AU661869B2 - Extruded foods containing high amylose starch - Google Patents

Description

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AUSTRALIA

Patents Act 1990 a.

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a *e 0a a S a a aft a t a St *4 I a a It COMPLETE SPECIFICATION STANDARD PATENT Applicant(s): NATIONAL STARCH AND CHEMICAL INVESTMENT HOLDING

CORPORATION

Invention Title: EXTRUDED FOODS CONTAINING HIGH AMYLOSE STARCH The following statement is a full description of this invention, including the best method of performing it known to me/us: sa a a a t,~ Ia a. a

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a SI) EXTRUDED FOODS CONTAINING HIGH AMYLOSE STARCH This invention relates to semi-moist or dry, low water activity, extruded foods which have been formulated to contain hot or cold water soluble high amylose starch, comprising at least 65% amylose. This starch is selected from a spray-dried, non-granular, high amylose starch, characterized in that the starch is substantially non-crystalline, substantially non-retrograded, and fully predispersed; or a spray-dried, uniformly gelatinized, high amylose starch in the form of granular indented spheres, with at least a majority of the granules being whole and unbroken, these starch granules being in the form of a .9 loosely-bound agglomerates or individual granules; or an enzymatically debranched, soluble starch, comprising at least 65% amylose; or an dC enzymatically debranched, gelatinized starch, comprising at least 65% crystalline short chain amylose; or a pre-extruded, fully predispersed high amylose starch; or a combination thereof. These starches are soluble in either hot or cold water, or both.

As used herein, "soluble" means that the high amylose starches in powdered form may be readily hydrated and dispersed in hot or cold water'or other aqueous medium to provide a starch solution in the form of a complex colloidal dispersion, rather than a true molecular solution. Crystalline short chain amylose starch preparations are soluble only in hot water.

Native high amylose starches are corn starches from hybrid varieties of corn which contain at least about 40% amylose. In contrast, ordinary corn starch typically contains about 28% amylose. As used herein, "high amylose starch" S. includes starch comprising at least about 65% amylose, obtained from hybrid Sstrains of corn, as well as other starches which contain added isolated amylose, or which have been enzymatically debranched to yield a starch comprising at least I 1 i' about 6'5% amylose. This debranched starch may comprise both native long chain amylose and short chain amylose generated by debranching amylopectin molecules, Because amylose, a linear polymer, readily aligns or associates through hydrogen bonding, starches containing large amounts of amylose will form more rigid gels and stronger, tougher films, and will provide surfaces having reduced air, water and oil absorption and migration in food applications, relative to ordinary starches which typically contain much less than 65% amylose. Other advantages include improved binding properties where the starch primarily function, as an adhesive and the related property of improved cling or adhesion between-dissimilar food substrates. The unique binding, film forming, structural and textural characteristics of the high amylose starches make them useful in dry extruded foods, wherein these starches provide improved organoleptic qualities.

In particular expansion properties are improved and formulations may be modified to contain more fiber, have better moisture resistance, and the like, without sacrificing crispness and textural qualities.

As used herein, "dry" refers to extruded foods containing no more than moisture or extruded foods cf the semi-moist type, containing more than moisture, but having a water activity (aw) of less than 0.8.

SAt the relatively low moisture content 10-20%) of low water Q activity, extruded foods cereals, snacks, bread crumbs, pet foods), S granular high amylose starches will not gelatinize under extrusion conditions typically used to manufacture such foods. More rigorous conditions must be used to gelatinize (and thereby, solubilize) high amylose starch. High amylose starches that have not been solubilized by the processes herein do not provide desirable textural and organoleptic qualities, such as crispness, moisturet impervious film barriers, expansion and binding properties. The use of more rigorous extrusion conditions or a higher moisture content is not commercially feasible in the manufacture of low water activity at an a of less than S: 0.8) extruded foods.

Due to the highly bonded linear structure of high amylose starches, full and effective gelatinization of granular high amylose starches typically requires cooking temperatures of about 154-171 0 C, when the starch contains about amylose. Thus, to obtain high amylose starches, or foods containing such starches, which are soluble in hot or cold water, super atmospheric cooking U temperatures are usually required. Furthermore, traditional methods of starch pregelatinization typically produce high amylose starches that are retrograded, or have crystalline long chain amylose portions or are otherwise incapable of full..dispersion, or are degraded such that their functional benefits are substantially reduced.

For example, a method for preparing drum-dried, non-granular, pregelatinized isolated potato amylose is described in U.S. Pat. No. 3,086,890, issued April 23, 1963, to A. Sarko, et al. The starch slurry is heated to a temperature from just above boiling to 191°C (3750F) and a pressure of about 0.35 to 9.7 Kg/cm 2 (5 to 140 psi) for 1 to 60 minutes. It is than drum-dried at 110-200°C (230-3920F) for 40-75 seconds and the resulting sheet is pulverized to a dry, porous, white fluffy powder. Sarko's assignee subsequently disclosed in U.S. Pat. No. 3,515,591, issued June 2, 1970, to Feldman, et al., that the product of Sarko's drum-drying method slowly retrogrades upon storage and is unsuited" for use in packaged foods. The Feldman patent teaches a different method for preparing cold water soluble high amylose starch which disadvantageously requires the high amylose starch to be solubilized at 140-170°C and mixed with an aqueous suspension of gelatinized starch before drying.

In the alternative, high amylose starches have been modified by 9 derivatization and conversion to enhance their gelatinization and dispersibility characteristics. The use of these "modified starches" is undesirable in food 4 'products that are advertised as "natural" products. Gel strength and water resistance qualities of the modified high amylose starches also are reduced in proportion to the amount of modification.

Thus, there is a need for hot or cold water soluble high amylose starches that can'.be formulated into dry extruded foods without altering the extrusion *8 8 processes that are traditionally used to manufacture dry extruded foods such as ready-to-eat cereals and snacks.

The present invention provides an improved method for preparing dry, extruded foods comprising the step of adding to the food formulation an effective amount of a soluble high amylose starch selected from a spray-dried, non-granular starch, characterized in that the starch is substantially non-crystalline, substantially non-retrograded, and fully pre-dispersed; or (2) a spray-dried, uniformly gelatinized starch in the form of granular indented 3 i: Y1

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spheres, with at least a majority of the granules being whole and unbroken, the starch granules being in the form of loosely-bound agglomerates or individual granules; or an enzymatically debranched, gelatinized starch, comprising at least 65% amylose; or an enzymatically debranched gelatinized starch, comprising at least 65% crystalline short chain amylose; or a pre-extruded, fully predispersed high amylose starch; or a combination thereof. The food formulation also contains 1-15% water and, optionally, other ingredients typically used in extruded foods.

Semi-moist or dry, low water activity, extruded foods prepared with soluble high amylose starch are characterized by one or more of the following beneficial properties: stronger structural cells, improved appearance, improved texture, better expansion during extrusion, air-, oil- and/or water-impermeable surfaces; and improved resistance to sogginess (cereals). These foods are easier to extrude when they contain the soluble high amylose starches herein, which in contrast to granular high amylose starches known in the art, can be extruded at normal extrusion conditions of moisture content, pressure and temperature, and can be completely and thoroughly dispersed into the food formulation as a dry blend, or as a pre-dispersion using hot or cold water, prior to extrusion.

