fatty acids; for example up to about 80%.
Alternatively, the oil may be subjected to steam stripping at temperatures in the range of about 90°C to about 210°C. Such a process may be carried out in a high pressure reactor using direct injection of steam at high pressure. This procedure has the advantage that trace elements are not added to the oil during hydrolysis but the extent of hydrolysis may be lower; for example around 20 to 25%.
Another procedure for hydrolyzing the oil is to react the oil with between 5 to 20% by weight water in a sealed reactor. Reaction temperatures in the range of about 175°C to 260°C may be used. Reaction times of about 30 minutes to 2 hours are suitable. Particularly good results are obtained with about 10 % by weight water reacted at 245°C for 1 hour. Usually the hydrolysis is terminated by allowing the reaction mixture to cool. This procedure also has the advantage that trace elements are not added to the oil. However, the procedure has the further advantage that high levels of free fatty acids are readily obtainable; for example up to 80%.
It will be appreciated that the hydrolyzed fats produced by these processes are unlikely to be completely hydrolyzed in that amounts of mono-, di- and/or triglycerides will be present in the product hydrolyzed oil. If desired these glycerides may be removed by conventional separation techniques but this is not necessary. Therefore it is to be understood that in this specification, the term "hydrolyzed fat" includes a fat which has been partially hydrolyzed and thus contains amounts of mono-, di- and/or triglycerides; for example from about 5%
to about 90% by weight mono-, di- and/or triglycerides. The hydrolyzed oils so produced usually have a melting point above about 30°C and therefore they are solid at room temperature. This has the advantage of better entrapment of the functional substance in the hydrolyzed oil; providing some improvement in functional substance retention during storage.
Once the oil has been hydrolyzed, the functional substance must be incorporated into it to form the preconcentrate. Any desired functional substance may be incorporated. If it is oil soluble or miscible, the functional substance may be simply mixed with the hydrolyzed oil; for example in a ribbon blender.
WO 96/23425 PCT/EP96l00367 Heating of the hydrolyzed oil to its melting point may be required. Or the functional substance may be mixed in a suitable carrier oil and the carrier oil mixed with the hydrolyzed oil. The carrier oil may be of the same source as the hydrolyzed oil, but being unhydrolyzed. Alternatively, for water soluble substances, the function substance may be dissolved in a small amount of water and the water mixed with the hydrolyzed oil as a dispersed phase.
Alternatively, the functional substance may be absorbed into the hydrolyzed oil; this procedure being particularly suitable for gaseous aromas.
Conveniently the functional substance is a flavour or aroma, or a precursor of a flavour or aroma, or mixtures thereof. Any suitable aromas and flavours, be they natural or synthetic, may be used as desired. Examples are fruit flavours and aromas, herb flavours and aromas, meat or animal fat flavours aromas, and the like. Further functional substances such as nutrients; for example vitamins, trace minerals and the like, salts, sugars, preservatives, and the like may also be incorporated.
Then the emulsion preconcentrate is applied to a food product. The food product may be any suitable food product as.desired and the emulsion preconcentrate may be mixed in using any suitable procedure. The emulsion preconcentrates, however, are particularly useful in frozen or chilled convenience foods. For example, the preconcentrates may be added to frozen dinners or may be used in frozen pizzas, frozen sweet and sour dishes, breads, frozen French fries, frozen deserts and pies, and the like. The preconcentrate may be sprayed on the food product, may be mixed in the food product, mixed in.~sauces forming part of the food product, and the like. If the food product does not naturally contain sufficient aqueous phase to form an emulsion, water may be added to the food product. Particularly if the food product is frozen, the small amounts of additional water should not caused any significant problem.
In use, the user merely heats the food product; for example in a microwave oven or a convection oven. Once heated, the hydrolyzed fat in the emulsion preconcentrate melts and spontaneously forms an emulsion with aqueous phase present in the food product; the droplets of the dispersed phase including droplets of size below about 200nm. These very fine droplets are stable but not visible to the eye. The functional ingredient in these droplets is released rapidly because of the very large surface area of the dispersed phase and as the droplets constantly reform. Then, for example, if the functional ingredient is an aroma, the user perceives a burst of aroma.
_7_ -.
That this can be achieved in a microwave oven is particularly surprising.
