CA2195319A1 - Positive hydration method of preparing confectionery and product therefrom - Google Patents

Abstract

The present invention is a new method of making a confectionery mass, such as a nougat, by hydrating sufficiently to form the mass without the need for cooking to drive off moisture. The present invention also includes a product prepared by positively hydrating a mixture of confectionery ingredients including a hydrobinding component and shearform product.

Description

W096l38~9 2l 953 PO~ v~ HYDRATION METHOD OF PREPARING
CONFECTI~N~~Y ~n PRODUCT .~ H

BAC~GROUND OF T~ INVENTION

The present invention relates to the art of confectionery manufacturing, and, in particular, to novel methods of making a functionalized confectionery mass which does not require cooking to dehydrate, and product(s) therefrom.

It is generally considered a necessity in the art of preparing confectionery masses, such as nougats, to use water as a mixing medium and source of hydration for ingredients. Specifically with respect to nougats, a typical recipe calls for soaking egg albumen in water over a period of time, such as overnight, in order to fully hydrate the protein. Following hydration, the egg albumen is stirred and strained before being beaten into a stiff foam. Other ingredients such as sugar, honey, and corn syrup are separately cooked together with water to a temperature of from about 135~ to about 138'C. The cooked mixture is then poured into the egg and beaten with a nougat mixer, which is similar to a marshmallow mixer but generally more robust. Additional parts of sugar and other ingredients must then be added and the mixture beaten or stirred over a hot water bath.
Excessive water is required in the preparation of the nougat to serve as a mixing medium and source of hydration. Consequently, moisture must be driven off as much as possible to provide structural integrity and consistency of the end product.

SUBSTITUTE SHEET (RULE 26) W O 96/38049 2 1 9 5 3 ~ 9 - PC~rNS9610800 ~

Prior art processes require excessive amounts of water to provide a mixing medium and to hydrate the components. With respect to hydration, water is supplied in more than sufficient quantity to ensure that specific ingredients are wetted and functionalized. With respect to use of water as a mixing medium, once again excessive amount of moisture is generally used 50 that ingredients can be contacted by suspension or dissolution in the medium. The overall process requires the use of far more moisture than is actually required to provide solubility of the ingredients which results in a coherent mass having structural integrity.

As a consequence of the use of excessive water to hydrate and as a mixing medium, the artisan is then required to reduce the unwanted additional moisture as best as possible. This is generally undertaken by a combination of mixing and boiling to drive the moisture off. This process is energy-inefficient and very costly.
Moreover, it is ineffective to eliminate a significant amount of the moisture contained in the confectionery mass .

One of the unwanted results of inefficient dehydration is that water remains as a separate phase in the end product. This water is not bound to other ingredients and can be referred to as "free moisture" or "unbound water." Free moisture can detract from the end product because it weakens the structural integrity and/or reduces the quality of organoleptic perception.
Free moisture has been identified in food art by "water activity."

Noreover, free moisture provides an environment in which micro-organisms can grow. Microbiological growth in food products has also been used to measure the existence of free moisture.

S~I~IES~ IIIE2~) ~ W096~8049 2 1 9 5 3 1 9 "Water activity" is measured as the ratio between the vapor pressure of water in an enclosed chamber containing a food and the saturation vapor pressure of water at the same temperature. Water activity is an indication of the degree to which unbound water is found and, consequently, is availability to act as a solvent or participate in destructive chemical and microbiological reactions.

Many food preservation processes attempt to eliminate spoilage by lowering the availability of water to microorganisms. Reducing the amount of free moisture or unbound water also minimizes other undesirable chemical changes which can occur in foods during storage.
The processes used to reduce the amount of unbound water in foods include techniques like concentration, dehydration, and freeze drying. These processes require intensive energy and are not cost efficient.

As a result of the present invention, the above difficulties and other difficulties generally associated with the prior art have been overcome.

~nMM~Rv OF Tn~ INV~NTION

The present invention is a method of making a confectionery mass, especially a nougat, by a positive hydrating step and without need for dehydrating in order to produce the confectionery mass. The present invention also includes the product resulting from the new method ~ of preparation.

~ The method of the present invention primarily includes the use of flash-flow processing to prepare ingredients to create a "water-starved," but functional, confectionery mass. Flash-flow processing opens the SU~I~E S~EEr (RUIE 26) W096/38049 2 1 953 1 9 .~

structure of the components to increase its ability to hydrate, e.g., enhance wettability. Flash-flow processing also mixes ingredients and brings them into intimate contact with each other. Flash-flow processing can be performed by either flash-heat processing or a flash-shear processing as defined herein.

In one preferred Pmho~;r-nt, shearform matrix is combined with a hydrated hydr~bin~;ng component. The hydrobinding component can also be subjected to flash-flow processing prior to hydration. When the hydrobinding component is flash-flow processed, a saccharide-based material can be included in the feedstock to improve processability. The hydrobinding - -nPnt can include a proteinaceous material such as a gelatin, or a food grade gum such as gum arabic, carrageenan, and mixtures thereof.

In another embodiment, the hydrobinding , o~Pnt can also be aerated, preferably in the presence of an aerating agent, prior to or after combining it with the shearform matrix. Aerating agents include, among other things, egg whites, soy protein, and combinations thereof.

A primary component of the shearform matrix can be a saccharide-based material such as sucrose, corn syrup solids, polydextrose, and mixtures t~ereof. A preferred saccharide-based ingredient is polydextrose. As previously mentioned, a saccharide-based ingredient can also be included with the hydrobinding component, especially when it is flash-flow processed prior to combining with the shearform matrix.

In a most preferred Prho~ nt of the invention the saccharide-based ingredient, e.g. polydextrose, is subjected to flash-flow processing prior to flash-flow ~IIIUIE SHEE~ ~RUIE 26) ~ W09~38049 2 1 9 5 3 1 9 ~ ' 3' processing associated with mixing and hydration. This prior flash-flow processing is referred to herein as "pre-flash-flow processing."

It is further contemplated that active ingredients can be included in the confectionery mass which is formed as a result of the present invention. The active ingredients can be quite varied, and a non-exhaustive list has been set forth below in the section entitled "Detailed Description of the Invention."

In a most preferred embodiment of the present invention a nougat mass is prepared which has a frappe consistency and is made with nutritional ingredients so that a health product can be produced. In particular, vegetable and/or fruit components can be added to provide a nutritious food product. If desired, a product having the minimum daily nutritional requirements can be produced. In fact a "health bar" has been prepared which contains up to five (5) "U.S. rPc~ -nded human adult dietary servings" of vegetable and/or fruit. ("The rec~ -n~Pd human adult dietary serving" is defined by the Consumer Affairs Division of the United States Food and Drug Administration, which is incorporated herein by reference). Furthermore in this regard, ingredients which have strong olfactory characteristics, e.g., aroma and flavor, can be treated to enhance patentability before incorporating into a health product prepared in accordance with the invention.

The product resulting from the present invention is ~ unique because it requires no cooking or dehydration by heating to produce, and has substantially no phase ~ separation of moisture. The only moisture present is an amount sufficient to functionalize the mass. Thus, the product can be preparing without cooking.

