The disclosure provides methods using mixed substrate cofeeding for bioproduct synthesis, which enables faster, more efficient, and higher yield carbon conversion in various organisms.

The present invention relates to processes for extracting lipid from vegetative plant parts such as leaves, stems, roots and tubers, and for producing industrial products such as hydrocarbon products from the lipids. Preferred industrial products include alkyl esters which may be blended with petroleum based fuels.

The present invention concerns an oleaginous yeast variant of the species Rhodosporidium azoricum characterized by higher biomass yields and intra- cellular lipid accumulation useful for the production of bio-fuels higher, in determined conditions, with respect to the wild type strain of the same species. Furthermore, the invention concerns a method through which said oleaginous yeast variant of the species Rhodosporidium azoricum was obtained. The invention further concerns the lipid production by means of said variant strain of oleaginous yeast of the species Rhodosporidium azoricum.

Disclosed are transformed cells comprising one or more genetic modifications that affect the lipid content of the cell, e.g., by increasing the concentration of oleic acid in the cell relative to an unmodified cell of the same type. Also disclosed are methods for modifying the lipid content of a cell by increasing the activity of one or more proteins in the cell and/or by decreasing the activity of one or more proteins in the same cell.

Disclosed are transformed cells comprising one or more genetic modifications that increase the lipid content of the cell, e.g., relative to an unmodified cell of the same type. Also disclosed are methods for increasing the lipid content of a cell by increasing the activity of one or more proteins in the cell and/or by decreasing the activity of one or more proteins in the cell.

The disclosure relates to microbial lipid compositions produced by oleaginous microorganisms as alternatives to plant-derived palm oil. The microbial lipid compositions may have one or more characteristics of plant-derived palm oil. These compositions may be fractionable or otherwise capable of separation into different states. Further provided are products produced by or comprising the microbial lipids.

The disclosure relates to microbial lipid compositions produced by oleaginous microorganisms as alternatives to plant-derived palm oil. The microbial lipid compositions may have one or more characteristics of plant-derived palm oil. These compositions may be fractionable or otherwise capable of separation into different states. Further provided are products produced by or comprising the microbial lipids.

Disclosed herein are rubber compositions comprising bio-oil produced by a recombinant cell. Also disclosed are methods of controlling the variability of fatty acid content in bio-oil containing rubber compositions or tires comprising at least one component incorporating the bio-oil containing rubber composition, and a method of providing a bio-oil-containing tire with a reduced carbon footprint.

A method for producing cis-unsaturated fatty acid includes the operations below. (i) An oil-water mixture is provided, wherein the oil-water mixture includes 1 to 10 parts by weight of oil and 1 part by weight of water. (ii) 0.002 to 0.5 parts by weight of a recombinant Candida rugosa lipase 1 (rCRL1) is added into the oil-water mixture. (iii) The oil-water mixture is emulsified. (iv) The emulsified oil-water mixture is hydrolyzed and fatty acid is generated. (v) Oil-water is separated at a temperature of 55° C. to 65° C. and an oil phase layer is extracted. (vi) The cooling and filtering step is performed to obtain cis-unsaturated fatty acid.

A method for producing cis-unsaturated fatty acid includes the operations below. (i) An oil-water mixture is provided, wherein the oil-water mixture includes 1 to 10 parts by weight of oil and 1 part by weight of water. (ii) 0.002 to 0.5 parts by weight of a recombinant Candida rugosa lipase 1 (rCRL1) is added into the oil-water mixture. (iii) The oil-water mixture is emulsified. (iv) The emulsified oil-water mixture is hydrolyzed and fatty acid is generated. (v) Oil-water is separated at a temperature of 55° C. to 65° C. and an oil phase layer is extracted. (vi) The cooling and filtering step is performed to obtain cis-unsaturated fatty acid.