CA2216875A1

CA2216875A1 - Fiber-derived colloidal dispersions and use in foods

Info

Publication number: CA2216875A1
Application number: CA002216875A
Authority: CA
Inventors: Radha Iyengar; Akiva T. Gross
Original assignee: Individual
Current assignee: Opta Food Ingredients Inc
Priority date: 1995-04-21
Filing date: 1996-04-16
Publication date: 1996-10-24
Also published as: EP0825821A1; AU5485196A; WO1996032852A1

Abstract

Fiber-derived homogeneous colloidal dispersions or gels and powders produced therefrom are described. The dispersions or gels are prepared by enzyme hydrolysis and subsequent mechanical disintegration. Food formulations comprising the stable, homogeneous colloidal dispersions, gels and powders are also described.

Description

CA 0221687~ 1997-10-20 W 096/32852 PCTrUS96/05213 FIBER-DERIVED COLLOIDAL DISPERSIONS AND USE IN FOODS

, Backqround Dietary fiber can be defined as including all the insoluble and soluble components of food that are not broken down by the digestive tract enzymes to produce low molecular weight compounds that can be readily absorbed into the blood stream. Plant cell wall materials such as cellulose, hemicellulose, lignin and pectins are the primary source of dietary fiber in human and many animal diets. The maintenance of adequate levels of fiber is important for the proper health and function of the body.
Diets high in fiber have been found to be useful in obesity control and weight reduction programs because of their high ratio of bulk to calories. For these reasons, the food and feed industries have turned to dietary fillers and bulking agents for supplying the fiber requirements demanded by the market.
Dietary fillers and bulking agents can be categorized by solubility. The soluble group includes primarily the gums, pectins and mucilages. These material can have a substantial effect on the functional properties of other food components, and therefore have limited application in many food formulations. The insoluble fillers which have played a major role in this field include alpha-cellulose and microcrystalline cellulose. Alpha-cellulose is produced by grinding ordinary, kraft paper pulp obtained by the sulfiting of hardwood. Consumer acceptance of this product has been limited to some extent by its objectionable texture and mouth ~eel. The cellulose chains of kraft pulp comprise both crystalline and amorphous regions. When treated with acid hydrolysis as described by Battista et al. in U.S. Patent No. 3,023,104, the amorphous CA 022l687~ l997-l0-20 W 096/32852 PCTnUS96/05213 regions are hydrolyzed, leaving particles of crystallite aggregates, otherwise known as microcrystalline cellulose.
Thompson et al. (U.S. Patent No. 4,307,121) discloses a method for converting relatively nonligneous cellulose material such as soybean hulls to a short fiber cellulose suitable for human consumption. The process involves heating these materials in a slurry with a strong oxidizing reagent such as chlorine gas, followed by an alkaline cook, to yield a purified cellulose product.
It has been the general view of those knowledgeable about the manufacture and applications of cellulose powder that in order to achieve an end product containing an appropriate level of cellulose microcrystals, the acid hydrolysis process described above, or minor modification thereof, should be used. Although other methods of cellulose degradation have been studied, e.g., enzymatic hydrolysis, such methods have not been considered appropriate for commercial cellulose powder production because the product does not have the desired crystallinity. Prior studies of cellulosic material have utilized enzyme hydrolysis to enzymatically convert cellulose into a soluble sugar solution and provide a practical process for cellulose utilization. Generally the aim of such studies has been to completely hydrolyze the cellulosic starting material and not to change its properties.

Summary of the Invention This invention pertains to the discovery that certain insoluble ~ibers can be converted into stable, homogeneous colloidal dispersions or gels. The gels can be dried to produce a powder with an average particle size of less than about 15~ when viewed under a light microscope. The resulting powder has a water absorption of from about 200 to about 400~ and an oil absorption of from about 100 to CA 0221687~ 1997-10-20 W 096/32852 PCTrUS96105213 about 200~. Rehydration of the powder with shear results in the formation of a colloidal dispersion or gel with characteristics similar to its never dried counterpart.
Additionally, the colloidal dispersion can be co-dried with other hydrocolloids or polymers to alter the properties of the dispersion.
The stable, homogeneous colloidal dispersions or gels are produced by treating an insoluble fiber material with a hydrolase enzyme, such as an endo-cellulase, and subsequent mechanical disintegration. The enzymatic treatment makes the fiber more susceptible to degradation when subjected to mechanical disintegration, such as by two-stage high pressure homogenization. The two step process yields a stable, homogeneous colloidal dispersion or gel which can be dried and subsequently rehydrated.
This invention also relates to the preparation of food products containing the stable, homogeneous colloidal dispersions, gels or powders, and to food formulations which comprise the colloidal dispersions, gels or powders produced by the methods detailed herein. Never dried or rehydrated colloidal dispersions or gels can be incorporated into foods and beverages to manage water activity, to increase bulk and to decrease caloric value.
For some food formulations, a powder resulting from the drying o~ the colloidal dispersion or gel can be used directly in foods without prior rehydration. The colloidal dispersions or gels and powders of the present invention are suitable for use in food formulations which would benefit ~rom a reduced particle size and low water and oil absorption. Some examples of suitable food formulations include, but are not limited to, chocolate, frostings, spreads, yogurt, cream fillings and peanut butter, juices, extruded ~oods, meats, and dairy products such as natural and processed cheese.

