IE61391B1 - Better tasting low calorie fat materials - Google Patents

Better tasting low calorie fat materials

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Publication number
IE61391B1
IE61391B1 IE53287A IE53287A IE61391B1 IE 61391 B1 IE61391 B1 IE 61391B1 IE 53287 A IE53287 A IE 53287A IE 53287 A IE53287 A IE 53287A IE 61391 B1 IE61391 B1 IE 61391B1
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Ireland
Prior art keywords
fatty acid
sugar
polyesters
viscosity
low calorie
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IE53287A
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IE870532L (en
Inventor
Christian Albert Bernhardt
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Procter & Gamble
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Priority to IE53287A priority Critical patent/IE61391B1/en
Publication of IE870532L publication Critical patent/IE870532L/en
Publication of IE61391B1 publication Critical patent/IE61391B1/en

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  • Edible Oils And Fats (AREA)

Description

Field of the Invention The present invention relates io edible compositions -1containing certain low calorie fat materials and additional ingredients to make the materials better tasting in the mouth.
Background of the Invention.
One of the most common metabolic problems among people today is obesity. This condition is primarily due to ingestion of a greater number of calories then are expended. Fat is the most concentrated form of energy in the diet, .with each gram of fat supplying approximately 9 calories. Overall» fat constitutes about 40% of the total calories in the diet.
Triglycerides constitute about 90% of the total fat consumed in the average diet. One method by which the caloric value of edible fat could be lowered would be to decrease the amount of triglyceride that is absorbed in the human system since the usual edible triglyceride fats are almost completely absorbed (see Lipids, 2, H. J. Deuel, S'nterscience Publishers, inc.» New York 1955, page 215). A low calorie fat offers a convenient and practical method by which obesity can be prevented or overcome.
Low caloric fats which can replace triglycerides are described by Mattson et al. U.S. Patent 3,500,186 to Mattson et al. discloses low calorie, fat-containing, food compositions in which at least a portion ©f the triglyceride content is replaced with a polyol fatty add ester, said polyol fatty aeid ester having at least four fatty acid ester groups with each fatty acid having- from 8 to 22 carbon atoms.
U.S. Patent 4,005,196 to Jandacek et al. discloses the low calorie fat-containing food compositions of the Mattson et : al. patent, in combination with sufficient fat-soluble vitamin selected from the group consisting of vitamin A, vitamin D, vitamin E and vitamin K.
The esters disclosed in the Matteon et al. and Jandacek et al. patents are effective fat substitutes for use in low calorie food products.
The use of esters of this type in edible products 5 is also disclosed in several Journal Articles, viz.
Mattson et al J. Nutrition 109 (1979) 10 pp 1688-1693, Mattson et al J. Nutrition 106 (1976) $ 6 pp 747-752 and Fallat et al Am. J. Clin Nutrition 29 (1976) pp 12041215. The J. Nutrition (109) Article relates to the 1q effect of sucrose polyester on the absorption of dietary cholesterol, the J. Nutrition 106 Article reports a study of the effect of sucrose polyester on. vitamin A metabolism, while the Am. J. Clin Nutrition Article relates to the lowering of blood plasma cholesterol by a dietary agent containing sucrose polyester.
Unfortunately, regular ingestion of moderate to high levels of these esters can produce an undesirable laxative” effect, namely, leakage of the ester through the anal sphincter. One way to prevent this undesirable 2q laxative effect is to formulate the esters so that they are completely solid at body temperature.
Another means of preventing the undesirable laxative effect is through the addition to the ester of anti-anal leakage agents such as those described in U.S. Patent 4,005,,195 to «jandacek. This patent discloses anti-anal leakage ©gents which include solid fatty acids (melting point 37®C or higher) and their triglyceride source, and solid polyol fatty acid polyesters. Specifically, the agents are selected from the group consisting of: edible C,.|9 and higher saturated fatty 0 acids, and their edible salts; edible, digestible sources of and higher saturated fatty acids; edible, nonabsorbable, nondigestible solid polyol fatty acid polyesters having at least 4 fatty acid ester groups, wherein the polyol is selected from the group consisting of sugars and sugar alcohols containing from 4 to 8 hydroxyl groups and wherein each fatty acid group has from about 8 to about 22 carbon atoms; and edible, nondigestible esters of alpha-branched chain C^-C.^ fatty adds.
The completely solid esters referred to above, and solid triglycerides or esters used as anfi-anel leakage agents, have drawbacks when used Sn low calorie food compositions. An ester or triglyceride having a high solids content tastes waxy” in the mouth when ingested. It would be desirable to have a substitute for triglyceride fats that is still effective at reducing calories, but that does not taste waxy in the mouth.
At the same time, it is critical that this fat substitute not produce an undesired laxative effect.
It is therefore an object of the present invention to provide a composition, useful as a fat substitute in foods, which dees not taste waxy in the mouth when ingested.
It is another object of this invention to provide a composition made with low calorie fat materials, so that food products made with the composition are low in calories.
St Is a further object of the present Invention to avoid a laxative side effect without having to add anti-anal leakage agents.
