Provided are the crystalline form of tefluthrin of formula (I), the crystal preparation process, the analyses of the crystal through various analytical methods and using the crystal to prepare stable agrochemical formulation. Also provided is the use of various solvents towards the crystalline form preparation conditions.

Provided are the crystalline form of tefluthrin of formula (I), the crystal preparation process, the analyses of the crystal through various analytical methods and using the crystal to prepare stable agrochemical formulation. Also provided is the use of various solvents towards the crystalline form preparation conditions.

Methods of isolating phenols from phenol-containing media. The methods include combining a phospholipid-containing composition with the phenol-containing medium to generate a combined medium, incubating the combined medium to precipitate phenols in the combined medium and thereby form a phenol precipitate phase and a phenol-depleted phase, and separating the phenol precipitate phase and the phenol-depleted phase. The methods can further include extracting phenols from the separated phenol precipitate phase. The extracting can include mixing the separated phenol precipitate phase with an extraction solvent to solubilize in the extraction solvent at least a portion of the phenols originally present in the phenol precipitate phase.

Methods of isolating phenols from phenol-containing media. The methods include combining a phospholipid-containing composition with the phenol-containing medium to generate a combined medium, incubating the combined medium to precipitate phenols in the combined medium and thereby form a phenol precipitate phase and a phenol-depleted phase, and separating the phenol precipitate phase and the phenol-depleted phase. The methods can further include extracting phenols from the separated phenol precipitate phase. The extracting can include mixing the separated phenol precipitate phase with an extraction solvent to solubilize in the extraction solvent at least a portion of the phenols originally present in the phenol precipitate phase.

The disclosure provides a decolorization and purification method of BHET material, which includes the following steps. A first dose of activated carbon is added to preliminarily treat the BHET material. After the preliminary treatment, a first cooling crystallization process and filtration are performed to obtain BHET crystals. Afterwards, an oxidant is used to chemically react with the BHET crystals to destroy a dye or impurities, and then a second dose of activated carbon is added to adsorb a chemically reacted oxide. Next, a second cooling crystallization process, filtration, and drying are performed to obtain a finished product of BHET.

The disclosure provides a decolorization and purification method of BHET material, which includes the following steps. A first dose of activated carbon is added to preliminarily treat the BHET material. After the preliminary treatment, a first cooling crystallization process and filtration are performed to obtain BHET crystals. Afterwards, an oxidant is used to chemically react with the BHET crystals to destroy a dye or impurities, and then a second dose of activated carbon is added to adsorb a chemically reacted oxide. Next, a second cooling crystallization process, filtration, and drying are performed to obtain a finished product of BHET.

The invention relates to a method for the production of acetylsalicylic acid lysinate, optionally lysine acetylsalicylate.glycine, comprising the following steps: a) providing a solution of acetylsalicylic acid in ethanol; b) providing an aqueous solution of lysine; c) combining the solutions of step a) and b) to form a mixture; d) optionally stirring the mixture; e) adding acetone to the mixture; f) incubating the mixture, to allow the formation of a acetylsalicylic acid lysinate product; g) isolating the acetylsalicylic acid lysinate product; wherein acetylsalicylic acid is used in excess compared to lysine and wherein no seed crystals are added to the mixture; and optionally the following further steps: h) providing a recrystallized glycine; wherein the glycine has been recrystallized with the following steps: h1) dissolving glycine in water; h2) adding acetone to the glycine solution; h3) stirring the mixture until a precipitate is obtained; i) combining the recrystallized glycine of step h) with the acetylsalicylic acid lysinate product of step g) to obtain lysine acetylsalicylate.glycine (LASAG) particles.

The invention relates to a method for the production of acetylsalicylic acid lysinate, optionally lysine acetylsalicylate.glycine, comprising the following steps: a) providing a solution of acetylsalicylic acid in ethanol; b) providing an aqueous solution of lysine; c) combining the solutions of step a) and b) to form a mixture; d) optionally stirring the mixture; e) adding acetone to the mixture; f) incubating the mixture, to allow the formation of a acetylsalicylic acid lysinate product; g) isolating the acetylsalicylic acid lysinate product; wherein acetylsalicylic acid is used in excess compared to lysine and wherein no seed crystals are added to the mixture; and optionally the following further steps: h) providing a recrystallized glycine; wherein the glycine has been recrystallized with the following steps: h1) dissolving glycine in water; h2) adding acetone to the glycine solution; h3) stirring the mixture until a precipitate is obtained; i) combining the recrystallized glycine of step h) with the acetylsalicylic acid lysinate product of step g) to obtain lysine acetylsalicylate.glycine (LASAG) particles.

A process for solubilizing a resveratrol glycolate compound by heating the resveratrol glycolate and mixing the resveratrol glycolate with one or more glycols is disclosed. The process comprises an initial heating step of the resveratrol compound to a temperature not greater than 45 C. and a mixing step that mixes the heated resveratrol glycolate compound with at least one glycol solvent at room temperature for ten minutes to one hundred and twenty minutes.

A process for solubilizing a resveratrol glycolate compound by heating the resveratrol glycolate and mixing the resveratrol glycolate with one or more glycols is disclosed. The process comprises an initial heating step of the resveratrol compound to a temperature not greater than 45 C. and a mixing step that mixes the heated resveratrol glycolate compound with at least one glycol solvent at room temperature for ten minutes to one hundred and twenty minutes.