CA 0221687~ 1997-10-20 W 096/32852 PCTrUS96/05213 Detailed Descri~tion of the Invention The present invention pertains to a stable, homogeneous colloidal dispersion or gel which can be dried to produce a powder. The powder has a reduced particle size (an average o~ less than about 15 ~ compared to 300-400 ~ o~ the starting material) and reduced water or oil absorption compared to the starting material. The powder can be rehydrated in the presence o~ shear to give a product with characteristics similar to the never dried colloidal dispersion or gel. Additionally, the stable, homogeneous colloidal dispersion or gel can be co-dried with other hydrocolloids or polymers to alter the properties o~ the dispersion.
The never dried or rehydrated stable, homogeneous colloidal dispersions or gels and powders there~rom can be incorporated into food ~ormulations to increase bulk, decrease caloric value and yield superior organoleptic properties, taste and mouth ~eel. Terms used herein have their art-recognized meAn;ng unless otherwise indicated.
Stable, homogeneous colloidal dispersions or gels are produced by treating an insoluble fiber material with a hydrolase enzyme, such as an endo-cellulase, and subsequent mechanical disintegration. The enzymatic treatment makes the fibers more susceptible to degradation when subjected to mechanical disintegration, such as by two-stage high pressure homogenization. The two step process yields a stable, homogeneous colloidal dispersion or gel which can be dried and subsequently rehydrated.
Various grades and ~orms o~ insoluble ~iber can be used as the starting material in the process o~ the present invention. Such materials include natural ~iber sources as well as products derived ~rom microbial sources such as fermentation. The insoluble ~iber can contain cellulose and hemicellulose, and can also contain a small percentage o~ lignin, pre~erably less than about 10 percent. For CA 0221687~ 1997-10-20 W 096/32852 PCT~US96/05213 example, the fiber can be derived from partially or fully delignified oat hulls, such as OPTATM Oat Fiber 770 (U.S.
Patent No. 5,023,103). The insoluble fiber can also be derived from various seed plant materials including cotton seed fiber, oat hulls, pea hulls, corn hulls, peanut hulls and stems, wood, straw, wheat fiber, sugar beet fiber, rice fiber and other similar materials. Preferably, the fiber is derived from a non-woody source. The raw starting material can be pretreated in order to remove hemicellulose and lignin and increase the enzymatic reactivity of the material. Such pretreatment methods include but are not limited to steam explosion, swelling with alkaline agents, acid treatment, ammonia treatment, delignification and grinding. The fiber can be dried or can be used in wet form such as undried pulp, pulp slurry or other hydrated form.
According to the method of the present invention, the insoluble fiber material is first treated with a hydrolase enzyme under conditions which effect hydrolysis. A
preferred enzyme is an endo-enzyme, particularly an endo-cellulase. Enzymes from various sources are suitable for use in the present invention to effect hydrolysis of the cellulose material in the fiber. Suitable sources include commercial cellulase preparations and enzymes derived from cultured native microorganisms or recombinant microbial sources. These include commercial preparations of cellulase which are combinations of several enzymes that have both endo-cellulase and exo-cellulase activity, as well as cellulases which have been enriched with particular components having endo-cellulase activity or modified to reduce or remove the exo-cellulase activity. Endo-cellulase activity selectively hydrolyzes the amorphous regions of the cellulose, while exo-cellulose activity acts to remove the crystalline portions and, thus, is less desirable. A rich source of cellulase is the organism CA 0221687~ 1997-10-20 W 096/32852 PCTrUS96/05213 Trichoderma lonqibrachiatum (formerly known as T. reesi), and several commercial preparations are available that have enriched endo-cellulase activity. For example, MULTIFECT~
Cellulase GC (Genencor International, Inc., Rochester, NY) or ECONASE~ CE (Enzyme Development Corp., New York, NY) can be used to hydrolyze the cellulose in the insoluble fiber.
Additionally, the cellulase enzyme may be produced by actinomyces, bacteria, ~ungi or yeast. Enzymes from different sources will normally dif~er in their ability to hydrolyze di~erent forms of cellulose.
The cellulase enzyme can also be combined with other enzymes which have a particularly desired activity. For example, the cellulase enzyme can be combined with a xylanase enzyme, which hydrolyzes hemicellulose, and/or with a peroxidase or laccase enzyme, which oxidize lignin, and/or with a ligninase enzyme, which hydrolyzes lignin.
The preferred concentration of enzyme is from about 100 ppm to about 5000 ppm of enzyme where the insoluble fiber is present at a concentration of from about 0.25 g/1 to about 200 g/1, and preferably ~rom about 0.25 g/1 to about 120 g/1, depending upon the starting material and the degree of hydrolysis to be effected.
The enzymatic hydrolysis step should be carried out in the presence of a suitable buffering system. A pre~erred buffering agent is citrate-phosphate or citric acid at from about pH 4.5. Other suitable bu~fers with appropriate pH
characteristics can also be selected based upon the particular enzyme used. Commercial bu~fer systems utilizing a pH probe can also be used to maintain the pH at a stable level in the desired range. The enzymatic hydrolysis step can be expedited by changing the buffer every 2 to 3 hours in order to reduce the end product inhibition of the reaction resulting ~rom the short chain polymers produced by the reaction. Alternatively, any method which removes the short chain polymers or low CA 0221687~ 1997-10-20 W 096/32852 PCTrUS96/05213 molecular weight compounds in the solution can be utilized to increase the efficiency of the enzymatic hydrolysis ~ reaction.
The enzymatic hydrolysis step should also be carried out at a temperature ranging from about 35~C to about 75~C, with from about 40~C to about 60~C being the preferred range. Higher or lower temperatures may be utilized as long as the activity of the enzyme is not adversely affected.
The reaction time for enzymatic hydrolysis of the cellulose in the fiber will vary depending on the identity of the starting material, enzyme and other reaction conditions; however, in general an appropriate degree of hydrolysis can be achieved in from about 5 to about 72 hours. As used herein, the degree of hydrolysis is considered appropriate when 11 to 15~ (w/w) of the starting material assays as glucose using an enzyme-linked membrane on a YSI Model 2700 Select Biochemical Analyzer. An appropriate degree of hydrolysis can also be determined by monitoring the effects of attrition or mechanical disintegration on the reaction product. If the level of hydrolysis is appropriate, subsequent high shear of the enzymatically-treated fiber results in disruption of the long strands of fiber into amorphous thread-like material projecting from the fiber when viewed under a phase contrast light microscope at lOOx magnification.
Additionally, any degree of enzymatic hydrolysis which, when followed by high shear, results in a stable, homogeneous colloidal dispersion or gel is appropriate.
The enzymatic hydrolysis step is followed by mechanical disintegration to disrupt the fiber. The concentration of enzyme-treated fiber prior to mechanical disintegration should be at least 2% by weight, with at least 5~ by weight being preferred. Mechanical shear or disintegration can be carried out in several ways. For CA 0221687~ 1997-10-20 W 096132852 PCT~US96/05213 instance, the material can be subjected to attrition in a mill, or to high speed cutting action, or to high pressure on the order of at least 2000 psi. For instance, a two- -stage Gaulin homogenizer or POLYTON~ Homogenizer can be used. The shear is carried out in the presence of a liquid medium, although when very high pressure alone is used the liquid medium may not be necessary. Water is the preferred medium, but other, preferably edible, liquids are suitable, including but not limited to sugar solutions, polyols (e.g., glycerol), milk, and alcohols (e.g., ethanol). A
preferred method of shear is the use of a two-stage Gaulin homogenizer in the presence of an aqueous medium.
Using an appropriate method, shear is carried out to such an extent to form a stable, homogeneous colloidal dispersion or gel in the aqueous medium in which the enzymatically-treated fiber is sheared. The phrase "stable, homogeneous colloidal dispersion~ is intended to mean a dispersion from which the product will not settle out but will remain suspended indefinitely under storage conditions, even for weeks or months. The stable, homogeneous colloidal dispersions or gels are further characterized by their ability to form extremely adherent films when deposited on a glass panel or sheet or other suitable surfaces. At lower solids concentration the product exists as a dispersion, while at higher solids concentrations it is a gel.
The sheared product having 35~ solids or greater, although not a gel, will easily form a gel upon manual stirring with water. The stable, homogeneous, colloidal dispersions and gels described herein are free of layers or sedimentation; instead, the stable dispersions and gels are uniform and homogeneous throughout, having a uniform color and a smooth mouth feel. The preferred dispersions and gels are those that are stable for at least a week, and the most preferred are stable for a month or longer.

