CA2052045A1 - Low fat mayonnaise product and method for making the same - Google Patents

Abstract

ABSTRACT

A low fat mayonnaise product which has an edible oil content of less than 10% by weight, which further comprises water, egg white, microcrystalline cellulose and polydextrose, and a process for producing the product.

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Description

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A LOW FAT MAYONNAISE PRODUCT
AND METHOD FOR MAKING THE SAME

This application is a continuation-in-part of Application Serial No. 07/587,887 filed September 25, 1990 BACKGROUND OF THE INVENTION

Mayonnaise i9 a thick, emulsified, non-pourable food dressing generally prepared from vegetable oil, water, egg yolk-containing materials and acidifying ingredients. The United States Food and Drug Administration (USFDA~ regulations set forth the standards which a mayonnaise produc~ must meet, including a requirement of at least 65% by weight vegetable oil.
However, over the past few years, numerous products have come out on the market expanding the SCOp2 of products recognized by the general public as mayonnaise products. Such products include mayonnaise products designated as cholesterol-free and low calorie or light mayonnaise and ~alad dressings. These mayonnaise products contain levels of oil and eg~

yolk-containing materials which do not meet the current Standard of Identity for mayonnaise as promulgat~d by the USFDA. These products may also contain additional ingredients, such as cooked starch paste as a thickening agent, which are not currently recognized as standard ingredients for mayonnaise. In this application, the term "mayonnaise product" is not meant to be limited to those products which meet ~he current USFDA S~andard of Identity, but is meant to encompass all spoonable dressing products which are recognized by the general public as mayonnaise or spoonable salad dressing products.

In today's health con~cious environment, there is a need for low or no fat mayonnaise products. A problem to overcome in order to produce no fat mayonnaice products is the removal of the vegetable oil ~rom the pxoducts, while maintaining similar product taste and texture. As the oil is present in levels o~ at least 65~ by weight in conventlonal mayonnaise products and about 30 to 60% by weight in light or low calorie products, substantial reformulation is necessary in order to produce a mayonna~se product with less than 5~ by weight vegetable oil.

DESCRIPTION OF RELATED ART

U.S. Patent Mo. 2,944,906 to Spitzer discloses and claims a mayonnaise-like food product with a relatively low caloric content~ The mayonnaise-like product ha~ wa~er as its ~32 ~ 1 ~

principle component, and includes from 5.0 to 30.0~ by weight edible oil, and a combination of a stiff and a soft gum to produce a product with the desired texture. Additionally, Spitzer requires the use of an egg yolk containing material as an emulsifying agent. The process disclosed in Spitzer for the production of the food product is a hot mix process to form a gel, which is then broken down into an oil in water emulsion of fine particle size.

U.S. Patent No. 3,023,104 to Battista discloses and claims reduced calorie food compositions, including a mayonnaise type salad dressing~ The food compositions comprise a food material, and, as a non-nutritive agent, cellulose crystallite aggregates, which are a product of acid hydrolysis of cellulose.
The cellulose crystallite aggregates are bland in taste and odor, have a smooth mouth feel, and have a physical appearance resembling starch. They are particularly well suited as a substitute for staxch in baked products.

Rispoli et al., in U.S. Patent No. 4,308,294 disclose and claim an oil-free, oil-replacement composition which has an oily mouth feel, texture and lubricity, and which may be used to form a salad dressing product. The composition is formed by hydra~ing and whipping a protein and cellulose gum to form a protein phase; hydrating an acid stable modified starch and an acid to form an acid phase; subjecting the acid phase to heat to 2~2~

swell the starch; and mixing the protein phase and the acid phase.

In U.S. Patent No. 4,923,707 to Schoenberg, a method is a taught for producing a low oil mayonnaise product. The claimed process, and the product therefrom, contains an edible oil at a level of from 65% to 72% by weight, and includes a low D.E. corn syrup at a level of from 4 to 15% by weight. The product further contains water at a level of from 5 to 15% and egg yolk as the emulsifier in an amount of from 4 to 8% by weight. The mayonnaise is prepared by adding water and the egg yolk to the low D.E. corn syrup to form a premix, combining the premix with the oil and an adible acid to form a mayonnaise product, and processing the mayonnaise product under conditions of high shear.

It has now been found that an acceptable low fat mayonnaise product can be made containing less than 5% by weight edible oil.

SUMMARY OF THE INVENTION

The present invention relates to a low fat mayonnaise product which contains less than 10% by weight edible oil, and a process for making the product. ~he product comprises water, egg whites, microcrystalline cellulose and polydextrose which, when properly combined, cxeate a product which has the ~3 organoleptic and rheological attributes comparable to a conventional mayonnaise product. A no fat mayonnaise product i5 also taught which comprises the same ingredients as the low fat mayonnaise, but with no edible oil.

