A power generation system, which includes a source of a seed oil, a source of alcohol, and a reactor in communication with the source of seed oil and the source of alcohol. The reactor produces a biofuel product. The system has a power source that operates on a biofuel energy source to produce heated exhaust and is in communication with the reactor to utilize a portion of the biofuel product as its biofuel energy source. The system has a heat transfer mechanism that transfers heat from the exhaust manifold to the reactor. The power source also converts mechanical power into electrical power. Also disclosed is a system that involves extraction of oil from an oilseed product. A method of extracting oil from an oilseed product, a method of making a transesterified seed oil, and a method of making a biofuel are also disclosed, as are products obtained thereby.

A power generation system, which includes a source of a seed oil, a source of alcohol, and a reactor in communication with the source of seed oil and the source of alcohol. The reactor produces a biofuel product. The system has a power source that operates on a biofuel energy source to produce heated exhaust and is in communication with the reactor to utilize a portion of the biofuel product as its biofuel energy source. The system has a heat transfer mechanism that transfers heat from the exhaust manifold to the reactor. The power source also converts mechanical power into electrical power. Also disclosed is a system that involves extraction of oil from an oilseed product. A method of extracting oil from an oilseed product, a method of making a transesterified seed oil, and a method of making a biofuel are also disclosed, as are products obtained thereby.

Blown corn stillage oils and methods for making blown corn stillage oils are disclosed. In one aspect the corn stillage oils are stripped to reduce the acid value of the resulting blown, stripped corn stillage oil. The method includes heating a corn stillage oil to a temperature of at least 90° C., and passing air through the heated oil to produce a blown corn stillage oil having a viscosity of at least 50 cSt at 40° C. In one aspect, the blown corn stillage oil is stripped to reduce the acid value of the blown, stripped corn stillage oil to 5 mg KOH/gram or less.

A system and method for the conversion of free fatty acids to glycerides and the subsequent conversion of glycerides to glycerin and biodiesel includes the transesterification of a glyceride stream with an alcohol. The fatty acid alkyl esters are separated from the glycerin to produce a first liquid phase containing a fatty acid alkyl ester rich (concentrated) stream and a second liquid phase containing a glycerin rich (concentrated) stream. The fatty acid alkyl ester rich stream is then subjected to distillation, preferably reactive distillation, wherein the stream undergoes both physical separation and chemical reaction. The fatty acid alkyl ester rich stream is then purified to produce a purified biodiesel product and a glyceride rich residue stream. The glycerin rich second liquid phase stream may further be purified to produce a purified glycerin product and a (second) wet alcohol stream. Neutralization of the alkaline stream, formed during the alkali-catalyzed transesterification process, may proceed by the addition of a mineral or an organic acid.

A process of preparation of carboxylic acids by oxidative cleavage of compounds having substituted or non-substituted, linear or branched, saturated or unsaturated alkyl chains containing at least one vicinal diol or an epoxide in the presence of an oxidant comprising molecular oxygen and a heterogeneous catalyst comprising a copper oxide.

A powder dispersant includes an ester compound of a polyglycerol having an average degree of polymerization of the polyglycerol, calculated from its hydroxyl value, in the range 2 to 20, a monovalent carboxylic acid or at least one derivative thereof, and a divalent carboxylic acid or at least one derivative thereof.

The present invention relates to a method for the production of an ozonized olive oil with a controlled degree of ozonization, wherein said method comprises at least one step of putting the olive oil into contact with ozone in the presence of water.

A method for producing lipid particles, including: injecting molten lipids directly into a liquid at a temperature lower than a melting point of the lipids through a liquid supply port of a two-fluid nozzle while injecting a gas directly into the liquid through a gas supply port of the two-fluid nozzle, so that the molten lipids are dispersed and atomized into particles in the liquid due to the gas and the particles are solidified to form lipid particles. The lipids have a water solubility of 10 g/L or less at 25° C. and are solid at 25° C. The two-fluid nozzle is heated to a temperature at least 10° C. higher than the melting point of the lipids. A ratio D50/Nd of a volume median diameter D50 of the lipid particles to an orifice diameter Nd of the liquid supply port of the two-fluid nozzle is 0.0017 or more and 0.17 or less.

Processes for transesterifying wax esters. Implementations may include: providing a feedstock including wax esters, contacting the feedstock with a lipase, and catalytically transesterifying the wax esters in the feedstock with the lipase to form a transesterified product. An oxidative stability index (OSI) of the transesterified product may be greater than an OSI of the feedstock.

Provided is means of thickening a liquid component, wherein the thickener contains an oil and/or fat composition, the oil and/or fat composition contains an oil and/or fat component containing one or more types of XXX-type triglycerides having fatty acid residues X, each with x carbon atoms, at positions 1 to 3 of glycerin, x, the number of carbon atoms, is an integer selected from 10 to 22, and the XXX-type triglyceride is contained at 50% by mass or more relative to a content of the oil and/or fat component being 100% by mass; or the thickener, wherein the oil and/or fat composition is a powder oil and/or fat composition having a loose bulk density of 0.05 to 0.6 g/cm.sup.3, the oil and/or fat component contains a 3-type oil and/or fat, and a particle of the powder oil and/or fat composition has a plate shape.