CA 022l687~ l997-l0-20 W 096132852 PCTnUS96/05213 Dispersions and gels that are stable for at least an hour to a day are also useful for some purposes, as they can be - used immediately.
Generally, the concentration of the fiber particles stably suspended in the homogeneous colloidal dispersion is at least 3~ by weight, and more preferably, 4~ to 5~ by weight. However, stable dispersions having solids content of up to about 6~ to 8~ by weight can be made. In some food formulations, lower use levels can also have benefits.
The concentration of fiber particles in the gel will be limited or determined by the handling conditions for the gel. The gels are usually thixotropic in nature when they contain 5~ to 10~ solids.
Either before or after mechanical disintegration of the enzymatically-treated fiber, the gels or suspensions can optionally be dried to any practical moisture content in which state they are redispersible in water, with the aid of a suitable attrition step, to reform a colloidal dispersion or gel. The resulting dispersion or gel can again be dried if desired, and again redispersed. When the attrition step is performed in an aqueous medium, drying is preferably carried out after the disintegration step.
Drying can be carried out under vacuum, or in air at room temperature or higher. Another useful drying method is displacing the water in the enzymatically-treated fiber by means of a low boiling point water miscible organic compound, such as a low molecular weight aliphatic alcohol (e.g., ethanol or methanol). Some drying procedures are more advantageous than others because the dried product re-disperses more easily. For example, freeze drying, spraydrying, drum drying and drying by solvent displacement produce a powder which is more easily re-dispersed in water, compared with a similar powder produced by oven drying or air drying.