4 The use of particular methods for providing pregelatinized, soluble high amylose'starches is a significant feature of the invention. The high amylose starches are cooked and spray-dried under conditions which provide pregelatinized starches with unique properties. Stabilized, unconverted and/or t converted high amylose starches derivatized starches such as ethers or esters and/or the crosslinked products) may be used as the main component provided the organoleptic or functional qualities of the foods are not adversely affected. The starch may be derived from any high amylose plant source which S contains concentrations of about 40-100% amylose, including, for example, high amyloseicorn and wrinkled pea. The preferred starches are those derived from high amylose corn hybrids, comprising at least 65% amylose.

High amylose starches which are obtained from special hybrids of corn, barley and pea may contain as much as 75% amylose and are more expensive and more difficult to isolate than the typical native starches from more readily available sources such as corn, potato, wheat, rice, tapioca and the like. Most of the readily .available starches contain less than 30% amylose. However, a starch

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L:~EI i -I i ill containing a high percentage of short chain amylose may be produced from any of the more readily available amylopectin-containing starches by treating the starch with an enzyme capable of cleaving the alpha-1,6-D-glucosidic linkages of the amylopectin. This enzymatic treatment cleaves the branch points on the amylopectin molecule, yielding a mixture of short chain amylose and partially debranched amylopectin, together with any remaining amylopectin or any long chain amylose present in the untreated starch. For use herein, the total amylose content of the debranched starch must be at least 65%, by weight.

Prior to gelatinizing or solubi'lizing the high amylose starch, the starch may be modified by conversion, crosslinking, derivatization, or a combination thereof. Procedures for carrying out these modifications are conventional and well-known to those skilled in the art and described in such publications as Handbook of Water-Soluble Gums and Resins, Robert L. Davidson (Editor), Chapter 22: "Starch and Its Modifications" by M.W. Rutenberg, McGraw Hill Book Co. (New York) 1980.

The high amylose starch may be solubilized by any of the following processes or a combination of these processes.

Simultaneous Cookinq/Spray-Drying Process 2£ A method for preparing suitable spray-dried, granular pregelatinized Sstarches is described in U.S. Patent No. 4,280,851, issued July 28, 1981, to E.

Pitchon,. et al., which is hereby incorporated by reference. In this process a slurry of the granular starch is cooked or gelatinized in an atomized state.

A slurry of the starch which is to be cooked is injected through an atomization aperture in a nozzle assembly to form a relatively finely-divided spray. A S heating .medium is also injected through an aperture in the nozzle assembly into ad -i S the spray of atomized material so as to heat the starch to a temperature effective to gelatinize the starch. An enclosed chamber surrounds the ,ra atomization and heating medium injection apertures and defines a vent aperture positioned to enable the heated spray of starch to be atomized again as the starch exits the chamber. Thus, it is a dual-atomization process. The arrangement is such that the lapsed time between passage of the spray of starch through the chamber, from the atomization aperture and through the vent aperture defines the gelatinization time of the starch. The resulting -6spray-dried pregelatiized starch comprises uniformly gelatinized starch granules in the form of indented spheres, with a majority of the granules being whole and unbroken and swelling upon rehydration. Nozzles suitable for use in the preparation of these starches are also described in U.S. Pat. No. 4,610,760, issued September 9, 1986, to P. A. Kirkpatrick, et al. A process for agglomerating these starches is described in U. S. Pat. No.

4,871,398, issued October 3, 1989, to Katcher, et al.

A preferred embodiment of the invention includes the steps of: slurrying the starch in an aqueous medium; feeding a stream of the starch slurry at a pressure from about 50 to 250 psig into an 15 atomizing chamber within a spray-drying nozzle; injecting a heating medium into the atomizing chamber at a pressure from about 3.52 oto 17.58 kg/cm 2 (50 to 250 psig); O* simultaneously cooking and atomizing the o* 20 starch slurry as the heating medium forces the starch through a vent in the chamber; and drying the atomized starch.

SA single-atomization method for preparing suitable spray-dried, substantially pregelatinized starch may be used herein. Such a method is described in U.S.

Patent Application Serial No. 07/471,141, filed January 26, 1990, by R. Rubens, which is hereby incorporated by reference.

Drum-drying processes, such as the one disclosed in the Sarko patent, have not been successfully used to predisperse or solubilize the native or isolated long chain amyloses due to retrogradation problems. However, drumdrying may be used to solubilize high amylose starches wherein the starches comprise about 65% short chain amylose .staWfieonalkeep/speci28106.92_1 9.6 t -V 1< -1 y 0 i i i i l-i i -6A the debranched starches herein). Thus, drum-drying may be used to dry only the enzymatically debranched soluble high amylose starches herein, or blends thereof.

Enzymatic Debranching Process Starches suitable for enzymatic treatment herein include any amylopectin-containing starch that is susceptible to attack by a debranching enzyme, such as pullulanase, with the resultant hydrolysis of the alpha- 1,6-D-glucosidic bond. Suitable starches include corn, S 10 potato, sweet potato, wheat, rice, sago, tapioca, sorghum, waxy maize, waxy rice, waxy barley, smooth pea, Canadian S. pea, high amylose starch varieties, and the like.

The starch is pregelatinized before enzyme a" a. treatment to provide a uniformly debranched starch. It may be used in a dried form or as an aqueous dispersion Sfollowing debranching to form foods having desirable S textural properties. Numerous methods of pregelatinizing a starch, such as jet-cooking, drum-drying and steam injection atomization processes, are known in the art and 20 may be used before debranching the starcn. In a preferred embodiment, the starch is slurried in water and jet-cooked at approximately 149 0 o (300 0 F) to instantaneously gelatinize the starch.

Sstaffieonalkeep/speci28106.92 1 9.6 i 0 SFollowing gelatinization, the starch is enzymati-ally treated by the methods disclosed in U.S. Pat. Nos. 4,971,723, issued November 20, 1990, to Chiu; and 4,937,091, issued June 26, 1990, to Zallie, et al., which are hereby incorporated by reference. Enzymatic treatment must continue until the starch product comprises at least 65%, by weight, total amylose (short chain amylose and native or long chain amylose).

Converted debranched starches may be used herein. Conversion degrades the starch and reduces the molecular weight of the starch and the viscosity of the cooked starch dispersions. Suitable conversion of the starches to thin-boiling or fluidity starches useful herein may be .chieved by standard oxidative, heat, acid or alpha-amylase enzyme conversion techniques which are well known in the art. A'method for starch conversion employing alpha-amylase enzyme is disclosed in U.S. Pat. No. 4,726,957, issued February 23, 1988, to Lacourse, et al.

Debranched starches that contain crystalline short chain amylose, preferably at least 65%, by weight, crystalline short chain amylose, are the debranched starches preferred for use in Oy, extruded foods. If the debranched starch is obtained in a crystalline form, it may be made cold water soluble by i subjecting it to the coupled jet-cooking/spray-drying processes or the steam injection and atomization/spray-drying processes disclosed herein. The 0 crystalline form may be obtained by con'r'uously agitating the reaction mixture "during .the enzymatic debranching process and drying the reaction product at a S temperature of at least 60°C, or, optionally, recovering the crystalline short 4 chain amylose by filtering the reaction product. The debranched starch, particularly the fully debranched starch, remains cold and hot water soluble and does not crystallize or retrograde if the starch solution or dispersion is dried immediately following the completion of the enzyme treatment. Thus to obtain soluble debranched starch, it is preferred to dry the debranched starch as soon a as practicable after debranching and preferably no more than 24 hours after debranching.