According to one aspect of the present invention there is provided a composition of matter having a Solid Fat Content less than 20% at mouth temperature (33.3°C), comprising; ' (a)an edible, wholly or partially nondigestible low calorie fat material selected from sugar fatty acid Dolyesters, sugar alcohol tatty acid polyesters and mixtures thereof wherein the sugars and sugar alcohols contain from 4 to 8 hydroxyl groups, wherein the sugar fatty acid, polyesters and sugar alcohol fatty acid polyesters have at least 4 fatty acid ester groups, and wherein the fatty acids are mixtures of fatty acids containing from 8 to 22 earbon atoms, wherein th© sugar fatty acid polyesters that are sucrose fatty acid polyesters have an octa ester content of at least 70%, said low calorie fat material having, at 37.8 °C : (i) a viscosity of at least 0.25 Pa.s. at a 800 seconds’1, a viscosity of least 0.4 Pa.s rate of 100 seconds*1, and a viscosity of at Pa.s. at a shear rate of 10 seconds*1; shear rate of at a shear least 2.5 (ii) a yield point of at least 250 Pa (iii) a thixotropic area of at least 0.2x10s Pa. sec'1 and (iv) a liquid/solid stability of at least 50%, defined as » 5 the weight percent of a sample not separating as a liquid after centrifuging at 60,000 RPM for 1 hour at 37.S’C; and (b)an edible, absorbable, digestible food material which acts as a solvent for said fat material.
According to another aspect of the invention there is provided a composition of matter comprising the above defined fat material in combination with a food emulsifier capable of forming an oil-in-water emulsion with the fat material in the mouth, said food emulsifier having an HLB value of at least 2. Ί 5 The compositions of this invention are useful as fat substitutes in low calorie fat-containing food products. The compositions provide a non-waxy taste in the mouth. At the same time, a laxative side effect is avoided without the use of anti-anal leakage agents.
Detailed Description of the Invention This invention relates to non-waxy-tasting compositions useful as fat substitutes for making low calorie food products.
The compositions do not produce an undesirable laxative side effect» Generally speaking, the invention involves the use of certain edible, wholly or partially nondigestible low calorie fat materials that are able to retain their viscosity and stability at relatively low solids content levels. Then, these fat materials are made even more palatable by adding either a food material that lowers the melting point of the composition or a food emulsifier capable of producing an oil-in-water emulsion' with the fat materials. it was discovered that some intermediate melting low calorie fat materials with pseudoplastic flow properties exhibit unique and unexpected, rheology and liquid/solid stability at body temperature. These compositions behave as stable, homogeneous non-Newtonian pseudoplaslic materials at body temperature. For example, specially synthesized sucrose fatty acid polyesters that were 12% solid and 88% liquid at body temperature (98.6°F, 37°C) were very viscous and had excellent liquid/solid stability. This is in contrast to the properties of a mixture containing 88% liquid sucrose polyester and 12% solid sucrose polyester. At body temperature the mixture will, separate into liquid, and solid. portions. Additionally, this mixture has a low viscosity. The specially synthesized sucrose polyesters, on the other hand, exhibit pseudoplastic flow and surprising viscosity and liquid/solid stability at relatively low levels of solids. The low calorie fat materials of this invention are thought to be homogeneous systems. While not intended to be bound by theory, evidence of networking between the solid crystals of the materials has been discovered which may be involved in their surprisingly high liquid/solid stability and viscosity at body temperature.
A benefit of the fat materials' high viscosity and liquid/solid stability is that ingestion of them does not result in an undesirable laxative side effect. Being viscous and stable, the materials pass from the digestive tract through the anal sphincter in much the same manner as normal feces.
Hence, the fat materials of this invention can be safely ingested without adding anti-anal leakage agents.
Another benefit accrues from the fact that the present fat materials are able to retain their high viscosity and stability at relatively low solids content levels. It has been found that they are capable of being ingested without a laxative side effect even at Solids Fat Content levels down to about 5%. When the fat substitute compositions are made with low solids content levels, less solids ar® perceived in the mouth when the compositions are eaten, so foods containing them taste less waxy.
The present invention relates to compositions containing these fat materials, in which additional ingredients are added to make compositions in which the taste of the fat materials is further improved.
A. Description of the Low Calorie Fat Materials By low calorie fat materials is meant edible materials which can replace triglyceride fats or oils in the human diet. These materials provide the benefits of triglyceride fats and oils, i.e., lubricity and flavors.
By wholly nondigestible is meant that substantially all of the materiel is not digested by the body. It passes through the digestive system substantially the same as when it was ingested. Th© - term partially nondigestible means that at least 3 0% of the material is not digested. Preferably at least 70% of the material is not digested.
By liquid/solid stability as used herein is meant that the liquid portion of the material does not readily separate from the solid portion at body temperature, i.e., the material appears to be a solid even though up to about 95% of it is liquid. Liquid/solid stability is measured by centrifuging a sample of the material at 60,,000 rpm for one hour at 100 °F (37.8°C). Liquid/solid stability is defined as: 1001 minus percentage of the material that separated as a liquid after centrifuging.
Th© present invention is concerned with the rheology of the low calorie fat materials at body temperature <93.6°F, 37*0 because they must be stable and viscous at body temperature to eliminate a laxative side effect. However, th® measurements herein were done at 100°F (37.8eC) as a matter of convenience and for easier calibration of instruments, and th® invention is defined in terms of properties at 10O°F (37.8°C). It is understood that measurements done at 100°F (37.8°C) are very close to measurements at body temperature, and they conservatively state the rheological properties at body temperature sine® a lower temperature increases the viscosity.
