Phytosterol esterification product and method of make same

a technology of esterification product and phytosterol, which is applied in the field of phytosterols, can solve the problems of brittle product, difficult to incorporate free sterols into edible fats or oils, and pose challenges in the manufacture of food products for consumer use, and achieve the effect of greater cholesterol-lowering potential

Inactive Publication Date: 2007-06-28
BUNGE OILS INC
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Benefits of technology

[0017] It is another object of the invention to provide a phytosterol-based product that is substantially solid at room temp...

Problems solved by technology

It is difficult to incorporate free sterols into edible fats or oils because of their insolubility, whereas sterols esterified to fatty acids are more fat soluble.
While phytosterols possess desirable qualities in terms of potential for lowering cholesterol, they can pose challenges in the manufacture of food products for consumer use.
While conventional fatty acids tend to form round crystal structures that promote spreadability and ease of handling, phytosterols tend to form sharp needle-like crystals at a...

Method used

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  • Phytosterol esterification product and method of make same
  • Phytosterol esterification product and method of make same
  • Phytosterol esterification product and method of make same

Examples

Experimental program
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example 1

[0040] A mixture of 60% phytopowder, 38% palm flakes and 2% glycerin was charged to a reaction flask with a nitrogen sparge, an agitator, and a stainless steel temperature probe. This same reaction flask with nitrogen sparge, agitator, and temperature probe was used in each of the following examples. The mixture was brought to a temperature of about 160° C., and stannous chloride catalyst was added. The temperature was brought to about 180-210° C., and the esterification reaction was allowed to proceed for about 2.5 hours under vacuum. Difficulties were noted with effective removal of evolved steam during the esterification reaction. The reaction mixture then was treated with 0.7% citric acid neutralizing agent for about 10 minutes. The neutralized material was treated with Filter Aid and Bleaching clay for about 10 minutes, and then filtered. It was determined that the esterification reaction was 44.6% complete. The final product had 8.35 ppm tin as residual catalyst, and 0.3% mois...

example 2

[0041] A mixture of 75% phytopowder, 20% palm flakes and 5% glycerin was charged to the reaction flask. The mixture was brought to a temperature of about 160° C., and stannous chloride catalyst was added. The method was carried out as described above, except that the temperature of the esterification reaction was in the range of about 180-230° C., and steam was more effectively removed by use of two cold fingers. It was determined that the esterification reaction was 48.3% complete. The final product had 34.90 ppm tin as residual catalyst.

example 3

[0042] A mixture of 60% phytopowder, 20% palm flakes, 15% high oleic canola oil and 5% glycerin was charged to the reaction flask. The mixture was brought to a temperature of about 160° C., and stannous chloride catalyst was added. The method was carried out as described above, except that the temperature of the esterification reaction was in the range of about 180-225° C., and the neutralization reaction time was increased to about 20 minutes. It was determined that the esterification reaction was only 6.9% complete. The final product had 1.01 ppm tin as residual catalyst.

[0043] A differential scanning calorimetry analysis for this product is shown in FIG. 1. It may be seen that the melting curve show a first peak at about 26 C, followed by a second peak at about 34 C, and a final peak at about 110 C. The cooling curve shows a first peak at about 95 C, a second peak at about 89 C, followed by a third peak at abut 14.5 C. It may be seen that the peaks are relatively broad, indicati...

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PUM

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Abstract

An ingredient suitable for use in the manufacture of specialty margarines and bakery shortenings with nutritional and functional benefits is the reaction product of a phytosterol material esterified with a saturated fatty acid material. The reaction product is substantially solid at ambient temperature, and thus is suitable for use as an ingredient in solid shortening products, yet without the adverse health effects believed to be associated with saturated fatty acids. In the method of making the product, the esterification reaction is carried out at elevated temperatures, under vacuum, and for a relatively longer duration than prior art procedures. The esterification reaction may be carried out in the presence of a catalyst and optionally, high oleic canola oil. The reaction product is neutralized, then filtered at least once and preferably twice to remove any residual catalyst.

Description

[0001] This invention relates to a class of phytosterol esters that are useful as ingredients in food products. More particularly, this invention relates to a class of phytosterol esters that are useful as ingredients in the preparation of specialty shortening products with nutritional and functional benefits, and that are substantially solid at ambient temperatures, and to methods of their manufacture. BACKGROUND OF THE INVENTION [0002] The term “phytosterols” as used herein covers both plant sterols, plant stanols, wood sterols, and wood stanols. Plant sterols are naturally occurring substances that are components of edible vegetable oils. Plant stanols, occurring in nature at a lower level, are saturated fatty acid compounds of the respective plant sterols. Wood sterols and wood stanols are also naturally occurring substances that are present in whole or in part from tall oil, a product derived during the processing of paper from wood. Commercial quantities of plant stanols are d...

Claims

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Application Information

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IPC IPC(8): A23D9/00A23L33/00
CPCA23D7/001A23D9/007A23D9/04
Inventor NAKHASI, DILIPDANIELS, ROGEREARTLY, JOSHUA
Owner BUNGE OILS INC
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