Process for purifying starches
a technology of starch and process, applied in the field of purifying starch, can solve the problems of unsuitable odor, unsatisfactory starch to affect the taste, odor or color of the foods in which it is used, and modification of the starch base can also affect the flavor, so as to achieve the effect of improving taste, odor or color
- Summary
- Abstract
- Description
- Claims
- Application Information
AI Technical Summary
Benefits of technology
Problems solved by technology
Method used
Image
Examples
example 1
[0044]Preparation of a purified stabilized and crosslinked starch derivative. A stabilized and cross-linked waxy corn starch (351.61 g), (THERMFLO® Starch, commercially available from National Starch and Chemical, Bridgewater, N.J., US) was loaded in the 600 ml extraction vessel of the supercritical CO2 extraction unit (model Spe-ed SFE, Applied Separations Co.). The starch was then pre-heated to 80° C. and CO2 was pumped into the vessel until a pressure of 620 bar was attained. The exact process details for the subsequent static and dynamic extractions are given in Table 1.
TABLE 1Static and Dynamic Extraction Process DetailsTimeCO2 flowTemperaturePressureCumulated[min][l / min][° C.][bar]extract [g]09806200.005Static806200.101568062023Static806203358062041Static80620515806200.2358Static806206858062071580-1006560.2475Static10065685510065690—1006560.2590-110De-10000.32pressurize
[0045]Based on these operating conditions, the overall solvent to feed ratio was 1.23. The collected extract ...
example 2
[0049]Preparation of a purified acetylated starch adipate. A waxy corn starch, modified with acetic adipic mixed anhydride, (350.4 g, Colflo67® starch, available from National Starch and Chemical, Bridgewater, N.J., US) was loaded in the 600 ml extraction vessel of the supercritical CO2 extraction unit (model Spe-ed SFE, available from Applied Separations Co.). The starch was pre-heated to 80° C. and CO2 was pumped into the vessel until a pressure of 620 bar (62.0 MPa) was attained. The exact process details for the subsequent static and dynamic extraction are described in Table 3.
TABLE 3Static and Dynamic Extraction Process DetailsTimeCO2 flowTemperaturePressureCumulated[min][l / min][° C.][bar]extract [g]06806200.010Static806200.282068062035Static806200.54568062055Static806200.8555-75De-80—0.89pressurize
[0050]Based on these operating conditions the overall solvent to feed ratio was 1.13.
[0051]The volatile components of the base starch and the purified starch were examined by GC / MS a...
example 3
[0053]An acid converted, cold water soluble, high amylose starch for use in yogurt was treated via solid-matrix supercritical CO2 and compared against the same untreated starch for clean taste when used in yogurt. Sample A was untreated, Sample B was treated at 80° C. and 620 bar, and Sample C was treated at 60° C. and 345 bar. Yogurts were prepared containing the treated and un-treated starch and tested for cleanness of taste by an expert taste panel. The yogurts containing the supercritical CO2 treated starches, Samples B and C, were both characterized by the expert panel as significantly cleaner in taste compared to Sample A, the yogurt containing the un-treated starch; Sample B was characterized as having the cleanest taste of the three.
PUM
| Property | Measurement | Unit |
|---|---|---|
| temperatures | aaaaa | aaaaa |
| pressures | aaaaa | aaaaa |
| pressures | aaaaa | aaaaa |
Abstract
Description
Claims
Application Information
Login to View More 