A process for the production of the mayonnaise products is also disclosed herein. Four premixes are prepared separately; one is a blend of dry ingredients and water, the second is the combination of microcrystalline cellulose and water, the third is a combination of gumsl preferably xanthsn gum, and water, and the fourth is a combination of water, egg white, whey protein concentrate, if present, and any added flavors or colors. The four premixes and any additional ingredients are mixed together to form a slurry, which is then subjected to a continuous cooking and cooling system. The cooked and cooled product is pumped through a milling device ~ust prior to being sent through the ~illing apparatus for packaging.

DETAILED DESCRIPTION

A low fat mayonnaise product is taught which comprises edible oil in an amount of less than 10% by weight. An alternate embodiment of this invention is a no ~at mayonnaise product which does not include any edible oil. As previously stated in this application, the term "mayonnaise product" is being used herein to define a product which has the look and ~2~

feel of a mayonnaise or spoonable salad dressing product to the general public, but which does not necessarily meet the current Standard of Identity of a mayonnaise or salad dressing product as promulgated by the USFDA.

The low fat mayonnalse product of the present invention uses a combination of a number of ingredients to replace the oil which is not present in the product. The main component of the low fat mayonnaise product is water, which is present in levels of from about 40 to about 90% by weight of the product, preferably from about 51 to about 85% by weight, with an optimal range o~ from about 60 to about 78% by weight.

In addition to the water, proteins, such as egg whites and whey protein concentrate, are present in the low fat mayonnaise product. The level of the protein must be carefully balanced in order to produce a product with an acceptable texture and flavor. Where both egg whites and whey protein concentrate are present, the egg whites should be present in an amount of from about 1.0 to about ~0% by weight of the~product~
preferably about l.0 to about 10% by weight, and the whey protein concentrate should be present in an amount of up to about 10% by weight of the final product. The preferred level of protein, i.e. the total amount of egg whites and whey protein concentrate, is at a level of from about l to about 12% by weight of the final product.

The use of proteins outside the ranges designated herein results in an unacceptable product. If the level of protein is too high, the resulting product becomes too stiff and rubbery or too thick.

Another important aspect of the low fat mayonnaise product is the inclu~ion of microcrystalline cellulose to control the consistency. The microcrystalline cellulose should be present in levels of from about 0.25 to about 5% of the product. At these levels, the microcrystalline cellulose imparts a thixotropic consistency and spreadability without any added gumminess, which is usually associated with the use of microcrystalline cellulose at higher levels.

It is common in commercial source~ of microcrystalline cellulose, for a hydrocolloid such as sodium carboxymethyl cellulose or protective colloids such as gum to be present. The hydrocolloid is necessary to prevent aggregation or flocculation of the colloidal microcrystalline cellulose particles, and may therefore be present in the mayonnaise product.

To provide a low fat mayonnaise product with acceptable body, polydextrose is a recommended ingredlent. In addition to the polydextrose, maltodextrin and a modified food starch may be included to result in a high quallty, low fat mayonnaise product.

~ u3~ ~ d The optimal balance of the polydextrose, maltodextrin and modified food starch is important for providing a creamy, smooth body and lubricity which is associated with a conventional mayonnaise product. An improper balance of these three ingredients can result in a product which exhibits a pudding-like texture and is a cuttable instead of a spaonable mixture. If the modified food starch or the maltodextrin are used at levels which are too high, the resulting product will be too pasty and grainy. Too much polydextrose results in products with increased browning and the potential for off-flavor development.

If present, the polydextrose should be in an amount of from 1.0 to about 15% by weight, preferably at a level of from about 3.0 to about 8.0~ by weight. The use o~ maltodextrin in the product has the added benefit of decreasing the brqakdown rate o~ the product in the mouth, which is typical in a true mayonnaise product. The maltodextxin should be a low D.E., such as 10 D.E., and should be present in a level of from about 0.5 to about 7.5% by weight, preferably about 2.0 to about 5.0%.
The D.E. designation is the amount of reducing sugar p~esent on a dry basis, when calculated as dextrose. The modified food starch should be present at a level of from about 2.0 to about 10% by weight, preferably about 4.0 to about 6.0~ by weight.