Coupled Jet-Cookinq/Spray-Dryinq Process Spray-dried, pregelatinized, non-granular, substantially non-crystalline, substantially non-retrograded h,tgh amylose starches can be provided by a novel continuous coupled jet-cooking/spray-drying process. A suitable process is 7 11~ disclosed in U.S. Patent Application Serial No. 07/242,657, filed September 12, 1988, by Kasica, et al., which is hereby incorporated by reference. The process comprises the steps of: forming a slurry or a paste comprising a converted or unconverted high amylose starch and water; jet-cooking the aqueous slurry or paste of the starch with steam at a temperature sufficient to fully disperse or solubilize the starch; conveying and introducing the jet-cooked dispersion or solution into a nozzle of a spray-dryer at substantially the same temperature and pressure as the jet-cooking step; atomizing the jet-cooked dispersion or solution through the nozzle of the spray-dryer; drying the atomized mist of the jet-cooked starch within the spray-dryer; and recovering the jet-cooked and spray-dried starch as a water-dispersible or water-soluble powder.

SThe cooking temperature will depend upon whether a converted or unconverted j/ ttte i( S starch is used. Typical temperatures are about 138-177*C (280-350 0

F).

S The cooking chamber pressure used in the continuous coupled process iOrt typically ranges from 1.4 to 10.4 Kg/cm 2 (20 to 150 psig), and is the saturation pressure of steam at the temperature used plus the small incremental pressure S* c needed to move the dispersion through the chamber. Cooking chamber pressures suitable for high amylose starches are 5.5 to 10.4 Kg/cm 2 (80 to 150 psig), most preferably 6.9 to 9.0 Kg/cm 2 (100 to 130 psig) for a starch having an amylose R |content of about S.a An essential step in the above process is the conveying of the thoroughly i cooked, substantially fully dispersed starch, under elevated pressure and v temperature, to the spray-dryer atomization nozzle. In the preferred method, a S low shear pneumatic nozzle is used, and the transfer is carried out at substantially the same temperature and pressure used in the jet-cooking. The transfer is carried out without any venting to the atmosphere. Atomization in c a pressure nozzle may be used. The pressure of the atomization gas (steam or air) used must be sufficient for proper atomization into small droplets to allow rapid drying to an appropriate moisture without retrogradation.

8 It Use of a pressure nozzle in the above process requires insertion of a high pressure pump (141 to 703 Kg/cm 2 (2,000 to 10,000 psig)) between the jet-cooker and atomization nozzle. The temperature after passage through the high pressure pump should be maintained substantially equivalent to the jet-cooking chamber temperature. The pressure after the high pressure pump must be sufficient to properly atomize the cook to allow rapid drying to an appropriate moisture without retrogradation.

The spray-dried starch produced by the above process is non-granular and is characterized in that it is substantially non-crystalline and substantially non-retrograded. If the starch is to be converted or otherwise modified, these processes are typically carried out before the coupled jet-cooking/spray-drying 6process.

Acid-conversion of high amylose starches is preferred due to the ease in handling and y-dcovery during manufacturing afforded by a granular starch as opposed to starch in dispersed form as necessitated by enzyme conversion.

In the preparation of the converted starches by acid-conversion, the granular starch is hydrolyzed to the desired degree in the presence of an acid, Sprosuch as sulfuric or hydrochloric acid, at a temperature below the gelatinization temperature of the starch. The starch is slurried in water, and the acid (usually in concentrated form) is then added. Typically, the reaction takes 1' C place over an 8-16 hour period, after which the acid is neutralized with alkali op(eposed to pH of and the starch is recovered by filtration.

It should be appreciatedon of th e degree of conversion, as indicated by the water fluidity, is affected by the amount of acid or enzyme used as well as the time and temperature. The conversion conditions should be adjusted to provide .an appropriate water fluidity.

place over Suitable conversion procedures are described in Handbook of Water-Soluble S (.Gums and Resins, Robert L. Davidson (Editor), Chapter 22: "Starch and Its Modifications" by M. W. Rutenberg, McGraw Hill Book Co. (New York) 1980.

PrIt should b e appreciate thatthe degree of conversioness as indicated bythe ccwater A pre-extruded, fully predispersed high amylose starch or flour may be provid by the following steps: forming a slurry or paste of the starch in about 10 to 25% water; 9 i debranched soluble starch which comprises at least 65% amylose; an enzymatically debranched, gelatinized starch, containing.

crystalline short chain amylose which comprises /2 extruding the slurry or paste at a temperature of about 110 to 150°C; and recovering the starch in a powdered form.

The pre-extrusion process is preferably carried out in a twin-screw extruder, wherein the rotating screws are contained within a horizontal cylindrical barrel with an entry port at one end and a shaping die at the other end. The starch slurry or paste may be extruded in any shape, dried if desired, and ground to any particle size desired for a particular food application.

Extruded Foods Containing Soluble High Amylose Starch The extruded foods may be prepared by any extrusion method known in the art, provided that the method is suitable for food formulations containing 1-15% water and an effective amount (up to 75% by weight of the food) of high amylose starch. Extrusion methods which can be carried out at a temperature of up to 160 0 C and a pressure of up to 35 Kg/cm 2 (500 psi) are preferred. The food may be extruded as sheets, rods or othcr shapes which can be cut and further processed to form desired food products.

The soluble high amylose starches herein can be used in extruded foods alone or in combination with other starches fluidity corn or tapioca 32 0 starches). When a second starch component is present, the soluble high amylose starch must be present in an amount sufficient to provide improved, extruded foods with crisp textures, good expansion volume during extrusion, impervious surfaces or other characteristic advantages of formulation with high amylose starch, at the extrusion temperatures pressures and moisture contents normally used for dry or semi-moist, extruded foods. Typically, the soluble high amylose s3tarch is present in an amount of about 10 to 90%, preferably 25 to 60%, by weight, on a dry solids basis in the starch blend. In foods, the soluble high amylose starch or starch blend is present in an amount typically used for a particular extruded food. Depending on the food, the high amylose starch may be r:i used at levels up to about 75%, on a dry weight basis. Cereal formulations typically contain 5 to 20% starch; breadings, 5 to 20% starch; and snacks, 5 to 4 Vt c 60% starch, in addition to the starch contributed by any flour in the cereal formulation.

r I I When a combination of starches is used in the food formulations, the starches can be used as a one-part system, they may be solubilized by cooking both starches at the same time and then drying the resulting cooked starch blend by the methods disclosed herein. They also can be used as a two-part system in which case the soluble high amylose starch is prepared and added to the food formulation, and the second starch component is blended with the soluble high amylose starch or separately added to the food formulation. In a preferred embodiment, the soluble high amylose starches are dispersed in liquids slowly, with mixing or other shear so they are uniformly wetted and do not lump. They may be pre-mixed or agglomerated to assist in uniform dispersion in liquids.

Starches preferred for use in combination with the Iuble high amylose starches include corn, potato, sweet potato, rice, sago, tapioca, waxy maize, sorghum, or the like. Flours may also be used as a starch source.