The fat materials herein exhibit unexpected rheology and liquid/solid stability at body temperature. For example, specially synthesised intermediate melting sucrose fatty acid polyesters which are 12% solid and 83% liquid at body temperature exhibit non-Newtonian pseudoplastic flow properties, are very viscous and have excellent liquid/solid stability. This is in contrast to th® properties of a mixture containing 83% of a liquid sucrose polyester and 12% of a solid sucrose polyester. At body temperature the mixture of 12% solid sucrose polyester and 88% liquid sucrose polyester separates into liquid and solid portions. Additionally, the mixture has a low viscosity. Th® specially synthesized sucrose polyesters, on the other hand, exhibit pseudoplastic flow and surprising viscosity and liquid/solid stability at relatively low levels -of solids.
A benefit of the low calorie fat materials'* high viscosity end Squid/solid stability Ss that ingestion of the materials does not result in an undesirable laxative side effect. Being viscous and stable, the materials pass from the digestive tract through the anal sphincter in much the same manner as normal feces. Bence, th® materials of this invention cun be safely ingested without adding anti-anal leakage agents.
Another benefit accrues from ths fact that the present fat materials ar® able to retain their high viscosity and stability at relatively low solids content levels. When the compositions are ingested,, less solids are perceived in the mouth, so the compositions taste less waxy.
The low calorie fat materials of this invention are thought io be homogenous systems. While not intended to be bound by theory, evidence of networking between the solid crystals and liquid of the materials has been discovered which may be involved in the surprisingly high liquid/solid stability and viscosity of the materials at body temperature.
The present invention, then,, relates to a composition of matter comprising an edible, wholly or partially nondigestible low calorie fat material having physical chemical properties such that it has a non-Newtonian pseudoplastic rheology- at 100°F (37„8®C). in particular, at 1Q0°P (37.8°C) the fat material has: (a) a viscosity of at least 0,.25 Pa.s (2.5 poise) at a shear rate of 800 seconds1, a viscosity of at least 0.4 Pa.s (4.0 poise) at a shear rate of 100 seconds!, and a viscosity of at least 2.5 Pa.s (25.0 poise) at a shear rate of 10 seconds-1; (b) a yield point of at least 250 Pa (2,500 dyn.es/cm-); (c) a thixotropic area of at least 0.20 x 10® Pa.sec-1 (0.20 x 10® dynes/cm^-sec); and (d) a liquid/solid stability of at least 50%.
Viscosity, yield point, and thixotropic area are well known rheological properties, and can be measured by use of an instrument such as a plate and cone viscometer (e.g., a Ferranti-Shirley viscometer, manufactured by Ferranti Electric, Inc., 87 Modular Ave., Commack, NY 11725). The basics of rheology are discussed in Idson, Rheology: Fundamental Concepts,” Cosmetics and Toiletries, Vol. 93, pp. 23-30 (July 1978). Viscosity is a measure of the internal friction resisting the movement of each layer of fluid es it moves past an adjacent layer of fluid. The yield value is ihe amount of shearing stress that must be applied before a material will begin to flow. Idson defines thixotropy as a reversible gel-sol-gel transition caused by ihe building up of a definite structure within the material.
The gelled structure upon shaking or stirring becomes a sol. which when allowed to remain undisturbed, becomes geHed again. ; To measure viscosity, yield point, and thixotropic area of a sample of the fat material of this invention, a plate and cone viscometer as used to record a rheograroa which Is a plot of shear stress versus shear rate. Viscosity and yield point ar© calculated from points on th© rheogrem curve, and the thixotropic area is the area within the curve (also known as the hysteresis loop). Additional details are provided below under the Analytical Methods section.
Preferably, at 100eF (37.8°C) the low calorie fat materials of this invention have a viscosity of at least 5 Pa.s (5 poise) at a shear rate of 800 seconds'*, a viscosity of at least 2.0 Pa.s (20 poise) at a shear rate of 100 seconds-1, and a viscosity of at least 20 Pa.s (200 poise) at a shear rate of 10 seconds-1. Th® preferred yield point of the compositions is at least 500 Pa (5,000 dynes/cm2), the preferred thixotropic area is at least 0.75 x 10^ Pa sec-1 (0.75 χ 10θ dynes/cm2sec). Preferably, the compositions have a liquid/solid stability of at least 90%.
Most preferably, at 100°F (37.8°C) the low calorie fat materials have a viscosity of at least 0.8 Pa.s (8 poise) at a shear rate of 800 seconds1, a viscosity of at least 3.0 Pa.s (30 poise) at a shear rate of 100 seconds-1, and a viscosity of at least 40 Pa.s (400 poise) at a shear rate of 10 seconds-1. The most preferred yield point of the compositions is at least 1500 Pa (15,000 dynes/cm2), and the most preferred thixotropic area is at least 1.00 x 10^ Pa sec-1 (1.00 x 10θ dvnes/cm2-sec).