Additional components which may be added are an edible oil and an acidifying agent. In the low fat mayonnaise product, ~J~ 2 edible oil may be added at levels of up to about 10% by weight, preferably not more than about 2% by weight. Obviously, if a no fat mayonnaise product is desired, no edible oil will be added.
The oils which can be added are those generally used in mayonnaise products, typically vegetable oils such as corn oil, soybean oil, sunflower oil and cottonseed oil. The acldifying agent can be any edible acid, such as citric acid, acetic acid or mixtures thereof~ Generally, the acidifying agent is acetic acid which is present in the form of vinegar, or citric acid in the form of lemon or lime juices.

Further optional ingredients may be included, such as gums, flavors, color~ and preservatives. Ingredients which are generally included in c~nventional mayonnaise formulas, such as salt, sugar and additional flavorings and 3pices and preservatives are also added to the low ~at and no fat mayonnaise products.

A low fat salad dressing type product could also be produced using the basic teaching of thls invention. In order to result in what would be known to the general public as a low fat spoonable salad dressing product, the amount of whey protein concentrate in the product would be at a level of no more than 8% by weight, the level of microcrystalline cellulose used would be at the lower end of the designated range, and there would be a change in the flavorings, such as an lncrease in the amount of sugar used.

~ ~32 ~3 The low fat or no fat mayonnaise products are made by the same procedure. The initial step in the process is the formulation of three or four premixes: a) a bulk dry ingredient blend premix; b) a microcrystalline cellulose premix; c) a gum and water premix; and d) a whey and/or egg premix. The bulk dry ingredient blend premix is defined as comprising any dry ingredients, except of course those specifically mentioned in one of the other premixes. Therefore, it would include polydextrose and any additional dry components such as modified food starch, maltodextrin, ~ums and water. The dry ingredients are preblended and then combined with water on a continuous basis.

Premix B comprises a blend of microcrystalline cellulosQ and water. The ingredients are combined in a powder/wa~er dispersing device and the resulting mixture is then pumped directly and continuously through a milling devlce, preferably a colloid mill. Tha gap on the mill is pre~erably between about 6 to about 1~ thousandths of an inch. The milling action is critical in order to form a uniform dispersion of the microcrystalline cellulose.

The third premix is the optional premix and is a combination of a protective colloid, such as xanthan gum, guar gum or combinations thereof and water. Preferably,~this premix is a combination of xanthan gum and water and its purpose is to prevent flocculation and insure proper dispersion of the 5 ~

microcrystalline cellulose. When used, this premix is combined with Premix B after Premix B is subjected to milling; and prior to being mixed with the other premixes.

The fourth premix is comprised of liquid egg whites, salt, flavors, colors and whey protein concentrate, when appropriate. The ingredients are combined in a refrigera~ed tank which has stirring means.

The premi~es are then added to a slurry make-up tank, with any additional ingredients such as sugar, oil, oil soluble flavors and colors and preservatives. The acidifying agent is also added directly to the slurry make~up tank, as the flnal ingredient. The ingredients are then blended ~or a period of at least 5 minutes. A~ter the slurry is blended, it is pumped to a continuous cooking and cooling system. The slurry is heated via steam jacketed swept surface heat e~changers to a temp~rature in the range of from about 175F to about 200F, where it is held for a period of from about 15 to about 75 seconds. The cooked slurry is then cooled to 70F in a series of swept sur~ace heat exchangers. The cooled product is then held in a non-jacketed and non-agitated tank until xe~uired on the packaging l~lne. The product is then pumped through a milling device, preferably a colloid mill prior ~o being rou~ed to the filling apparatus.

An alternate process can be used when making a low fat mayonnai e product which would change the point of addition of 2 ~ 3 some of the gums being added. Any gums which would be part of the bulk dry ingredient premix, can alternately be mixed with the oil, and the resulting mixture would be added directly to the slurry make-up tank. This does not apply to any gums which are used as protective colloids and form optional Premix C.

Incorporated in this procedure are a number of noteworthy features, such as the ability to cook the entire mixture, including the egg whites. This is contrary to a process for a true mayonnaise product where the egg portion is not cooked. It is preferable to cook the en~ire mixture in order to get a product with an acceptable texture. Other important features of this process are the milling steps, and the inclusion of Premix C when possible. As previously stated, the milling of the microcrystalline callulose is necessary in order to ~orm a uniform dispersion. The functlon of Premix C is important for good dispersion and prevention of subjecting the microcrystalline cellulose to acids or salts before it is protected by the gums. Therefore, when possible this additional premix should be formulated and combined with Premix ~ prior to incorporation in the slurry ma~e-up tank.

The final milling step smooths out the product resulting in a visually smoother, less gritty appearance and a "fattier" texture. This final milling step is similar to a full fat mayonnaise process, but differs from a so-called light mayonnaise process which may not require milling.

The following examples further illustrate various features of the invention, but are intended to in no way limit the scope of the invention which is described in the appended claims.