Among the extruded foods which are improved herein are ready-to-eat, flaked, puffed and expanded cereals. The soluble high amylose containing cereals have improved expansion volume, a crisp eating texture, acceptable mouth feel and acceptable bowl life in milk. Soluble high amylose starches prepared by any Smethod disclosed herein may be used in improved, extruded cereals. Of the rd,, debranched starches, crystalline short chain amylose is preferred.

Si- i Various extruded snack products may be improved by the addition of soluble high amylose starch. Improvements are similar to those observed for cereals.

staMuch as the bowl life is improved n cereal, the surface moisture reslistance ind by snacks is improved and shelf life, especially in high humidity environments, is cooked extended.

starchAlso includedby the brmethods ding materials (crumbs) extruded and ground to a size acceptable for coating a variety of prepared foods. In a preferred embodiment, crumbs are ground into particles that pass through a #10 U.S. Sieve size screen added are retained on a #20 screen.

the olublThese coated foods include battered and breaded items such as chicken, a prvegetables, cheese, comminuted foods, and the like hich may be prepared in liquids sl conventional or microwave ovens, with or without the additional steps of i:par-frying and freezing. In addition to preparation by baking, these foods may be prepared by frying, with or without precooking and/or freezing.

ii m:.11: The resultant extruded, ground crumb is more effective than conventional bread crumbs in retarding the passage of moisture and water into or out of the food during processing and storage.

Pet foods of the dry or semi-moist variety are included. All or part of the pet food may be extruded by the process herein. For example, in preparing dog food, either "cheese" bits within a semi-moist patty or an entire patty, or both may be extruded by the process disclosed herein.

The group of foods described above exemplifies preferred uses of soluble high amylose starches in extruded foods. The practitioner may readily apply these teachings to other applications in the art. Thus, other extruded foods and other methods of using these starches in extruded foods are included herein.

In the examples which follow, all spray-drying nozzles are obtainable from Spraying Systems Co., Wheaton, Illinois. The following test procedures were used.

WATER SOLUBILITY MEASUREMENT A. Cold Water Solubility The determination is carried out using distilled water at room temperature.

t* IAbout 0.5 g of starch is dispersed in 30-40 ml of water in a semi-micro stainless |steel cup on a Waring blender base (Model 31B292). The blender is run at low r ct speed while the starch is added (all at once) and then run at high speed for 2 j t, minutes. The dispersion is immediately transferred to a 50 ml volumetric flask i and diluted to 50 ml with water. A 25 ml portion of the stock dispersion (shaken well to ensure a homogenous dispersion) is removed by pipet and transferred to a 50 ml centrifuge tube. The sample is spun down at 1800-2000 i, S rpms for 15 minutes. Once spun down, 12.5 ml of supernatant is pipetted into a I ml volumetric flask, 5 ml of 5 N potassium hydroxide (KOH) are added with 1 *swirling, and the mixture is diluted with water. The remainder of the stock i dispersion is shaken well, the insoluble starch dispersed with 10 ml of 5 N KOH while swirling. The mixture is diluted to 50 ml with water. The optical rotation of both the concentrated stock solution and the supernatant solution is S' measured.

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optical Rotation of Supernatant Path Length of Supernatant x 100 Cold Water Solubles 12 Li_ I~ o optical Rotation of Stock Solution/ Path Length of Stock Solution B. Hot Water solubility The procedure is the same as that described above except that boiling distilled water at 90-100 0 C (194-212 0 F) is used for dispersing the starch and all subsequent dilutions. No attempt is made to maintain temperature during the procedure.

WATER FLUIDITY MEASUREMENT A. Water Fluidity (WF) The water fluidity of the starches is measured using a Thomas Rotational Shear-Type Viscometer (manufactured by Arthur H. Thomas Co., Philadelphia, PA 19106), standardized at 30'C with a standard oil having a viscosity of 24.73 cps, which oil requires 23.12+ 0.05 sec. for 100 revolutions. Accurate and reproducible measurements of the water fluidity are obtained by determining the time which elapses for 100 revolutions at different solids levels depending on cc the starch's degree of conversion (as conversion increases, the Water Fluidity increases and the viscosity decreases) The procedure used involves slurrying the required amount of starch 6.16 g, dry basis) in 100 ml of distilled water in a covered copper cup and heating the slurry in a boiling water bath for minutes with occasional stirring. The starch dispersion is then brought to 1; the final weight 107g) with distilled water. The time required for 100 revolutions of the resultant dispersion at 81-83 0 C is recorded and converted to a water fluidity number using a conversion table.

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tj: Table I Time Required for 100 Revolutions (seconds) Amount of Starch Used (anhydrous, g)

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.4 4V re V 4 C 4~ 44C 44 6.16 a 8.80 1 11.44 c 13.20 d Water Fluidity 60.0 39.6 29.3 22.6 20.2 33.4 27.4 22.5 32.5 26.8 22.0 24.2 19.2 15.9 13.5 11.5 10.0 For a, b, c and d, final weights of starch solutions are 107, 110, 113 and 115 g, respectively.

B. Calcium Chloride Viscosity Solids Test) The calcium chloride viscosity of the converted high amylose starch is measured using a Thomas Rotation Shear-Type Viscometer standardized at (86 0 F) with a standard oil having a viscosity of 24.73 cps, which oil requires 23.12 0.05 seconds for 100 revolutions. As the conversion of the starch increases, the viscosity of the starch decreases and the calcium chloride viscosity decreases. Accurate and reproducible measurerents of the calcium 14

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4. I 4 41 4444 4.

4 444,4 t' C CC C C C C V: Co L chloride viscosity are obtained by determining the time which elapses for 100 revolutions at a specific solids level.

A total of 7.2 g of the converted starch (anhydrous basis) is slurried in 100 g of buffered 20% calcium chloride solution in a covered semi-micro stainless steel cup (250 ml capacity available from Eberbach), and the slurry is transferred to a glass beaker and is heated in a boiling water bath for minutes with occasional stirring. The starch solution is then brought to the final weight (107.2 g) with hot (approximately 90-1000C (194-212 0 distilled water. The time required for 100 revolutions of the resultant solution at 81-83 0 C (178-181 0 F) is measured three times in rapid succession and the average of the three measurements is recorded.

The calcium chloride solution is prepared by dissolving 264.8 g of reagent grade calcium chloride dihydrate in 650 ml of distilled water in a tared 1 L glass beaker. Thereafter 7.2 g of anhydrous sodium acetate is dissolved in the solution. The solution is allowed to cool and the pH is measured. If necessary, the solution is adjusted with hydrochloric acid to pH 5.6 0.1. The solution is then brought to weight (1007.2 g) with distilled water.

GEL PERMEATION CHROMATOGRAPHY .:QL 2Starches were prepared for analysis by slurrying 5 mg of enzymatically 4 5 debranThed starch in 4 ml of dimethylsulfoxide ("DMSO") containing 0.3M sodium S nitrate and heating the slurry to 80 0 C for at least 30 minutes. Samples (200 ml) were injected into an ALC/GPC-150C Chromatograph (Waters Associates, Milford, Massachusetts) (equipped with a Nelson 3000 Series Chromatography Data System and two PLgel mixed 10 mm columns (Polymer Laboratory, Amherst, Massachusetts), i S employing DMSO containing 0.03 M sodium nitrate as the mobile phase), and diluted at a rate of 1 ml/min. The columns were calibrated using dextran standards (with molecular weights of 2,000; 20,000; 80,000; 500,000; and :.2,000,000, obtained from Pharmacia Fine Chemicals, Piscataway, New Jersey). The S percentage short chain amylose was calculated from the relative area of the eak Sobtained within the molecular weight range from about 500 to 20,000.

