Disclosed herein is a method of using dissipation factor to control the purification of candle wax compositions, comprising purifying a modified natural oil until a dissipation factor ranging from 0.0001-0.0600 is achieved.

Disclosed herein is a method of using dissipation factor to control the purification of candle wax compositions, comprising purifying a modified natural oil until a dissipation factor ranging from 0.0001-0.0600 is achieved.

The present disclosure relates to methods and systems for refining grain oil compositions using an esterase enzyme component, water, bleaching processes, and combinations thereof, and related compositions produced therefrom having one or more reduced color values. The present disclosure also relates to methods of using said compositions, e.g., as mineral oil replacements.

The present invention relates to a process for reducing an amount of intact phospholipids in a triacylglyceride oil comprising incubating the oil with a polypeptide having phospholipase A1 activity, wherein the polypeptide comprises a polypeptide having at least 80% identity to the mature amino acid sequence of SEQ ID NO: 1.

The present technology provides a method that includes contacting a composition with a caustic solution to produce a caustic-treated composition; combining the caustic-treated composition with silica particles to produce a slurry; and removing the silica particles from the slurry to produce a treated composition; wherein the composition includes one or more of animal fats, animal oils, plant fats, plant oils, vegetable fats, vegetable oils, greases, and used cooking oil and the composition includes: at least about 10 wppm of total metals, at least about 8 wppm of phosphorus, at least about 10 wppm of chlorine, at least about 10 wppm of sulfur, at least about 20 wppm of nitrogen, at least about 5 wt. % of free fatty acids; and has an acid number from about 10 mg KOH/g to about 150 mg KOH/g, and the silica particles has a particle size from about 10 microns to about 50 microns, a BET surface area from about 200 m.sup.2/g to about 1000 m.sup.2/g.

The present invention relates to methods of producing industrial products from plant lipids, particularly from vegetative parts of plants. In particular, the present invention provides oil products such as biodiesel and synthetic diesel and processes for producing these, as well as plants having an increased level of one or more non-polar lipids such as triacylglycerols and an increased total non-polar lipid content. In one particular embodiment, the present invention relates to combinations of modifications in two or more of lipid handling enzymes, oil body proteins, decreased lipid catabolic enzymes and/or transcription factors regulating lipid biosynthesis to increase the level of one or more non-polar lipids and/or the total non-polar lipid content and/or mono-unsaturated fatty acid content in plants or any part thereof. In an embodiment, the present invention relates to a process for extracting lipids. In another embodiment, the lipid is converted to one or more hydrocarbon products in harvested plant vegetative parts to produce alkyl esters of the fatty acids which are suitable for use as a renewable biodiesel fuel.

The present invention relates to methods of producing industrial products from plant lipids, particularly from vegetative parts of plants. In particular, the present invention provides oil products such as biodiesel and synthetic diesel and processes for producing these, as well as plants having an increased level of one or more non-polar lipids such as triacylglycerols and an increased total non-polar lipid content. In one particular embodiment, the present invention relates to combinations of modifications in two or more of lipid handling enzymes, oil body proteins, decreased lipid catabolic enzymes and/or transcription factors regulating lipid biosynthesis to increase the level of one or more non-polar lipids and/or the total non-polar lipid content and/or mono-unsaturated fatty acid content in plants or any part thereof. In an embodiment, the present invention relates to a process for extracting lipids. In another embodiment, the lipid is converted to one or more hydrocarbon products in harvested plant vegetative parts to produce alkyl esters of the fatty acids which are suitable for use as a renewable biodiesel fuel.

A process for manufacturing a refined vegetable oil having a reduced content of 3-MCPD esters characterized in that it comprises the following steps: treating a deodorized vegetable oil with a base in a continuous pipe reactor, and contacting the base treated oil with an adsorbent and/or an acid. The thus obtained oil is low in 3-MCPD and has a low degree of interesterification and a low DAK content. It further relates to the use a continuous pipe reactor for treating a deodorized vegetable oil with a base wherein 3-MCPD ester content is reduced in the oil.

The disclosure provides a method of obtaining an isolated phospholipid enriched krill composition. The method includes a) contacting a crude krill composition with an alcohol in an amount sufficient to provide a phospholipid enriched layer and a non-phospholipid enriched layer; b) forming a phospholipid enriched layer and a non-phospholipid enriched layer, wherein the phospholipid enriched layer is above the non-phospholipid enriched layer; c) isolating the phospholipid enriched layer and the non-phospholipid enriched layer; and d) removing the alcohol from the phospholipid enriched layer to provide an isolated phospholipid enriched krill composition.

A method for purification of a triacylglyceride oil comprising the steps: (a) admixing the triacylglyceride oil with an auxiliary trapping agent, wherein the melting temperatures of the triacylglyceride oil and the auxiliary trapping agent are substantially different, wherein the auxiliary trapping agent is soluble in the triacylglyceride oil, and wherein the auxiliary trapping agent is more polar than the triacylglyceride oil; (b) (i) crystallising the auxiliary trapping agent by cooling the mixture of step (a) below the melting temperature of the auxiliary trapping agent, wherein the auxiliary trapping agent has a higher melting temperature than the triacylglyceride oil; or (ii) crystallising the triacylglyceride oil by cooling the mixture of step (a) below the melting 10 temperature of the triacylglyceride oil, wherein the triacylglyceride oil has a higher melting temperature than the auxiliary trapping agent; and (c) separating solid and liquid phases of the product of step (b).