CA 0221687~ 1997-10-20 W 096J328S2 PCTrUS96/05213 As described above, the method for making stable, homogeneous colloidal dispersions or gels and powders is completely carried out prior to the incorporation of the fiber into the food formulations. However, the final mechanical disintegration step can be performed in situ during the preparation of a wide range of foods and beverages. According to this embodiment, the ingredients of the food product are added to the slurry containing the enzymatically-treated fiber material. The mixture is then subjected to mechanical disintegration, attrition or high shear. The attrition process disrupts the enzymatically-treated fiber and produces a food product containing a stable, homogeneous colloidal dispersion or gel. Producing foods containing the colloidal dispersions or gels of the present invention in a single stage operation provides a cost advantage from a manufacturing standpoint. In addition, there may be some product advantages which result from the single stage operation. The properties of the products from the single stage operation are indistinguishable ~rom the properties of the corresponding product, prepared from the same ingredients, in which the colloidal dispersion or gel is separately prepared. This process is useful for producing fillings, soups, gravies, toppings, beverages and other food products.
The organoleptic properties of the stable, homogeneous colloidal dispersion or gel can be altered by the addition of hydrophilic polymers such as cellulose esters or ethers (e.g., carboxymethyl cellulose, methyl cellulose), gums and starches. A small amount o~ such a hydrocolloid can vary the mouth feel and texture of the resulting fiber-derived product. The amount of the hydrocolloid can range from about 0.1~ to about 30~ by weight, with about 5~ being preferred. Suitable gums and polymers include but are not limited to guar gum, gum arabic and locust bean gum and hydrocolloids such as carrageenan, agar and alginate. The CA 0221687~ 1997-10-20 W O 96/32852 PCTrUS96/05213 polymers can be added to the enzymatically-treated fiber before or after the mechanical disintegration step. The - step at which the polymer or polymers should be added will be dictated by the properties of the hydrocolloid.
Addition of the hydrocolloid to the liquid suspension o~
the fiber material prior to mechanical disintegration can prevent de-watering of the fiber under high pressure and allow the slurry to be homogenized at higher slurry concentrations. However, certain hydrocolloids or polymers, such as guar gum or xanthan gum, may result in an undesirably high viscosity of the mixture if added prior to shearing, and, thus, should be added to the product after mechanical disintegration.
The colloidal dispersions or gels and powders of the present invention are suitable for use in food formulations which would benefit from a reduced particle size and low water and oil absorption. For example, the products of this invention are suitable as bulking agents in low fat/low sugar foods which rely on low water activity for microbial preservation. The small size of the fiber particles also make them suitable for use in beverages because they are readily suspended in solution and are virtually undetectable in the mouth. Furthermore, the colloidal dispersions, gels and powders of this invention facilitate the manufacture of food products that are fiber-~ortified. The colloidal dispersions, gels and powders can be used in ready-to-drink beverages, yogurt, cream fillings, peanut butter, among other food formulations.
The colloidal dispersions, gels and powders are also suitable for use in bakery products including but not limited to breads, cakes, cookies, biscuits, pies, doughnuts; snack items, such as pretzels; pastries and other specialtiesi prepared mixes for making any of the above-mentioned products; and in cereals and pasta products. Baked goods contain predominantly starch. It is CA 0221687~ 1997-10-20 W 096t32852 PCTrUS96/05213 possible to replace the ~lour and reduce the caloric content o~ the baked products without e~fecting the organoleptic properties o~ the product by using the colloidal dispersions or gels and powders. Cakes and cookies prepared with the products of~ this invention retain moisture and help to prevent the staling o~ the baked goods.
The ~iber-derived product o~ this invention can be incorporated into ~oods containing predominantly carbohydrates such as sugars and starches; for example, the product can be incorporated into puddings, custards and toppings and dry mixes ~or preparing the same. In the case o~ dry mixes, the ~iber-derived product helps to retain the aqueous or oily ingredients, thereby preventing leaching o~
the liquid or absorption o~ the liquid onto the walls o~
the package containing the mix.
The products of this invention can be used in ~oods such as dressings and spreads which are prepared with ~ats and oils. Besides reducing the caloric content o~ the product, the ~iber-derived product assists in preventing syneresis while providing a desirable thickening e~ect.
In reduced ~at/reduced sugar low water activity systems such as peanut butter and cream fillings, the low oil and water holding capacity provides a desired thickening e~ect without a deleterious increase in ~irmness typical of most ~ood polymers.
In meat products such as sausages, sausage products and meat loa~, the texture, juiciness and other organoleptic characteristics are improved by the use o~
products o~ this invention. In the preparation o~ sausage products and meat loa~, the addition o~ the product helps to simplify the processing steps by making the meat emulsion and meat mixers easier to handle.
Ancther ~ood application ~or the products o~ this invention is in dairy ~ood products, such as natural and CA 0221687~ 1997-10-20 W 096/32852 PCTrUS96/OS213 processed cheese and in foods using milk and cream. No-fat natural cheese can be produced by dispersing the product into milk before the culturing and renneting steps. The fiber-derived product may function as a fat mimetic by partitioning into the curd and increasing the yield as well as softening the texture.
The fiber-derived products are also suitable for confections including candy, chewing gum, bakers confections and similar products. In candy, the colloidal dispersions, gels or powders can be used to deliver colors by absorption of edible dyes. In chewing gum, the fiber-derived product can be used as a carrier for the flavors.
Other foods in which the fiber-derived product may be incorporated include gravies, sauces, jellies, beverages and similar foods. The thickening effect of the product is particularly advantageous for products such as gravies and sauces.