A low fat mayonnaise product was produced by forming the following three premixes:

Premix A % by weiqht Polydextrose 10.00 Modified food starch5.00 gums 0 30 water 30.00 Premix B

Av~cel 1.20 water 25.00 Premix C

Whey protein concentrate, dry basis 4.00 Egg white 6.00 flavors, colors 2.00 wa~er 5.50 Premix A was prepared by placing all the ingredients except water in a ribbon blender. After mixing, the water and blend were combined on a continuous bas~s in a powderiwater dispersing apparatus. The premix was then pumped to a slurry tank. Premix B was formed by combining Avicel (a blend of microcrystalline cellulo~e and sodium carboxymethyl cellulose from FMC Corporation, Philadelphia, P~ and water in a powder/water dispersing device. The mixture was then ~umped directly and continuously through a colloid mill at a rate of 40 to 50 gallons per minute, through a mill gap between 7 and 10 thousandths of an inch. The mixture was then pumped to the slurry tank, simultaneous with Premix A.

Premix C was formed by combining all the ingredients batchwise in a refrigerated, well stirred tank, where they were held until required. They were then pumped to the slurry tank after Premixes A and B had begun to be added to said slurry tank.

The remaining ingredients, 3.00% sugar, additional flavors and preservatives, and 2.00% vegetable oil were added directly to the slurry tan]c. ThQ 6.0~ vinegar was added to the ~lurry tank last. The slurry was then mixed for a perlod of about 10 minutes. There~ter, the slurry was pumped to a holding tank and from there to a continuous cooking and cooling system. The slurry was heated via steam ~acketed swept surface heat exchangers from ambient tempera~ures to 200F. It was then held at this temperature for 30 - 40 seconds in an insulated holding tube. The product was then cooled from 200 to 70 F in a series of swept surface heat exchangers, cooled first by chilled water, then by a standard refrigerant. The cooked and cooled product was then held in a non ~acketed and non agitated tanX until it was required at the packaging line. From this 2'3~2~

tank, the product was pumped through a colloid mill (gap between 10 and 30 thousandths of an inch) and then to the required filling apparatus.

~ he low fat mayonnaise product which resulted exhibited acceptable texture and taste qualities.

A low fat mayonnaise product wa~ made following the process in Example 1 but which further comprised a low D.E.
maltodextrin in Premix A. The three premixes were made up as ~ollows~

Premix ~ ~ by weiqht Polydextrose 6.00 Modified food ~tarch6.00 Maltodextrin (15 D.E.) 1.00 gums 0.30 water 25.00 Premix ~

Avicel 1.25 water 24.75 Premix C

Whey protein concentrate, dry basis 5.00 E~g white 11~00 flavors, colors 2.00 water 2.00 The remaining ingredients were 5.50% sugar, 2.00%
vegetable oil and 5.0% vinegar, as well as additional flavors and preservatives.

The resulting low fat mayonnaise product was judged to have acceptable organoleptic qualities~

The process of Example 1 was followed but a no fat mayonnaise product was produced. Premix C contained no whey protein concentrate and no edible oil was added. The total amount of water increased by about 4.0~, with a slight (le~s than 0.5~) in~rease in egg white content. The resulting no fat mayonnaise product exhibited acceptable texture and taste properties.

A low fat salad drQssing product was made following the process set out in Example 1 but with the following ingredients.

Premix A Salad Dressinq Polydextrose 9.5 Modified Food Starch5.0 Gums 0.3 Water 30.0 ~ 3 ;3 2 ~

Premix BSalad Dressinq Avicel 0.5 Water 25.0 Premix C

Whey Protein Concentrate ~Dry Base) 6.0 Egg White 4.0 Flavor, Colors 2.2 Water 5.0 Additional Ingredients Vinegar 5.0 Sucrose 5.5 Oil 2.0 The resulting product was found to exhibit textual qualities similar to the low fat mayonnaise products, but with a taste more characteristic of a salad dressing product.

A low Pa~ mayonnaise product was made containing the ~ollowing inqredients:

Premix A % by~weiqht modified food starch6~0 Polydextro~e 5.0 Maltodextrln ~:i5 D.E~) 3.0 guar gum 0.1 water 18.0 Premix B

Avicel 0.5 water 27.0 ~'2~l~3 Premix C % by weiqht xanthan gum 0.20 water 9.00 Premix ~
Protein 6.0 flavors, colors 4.0 water 11.0 Additional Ingredients sugar 4-0 vinegar 4.5 oil 2.0 The process of Example 1 was followed except that an additional premix, Premix C, was formulated. After milling Premix B, it is combined in a mixer with Premix C and then the combination is pumped to a slurry tank, simultaneous wlth Premix A.

