Process for modifying starches

Patent metadata

Field	Value
Publication number	US-10239958-B2
Application number	US-201615254610-A
Country	US
Kind code	B2
Filing date	Sep 1, 2016
Priority date	Apr 7, 2010
Publication date	Mar 26, 2019
Grant date	Mar 26, 2019

Abstract

A process for modifying starch comprises atomising an aqueous slurry of non-pregelatinised starch into an internal chamber in a bi-fluid nozzle of a spray dryer and treating the atomized slurry, in the internal chamber, with superheated steam to cause partial gelatinisation of the starch. The aqueous slurry containing partially gelatinised starch is discharged through an outlet in the internal chamber into a reactor where the droplets containing the partially gelatinised starch are subjected to further treatment with superheated steam, resulting in the completion of the gelatinisation of the starch in the reactor. Also disclosed is a bi-fluid nozzle for use in spray drying starch which comprises a nozzle body, a nozzle cap and an internal chamber located between the nozzle body and the nozzle cap. The nozzle body comprises at least one atomiser, for connection to a supply of an aqueous starch slurry, for atomising the slurry into the internal chamber and it has at least one inlet, for connection to a supply of superheated steam under pressure, for introducing superheated steam under pressure into the internal chamber. The nozzle cap comprises at least one outlet from the internal chamber. The internal chamber also comprises an interchangeable spacer element with a length of from 10 to 60 mm enabling the length of the internal chamber to be changed. A pregelatinised starch and its use in foods, especially baby foods and infant formulas, feed, pharmaceuticals, cosmetics and personal care products are also disclosed.

First claim

The invention claimed is:

1. A process for modifying starch comprising the steps:
a) supplying an aqueous slurry of non-pregelatinised starch to a bi-fluid nozzle of a spray dryer, wherein the hi-fluid nozzle has an internal chamber having at least one inlet for the aqueous slurry of non-pregelatinised starch, at least one inlet for the supply of superheated steam and at least one outlet
b) atomising the aqueous slurry of non-pregelatinised starch into the internal chamber of the hi-fluid nozzle;
c) injecting superheated steam into the internal chamber of the bi-fluid nozzle whereby the atomised aqueous slurry of non-pregelatinised starch is heated by the superheated steam in the internal chamber to produce a slurry of partially gelatinised starch, wherein the temperature of the superheated steam at the at least one inlet into the internal chamber is in the range of 150° to 650° C.
d) discharging the slurry of partially gelatinised starch from the internal chamber through the at least one outlet into a reactor; and
e) contacting the discharged slurry in the reactor with superheated steam to completely gelatinise the partially gelatinised starch in the discharged slurry and to dry the completely gelatinised starch to produce dry, particulate pregelatinised starch.

2. A process according to claim 1 , wherein the non-pregelantised starch in the aqueous slurry of non-pregelatinised starch has an amylose content not greater than 35% by weight.

3. A process according to claim 1 ,
wherein the aqueous slurry of non-pregelatinised starch has a solids content of from 1 to 40% by weight.

4. The process of claim 1 , wherein the temperature of the superheated steam at the at least one inlet into the internal chamber is in the range of 250° to 550° C.

5. The process of claim 1 , wherein the temperature of the superheated steam at the at least one inlet into the internal chamber is in the range of 350° to 450° C.

6. The process of claim 1 , wherein the starch has an amylose content not greater than 10% by weight.

7. The process of claim 1 , wherein the non-pregelantised starch in the aqueous slurry of non-pregelatinised starch has an amylose content not greater than 5% by weight.

8. The process according to claim 1 , wherein the aqueous slurry of non-pregelatinised starch has a solids content of from 20 to 40% by weight.

Assignees

• Cargill Inc

Inventors

• Berckmans Marc
• Coppin Jozef Victor Jean-Marie
• Debon Stephane Jules Jerome

Classifications

• A61K2800/10

  General cosmetic use · CPC title

• A61K8/732

  Starch; Amylose; Amylopectin; Derivatives thereof · CPC title

• A61K8/042

  Gels · CPC title

• C08B30/16

  Apparatus therefor · CPC title

• A23K20/163

  Sugars; Polysaccharides · CPC title