Usually foods reheated or cooked in a microwave oven are not subjected to high . s. .~ ~;;" :> ..,; ~.. ~ ~.. " ~..: ~~--_"~<. ..
enough temperatures and long enough cooking times for flavours and aroma to develop. Consequently most frozen foods heated in a microwave oven give off no substantial amounts of aromas. However food heated or cooked in a microwave is likely to be heated to a temperature at least above the melting point of the hydrolyzed fat. Hence if the food contains the emulsion preconcentrate, aromas and flavours will be released rapidly in a burst.
To further illustrate the invention, the following examples are given:
Exa a 1 Pressure and Temperatures Hydrolysis of Butter fat and Chicken fat Two reaction mixtures are made up; one of a sample of butter fat (Land O'Lake butter obtained from a local supermarket) and the other of a sample of chicken fat (again obtained from a local supermarket). Water is added to each reaction mixture to make up 90% by weight of the mixture. Each mixture is degassed under vacuum and placed in a Pan bomb and the bomb heated to 246°C
for 60 minutes. Each bomb is placed in an ice bath to terminate hydrolysis.
Each bomb is allowed to depressurize and is opened. Once the oil has solidified, the aqueous phase is discarded. In each case, the hydrolyzed oil has a melting point in the range of 30 to 40°C.
A sample of 20 ~.g of each hydrolyzed oil is dissolved in 20 ~,l of a 2:1 chloroform:hexane mixture and then applied on a HPTLC plate (silica gel 60 F
254 obtained from Merck GmbH, Darmstadt, Germany) using capillaries. The plates are then subjected to HPTLC analysis using the two-stage development technique described in Jork et al; 1989; Dunns hicht-Chromato -~raphie, Band 1 a, Merck, VCH, Weinheim, Germany, pages 327 to 330. The composition of the neutral lipids is then determined by titration or gas chromatography. The free fatty acid content is about 80%. At least 95% by weight of the fatty acids contain 14 or more carbon atoms.
100 ml of water at pH 7 is held at a temperature of about 60°C. 20 mg of the hydrolyzed oil is added to the water. A slightly turbid emulsion spontaneously forms. The emulsion is subjected to droplet size analysis and the mean droplet size is determined to be about 290 nm; including droplets of size less than 200 nm (for example about 50 nm). Small amounts of very fine droplets of oil are detected on the surface of the water. The emulsion is inspected _$_ a week later and is found to be stable. These results indicate the presence of a microemulsion; along with stable droplets having a size outside of the microemulsion range.
le 2 Alkaline Hydrolysis of butter fat and chicken fat The butter fat and chicken fat of example 1 are used. A 600 ml sample of each fat is placed in a reaction vessel in a water bath at 70°C. An aliquot of 200 ml of 2 N KOH is added to each sample and the mixture incubated for 2 hours at 70°C. The reaction is stopped by adding 70 ml of 6N HCI.
Upon addition of the HC1, the mixture separates into an aqueous phase and an oil phase, the latter solidifying with cooling. Upon solidification of the oil phase, the aqueous phase is discarded leaving the hydrolyzed oils. The melting point of each hydrolyzed oil is determined to be in the range of 40 to 55°C. The free fatty acid content of each hydrolyzed oil is determined as described in example 1. The hydrolyzed fats contain about 80 to 85% by weight of free fatty acids. At least 95% by weight of the fatty acids contain 14 or more carbon atoms.
Each hydrolyzed oil is added to hot water as described in example 1 and subjected to droplet size analysis. The emulsion includes droplets of size less than 200 nm. Small amounts of very fine droplets of oil are detected on the surface of the water. The emulsion is inspected a week later and is found to be stable. These results indicate the presence of a microemulsion; along with stable droplets having a size outside of the microemulsion range.
Example Steam Hydrolysis of butter fat and chicken fat 500 g of each of the butter fat and chicken fat of example 1 is loaded into a separate 1.5 litre high pressure bomb (Pressure Products Industries, Inc., Warminster, Pennsylvania, USA). Steam at 2070 kPa (300 psi) is directly injected into each pressure bomb to provide a reaction temperature of 204°C
(400°F). The contents are held at the reaction temperature for about 1 minute.
Then the pressure is released and the hydrolyzed oil removed. The hydrolyzed oil has a melting point of about 40°C and a free fatty acid content of about 25%. , At least 95% by weight of the fatty acids contain 14 or more carbon atoms.
