A23P10/20

Sugar compositions for tableting by direct compression
10342247 · 2019-07-09 · ·

Directly compressible compositions that include more than 30% by weight of allulose, and tablets obtainable thereof.

Sugar compositions for tableting by direct compression
10342247 · 2019-07-09 · ·

Directly compressible compositions that include more than 30% by weight of allulose, and tablets obtainable thereof.

METHOD FOR THE PRODUCTION OF A DOSAGE FORM

A method is described for producing a dosage form and granules including surface-reacted calcium carbonate. Also described, are tablets and/or capsules obtained by the method. Methods using such a surface-reacted calcium carbonate, and a dosage form comprising the granules are also described. Further, methods of using the granules, or the tablets and/or capsules, or the dosage form in a pharmaceutical product, a nutraceutical product, an agricultural product, a cosmetic product, a home product, a food product, a packaging product and a personal care product are also described. A pharmaceutical product, a nutraceutical product, an agricultural product, a cosmetic product, a home product, a food product, a packaging product and a personal care product including the granules, or the tablets and/or capsules, or the dosage form are also described.

METHOD FOR THE PRODUCTION OF A DOSAGE FORM

A method is described for producing a dosage form and granules including surface-reacted calcium carbonate. Also described, are tablets and/or capsules obtained by the method. Methods using such a surface-reacted calcium carbonate, and a dosage form comprising the granules are also described. Further, methods of using the granules, or the tablets and/or capsules, or the dosage form in a pharmaceutical product, a nutraceutical product, an agricultural product, a cosmetic product, a home product, a food product, a packaging product and a personal care product are also described. A pharmaceutical product, a nutraceutical product, an agricultural product, a cosmetic product, a home product, a food product, a packaging product and a personal care product including the granules, or the tablets and/or capsules, or the dosage form are also described.

COLD WATER-SWELLING, INTACT, HIGH AMYLOSE STARCH GRANULES

A process for modifying starches comprises atomising an aqueous slurry of a non-pregelatmised, granular, high amylose starch into an internal chamber in a bi-fluid nozzle of a dryer and treating the atomized slurry, in the internal chamber, with medium pressure steam to produce a slurry of partially treated starch granules followed by discharging the slurry into a reactor where it is contacted with superheated steam to produce dry, particulate, cold water-swelling, intact, high amylose starch granules. The cold water-swelling, intact, high amylose starch granules have greater than 15% solubles. At a starch concentration of 1%, in UDMSO (9 volumes DMSO and 1 volume 6M urea) at 25 C., the ratio of apparent viscosity of said cold water-swelling, intact, high amylose starch granules to the apparent viscosity of the parent non-pregelatinised, granular, high amylose starch is lower than 1.00. The cold water-swelling, high amylose granular starch of the invention is useful in the manufacture of food products, especially confectionery products and convenience food products.

COLD WATER-SWELLING, INTACT, HIGH AMYLOSE STARCH GRANULES

A process for modifying starches comprises atomising an aqueous slurry of a non-pregelatmised, granular, high amylose starch into an internal chamber in a bi-fluid nozzle of a dryer and treating the atomized slurry, in the internal chamber, with medium pressure steam to produce a slurry of partially treated starch granules followed by discharging the slurry into a reactor where it is contacted with superheated steam to produce dry, particulate, cold water-swelling, intact, high amylose starch granules. The cold water-swelling, intact, high amylose starch granules have greater than 15% solubles. At a starch concentration of 1%, in UDMSO (9 volumes DMSO and 1 volume 6M urea) at 25 C., the ratio of apparent viscosity of said cold water-swelling, intact, high amylose starch granules to the apparent viscosity of the parent non-pregelatinised, granular, high amylose starch is lower than 1.00. The cold water-swelling, high amylose granular starch of the invention is useful in the manufacture of food products, especially confectionery products and convenience food products.

GRANULATED PRODUCT
20240180214 · 2024-06-06 · ·

A granulated product that includes a dark-green vegetable, wherein a particle size distribution of particles having a diameter of less than 500 mm is 10% or more, and a method of producing the granulated product that includes granulating the dark-green vegetable by fluidized-bed granulation.

GRANULATED PRODUCT
20240180214 · 2024-06-06 · ·

A granulated product that includes a dark-green vegetable, wherein a particle size distribution of particles having a diameter of less than 500 mm is 10% or more, and a method of producing the granulated product that includes granulating the dark-green vegetable by fluidized-bed granulation.

WHEAT BASED BINDING AGENT
20190142049 · 2019-05-16 ·

Provided herein are compositions that are useful as binding agents for clusters, bars, and other food applications where various components need to be adhered to each other. The binding agents comprise a wheat protein isolate in combination with flour and water.

PROCESS TO PREPARE SODIUM AND/OR POTASSIUM SALT PRODUCTS, SALT PRODUCT OBTAINABLE THEREBY AND THE USE THEREOF

The present invention relates to a process to prepare a free-flowing salt product comprising sodium chloride (NaCl) and/or potassium chloride (KCl), wherein the salt product has a particle size of from 50 m to 1000 m, which process comprises the steps of (a) processing a source of pure NaCl, pure KCl, or mixture of salts, to form particles with an average size of less than 100 micrometer; (b) subsequently, compacting the particles from step a) using a pressure of from 40 to 400 MPa; and optionally, crushing the thus obtained particles; and (c) subsequently, absorbing one or more agents into the salt particles, characterized in that no agent is added in or during steps a) and b) or between steps a) and b).