Described herein are methods of preparing cutin-derived monomers, oligomers, or combinations thereof from cutin-containing plant matter. The methods can include heating the cutin-derived plant matter in a solvent at elevated temperature and pressure. In some preferred embodiments, the methods can be carried out without the use of additional acidic or basic species.

Described herein are methods of preparing cutin-derived monomers, oligomers, or combinations thereof from cutin-containing plant matter. The methods can include heating the cutin-derived plant matter in a solvent at elevated temperature and pressure. In some preferred embodiments, the methods can be carried out without the use of additional acidic or basic species.

A method for preparing the borate ester using a lithium compound includes: under the inert gas, stirring and mixing carboxylic acid and borane, and a catalyst lithium compound is added, then the borate ester is obtained with hydroboration; wherein the hydroboration is at room temperature for 10 to 80 min. After the hydroboration and is stopped by contacting air, the solvent is removed under reduced pressure, to obtain the borate esters with different substituents. The lithium compounds are n-butyl lithium, lithium aniline, p-methyl lithium aniline, o-methyl lithium aniline, 2-methoxyaniline lithium, 4-methoxyaniline lithium, 2,6-dimethylaniline lithium, and 2,6-diisopropylaniline lithium. The lithium compounds disclosed in the present invention can catalyze the boron hydrogenation reaction of carboxylic acid and borane with high activity under room temperature conditions; the amount of lithium compound is 0.1-0.9% of the molar amount of carboxylic acid.

A method for preparing the borate ester using a lithium compound includes: under the inert gas, stirring and mixing carboxylic acid and borane, and a catalyst lithium compound is added, then the borate ester is obtained with hydroboration; wherein the hydroboration is at room temperature for 10 to 80 min. After the hydroboration and is stopped by contacting air, the solvent is removed under reduced pressure, to obtain the borate esters with different substituents. The lithium compounds are n-butyl lithium, lithium aniline, p-methyl lithium aniline, o-methyl lithium aniline, 2-methoxyaniline lithium, 4-methoxyaniline lithium, 2,6-dimethylaniline lithium, and 2,6-diisopropylaniline lithium. The lithium compounds disclosed in the present invention can catalyze the boron hydrogenation reaction of carboxylic acid and borane with high activity under room temperature conditions; the amount of lithium compound is 0.1-0.9% of the molar amount of carboxylic acid.

Alkoxylated hydroxycarboxylic acids according to a formula I′ are provided herein, as well as uses thereof and a process for production thereof. ##STR00001##
Compound 2-[2-(2-hydroxyethoxy)ethoxy]propanoic acid being exclude.

Alkoxylated hydroxycarboxylic acids according to a formula I′ are provided herein, as well as uses thereof and a process for production thereof. ##STR00001##
Compound 2-[2-(2-hydroxyethoxy)ethoxy]propanoic acid being exclude.

Hydroxycarboxylic acids may be biosynthesized from a carbonaceous feedstock and then isolated through forming and subsequently hydrolyzing an intermediate sophorolipid. After biosynthesizing a hydroxycarboxylic acid in a cell culture medium or otherwise providing a hydroxycarboxylic acid in a first aqueous medium, the hydroxycarboxylic acid and glucose may be converted into at least one sophorolipid by a suitable microorganism or an enzyme cocktail. The at least one sophorolipid may be then be separated from the cell culture medium or first aqueous medium and then hydrolyzed in a second aqueous medium to form the hydroxycarboxylic acid and glucose as free components separate from the cell culture medium or first aqueous medium. The hydroxycarboxylic acid is present as a phase separate from the second aqueous medium and the glucose remains in the second aqueous medium.

Hydroxycarboxylic acids may be biosynthesized from a carbonaceous feedstock and then isolated through forming and subsequently hydrolyzing an intermediate sophorolipid. After biosynthesizing a hydroxycarboxylic acid in a cell culture medium or otherwise providing a hydroxycarboxylic acid in a first aqueous medium, the hydroxycarboxylic acid and glucose may be converted into at least one sophorolipid by a suitable microorganism or an enzyme cocktail. The at least one sophorolipid may be then be separated from the cell culture medium or first aqueous medium and then hydrolyzed in a second aqueous medium to form the hydroxycarboxylic acid and glucose as free components separate from the cell culture medium or first aqueous medium. The hydroxycarboxylic acid is present as a phase separate from the second aqueous medium and the glucose remains in the second aqueous medium.

Hydroxycarboxylic acids may be biosynthesized from a carbonaceous feedstock and then isolated through forming and subsequently hydrolyzing an intermediate sophorolipid. After biosynthesizing a hydroxycarboxylic acid in a cell culture medium or otherwise providing a hydroxycarboxylic acid in a first aqueous medium, the hydroxycarboxylic acid and glucose may be converted into at least one sophorolipid by a suitable microorganism or an enzyme cocktail. The at least one sophorolipid may be then be separated from the cell culture medium or first aqueous medium and then hydrolyzed in a second aqueous medium to form the hydroxycarboxylic acid and glucose as free components separate from the cell culture medium or first aqueous medium. The hydroxycarboxylic acid is present as a phase separate from the second aqueous medium and the glucose remains in the second aqueous medium.

Provided are a carboxylic acid compound of formula I, and a preparation method therefor and application thereof. When being applied to the extraction and separation of metal ions, the carboxylic acid compound can achieve a high separation coefficient, low back extraction acidity, high load rate, high back extraction rate, high stability, and low water solubility, so that the extraction process is stable, and environmental pollution and components can be reduced. The present application can be used in various systems such as ternary battery recycling and battery-grade nickel sulfate preparation.