SllBStllU~E SHEI ~WIE 26) W096/38049 2 ~ 9 5 3 1 9 It is well known that free moisture in food products can detract from the product. Free moisture has been identified in the art by the use of water activity. In the present invention, the water activity is not greater than 60% ERH, and is preferably not greater than about 55% ERH.

Another measure of free moisture in foodstuffs is the amount of biological growth within the composition.
In the present invention, the biological activity is less than about 100 ppm, preferably less than about 25 ppm, and most preferably less than 10 ppm.

Excessive water previously required to mix and hydrate one or more ingredients is eliminated without dehydrating. Heat and mixing normally used to drive off excessive moisture are no longer required. Consequently, heat history generally associated with energy-intensive procedures is also eliminated.

The present invention also provides the ability to formulate confectionery masses with a significantly reduced fat and calorie content. This result is quite unexpected, since fat has traditionally been used to assist in functionalizing food masses by providing internal lubrication without water.

For a better understanding of the present invention, together with other and further objects, reference is made to the following description taken in conjunction with the examples, and the scope is set forth in the appended claims.

9J~ITIUIE SHEEI (RUL~ 2~

~ W096~8049 72 t 9 5 3 t 9 P~

DETAI~ED DESCRIPTION OP T~E INVENTT0N

The method for making confectionery mass in accordance with the present invention includes combining shearform matrix and a hydrobinding cn~ponant, which is hydrated sufficiently to provide "controlled water delivery" to the shearform matrix and/or other ingredients. "Controlled water delivery" means delivery of water suf'icient to provide internal viscosity and cohesivity to the shearform matrix, understanding, of course, that shearform matrix has significantly anhAnaa~
wettability because of a randomized structure resulting from flash-flow processing. The word "hydrated" as used in the term "hydrated hydrobound cn~pnnont" herein means sufficient water to provide "controlled water delivery."

The system created by the combination of the present invention is a "water-starved" system, which means having only enough moisture to bind the ingredients together and provide ;ntP~nAl lubricity. Since the ingredients are competing for moisture due to anhAn~o~ wettability, there is virtually no free moisture available to separate from the mass.

Shearform matrix is prepared by ~lash-flow procQ~sing which mixes and conditions ingredients for intir,ate contacting and anh~n~ad hydration. The hydrobinding - L can also be subjected to flash-flow processing, preferably in the presence of a saccharide-based material, included as a carrier in the feedstock, before hydrating. The hydrobinding component can also be aerated, preferably in the presence of an ~30 aerating agent, before or after combining with the shearform matrix.

W096/38049 ~ t 9 5 3 1 9 p "~ , ~

An~~her prefer_ed embodiment of the presen~
invention includes flash-flow processing of cer,ain ingredients prior to combining with other ingredients as set forLh hereinabove. This is referred to as pre-flash-S flow processing. The saccharide-based material, e.g., polydextrose, can be pre-flash-flow processed. Flash-flow processing results in increased surface area and increased solubility of the ingredients subjected thereto, and contributes to actual binding of the ingredients to each other.

An impor ant concept of the present invention is to increase the wettability of the ingredients of a confectionery m~ss s~ iPntly to ~unctionalize the mass without the use of excess water. 'lFunct;nnAl;7ation~ of a confectionery mass means providing the ingredients with sufficient internal cohesivity to be handled wi hout losing its integrity as a mass. In order to be "handled"
in the context of functionalization, the mass must also possess internal lubricity which permits inter- and intra-par,icle v~ L without loss of cohesiveness.
Functionalized food masses have been described as having the consistency of a dough, paste or as chewy, etc.
~owever, the present invention is not to be linited by any "shor.-hand" description of the consistency.

Fat has been used in the past to functionalize food masses, and the present invention enables the ar~isan to functionalize a confectionery mass without need for added fat. Functionalization is achieved in the present invention by u~;li7;ng certain ingredients and flash-flow processins. ~o~ever, selected amounts of f~t may be added to obtain perceived texture and/or flavor characteristics.

In the present invention, a hydrobinding component is used in conjunction with flash-flow processing to ~ W096/38049 2 1 9 5 3 1 9 PCT~S96~8005 provide a functionalized hydrobound confectionery mass.
A functionalized "hydrobound confectionery mass" as used herein is a functionalized mass of confectionery ingredients which contains substantially no excessive free moisture or unbound water. A functin~Ali~
hydrobound confectionery mass of the present invention does not require dehydration to remove excess water.

While not bound by theory, it is believed that water is hydrobound because it is tightly bound to surface polar sites through chemisorption. These sites may include the hydroxyl groups of hydrophilic materials such as proteins, gums, starches, and sugar.

A "hydrobinding component" is an ingredient which imbibes, delivers and maintains water in an amount sufficient to functionalize the resulting mass. The water which is hydrobound does not separate and become a separate phase. A "hydrobinding component" cooperates with other ingredients to deliver and maintain water sufficient to functionalize the mass of ingredients which have been subjected to flash-flow processing. Other ingredients are flash-flow processed in accordance with the invention. Flash-flow processing not only ensures intimate mixing without the use of water as a medium, but also conditions the ingredients for wetting with a minimum of water.

Thus, a hydrobinding component can be hydrated and mixed with shearform product (i.e., ingredients which have been subjected to flash-flow processing) to form a functionalized hydrobound confectionery mass. The hydrobinding component can also be subjected to flash-flow processing prior to hydration in order to enhance wettability. It is preferred to include a saccharide-based material with hydrobinding component when it is subjected to flash-flow processed. After combining the SUBSlm~ES~E~ (RVIE26) W096/38049 2 l 953 l 9 hydrated hydrobinding component and the shearform matrix, moisture is readily imbibed and disseminated throughout the non-hydrated components and/or ingredients. Unlike prior art mixtures, additional moisture is not required to form a hydrated mixture. Thus, excess water is not present in the resulting mass.

The hydrobinding component and shearform matrix captures or binds sufficient moisture to functionalize the total mass. The ingredients capture the moisture o physically, chemically and/or even biologically.
Whatever the binding vehicle may be, water is held and made available for absorption by the rr~-;a~r of the ingredients.

Hydrobinding components useful in the present invention include proteinaceous material, such as gelatin, and food grade gums, such as gum arabic, carrageenan, and mixtures thereof.

Ingredients which are used in the hydrrh;n~;ng component can also be included in the shearform matrix component. Thus, gelatins and food grade gums such as gum arabic, carrageenan, et al., can be incIuded in the feedstock used to prepare the shearform matrix.

Flash-flow processing prepares ingredients to be easily and quickly hydrated. Another very important result of flash-flow processing is intimate mixing of the ingredients. Intimate mixing has traditionally been achieved by use of water as a mixing medium. Flash-flow processing, however, intimately contacts ingredients and randomizes ingredient location and structure of the resulting matrix. Randomizing the structure can be thought of as opening the physical and/or chemical structure for hydration.

SU~IIUIE SNÇE~ ~UIE 2~) W09~38049 21 9531 q ~

11 , In one embodiment of the invention the saccharide-based material can be pre-flash-flow processed. For example, polydextrose, a preferred saccharide-based ingredient, can be pre-flash-flow processed.

