The invention relates to a process for the chromatographic purification of a starting stream containing ammonium sulfate and 2-hydroxy-2-methylpropionic acid, comprising: passage of the starting stream through a bed of stationary phase; elution of a raffinate enriched in ammonium sulfate and depleted in 2-hydroxy-2-methylpropionic acid; and elution of an extract enriched in 2-hydroxy-2-methylpropionic acid and depleted in ammonium sulfate.

Provided in the present invention are ingenol compounds and a use thereof in preparing an anti-HIV latency drug. In particular, provided in the present invention is a use of ingenol compounds and pharmaceutically acceptable salts thereof for preparing a drug for: (a) intervening with HIV viral latency; (b) activating an HIV virus that has been integrated into mammalian genomes; and/or (c) inducing the expression of the dormant HIV provirus in infected cells. The compounds of the present invention may also be used in combination with antiretroviral drugs to accelerate the removal of latent viral reservoirs.

Provided in the present invention are ingenol compounds and a use thereof in preparing an anti-HIV latency drug. In particular, provided in the present invention is a use of ingenol compounds and pharmaceutically acceptable salts thereof for preparing a drug for: (a) intervening with HIV viral latency; (b) activating an HIV virus that has been integrated into mammalian genomes; and/or (c) inducing the expression of the dormant HIV provirus in infected cells. The compounds of the present invention may also be used in combination with antiretroviral drugs to accelerate the removal of latent viral reservoirs.

A process is useful for producing optical molding materials on the basis of methyl methacrylate (MMA), wherein this MMA has been produced by an optimized method and the molding materials feature in particular a very low yellowness index. This MMA has been produced by direct oxidative esterification of methacrolein. In particular, an optimized workup of the reactor output from the oxidative esterification of methacrolein is useful for removing particularly discoloring byproducts. This process moreover has the advantage that fewer demands than described in related art are placed on plant apparatus configuration.

A process is useful for producing optical molding materials on the basis of methyl methacrylate (MMA), wherein this MMA has been produced by an optimized method and the molding materials feature in particular a very low yellowness index. This MMA has been produced by direct oxidative esterification of methacrolein. In particular, an optimized workup of the reactor output from the oxidative esterification of methacrolein is useful for removing particularly discoloring byproducts. This process moreover has the advantage that fewer demands than described in related art are placed on plant apparatus configuration.

Methods are provided for synthesizing the grape mealybug pheromone, trans--necrodyl isobutyrate, starting with essential plant oils that contain trans--necrodyl acetate. The synthesis method, in two steps, converts the trans--necrodyl acetate to trans--necrodol and then converts the trans--necrodol to the desired trans--necrodyl isobutyrate. The first step can be achieved by either of a hydrolysis reaction or a reduction reaction. In the hydrolysis reaction, the essential oil is mixed in an alcohol solvent with a hydroxide base, or by mixing the essential oil in an aqueous acid. A reduction reaction can instead by performed in an organic solvent in the presence of a reducing agent. The trans--necrodol is converted to the desired trans--necrodyl isobutyrate by an esterification reaction with a carboxylic acid, an acyl halide, or an acid anhydride.

Methods are provided for synthesizing the grape mealybug pheromone, trans--necrodyl isobutyrate, starting with essential plant oils that contain trans--necrodyl acetate. The synthesis method, in two steps, converts the trans--necrodyl acetate to trans--necrodol and then converts the trans--necrodol to the desired trans--necrodyl isobutyrate. The first step can be achieved by either of a hydrolysis reaction or a reduction reaction. In the hydrolysis reaction, the essential oil is mixed in an alcohol solvent with a hydroxide base, or by mixing the essential oil in an aqueous acid. A reduction reaction can instead by performed in an organic solvent in the presence of a reducing agent. The trans--necrodol is converted to the desired trans--necrodyl isobutyrate by an esterification reaction with a carboxylic acid, an acyl halide, or an acid anhydride.

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.

Provided is a method of producing a chlorogenic acid-containing composition, including a step of subjecting coffee beans to column extraction using an aqueous solvent, in which the coffee beans include at least one selected from the group consisting of green coffee beans, decaffeinated green coffee beans, roasted coffee beans having an L value of 40 or more, and decaffeinated roasted coffee beans having an L value of 25 or more, and include at least one selected from the group consisting of unground coffee beans and ground coffee beans having an average particle size of 2.0 mm or more.