Abstract: Porous modified gelatinized cereal flour that has high swelling property in cold water, high solubility and good digestability and which is useful as a fragrance adsorbent or an emulsion stabilizer. Also disclosed is a process for producing such porous gelatinized cereal flour which comprises adding water to a cereal flour containing starch as a principal component, heating said flour to gelatinize it, adding an alcohol to the gelatinized flour, and freeze-drying the same.

Abstract: A process for producing corn fiber having a high total dietary fiber content. A dilute aqueous slurry of the corn fiber obtained from the corn wet-millng process is separated by means of a hydroclone to give a fiber fraction of enhanced total dietary fiber content. This fiber fraction may then be passed into a centrifual paddle screen to give a product of even higher total dietary fiber content.

Abstract: The invention refers to a process for obtaining a melt of destruction starch containing a finite amount of electrolytes comprising:A. providing a starch material containing free electrolytes and/or bound phosphate salts,B. removing partially or wholly the free electrolytes and/or the metallic cations from the phosphate groups of the starch,C. optionally replacing a part or all of the free H.sup.+ -ions of the free phosphate groups with metallic monovalent and/or polyvalent cations,D. conditioning the obtained starch material to a water content of 10 to 25% by weight calculated on the basis of starch and water,E. heating said starch/water composition at elevated pressure to a temperature sufficient to essentially destructure the starch while maintaining said water content until a melt of destructurized starch is formed.The invention further refers to the process ofF. cooling said melt (as obtained under E.

Abstract: A continuous process for producing agglomerated spray-dried, pregelatinized starch wherein two or more spray-cook nozzles are aligned in a drying tower such that their spray patterns intersect. The point of intersection is distant enough from the nozzles to avoid globbing or clumping and close enough to the nozzles so that the surface of the particles are tacky enough to effect adhesion and a build-up of agglomerates.

Abstract: This invention provides a process for easily recovering nearly white starch and protein having a high commercial value by depressing darkening of crushed slurry and juice in producing starch and protein of a subterranean stem.The above-mentioned process is characterized by adding at least one member selected from the group consisting of sodium thiosulfate, potassium thiosulfate, sodium hydrogen sulfite, sodium sulfite and potassium sulfite at the time of crushing the subterranean stem.

Abstract: Novel, highly useful, sweet fructose-containing syrups also containing fructooligosaccharides are provided herein by the partial or substantially complete hydrolysis of inulin. The process includes first providing an aqueous solution containing inulin from Jerusalem artichoke tubers or chicory roots. Then the warm aqueous solution of inulin is passed through a column containing a strong acid cation-exchange resin, thereby providing an effluent having a pH of about 2.0-about 3.0. The effluent is then hydrolyzed by heating at a temperature of about 70.degree.-about 100.degree. C., and the hydrolyzate is passed through a column containing of about 6.5-about 7.0. resin, thereby providing an effluent having a pH about 6.5-about 7.0. Optionally, after the hydrolysis step, the hydrolyzate is decolorized by contact with activated or granular charcoal. The effluent is then concentrated to a syrup containing less water than the effluent, e.g. one containing about 40-about 70% solids.

Abstract: Alpha-potato starch with a quality suitable for use as a binder in feeds for fish can be produced by first adjusting the electrical conductivity of a potato starch slurry, then thermal gelatinizing and dehydrating the same.

Abstract: In a process utilizing a battery of hydrocyclones for separating wheat starch and gluten contained in an aqueous wheat flour slurry, the slurry is supplied to a first section of the hydrocyclone battery, in which a gluten fraction is removed as overflow, and the starch-rich fraction from such first battery section is first treated to reduce its pentosan content and is then treated in a second section of the hydrocyclone battery which delivers a concentrated starch fraction as underflow.