The invention will be further illustrated by the following non-limiting examples:

EXAMPLES

Pilot Scale Production of a Stable, Homoqeneous Colloidal Dispersion or Gel A total of 30 liters of buffer (100 mM citrate-phosphate, pH 4.5), was placed in a jacketed ribbon blender DRB-5 (American Process Systems, Gurnee, IL) with 60~C
water recirculating through the jacket. The cellulase enzyme (200 ml, MULTIFECT~ Cellulase GC, Genencor International, Inc., Rochester, NY) was added to the bu~fer and mixed. Then 3 kilograms of OPTA~ oat fiber 770 (Opta Food Ingredients, Inc., Bedford, MA) was added. The mixture was agitated by the blender mixing blades and the temperature maintained at 60~C throughout the enzymatic CA 0221687~ 1997-10-20 W 096/32852 PCTrUS96/05213 reaction. The reaction was ~ollowed by periodically removing 10 ml aliquots and (i) assaying ~or glucose and (ii) shearing the sample. The ~iber/buf~er suspension was centri~uged at approximately 1400 g ~or 5 minutes. The supernatant was assayed ~or glucose using a YSI model 2700 Select Biochemical Analyzer (Yellow Springs instrument Co., Inc., Yellow Springs, OH). The reaction was complete when 11-15~ (w/w) assayed as glucose. The remainder o~ the ~iber was resuspended in water and homogenized with a POLYTON~ Homogenizer (Brinkmann Instruments Inc., Westbury, NY) at 24,000 rpm ~or 5 minutes. The ~iber was examined under a light microscope (Olympus BH-2 with Optimus image analyzer) with phase contrast at 100x magni~ication. As the reaction progressed, the long strands of ~iber were disrupted into amorphous thread-like material projecting ~rom the ~iber. A~ter 46 hours, when the long ~iber strands could no longer be seen, the reaction was complete.
The ~iber suspension was heated to 70~C to irreversibly inactivate the enzyme. The ~iber was centri~uged and washed with excess water. The washed ~iber was resuspended in water at approximately 5-6~ solids by weight and then homogenized using a two-stage Gaulin Homogenizer 15MR-8TBA (APV Gaulin Inc., Wilmington, MA) at 5000 to 6000 psi, 2 passes. The overall yield o~ the ~iber was approximately 70~. The homogeneous colloidal disperion or gel was then spray dried (APV Crepaco, Tonawanda, NY) using an inlet temperature o~ 340-350~F (170-176~C) to give a ~ine powder.

-- =
CA 022l687~ l997-l0-20 W 096l32852 PCTrUS96/05213 EX~MPLE 2 Characterization of a Stable, Homoqeneous Colloidal DisPersion or Gel A. ComPositional Analysis Cellulose, hemicellulose and lignin determinations were conducted at Hazelton, Wisconsin. The methods used have been developed for the characterization of forages and feeds. They involve the determination of neutral detergent fiber (NDF; USDA Forage and Fiber Analysis, Agriculture 10 Handbook X379 (1970); American Association of Cereal Chemists, 8th Edition (1983) Method 32.20, (modified)), acid detergent fiber (ADF; Forage and Fiber Analysis, Agriculture Handbook #379. 8, United States Department of Agriculture (1970) (modified)) and acid detergent lignin 15 (ADL; USDA Forage Fiber Analysis, Agriculture Handbook X379 (1970) (modified)) by different boiling detergent treatments followed by gravimetric analysis. From the values obtained, the cellulose and hemicellulose content of the spray dried fiber are calculated as follows (see Table 1):
NDF - ADF = Hemicellulose (~) ADF - ADL = Cellulose (~) ADL = Lignin (~) Table 1 Compositional AnalYsis Sample Cellulose (%) ~ c~lulose (%) T~ (%) OPTA~ Oat Fiber 770 76.0 12.3 0.1 Enzyme-Modi~ied Sheared 78.9 5.4 0.1 OPTA~ Oat Fiber 770 (Spray Dried Powder, Example 1) CA 022l687~ l997-l0-20 W 096/32852 PCTrUS96/05213 B. Water AbsorPtion The water absorption (percent by weight) was determined by a modification of American Association of Cereal Chemists Method 88-04 (see Table 2). Instead of using 5 grams of the test fiber and centrifuging at 2000 g, 3.0 grams of the fiber was centrifuged at 1450 g and spray dried as described in Example 1.