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flr l li EXAMPLE 1 This example illustrates the preparation of soluble high amylose starch by the coupled jet-cooking/spray-drying process.

Part A The process variables used for jet-cooking/spray-drying unmodified high amylose (about 70% amylose) corn starch are shown below, in Table II. A slurry of unmodified granular high amylose starch was fed into a jet-cooker (model available from National Starch and Chemical Company). Steam was metered into the slurry to cook the starch and the cooked starch was conveyed to a pneumatic atomization nozzle top mounted in a 10.68 meter (35 foot) tall, 4.88 meter (16 foot) diameter Hensey spray-dryer. Steam at 8.44 Kg/cm 2 (120 psig) was used to atomize the starch. The atomized starch mist was dried with air at 2040C (400 0

F).

Table II Process Conditions for Jet Cookine/Sprav DrvinQ r :s B BrI B4' Sx;

II

Sa Ji High Amvlose Starch Part A Part B Slurry Solids 32.0% 26.2% Cook Solids 28.0% 25.0% Jet Cooking Temperature 0 C (OF) 143 (290) 163 (325) Steam Flow 4.2 Kg/cm 2 (9.25 lb/min) Cook Flow L/min (gal/min) 14.4 24.6 Nozzle Type a 1J-152 1J-152 Dryer Inlet Temp C (OF) 230-191 230-191 (446-375) (446-375) Dryer Outlet Temp "C 82-96 (82-96) (180-205) (180-205) Atomizing Steam Kg/cnm (psig) 8.44 (120.0) 8.44 (120) i.

i 9rra 959 9 12 a. Pneumatic nozzle obtained from Spraying System, two-fluid).

Inc. (Model 1J; 412 t

C

I C The cold water solubility of the non-granular starch powder was 97.4% and the hot water solubility was greater than 99%.

16 i j Part B Under process conditions shown above, in Table II, a converted high amylose corn starch (about 70% amylose) was processed using the coupled jet-cooking/spray-drying process. A slurry of the starch was treated with hydrochloric acid at 52 0 C (126 0 F) for 16 hours to give a converted starch having a calcium chloride viscosity of 25 seconds. After neutralization with sodium carbonate to a pH of about 6, the granular converted starch was filtered, washed and dried. The starch was then jet-cooked, and the jet-cooked starch dispersion was conveyed to a pneumatic atomization nozzle top mounted in a 10.68 meter foot) tall, 4.88 meter (16 foot) diameter Hensey spray-dryer. The atomized starch mist was dried with air at 2040C (400 0

F).

SIThe converted starch powder was 93.0% soluble in cold water and 97.1% soluble in hot water.

EXAMPLE 2 This example illustrates the preparation of soluble high amylose starch by steam-injection/dual-atomization or single-atomization spray-drying processes.

Unmodified granular corn starch containing about 70% amylose was slurried in water at 25.5% solids. This slurry was pumped by a Matt and Gaulin triplex pump at about 9.08 Liters (2.4 gallons) per minute under about 352 Kg/cm 2 (5,000 psig) to three steam atomization nozzles (dual-atomization nozzles as described i in Figure 1 of U.S. Pat. No. 4,280,851, issued July 28, 1981, to Pitchon, et mounted at the top of a 10.68 meter (35 foot) tall, 4.88 meter (16 foot) diameter Hensey spray-dryer. Steam at about 11.6 Kg/crm (165 psig) was used to gelatinize and atomize the starch. Air at 200 0 C (396 0 F) was used to dry the y atomized starch mist.

j S The recovered granular pregelatinized starch powder had a cold water solubility of about 75 percent and a hot water solubility of about 95 percent.

S t17 t t 17 I: 1 1 1 1 II-: t~ i i i I Illl~i EXAMPLE 3 This example illustrates the enzymatic preparation of starch containing either soluble or crystalline short chain amylose, and, optionally, long chain amylose, wherein the starch product comprises at least 65% total amylose.

PREPARATION OF THE DEBRANCHED STARCH The starches were converted, crosslinked, derivatized or dextrinized, where applicable, prior to gelatinization and treatment with a pullulanase enzyme. An aqueous slurry (20-30% solids) was prepared employing a native starch, or where applicable, a modified starch. The aqueous starch slurry was jet cooked at approximately 149 0 C (300 0 F) to gelatinize the starch. The cooked starch dispersion was placed in a constant temperature bath at 58-60°C with constant stirring. The pH was adjusted to 5 with 3% hydrochloric acid.

Dependinc on the type of starch used and its amylopectin content, between 0.5 and 10.0 mls of pullulanase per 100 g of starch were added to the cooked Sstarch dispersion. The pullulanase 3.2.1 41, pullulan 6-glucanohydrolase) which was used is a starch debranching enzyme produced by a novel species of Bacillus. This enzyme (Promozyme®) was obtained from Novo Industri A/S of Denmark. The enzymatic activity of a 1.25 g/ml solution of Promozyme is standardized at 200 PUN/ml of solution. One PUN (Pullulanase Unit Novo) is the amount of enzyme which, under standard conditions, hydrolyzes pullulan, liberating reducing carbohydrate with a reducing power equivalent to 1 micro-mol glucose per minute. The procedure for determining PUN is available from Novo Industri A/S. Thus, for example, in a starch dispersion employing corn starch, 125 PUN ofpullulanase per 100 g corn starch were added to the dispersion. For S a waxy maize starch dispersion (with higher amylopectin content), 750 PUN of «f pullulanase per 100 g waxy maize starch were added to the dispersion.

The pullulanase was permitted to debranch the starch until at least a total Sof 65% amylose had been reached. The pullulanase was deactivated in preparing 39 debranched starch by heating the dispersion to at least 80 0 C. The starch 9 dispersion was spray-dried at an inlet temperature of 200-210 0 C and an outlet o so temperature of 120-125°C. The spray dried-starch was screened through #40 mesh screen.

i 4 -i N'

I

PREPARATION OF SHORT CHAIN AMYLOSE Part A. Crystalline A 28% solids slurry of waxy maize starch in water was jet cooked at 149°C (300 0 F) to yield a 25% solids starch dispersion. The dispersion was placed into a constant temperature water bath at 600C, the pH was adjusted to 5.0, and 8 mls of the Promozyme pullulanase/100 g starch were added to the dispersion. The enzyme reaction was permitted to continue with continuous stirring for 88 hours.

Upon standing, a crystalline precipitate was formed in the milky starch dispersion. This precipitate was filtered, washed three times and air-dried to yield crystalline short chain amylose in about 85% yield. Gel permeation chromatography indicated th- product contained 84% short chain amylose.

The crystalline short chain amylose was not soluble in cold water. It was 23% soluble in hot water, and after continued heating for 20 minutes, was 98% soluble in hot water.

4...r 9#*4 9 c 9.

4.

4 Part B. Soluble A second dispersion of waxy maize starch was debranched in the same manner as Part A. except that the enzyme reaction was continued for 48 hours and filtering and washing steps were omitted. Thereafter the dispersion was spray-dried at 26% solids in a Niro laboratory spray-drier at an inlet temperature of 210 0 C and an outlet temperature of 125 0 C. The product, which comprised 78% short chain amylose, was recovered in about 75% yield.