Abstract: Starch derived from a dry milled cereal grain such as corn or milo is hydrolyzed to provide a sterile aqueous fermentable sugar solution which is especially adapted for fermentative conversion to ethanol with minimum thermal expenditure. Following an initial mild hydrolysis to thin, or liquefy, the starch, substantially all of the water insoluble protein and oil components, and a portion of the water soluble components, e.g., sugars, lipids, proteins and vitamins, are separately recovered from the partial starch hydrolysate with the water solubles being recycled to the system. Thereafter, the partial starch hydrolysate is subjected to further hydrolysis to provide an aqueous solution of fermentable sugar.

Abstract: A thickener is prepared comprising water and a waxy starch from a selected plant of a wxsu2 genotype, the sol of which starch exhibits superior resistance to breakdown on storage at low temperatures. The starch may optionally be modified. The thickener, which preferably employs a starch extracted from maize, is particularly useful for food applications.

Abstract: The method for the production of starch from grain or ground grain products by the wet process comprises a brief steeping of the raw material during which the morphological structures are not broken down by chemical or microbiological processes, and of a comminution of the steeped raw material in a high-pressure apparatus equipped with a splitter head. In this high-pressure apparatus, the steeped raw material is subjected to a pressure of at least 10 bar, fragmented under the action of high shear forces, and exposed to the atmosphere, thus causing the necessary structural breakdown between the starch grains and the protein. For shelled corn after the addition of process water, the shelled corn is fed to a heated pressure steeping apparatus. After a maximum of three hours at a pressure of 10 to 15 bar, the necessary moisture absorption is achieved. Excess water is fed to an evaporator. A pressure reducing apparatus at the output of the steeping apparatus produces a preliminary fragmentation of the corn grains.

Abstract: Wet milling of starch bearing materials (e.g. corn, potatoes or wheat) wherein water being used in the process is separated by reverse osmosis or ultrafiltration, into two fractions, one fraction (the first fraction) having a lower content of soluble and insoluble matter than the other (second) fraction. The first fraction is then recycled to the washing step of the milling process where it is used to wash the starch. The separation and recycling steps reduce the water requirement of the milling process and also reduce the volume of effluent leaving the process, which needs to be evaporated and/or disposed of.

Abstract: The production rate and yield resulting from the dewatering of starch conversion products containing swollen starch granules resulting from treatments with cationic reagents is improved by the addition to the starch slurry of a water soluble anionic polymer.

Abstract: The production rate and yield resulting from the washing of starch conversion products containing swollen starch granules is improved by the addition to the wash water of 0.1 to 1% by weight, based on starch solids, of a cationic polymer which is a water-soluble acid salt of an aminoalkyl ester of a carboxylic acid polymer.

Abstract: A method of producing milo starch which comprises the steps of immersing refined milo in a weakly acidic solution of sodium chlorite to remove the tannin, grinding the same to provide a starch slurry, and removing the proteins from the latter. The method is capable of producing milo starch of high purity at low cost without causing odor pollution.A method of producing milo starch includes, besides the steps described above, the steps of lactic-fermenting the waste liquid resulting from the immersion of white grain milo, concentrating the liquid, mixing the concentrated liquid with the bran resulting from the refining of milo, and drying the mixture to provide milo feed. By this method, it is possible to produce milo starch without having to provide any special equipment for treating the waste water.

Abstract: Starch derived from dry milled corn is hydrolyzed to provide a sterile aqueous fermentable sugar solution which is especially adapted for fermentative conversion to ethanol with minimum thermal expenditure. Following an initial mild hydrolysis to thin, or liquefy, the starch, substantially all of the water insoluble protein and oil components, and a portion of the water soluble components, e.g., sugars, lipids, proteins and vitamins, are separately recovered from the partial starch hydrolysate with the water solubles being recycled to the system. Thereafter, the partial starch hydrolysate is subjected to further hydrolysis to provide an aqueous solution of fermentable sugar.

Abstract: A process and apparatus is provided for cooking or gelatinizng a material in an atomized state, so that there is obtained an easily dryable, uniform and finely-sized product. The material which is to be cooked is injected through an atomization aperture in a nozzle assembly to form a relatively finely-sized spray. A heating medium is also injected through an aperture in the nozzle assembly into the spray of atomized material so as to heat the material to a temperature effective to cook or gelatinize the material. An enclosed chamber surrounds the atomization and heating medium injection apertures, and defines a vent aperture positioned to enable the heated spray of material to exit the chamber. The arrangement is such that the elapsed time between passage of the spray of material through the chamber, i.e., from the atomization aperture and through the vent aperture, defines the cooking or gelatinization time of the material.