The preferred upper limit of the viscosity of the fat materials of this invention is 1 x 10^ Pa.s (1 x 10^ poise) at a shear rate of 10 seconds-1, and 100 Pa.s (1,000 poise) at a shear rate of 100 seconds-1. The fat materials must have pseudoplastic flow properties as defined herein. «, ο Iodine Value is a measure of the degree of unsaturation of fatty adds. The low calorie fat materials of this invention preferably have an Iodine Value of from 36 to 55.
The Solid Fat Content value (SFC) provides a reasonable approximation of the percent by weight solids of a particular fatty material at a given temperature. The present low calorie fat material preferably has © Solid Fat Content at 100°F (37.8°C) of at least 5%. Most preferably, the Solid Fat Content at 100°F ¢37.8°C) Is at least 10%.
The low calorie fat material preferably has a complete melting point higher than 98„S°F (37°C).
The low calorie fet materials of the present invention comprise sugar fatty add polyesters, sugar alcohol fatty add polyesters, and mixtures thereof, wherein the sugars and sugar alcohols contain from 4 to 8 hydroxyl groups, wherein the sugar fatty add polyesters and sugar alcohol fatty add polyesters have at least 4 fatty add ester groups and wherein the fatty acids are mixtures of fatty acids containing from 8 to 22 carbon atoms, wherein the sugar fatty add polyesters that are sucrose fatty add polyesters have an octa ester content of at least 70%.
Sugar or sugar alcohol fatty acid polyesters comprise sugars or sugar alcohols, and fatty adds. The term sugar Is used herein in its conventional sense as generic to monoand disaccharides. Th® term sugar alcohol is also used in its conventional sens® as generic to the reduction product of sugars wherein the aldehyde or ketone group has been reduced to an alcohol. The fatty acid ester compounds are prepared by reacting a monosaccharide,,, disaccharide or sugar alcohol with fatty acids as discussed below.
Examples of suitable monosaccharides are those containing 4 hydroxyl groups such as xylose, arabinose, and ribose; the sugar alcohol derived from xylose, i.e.. xylitol, ΐ. i Se also suitable. The monosaccharide erythrose is not suitable for the practice of this invention sine® it only contains 3 hydroxyl groups; however, the sugar elcohol derived from * erythrose, i.e. erythritol, contains 4 hydroxyl groups and is •dthus suitable. Among 5 hydroxyl-containing monosaccharides ' < that are suitable for use herein are glucose, mannose, galactose, fructose, and sorbose. A sugar alcohol derived from fructose, glucose, or sorbose, e.g., sorbitol, contains 6 hydroxyl groups and is also suitable as the alcohol moiety of th© fatty add ester compound. Examples of suitable disaccharides are maltose, lactose, and sucrose, all of which contain <3 hydroxyl groups.
In preparing sugar or sugar alcohol fatty acid polyesters ©f the present invention a sugar or sugar alcohol compound such as those identified above must be esterified with a mixture of fatty acids having from 8 to 22 carbon atoms. Examples of such fatty acids are capryKc, caprie, lauric, myristic, myristoleic, palmitic, palmitoleic, stearic, deic, ridnoleic, linoleic, Unolenic, eleostearic, arachidic, behenic, and erucic. The fatty acids can be derived from suitable naturally occurring or synthetic fatty acids and can be saturated or unsaturated, including positional and geometric isomers. The fat materials of this invention ara mixed esters of fatty adds, rather than esters of a single type of fatty acid.
Fatty acids per s© or naturally occurring fats and oils can serve as th© source for th© fatty acid component in th.® sugar or sugar alcohol fatty acid ester. For example, rapeseed oB, provides a good source for Setty acid.
C,g-Cflg fatty acid can be provided by tallow, soybean cal, or cottonseed ©3. Shorter chain fatty acids can be provided by fo coconut, palm kernel, er babassu ©3s. Corn efil, lard, olive oil, palm ®3, peanut oil, safflower seed ©3, sesame seed oil, and sunflower seed oil, ar® examples of other natural oils which can serve as the source of the fatty acid component.
I 2 The sugar or sugar alcohol fatty acid polyesters suitable for use herein can be .prepared by a variety of methods well known to those skilled in the art. These method include: transesterification of the sugar or sugar alcohol with methyl, ethyl or glycerol fatty acid esters using a variety of catalysts; acylation of the sugar or sugar alcohol with a fatty acid chloride; acylation of the sugar or sugar alcohol with a fatty acid anhydride; and acylation of the sugar or sugar alcohol with a fatty acid, per se. As an example, the preparation of sugar and sugar alcohol fatty add esters is described in U.S. Pat. No. 2,831,854.
A characterizing feature of the sugar or sugar alcohol fatty acid polyesters useful in this invention is that they predominantly contain at least 4 fatty add polyester groups. Sugar or sugar alcohol fatty add polyester compounds that contain 3 or less fatty acid ester groups are 'digested in the intestinal tract much in the manner as ordinary triglyceride fats, but sugar or sugar alcohol fatty add polyester compounds that contain four or more fatty acid ester groups are digested to a lesser extent and thus have the desired low calorie properties for use in this invention.
Highly preferred low calorie fat materials according to this' invention are sucrose fatty add polyesters. Preferred sucrose fatty acid polyesters have the majority of their hydroxyl groups esterified with fatty acids. Preferably at least 80%, and most preferably at least 95%, of the . sucrose fatty acid polyesters are octaesters, heptaesters or hexaesters, and mixtures thereof. Preferably, no more than 35% of the esters ar© hexaesters or heptaesters, but at least 60% of th© sucrose fatty add polyesters are octaesters. More preferably, at least -70% of the polyesters are octaesters.
