Method for the physical treatment of starch (derivatives)

• US 20080230050A1
• Filed: 03/17/2008
• Published: 09/25/2008
• Est. Priority Date: 07/04/2001
• Status: Abandoned Application

• Current Assignee: Hans-Josef Kersting, Johann Wiesmuller, Jurgen Heidlas, Lothar Heinrich, Ulrike Funke, Zhengfeng Zhang
• Original Assignee: Hans-Josef Kersting, Johann Wiesmuller, Jurgen Heidlas, Lothar Heinrich, Ulrike Funke, Zhengfeng Zhang
• Inventors: Zhang, Zhengfeng, Heidlas, Jurgen, Wiesmuller, Johann, Kersting, Hans-Josef, Funke, Ulrike, Heinrich, Lothar
• Application Number:
  US12/077,164
• Publication Number:
  US 20080230050A1
• Time in Patent Office: Days
• US Class Current: 127/32
• CPC Class Codes: C08B 30/12 Degraded, destructured or non-chemically modified starch , e.g. mechanically, enzymatically or by irradiation; Bleaching of starch preparation of chemical derivatives of starch C08B31/00
• CPC Class Codes: C08B 31/00 Preparation of derivatives of starch derivatives of amylose C08B33/00; derivatives of amylopectin C08B35/00

Abstract

The present invention relates to a method for the physical treatment of starch (derivatives) using densified gases, in which essentially the starting material is treated at process temperatures between 20 and 200° C. and at process pressures between 50 and 800° C. for at least one minute, the density of the densified gas (mixture) being >180 kg/m³. Suitable starting materials are, in particular, native plant starches, starch from genetically modified plants, or physically and/or chemically modified starches. The treatment with, in particular, densified carbon dioxide, can be carried out under defined pressure change sequences, for which, in particular, liquid aids, such as water or suitable organic solvents, can also be added. The starches thus treated have, in particular, advantages in the form of considerably reduced contents, or complete elimination, of accompanying substances, gelatinization enthalpy and gelatinization temperature, and also of the mean particle diameter and can thus be advantageously used in the food, pharmaceutical, chemistry and constructional chemistry and also agrochemical sectors, but also in other fields of application.

Claims

1-23. -23. (canceled)

24. A method for physically modifying starch, comprising treating a mixture consisting of

a) a starch selected from the group consisting of a native plant starch, starch from a genetically modified plant, a physically modified starch, a chemically modified starch and mixtures thereof,

b) a densified gas selected from the group consisting of carbon dioxide, propane, butanes, ethane, ethylene, dimethyl ether, nitrogen, sulfur hexafluoride, ammonia, partially fluorinated hydrocarbons, perfluorinated hydrocarbons and mixtures thereof, and

c) 0 to 20 % by weight of a liquid aid selected from the group consisting of water, an organic solvent, a compound having surface-active properties and mixtures thereof, said organic solvent being selected from the group consisting of alcohols having from 1 to 5 carbon atoms, ketones having from 3 to 5 carbon atoms and esters having from 2 to 7 carbon atoms, for at least one minute at a process temperature between 20 and 200°

C. and a process pressure between 50 and 800 bar, wherein the density of the densified gas is greater than 180 kg/m.

25. The method of claim 24, wherein the starch is a native plant starch from maize, wheat or potatoes.

26. The method of claim 24, wherein the starch is from genetically modified maize, wheat or potatoes.

27. The method of claim 24, wherein the starch has a water content between 5 and 30 % by weight.

28. The method of claim 24, wherein the process temperature is from 31 to 180°

C.

29. The method of claim 24, wherein the process pressure is between 100 and 500 bar.

30. The method of claim 24, wherein the density of the densified gas is between 400 and 1000 kg/m³.

31. The method of claim 24, wherein the mixture is treated for 30 to 200 minutes.

32. The method of claim 24, wherein the mixture while treated is subjected to a succession of pressure pulsations.

33. The method of claim 32, comprising 1 to 100 pulsations.

34. The method of claim 32, wherein the pressure difference between individual pulsations is no greater than ten times the critical pressure of said densified gas.

35. The method of claim 24, wherein the mixture is treated batchwise.

36. The method of claim 24, wherein the densified gas is carbon dioxide.

37. A native plant starch, physically modified by the method of claim 24, having a gelatinization enthalpy that is more than 30% lower than the gelatinization enthalpy of the non-modified starch.

38. The physically modified starch of claim 37, having a gelatinization enthalpy of less than 10 J/g.

39. A native plant starch, physically modified by the method of claim 24, having a gelatinization temperature that is 2 to 10°

C. lower than the gelatinization temperature of the non-modified starch.

40. A native plant starch, physically modified by the method of claim 24, having a mean particle diameter that is more than 5% larger than the mean particle diameter of the non-modified starch.

41. A native plant starch, physically modified by the method of claim 24, having a content of water and lipids that is from 30 to 90% lower than the content of water and lipids of the non-modified starch.

42. The method of claim 25, wherein the densified gas is carbon dioxide.

43. The method of claim 32, wherein the densified gas is carbon dioxide.