C11C3/10

Enrichment of triterpine esters
09809618 · 2017-11-07 · ·

A new process for enriching triterpene esters comprising: providing a mixture comprising a non-distilled vegetable oil and/or a non-distilled vegetable fat, further comprising triterpene esters, performing a mild transesterification with a lower alcohol, removing lower alcohol esters by deodorization, physical refining, evaporation or distillation, and recovering the remaining fraction rich in triterpene esters. Triterpene esters enriched with the method as well as uses of the same are also provided. One advantage is that it is a more economically viable way of achieving higher concentration of triterpene esters. There is both the chance to fully keep the natural distribution of triterpene esters but in the other end also to replace the natural level of cinnamic and acetic acids-triterpene esters with a high level of long fatty acid triterpene-esters.

Method for preparation of a group 4 metal silicate and use thereof

The invention provides a method for the preparation of an amorphous silicate of at least one metal from the Group 4 of the Periodic Table of Elements with a total pore volume of at least 0.3 mL/g. The method of preparation involves the use of pore shaping conditions, which can be the use of a pore shaper and optionally an increased precipitation temperature, e.g. at least 60° C. The silicate of the invention is especially suitable in catalytic reactions such as esterifications, Michael additions, transesterifications, (ep)oxidations, hydroxylations, or in adsorbance of small inorganic and organic molecules e.g. CO.sub.2 or aromatic compounds.

Method for preparation of a group 4 metal silicate and use thereof

The invention provides a method for the preparation of an amorphous silicate of at least one metal from the Group 4 of the Periodic Table of Elements with a total pore volume of at least 0.3 mL/g. The method of preparation involves the use of pore shaping conditions, which can be the use of a pore shaper and optionally an increased precipitation temperature, e.g. at least 60° C. The silicate of the invention is especially suitable in catalytic reactions such as esterifications, Michael additions, transesterifications, (ep)oxidations, hydroxylations, or in adsorbance of small inorganic and organic molecules e.g. CO.sub.2 or aromatic compounds.

Reaction system for producing fatty alkyl esters using a liquid-film reactor operated countercurrentwise

This invention discloses a reaction system for producing fatty-acid alkyl esters using liquid film reactors, with countercurrent flow scheme based on the alcoholysis of fats and oils. Reaction system comprises a descending film reactor using semi-structured packing for generating interfacial area. It is fed through the bottom with oil or fat, and with a mixture containing alcohol, glycerol and catalyst through an intermediate stage. Products are a mixture of fatty-acid alkyl esters, alcohol and catalyst and alcohol, glycerol and catalyst, exit via the top and the bottom of the reactor, respectively. Volumetric packing fraction is between 2% and 50%, reaction temperature from 25 to 180° C., molar ratio alcohol to oil between 3:1 and 10:1, and CH3OH, NaOH, KOH, or their mixtures (0.5% to 3% based on the oil mass flow rate). Conversion and yield in a single reaction step are greater than 99.7% and 99.9%, respectively.

Reaction system for producing fatty alkyl esters using a liquid-film reactor operated countercurrentwise

This invention discloses a reaction system for producing fatty-acid alkyl esters using liquid film reactors, with countercurrent flow scheme based on the alcoholysis of fats and oils. Reaction system comprises a descending film reactor using semi-structured packing for generating interfacial area. It is fed through the bottom with oil or fat, and with a mixture containing alcohol, glycerol and catalyst through an intermediate stage. Products are a mixture of fatty-acid alkyl esters, alcohol and catalyst and alcohol, glycerol and catalyst, exit via the top and the bottom of the reactor, respectively. Volumetric packing fraction is between 2% and 50%, reaction temperature from 25 to 180° C., molar ratio alcohol to oil between 3:1 and 10:1, and CH3OH, NaOH, KOH, or their mixtures (0.5% to 3% based on the oil mass flow rate). Conversion and yield in a single reaction step are greater than 99.7% and 99.9%, respectively.

Phospholipid compositions enriched for palmitoleic, myristoleic or lauroleic acid, their preparation and their use in treating metabolic and cardiovascular disease

The present invention concerns phospholipid compositions having a relatively high concentration of compounds of the following structure (I): wherein at least one of R.sup.1 and R.sup.2 is palmitoleoyl, myristoleoyl or lauroleoyl and methods for their preparation. The present invention also concerns the use of these phospholipid compositions to treat a variety of disorders by administering the composition to a patient in need thereof. ##STR00001##

Phospholipid compositions enriched for palmitoleic, myristoleic or lauroleic acid, their preparation and their use in treating metabolic and cardiovascular disease

The present invention concerns phospholipid compositions having a relatively high concentration of compounds of the following structure (I): wherein at least one of R.sup.1 and R.sup.2 is palmitoleoyl, myristoleoyl or lauroleoyl and methods for their preparation. The present invention also concerns the use of these phospholipid compositions to treat a variety of disorders by administering the composition to a patient in need thereof. ##STR00001##

EDIBLE FAT COMPOSITION
20170251695 · 2017-09-07 ·

The present invention relates to a process for preparing a cocoa biomass with a modified fat phase by mixing a cocoa biomass having a fat phase I with a vegetable fat having fat phase 2, thereby forming fat phase 3 in the cocoa biomass, followed by separating fat phase 3 from the cocoa biomass to a desired fat level of the cocoa biomass. The present invention also relates to fat compositions comprising said cocoa biomass with a modified fat phase and edible products comprising said cocoa biomass with a modified fat profile, and uses of the process.

COMPOSITION CONTAINING EICOSAPENTAENOIC ACID ALKYL ESTER, AND METHOD FOR PRODUCING SAME
20170252315 · 2017-09-07 ·

Provided are: an eicosapentaenoic acid alkyl ester-containing composition which comprises 96-99 area % of an eicosapentaenoic acid alkyl ester, wherein the content of an arachidonic acid alkyl ester is 0.7 area % or less, and the content of mono-trans forms of the eicosapentaenoic acid alkyl ester is 2.5 area % or less; a method for producing a high-concentration eicosapentaenoic acid alkyl ester-containing composition, which comprises performing rectification on an eicosapentaenoic acid alkyl ester-containing composition with the degree of vacuum being 0.2 Torr or less and at a whole-column temperature 190° C. or less, and performing a concentration treatment on the rectified composition using chromatography, the eicosapentaenoic acid alkyl ester-containing composition being obtained by alkyl esterifying a feed oil containing eicosapentaenoic acid.

DIETARY BUTYRATE AND ITS USES

Use of a compound having the formula (1), formula (2), formula (3) or formula (4), or combinations thereof, for promoting and/or accelerating myelination, wherein R.sup.1, R.sup.2, R.sup.3, R.sup.4, R.sup.5 and R.sup.6 are independently a long chain fatty acid having between 16 and 20 carbons.

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