Each hydrolyzed oil is added to hot water as described in example l and subjected to droplet size analysis. The emulsion includes droplets of size less than 200 nm. Small amounts of very fine droplets of oil are detected on the surface of the water. The elrtitlsion is insp~~t~d a Vveek later and is found to be stable. These results indicate the presence of a microemulsion; along with stable droplets having a size outside of the microemulsion range.
Ex~le 4 Hydrolysis of Butter fat and Chicken shortening Crisco Chicken shortening and O'Dells butter fat are obtained commercially and hydrolyzed as described in example 1. Each hydrolyzed oil is added to hot water as described in example 1 and subjected to droplet size analysis. The emulsion includes droplets of size less than 200 nm. Small amounts of very fine droplets of oil are detected on the surface of the water. The emulsion is inspected a week later and is found to be stable. These results indicate the presence of a microemulsion; along with stable droplets having a size outside of the microemulsion range.
A chicken aroma is mixed into the hydrolyzed chicken shortening. The mixture is comminuted and added to a Lean Cuisine sweet and sour frozen chicken dinner. The dinner is placed in a microwave oven and heated as directed on the package. The chicken dinner has a strong chicken aroma.
A garlic aroma/flavour is mixed into the hydrolyzed butter fat. The mixture is comminuted and placed into french bread. Butter is also added. The bread is frozen and then reheated in a microwave oven. The bread has a strong garlic flavour.
E a Frozen Pizza product A frozen Lean Cuisine French bread pizza and a Stouffer French bread pizza is obtained from a local supermarket. A small amount of water is sprayed on each pizza and the pizzas returned to the freezer to freeze the water.
Hydrolyzed chicken fat produced as described in example 1 is heated to above its melting point. A cooked chicken aroma is mixed into the hydrolyzed chicken fat.
The hydrolyzed chicken fat is then sprayed on the pizzas. The pizzas are returned to the freezer. After 1 hour, the pizzas are placed in a microwave oven and heated as conventional. The pizzas have a strong chicken aroma.
For comparison, an untreated frozen pizza is heated in the microwave oven for the same time and under the same conditions. The cooked pizza has little aroma.
In the production of a frozen pizza, the microemulsion preconcentrate may also be sprayed onto the base prior to addition of the topping.
~ m le Frozen Chicken Dinners Several frozen chicken dinners (Stouffer's Lean Cuisine Chicken Fettucini, Glazed Chicken, Chicken in Peanut Sauce, Chicken Chow Mein, Chicken Sweet and Sour, Chicken Marsala, and Teriyaki Chicken) are obtained from a local supermarket. Hydrolyzed chicken fat produced as described in example 1 is heated to above its melting point. Cooked chicken aroma is mixed into the hydrolyzed chicken fat. The hydrolyzed chicken fat is then sprayed on each chicken dinner. The chicken dinner is returned to the freezer. After 1 hour, each chicken dinner is placed in a microwave oven and heated as directed on the package. The chicken aroma from each dinner is then evaluated by a test panel:
Dinner Aroma Intensity Chicken Fettucini ++
Glazed Chicken +
Chicken in Peanut +
Sauce Chicken Chow Mein +++
Chicken Sweet and +++
Sour Chicken Marsala +
Teriyaki Chicken +++
"-" indicates no aroma and "+++" indicates very intense aroma.
For comparison, an untreated Teriyaki Chicken dinner is heated in the microwave oven for the same time and under the same conditions. The cooked chicken dinner has almost no chicken aroma; equivalent to "-".
' In the production of a frozen dinner, the microemulsion preconcentrate may also be dispersed within the sauce.
Claims (9)
1. An emulsion preconcentrate comprising a hydrolyzed fat which contains at least 10% by weight free fatty acids, and a functional substance captured in the hydrolyzed fat; the emulsion preconcentrate spontaneously forming an emulsion including droplets of dispersed phase of size less than 200 nm upon admixture with water at a temperature higher than the melting point of the hydrolyzed fat.
2. An emulsion preconcentrate according to claim 1 in which the fat which is hydrolyzed is a natural or fractionated natural fat, or such a fat which has been subjected to selected and directed interesterification.
