The present invention relates to processes of recovering oil after liquefaction and/or from thin stillage and/or syrup/evaporated centrate from a fermentation product production process by adding a thermostable protease to the whole stillage, thin stillage and/or syrup.

The present invention relates generally to the field of recombinant fatty acid synthesis, particularly in transgenic plants. The application describes genes involved in fatty acid synthesis and provides methods and vectors for the manipulation of fatty acid composition of plant oils. In particular, the invention provides constructs for achieving the integration of multiple heterologous genes involved in fatty acid synthesis into the plant genome, such that the resulting plants produce altered levels of polyunsaturated fatty acids. Also described are methods for enhancing the expression of fatty acid biosynthesis enzymes by co-expressing a silencing suppressor within the plant storage organ.

According to the present disclosure, on the basis of all existing mutations, the tenth glycine of a BC-PC-PLC is mutated into aspartic acid, a specific enzyme activity thereof is 83% higher than that of a sequence before the mutation, and protein expression and degumming activity of unit enzyme activity do not change, so as to further reduce manufacturing costs.

According to the present disclosure, on the basis of all existing mutations, the tenth glycine of a BC-PC-PLC is mutated into aspartic acid, a specific enzyme activity thereof is 83% higher than that of a sequence before the mutation, and protein expression and degumming activity of unit enzyme activity do not change, so as to further reduce manufacturing costs.

Described herein is a method of remediating a water source of a target aquatic life. The method comprises collecting at least one target species of aquatic life from a water source, separating an oil from the solids of the target aquatic life, and refining a polyunsaturated fatty acid (PUFA) mixture from the oil. The water source is at least partially remediated by collecting the at least one target species of aquatic life from the water source.

Described herein is a method of remediating a water source of a target aquatic life. The method comprises collecting at least one target species of aquatic life from a water source, separating an oil from the solids of the target aquatic life, and refining a polyunsaturated fatty acid (PUFA) mixture from the oil. The water source is at least partially remediated by collecting the at least one target species of aquatic life from the water source.

Methods of refining palm oil in order to produce a refined, bleached and deodorized palm oil with reduced level of 3-monochloropropane-1, 2-diol (3-MCPD) ester are disclosed. The methods may include premixing a palm oil with an acid to chelate metals and form a reaction mixture, and subjecting the reaction mixture to hydrodynamic cavitation mixing for less than 1 second.

Provided is a method for upgrading a bio-based material, the method including the steps of pre-treating bio-renewable oil(s) and/or fat(s) to provide a bio-based fresh feed material, hydrotreating the bio-based fresh feed material, followed by separation, to provide a bio-propane composition.

Provided herein are pongamia oil compositions suitable for animal consumption, in particular human consumption, as well as methods of producing such compositions. The compositions are edible and non-bitter tasting, and have certain attributes that make such compositions suitable for use as and/or in various food and beverage products. Provided herein are also methods of analyzing pongamia oil.

Provided are methods to destabilize emulsion feedstocks. In the methods, a moderate temperature is applied to the feedstock to create a first mixture. The moderate temperature may be between 120 and 220 degrees Celsius. The first mixture is mixed at the moderate temperature, such as by staged mixing in some embodiments. Moreover, the first mixture is retained at the moderate temperature for up to six hours. The first mixture is separated into an oil phase, convoluted phase, and a water phase. In some embodiments, the moderate temperature may be 125 to 150 degrees Celsius, such as between 125 and 130 degrees Celsius. Moreover, the first mixture may be retained at the moderate temperature for between forty-five minutes and four hours, such as from two to four hours. The separation may occur at the moderate temperature.