In order to provide the required physical properties, the sucrose fatty acid polyesters of this invention are preferably esterified with particular kinds of fatty acids. Preferably, at 3 least 80%, and most preferably at least 90%, of the fatty acids ar® mixtures of palmitic, stearic, oleic, linoleic, and behenic acids.
More specifically, the foil owing is a preferred fatty acid composition: from 9¾ to 12% palmitic; from % to 33% stearic; from 19% to 43% oleic; from 2% to 17% linoleic; from 0% to 2% linolenic; from 0% to 2% arachidic; from 0% to 10% behenic; and from 0% to 2% erucic.
The following fatty .acid composition is most preferred: from 9% to 12% palmitic; from 42% to 53% stearic; from 19% to 39% oleic; from 2% to 17% linoleic; from 0% to 2% linolenic; from 0% to 2% arachidic; from 0% to 10% behenic; and from 0% to 2% erucic.
B. Methods for Making the Fat Materials Better Tasting While the fat materials of this invention offer an improvement in non-waxy taste when used alone in a food., product, this invention relates to methods for making the fat materials even better-tasting than they are alone.
One method involves the use of an edible, absorbable, digestible food material which acts as a solvent for the fat material. It was discovered that by the addition of a food material such as a liquid triglyceride to the fat materials, the melting point of the materials is lowered, so that at mouth temperature (92°F, 33.3°G) the fat materials have a Solid Fat Content less than 20%. Hence, when the fat materials are ingested they do not taste waxy in the mouth. After being ingested, the food material that acts as a solvent is digested in the stomach and intestines, and the melting point reduction effect is thereby eliminated. The fat materials revert to their original solids content in the gastrointestinal tract. When the fat materials pass from the colon, then, they are viscous and stable enough to not cause a laxative side effect. ϊ 4 Therefore, one aspect of the present invention is a composition of matter having a Solid Fat Content less than 20% at mouth temperature (33.3°Cf 92°F), comprising: (a) an edible, wholly or partially nondigestible low 5 calorie fat material selected from sugar fatty acid polyesters, sugar alcohol fatty acid polyesters and mixtures thereof wherein the sugars and sugar alcohols contain from 4 to 8 hydroxyl groups, wherein the sugar fatty acid polyesters and sugar alcohol fatty acid 1q polyesters have at least 4 fatty acid ester groups, and wherein the fatty acids are mixtures of fatty acids containing from 8 to 22 carbon stems, wherein the sugar fatty acid polyesters that are sucrose fatty acid polyesters have an octa ester content of at least 70%, -j 5 said low calorie fat material having, at 37,8C (100°F): (i) a viscosity of at least 0.25 Pa.s (2.5 poise) at a shear rate of 800 seconds”^, a viscosity of least 0.4 Pa.s (4 poise) at a shear rate of 100 seconds-*, and a viscosity of at least 2.5 Pa.s (25 poise) at a shear rate 2θ of 10 seconds-*,· (ii) a yield point of at least 250 Pa (2500 dynes/cm ) (iii) a thixotropic area of at least 0.2x10s Ps-sec’ (0.2.10^ dynes/cm^-sec) and (iv)a liquid/solld stability of at least 50%, defined as the weight percent of a sample not separating as a liquid after centrifuging at 50,000 RPM for 1 hour at 37.8°c (100°F) and (b)an edible, absorbable, digestible food material which acts as a solvent for said fat material. ϊ 5 For very good non-waxy taste in th® mouth, it is preferable that the composition have a Solid Fat Content less than 10% at mouth temperature (92°F, 33.39C), and most preferably less than 5%.
'The edible, absorbable, digestible food material which acts as a solvent for the fat material Ss preferably selected frcm the group consisting of triglycerides, monoglycerides, diglycerides, substituted mono- and diglycerides, pedyglycerol esters, citrus oils, flavorants, edible alcohols, edible food emulsifiers, and mixtures thereof. Most preferably, the food material is selected from the group consisting of triglycerides and substituted mono- and diglycerides, and mixtures thereof. By substituted mono- and diglycerides is meant. mono- and diglycerides in which the free hydroxyl groups are substituted with edible short chain fatty acids, i.e., C9 through Cg.
Edible food emulsifiers include mono- and diglycerides, lower sucrose esters (C,- C,)( and lower polyglycerol esters «γο,).
Th© digestible food material must be capable of lowering the melting point (freezing point) of th© fat materials. Freezing point depression generally follows the formula: 1/T - I/T - CR ln xZdelta where T - freezing point, T = © ii. © pure freezing point, X = mol© fraction, and delta Hf - heat of fusion.
Th© amount and type of digestible food material used as & solvent will depend on the end food product in which the composition of this invention wil be used. For example, a preferred food material for this purpose is triglycerides. In a margarine product what is desired is a low Solid Fat Content and a fairly Sow viscosity. There is an optimum viscosity -so that the margarine is thin enough so that the saliva in the mouth can act on St and make it invert. If th® margarine is too thin, it will disperse in the mouth before the ϊ 6 saliva is able to act on it» As another example, shortening must have substantial · plasticity because of its use an the areas of frying and baking. Yet, the shortening should not be so firm as to taste very firm in the mouth. In summary, a specific triglyceride or other food material is picked depending on the food product in which it will be used.