Abstract: Starch is recovered from an amylaceous material such as manioc root or corn in the form of an aqueous slurry containing substantially all of the soluble components, e.g., carbohydrates and proteins, of the amylaceous material prior to processing. To accomplish such recovery, amylaceous material is milled in one or more steps in the presence of water to provide a slurry containing liberated starch particles and non-starch components. The initial aqueous starch slurry is then concentrated by removal of water therefrom. The water removed from the initial starch slurry contains soluble elements of the starch and is recycled to restore these elements to the starch recovery system.

Abstract: A system for separating the mill starch fraction in a corn wet milling operation into a protein enriched stream and a starch enriched stream to obtain therefrom a protein-rich product and a starch-rich product. The system utilizes only hydrocyclones arranged in a plurality of separation stages that are divided into two separation zones. The mill starch is fed sequentially through the two separation zones under controlled conditions so as to obtain a protein-rich product from one separation zone and a starch-rich product from the other separation zone.

Abstract: A starch wet milling process, in which a series of independent classifications and separations is carried out in the production of starch, employs a Starch Gluten Separation Station having a three-stage centrifugation treatment including passing the entire mill stream through a mill stream centrifuge thickener, followed by primary starch centrifuge separation and gluten centrifuge thickening.

Abstract: A process and apparatus are described for producing modified starch products. In the method of the invention, a slurry of starch is continuously moved at elevated temperature and pressure through a tubular heating zone and the hot fluid mass emerging from the heating zone is forced through a flow restricting zone within which the fluid mass is highly compressed. This highly compressed fluid material emerges from the confining zone into a tubular reaction zone with a sudden release of energy in the form of a fine spray or mist. The compressive forces followed by the sudden energy release act on the starch molecules to temporarily greatly increase the reactivity of the starch within the reaction zone, whereby modified starch products are quickly formed.

Abstract: A system for separating the mill starch fraction in a corn wet milling operation into a protein enriched stream and a starch enriched stream to obtain therefrom a protein-rich product and a starch-rich product. The system utilizes only hydrocyclones arranged in a plurality of separation stages that are divided into two separation zones. The mill starch is fed sequentially through the two separation zones under controlled conditions so as to obtain a protein-rich product from one separation zone and a starch-rich product from the other separation zone.

Abstract: A process for fractionating the whole wheat kernel into its gluten, starch and bran-germ components including the steps of tempering the whole wheat kernel in water to increase its moisture content, milling the tempered kernel to reduce the particle sizes of the kernel components, forming a homogeneous slurry of the particles and water, the wheat to water ratio of the slurry being in the range 1:3 to 1:10, by weight, vigorously admixing the slurry to achieve uniform dispersion of the particles in the water, applying centrifugal forces to the slurry to cause it to separate into its gluten, starch and water phases, separating the gluten and starch phases and purifying them by conventional techniques to recover gluten, starch and bran-germ in very high yield fractions.

Abstract: Process for concentrating starch contained in very dilute, aqueous mixtures having, for example, a starch content of less than about 1 weight percent. The concentrated product is obtained as an aqueous mixture containing starch solids in the amount of at least about 30 weight percent, preferably about 35 to 50 weight percent. The concentrating operation involves the sequential use of a gravity settling technique, especially lamellar plate settling, to increase the starch content of the solid-liquid mixture to about 5 to 20 weight percent. This mixture can be readily removed from the settler, and further concentrated centrifugally, e.g., in a liquid cyclone, by a factor of at least about 2 to provide the desired aqueous mixture having a concentration of at least about 30 weight percent of starch solids. The latter stream can be readily and effectively handled and treated to recover relatively pure, essentially solid, food grade starch of low moisture content, e.g., less than about 10 weight percent.