The term "flash-flow" has become recognized in the art as referring to a process which uses conditions of temperature and force to transform a solid feedstock to a new solid having a different morphological and/or chemical structure. The term "flash-flow" is described in commonly-owned U.S. Patents 5,236,734, issued August 17, 1993 and 5,238,696, issued August 24, 1993, as well as co-pending U.S.S.N. 07/787,245 filed November 4, 1991, U.S.S.N. 07/893,238, filed June 30, 1992, U.S.S.N.
07/847,595, filed March 5, 1992 and U.S.S.N. 099,200, filed July 29, 1993, which are incorporated herein by reference.

In "flash-flow" processing, the time during which the feedstock material is subjected to elevated temperature is very short. Flash-flow processing can be accomplished either by a flash-heat method or a flash-shear method, as described further herein. In the flash-heat method, the feedstock is subjected to elevated temperature usually for only tenths of a second, and in the flash-shear method the feedstock is subjected to elevated temperatures for a time on the order of seconds.

In the flash-heat process, the feedstcck is heated sufficiently to create an internal flow condition which permits internal movement of the feedstock at subparticle level and exit openings provided in the perimeter of a spinning head. The centrifugal force created in the spinning head flings the flowing feedstock material outwardly from the head so that it reforms with a changed structure. The force necessary to separate and discharge flowable feedstock is provided by centrifugal force and SUBSTITUTE SHEET (RULE 26~

W096/38049 2 I q 5 3 l q r~"~

the force of the ambient atmosphere impinging on feedstock exiting the spinning head.

One ap~L~tu~ for implementing a flash-heat process is a "cotton candy" fabricating type machine, such as the Econo-floss model 3017 manufactured by Gold Medal Products company of Cincinnati, Ohio. Other apparatus which provides similar forces and temperature gradient conditions can al50 be used.

In the flash-shear process, shearform matrix is produced by raising the temperature of the feedstock, which includes a non-solubilized carrier such as a saccharide-based material, until the carrier undergoes internal flow upon application of a fluid shear force.
~he feedstock is advanced and ejected while in internal flow condition, and subjected to disruptive fluid shear force to form multiple parts or masses which have a morphology dif~erent from that of the original feedstock.

The flash-shear process can be carried out in an apparatus which has means for increasing the temperature of a non-solubilized feedstock and means for simultaneously advancing it for ejection. A multiple heating zone twin screw extruder can be used for increasing the temperature of the non-solubilized feedstock. A second element of the apparatus is an e~ector which reduces the feedstock to a condition for shearing. The ejector is in fluid communication with the means for increasing the temperature and is arranged at a point to receiYe the feedstock while it is in internal flow condition. See commonly-owned ~.S. Patent No.
5,380,473, issued on January 10, 1995 and entitled "Process for Making Shear-Form Matrix," which is incorporated herein by reference.

SUBSTITUTE SHEET (RULE 26) ~ W096/38049 2 1 9 5 3 1 9 ~ r The feedstock for producing shearform matrix includes a carrier material. The carrier material can be selected from material which is capable of undergoing both physical and/or chemical change associated with flash-flow processing.

Material8 which can be used as carrier materials in the feedstock include saccharide-base ingredients such as sucrose, corn syrup solids, polydextrose, and mixtures thereof.

Corn syrup solids are commonly known as maltodextrins. Maltodextrins are composed of water soluble glucose polymers obtained from the reaction of the starch with acid or enzymes in the presence of water.
The hydrolysis reaction produces a carbohydrate mixture of saccharides having a dextrose equivalence (D.E.) of less than 20, or greater than 20 when the hydrolysis proceeds to produce what the FDA has termed corn syrup 801 ids.

Polydextrose is a non-sucrose, essentially non-nutritive carbohydrate substitute. It can be prepared from polymerization of glucose in the presence of polycarboxylic acid catalysts and polyols. Generally, polydextrose is known to be commercially available in three forms: Polydextrose A and Polydextrose K, which are powdered solids, and Polydextrose N supplied as a 70 solution. Each of these products can also contain some low molecular weight -n~nts, such as glucose, sorbitol, and oligomers. Applicants incorporate herein the contents of commonly-owned U.S. Patent No. 5,279,849 issued on January 18, 1994.

Sugars can also be used as an ingredient in the feedstock. "Sugars~ are those substances which are based on simple crystalline mono- and di-saccharide structures, SUBSIIIUIE SHEEI alUlE 26) W096f38049 2 1 9 5 3 t 9 , ~

i.e., based on C5 and Cb sugar structures. "Sugars"
include sucrose, fructose, lactose, maltose and sugar ~lc~h~ls such as sorbitol, mannitol, maltitol, etc.

Other materials which can be incorporated into the feedstock to enhance the shearform matrix include flavors, sweeteners, and surfactants (other than the carrier itself).

Flavors may be chosen from natural and synthetic flavoring liquids. An illustrative list of such agents includes volatile oils, synthetic flavor oils, flavoring aromatics, oils, li~uids, oleoresins or extracts derived from plants, -leaves, flowers, fruits, stems and combination thereof. A non-limiting representative list of examples includes citrus oils such as lemon, orange, grape, lime and grapefruit and fruit essences including apple, pear, peach, grape, strawberry, raspberry, cherry, plum, pineapple, apricot, or other fruit flavors.

Other useful flavorings include aldehydes and esters such as benzaldehyde ~cherry, almond), citralm i.e., alphacitral (lemon, lime), neural, i.e., betacitral (lemon, lime) decanal (orange, lemon), aldehyde C-8 (citrus fruits), aldehyde C-g (citrus fruits), aldehyde C-12 (citrus fruits), tolyl aldehyde (cherry, almond), 2,6-dimethyloctanal (green fruit), and 2-dodecenal (citrus, mandarin), mixtures thereof and the like.

~he sweeteners may be chosen from the following non-limiting list: glucose (corn syrup), dextrose, invert sugar, fructose, and mixtures thereof (when not used as a carrier); saccharin and its various salts such as the sodium salt; dipeptide sweeteners such as aspartame;
dihydrochalcone compounds, glycyrrhizin; ~Yia Reban~i~na (Stevioside); chloro derivatives of sucrose such as sucralose; sugar alcohols such as sorbitol, SU~511~UlESHEEr (~U~E2~) .. . . ... . .. ..

wo 96/3804g 2 1 9 5 3 1 9 ' ~

mannitol, xylitol, and the like. Also contemplated are hydrogenated starch hydrolysates and the synthetic sweetener 3,6-dihydro-6-methyl-1-1-1,2,3-oxathiazin-4-one-2, 2-dioxide, particularly the potassium salt (acesulfame-K), and sodium and calcium salts thereof.
Other sweeteners may also be used.

The surfactants may be chosen from the following non-limiting list; Lecithin, Hydrol, Durem, Myverol, and Paramount.

Additional materials which can be incorporated into the feedstock to enhance the shearform matrix include biologically active ingredients such as medicinal substances and antacids.