It has been discovered that particular ratios of triglyceride and fat substitute (in particular sucrose polyesters) are desirable in terms of calorie reduction. To maximize the calorie reduction benefit, from 67% to 90% . of the sucrose polyester is combined with from 33% to 10¾ triglyceride. To obtain the minimum reduced calorie benefit that is allowed' by current Government regulations, from 33% to 90% sucrose polyester is combined with from 66% to 10% triglyceride.
The other method of this invention, for making the low calorie fat materials even more palatable, comprises adding to the fat materials an edible, digestible food emulsifier capable of forming an ©fi-in-water emulsion with the fat materials in the mouth. Saliva from the mouth and any water in the food comprises the water portion of the emulsion, while the present fat material and any oil from the food comprises the oil part. When the fat saaterial is made into sn ofl-in-watar emulsion with saliva, ft does not taste waxy in the mouth. After ingestion, the food emulsifier is digested while the fat material remains undigested, so the fat material reverts to its original form. A good-tasting food product can b® made that does not produce a laxative side effect.
Tendency of an emulsifier to form an oft-in-water emulsion is measured by its hydrophilic /lipophilic balance (HLB). The emulsifier used in the composition of this invention must have an ELB value of at least 2.
Preferred food emilsifiers for us® herein ar® selected from the group consisting of mono- and diglycerides, lower sucrose esters, lower polyglyeerol esters, and mixtures thereof. ί ? The compositions of the present invention can be used es a partial er total replacement for normal triglyceride fat in any fat-containing food composition to provide low calorie * benefits. In order to obtain a significant low calorie effect, St is necessary that at least 10% of the fat in the food < composition comprises the present compositions. On the other hand, very low calorie and thus highly desirable food compositions of the invention are obtained when the fat comprises up to 100% of the compositions of this invention. Hence, the compositions of the present invention can be used as a partial or complete replacement for normal triglyceride fat in a salad ©r cooking oil. or a plastic shortening, or the like. Th® compositions can also be used as a partial or complete replacement for' normal triglyceride fat in fat-containing food products such ss mayonnaise, margarine, and dairy products. 8 Analytical Methods I. Rheology Measurements A. Sample Preparation The low calorie fat material ie melted in a microwave oven at from 150°F <®S°C> to 170°F <77*0. This takes approximately 2 minutes. The melted fat material is held at 100°F ± S°F (37.8°C ± 3°C), and a 3 gram sample is weighed into a Solo plastic souffle cup. The sample is then allowed to recrystallize at 100°F ± 5°F ¢37.8°C ± 3°C) for 24 hours. After the 24 hour time period has elapsed, the sample is taken to th® viscometer in an insulated cup and the viscosity as measured.
B. Ferranti-Shirley Viscometer Operation Procedure A Ferranti-Shirley viscometer is used for the viscosity, yield point, and thixotrooic area measurements. A cone is / put into place, and the viscometer temperature is adjusted to 100°? ¢37.8°C). The chart recorder is calibrated, and the gap between the cone and plate is set. The cone speed is checked, and the cone and plate temperatures are equilibrated •20 to 100°F ¢37.8°C). The panel controls are set. Sufficient sample is placed between the plate and the cone so that the gap is completely filled. The temperature is allowed to stabilize at 100°F <37„8®C> for 30 seconds, end then the cone rotation end recording ere started. A rheogram for the fat material is recorded and analyzed to determine the viscosity, yield point, and thixotropic area. Viscosity is -1 -I measured at shear rates of 800 seconds , ISO seconds „ and seconds™^. Π. Liquid/Sond Stability Measurement Th© sample is heated until at completely melts and is thoroughly mixed. Th® sample is then poured into centrifuge tubes at 100°F ± 5°F (37.8°C ± 3°C). The samples then are allowed to recrystallise for 24 hours at 100°F ± 5°F (3/8°C ± 3°C). The samples are then centrifuged at 60,000 rpm for one hour at 37°C. The percent liquid separated is then measured by comparing the relative heights of the liquid and solid phases. ί 9 Π ϊ. Solid Fat Content Measurement Before determining SFC values, the fat material sample is heated to a temperature of 158°F (70°C) or higher for at least 0.5 hours or until the sample is completely melted. The melted sample is then tempered st a temperature of 40°F (4.4°C) for at least 72 hours. After tempering, the SFC value of the fat material at a temperature of 100°F (37.8°C) is determined by pulsed nuclear magnetic resonance (PNMB). The method for determining SFC values of a fat by PNMR is described in Madison and Hill, J. Amer, Oil. Chem. Soc..
Vol. 55 <1978), pp. 328-31.
The foil owing Example is intended to be further illustrative θ Example 1 15 Methyl esters of a fully hydrogenated soy oil and a touch-hardened soy oil, blended in a 55/45 ratio (IS kg), and 2 kg. of an 15 wt. percent solution of potassium hydroxide ih methanol are mixed in a stainless steel batch reactor. This mixture is then heated to 86°F (30°C) with agitation for 1 to 2 hours at atmospheric pressure. During this time, a portion of the methyl esters are saponified. A vacuum is then pulled on the system to remove the last traces of methanol.