The resultant low fat mayonnaise product exhibited good taste and texture qualities.

Claims (27)

1. A low fat mayonnaise product comprising less than 10% by weight edible oil, water, egg white, microcrystalline cellulose and polydextrose.

2. The low fat mayonnaise product of claim 1 wherein the egg white is present in an amount of from about 1 to about 20%
by weight.

3. The low fat mayonnaise product of claim 1 which further comprises whey protein concentrate in an amount up to 10%
by weight.

4. The low fat mayonnaise product of claim 1 wherein the microcrystalline cellulose is present in an amount of about 0.25 to about 5% of the total product.

5. The low fat mayonnaise product of claim 1 which further comprises from about 0.5 to 7.5% maltodextrin.

6. The low fat mayonnaise product of claim 1 which comprises from 1.0 to 15% polydextrose.

7. The low fat mayonnaise product of claim 1 which further comprises from about 2.0 to about 10% modified food starch.

8. The low fat mayonnaise product of claim 1 which further comprises an acidifying agent.

9. A low fat mayonnaise product which comprises from about 1.0 to about 4.0 added edible oil, from about 40 to about 90%
water, from about 7.0 to about 15% egg white, from about 0.5 to about 4.0% whey protein concentrate, from about 0.2 to about 3.5% microcrystalline cellulose, from about 2.0 to about 5.0 maltodextrin, from about 4.0 to about 6.0%
modified food starch, and from about 2.0 to about 10%
polydextrose.

10. The low fat mayonnaise product of claim 9 which further comprises an acidifying agent.

11. The low fat mayonnaise product of claim 10 which further comprises flavorings, colors, and preservatives.

12. A no fat mayonnaise product with no edible oil which comprises water, egg white, microcrystalline cellulose and polydextrose.

13. The no fat mayonnaise of claim 12 which further comprises whey protein concentrate.

14. The no fat mayonnaise of claim 12 which further comprises modified food starch.

15. The no fat mayonnaise of claim 12 which further comprises maltodextrin.

16. The no fat mayonnaise of claim 12 wherein the egg white is present in an amount of from 1.0 to about 20% by weight.

17. The no fat mayonnaise of claim 12 wherein the whey protein concentrate is present in an amount up to 10% by weight.

18. A low fat mayonnaise product comprising less than 10% by weight edible oil, water, egg white, microcrystalline cellulose and polydextrose.

19. A low fat salad dressing product comprising no more than 10% by weight edible oil, water, egg white, whey protein concentrate, microcrystalline cellulose and polydextrose.

20. A process for the production of a low fat or no fat mayonnaise product which comprises forming three premixes:

a) dry ingredients and water;
b) microcrystalline cellulose and water; and c) egg white and water;

combining the premixes a, b and c and additional components in a mixing tank to form a slurry; mixing for a period of at least about 5 minutes; heating the slurry to a temperature of about 175°F to about 200°F for a period of about 15 to about 75 seconds; cooling the slurry to about 70°F and then pumping the slurry through a milling device.

21. The process of claim 20 wherein premix b is pumped through a milling device prior to being combined with premixes a and c.

22. The process of claim 20 or 21 wherein the mill is a colloid mill.

23. The process of claim 20 which further comprises premixing gums with vegetable oil and adding the resulting mixture directly to the mixing tank with premixes a, b and c to form a slurry.

24. A process for the production of a low fat mayonnaise product which comprises forming three premixes:

a) dry ingredients and water, b) microcrystalline cellulose and water; and c) whey protein concentrate, egg white and water;

combining the premixes a, b and c and additional components in a mixing tank to form a slurry; mixing for a period of at least about 5 minutes; heating the slurry to a temperature of about 175°F to about 200°F for a period of about 15 to about 75 seconds; cooling the slurry to about 70°F and then pumping the slurry through a milling device.

25. The process of claim 24 wherein premix b is pumped through a milling device prior to being combined with premixes a and c.

26. A process for the production of a low fat or no fat mayonnaise product which comprises forming four premixes:

a) dry ingredients and water;
b) microcrystalline cellulose and water;
c) colloid gum and water; and d) protein and water;

combining Premixes B and C to form Premix E, and then combining Premixes A, D and E in a mixing tank to form a slurry; mixing for a period of at least 5 minutes; heating the slurry to a temperature of about 175°F to about 200°F
for a period of about 15 to about 75 seconds; cooling the slurry to about 70°F and then pumping the slurry through a milling device.

27. The process of claim 26 wherein Premix B is pumped through a milling device prior to being combined with Premix C.

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