3. An emulsion preconcentrate according to claim 1 in which the hydrolyzed fat contains from about 50% to 90% by weight free fatty acids.
4. An emulsion preconcentrate according to claim 3 in which at least 90% by weight of the free fatty acids contain at least 14 carbon atoms.
5. An emulsion preconcentrate according to any one of claims 1 to 4 in which the hydrolyzed fat has a melting point of about 15 to 40°C.
6. An emulsion preconcentrate according to any one of claims 1 to 4 in which the functional substance comprises from 0.01 % to 2% by weight of the preconcentrate
7. An emulsion preconcentrate according to claim 1 in which the function substance is selected from an aroma, a flavourant, a precursor of an aroma or flavourant, or mixtures thereof.
8. A food product which includes an emulsion preconcentrate comprising a hydrolyzed fat which contains at least 10% by weight free fatty acids, and a functional substance captured in the hydrolyzed fat, the emulsion preconcentrate spontaneously forming an emulsion including droplets of dispersed phase of size less than 200 nm upon admixture with water at a temperature higher than the melting point of the hydrolyzed fat.
9. A food product according to claim 8 in which the emulsion preconcentrate comprises from 0.05 to 2% by weight of the food product.
Applications Claiming Priority (3)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US38232995A | 1995-02-01 | 1995-02-01 | |
| US08/382,329 | 1995-02-01 | ||
| PCT/EP1996/000367 WO1996023425A1 (en) | 1995-02-01 | 1996-01-24 | Food microemulsion formulations |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CA2209765A1 CA2209765A1 (en) | 1996-08-08 |
| CA2209765C true CA2209765C (en) | 2006-04-25 |
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| CA002209765A Expired - Fee Related CA2209765C (en) | 1995-02-01 | 1996-01-24 | Food microemulsion formulations |
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| EP (1) | EP0809446B1 (en) |
| JP (1) | JPH10513051A (en) |
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| AU (1) | AU708234B2 (en) |
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| GR (1) | GR3035508T3 (en) |
| PT (1) | PT809446E (en) |
| WO (1) | WO1996023425A1 (en) |
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| JP3480938B2 (en) * | 1995-02-01 | 2003-12-22 | ソシエテ デ プロデユイ ネツスル ソシエテ アノニム | Encapsulated organoleptic |
| PT809446E (en) * | 1995-02-01 | 2001-04-30 | Nestle Sa | MICROEMULSIONED FOOD FORMULATIONS |
| US6261812B1 (en) | 1997-08-18 | 2001-07-17 | Kao Corporation | Process for producing diglycerides |
| US6025348A (en) * | 1998-04-30 | 2000-02-15 | Kao Corporation | Oil and fat composition containing phytosterol |
| GB9811691D0 (en) * | 1998-06-01 | 1998-07-29 | Kerry Ingredients Uk Limited | Flavour delivery systems |
| NL1010673C2 (en) * | 1998-11-27 | 2000-05-30 | Stork Pmt | Add additive to a meat product. |
| GB9826555D0 (en) * | 1998-12-03 | 1999-01-27 | Univ Nottingham | Microemulsion compositions |
| US6403144B1 (en) | 1999-04-30 | 2002-06-11 | The Procter & Gamble Co. | Food preparation compositions |
| US7214400B1 (en) | 1999-04-30 | 2007-05-08 | Smucker Fruit Processing Company | Flavor enhancing oils |
| US6365211B1 (en) | 1999-06-18 | 2002-04-02 | The Procter & Gamble Co. | Cooking aid with reduced foaming |
| DE60218919T2 (en) * | 2001-03-22 | 2007-12-06 | Firmenich S.A. | Transparent microemulsions with high oil content |
| US6902756B2 (en) | 2001-04-02 | 2005-06-07 | Firmenich Sa | Transparent high oil loaded microemulsions |
| DK2337627T3 (en) * | 2008-09-18 | 2013-09-08 | Univ Eindhoven Tech | PROCEDURE FOR PREPARING MONODISPERGED EMULSIONS |
| US8431178B2 (en) | 2010-09-10 | 2013-04-30 | Pepsico, Inc. | Increasing the concentration of terpene compounds in liquids |