Powdered sucrose (3 kg.) is added to th® soap/esier mixture to give a 5:1 molar ratio of ester to sucrose.
Potassium carbonate is then added to th® mixture (approx. 0.5 wt. percent of th® reaction mix) to catalyze th® transesterification. This mixture is agitated and heated under vacuum at about 275°F (135°C) for up to 2-1/2 hours to form the mono-, di- and trisucrose esters. Small quantities of tetra- and pentaesters are also formed during this stage. Additional methyl ester ¢19.5 kg) which has been preheated to 275°F (135®C) is added to bring and maintain the molar ratio of the esters to sucrose to 12:1. When the reaction conditions stabilize at 275°F (135eC), a nitrogen sparge is used to improve agitation and promote methanol stripping. As the reaction occurs, the reaction mixture becomes viscous end then thins out. This second reaction stage lasts approximately 4 to 8 hours. 0 After the reaction mixture has become thin,, it is socled to between. 149*»F <65°C) and 185°F (85®C). The crude reaction mixture is agitated with a dilute solution of methanol, sodium chloride and water. The volume of this wash solution is equal t© 20% to 40% of the reaction mixture volume. The mixed phases are then allowed to settle for approximately 30 to 60 minutes. Th® lower settled phase which contains the soaps, excess sugars and methanol is drawn ©iff and discarded. The upper settled phase which comprises the refined sucrose polyesters is washed again. Usually 2 to 4 wash-es ar® used.
The sucrose polyesters are then washed with a 1% glacial acetic acid in water solution at 10% to 20% of the volume of the reaction mix. This is followed by water wash ©f the same volume.
The reaction mix is then dried to remove moisture at 176°F <80®C) under 10 no Hg or less vacuum for 30 to 60 minutes. Filtrol 105 ¢0.5 wt. percent), and a filter aid (0.5 wt. percent) are added and the mix is agitated at 157®F (75°C) to 185°F (85®C). The slurry is separated by filtration or other means until there is less than 0.1 wt. percent fines. The Squid is then passed through a 1 micromillimeter filter.
The refined and bleached reaction mix is put into a stainless steel batch reactor to distill off the bulk of the methyl esters. Th© distillation takes place at 374®F to 482®F (259°C) under approximately 5 ona Hg of vacuum. This step is complete when it is visually evident that th® distillation has slowed down.
The sucrose polyester is then deodorized in a stainless steel batch deodoriser ©r ©ther suitable device at 374®T (ISO^C) to 482°F <25βθΟ> under a vacuum of aboui 5 eh» Hg with steam sparging. Deodorization is continued until th© methyl ester eontent is below 200 ppm. The deodorizer content® are then cooled while using inert gas sparging. After cooling to 149®F (65®C), ih© deodorizer is brought to 1 atmospheric pressure. The sucrose polyester is stored in clean stainless steel drums.
This produces a sucrose polyester product having the v fatty add composition specified in Table !. Rheology and effectiveness at preventing laxative side effect are fisted in ' < Table ΪΙ.
•The results shown in Tables I and ΪΪ illustrate that sucrose polyesters prepared according to Example. 1 have the properties of the low calorie fat materials of the present invention. The second column in Table I shows the properties of a Mquid sucrose polyester prepared according to a method known to the fart,» and not falling within the present invention,.
Table Π compares the rheology and effectiveness at preventing laxative side effect of the · two samples.
Example 1 has rheological properties according to this invention; the liquid sucrose polyester does not. The liquid sucrose polyester results in a 15% oil loss when ingested. By contrast, the sucrose polyesters prepared in Example 1 result in 0% oil loss, showing that they are very effective at eliminating laxative side effect.
When the sucrose polyesters of Example 1 are mixed with triglyceride in a ratio of 75% sucrose polyester and 25% triglyceride, a composition is made that tastes very good when ingested and that does not cause a laxative side effect.
Fatty Acid Composition C pi® £18 «18 pis Λ Λ ι (¾ £t ’able ΐ Sucrose Polyester Composition Ss di Q 50.8 20.4 14.8 9.3 ιπ> .O 1.4 liquid Sucres Polyester e σ aj? o 0 45.6 31.7 0.4 '22 0.0 w *·« ii-¥ . 47.6 62.S Ester Distribution Λ ;§ % Octa 79.0 71.1 Hepta, I Q 9 A ¢/ to Vj 24.0 Hexa 1.8 4.9 Penta 0.1 0.1 0.1 0.1 SFC ProfU® •5 % 50 *F. 64.3 0 70 p. 53.6 0 80F. 43.0 e 09 T? 21 0 vj eH iib m 105*F. 2.7 o 98.6’F. 11.9 0 DSC Behavior *C. ®c.
Melt Point Maximum !K -20.0 Melt Point Heat of iPj)(3l ii! u, -35.0 Fusion 11 A A 11 1Θ.6 Cal./g Cal./g TABLE II Comparison of Physical Properties of the Sucrose Polyesters with Effectiveness Against Laxative Side Effect LSE Effectiveness Oil Loss C%3 Rheology SO (sec.’b Viscosity (poise) / (Pa.s) 100 (sec.
