The present invention relates to a novel Chlamydomonas strain with an improved oil generation function, the strain of the present invention having useful mycological characteristics as a strain that provides a useful substance, such as a vegetable oil, in a microalga, as the strain has a fast cell growth speed and an excellent lipid generation function compared to conventional strains. In particular, the present invention can provide a vegetable oil with improved stability and a longer preservation period by containing, in a cell, a large amount of antioxidant pigments such as lutein and zeaxanthin, and can, thereby, be usefully used in industries such as food, medicine, cosmetics, etc., which utilize a vegetable oil.

The present invention relates to a novel Chlamydomonas strain with an improved oil generation function, the strain of the present invention having useful mycological characteristics as a strain that provides a useful substance, such as a vegetable oil, in a microalga, as the strain has a fast cell growth speed and an excellent lipid generation function compared to conventional strains. In particular, the present invention can provide a vegetable oil with improved stability and a longer preservation period by containing, in a cell, a large amount of antioxidant pigments such as lutein and zeaxanthin, and can, thereby, be usefully used in industries such as food, medicine, cosmetics, etc., which utilize a vegetable oil.

A method for producing a polyunsaturated fatty acid (PUFA) or a lipid containing a PUFA, a microbial cell containing a PUFA, and use of the microbial cell are provided. A method for producing a polyunsaturated fatty acid (PUFA) or a lipid containing a PUFA including culture of a microorganism capable of producing arachidonic acid (ARA) and/or dihomo-gamma-linolenic acid (DGLA) is provided, the method including at least one of the following steps: (a) adding an organic acid in an amount of 0.01 to 5 w/v % to a culture medium after the beginning of main culture; (b) increasing the pH of the culture medium to a range effective for culture after the beginning of the main culture; and (c) adding a metal sulfate in an amount of 0.01 to 0.5 w/w % to the main culture medium.

Provided herein are methods, compositions, and non-naturally occurring microbial organism for preparing compounds such as α-butanol, butyric acid, succinic acid, 1,4-butanediol, 1-pentanol, pentanoic acid, glutaric acid, 1,5-pentanediol, 1-hexanol, hexanoic acid, adipic acid, 1,6-hexanediol, 6-hydroxy hexanoic acid, ε-Caprolactone, 6-amino-hexanoic acid, ε-Caprolactam, hexamethylenediamine, linear fatty acids and linear fatty alcohols that are between 7-25 carbons long, linear alkanes and linear α-alkenes that are between 6-24 carbons long, sebacic acid and dodecanedioic acid comprising: a) converting a C.sub.N aldehyde and pyruvate to a C.sub.N+3 β-hydroxyketone intermediate through an aldol addition; and b) converting the C.sub.N+3 β-hydroxyketone intermediate to the compounds through enzymatic steps, or a combination of enzymatic and chemical steps.

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 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.

A method of obtaining a compound may include adding a substrate to a medium in a reactor, and reacting the substrate in the reactor to form the compound. A first stream is separated from the reaction liquid through a first membrane. A second stream is separated from the reaction liquid through a second membrane. The first membrane is a filtration membrane and the second membrane is configured for liquid-gas or liquid-liquid extraction The first membrane and the second membrane are at least partially immersed in the medium and are moved relative to the reactor during the separation steps.

An enzymatic glycerolysis method to convert an oil having a first monoacylgycerol (MAG), diacylglycerol (DAG), triacylglycerol (TAG) and fatty acid composition into a structured fat is provided. The method comprising the steps of exposing the oil to glycerol in the presence of an enzyme catalyst under conditions sufficient to convert the triacylglycerols to mono- and/or di-acylglycerols; and cooling the oil to yield the structured fat having a second monoacylgycerol, diacylglycerol, triacylglycerol and fatty acid composition, wherein the fatty acid composition of the oil is essentially retained in the structured fat. The structured fat provides a healthy substitute for saturated fats in foods.

The present invention relates to recombinant protein production in algal cells. In particular, the present invention provides methods for making recombinant polypeptides in association with accumulated lipid particles or chloroplasts. The methods involve producing the recombinant polypeptide as a fusion polypeptide with an oil body protein and the growth of the algal cells under non-homeostatic conditions to form accumulated lipid particles within the algal cells, wherein the algal lipid particles contain the fusion polypeptide.

A method of producing a mixture of pure feedstock-based native polyphenols from a feedstock. Contaminant polyphenols are first removed from an enzyme solution for converting feedstock to a product to produce a polyphenol reduced enzyme solution. The polyphenol reduced enzyme solution is combined with the feedstock and the feedstock is converted to a product and by-product. Heretofore, there has been no process available to reduce or remove the contaminant phenols introduced to the feedstock by commercial enzyme solutions. This method allows for the removal of contaminant phenols prior to introduction to the processing stream and subsequent harvesting of pure feedstock—based native polyphenols. The pure feedstock-based polyphenols are removed from the product or by-product to produce a pure mixture of feedstock-based polyphenols.