Medicinal substances which can be used in the present invention are varied. A non-limiting list of such substances is as follows: antitussives, antihistamines, decongestants, alkaloids, mineral supplements, laxatives, vitamins, antacids, ion exchange resins, anti-cholesterolemics, anti-lipid agents, antiarrhythmics, antipyretics, analgesics, appetite suppressants, expectorants, anti-anxiety agents, anti-ulcer agents, anti-inflammatory substances, coronary dilators, cerebral dilators, peripheral vasodilators, anti-infectives, psycho-tropics, antimanics, stimulants, gastrointestinal agents, sedatives, antidiarrheal preparations, anti-anginal drugs, vasodialators, anti-hypertensive drugs, vasoconstrictors, migraine treatments, antibiotics, tranquilizers, anti-psychotics, antitumor drugs, anticoagulants, antithrombotic drugs, hypnotics, anti-emetics, anti-nauseants, anti-convulsants, neuromuscular drugs, hyper- and hypoglycemic agents, thyroid and antithyroid preparation, diuretics, antispasmodics, uterine relaxants, mineral and nutritional additives, antiobesity drugs, anabolic drugs, SU~Sllll-dl~SHEI ~RUIE26) W096~8049 2 ~ 9 5 3 1 ~ PCT~S9610800 ~

erythropoietic drugs, antiasthmatics, cough suppressant6, mucolytics, anti-uricemic drugs and mixtures thereof.

Especially preferred active ingredients contemplated for use in the present invention are antacids, H2-antagonists, and analgesics. For example, antacid dosages can be prepared using the ingredients calcium carbonate alone or in combination with magnesium hydroxide, and/or aluminum hydroxide. Moreover, antacids can be used in combination with H2-antagonists.

Analgesics include aspirin, acetaminophen, and acetaminophen plus caffeine.

Other preferred drugs for other preferred active ingredients for use in thc present invention include antidiarrheals such as immodium AD, antihistamines, antitussives, decongestants, vitamins, and breath fresheners. Also contemplated for use herein are anxiolytics such as Xanax; antipsychotics such as clozaril and Haldol; non-steroidal anti-inflammatories (NSAID's) such as Voltaren and Lodine; antihistamines such as Seldane, ~;c~-n~l, Relafen, and Tavist;
antiemetics such as Kytril and Cesamet; bL~n~h~dilators such as Bentolin, Proventil; antidepressants such as Prozac, Zoloft, and Paxil; antimigraines such as Imigran, ACE-inhibitors such as Vasotec, Capoten and Zestril;
Anti-Alzheimers agents, such as Nicergoline; and ca~-Antagonists such as Procardia, Adalat, and Calan.

The popular H -antagonists which are contemplated for use in the present invention include cimetidine, ranitidine hydrochloride, famotidine, nizatidine, ebrotidine, mifentidine, roxatidine, pisatidine and aceroxatidine.

SU~IIIUIE glEE~ (RUlE 26) ~ W096l38049 2 1 9 5 3 1 9 P_ll. 1 ~!

Active antacid ingredients include, but are not limited to, the following: aluminum hydroxide, dihydroxyaluminum aminoacetate, ~mi noacetic acid, aluminum phosphate, dihydroxyaluminum sodium carbonate, bicarbonate, bismuth aluminate, bismuth carbonate, bismuth subcarbonate, bismuth subgallate, bismuth subnitrate, calcium carbonate, calcium phosphate, citrate ion (acid or salt), amino acetic acid, hydrate magnesium aluminate sulfate, magaldrate, magnesium aluminosilicate, magnesium carbonate, magnesium glycinate, magnesium hydroxide, magnesium oxide, magnesium oxide, magnesium trisilicate, milk solids, aluminum mono- or dibasic calcium phosphate, tricalcium phosphate, potassium bicarbonate, sodium tartrate, sodium bicarbonate, magnesium aluminosilicates, tartari acids and salts.

Other active ingredients include antiplaque medicaments and r-~;r~-~nts for veterinary use.

Another component which can be included in products made in accordance with the present invention i5 a nutritional component. A nutritional component can include ingredients which have vitamins and minerals required to maintain good health. A "health bar" product has been prepared in accordance with the present invention which includes a dry residue of whole vegetables and/or fruits. In fact, a health bar product has been made which includes up to five (5) times the U.S. r~l -rded human adult dietary serving of vegetables and/or fruit by incorporation of the dry residue of such fruits and vegetables. Sources of minerals and fiber can also be included.

A preferred embodiment of the nutritional form of the product contemplates treating ingredients having strong olfactory characteristics, e.g., flavor and aroma, to reduce such characteristics. For example, dry residue SIBSIIIUIE ~EEI (RUIE 26) W096l38049 of spinach and broccoli have been treated by heating in the presence of yoghurt powder and a small amount of moisture to drive off strong aroma and flavor notes.
This technique conditions such ingredients for incuL~ùLction ln a health product without detracting from the overall smell and taste of the product. It has been found that the above technique is particularly effective for preparing a nutritional "health bar product."

One Pmho~ir~nt of the present invention includes flash-flow processing a hydrobinding component and subsequently hydrating the hydrobinding component. The hydrobinding component, e.g., the gelatin and/or gum, can be aerated, preferably in the presence of an aerating agent, before or after being combined with shearform matrix. Preferred aerating agents include egg whites and soy protein.

The confectionery ingredients of this embodiment can include the active ingredients and non-active ingredLents described hereinabove.

The products r~C~lt;n1 from the present invention are unique because they require no dehydration to produce, e.g., the product can be prepared without cooking. There is substantially no separation of moisture in the r~nl~;n~ product. The only moisture present is an amount sufficient to functionalize the mass.

The hydrobound system of the present invention is a mass which has been hydrated by adding moisture to provide hydrocolloidal stability, but which does not have measurable free water, e.g., syneresis is substantially halted. "Syneresis" is referred to as the phenomenon of separation of water from a mass of material as a distinct phase. When the moisture is so minimal in a mass or ~mUlE SH~E~ (RUIE 26) =, . . .

~ W096/38~9 2 1 953 1 9 ~ 6~ .

sufficiently bound to other components in the mass that phase separation does not occur, syneresis is stopped or halted. When syneresis occurs, free water is available within the system. Free water is generally unwanted in confectionery products of the type disclosed herein because of product deterioration and micro-organic growth. A correlation between free water and water activity has been made as a measure of product stability.

Nany properties of foods are affected by the content and nature of water which they contain. Water participates in mass transfer and chemical reactions where it assumes a major role in determining physical and chemical content of foods. The production of a new food must almost inevitably confront the nature of water if the final product is to be stabilized with regard to nutritional content, microbial growth, and other factors.

A well-known method for characterizing the presence of water is by water activity. Water activity is measured as the ratio between the vapor pressure of water in an enclosed chamber containing a food and the saturation vapor pressure of water at the temperature.
Water activity indicates the degree to which water is bound and, subsequently, available to act as a solvent or participate in destructive rhem; r~ 1 and microbiological reactions.

When the water activity is low, water is unavailable because it is tightly bound to surface polar sites through chemisorption. Water activity is defined in the following manner.
aw = --where aw is water activity, p is the partial pressure of water above the sample, and P,~ is the vapor pressure of Sll~ll~UIESIIE~ (IWIE 26~

W096/38049 2 1 9 5 3 1 9 PCT~S96/0800 ~

pure water at the same temperature (must be specified).