Yield Point Thixotropic (dynes/cm )/ Area Pa .. —;—2 S (sec. S Liq/Solld Stability (100%-% (dynes/cnri-see . 3 / Pa. sec EFFECTIVE: Example 1 INEFFECTIVE: 0 10.3/ 1.03 48.6/ 4.86 4627 46.2 17,406/ 1749.6 1.858 χ 108/ 1 .658.105 100 Liquid Sucrose 15 2.1/ 2.1/ 2/ None None »NA' Polyester 0.21 0.21 0.2 CXAJJSS

Claims (6)

1. A composition of matter having a Solid Fat Content less than 20% at mouth temperature (33.3°C, 92°F), comprising: (a)an edible, wholly or partially nondigestible low 5 calorie fat material selected from sugar fatty acid polyesters, sugar alcohol fatty acid polyesters and mixtures thereof wherein the sugars and sugar alcohols contain from 4 to 8 hydroxyl groups, wherein the sugar fatty acid polyesters and sugar alcohol fatty acid 10 polyesters have at least 4 fatty acid ester groups, and wherein the fatty acids are mixtures of fatty acids containing from 8 to 22 carbon storas, wherein the sugar fatty acid polyesters that are sucrose fatty acid polyesters have an octa ester content of at least 70%, 15 said low calorie fat material having, at 37.8 °C (100°F): (i) a viscosity of at least 0.25 Pa.s (2.5 poise) at a shear rate of 800 seconds -1 , a viscosity of least 0.4 Pa.s (4 poise) at a shear rate of 100 seconds -1 , and a viscosity of at least 2.5 Pa.s (25 poise) at a shear rate 2. Q of 10 seconds -1 ; (ii) a yield point of at least 250 Pa (2500 dynes/cm 2 ) (iii) a thixotropic area of at least .0.2x10 s “1 6 2 Pa.sec (0.2.10 dynes/cm -sec) and (iv>a liquid/solid stability of at least 50%, defined as 25 the weight percent of a sample not separating as a liquid after centrifuging at 60,000 RPH for 1 hour at 37.8 P C(100 0 F) and (b)an edible, absorbable, digestible food material which acts as a solvent for said fat material.
2. A composition according to claim l wherein th® digestible food material is a member selected from triglycerides, monoglycerides, diglvcerides, substituted mono- and diglycerides, polyglyeerol esters, citrus oils, 5 flavorants, edible alcohols, edible food emulsifiers, and mixtures thereof. 6
3. A composition according to Claim 2 wherein the low calorie fat material is a sucrose fatty acid polyester and the digestible food material is a triglyceride, and 10 wherein the composition comprises from 33% to 90% sucrose fatty acid polyester and from 10% to 66% triglyceride.
4. A composition according to claim 3 wherein the composition comprises from 67% to 90% sucrose fatty acid 15 polyester and from 10% to 33% triglyceride.
5. A composition of matter comprising ; (a) an edible, wholly or partially nondigestible low calorie fat material selected from sugar fatty acid polyesters, sugar alcohol fatty acid polyesters and 20 mixtures thereof wherein the sugars and sugar alcohols contain from 4 to 8 hydroxyl groups, wherein the sugar fatty acid polyesters and sugar alcohol fatty acid polyesters have at least 4 fatty acid ester groups, .wherein the fatty acids are mixtures of fatty acids 25 containing from 8 to 22 carbon atoms, wherein the sugar fatty acid polyesters that are sucrose fatty acid polyesters have an octa ester content of at least 70% by weight, said low calorie fat material having, at 37.8°C (100°F): (i) a viscosity of at least 0.25 Pa.s (2.5 poise) at a 3 q shear rate of 800 seconds -1 , a viscosity of least 0.40 Pa.s (4 poise) at 100 seconds -1 , and a viscosity of at least 2.5 Pa.s (25 poise) at 10 seconds -1 ; (il)a yield point of at least 250 Pa (2500 dynes/cm^); 2G 10 6 (iii) a thixotropic area of at least 0.20 x 10$ Pa sec (0-2.10° dynes (cm^-sec); (iv) a liquid/solid stability of at least 50% defined as the weight percent of a sample not separating as a liquid after centrifuging at 60,000 RPM for 1 hour at 37.8 °c (100°F); and (to) a food emulsifier capable of forming an oil-in-water emulsion with the low calorie fat material in the mouth wherein the emulsifier has an HLS value of at least 2. . A composition according to.Claim 4 wherein the food emulsifier is selected from mono- and diglycerides, lower sucrose esters, lower polyglycerol esters, and mixtures thereof. > A low calorie fat composition according to any one of Claims 1-5 wherein at least 80%, preferable at least 90% by weight of the mixture of fatty acids comprises a mixture of palmitic, stearic, oleic, linoleic and behenic acids! A low calorie fat composition according to Claim 6 wherein the mixture of fatty acids comprises from 9% to 12% palmitic acid, from 35% to 53% stearic acid, from 19% to 43% oleic acid, from 2% to 17% linoleic acid, from 0% to 2% linolenic acid, from 0% to 2% arachidic acid, from 0% to 10% behenic acid and from 0% to 2% erucic acid.
6. 9. A composition according to Claim 1, substantially as hereinbefore described and exemplified.
IE53287A 1987-03-02 1987-03-02 Better tasting low calorie fat materials IE61391B1 (en)

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