The starch was 100% soluble in cold and hot water.

i:8 i i ii *9 EXAMPLE 4 Si it This example illustrates the preparation of ready-to-eat extruded cereal tc containing soluble high amylose starch.

o The soluble high amylose starches and controls listed in Table III, below were prepared by the methods of Examples 1-3 and incorporated into the following 30 cereal formulation.

cereal formulation.

j 1

I

i- I "~ii u, CEREAL FORMULATION Control 1 .l ii .1 i.,l|i (by weight) Weight (grams) Ingredient (by weigl.) Weight (grams) Starch Corn Flour Oat Flour Wheat Flour Sugar Salt

TOTA"

0 75 10 10 4 1 100% 0 7,500 1,000 1,000 400 100 10,000 10 60 15 10 4 1 100% 100 600 150 100 1,000 :i y.

4IV a 4

S

*r 4 5 *9 S 4I 20 The ingredients for the control were weighed out, charged into a one gallon jar, capped and set on rollers at 100 rpm for three hours to insure sufficient blending. Formulations (1,000g) containing starches were prepared in the same manner by replacing a portion of the corn flour.

The cereal was extruded using a Werner and Pfleiderer OZSK-30 twin-screw, co-rotating extruder (oil heated barrels) with either a Acrison Model #105 feeder, or a Zeranox Model #E-2 feeder.

Extruder conditions were set as follows: cl 4( 4' 1

SCF

r 444441tt 4c 4 Barrel Length Screw ConfiguLation Screw Speed Die Diameter Dry Feed Rate Input Moisture Barrel Temperature 5 SC-5-18 a 250 rpm 4 mm 10 kg/hr 6.7% 40/150/140°C a. SC-5-18 provides 2 reverse flig.s, 2 kneading blocks and 65% torque.

I S c Cereal formulation blends were fed into the extruder using the above processing conditions. After steady state conditions were obtained (uniformity of exiting extrdates and steady torque reading), samples were handcut at the die using a razor blade and measured for expansion using calipers. Samples were i ::r o i i

,B

pil~ i rl :-IH ~-UIIC~LL(UVUJ ruuy'cu JZL~ 7 immediately toasted in a Narco mechanical convection oven at 200-210C for 2-6 rmnute Samples were sealed in glass jars to await eval.tion.

Control and experimental samples were evaluated by measuring expansion, cereal bowl-life, texture and eating quality. Bowl-life was evaluated-by placing of cereal in 25.Og of cold milk (35-40 0 C) Taste panelists made observations, visually and organoleptically, at 1 minute intervals to determine when the cereal became unacceptably soggy. Taste panelists also evaluated samples milk and in dry form for firmness, stickiness, taste, tooth packing, chewiness, meltaway and overall eating quality.

Results are shown in Tables III and IV.

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I

I V V 21 3 ;1 7 a~ 6 V ft Table IIIa Evaluation of Extruded Cereals C ntaininr S.nlnhle Hiol, Amyvlnse Stareh Sample Percent Expansion Eating Quality Bowl Life-minutes (diameter) mm relative to control) I Steam-Atomized/Spray-Driec 5.5 12.0 Good (300%) Amylose Starch Amylose Starch II Jet-Cooked/Spray-Dried c Amylose Starch 12.0 Good 6.0 (270%) Acid-converted 15.0 Good Amylose Starch Amylose Corn Flour -11.0 Fair (170%) III Dehranchedc Crystalline waxy maize 23.0 Fair (81% short chain amylose) (270%) Spray-dried waxy maize 15.0 Fair 2.5 (78% short chain amylose) (70%) t,

(D

*a i-.

3 i Ct 0 r- 0 S i

I-

0 rt 1 rD ni- 3 Control: No Starche Control: Granular 70% amylose corn starchl Control: Granular 50% amylose corn starchi Good Good (100%) z;=jiJ;ci~ i lli -r p 4 0 0 f 0e e 4

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44' *ir4 0 0 9 4 P 4 a 4 00 4 0~~ 4 4 1' 4, Table III a (continued) Evaluation of Extruded Cereals Containing Soluble High Amylose Starch Sample Percent Expansion Eating Quality Bowl Life-minutes (diameter) mm relative to control) Control: Uncooked 70% amylose corn -8.0 Poor flour (170%) Control: Modified granular 50% 15.0% Poor amylose corn starch g acetylated) Control: Drum-dried, cross-linked 7.5 Poor waxy maize h Control: Modified uncooked amylose corn flour Propylene 7.5 Good oxide-treated) (100%) Control: Drum-dried corn starch 1 13.0 Good a. See Example 4 for cereal preparation.

b. Starch was solubilized by the method of Example 2.

c. Starch was solubilized by the method of Example 1.

d. Starch was debranched and solubilized by the method of Example 3 (Part A for crystalline waxy maize).

e. See Cereal Formulation Control in Example 4.

f. Starches and flour were not solubilized before formulating the cereal.

g. Starch derivatives were prepared by the methods disclosed in U.S. Pat. No. 4,937,091, issued June 26, 1990, to Zallie, et al.

h. Starches were dried by conventional methods.

disclosed in Examples 1 and 2. Crystalline debranched starch (containing at characteristics.

The beneficial properties of the soluble high amylose starches became lesswith apparent as the solubility of the starches increased beyond an optimum point spray-dried, debranched waxy maize starch and acid-converted 70% amylose starch); as the molecular weight decreased acid converted 70% amylose starch); and as the percentage amylose decreased the flours vs. the starches; and 50% vs. 70% amylose starch).

A second experiment (see Table IV) demonstrated that while excellent bowl life could be achieved by formulating cereals with 50-70% amylose starches that had not been solubilized, these cereals were commercially unacceptable. The cereal containing the insoluble starch was very hard, the texture was tough and the eating quality very poor. Notably, expansion during extrusion was much more limited for these samples than for the soluble starch samples.

The control containing no starch was a standard extruded oat cereal, representative of commercially used formulations. The soluble starches containing at least 65% amylose had expansion and eating qualities clearly superior to those of the control containing no starch.

C t 4: 24 I fc H I t.

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B

ii i.

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Table IV Evaluation of Extruded Cereals Containin Extruded High Amvlose Starch Sample Expansion Crispness b Bowl Life c Overall Eating Process: Starch mm (inches) Qualityd Control: No starch 4.32 (.170) 4 10 18 Control: Granular 50% amylose 4.01 (.158) 3 10 16 starch Control: Granular 70% amylose 4.34 (.171) 3 10 17 starch Control: Modified granular 50% 4.88 (.192) 3 6 14 amylose starch Steam-atomized spray dried e: amylose starch 6.45 (.254) 10 6 24 Jet-cooked/spray-dried g: 70% amylose starch 5.97 (.235) 8 5 Converted 70% amylose starchh 7.32 (.288) 9 8 27 a. Cereals contained 70% oat flour, 20% corn flour, 10% sugar. Treatments contain 15% starch in place of an equal quantity of corn flour.

b. 10 most crisp c. Subjective evaluation of 10g cereal in 100g milk after 6 minutes. 10 longest bowl life.

d. Subjective evaluation which includes bowl life, expansion, texture and crispness. 30 highest eating quality.

e. Starch was steam-atomized/spray-dried by the method of Example 2.

f. Acetylated corn starch containing about 50% amylose.

g. Starches were jet-cooked/spray-dried by the method of Example 1.

h. Starch containing 70% amylose was acid-converted to Example Extruded bread crumbs containing soluble high amylose starch were prepared according to the following formulation and process.