Another definition of water activity which is more thermodynamically appropriate is Peg aw = -Po where Peq is the partial vapour pressure of water in equilibrium with the solution and P0 is the vapour pressure of pure water at the same temperature and pressure as the solution. When a solute is added to water, water molecules are "displaced" by solute molecules and the ratio of the vapour pressures or a~ is altered. Entropy is also lowered as solute molecules become oriented to water molecules. As a result, water molecules are not as free to escape from the liquid phase and the vapour pressure is therefore decreased. This change is governed by Raoult's law, which states that the decrease in vapour pressure of a solution is equal to the mole fraction of its solute. similarly the ratio of vapour pressures (aw~ is governed by the number of moles of solute (n,) and solvent (n2):

P n~
aw =
P0 n, + n2 Different solutes tie up or bind water to varying degrees depending on the nature of the solute, such as its level of dissociation, extent and nature of intramolecular binding, solubility and chemical components.

Further, a portion of total water content present in foods is strongly bound to specific sites on the ch~;c~lS that comprise the foodstu~. These sites may include the hydroxyl groups o~ polysaccharides, the carboxyl, amino groups o~ proteins, and other polar sites ~illUESl~E~ (RUU 26) ~ W096~8049 2 1 9 5 3 ~ 9 P~

that may hold water by hydrogen bonding or other strong chemical bonds. In addition to strongly bound water molecules, some of the water in foods is usually bound less firmly but is still not available as a solvent for various water-soluble food component. Thus, water activity is low when water is tightly bound to surface polar sites through chemisorption. The sites can include hydroxyl groups of hydrophilic material which are effective in controlling water activity.

In the present invention water activity is significantly lower than water activity of similar products found in the candy bar industry. For example, candy bars usually have a water activity of 62% - 68%
equilibrium relative humidity (ERH). The confectionery product of the invention, however, has only a 60% ERH, and is preferably not greater than about 55% ERH.

Another measure of free water in foodstuffs can be provided by the amount of biological growth within the composition. In the present invention, the biological activity is less than about 100 ppm, preferably less than about 25 ppm, and most preferably less than lO ppm.

Another distinctive feature of the present invention is the ability to reduce fat and calories in confectionery products. As a result of the present invention, a confectionery nougat product can be made which has little or no fat content. This product qualifies under industry standards to be referred to as "Reduced Fat" (which means the fat content is reduced by 1/3) and as "Low Fat" (which means the fat content is reduced by 50%).

For a better understanding of the present invention, together with other and further objects, the following examples and tables are provided to illustrate the unique SU9SIIIUIE SHEEr (RUIE 26) W096/38~49 2 1 9 53 1 9 methods of making a confectionery mass and products resulting therefrom.
~lr~MPL~ I

A shearform matrix was formed from the composition set forth in Table IA below. The sucrose, corn syrup solids and antacid c L-nents were blended to form a first mixture. Hydrogenated palm oil, and surfactants were combined under heat conditions sufficient to melt and form a second mixture. The second mixture was blended with the first mixture while still molten.

T~RT~ I A
IngredientPercent of Composition Sucrose 29.74%
Corn Syrup Solids35.51%
Antacid (CaC03)21.00%
Hydrogenated Palm Oil 11.46%
Emulsifiers (Lecithin) 1.72%
tMono-glyceride)0.57%

TOTAL 100.00%
The resulting mixture waG cooled and subjected flash-flow processing by spinning in a flash-heat apparatus operated at about 3500 r.p.m. to produce a shearform matrix.

Separately, hydrobinding components were prepared by hydrating the Gelatin and Gum combination set forth in TABLE I B, and mixed at above room temperature until a smooth consistency was attained.

SU~IIIUIE SHEEI (~UIE 26) ~ W096/38049 2195319 r~ s ~ ,~

TAB~E I B
Ir,gredient Percert of Co=position ~ydrobinding ~ -nts Gelatin 2.73 Gum Arabic 0.43~
Water 8.00%

Shearform Natrix 87.29%
from Table IA
Color 0.08%
Flavor 0.47%
Glycerin 1.00%
TOTAL 100.00~
1.
Shearform matrix resulting from the preparation of TABL2 IA was combined with color in a mixer and warmed to above room te~per~L4Le. The hydrobinding cn~po~nts prepared as set forth above were tben added to the colored shearform matrix. Flavors and glycerin were added while mixing.
., The amount of moisture captured and delivered by the hydrobinding ~nts was sufficient to hydrate the shearform matrix and functionalize the entirc mass. The resulting system was a fully functional water-starved system, i.e., having virtually no separate water phase.
The resulting mass was permitted to set in a pan, and subsequently separated into bite size squares (e.g., about 3.0 grams)~

The resulting product was a well-forme~ excellent tasting nougat having well-structured intesrity. The nougat was only nodestly tacky. The nougat was an excellent dosage form for delivery of the zntacid component, i.e., calcium carbonate.

~y-AMpLE Il A shearfor~ matrix was for~ed from the composition set for,h in Table II A below. The surfactants were (pre-melted) and blended to form a first mix,ure.
Antacid ~~ts, powder fructose, polydextrose, gum arabic (a non-hydrated hydrobinding ingredient), and flavors were blended separately to form a mixture. The first mix.ure was added while mixing. Glycerin was then added also while mixing.
T~3LE II A

Ingredier,tPercent of Composition Antacid (Calciun Carbonate) 2.58%
Sweetene-(Powde- Fructose) 20 79%
Saccharide (Polydextrose) 46.57%
Coconut Oil 2.58%
F~--l cif i ers (Glycer~l Monostearate) 0.52%
(Lecithin) 1. 29 Flavors (Cocoz Powder~ 10.00%
(Vanilla Powder) o. 21%

~ydrobinding Ingredient Gum Arabic 12.88%
Glycerin 2.58%
TOTAL _ 100.00%

The resulting mixture was cooled and subjected to flash~
flow pro~essing by spinning in a flash-heat apparatus operated at about 95'c and at 3,600 rpm. to produce a shearforn matrix.

~096/38049 Separately, a hydrobinding component was prepared by hydrating carrageenan according to the formula set forth in Table II B below. The ingredients in Table II B were blended thoroughly until a uniform solution was attained.

~r~Rr.r~ TT B

Ingredient Percent of composition Carrageenan 2.31%
Sucrose 2.31%
Glycerin USP (anhydrous)3.08%
Water 92.30%
TOTAL 100.00%

Finally, a confectionery mass was formed from the composition set forth in Table II C below. Shearform matrix resulting from the preparation of Table II A was combined with flavors and polydextrose, hand mixed, warmed to above room temperature, and permitted to cool.
The hydrobound carrageenan prepared as set forth above was then added to the cooled shearform matrix.

T~RTT' IT C

Ingredient Percent of Composition Shearform Matrix from IIA64.80%
Flavors (Caramel Flavor) 0.59%
(Vanilla Cream Flavor)0.26%
(Non-Fat Dry Milk) 2.59%
Hydrobound Carrageenan 11 01%
Polydextrose 20.75%
TOTAB 100.00%
A homogenous water-starved system displaying substantially no moisture separation was produced. The SIIBSIIIUIE SHEEr (RUIE 26) w096138049 2195319 ~.,l l "~

resllting mass was deposite on a ~lat surfa~e and permit_-d to set.

