Archer Daniels Midland Company

Other

Doug Geier

John Glenn Soper

Thomas P Binder

Ahmad K Hilaly

Robert Duane Sandage

Greg Dodson

Kristen Eilts

John G Soper

Ahmad Hilaly

Processes of fractionating phospholipids are disclosed. In one embodiment, the process includes placing a phospholipid containing material in contact with an adsorbent, such that the adsorbent associates with at least one phospholipid of the phospholipid containing material. The process may further include eluting the at least one phospholipid from the adsorbent.

Processes for fractionating phospholipids

The present invention is directed to a method of preparing compositions enriched in compounds containing carbon chains of varying degrees of unsaturation using argentation chromatography. The present method utilizes an argentized cationic resin or a conditioned argentized alumina to separate compounds containing saturated or mono-unsaturated carbon chains from compounds having polyunsaturated carbon chains present in a starting composition. The invention is particularly useful for preparing a composition enriched in polyunsaturated fatty acid alkyl esters from mixtures of fatty acid esters in a starting composition derived from vegetable oils. The present invention is also directed to a method of preparing a conditioned argentized alumina adsorbent having increased selectivity for compounds containing one or more polyunsaturated carbon chains.

Method of preparing a composition using argentation chromatography

Simultaneous synthesis and purification of a fatty acid monoester biodiesel fuel from a triacylglycerol feedstock is described. In an exemplary method, the triacylglycerol feedstock is continuously contacted with a catalytic chromatographic bed comprising a first (solid phase) basic catalyst through a first port of a simulated moving bed chromatographic apparatus. A monohydric alcohol and optional second (mobile phase) basic catalyst is continuously contacted with the catalytic chromatographic bed through a second port and pumped in a first direction toward the triacylglycerol feedstock to contact the triacylglycerol in a reaction zone of the catalytic chromatographic bed where the fatty acid monoester and glycerol coproduct are formed. The fatty acid monoester is removed from the reaction zone through a product port of the simulated moving bed apparatus. Segments of the catalytic chromatographic bed are incrementally moved in a second direction, opposite the first direction, and the glycerol is removed from a raffinate port located opposite the product port of the apparatus.

Simultaneous synthesis and purification of a fatty acid monoester biodiesel fuel

Growing community of inventors

Decatur, IL, United States of America

Doug Geier