C

IL t~ IL IL 4.

9>1 mrirs~ ;r ru-- t ~7 a

I:

Bread Crumb Formulation Control L;nlJ~lllll~jllLal Kg Weight (Ibs) Kg Weight (Ibs) Ingredient Percent Percent

I

Wheat Flour Starch Sugar Vegetable Shortening Non-fat dry Milk Salt Distilled Monoglyceride 89.35 90.72 (200) 0.00 0 (0) 5.80 5.88 (12.96) 1.03 1.05 (2.32) 1.93 1.96 (4.32) 1.45 1.47 (3.24) 0.45 0.46 (1.008) 71.48 17.86 5.80 1.03 1.93 1.45 0.45 24.52 (54.054) 6.13 (13.514) 1.99 (4.378) 0.36 (0.784) 0.66 (1.459) 0.50 (1.095) 0.15 (0.341) 34.30 (75.624) 100.00 101.52 (223.848) 100.00 o *a 0 a 0*9.

*r 0 a a a a i i ii; i i i- The bread crumb dough was prepared by mixing melted shortening with the sugar for 15 minutes in a Hobart mixer; mixing in the milk, salt and monoglyceride; and mixing the flour and starch, as indicated, with the other ingredients for 30 minutes.

Samples were extruded according to the conditions listed below, with a Wenger X-20 single screw cooking extruder: rI t I~

C

S

S

4o i Screw/Barrel Configuration Barrel Segment Screw Element Inlet-714 Spiral-372 Single Flight Spiral-372 Single Flight Spiral-372 Double Flight Fluted-318 Double Flight Cone-350 Triple Flight Operating Conditions Screw Speed 400 RPM Drive Load 14 Amps Die Spacer 2.5 cm Die Orifice 0.5 cm Dry Feed Rate 3 kg/min Input Moisture 12% Discharge Moisture 29% Barrel Temperature 10/70/120°C Shearlock 364 364 364 324 -7: After extrusion, samples were dried for 2 1/2 hours in an oven at 93 0 C, and ground in a mortar and pestle to crumb particles that passed through a #10 U.S.

Sieve size screen and were retained on a #20 screen.

Crumbs prepared from the control formulation and the experimental formulation, containing jet-cooked/spray-dried (Example 1) 70% amylose corn starch, jet-cooked/spray-dried (Example 1) 70% amylose corn starch that had been acid-converted to 35WF, or waxy maize starch debranched (Example 3) to contain about 45% short chain amylose, were coated onto skinned chicken pieces and the chicken was cooked in a microwave oven for 3-4 minutes. The coated chicken was evaluated for coating crispness, color and adhesion. None of the samples developed a brown color in the coating. All coating adhered to the chicken. Samples containing jet-cooked/spray-dried 70% amylose starch and acidconverted (35WF) jet-cooked/spray-dried 70% amylose starch were judged to have good crispness qualities and to be the best coatings. The sample containing waxy maize starch that had been enzymatically debranched to contain about 45% short t chain amylose yielded poor crispness characteristics.

Thus, textural qualities of extruded breadings were improved by adding jet- 1 cooked/spray-dried (Example 1) 70% amylose starch to the breading formulation before extrusion.

:f

I

I I i i i /i: i-

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i i:: i i Example 6 Half-product snacks containing soluble high amylose starch were prepared according to the following formulation and procedure.

i

I

C CC (I C r vc; S tr CC C C. uc C C a 1 1 1 1 1 '4I 4 S iil._-i I Snack Formulation Percent by Weight Exnerimentar Ingredient Control Modified Starcha 60.0 54.0 30.0 0 Soluble High 0 6.0 30.0 60.0 Amylose Starchb Cheeztangg 17.0 17.0 17.0 17.0 Salt 2.0 2.0 2.0 Mustard Powder 0.1 0.1 0.1 0.1 Onion Powder 0.5 0.5 0.5 ca *4 4i 44 20 4. 4 .4 6 44 Monosodium Glutamate Garlic Powder Water 0.1 0.03 20.27 100.00 0.1 0.03 20.27 100.00 0.1 0.03 20.27 100.00 0.1 0.03 20.27 100.00 i i:, i; i:i j_ i

I

i: i i m::jn~_ r a. A crosslinked, acetylated, pregelatinized waxy maize starch.

b. An acid-converted (35WF) 70% amylose starch jet-cooked/spray-dried by the method of Example 1.

c. Cheese flavoring powder obtained from Kraft Food Ingredients Corp.

d. Samples A, B and C represent 10, 50 and 100%, respectively, replacement of modified starch with soluble high amylose starch.

ce e C cC C C

IC

C C (I IF CC t C C C C CC( ii i- i r ~L The dry ingredients wee blended and the water was added with mixing to form a dough. The dough was extruded at room temperature using a hand homogenizer (obtained from C.W. Logeman Company), cut and dried to 10% moisture.

Samples of control and experimental snacks were either baked at 177 0 C (350 0

F)

for 10 minutes, or deep-fat fried at 190 0 C (375 0 F) for 1 1/2 minutes.

Samples were evaluated for organoleptic qualities, including texture or crispness and appearance, and expansion. The best samples, whether fried or baked, were those in which 10% of the modified starch was replaced with soluble high amylose starch. These samples had improved crispness and harder textures than the modified starch controls. Samples containing a starch blend of 50 or 100% high amylose starch showed progressively less expansion and less desirable textural qualities.

Example 7 This example illustrates the preparation of an improved ready-to-eat cereal 1 c5'c formulated wi h a pre-extruded, fully predispersed high amylose starch flour.

tctc Part A: Pre-Extrusion Proues3 tl: A sample of fully predispersed, 70% amylose starch-containing flour I i S (Microcrispe flour, obtained from National Starch and Chemical Company, Bridgewater, New Jersey) was extruded under the extrusion conditions set out in Example 4, herein, for cereals, except that the flour was slurried in water to give 13.5% input moisture and the barrel temperature was 130 0 C. The extruded flour was ground to a powder.

Sc Part B: Cereal Extrusion or The extruded flour of Part A, above, was added at a 50% corn flour 1 r replacement level to a cereal formulation containing 50 parts corn flour, h parts oat flour, and 10 parts sugar. The experimental and control cereals were os formulated and extruded by the method of Example 4. Cereal bowl-life was 3Qc evaluated by the method of Example 4.

The bowl-life of the pre-extruded, fully predispersed high amylose flourcontaining cereal was between 1 and 2 minutes longer than that of the control cereal. Thus, the pre-extruded high amylose flour provided improved water resistance and crispness in extruded cereal.