The resulting product was an attractive, eY~ llent tastinS candy having well-structured integri~y, which is excellent for use as a "center" for a low calorie candy bzr. ~oreover, the candy was an excellent dosage formed for delivery of the antacid ~- ~nt, e.g., calcium carbonate.

FY~MPLE III

A spun matrix was ~ormed from the compcsition set forth in Table III A below. Antacid compone~ts, corn syrups solids, sucrose, and ~lavors were blended to form a firs~ mixture. ~ydrogenated palm oil, emulsifiers and mono-glyceride were combined and melted to form a second mix-ure, and lecithin was added thereto. The second mixture was blended with the first mixture.

m~R~.F! III 7 T~grediertPercent of Composition Antacid (CaCQ3) 10.00%
Saccharides (Corn Syrup solids~38.40S
(Sucrose) 32.00%
Flavor Defatted Cocoa Powder10.00%
10-12$
~ydrogenated Palm Oil7.00%
F~ll r_~ f;e~
(Leci hin) 2.00%
(~ono-glyceride) 0.60%
TOTAL 100.00$

~ W09638049 21 '~53 1 9 .~ "-The resulting mixture W25 c_ole~ znd subjected flash-flow processing in a flash-heat apparatus having a ~-inch cable head which _as a 0.030" gap to produce a shearform matrix.

Separately, a hydrnh;n~ing --~nt was prepared by hydrating a gelatin and a gum with a glycèrin in water combination as set forth in Table III B. The resulting hydrobound mass was mixed at above room temperature until a smooth consistency was attained.
TABBF III B

IngredientPercent of Composition ~ydrobinding O -nt Gelatin Type B 2.~3%
Gum Arabic 0.43%
Water 8.00%
Glycerin 1.00%
Shearform ~atrix from87.69%
Table III A
Flavors (Vanilla) 0.05%
(Salt~ 0.10%
TOTAL 100.00%

Shearform matrix resulting from the preparation described in Table III A was combined with flavors in a mixer and warmed to above room temperature. The hydrobound mass prepared as set for h above was then added. The overall composition is set forth in Table III B.

The resulting composition was fully functional and displayed no water separation. A mass of the composition was laid out on a flat surface and rolled to a thickness of lo cm, permitted to set, and cut into bars of desired shape and size. The resulting product was a well-formed, W096~8~9 2 1 953 1 9 T~ r excellent tasting chewy nougat bar with low calorie content.
EX~P~E IV

A non-hydrated confectionery shearform matrix was prepared frcm the composition set forth in Tzble IV A
below. The resulting mixture was subjected to flash-flow processing by spinning in a flash-heat apparatus operated at about 3500 rpm. The resulting product WZ5 a non-hydrated shearform matrix. The product contained z non-hydrated hydrobinding ingredient znd other components.

~Rl'.7~ V A

Ingredient Percent o~ corposition Non-hydrated Shearform Matrix:
Saccharides (Polydextrose) 40.00%
~Powder Sucrose) 35.86%
Flavors (Vanilla) 1.00%
(Caramel) 1.00%
(Non-Fat Dried ~ilk) 6.34%
Pm~ i / iP;
(~ono- and di-glyceride es~ers) 0.25%
(Hydrogenated Vegetable Oil) 0.2~%

Antacid (Calcium Carbonate) 5.30 Hydrobinding Ingredient (Gum Arabic) 8.30%
Glyce_in 1.70%
TOTAL 100.00%

A confectionery mass composition was then prepared in accor~ance with the for~ulation set ~orth in Table IV
B. A hvdrobinding component, gum arabic, was first hy~rated with glycerin and water. The resulting W096~8049 21 9 531q P~ .'. 3' hydrobound component was mixed with the other components resulting from Table IV A and a little salt.

~T.T' IV B

IngredientPercent of Composition Non-hydrated Shearform59.75%
Matrix of Table IVA
Hydrobinding Component Carrageenan 0.25%
Glycerin 3.00%
Water 8.00%

Flavors Salt 0.25%
Densified Rice 6.75%
8ran Flakes 5.00%
Raisins 10.25%
Partially Defatted Peanuts 6.75%
TOTAL 100.00%
Rice, bran flakes, and raisins were added to the resulting mixture to form a confectionery mass which was permitted to set on a flat surface, and subsequently smoothed out to 1 1/2 inch thickness. The inclusion of particulate additives did not destroy the functional cohesiveness of the water-starved system.

The resulting product was a well-formed low fat, low calorie, caramel nougat candy bar center.

The products resulting from the invention (e.g.
Examples I-IV) are quite unique. No cooking was required to prepare the compositions set forth above.
Furthermore, the compositions did not require dehydration to arrive at the final product.

SUBSTITUTE SHEET (RUEE 26) ~096/38049 2 ~ q 5 3 1 9 F~y~upLF V

FRAPPE PRODUCT

A product was prepared in accordance wi~h the invention wherein the texture of the nougat was "shortened" to provide what has been referred to by the inventors as a "frappe" product.

A shearform matrix was prepared according to the formula set forth in Table V A.

T}~3L2: V A
.. ngredient Percent c~ Co=positio~
Corn Syrup sOlids 10.93%
Polydextrose 67.47%
Calcium Carbonate 9.44 Non-fat Dried ~ilk 11.28 Salt 0.73 ~igh Intensity sweeteners Aspar.ame 0.09%
~I--~C117 t A~ O.06%
The high intensity sweetenerS were pre~ixed with corn syrup solids and the salt, and subseguently blended with polydextrose, calcium carbonate and dry milk until a substantially uniform mix was achieved. Ihe mixture was then flash-heat Q~ocessed at about 3500 r.p.m. to produce a shearform matrix.

A hydrobinding o L was separately prepared according to the formula described in Table V B, and then aerating agents and flavor ingredients were added in accordance with the formula set for.h in Table V B.

~ W096~8049 2 1 9 5 3 1 9 . .,I ~ D

T~BLE v B
.. ~sredie3t Percent Oc compcsiticn ~Ivdrohinding rnmrnllant Carraceenan 0.18%
Wettir.g Agent (Glycerin) 3.82%
Water 10.69%

Shearform ~atrix (V A) 45.82%
Aerating Agent Soy Protein 0.46%
Flavor Vanilla 0.23%
C-eme 0.15%
Caramel 0.15%
Sugar 22.91%
Peanut 0.31%
Texture Agents De-fatted Peanuts 9.16%
C-isp Rice 3.05 Densified Crisp Rice 3.05%
Shearfor3 matrix prepared in accordance wi~h TABLE V A
was separately mixed with Texture Agents in the percentages set forth in TABLE V B.

Snhsa~lantly, the hydro_inding cnmronan., aerating and flavor agents were co~'cined with shearfonn matrix plus texture agents, and su'cjected to an aerzting whick;ng for about 15 minutes.

The resulting product was a fully functional confecticnery mass having substantially no water phase separation. The confectionery mass had an excellent flavor and shortened textured which i5 ideal for use as a low fat, low calorie nougat candy _ar center.