C. Oil AbsorPtion The determination of the oil absorption (percent by weight) of the fiber was identical to that described in method B except that store bought Wesson vegetable oil was used instead of water (see Table 2).

Table 2 Water and Oil Absorption of a Spray Dried Powder Prepared from a Stable, Homoqeneous Colloidal Dispersion or Gel Sample Water Oil Absorption AbBOrptiOn (%)(%) OPTA~ Oat Fiber 770625 + 6.0 496 + 8.2 Enzyme-Modified 372 + 2.4 104 + 3.8 Sheared OPTA~ Oat Fiber 770 (Spray dried powder, Example 1) D. Liqht Microscope The fiber was suspended in water and an aliquot mi ned under the light microscope using phase contrast and 100x magnification. The OPTAW Oat Fiber 770 had long thin strands with an average length of 300 - 400 ~. The spray dried powder had an average particle size of 10 with an occasional particle of 50 to 60 ,LL.

CA 0221687~ 1997-10-20 W 096/32852 PCTrUS96/05213 E. SuspendabilitY
The suspendability of the fiber was determined by placing 2 grams of spray dried powder (as prepared in ~: Example 1), or a homogeneous colloidal dispersion prepared by rehydrating the spray dried powder, in a 100 ml graduated cylinder. After the addition of water up to the 100 ml mark, the cylinder was placed in a Branson bath sonicator and sonicated until a steady packed volume was obtained. The cylinder was then removed and the volume of the packed fiber was recorded (see Table 3). The number of inversions by hand required to completely free the packed fiber and create a free-flowing suspension was also noted.

Table 3 Suspendabilitv of the Fiber 15Sample Volume }'.fter Nu~nber of Inversion~;
Sonication (ml) OPTA~ Oat Fiber 770 l9 32 Enzyme-Modi~ied Sheared OPTA~ Oat Fiber 770 20 over lOO
(Spray Dried Powder, 20Example l) Sheared Enzyme-Modified Sheared OPTA~ Oat Fiber 75 To free 85~:

(Homogeneous Colloidal To free lOO~:
25Dispersion, Rehydrated) 85 Bench Scale Production of a Stable, Homoaeneous Colloidal Dispersion or Gel Usinq MULTIFECT~ Cellulase GC
200 gralTls of OPTATM Oat fiber 770 or 780 (Opta Food Ingredients, Inc., Bedford, MA) was added to buffer (5mM

CA 0221687~ 1997-10-20 W 096/32852 PCTrUS96/05213 citrate-phosphate, pH 4.5) containing 13.4 ml MULTIFECT~
Cellulase GC. The mixture was then incubated in a shaking water bath at 60~C. A~ter 2-3 hours, the ~iber suspension was ~iltered and the ~iber resuspended in fresh bu~er, and the incubation continued at 60~C. The reaction was monitored as described in Example 1. A~ter a total oE 6- 8 hours with 2 bu~er changes, the enzymatic reaction was complete. The fiber suspension was heated to 70~C to irreversibly inactivate the enzyme. The ~iber was centri~uged and washed with excess water. The washed ~iber was resuspended in water at approximately 5-6~ solids by weight and then homogenized using a two-stage Gaulin Homogenizer (APV Gaulin Inc., Wilmington, MA) at 2000 to 3000 psi, 2 passes. The overall yield of the ~iber was approximately 70~. The homogeneous colloidal dispersion or gel was then spray dried (APV Crepaco, Tonawanda, NY) using an inlet temperature o~ 340-350~F (170-175~C) to give a ~ine powder.

Bench Scale Production o~ a Stable, Homoqeneous Colloidal Dispersion or Gel Usinq ECONASE~ CE
Two hundred grams o~ OPTA~ Oat Fiber 770 or 780 (Opta Food Ingredients, Inc., Bed~ord, MA) was added to bu~er (5mM citrate-phosphate, pH 5.0) containing 13.4 ml ECONASE~
CE (Enzyme Development Corp., New York, NY). The mixture was then incubated in a shaking water bath at 50~C. The rest o~ the experiment was identical to that described in Example 3.

sench Scale Production o~ a Stable, Homoaeneous Colloidal Dispersion or Gel Usina MULTIFECT~ Cellulase GC
This experiment was identical to that described in Example 3 except that the ~iber was not sheared a~ter the CA 0221687~ 1997-10-20 W 096/32852 PCT~US96/05213 enzymatic reaction was completed. The enzyme-modified fiber was air-dried to give very hard rock-like pellets.
The hard rock-like material was ground to a fine powder using a ~Amme~mill followed by a milling using a Retsch Ultra Centrifugal Mill ZM-1 (Brinkmann Instruments, Inc.) equipped with a 0.12 mesh screen. Alternatively the filter cake was reslurried into ethanol and rinsed to remove any water. The fiber was air-dried and then ground in a Retsch Ultra Centrifugal Mill to give a fine powder.