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| US2929716A (en) * | 1957-02-25 | 1960-03-22 | Standard Brands Inc | Instant coffee |
| GB1029552A (en) * | 1962-03-23 | 1966-05-11 | Unilever Ltd | Fatty composition |
| US3917858A (en) * | 1972-12-13 | 1975-11-04 | D E J Int Research | Agglomeration of instant powders |
| CH639246A5 (en) * | 1978-08-07 | 1983-11-15 | Nestle Sa | COFFEE CAPSULES. |
| US4414229A (en) * | 1981-11-23 | 1983-11-08 | Cumberland Packing Corp. | Margarine and the like spread with natural butter flavor |
| US4528201A (en) * | 1983-06-20 | 1985-07-09 | The Procter & Gamble Co. | Alkali-treated lecithin in fats |
| US4544567A (en) * | 1984-01-18 | 1985-10-01 | General Foods Corporation | Simultaneous coffee hydrolysis and oil extraction |
| GB8616041D0 (en) * | 1986-07-01 | 1986-08-06 | Unilever Plc | Phosphatide-containing compositions |
| US4996072A (en) * | 1987-03-02 | 1991-02-26 | General Mills, Inc. | Physical process for the deodorization and/or cholesterol reduction of fats and oils |
| US4835002A (en) * | 1987-07-10 | 1989-05-30 | Wolf Peter A | Microemulsions of oil in water and alcohol |
| US4906490A (en) * | 1987-08-26 | 1990-03-06 | Cumberland Packing Corp. | Method of producing butter flavored granules |
| US5202146A (en) * | 1988-07-07 | 1993-04-13 | The Nutrasweet Company | Flavor delivery system for fat free foods |
| US5045337A (en) * | 1990-04-19 | 1991-09-03 | The Procter & Gamble Company | Food microemulsion |
| US5376397A (en) * | 1993-05-06 | 1994-12-27 | Kraft General Foods, Inc. | Microemulsions of oil and water |
| US5283056A (en) * | 1993-07-01 | 1994-02-01 | International Flavors & Fragrances Inc. | Transparent oil-in-water microemulsion flavor or fragrance concentrate, process for preparing same, mouthwash or perfume composition containing said transparent microemulsion concentrate, and process for preparing same |
| US5496574A (en) * | 1995-02-01 | 1996-03-05 | Nestec S.A. | Encapsulated sensory agents |
| JP3480938B2 (en) * | 1995-02-01 | 2003-12-22 | ソシエテ デ プロデユイ ネツスル ソシエテ アノニム | Encapsulated organoleptic |
| PT809446E (en) * | 1995-02-01 | 2001-04-30 | Nestle Sa | MICROEMULSIONED FOOD FORMULATIONS |
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1996
- 1996-01-24 PT PT96902943T patent/PT809446E/en unknown
- 1996-01-24 AT AT96902943T patent/ATE198023T1/en not_active IP Right Cessation
- 1996-01-24 WO PCT/EP1996/000367 patent/WO1996023425A1/en active IP Right Grant
- 1996-01-24 CA CA002209765A patent/CA2209765C/en not_active Expired - Fee Related
- 1996-01-24 DK DK96902943T patent/DK0809446T3/en active
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- 1996-01-24 EP EP96902943A patent/EP0809446B1/en not_active Expired - Lifetime
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- 1996-01-24 JP JP8523246A patent/JPH10513051A/en not_active Abandoned
- 1996-02-16 US US08/603,002 patent/US5674549A/en not_active Expired - Lifetime
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- 2001-03-05 GR GR20010400348T patent/GR3035508T3/en not_active IP Right Cessation
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| US5674549A (en) | 1997-10-07 |
| EP0809446B1 (en) | 2000-12-13 |
| CA2209765A1 (en) | 1996-08-08 |
| DK0809446T3 (en) | 2001-04-09 |
| ES2153561T3 (en) | 2001-03-01 |
| WO1996023425A1 (en) | 1996-08-08 |
| EP0809446A1 (en) | 1997-12-03 |
| JPH10513051A (en) | 1998-12-15 |
| ATE198023T1 (en) | 2000-12-15 |
| AU4715496A (en) | 1996-08-21 |
| GR3035508T3 (en) | 2001-06-29 |
| PT809446E (en) | 2001-04-30 |
| AU708234B2 (en) | 1999-07-29 |
| DE69611233D1 (en) | 2001-01-18 |
| DE69611233T2 (en) | 2001-04-05 |
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