W096~9 2 1 9 5 3 1 q . ~ J ~

R~MPLE VI
FRAPPE PRODUCT

Another frappe product was prepared using a shearform matrix component having the formula set forth 5in TABLE VI A.
~RT.~ VI~
Ingredients Percent of Compositior Polydextrose 88.78%
Flavor Peanut Butter 7.14%
Oleaginous Coconut Oil 2.75%
Salt 1.32%
The ingredients were combined and subjected to flash-heat 15processing to produce a,shearform matrix.

The shearform matrix was then combined with the ingredients set forth in TABLE VI B (except for the solid texturi~ng ingredients peanuts and densified rice) and whipped to a stiff frappe consistency.

SUBSTITUTE SHEET (RULE 26~

W096~8049 PCT~S96/08005 ~RT,T! VI B

~ngredients Percent of Composition Hydrobinding C~ ~n~nt Protein Colloid (Gelatin)0.38%
Water 10.70%
Wetting Agent Glycerin 1.80%

Shearform Matrix (VI A) 46.63%
Aerating Agent Milk Protein 0.38%
Flavor Sweetener (Dextrose) 14.31%
Confection Sugar 2.86%
Polydextrose I 0.50%
Peanut Butter Flavor 0.50%
Texture Agents Densified Rice 10.97%
Defatted Peanuts w/1~ Salt10.97%
The texture agents were subsequently added to form an excellent nougat candy bar center which was low calorie and low fat.

LT~' VI
HF~T~TH B~R

A unique health product was prepared as a frappe product. The nougat frappe product provides the basis for a "health" bar. It can include up to at least five (5) times of the U.S. recommended human adult serving of whole vegetables and/or fruits by use of dry residue of such whole vegetables or whole fruit.

The composition of the product prepared in accordance with the invention is set forth in Table VII.

SUE STITUTE SHEET (RULE 26) 2 ~ 953 1 ~
W09~38049 Xezlt~ Bar ~A~EE VII
Inc,redientsPercant of Composition Shearform ~atrix S Polydextrose 15.00%
Corn SyruD Salids 8.50%
~on-fat Dry NilX 4.00%
Wheat Protein Concentrate 3.00%
Powde-ed Brown Sugar 5.18%
Fibe Source 4.39%
Calciun Carbonate 1.00%
Salt 0.60%
Vegetable Powder 3.84%
Fruit Powder 5.90%
Iron 0.02%
Strons Olfactory Vegetable Component Broccoli Powder 1.62%
Spinach Powder 1.24%
Yoghurt Powder 3.00%
Water 0.18%
drobinding r Gum (Visczrin and Solka Floc~ 2.75%
Glycerin 3.00%
Yoghur. Powder 3.00~
Water 8.82%
Sweeteners Fruc~ose 4.00~
Powdered Brown Sugar 5.17%
~igh Intensity Sweeteners 0.08%
Aerating Agent (Versa Whip) 0.60%
Texturizing Agent Rice Rrisples 5.37%
r ; ni n~ Ingredients Vegetable Powder 3.84%
Fruit Powder 5.90%
A shearform matrix was prepared using the ingredients ~et for~h in Table VII. The ingredients were dry mixed and spun in a flash-heat apparatus.

Also, those ingredients which have strong vegetable-olfactory notes, e.g., spinzch znd broccoli powders, were treated to reduce the strength of the olfactory notes.
Specifically, they were mixed with yoghurt powder in the ~ W096~8049 - 21 95319 r ~

presence of a trace of moisture and heated to drive off strong odor and flavor characteristics.

A hydrobinding component was separately prepared by hydrating gum and glycerin along with sweeteners and an aerating agent. The combination was blended and then whipped for three (3) minutes.

The shearform matrix and modified strong-vegetable olfactory component were added to the whipped composition. The texturizing agent and rrm-inin7 ingredients were also added and the combination was mixed by beating for two (2) minutes.

The resulting product was transferred to a flat surface at the desired thickness and allowed to set for at least two (2) hours. The resulting product was a highly nutritious health bar filling which had a pleasing flavor and excellent texture.

The product was a sweet, fibrous bar which included dehydrated fruits, vegetables, dietary fibers and minerals. The product had no fat and was very low calorie, e.g., only about 120 calories per unit.

SUBSTITUTE SHEET (RULE 26~

W096~W~9 2 1 9 5 3 1 9 . ~IIU~

BIoLoGIr~R ~rTIvI~y E~ MpLF!Q

Moreover, products which were produced in accordance with the present invention have very low water activity and very low biological activity. The industry standard is well above the biological activity level exhibited from the inventive product.

T~MPT~ VIII

A first nougat was prepareq using a shearform matrix having a formula set forth in Table VIII A.

0 ~RT.~ VIII A
IngredientsPercent of Composition Powdered Suqar 35.86%
Polydextrose 40.00%
Calcium Carbonate 5.30%
Emulsifier (mono- and di-glyceride esters 0.25%
Hydrogenated Vegetable Oil 0.25%
Gum Arabic 8.30%
Glycerin 1.70~
Flavorant 2.00%
Non Fat Dried Milk 6.34%
A feedstock composed of the ingredients set forth above was flash-heat processed at temperatures of between 81~ - 85CC and at a spin speed of 3600-~9Oo r.p.m.

The resulting shearform product was then used to prepare a nougat according to the formula set forth in Table VIII B.

SUBSTITUTE SHEET (RULE 26 T~BLE VIII B

IngredientsPercent of Co=position Shearform Matrix fro~ VIIIA 59.75 ~ydrobinding C~np~n~nts Carrageenan 0.25%
Glycerin 3.00%
Water 8.00%
Texture (and flavor) Densified Rice 6.75%
Bran Flakes 5.00%
Raisins 10.25 Partially Defatted Peanuts 6.75~
salt 0.25%
A hydrobinding conponent was prepared by mixing the carrageenan and glycerin and hydrating with the total water used in the final composition.

~ The shearform matrix and salt were then combined with the resulting hydrobinding - -nt and subjected to 16-17 ~inutes of ~ixing to functionalize the nass.
Texture ingredients were then added to the mass and folded in via low speed mixing until the inclusions were evenly coated.

The resulting mass was poured on a flat surface, rolled to a 1/2 inch t~ n~S, and pernitted to set.
The resulting product had an excellent nougat flavor and texture. A sample of the product was tested for biological activity, and the results are reported in a "Eiological Activity" Table set forth hereinafter.

E~A~E IX

A shearform matrix was prepared in accordance with the form set forth in Table IX B.

WO 96/38049 2 1 9 5 3 l ~ P~

T~B LF IX B

InsredientPercent of Compositior.
Pcwdered S~gar 34.50%
Polydextrcse 40,00%
Calciu Carconate 4.61%
Gum Arabic 7.24%
Glycerin 1.48%
Flavorant 2.60%
Cocoa Pcwder 3.26%
Ncn Fat Dried NiLk5.51~
Szlt 0.36%
Oleagincus (Butter Oil) 0.44%
A feecstcck ,-sed of the ingredients set fcrth a'ccve were flash-heat prccessed at a temperature of frcm abcut 55 C to abcut 60-C at a spin speed cf zbcut 3600 r.p .m.