Bench Scale Production of a Stable, Homoqeneous Colloidal Dispersion or Gel Usinq Wet Fiber as the Startinq Material This experiment was identical to that described in Example 3 except that wet fiber was used as the starting material. The product was the same as that produced in Example 3.

Preparation of Co-Dried HYdrocolloids and Stable, Homoqeneous Colloidal Dispersion or Gel A. Guar Gum Guar gum (Germantown, Broomall, PA) was prehydrated in water and added to the sheared colloidal dispersion prepared as described in Example 1. The concentration of the guar gum was 5~ that of the fiber (w/w). The resulting mixture was then spray dried as described in Example 1.

B. CarboxvmethYl Cellulose Carboxymethyl cellulose (FMC Corp., Philadelphia, PA) was prehydrated in water and then added to the sheared colloidal dispersion prepared as described in Example 1.
The concentration of the carboxymethyl cellulose was 10~
- that of the fiber (w/w). The resulting mixture was then spray dried as described in Example 1.

, CA 022l687~ l997-l0-20 W 096/32852 PCTrUS96/OS213 Preparation of Sheared Fiber Without Enzymatic Treatment OPTATM Oat Fiber 770 or 780 (Opta Food Ingredients, Inc., Bedford, MA) at 6~ by weight solids in water was sheared using a Gaulin Homogenizer (APV Gaulin Inc., Wilmington, MA) at 5000 to 6000 pSi. A sample of the fiber was sheared further using a Microfluidizer (Microfluidics International Corp., Newton, MA). The resulting fiber was lyophilized to dryness and then ground in a Retsch Ultra Centri~ugal Mill ZM1 (Brinkmann Instruments, Inc., Westbury, NY). Table 4 shows that the water absorption o~
the fiber increased slightly with the number of passes through the Gaulin homogenizer. After homogenization, the product was more colloidal in nature and had the same or increased water absorption as compared with the product of enzyme hydrolysis ~ollowed by high shear treatment (Example 1) .
Table 4 Water AbsorPtion as a Function of Shear Gaulin Treatment Water Absorption 0 passes 593 2 passes 568 5 passes 600 10 passes 620 15 passes 620 20 passes 634 5 passes Gaulin, 3 730 passes Microfluidizer 30 Peanut Butter The spray dried powder prepared as described in Example 1 was incorporated into a peanut butter spread;
percents listed are percent by weight.

CA 0221687~ 1997-10-20 W 096/32852 PCTrUS96/05213 Formulation:
Ingredients SAMP~ES
A B C D E

SKIPPYW Peanut Butter 70 70 92.19 92.19 100 MALTRIN~ M-520 (Grain 30 20 0 0 0 5 Processing Corporation) Spray dried powder 0 10 7.81 0 0 (Example 1) OPTA~ Oat Fiber 770 (Opta 0 0 0 7.81 0 Food Ingredients, Inc.) The peanut butter was heated to 170~F (76~C) by placing in a conventional oven. The warmed peanut butter and the rest of the ingredients were placed in a bowl of a mini food processor (SUNBEAM OSKAR~). The ingredients were blended until uniformly dispersed using maximum shear (2-3 minutes). The mixture was cooled to 95-100~F (35-37.8~C) before filling containers.
The samples were paneled by 3 expert tasters. The samples A and C were most similar to the peanut butter control (Sample E).

Chocolate Drink The spray dried powder prepared as described in Example 1 was incorporated into a ready-to-serve chocolate drink; percents listed are percent by weight.

CA 0221687~ 1997-10-20 W 096/32852 PCTnUS96105213 Formulation:
Ingredient~ SAMPLES
A (~) B (~) C (~) Whole milk 91.975 90.935 90.935 Granulated sugar 7.0 7.0 7.0 Carrageenan (Seakem 0.025 0.025 0.025 CM 611, FMC Corp) Cocoa powder (De Zaen 1.0 1.0 1.0 D-ll-ASOL) OPTA~ Oat Fiber 770 0 0 1.04 (Opta Food Ingredients, Inc.) Spray dried powder 0 1.04 0 (Example 1) The cold milk and all the dry ingredients were blended in a kitchen blender at a high speed ~or 5 minutes. The mixture was then pasteurized at 195~F (90~C) ~or 60 seconds ~ollowed immediately by homogenization in a two-stage Gaulin Homogenizer 15MR-8TBA (APV Gaulin Inc., Wilmington, MA) at 2500/500 psi. The drinks were then trans~erred to capped containers and quickly cooled to 40~F (5~C) Samples were held at 40~F (5~C) ~or at least 24 hours before analysis.
The samples were subsequently paneled by 3 expert panelists. The sample containing the spray dried powder (Sample B) was very similar in smoothness and overall textural pre~erence to the control (Sample A). Sample C
was less smooth relative to Sample A and B and also showed some settling o~ the ~iber.

CA 0221687~ 1997-10-20 W 096132852 PCTrUS96/05213 No-Fat Yoqurt The spray dried powders prepared as described in Examples 1 and Example 7A were used to prepare no-fat yogurts; percents listed are percent by weight.