29 a a m I Hi

Claims (9)

1. A method for preparing a dry, extruded food, comprising the steps: formulating a food for extrusion, said food comprising 1-15% water and an effective amount, up to 75% by weight, of a solubilized high amylose starch, selected from the group consisting of a spray-dried, non-granular high amylose starch jharacterized in that the 10 starch is substantially non-crystalline, Ssubstantially non-retrograded, and fully predispersed, and comprises at least 65% amylose; a spray-dried, uniformly gelatinized high amylose starch which comprises at least amylose and is in the form of granular indented i spheres, with at least a majority of the granules being whole and unbroken, these starch granules S: being in the form of loosely-bound agglomerates or individual granules; an enzymatically 20 debranched soluble starch which comprises at least 65% amylose; an enzymatically debranched, gelatinized starch, containing crystalline short chain amylose which comprises at least 65% amylose; a pre-extruded, fully r 25 predispersed high amylose starch which comprises at least 65% amylose; and a combination thereof; and extruding the food at a temperature of up to 0 o°C and a pressure of to 35.2 kg/cm 2 (500 psi), wherein the dry, extruded food is characterized by a crisp texture and by resistance to migration of water, oil and air into and out of the food. staf/ieonalkeep/speci/28106.921 9.6 A 0/

2. The method of Claim 1, wherein the food is formulated with solubilized high amylose starch and the starch is prepared by a process comprising the steps of: forming a slurry or a paste comprising a converted or unconverted high amylose starch and water; jet-cooking the aqueous slurry or paste of the starch with steam at a temperature sufficient to fully disperse or solubilize the starch; 0 0 0 1 0 a0 f I i staf1ieonalkeepspeci/28106.9.91 9.6 Wl! u *fLk. i I 0" i:i I ZC I I: I II conveying and introducing the jet-cooked dispersion or solution into a nozzle of a spray-dryer at substantially the same temperature and pressure as the jet-cooking step; .atomizing the jet-cooked dispersion or solution through the nozzle of the spray-dryer; drying the atomized mist of the jet-cooked starch within the spray-dryer; and recovering the jet-cooked and spray-dried starch as a water- soluble powder.

3. The method of Claim 1, wherein the food is formulated with solubilized high amylose starch and the starch is prepared by a process comprising the steps of: slurrying the starch in an aqueous medium; atomizing the slurry into an enclosed chamber; interjecting a heating mediun. into the atomized slurry in the enclosed chamber to cook the starch, said chamber containing a vent aperture positioned to enable the atomized slurry to exit the chamber, the size and shape of the chamber and the vent aperture being effective to maintain the temperature and moisture of the material for a period of time sufficient to cook the starch; and drying the atomized starch.

4. The method of Claim 1, wherein the food is formulated with solubilized high amylose starch and the starch is prepared by a process comprising the steps of: slurrying the starch in an aqueous medium; feeding a stream of the starch slurry at a pressure from about 50 to 250 psig into an atomizing chamber within a spray-drying nozzle; injecting a heating medium into the atomizing chamber at a pressure from about 3.52 to 17.58 Kg/'-m 2 (50 to 250 psig); simultaneously cooking and atomizing the starch slurry as the heating medium forces the starch through a vent in the chamber; and drying the atomized starch.

I I:1 The method of Claim 1, wherein the food is formulated with solubilized high amylose starch and the starch is prepared by a process comprising the steps of: providing a pregelatinized starch; hydrolyzing alpha-1, 6-D-glucosidic bonds of the starch with an aloha- 1,6-D-glucanohydrolase until the starch comprises at least 65% by weight, amylose; and recovering the starch as a soluble powder.

6. The method of Claim'1, wherein th3 food is formulated with solubilized high amylose starch and the starch is prepared by a process comprising the steps of: gelatinizing a starch slurry; with continuous agitation of the gelatinized starch slurry, a o debranching the starch with an enzyme which selectively hydrolyzes the alpha-1,6-D-glucosidic linkages of the starch to yield a starch t ixture, comprising crystalline and non-crystalline short chain amylose, where n at B S least 65% by weight of the starch mixture is amylose; and S* drying the starch mixture at a temperature in excess of 60 0 C.

7. The peeees.~of Claim 6, further comprising the steps of filtering the I starch mixture to separate *ne crystalline short chain amylose from the starch j mixture and washing and drying the crystalline short chain amylose. c

8. The method of Claim 1, wherein the food is formulated with solubilized high N" *amylose starch and the starch is prepared by a process comprising the steps of: forming a slurry of the starch in water; Sc* extruding the starch slurry at a temperature of from o 150 0 C; and S(c) recovering the starch as a soluble powder. -3 32 A

9. The method of Claim 1, wherein the solubilized high, amylose starnh is modified by conversion, crosslinking, derivatz-ati-qn, or a combination thereof, prior to bell r-j solubilized. The method of claim 1, wherein the dry, extruded food is selected from extruded cereals, breadings, snacks, and pet foods. DATED THIS 02ND DAY OF NOVEMBER 1992 NATIONAL STARCH AND CHEMICAL INiVESTMENT HOLDING CORPORATION By its Patent Attorneys: GRIFFITH HACK CO. Fellows Inst,.;,tute of Patent Attorneys of Australia tc C C C 4 ~I #6 ABSTRACT The present invention provides a method for preparing semi-moist or dry, low water activity, extruded foods, comprising the steps: formulating a food for extrusion, comprising 1-15% water and an effective amount of a soluble high amylose starch, up to 75% iy weight, selected from: spray-dried, non-granular starch, characterized in that the starch is substantially non-crystalline, 10 substantially non-retrograded, and fully pre-dispersed; spray-dried, uniformly gelatinized starch in the form of granular indented spheres, with at least a majority of the granules being whole and unbroken, the starch granules being in the form of loosely-bound agglomerates or individual granules; (3) p 7 enzymatically debranched soluble starch, comprising at least 65% amylose; an b t 151< enzymatically debranched, gelatinized starch, containing crystalline short chain il ABSTRACT 5 Tha e present comprsinvg at least 65% amylose; a pre-extruded, fully C ct' predispersed high amylose starch; and a combination thereof; and extruding the foods at a temperature of up to 1600C and a pressure of up to 35.2 Kg/cm 2 (500 psi). The low water activity extruded foods, comprising p repared with soluble high a foodse starch are characterized by one or more of the following beneficial properties: i mproved expansion during 15% water and anextrusion, improved appearance, improved air-, oil- and/mylose starch, uimpermeable surfaces; and improvselected from:textures. These foods are easier to prepare when they contain the soluble high amylose starches herein, stalline, substantially non-retrograded, and fully pre-dispersed; spray-dried, theseuniformly gelats, in co n t rast to granular high amylose starches used in the same l east a majority of the gruson condition can be complhetly and thogranules Sdispersed in the extruded foods without chemical modification of the starch, or 1 C enzymatically debranched, gelatinized starch, containing crystalline short chain t r t amylose and comprising at least 65% amylose; a pre-extruded, fully c <C*ti predispersed high amylose starch; and a combination thereof; and (b) extruding the foods at a temperature of up to 160 0 C and a pressure of up to 35.2 Kg/cm 2 (500 psi). The low water activity extruded foods prepared with soluble high amylose S| starch are characterized by one or more of the following beneficial properties: 1 improved expansion during extrusion, improved appearance, improved air-, oil- and/or water-impermeable surfaces; and improved textures. These foods are easier S11 t ct to prepare when they contain the soluble high amylose starches herein, since tc D these starches, in contrast to granular high amylose starches used in the same C foods under normal extrusion condition, can be completely and thoroughly dispersed in the extruded foods without chemical modification of the starch, or significant alteration of typical food extrusion processes. C 1 11