The shearform ~atrix was included in a nougat produc_ prepared according to the formula se= for8h below in Table IX B.
T~B~E IX B

Ir~qredients Percent of Composition Shearform ~atrix frcm IX A 63.56%
~ydrobinding C -~t Carrageenzn 0.29%
Glycerin 3.45%
Water 9.21%
Flavors Suqar 5.00%
~igh Intensity Sweetener 0.04%
Butter Flavor 0.30%
Nalt Flavcr 0.15%
Texture Densified Rice 9.00%
Partially Defatted Peanuts 9.00%

~ W096~8049 2 1 9 5 3 1 9 r~

A hydrobinding component was prepared by combining carrageenan and glycerin and hydrating with water.

A functionalized nougat mass was then prepared by pre-combining the shearform matrix and salt, and subsequently mixing the pre-combined mixture with the hydrobinding component for 16-17 minutes. Texture ingredients were then folded in until the inclusions were evenly and thoroughly coated.

The resulting nougat mass was poured on a flat surface, smoothed to a thickness of about 1/2 inch and permitted to set. The product had an excellent flavor and texture.

A sample of the product was subjected to biological testing and the results are set forth hereinafter in the "Biological Activity" Table.

Report of BiolQgical Te~c Samples of product from Examples VIII and IX were subjected to testing to determine biological activity.
The test results are set forth below in the "Biological Activity" Ta~le.

SUBSTITUTE SHEET (RULE 26) W0 96138049 2 1 9 5 3 l 9 ~ . D~

o o a ~ ~1 ~1 o V V

.
r,o ~ _ O o o rs r~
V V U~--O
P; , , ~ .C JsJ
~ h ~ - S
R ~ ~ .rl _ H r~
V V X

r~ J r~
U O ~
V V

U ~ ..
O O
. r~ V V ' m U ~

O .~ l ~ U~ U

~3 H X I ~1 J ~ ,~

~mUlES~EE~ (~UIE26) ~ W096l38049 2 l 9 ~ 3 1 9 P~

As can be seen from the results reported in the Biological Activity Table, the biological activity is virtually non-existent. Normally, confectionery products can be expected to exhibit biological activity in the range of 300-400 ppm. The inventive samples tested displayed less than 10 colony form units per gram against standard bacteria, and negative results against Salomella.

Thus, while there have been described what are primary believed to be the preferred embodiments, those skilled in the art well appreciate that other and further changes and modifications can be made without departing from the true spirit of the invention, and it is intended to include all such changes and modifications within the lS scope of the claims which are appended hereto.

SUBSTITUTE SHEET (RULE 26)

Claims (42)

WHAT IS CLAIMED IS:

1. A method of making a confectionery mass comprising combining a shearform matrix and a hydrated hydrobinding component.

2. The method of claim 1, wherein said shearform matrix is provided by a flash-heat process.

3. The method of claim 1, wherein said shearform matrix is provided by a flash-shear process.

4. The method of claim 1, wherein said hydrobinding component has been subjected to flash-flow processing prior to hydration.

5. The method of claim 4 wherein said hydrobinding component is combined with a saccharide-based material for flash-flow processing.

6. The method of claim 5 wherein said saccharide-based material is pre-flash-flow processed.

7. The method of claim 1, wherein said hydrobinding component comprises a proteinaceous material.

8. The method of claim 7, wherein said proteinaceous material is a gelatin.

9. The method of claim 1, wherein said hydrobinding component comprises a food grade gum.

10. The method of claim 9, wherein said food grade gum is selected from the group consisting of gum arabic, carrageenan, and mixtures thereof.

11. The method of claim 1, wherein said shearform matrix is prepared from a feedstock which comprises a saccharide-based material.

12. The method of claim 11, wherein said saccharide-based material is selected from the group consisting of sucrose, corn syrup solids, polydextrose, and mixtures thereof.

13. The method of claim 12, wherein said saccharide-based ingredient is polydextrose.

14. The method of claim 11 wherein said saccharide-based material is pre-flash-flow processed.

15. The method of claim 1 wherein said hydrated hydrobinding component includes an aerating agent.

16. The method of claim 15 wherein said aerating agent is selected from the group consists of egg white, soy protein, and mixtures thereof.

17. The method of claim 1 wherein at least one biologically active ingredient is included in said mass by adding said active ingredient to one of said shearform matrix, said hydrated hydrobinding component, and said combination.

18. The method of claim 1 wherein at least one nutritional agent is included in said mass by adding said agent to one of said shearform matrix, said hydrated hydrobinding component, and said combination.

19. The method of claim 18 which further comprises reducing olfactory characteristics of at least one ingredient of said nutritional agent.

20. The method of claim 19 wherein said reducing of olfactory characteristics comprises driving off flavor and aromatic notes.

21. The method of claim 18 wherein said nutritional agent is selected from a group consisting of dry residue of whole vegetables, a dry residue of whole fruit, a source of mineral, a source of fiber, and combinations thereof.

22. The method of claim 20 wherein said agent is said dry residue of whole vegetable.

23. A confectionery mass comprising a fully functionalized hydrobound mass having substantially no phase separation of moisture.

24. The confectionery mass of claim 23 comprising a shearform matrix and a hydrobinding component.

25. The confectionery mass of claim 24 which further comprises confectionery ingredients hydrated sufficiently to provide said functionalized hydrobound mass.

26. The confectionery mass of claim 23 wherein said hydrobinding component comprises a proteinaceous material.

27. The confectionery mass of claim 26 wherein said proteinaceous material is a gelatin.

28. The confectionery mass of claim 23 wherein said hydrobinding component comprises a food grade gum selected from the group consisting of gum arabic, carrageenan, and mixtures thereof.

29. The confectionery mass of claim 23 which has a water activity of not greater than 60% ERH.

30. The confectionery mass of claim 29 wherein said water activity is not greater than about 55% ERX.

31. The confectionery mass of claim 23 which further comprises an active ingredient.

32. The confectionery mass of claim 31, wherein said active ingredient is an antacid.

33. The confectionery mass of claim 23, wherein biological activity is less than about 100 ppm.

34. The confectionery mass of claim 33, wherein said activity is less than 25 ppm.

35. The confectionery mass of claim 23 which further comprises a nutritional component.

36. The confectionery mass of claim 35 wherein said nutritional component comprises at least one ingredient which has been treated to reduce olfactory characteristics.

37. The confectionery mass of claim 23 wherein at least one nutritional agent is included in said mass by adding said agent to one of said shearform matrix, said hydrated hydrobinding component, and said combination.

38. The confectionery mass of claim 37 wherein said nutritional agent is selected from a group consisting of a dry residue of whole vegetable, a dry residue of whole fruit, a source of mineral, a source of fiber, and combinations thereof.

39. The confectionery mass of claim 38 wherein said agent is said dry residue of whole vegetable.

40. The confectionery mass of claim 23 wherein the biological activity is less than about 100 ppm.

41. The confectionery mass of claim 40 wherein the activity is less than about 25 ppm.

42. The confectionery mass of claim 41 wherein said activity is less than about 10 ppm.