Formulation:

Ingredients SAMPLES
A (~) B (~) C (~) Water 86.25 86.25 86.25 Non-fat milk 10.50 10.50 10.50 Granulated sugar 3.25 3.25 3.25 Spray dried powder 0 1.1 0 (Example 1) Spray dried powder 0 0 1.4 with guar (Example 7A) The water was heated to 200~F (93~C) and trans~erred to a standard kitchen blender. The other dry ingredients were added as a blend and sheared on high speed ~or 2 minutes. The mixture was then pasteurized by holding at 185~F (88~C) ~or 30 minutes and then homogenized in a two-stage Gaulin Homogenizer 15MR-8TBA (APV Gaulin Inc., Wilmington, MA) at 2500/500 psi. A~ter homogenization, the mixture was cooled to 104~F (42~C) and inoculated with the yogurt starter culture 653 (Marshall Products, Wisconsin), incubated at 104~F (42~C) for 6 hours and then stored at 50~F (10~C).
Sample B, containing the spray dried powder, had the least amount o~ decantable serum and syneresis. It was superior in stir down and ~at-like sensory qualities relative to the other two samples.

CA 0221687~ 1997-10-20 W 096/32852 PCTnUS96/05213 Equivalents Those skilled in the art will recognize, or be able to ascertain, using no more than routine experimentation, many 7 equivalents to the specific embodiments of the invention described herein. Such equivalents are intended to be encompassed by the following claims.

Claims

The invention claimed is:

1. A stable, homogeneous colloidal dispersion or gel, derived from an insoluble fiber material that has been subjected to a hydrolytic method consisting essentially of treatment with a hydrolase enzyme and then subjected to mechanical disintegration, having low water absorption or low oil absorption.

2. The colloidal dispersion or gel of Claim 1 wherein the insoluble fiber material is derived from partially or totally delignified wood, oat hulls, pea hulls, corn hulls, peanut hulls and stems, cotton seed fiber, straw, wheat fiber, sugar beet fiber or rice fiber.

3. A powder produced by drying a stable, homogeneous colloidal dispersion or gel, derived from an insoluble fiber material that has been subjected to a hydrolytic method consisting essentially of treatment with a hydrolase enzyme and then subjected to mechanical disintegration, having an average particle size of less than about 15 µ and having low water absorption or low oil absorption.

4. The powder of Claim 3 having a water absorption of from about 200 to about 400% and an oil absorption of from about 100 to about 200%.

5. The powder of Claim 3 wherein the insoluble fiber material is derived from partially or totally delignified wood, oat hulls, pea hulls, corn hulls, peanut hulls and stems, cotton seed fiber, straw, wheat fiber, sugar beet fiber or rice fiber.

6. A food formulation comprising a stable, homogeneous colloidal dispersion, gel or powder, said powder having an average particle size of less than about 15 µ and having a low water absorption or low oil absorption, derived from an insoluble fiber material that has been subjected to a hydrolytic method consisting essentially of treatment with a hydrolase enzyme and then subjected to mechanical disintegration.

7. The food formulation of Claim 6 wherein the insoluble fiber material is derived from partially or totally delignified wood, oat hulls, pea hulls, corn hulls, peanut hulls and stems, cotton seed fiber, straw, wheat fiber, sugar beet fiber or rice fiber.

8. The food formulation of claim 6 wherein the food is a low water activity food.

9. The food formulation of Claim 6, wherein the food is selected from the group consisting of a meat product, a dairy product, a baked good, a dressing, a spread, a confection and a beverage.

10. The food formulation of Claim 6 which is a peanut butter, yogurt, chocolate, frosting or cream filling, gravies, sauce, jelly, candy, chewing gum.

11. A stable, homogeneous colloidal dispersion or gel having a low water absorption or low oil absorption produced by a process, said process comprising the steps of:
a) subjecting an insoluble fiber material to a hydrolytic method consisting essentially of treatment with a hydrolase enzyme, to hydrolyze cellulose present in the fiber; and b) subjecting the product of step a) to mechanical disintegration, thereby producing the stable, homogeneous colloidal dispersion.

12. The colloidal dispersion of Claim 11 wherein the insoluble fiber material is derived from partially or totally delignified wood, oat hulls, pea hulls, corn hulls, peanut hulls and stems, cotton seed fiber, wheat fiber, sugar beet fiber or rice fiber.

13. The colloidal dispersion of Claim 11 wherein the hydrolase enzyme is an endo-cellulase.

14. A method of making a food formulation comprising a stable, homogeneous colloidal dispersion or gel, derived from an insoluble fiber material that has been subjected to a hydrolytic method consisting essentially of treatment with a hydrolase enzyme and then subjected to mechanical disintegration, comprising the steps of:
a) adding an insoluble fiber material that has been subjected to a hydrolytic method consisting essentially of treatment with a hydrolase enzyme to a food formulation and b) subjecting the product of step (a) to mechanical disintegration to decrease particle size of the enzyme-treated fiber material, thereby producing a food formulation containing a stable, homogeneous colloidal dispersion or gel having low water and oil absorption properties.

15. A process of preparing a food formulation comprising incorporating therein the stable, homogeneous colloidal dispersion or gel of Claim 1.